Glass forming machine particle filter, a plunger unit, a blow head, a blow head support and a glass forming machine adapted to or comprising said filter

Information

  • Patent Grant
  • 10308541
  • Patent Number
    10,308,541
  • Date Filed
    Friday, February 6, 2015
    9 years ago
  • Date Issued
    Tuesday, June 4, 2019
    4 years ago
  • Inventors
    • Röhrhoff; Uwe
    • Bürkel; Bruno
    • Maiberger; Thomas (Frankfort, IL, US)
  • Original Assignees
  • Examiners
    • Szewczyk; Cynthia
    Agents
    • McCormick, Paulding & Huber LLP
Abstract
The present invention relates to a particle filter (F) for a glass forming machine operating according to a blow-and-blow process or according to a press-and-blow process, said particle filter (F) is adapted for placing in at least an air channel (14a) serving pressurized air for counter blow (5) of a parison (P) in a blank mold (2) forming station of said glass forming machine, and/or an air channel (14b, 20) serving pressurized air for final blow (11) and/or for finish cooling (21) of a glass container (12) made of said parison (P) in a finish mold (8) station of said glass forming machine, said particle filter (F) comprising a surface filter as a main filter media (MF) and said particle filter (F), if placed in at least said air channel (14a) serving pressurized air for counter blow (5) of said parison (P) in said blank mold (2) forming station of said glass forming machine, and/or said air channel (14b, 20) serving pressurized air for final blow (11) and/or for finish cooling (21) of said glass container made of said parison (P) in said finish mold (8) station of said glass forming machine, avoiding passage of particles above a certain size from a dirty side of said main filter media (MF) to a clean side of said main filter media (MF) and thus, also avoiding final passage of said particles above said certain size into said parison (P) or said glass container (12) blown by said glass forming machine and a plunger unit (PU), a blow head (BH), a blow head support and a glass forming machine adapted for a particle filter (F) according to the present invention.
Description
TECHNICAL FIELD

The present patent application relates to a glass (container) forming machine particle filter, a plunger unit, a blow head, a blow head support and a glass forming machine adapted to or comprising said filter.


BACKGROUND

In the mechanized container glassmaking sector, a gob is cut from the glass melt in the furnace via a feeder and fed via a delivery system to a blank mold in which a solid body with a certain cavity is formed in accordance with weight and the bottle shape finally targeted later. This generally happens by virtue of the fact that the gob from the glass melt firstly slides via the abovementioned delivery system into the blank mold and is then set or blown downward from above against the mold wall whereupon a cavity is blown into the solid gob body by a counterblow from below, as a result of which an upper region of the later glass container, specifically a finish of the later glass container—commonly called parison—, is already formed in the lower region of the blank mold. This method is denoted as a blow-and-blow process-type.


Furthermore, there also exists a method called a press-and-blow process-type in which a bottle body is firstly prepressed from below via a plunger.


The counterblow necessary to form the parison in the blank mold—also called a parison mold—is done with compressed air via a plunger unit into the gob from underneath after the plunger is drawn back a little bit—preferably downward—from the gob in the blank mold above.


In case of the two abovementioned methods, the parisons thus preformed, which are still unfinished but already have an incipient inner cavity, are therefore brought from the blank into the finish mold, something which can happen by virtue of the fact that a swinging arm that has a finish support gripping the parison in the region of its finish brings the preformed glass body (the parison) from the blank mold, which is opening for this purpose, into a finish mold, which is likewise opening for this purpose, the parison being rotated by 180° about its horizontal axis, and the finish thus now pointing upward in the finish mold. After reheating, if appropriate—this glass body (parison) is then finally blown—doing so now from above—with compressed air via a blow head comprising a blowing passage (air channel) (and preferably a tube), The blow head is preferably mounted on a blow head support. The glass container is blown in the finish mold station into its final shape in the finish mold whereupon it can be removed after opening of the finish mold, preferably by take-out-tongs onto a conveyor belt for further transportation in the product flow process.


See for example of aforesaid glass forming process FIGS. 1 to 4 relating to prior art as well as such early publications as Lueger/Matthée Lexikon der Fertigungstechnik (“Dictionary of Production Engineering”), 4th edition, Stuttgart 1967, vol. 8, page 370.


In glass container forming machines working in accordance with aforesaid production methods i.e. in so called I.S. glass forming machines it could appear rarely that a very small particle arising from the glass container forming machine (made of steel parts mainly) itself is blown by the counterblow into the parison or by the final blow into the finally moulded glass container. Because of the temperature of the parison as well as the finally moulded glass container such particles may be adhesive to the inner glass surface of the parison or the glass container to be finished and thus will remain on said inner surface. Especially in case of the production of a glass container used for food storage purposes, i.e. baby food glass containers but primarily in case of the production of glass containers for a storage of pharmaceutical products even such rare entries of aforesaid small particles i.e. oxidizing particles such as oxidizing or already oxidized iron or steel particles should be avoided because such particles may have negative effects on phamaceuticals exposed to said particles. While glass for example i.e borosilacte is the most commonly used and normally suitable primary container material for phamaceuticals i.e. biophamaceuticals (See: Bee, Jared S.; Randolph, Theodore W.; Carpenter, John F.; Bishop, Stephen M.; Mitrova, Mariana N.; “Effects of Surfaces and Leachables on the Stability of Biopharmaceuticals”, Journal of Phamaceutical Sciences, Vol. 100, No. 10, October 2011, p. 4158-4170, 4162, right column.) nevertheless foreign particles (See: Bee et al., ibid., p. 4160, left column.) for example steel particles could lead to an “agglomeration of protein-coated particles and/or nucleated formation of larger aggregates of a mAb [monoclonal antibody, author's remark]” (See: Bee et al., ibid., p. 4161, right column.). Thus, a contamination of the inner area of glass container used for aforesaid purposes should be avoided as far as technically possible.


Unfortunately such entry prevention of small particles into the parison or final glass container is a quite complicate technical task.


One problem arises from the possible source of aforesaid particles. As already mentioned particles contaminating the glass container could derive from the components of the glass forming machine itself, i.e. from metal (steel) parts of aforesaid machine. Therefore an entry prevention of such unintentional particles has to be positioned as close as possible to the glass container or parison to be formed in order to avoid that particles from machine parts after the entry prevention system will jeopardize such technical precautionary measures.


SUMMARY

So, it is an object of the present invention to provide a particle entry prevention for glass containers produced in a glass forming machine operating according to said blow-and-blow type-process or said press-and-blow type-process, i.e. said I.S. glass forming machine that is able to operate very close to said parison or said glass container to be finished.


Another problem derives from the necessary air pressure for said counterblow in order to form the parison as well as said final blow to mould the glass container finally on one side and the relatively small particles on the other side. A particle contamination prevention shouldn't have any significant impact on the necessary air pressure for aforesaid blow processes, otherwise a glass container could not be formed economically i.e. properly formed in adequate time, but, of course has to catch all particles bigger than a certain amount, whereby said certain diameter has to be as small as possible.


Thus, it is furthermore an object of the present invention to provide a particle entry prevention for glass containers produced in a glass forming machine operating according to said blow-and-blow type-process or said press-and-blow type-process, i.e. said I.S. glass forming machine that does have a preferably small (enough)—most preferably no—reduction effect on the air pressure necessary to form said glass container in adequate time.


Aforesaid objects of the present invention are solved by a particle filter according to claim 1 as well as a plunger unit according to claim 28, a blow head according to claim 31, a blow head support according to claim 34 and a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type according to claim 37.


Dependent claims relate to and disclose further suitable and/or preferable and/or advantageous embodiments of the present invention.


As already mentioned above it is an object of the present invention to provide a particle entry prevention for glass containers produced in a glass forming machine operating according to said blow-and-blow type-process or said press-and-blow type-process, i.e. said I.S. glass forming machine that is able to operate very close to said parison or said glass container to be finished as well as to provide a particle entry prevention for glass containers produced in said glass forming machine that does reduce the air pressure necessary to form said glass container in adequate time only in a tolerable amount (preferably does not reduce said air pressure), but is able to prevent said parisons and glass-containers from contamination with particles being as small as possible.


This problem is solved in accordance with the present invention by a particle filter for a glass forming machine operating according to a blow-and-blow process or according to a press-and-blow process—preferably an I.S. glass forming machine—, said particle filter is adapted for placing in at least

    • an air channel serving pressurized air for counter blow of a parison in a blank mold forming station of said glass forming machine, and/or an air channel serving pressurized air for final blow and/or for finish cooling of a glass container made of said parison in a finish mold station of said glass forming machine,
    • said particle filter comprising a surface filter as a main filter media and said particle filter, if placed in at least
    • said air channel serving pressurized air for counter blow of said parison in said blank mold forming station of said glass forming machine, and/or
    • said air channel serving pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station of said glass forming machine,
    • avoiding passage of particles above a certain size from a dirty side of said main filter media to a clean side of said main filter media and thus, also avoiding final passage of said particles above said certain size into said parison or said glass container formed, respectively blown by said glass forming machine;


      and by
    • a plunger unit comprising at least an air channel for counter blow of a parison and said plunger unit suitable to be positioned in a plunger cylinder underneath a blank mold forming station of a glass forming machine of a blow-and-blow process-type, preferably an I.S. glass machine, wherein said plunger unit
    • preferably at least said air channel of said plunger unit—is adapted to receive a particle filter according to the present invention;


      and by
    • a blow head comprising at least an air channel for final blow and/or for finish cooling of a glass container made of a parison and said blow head suitable to be positioned above a finish mold station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, preferably an I.S. glass machine, wherein said blow head—preferably at least said air channel of said blow head—is adapted to receive a particle filter according to the present invention;


      and by
    • a blow head support for support of a blow head comprising at least an air channel for supply of said blow head with pressurized air and said blow head support suitable to be positioned above said blow head suitable to be positioned itself above a finish mold station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, preferably an I.S. glass machine, wherein said blow head support—preferably at least said air channel of said blow head support—is adapted to receive a particle filter according to the present invention;


      and
    • a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, said glass forming machine adapted to receive at least one particle filter according to the present invention and wherein said glass forming machine comprises an air channel serving pressurized air for counter blow of a parison in a blank mold forming station of said glass forming machine and/or an air channel serving pressurized air for final blow and/or for finish cooling of a glass container made of said parison in a finish mold station of said glass forming machine and said air channel of said glass forming machine is adapted to receive said particle filter.


In a preferred embodiment of a glass forming machine in accordance with the present invention said glass forming machine comprises a particle filter according to the present invention and said particle filter is already placed in at least said air channel of said glass forming machine adapted to receive said particle filter. If there is more than one of said air channels preferably in each of said air channels a particle filter according to the present invention is situated in order to prevent unwanted contamination with particles of parisons and/or glass containers formed (blown) during operation of said glass forming machine.


The particle filter according to the present invention could be secured in said glass forming machine air channel by a safety ring, preferably a Seegering™ that fits into a slot of said glass forming machine air channel. Thus said particle filter will not fall down to the ground during assembly nor will it be lifted due to an air blowback.


In a preferred embodiment of a glass forming machine according to the present invention the said glass forming machine air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said glass forming machine air channel only in a position, in which said particle filters main filter medias dirty side is situated on the incoming air side of said air channel to prevent said glass forming machine from a false installation of said particle filter. Especially in an assembly situation a new or cleaned particle filter could be confused with the dirty particle filter. In such a situation it is important that the confused dirty filter is mounted in its original orientation in the glass forming machines air channel because otherwise the particles collected before the main filter media are blown into the parisons or glass containers produced after such a faulty filter assembly.


The glass forming machine according to the present invention preferably comprises

    • a plunger unit according to the present invention, and/or
    • a blow head according to the present invention, and/or
    • a blow head support according to the present invention.


A preferred plunger unit according to the present invention comprises a particle filter according to the present invention where said particle filter is already placed in at least said air channel of said plunger unit adapted to said particle filter. Preferably said particle filter is placed in said plunger unit air channel during operation of said glass forming machine to prevent parisons and/or glass containers from contamination with undesired particles.


In a further embodiment of a plunger unit according to the present invention said plunger unit comprises a plunger and a plunger adapter to be adapted to—preferably (already) connected with, e.g. inserted into—the plunger—preferably inserted into or screwed together with, more preferably from below—, said plunger adapter comprising said air channel with said particle filter to be placed—preferably said particle filter is already placed in said air channel of said plunger adapter—. The use of such an adapter is more flexible because not every type of different plungers used in said glass forming machine have to be constructed for placement of a particle filter in accordance with the present invention, but only said adapter that, of course has to fit the different plungers on one hand, but also has to be designed for proper placement of said particle filter according to the present invention.


Of course a plunger unit according to the present invention preferably comprise only a plunger.


The particle filter according to the present invention is preferably secured in said plunger unit air channel by a safety ring, preferably a Seegering™ that fits into a slot of said plunger unit air channel. Thus said particle filter will not fall down to the ground during assembly i.e. in said plunger unit—e.g. during assembly in the plunger itself or said plunger adapter—nor will it be lifted due to an air blowback.


In a preferred embodiment of a plunger unit according to the present invention said plunger units air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said plunger unit air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said plunger unit air channel to prevent said plunger unit from a wrong assembly of said particle filter. E.g. during assembly of a new or clean(ed) particle filter the clean(ed) particle filter could be confused with the dirty particle filter. Thus, it is important that even a confused dirty filter could be mounted only in its original orientation in the plunger unit air channel, because otherwise after such a wrong filter assembly the particles collected at the dirty side of the main filter media are blown into the parisons produced. So, said plunger unit air channel is preferably adapted to said particle filter in such a way that said particle filter projects beyond said plunger unit if improperly placed in said plunger unit air channel, e.g. in wrong orientation or wrong direction and thus, said plunger unit cannot be mounted properly into the glass forming machines blank mold forming station if said particle filter is mounted faulty and projects therefore beyond the plunger unit.


Furthermore a blow head is proposed according to the present invention, preferably said blow head comprises a particle filter according to the present invention where said particle filter is already placed in at least said air channel of said blow head adapted to said particle filter. Preferably said particle filter is placed in said blow head air channel, preferably during operation of said glass forming machine to prevent glass containers from contamination with undesired particles.


The particle filter according to the present invention is preferably secured in said blow head air channel by a safety ring, preferably a Seegering™ that fits into a slot of said blow head air channel. Thus, said particle filter will not fall down to the ground during assembly—e.g. during assembly in the blow head—nor will it be lifted due to an air blowback in the blow head from the glass container to be blown finally underneath the blow head.


In a further preferred embodiment of the blow head according to the present invention said blow head air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said blow head air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said blow head air channel to prevent said blow head from a faulty assembly of said particle filter. I.e. during assembly of a new or clean(ed) particle filter the clean particle filter could be confused with the dirty particle filter. But, it is very important to prevent an already dirty particle filter from its wrong assembly, that is e.g. in opposite of its original orientation in the blow head air channel, because otherwise the particles collected at the dirty side of the main filter media are blown into glass containers produced after such a wrongly oriented filter assembly. So, said blow head air channel is preferably adapted to said particle filter in such a way that said particle filter projects beyond said blow head if improperly placed in said blow head air channel, e.g. in wrong orientation or wrong direction and thus, said blow head cannot be mounted properly into the glass forming machine's finish mold station, because said particle filter is mounted in wrong position and projects therefore beyond the blow head that will therefore not fit into the glass forming machine's finish mold station.


Not only a blow head is proposed according to the present invention, but also a blow head support comprising at least an air channel for supply of said blow head support with pressurized air and said blow head support for placement above said blow head that is suitable for placement of itself above said finish mold station of the glass forming machine, said blow head support preferably comprising a particle filter according to the present invention and where said particle filter is already placed in at least said air channel of said blow head support adapted to said particle filter, preferably during operation of said glass forming machine to prevent glass containers from contamination with undesired particles.


Once again, the particle filter according to the present invention is preferably secured in said blow head support air channel by a safety ring, preferably a Seegering™ that fits into a slot of said blow head support air channel. Therefore, said particle filter will not fall down to the ground during assembly i.e. in said blow head support nor will it be lifted due to an air blowback in the blow head support from the glass container to be blown finally underneath the blow head below the blow head support.


In a preferred embodiment of the blow head support according to the present invention said blow head support air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said blow head air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said blow head air channel to prevent said blow head from a wrong assembly of said particle filter. Preferably during assembly of a new or clean(ed) particle filter the clean particle filter could be confused with the dirty particle filter. Thus, it is of great importance to prevent an unclean particle filter from its wrong assembly, i.e an assembly that is in opposite of its original orientation in the blow head support air channel, because otherwise the particles collected at the dirty side of the main filter media are blown into glass containers produced after such a faulty oriented filter assembly. Therefore, said blow head support air channel is preferably adapted to said particle filter in such a way that said particle filter projects beyond said blow head support if improperly placed in said blow head support air channel, for instance in wrong orientation or wrong direction and thus, said blow head support cannot be properly mounted into the glass forming machine's finish mold station, because said particle filter is assembled in wrong position and projects therefore beyond the blow head support that will therefore not fit into the glass forming machine's finish mold station.


So, the particle filter for a glass forming machine according the present invention is preferably adapted for placing in at least

    • said air channel serving pressurized air for counter blow of said parison in said blank mold forming station before or after a manifold that distributes said pressurized air to at least one said blank mold forming station, and/or
    • said air channel serving pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station before or after a manifold that distributes said pressurized air to at least one said finish mold station.


In a preferred embodiment of the particle filter for a glass forming machine according to the present invention, said particle filter is adapted for placing in at least

    • said air channel situated in a plunger unit and serving pressurized air for counter blow of said parison in said blank mold forming station of said glass forming machine and said plunger unit situated in a plunger cylinder underneath said blank mold forming station of said glass forming machine, and/or
    • said air channel situated in a blow head and serving pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and said blow head situated above said finish mold station of said glass forming machine, and/or
    • said air channel situated in a blow head support for supply of said blow head with pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and for support of said blow head and said blow head support situated above said blow head that is situated itself above said finish mold station of said glass forming machine


      and said particle filter, if placed in at least
    • said air channel situated in said plunger unit and serving pressurized air for counter blow of said parison in said blank mold forming station of said glass forming machine and said air plunger unit situated in said plunger cylinder underneath said blank mold forming station of said glass forming machine, and/or
    • said air channel situated in said blow head and serving pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and said blow head situated above said finish mold station of said glass forming machine, and/or
    • said air channel situated in said blow head support for supply of said blow head with pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and for support of said blow head and said blow head support situated above said blow head that is situated itself above said finish mold station of said glass forming machine


      avoids passage of said particles above said certain size from said dirty side of said main filter media to said clean side of said main filter media and thus also avoids final passage of said particles into said parison or said glass container blown (formed) by said glass forming machine.


The main filter media of the particle filter according to the present invention preferably comprises a slotted filter, for instance with slotted holes. Such slotted filter media can be produced for small pore sizes similar to track-etched filter media, but with an advantageously relatively high open filter area much better than in case of a track-etched filter media (See: Holdich, Richard; Kosvintsev, Serguei; Zhadanov, Sergey; “Pore design and engineering for filters and membranes”, Philosophical Ttransactions of the Royal Society, Mathematical, Physical & Engineering Sciences, Vol. 364, 2006, p. 161-174, 163 et seq.) and with an advantage of a better flow resistance in comparison with a circular pore filter media. Preferred is a ratio of length to diameter of a slot of between 5 to 20 (See: Holdich et al, ibid, p. 167, FIG. 3 and second para.). For instance such slotted filter media preferably comprises a silicon substrate covered by a—preferably thin—layer of silicon nitride (See: Holdich et al., ibid, p. 163 et seq.).


But, of course the main filter media of the particle filter according to the present invention could also comprise a sieve filter that also preferably comprises a silicon substrate covered by a layer of silicon nitride (See: Holdich et al., ibid, p. 164.).


In a further preferred embodiment the particle filter for a glass forming machine according to the present invention comprises said sieve filter of said main filter media with a mesh, preferably a PSW (Plain Square Woven) or a TSW (Twill Square Woven) mesh—preferably a wire mesh—made of an anti-corrosive material. For the particle separation PSW (Plain Square Woven) weave type of the mesh is preferred, but also other types of weaves like a TSW (Twill Square Woven) mesh are possible.


Preferably a wire mesh is made of an anti-corrosive metal or metal alloy, more preferably made of anti-corrosive metal or metal alloy with a yield strength of in minimum 200 N/mm2 and more preferably a yield strength of 350 N/mm2 in minimum or most preferably 450 N/mm2 in minimum. More preferably said anti-corrosive material of said sieve filter of said main filter media is stainless steel, preferably a X5CrNiMo17-12-2 steel according to the European norm EN 1.4401 or the equivalent American norm AISI 316 (S31800 in the Unified Numbering System [UNS]). Stainless steel differs from carbon steel by the amount of chromium present. Unprotected carbon steel rusts readily when exposed to air and moisture. This iron oxide film (the rust) is active and accelerates corrosion by forming more iron oxide, and due to the greater volume of the iron oxide this tends to flake and fall away. Stainless steels contain sufficient chromium to form a passive film of chromium oxide, which prevents further surface corrosion by blocking oxygen diffusion to the steel surface and blocks corrosion from spreading into the metal's internal structure, and due to the similar size of the steel and oxide ions they bond very strongly and remain attached to the surface. Thus, stainless steel is suitable to meet the requirement of the present invention, that is not to contaminate the pressurized air with particles (i.e. rust particles) itself. Preferably the stainless steel is additionally passivated, most preferably by electropolishing. Furthermore X5CrNiMo17-12-2 steel is strong enough to retain high speed particles arriving on the dirty filter side because its yield strength is ≥200 N/mm2 (200 Mega Pascal [MPa]), typically between 350 N/mm2 band 370 N/mm2.


Furthermore it is necessary that the particle filter according to the present invention does on one hand stop undesired particles, but does also not cause a pressure drop that is too high to guarantee that a parison and/or a final glass container can be blown (formed) in the glass forming machine in sufficient time. The air pressure in the glass forming machine is typically in maximum 4 bar (1 bar=100 000 Pascal [Pa]), but it might be lower (down to 1.2 bar). To ensure a proper glass forming of the parison and/or the final glass container a minimum of 1 bar air pressure is necessary. So the particle filter should cause a pressure drop in maximum of 0.1 bar, more preferably in maximum of 0.05 bar, most preferably no pressure drop.


In case of a slotted as well as in case of a circular filter media the pressure drop of such filter media could be calculated in case of steady flow. According to Holdich et al. (see: Holdich et al., ibid, p. 166, equation (2.2) and (2.3)) the pressure drop is







Δ





p

=



[



12

L





μ


ld
3


+


32

μ


π






ld
2




]



Q
N




f
2



(
k
)







with







f
2



(
k
)



=



-

π
2




k
2



8






ln




[

cos






(


π





k

2

)


]










    • where L is the pore depth i.e. the flow channel height (preferably the thickness of the filter media),
      • μ is the coefficient of dynamic viscosity of the flow media (preferably air in case of the present invention),
      • l is the slot length,
      • d is the slot width,
      • l=d i.e. in case of circular pores ore quadratic pores (preferably in case of a Plain Square Woven [PSW] or a Twill Square Woven [TSW] sieve),
      • Q is the flow rate,
      • N is the number of pores, and
      • k is the fraction of open filter area.





In case of the present invention the counterblow to form the parison as well as the final blow to form the glass container and/or the finish cooling air flow is not necessarily a steady flow, but could also be an unsteady flow especially during the initial phase of the blow and due to blowbacks that could appear i.e. in the finish mold station (For that reason a safety ring is also proposed by the present invention to secure the particle filter in the air channel.).


It is not clear what the exact equation for pressure drop will be in such an unsteady flow situation, but it might be clear—i.e. in view of the aforesaid given equation for the pressure drop Δp—that especially the open filter area is of essential importance for the pressure drop caused by the particle filter (f2(k)→0, if k→1 thus leads to a decreasing pressure drop Δp for increasing open filter area).


Experiments with a main filter media with a maximum pore size of 110 micron (in the United States: US mesh 165) have shown no or no significant pressure drop (see FIG. 32).


Thus, if a wire mesh is used preferably wire cloth dimension should follow—most preferably need to follow—ASTM E2016-11 standard (Standard of the American Society for Testing and Materials), because a constant mesh wire diameter is highly important to maintain and ensure desired filtration and necessary opening space for sufficient air flow.


Experiments led to a preferred embodiment of the particle filter according to the present invention that comprises a main filter media with a (maximum) pore size of 100 micron (in the United States: US mesh 160) and an open filter area fraction of about 40% with insignificant pressure drop for the purpose of the present invention.


More preferably the (maximum) pore size of said main filter media could be reduced to 40 micron (μm) (equivalent to US mesh 325) without further significant air pressure drops and with an open filter area fraction of about 30% (wire diameter: 0.0014 inch that is 0.0356 mm). Even a reduction to a (maximum) pore size of 25 micron (US mesh 500) and an open filter area fraction of 25% (wire diameter: 0.0010 inch that is 0.0254 mm) will not result in an air pressure drop that avoids a parison and/or final glass container blow in adequate time.


Furthermore a particle filter for a glass forming machine according to the present invention could comprise also an additional surface filter as a protective filter media more coarse than said main filter media and wherein said protective filter media is situated on said dirty side of said main filter media in order to protect said main filter media against impact of particles, preferably bigger particles that might have a greater momentum according to their greater mass than smaller particles of less mass at the same velocity of both particles caused by the stream of pressurized air (p=m·v). Thus, the protective filter media protects the main filter media against impacts of such bigger particles with a greater momentum.


Also this protective filter media comprises a mesh, preferably a PSW (Plain Square Woven) mesh or a TSW (Twill Square Woven) mesh—preferably a wire mesh—made of anti-corrosive material, preferably anti-corrosive metal or metal alloy, more preferably made of anti-corrosive metal or metal alloy with a yield strength of in minimum 200 N/mm2 and more preferably a yield strength of 350 N/mm2 in minimum or most preferably 450 N/mm2 in minimum, most preferably with a higher yield strength than the material of said main filter media and/or with a mesh wire diameter thicker than a mesh wire diameter of said main filter media.


Preferably said anti-corrosive material of said wire mesh of said protective filter media is stainless steel, preferably a X5CrNiMo17-12-2 steel according to the European norm EN 1.4401 or the equivalent American norm AISI 316 as already explained in the context of said main media filter. Also said mesh of said protective filter media made of an anti-corrosive metal or metal alloy can also be passivated, additionally preferably by electropolishing.


In a further preferred embodiment the particle filter according to the present invention comprises also a porous support mean—preferably more coarse than said main filter media—and wherein said porous support mean is situated on said clean side of said main filter media to stabilize said main filter media against forces arising from particles arriving on said dirty side of said main filter media. Said porous support mean could also comprise a mesh, preferably a PSW (Plain Square Woven) mesh or a TSW (Twill Square Woven) mesh—preferably a wire mesh—, said mesh being preferably more coarse than said main filter media itself. In case of an impact of a particle on the dirty side of the main filter media the momentum of that arriving particle causes a force arising from that particle that depends on the mass and the velocity of said particle as well as the deceleration time necessary to stop the particle. The deceleration time is dependent on the resiliency of the main filter media absorbing the energy brought in by the arriving particle. If the material of the main filter media is not sufficiently resilient i.e. due to insufficient yield strength of its material it may happen that the filter media is plastically deformed or in certain cases the filter media will be pierced by the arriving particle. To avoid this said porous support mean stabilizes the main filter media by supporting the main filter media mechanically, preferably with a stronger material and/or a more stable structure and/or more mass than in case of the main filter media. Thus, in case of a particle impact on the dirty side of the main filter media said main filter media is deformed and will get into contact with the stronger support mean on the clean side of said main filter media. The main filter media will be pressed in such a case against the stronger, preferably coarser support mean that will therefore absorb a certain part of the energy caused by the particle arriving at the clean side of the main filter media and therefore the main filter media is not stressed so much.


A further preferred embodiment of a particle filter for a glass forming machine according to the present invention comprises a porous support mean comprising a sieve filter with a mesh, preferably a PSW (Plain Square Woven) or a TSW (Twill Square Woven) mesh—preferably a wire mesh—made of anti-corrosive material, preferably made of anti-corrosive metal or metal alloy, more preferably made of anti-corrosive metal or metal alloy with a yield strength of in minimum 200 N/mm2 and more preferably a yield strength of 350 N/mm2 in minimum or most preferably 450 N/mm2 in minimum, most preferably with a mesh wire diameter thicker than a mesh wire diameter of said main filter media and/or preferably with a higher yield strength than the material of said main filter media.


Again, said anti-corrosive material of said wire mesh of said protective filter media is preferably stainless steel, more preferably a X5CrNiMo17-12-2 steel according to the European norm EN 1.4401 or the equivalent American norm AISI 316 as already explained in the context of said main media filter. Also said mesh of said protective filter media is made of an anti-corrosive metal or metal alloy could also be passivated, additionally preferably by electropolishing.


In a further preferred embodiment of the particle filter according to the present invention said main filter media is situated between said protective filter media and said support mean. Preferably said main filter media that is situated between said protective filter media and said porous support mean is held together with said protective filter media and said porous support mean by a filter body and a fastening mean, preferably an insert mean that is adapted to—preferably connected with—said filter body, preferably inserted—more preferably pressed—into said filter body with interference fit to said filter body or screwed together with said filter body or connected the like with said filter body.


The outer dimension of said filter body can overlap the outer dimension of said fastening mean, preferably said insert mean. The latter embodiment will lead to a particle filter according to the present invention that is able to be used in an air channel only in a proper position—preferably in one orientation or direction—due to the fact of its geometry, if the respective air channel is adapted to said geometry of said particle filter. Such embodiment allows for safety reasons to avoid a wrong assembly of a particle filter in a glass forming machine, preferably in a plunger unit and/or a blow head and/or a blow head support. I.e. the wrong assembly of an already used particle filter could be harmful to parisons or glass containers to be blown (formed) by the glass forming machine because in such a case the particles formerly collected on the dirty side of the particle filter may turn to the clean side and will be blown from there into the parison and/or the final glass container, a situation that should be avoided.


Once again, said filter body and fastening mean, preferably said insert mean preferably are made of an anti-corrosive material, preferably of an anti-corrosive metal or metal alloy, preferably an anti-corrosive metal or metal alloy with a yield strength of in minimum 200 N/mm2 and more preferably a yield strength of 350 N/mm2 in minimum or most preferably 450 N/mm2 in minimum. The anti-corrosive material of said filter body and fastening mean, preferably said insert mean is preferably stainless steel, more preferably a X5CrNiMo17-12-2 steel according to the European norm EN 1.4401 or the equivalent American norm AISI 316 as already explained in the context of said main media filter. Said filter body and said fastening mean, preferably said insert mean are made of an anti-corrosive metal or metal alloy and can be passivated additionally, too, preferably by electropolishing.


In a further most preferred embodiment of the particle filter for a glass forming machine according to the present invention, said main filter media and said protective filter media and said support mean is each a circular disc and wherein said filter body is a filter body ring and said fastening mean, preferably said insert mean is a fastening ring—preferably a press ring—that is adapted to—preferably connected with—said filter body ring, preferably inserted into said filter body ring with cylindrical interference fit to said filter body ring or screwed together with said filter body ring or connected the like with said filter body ring.


The outer diameter of said filter body ring can overlap the outer diameter of said fastening ring, preferably said press ring. This embodiment of the present invention will lead to a particle filter that is—as already explained above—able to be used in an air channel only in a proper position—preferably in one orientation or direction—due to the fact of its geometry, if the respective air channel is adapted to said geometry of said particle filter, thus, for safety reasons to avoid a wrong assembly of a particle filter in a glass forming machine, preferably in a plunger unit and/or a blow head and/or a blow head support. The circular geometry of the particle filter of the aforesaid described embodiment of the present invention is most suitable for assembly into an air channel and therefore most preferred.


As mentioned above the particle filter according to the present invention can be electropolished. This should be done preferably according ASTM B912. Electropolishing is an electrochemical etching and passivation process that is used to deburr, smooth, and brighten parts. Electrolytic reactions cause ionic conduction resulting in the removal of metal particles from parts. Metal dissolution reactions with the electrolyte form a viscous resistive layer film at the surface of the metal; the viscous layer is thicker over the valleys than over the peaks of the surface. This causes de-burring, smoothing, and brightening by removal of material from the peaks and leveling the surface. Electropolishing according to ASTM B912 may be used for de-burring of all filters. ASTM B91 specification covers the passivation of stainless steel alloys in the 300 series of the Unified Numbering System for metals and alloys (UNS3XXXX), and the use of electropolishing procedures. Electropolishing may be executed by the filter manufacturer or outsourced to a third party preferably. The filters should preferably be electropolished according to ASTM B912. If the electropolishing of the filters is outsourced the purchaser shall preferably state the following:

    • Alloy Designation SAE grade 316.
    • Appearance required bright.
    • The metal to be removed shall preferably not exceed 6 μm.
    • Finished parts should be immediately placed in clean room ISO (or equivalent) certified bags (see packaging specification) and kept sealed.


The assembled filter shall be preferably cleaned roughly according ISO 14952-4 (Part 4: Rough-cleaning processes). The actual choice of the specific cleaning material, degreaser, should be determined according to “Table 1—Selection chart for rough-cleaning processes”. After cleaning tap water is used to remove the residual particles and degreaser.


The assembled filter shall preferably be cleaned precisely according ISO 14952-6 (Part 6: Precision-cleaning processes). If the precision cleaning is outsourced the purchaser shall preferably state the following. If the cleaning is done otherwise, i.e. inhouse the following shall preferably be observed and/or put into the (quality control) records:

    • Preferably the particle filter shall be cleaned according ISO 14952-6 (Part 6: Precision-cleaning processes) or equivalent.
    • Preferably the expected cleanliness level 100 for metal particle, more preferably with reference to ISO 14952-2 (Part 2: Cleanliness levels) or equivalent.
    • Preferably the part name, and more preferably: “Stainless Steel Air filter SAE Grade 316”.
    • Preferably an approved cleaning method is used: more preferably ultrasonic cleaning, most preferably under avoidance of cavitation pitting.
    • Preferably approved cleaning material is used: more preferably Brulin 815G, Blue Gold, Alconox or equivalent.
    • Preferably the filter needs to be placed with the porous support mean (Support Disc) (dirty side) down into the ultrasonic cleaning unit.
    • The cleaning needs to be under controlled environment. Class 100,000 Federal Standard 209E clean room or equivalent.
    • Each filter shall preferably be bagged separately, in a bag suitable for Class 100 Federal Standard 209E (or equivalent) clean rooms after cleaning and drying, preferably 25 individually wrapped bags should than be placed into a larger bag prior to shipping.
    • Preferably the liquid flush test according to 14952-3 (or equivalent) shall be used as verification methods for cleanliness level.
    • Preferably a part number.
    • Preferably the quantities.


To verify the cleanliness level of the precision cleaning a liquid flush test for particle in a controlled environment ISO 14952-3 (Part 3: Analytical procedures for the determination of nonvolatile residues and particulate contamination) can be and preferably shall be performed. The liquid flush test can and preferably shall be performed on a statistically relevant population of the precision cleaning lot. Preferably, only cleaning lots which meet cleanliness level 100 for metal particle, according to ISO 14952-2 (Part 2: Cleanliness levels) “Table 1—Particle cleanliness levels”, will be verified and shipped for final use. The certification of cleanliness needs to be attached on each lot.


After each cleaning process, each filter can and preferably shall be bagged separate, in a bag suitable for Class 100 Federal Standard 209E (or equivalent) clean room, 25 individually wrapped bags should than preferably be placed into a larger bag prior to shipping.


A bag specification as follows is preferably recommended:

    • Material: Polyethylene
    • Color: Clear
    • Cleanroom: Class 100
    • Size: N/A
    • Thick. Mils N/A


In order to eliminate metal particles in the parison and later the final glass container, the present invention discloses a filtration in the counterblow and final blow air stream to filter potential metal particles. In the present application the entire range of particle filters according to the present invention as well as their point of operation in the glass forming machine particular and respective mould equipment like blow heads, blow head supports and plunger units or retaining rings (safety rings) used to fasten filters in mentioned mould equipment in regard of their design, material and cleanliness level are also described. Furthermore preferred procedures to insure desired cleanliness level are disclosed as well.


Examples of preferred embodiments of the present invention are illustrated in the drawings:





BRIEF DESCRIPTION OF THE DRAWINGS


FIGS. 1 to 4 show a blow-and-blow process for the production of glass containers and relate to prior art;



FIG. 5 shows an unmounted particle filter for a glass forming machine according to the present invention in a sectional view;



FIG. 6 shows also an unmounted particle filter for a glass forming machine according to the present invention, but in an perspective view;



FIG. 7 shows a mounted particle filter for a glass forming machine according to the present invention in a sectional view;



FIG. 8 shows a set of four unmounted particle filters of different sizes for a glass forming machine according to the present invention with parts of it as a circular disc or ring shown in an bird's eye view on the surface of said discs or rings;



FIG. 9 shows an unmounted particle filter according to the present invention with preferred dimensional specification parameters of three preferred embodiments;



FIG. 10 shows a mounted particle filter according to the present invention in a perspective view on the left side from its intentional clean side and on the right side from its intentional dirty side;



FIG. 11 shows a sectional view of a plunger unit according to the present invention comprising at least an air channel for counter blow of a parison;



FIG. 12 shows a perspective view of a plunger unit according to the present invention showing the outlets through the pressurized air flows into the par-son's inner cavity as counter blow;



FIG. 13 shows a perspective view of a plunger unit according to the present invention from downside;



FIG. 14 shows a partly sectional view of a plunger unit according to the present invention comprising at least an air channel with a particle filter already placed in at least said air channel;



FIG. 15 shows a perspective view of a plunger unit according to the present invention comprising at least an air channel with a particle filter already placed in said air channel;



FIG. 16 shows a perspective view of a plunger unit according to the present invention partially opened comprising at least an air channel with a particle filter already placed in said air channel;



FIG. 17 shows a partly sectional view of a plunger unit according to the present invention comprising at least an air channel with a particle filter already placed, but wrongly placed in said air channel;



FIG. 18 shows a side view of a plunger unit according to FIG. 17;



FIG. 19 shows a sectional view of the air flow of a counter blow of a plunger unit according to the present invention;



FIG. 20 shows a side view of the air flow of a counter blow of a plunger unit according to FIG. 19;



FIG. 21 shows a sectional view of a blow head according to the present invention comprising at least an air channel for final blow of a glass container made of a parison;



FIG. 22 shows a perspective view of a blow head according to the present invention showing the air channel's insert area that is adapted for insertion of a particle filter according to the present invention from upside;



FIG. 23 shows a perspective view of a blow head according to FIG. 22 from downside;



FIG. 24 shows a sectional view of a blow head according to the present invention comprising at least an air channel with a particle filter already placed in at least said air channel;



FIG. 25 shows a perspective view of a blow head according to the present invention comprising at least an air channel with a particle filter already placed in at least said air channel;



FIG. 26 shows a partly sectional view of a blow head according to the present invention partially opened and comprising at least an air channel with a particle filter already placed in at least said air channel;



FIG. 27 shows a sectional view of a blow head according to the present invention comprising at least an air channel with a particle filter wrongly placed in at least said air channel;



FIG. 28 shows a perspective view of a blow head according to the present invention comprising at least an air channel with a particle filter wrongly placed in said air channel according to FIG. 27;



FIG. 29 shows a partly sectional view of blow head according to FIG. 27;



FIG. 30 shows a sectional view of the air flow of a final blow in a blow head according to the present invention;



FIG. 31 shows a side view of the air flow of a final blow in a blow head according to FIG. 29;



FIG. 32 shows a pressure drop chart from experiments with a main filter media with a maximum pore size of 110 micron (in the United States: US mesh 165); and



FIG. 33 shows in the upper row a set of four unmounted parts of another preferred embodiment of a particle filter according to the present invention with said parts as circular discs or disc like parts shown in an bird's eye view and below the upper row a preferred embodiment of a mounted particle filter according to the present invention shown also from an birds eye view perspective.





DETAILED DESCRIPTION


FIGS. 1 to 4 show a blow-and-blow process for the production of glass containers and relate to prior art. First a gob 1 is cut from the glass melt in the furnace via a feeder and fed via a delivery system to a blank mold 2 in which a solid body with a certain cavity is formed in accordance with the weight and the bottle shape finally targeted later. This generally happens by virtue of the fact that the gob 1 from the glass melt firstly slides via the abovementioned delivery system 3 into the blank mold 2 and is then set or blown downward with pressurized (compressed) air 4 from above against the mold wall whereupon a cavity 6 is blown into the solid gob 1 body by a counterblow 5 from below (via an air channel 14a serving pressurized air for the counter blow 5), as a result of which an upper region of the later glass container, specifically a finish of the later glass container—commonly called parison P—, is already formed in the lower region of the blank mold. This method is denoted as a blow-and-blow process-type.


The counterblow 5 necessary to form the parison P in the blank mold 2—also called a parison mold—is done with compressed air 5 via a plunger unit PU into the gob 1 from underneath after the plunger PL is drawn back a little bit—preferably downward 7—from the gob 1 in the blank mold 2 above.


In case of the abovementioned method, the parisons P thus preformed, which are still unfinished but already have an incipient inner cavity 6, are therefore brought from the blank mold 2 into the finish mold 8, something which can happen by virtue of the fact that a swinging arm 9 that has a finish support 10 gripping the parison P in the region of its finish brings the preformed glass body (the parison P) from the blank mold 2, which is opening for this purpose, into a finish mold 8, which is likewise opening for this purpose, the parison P being rotated by 180° about its horizontal axis, and the finish thus now pointing upward in the finish mold 8. After reheating, if appropriate—this glass body (parison P) is then finally blown—doing so now from above—with compressed air 11, 21 via a blow head BH comprising a blowing passage (air channel) 14b and preferably a tube 19. Said blow head BH is preferably mounted on a blow head support (not shown here). The parison P is blown into its final shape of a glass container 12 in the finish mold 8 whereupon it can be removed after opening of the finish mold 8, preferably by take-out-tongs onto a conveyor belt for further transportation in the product flow process. In a preferred embodiment the final blow 11 process can be supported by a vacuum system 13 that draws the glass container's 12 outer wall in the finish mold station 8. Compressed air may preferably also directed for finish cooling 21 through a finish cooling passage (also [an] air channel[s]) 20 if necessary or if preferred.



FIG. 5 shows an unmounted particle filter F for a glass forming machine according to the present invention in a sectional view, wherein a main filter media MF that is situated between a protective filter media PF and a porous support mean PS is held together with said protective filter media PF and said porous support mean PS by a filter body FB and a fastening mean FM, preferably an insert mean that is adapted to—preferably connected with—said filter body FB, preferably inserted into said filter body FB with interference fit to said filter body FB.



FIG. 6 shows also an unmounted particle filter F for a glass forming machine according to the present invention, but in an perspective view, wherein a main filter media MF (a wire mesh with small pores) that is situated between a protective filter media PF (also a wire mesh, but more coarse than the wire mesh of said main filter media MF, meaning that the pores of mesh of the protective filter media PF are bigger than the pores of the main filter media MF) and a porous support mean PS (also a wire mesh, but more coarse than the wire mesh of said main filter media MF, meaning that the pores of mesh of the support mean PS are bigger than the pores of the main filter media MF) is held together with said protective filter media PF and said support mean PS by a filter body FB and a fastening mean FM, preferably an insert mean that is adapted to—preferably connected with—said filter body FB, here to be inserted into said filter body FB with interference fit to said filter body FB.



FIG. 7 shows a mounted particle filter F for a glass forming machine according to the present invention in a sectional view, wherein a main filter media MF that is situated between a protective filter media PF and a porous support mean PS is held together with said protective filter media PF and said porous support mean PS by a filter body FB and a fastening mean FM, preferably an insert mean that is adapted to—preferably connected with—said filter body FB, preferably inserted into said filter body FB with interference fit to said filter body FB. The outer dimension (here the outer diameter) of said filter body FB overlaps the outer dimension (here the outer diameter) of said fastening mean FM, preferably a press ring. Such an embodiment of a particle filter according to the present invention is able to be used in an air channel 14a, 14b, 20 only in a proper position—preferably in one orientation or direction—. This is due to the fact of its geometry, if the respective air channel 14a, 14b, 20 is adapted to said geometry of said particle filter F. Such an embodiment allows for safety reasons to avoid a wrong assembly of a particle filter F in a glass forming machine, preferably in a plunger unit PU and/or a blow head BH and/or a blow head support. I.e. the wrong assembly of an already used particle filter could be harmful to parisons P or glass containers 12 to be blown (formed) by the glass forming machine because in such a case the particles formerly collected on the dirty side of the particle filter F may turn to the clean side and will be blown from there into the parison P and/or the final glass container 12, a situation that should be avoided.



FIG. 8 shows a set of four unmounted particle filters F of different sizes for a glass forming machine according to the present invention with parts of it as a circular disc or ring shown in an bird's eye view on the surface of said discs or rings, wherein a main filter media wire mesh disc MF that has to be positioned between a protective filter media wire mesh disc PF and a support mean wire mesh disc PS should be held together with said protective filter media wire mesh disc PF and said support mean wire mesh disc PS by a filter body ring FB and a fastening mean, here a press ring FM, if the press ring FM is inserted into said filter body ring FB with interference fit to said filter body ring FB. Preferably the outer diameter of the filter body ring FB of the smallest particle filter shown here (in the very left column) is 0.6 inches that is 15.24 mm, the outer diameter of the filter body ring FB of the next particle filter shown in the next column to the right is preferably 0.75 inches that is 19.05 mm, the next one is preferably 0.9 inches that is 22.86 mm and the last one (in the very right column) is preferably 1.2 inches that is 30.48 mm.














Press Ring (as fastening mean FM)











Filter#








PR


-


O






(
inches
)





(
mm
)













PR


-


I






(
inches
)





(
mm
)













PR


-


H






(
inches
)





(
mm
)













PR


-


CH






(

deg





inches

)





(

deg





mm

)










CH#-1.200






1.000


+

/

-

0.001





25.4





mm

+

/

-

0.0254





mm











0.900



22.86





mm










0.234



5.9436





mm










45

°






0.015




45

°





0.381





mm










CH#-0.925






0.750


+

/

-

0.001





19.05





mm

+

/

-

0.0254





mm











0.660



16.764





mm










0.234



5.9436





mm










45

°






0.015




45

°





0.381





mm










CH#-0.750






0.653


+

/

-

0.001





16.5862





mm

+

/

-

0.0254





mm











0.530



13.462





mm










0.234



5.9436





mm










45

°






0.015




45

°





0.381





mm


























Disc (as protective filter media PF, as main



filter media MF and as porous support mean PS)










Filter#








D


-


C






(
inches
)





(
mm
)













D


-


F






(
inches
)





(
mm
)













D


-


D






(
inches
)





(
mm
)










CH#-1.200






0.985


+

/

-

0.003





25.019





mm

+

/

-

0.0762





mm












0.985


+

/

-

0.003





25.019





mm

+

/

-

0.0762





mm












0.985


+

/

-

0.003





25.019





mm

+

/

-

0.0762





mm











CH#-0.925






0.735


+

/

-

0.003





18.669





mm

+

/

-

0.0762





mm












0.735


+

/

-

0.003





18.669





mm

+

/

-

0.0762





mm












0.735


+

/

-

0.003





18.669





mm

+

/

-

0.0762





mm











CH#-0.750






0.625


+

/

-

0.001





15.875





mm

+

/

-

0.0762





mm












0.625


+

/

-

0.001





15.875





mm

+

/

-

0.0762





mm












0.625


+

/

-

0.001





15.875





mm

+

/

-

0.0762





mm



























Filter Body FB













Filter#








FB


-


O






(
inch
)





(
mm
)













FB


-


I






(
inch
)





(
mm
)













FB


-


H






(
inch
)





(
mm
)













FB


-


IH






(
inch
)





(
mm
)













FB


-


B






(
inch
)





(
mm
)













FB


-


CH






(

deg





inch

)





(

deg





mm

)










CH#-1.200





1.200



30.48





mm











0.997


+

/

-

0.001








25.3238





mm

+

/

-






0.0254





mm














0.160


+

/

-

0.002








4.046





mm

+

/

-






0.0508





mm













0.118



2.9972





mm










0.900



22.86





mm










30

°






0.060




30

°





1.542





mm










CH#-0.925





0.925



23.495





mm











0.747


+

/

-

0.001








18.9738





mm

+

/

-






0.0254





mm














0.160


+

/

-

0.002








4.064





mm

+

/

-






0.0508





mm













0.118



2.9972





mm










0.625



15.875





mm










30

°






0.060




30

°





1.542





mm










CH#-0.750





0.750



1905





mm











0.650


+

/

-

0.001








16.51





mm

+

/

-






0.0254





mm














0.160


+

/

-

0.002








4.064





mm

+

/

-






0.0508





mm













0.118



2.9972





mm










0.450



11.43





mm










30

°






0.060




30

°





1.542





mm















FIG. 9 shows an unmounted particle filter F according to the present invention with preferred dimensional specification parameters of three preferred embodiments, wherein (of course in an respective mounted embodiment of the filter F) a main filter media MF that is situated between a protective filter media PF and a porous support mean PS is held together with said protective filter media PF and said porous support mean PS by a filter body FB and a fastening mean FM, preferably an insert mean, most preferably a press ring that is adapted to—preferably connected with—said filter body FB, preferably inserted into said filter body FB with interference fit to said filter body FB as follows:


Break all sharp edges 45° 0.015″ that is 45° 0,381 mm. Tolerances +/−0.003″ that is 0.0762 mm on all but marked dimensions. The values in inches are the original values and a conversion relation was used wherein 1″ (1 inch) is 2.54 cm.



FIG. 10 shows a mounted particle filter F according to the present invention in a perspective view on the left side from its intentional clean side and on the right side from its intentional dirty side wherein a main filter media is situated between a protective filter media wire mesh disc PF and a porous support mean wire mesh disc PS held together with said protective filter media wire mesh disc PF and said support mean wire mesh disc PS by a filter bodyring FB and a press ring FM inserted into said filter body ring FB with interference fit to said filter body ring FB. According to its geometry (the filter body ring FB has a larger outer diameter than the press ring FM and thus the outer diameter of said filter body ring FB overlaps the outer diameter of said press ring FM) the particle filter F can be positioned in an air channel 14a, 14b, 20 only in a proper position (preferably a certain orientation or certain direction), if the air channel 14a, 14b, 20 is adapted to the particle filter F in its geometry. Thus, a wrong assembly of the particle filter F according to the present invention can be avoided.



FIG. 11 shows a sectional view of a plunger unit PU according to the present invention comprising at least an air channel 14a for counter blow 5 of a parison P and said plunger unit PU suitable for placement in a plunger cylinder underneath a blank mold 2 forming station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, preferably an I.S. glass machine, said plunger unit PU adapted to receive a particle filter F according to the present invention and said particle filter F to be placed in at least said air channel 14a of said plunger unit PU adapted to said particle filter. Here the plunger unit PU is adapted to the particle filter F in an insert area 15 at the lower end of the air channel 14a that leads to the outlets 16 through the pressurized air flows into the parison's P inner cavity 6 as counter blow 5.



FIG. 12 shows a perspective view of a plunger unit PU according to the present invention showing the outlets 16 through the pressurized air flows into the parison's P inner cavity 6 as counter blow 5.



FIG. 13 shows a perspective view of a plunger unit PU according to the present invention from downside. As already disclosed in FIG. 11 the plunger unit PU is adapted to the particle filter F in an insert area 15 at the lower end of the air channel 14a that leads to the outlets 16 through the pressurized air flows into the parison's P inner cavity 6 as counter blow 5.



FIG. 14 shows a partly sectional view of a plunger unit PU according to the present invention comprising at least an air channel 14a for counter blow 5 of a parison P and said plunger unit PU suitable for placement in a plunger cylinder underneath a blank mold 2 forming station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, preferably an I.S. glass machine, said plunger unit PU adapted to receive a particle filter F according to the present invention and said particle filter F already placed in at least said air channel 14a of said plunger unit PU adapted to said particle filter F. Here the plunger unit PU is adapted to the particle filter F in an insert area 15 at the lower end of the air channel 14a that leads to the outlets 16 through the pressurized air flows into the parison's P inner cavity 6 as counter blow 5.



FIG. 15 shows a perspective view of a plunger unit PU according to the present invention comprising at least an air channel 14a with a particle filter F already placed in at least said air channel 14a.



FIG. 16 shows a perspective view of a plunger unit PU according to the present invention partially opened and comprising at least an air channel 14a and a particle filter F already placed in at least said air channel 14a.



FIG. 17 shows a partly sectional view of a plunger unit PU according to the present invention comprising at least an air channel 14a with a particle filter F already placed, but wrongly placed in at least said air channel 14a. As a consequence of this improper placement of the particle filter F in the air channel 14a of the plunger unit PU said particle filter F projects beyond said plunger unit PU and thus, the plunger unit PU cannot be installed in the blank mold 2 forming station of the glass forming machine. Therefore a wrong assembly could be avoided effectively using this embodiment of the present invention.



FIG. 18 shows a side view of a plunger unit PU according to FIG. 17.



FIG. 19 shows a sectional view of the air flow of a counter blow 5 in a plunger unit PU according to the present invention. The pressurized air enters the plunger unit PU from downwards passing the particle filter F at the lower end of the air channel 14a that leads to the outlets 16 through the pressurized air flows into the parison's P inner cavity 6 as counter blow 5. By passing the particle filter F according to the present invention undesired particles will be separated and collected on the dirty side (here the downside) of said particle filter F.



FIG. 20 shows a side view of the air flow of a counter blow 5 in a plunger unit PU according to FIG. 19.



FIG. 21 shows a sectional view of a blow head BH according to the present invention comprising at least an air channel 14b for final blow 11 of a glass container 12 made of a parison P and said blow head BH suitable for placement above a finish mold 8 station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, preferably an I.S. glass machine, said blow head BH adapted to receive a particle filter F according to the present invention and said particle filter F to be placed in at least said air channel 14b of said blow head BH adapted to said particle filter F. Here the blow head BH is adapted to the particle filter F in an insert area 15 at the upper end of the air channel 14b that lead to the air inlet of the finish mold 8 through the pressurized air flows into the glass container's 12 inner space as final blow 11.


It is also possible—but not shown here—to have a particle filter F according to the present invention of a larger size than shown here that covers not only the air channel 14b for final blow 11 of the glass container 12, but also one or more finish cooling channel(s) 20 for a finish cooling air flow 21 as for example shown in FIG. 4.



FIG. 22 shows a perspective view of a blow head BH according to the present invention showing the air channel's 14b insert area 15 that is adapted to the geometry of a particle filter F according to the present invention for insertion of said particle filter F according to the present invention from upside.



FIG. 23 shows a perspective view of a blow head BH according to FIG. 22 from downside showing the air channel 14b leading to the air inlet of the finish mold 8 through the pressurized air flows into the glass container's 12 inner space as final blow 11.



FIG. 24 shows a sectional view of a blow head BH according to the present invention comprising at least an air channel 14b for final blow 11 of a glass container 12 and said blow head BH suitable for placement above a finish mold 8 station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, preferably an I.S. glass machine, said blow head BH adapted to receive a particle filter F according to the present invention and said particle filter F already placed (inserted here) in at least said air channel 14b of said blow head BH adapted to said particle filter F. Here the blow head BH is adapted to the particle filter F in an insert area 15 at the upper end of the air channel 14b that leads to the air inlet of the finish mold 8 through the pressurized air flows into the glass container's 12 inner space as final blow 11.



FIG. 25 shows a perspective view of a blow head BH according to the present invention comprising at least an air channel 14b with a particle filter F already placed in at least said air channel 14b.



FIG. 26 shows a partly sectional view of a blow head BH according to the present invention partially opened and comprising at least an air channel with 14b and a particle filter F already placed in at least said air channel 14b.



FIG. 27 shows a sectional view of a blow head BH according to the present invention comprising at least an air channel 14b with a particle filter F already placed, but wrongly placed in at least said air channel 14b. As a consequence of this improperly placement of the particle filter F in the air channel 14b of the blow head BH said particle filter F projects beyond said blow head BH and thus, the blow head BH cannot be installed in the finish mold 8 forming station of the glass forming machine. Therefore a faulty assembly could be avoided effectively using this embodiment of the present invention.



FIG. 28 shows a perspective view of a blow head BH according to the present invention comprising at least an air channel 14b with a particle filter F wrongly placed in said air channel 14b according to FIG. 27.



FIG. 29 shows a partly sectional view of a blow head BH partially opened according to FIG. 27.



FIG. 30 shows a sectional view of the air flow of a final blow 11 in a blow head BH according to the present invention. The pressurized air enters the blow head BH from upwards passing the particle filter F at the upper end of the air channel 14b that leads to the air inlet of the finish mold 8 through the pressurized air flows into the glass container's 12 inner space as final blow 11. By passing the particle filter F according to the present invention undesired particles will be separated and collected on the dirty side (here the upside) of said particle filter F.



FIG. 31 shows a side view of the air flow of a final blow 11 in a blow head BH according to FIG. 29.



FIG. 32 shows a pressure drop chart from experiments with a main filter media with a maximum pore size of 110 micron (in the United States: US mesh 165). Four experiments took place:

    • A 1st experiment with 1 vent without the filter (upper line with dots placed on the line) and also 1 vent with the filter (upper line without dots),
    • a 2nd experiment with 2 vents without the filter (second line from the top with dots placed on the line) and also 2 vents with the filter (second line from the top without dots),
    • a 3rd experiment with 3 vents without the filter (second line from the bottom with dots placed on the line) and also 3 vents with the filter (second line from the bottom without dots), and
    • a 4th experiment with 4 vents without the filter (lower line with dots placed on the line) and also 4 vents with the filter (lower line without dots).


For each of the aforesaid experiments the x-axis of the pressure drop diagram of FIG. 32 shows the input pressure in psi (psi=pound force per square inch; psi could be convertetd into Pascal [Pa] under the assumption of a gravitational constant of g=9.80665 ml s2 and a US pound as lb=0.4536 kg as follows: 1 psi≈6 895 Pa and vice versa 1 Pa≈1.4504·10−4 psi) at the regulator and the y-axis the (resulting) output pressure in psi.


One can read from the pressure drop diagram shown here that there is no or no significant pressure drop using the main filter media with a maximum pore size of 110 micron (in the United States: US mesh 165).



FIG. 33 shows in the upper row a set of four unmounted parts of another preferred embodiment of a particle filter F according to the present invention with said parts as circular discs or disc like parts PS, MF, PF, FB, FM shown in an bird's eye view on the surface of said discs or disc like parts PS, MF, PF, FB, FM, wherein a main filter media wire mesh disc MF that has to be positioned between a protective filter media wire mesh disc PF and a support mean wire mesh disc PS should be held together with said protective filter media wire mesh disc PF and said support mean wire mesh disc PS by a filter body ring FB and a fastening mean, here a press ring FM, if the press ring FM is inserted into said filter body ring FB with interference fit to said filter body ring FB.


Below the upper row a mounted preferred particle filter F according to the present invention is shown also from an birds eye view perspective.


The particle filter F according to the present invention as shown here is of—preferably larger—size that covers not only the air channel 14b for final blow 11 of the glass container 12, but also one or more finish cooling channel(s) 20 of a blow head BH for a finish cooling air flow 21 as for example shown in FIG. 4. The compressed air flows through a central hole CH in the filter body ring FB of the particle filter F for the final blow 11 as well as a respective hole CH in the the press ring FM of the particle filter F and for the finish cooling 21 through (a) peripheral hole(s) PH as well as (a) respective hole(s) PH in the the press ring FM of the particle filter F.


While the present disclosure has been illustrated and described with respect to a particular embodiment thereof, it should be appreciated by those of ordinary skill in the art that various modifications to this disclosure may be made without departing from the spirit and scope of the present disclosure.

Claims
  • 1. A particle filter for a glass forming machine operating according to a blow-and-blow process or according to a press-and-blow process, said particle filter is adapted for placing in at least an air channel serving pressurized air for counter blow of a parison in a blank mold forming station of said glass forming machine, and/or an air channel serving pressurized air for final blow and/or for finish cooling of a glass container made of said parison in a finish mold station of said glass forming machine, said particle filter comprising: a surface filter as a main filter media that prevents passage of particles above a certain size from a dirty side of said main filter media to a clean side of said main filter media and that also prevents final passage of said particles above said certain size into said parison or said glass container blown by said glass forming machine;an additional surface filter as a protective filter media more coarse than said main filter media and wherein said protective filter media is situated on said dirty side of said main filter media in order to protect said main filter media against impact of particles; anda porous support that is more coarse than said main filter media and is situated on said clean side of said main filter media to stabilize said main filter media against forces arising from particles arriving on said dirty side of said main filter media;wherein said main filter media is situated between said protective filter media and said porous support; andwherein said main filter media that is situated between said protective filter media and said porous support is held together with said protective filter media and said porous support by a filter body and a fastening that is inserted into said filter body with interference fit to said filter body or screwed together with said filter body; andwherein said particle filter is adapted for placing in at least said air channel due to its geometry wherein the outer dimension of said filter body overlaps the outer dimension of said fastening.
  • 2. The particle filter for a glass forming machine according to claim 1, wherein said particle filter is adapted for placing in at least: said air channel situated in a plunger unit and serving pressurized air for counter blow of said parison in said blank mold forming station of said glass forming machine and said plunger unit situated in a plunger cylinder underneath said blank mold forming station of said glass forming machine, and/orsaid air channel situated in a blow head and serving pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and said blow head situated above said finish mold station of said glass forming machine, and/orsaid air channel situated in a blow head support for supply of said blow head with pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and for support of said blow head and said blow head support situated above said blow head that is situated itself above said finish mold station of said glass forming machine, andwherein said particle filter is adapted to be placed in at least:said air channel situated in said plunger unit and serving pressurized air for counter blow of said parison in said blank mold forming station of said glass forming machine and air plunger unit situated in said plunger cylinder underneath said blank mold forming station of said glass forming machine, and/orsaid air channel situated in said blow head and serving pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and said blow head situated above said finish mold station of said glass forming machine, and/orsaid air channel situated in said blow head support for supply of said blow head with pressurized air for final blow and/or for finish cooling of said glass container made of said parison in said finish mold station and for support of said blow head and said blow head support situated above said blow head that is situated itself above said finish mold station of said glass forming machine,to prevent the passage of said particles above said certain size from said dirty side of said main filter media to said clean side of said main filter media and thus also avoids the final passage of said particles into said parison or said glass container blown by said glass forming machine.
  • 3. The particle filter for a glass forming machine according to claim 2, wherein said glass forming machine operating according to said blow-and-blow process or to said press-and-blow process is of an I.S. glass forming machine type.
  • 4. The particle filter for a glass forming machine according to claim 1, wherein said glass forming machine operating according to said blow-and-blow process or to said press-and-blow process is of an I.S. glass forming machine type.
  • 5. The particle filter for a glass forming machine according to claim 1, wherein said main filter media comprises a slotted filter.
  • 6. The particle filter for a glass forming machine according to claim 5, wherein said slotted filter comprises a silicon substrate covered by a layer of silicon nitride.
  • 7. The particle filter for a glass forming machine according to claim 1, wherein said main filter media comprises a sieve filter.
  • 8. The particle filter for a glass forming machine according to claim 7, wherein said sieve filter comprises a silicon substrate covered by a layer of silicon nitride.
  • 9. The particle filter for a glass forming machine according to claim 7, wherein said sieve filter of said main filter media comprises a wire mesh made of anti-corrosive material.
  • 10. The particle filter for a glass forming machine according to claim 9, wherein said anti-corrosive material of said sieve filter of said main filter media is stainless steel.
  • 11. The particle filter for a glass forming machine according to claim 9, wherein said mesh of said sieve filter of said main filter media is made of an anti-corrosive metal or metal alloy and is also passivated by electropolishing.
  • 12. The particle filter for a glass forming machine according to claim 9, wherein said main filter media has a maximum pore size of 100 micron (US mesh 160).
  • 13. The particle filter for a glass forming machine according to claim 12, wherein said main filter media has a pore size of 100 micron (US mesh 160).
  • 14. The particle filter for a glass forming machine according to claim 12, wherein said main filter media has a maximum pore size of 40 micron (US mesh 325).
  • 15. The particle filter for a glass forming machine according to claim 14, wherein said main filter media has a pore size of 40 micron (US mesh 325).
  • 16. The particle filter for a glass forming machine according to claim 14, wherein said main filter media has a maximum pore size of 25 micron (US mesh 500).
  • 17. The particle filter for a glass forming machine according to claim 16, wherein said main filter media has a pore size of 25 micron (US mesh 500).
  • 18. The particle fitler for a glass forming machine according to claim 9, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 200 N/mm2.
  • 19. The particle fitler for a glass forming machine according to claim 9, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 350 N/mm2.
  • 20. The particle fitler for a glass forming machine according to claim 9, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 450 N/mm2.
  • 21. The particle filter for a glass forming machine according to claim 1, wherein said protective filter media comprises a wire mesh made of anti-corrosive material.
  • 22. The particle filter for a glass forming machine according to claim 21, wherein said anti-corrosive material of said wire mesh of said protective filter media is stainless steel.
  • 23. The particle filter for a glass forming machine according to claim 21, wherein said mesh of said protective filter media is made of an anti-corrosive metal or metal alloy and is also passivated by electropolishing.
  • 24. The particle fitler for a glass forming machine according to claim 21, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 200 N/mm2.
  • 25. The particle fitler for a glass forming machine according to claim 21, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 350 N/mm2.
  • 26. The particle fitler for a glass forming machine according to claim 21, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 450 N/mm2.
  • 27. The particle fitler for a glass forming machine according to claim 21, wherein a mesh wire diameter of the wire mesh is thicker than a mesh wire diameter of said main filter media.
  • 28. The particle filter for a glass forming machine according to claim 1, wherein said porous support comprises a wire mesh that is more coarse than said main filter media itself.
  • 29. The particle filter for a glass forming machine according to claim 28, wherein said porous support comprises a wire mesh made of anti-corrosive material.
  • 30. The particle filter for a glass forming machine according to claim 29, wherein said anti-corrosive material of said mesh of said porous support is stainless steel.
  • 31. The particle filter for a glass forming machine according to claim 29, wherein said mesh of said porous support is made of an anti-corrosive metal or metal alloy and is also passivated, by electropolishing.
  • 32. The particle fitler for a glass forming machine according to claim 29, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 200 N/mm2.
  • 33. The particle fitler for a glass forming machine according to claim 29, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 350 N/mm2.
  • 34. The particle fitler for a glass forming machine according to claim 29, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 450 N/mm2.
  • 35. The particle filter for a glass forming machine according to claim 1, wherein said filter body and said fastening is made of an anti-corrosive material.
  • 36. The particle filter for a glass forming machine according to claim 35, wherein said anti-corrosive material of said filter body and said fastening is made of stainless steel.
  • 37. The particle filter for a glass forming machine according to claim 35, wherein said anti-corrosive material of said filter body and said fastening is made of an anti-corrosive metal and is also passivated by electropolishing.
  • 38. The particle fitler for a glass forming machine according to claim 35, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 200 N/mm2.
  • 39. The particle fitler for a glass forming machine according to claim 35, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 350 N/mm2.
  • 40. The particle fitler for a glass forming machine according to claim 35, wherein the anti-corrosive material is an anti-corrosive metal or metal alloy with a minimum yield strength of 450 N/mm2.
  • 41. The particle filter for a glass forming machine according to claim 1, wherein said main filter media and said protective filter media and said porous support are each a circular disc and wherein said filter body is a filter body ring and said fastening is a fastening ring that is inserted into said filter body ring with cylindrical interference fit to said filter body ring or screwed together with said filter body ring and wherein the outer diameter of said filter body ring overlaps the outer diameter of said press ring.
  • 42. A plunger unit comprising at least an air channel for counter blow of a parison and said plunger unit being adapted to be positioned in a plunger cylinder underneath a blank mold forming station of a glass forming machine of a blow-and-blow process-type, wherein said air channel of said plunger unit is adapted to receive a particle filter according to claim 1 and said plunger unit air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said plunger unit air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said plunger unit air channel and wherein said particle filter is placed in at least said air channel of said plunger unit adapted to said particle filter.
  • 43. The plunger unit according to claim 42, wherein said plunger unit air channel is adapted to said particle filter in such a way that said particle filter projects beyond said plunger unit if improperly placed in said plunger unit air channel.
  • 44. The plunger unit according to claim 42, wherein said particle filter is secured in said plunger unit air channel by a safety ring that fits into a slot of said plunger unit air channel.
  • 45. The plunger unit according to claim 44, wherein the safety ring is a Seegering™.
  • 46. The glass forming machine according to claim 42, wherein the glass forming machine of a blow-and-blow process-type is an I.S. glass machine.
  • 47. A blow head comprising at least an air channel for final blow and/or for finish cooling of a glass container made of a parison and said blow head being adapted to be positioned above a finish mold station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, wherein said air channel of said blow head is adapted to receive a particle filter according to claim 1 and said blow head air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said blow head air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said blow head air channel and where said particle filter is placed in at least said air channel of said blow head adapted to said particle filter.
  • 48. The blow head according to claim 47, wherein said blow head air channel is adapted to said particle filter in such a way that said particle filter projects beyond said blow head if improperly placed in said blow head air channel.
  • 49. The blow head according to claim 47, wherein said particle filter is secured in said blow head air channel by a safety ring that fits into a slot of said blow head air channel.
  • 50. The glass forming machine according to claim 49, wherein the safety ring is a Seegering™.
  • 51. The glass forming machine according to claim 47, wherein the glass forming machine of a blow-and-blow process-type or a press-and-blow process-type is an I.S. glass machine.
  • 52. A blow head support for support of a blow head comprising at least an air channel for supply of said blow head with pressurized air and said blow head support being adapted to be positioned above said blow head which itself is adapted to be positioned above a finish mold station of a glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, wherein said air channel of said blow head support is adapted to receive a particle filter according to claim 1 and said blow head support air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said blow head support air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said blow head support air channel and wherein said particle filter is placed in at least said air channel of said blow head support adapted to receive said particle filter.
  • 53. The blow head support according to claim 52, wherein said blow head support air channel is adapted to said particle filter in such a way that said particle filter projects beyond said blow head support if improperly placed in said blow head support air channel.
  • 54. The blow head support according to claim 52, wherein said particle filter is secured in said blow head support air channel by a safety ring that fits into a slot of said blow head support air channel.
  • 55. The glass forming machine according to claim 54, wherein the safety ring is a Seegering™.
  • 56. The glass forming machine according to claim 52, wherein the glass forming machine of a blow-and-blow process-type or a press-and-blow process-type is an I.S. glass machine.
  • 57. A glass forming machine of a blow-and-blow process-type or a press-and-blow process-type, said glass forming machine adapted to receive at least one particle filter according to claim 1 and wherein said glass forming machine comprises an air channel serving pressurized air for counter blow of a parison in a blank mold forming station of said glass forming machine and/or an air channel serving pressurized air for final blow and/or for finish cooling of a glass container made of said parison in a finish mold station of said glass forming machine and said air channel of said glass forming machine is adapted to receive said particle filter and said glass forming machine air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said glass forming machine air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said air channel and wherein said particle filter is placed in at least said air channel of said glass forming machine adapted to receive said particle filter.
  • 58. The glass forming machine according to claim 57, wherein said particle filter is secured in said glass forming machine air channel by a safety ring that fits into a slot of said glass forming machine air channel.
  • 59. The glass forming machine according to claim 58, wherein the safety ring is a Seegering™.
  • 60. The glass forming machine according to claim 57, wherein said glass forming machine comprises a plunger unit comprising at least an air channel for counter blow of the parison and said plunger unit being adapted to be positioned in a plunger cylinder underneath the blank mold forming station of the glass forming machine, wherein said air channel of said plunger unit is adapted to receive said particle filter and said plunger unit air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said plunger unit air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said plunger unit air channel and wherein said particle filter is placed in at least said air channel of said plunger unit adapted to said particle filter.
  • 61. The glass forming machine according to claim 57, wherein said glass forming machine comprises a blow head comprising at least an air channel for final blow and/or for finish cooling of the glass container made of the parison and said blow head being adapted to be positioned above the finish mold station of the glass forming machine, wherein said air channel of said blow head is adapted to receive said particle filter and said blow head air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said blow head air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said blow head air channel and where said particle filter is placed in at least said air channel of said blow head adapted to said particle filter; and/or a blow head support for supporting the blow head comprising at least an air channel for supplying said blow head with pressurized air and said blow head support being adapted to be positioned above said blow head which itself is adapted to be positioned above the finish mold station of the glass forming machine, wherein said air channel of said blow head support is adapted to receive said particle filter and said blow head support air channel is adapted to said particle filter in such a way that said particle filter can properly be placed in said blow head support air channel only in a position, in which said particle filter's main filter media's dirty side is situated on the incoming air side of said blow head support air channel and wherein said particle filter is placed in at least said air channel of said blow head support adapted to receive said particle filter.
  • 62. The glass forming machine according to claim 57, wherein said glass forming machine of said blow-and-blow process-type or said press-and-blow process-type is an I.S. glass forming machine.
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a National Stage application of International Patent Application No. PCT/EP2015/000244, filed on Feb. 6, 2015, which claims priority to U.S. Provisional Application No. 62/079,208, filed on Nov. 13, 2014, each of which is hereby incorporated by reference in its entirety.

PCT Information
Filing Document Filing Date Country Kind
PCT/EP2015/000244 2/6/2015 WO 00
Publishing Document Publishing Date Country Kind
WO2016/074750 5/19/2016 WO A
US Referenced Citations (382)
Number Name Date Kind
2752731 Altosaar Jul 1956 A
3615958 Cohen Oct 1971 A
3630700 Hammel Dec 1971 A
3632414 Dayton et al. Jan 1972 A
3645711 Pirooz Feb 1972 A
3645777 Sierad Feb 1972 A
3646908 Bowen et al. Mar 1972 A
3647490 Pirooz Mar 1972 A
3650721 Hammel et al. Mar 1972 A
3652318 Heins Mar 1972 A
3714055 Matsuura et al. Jan 1973 A
3734802 Cohen May 1973 A
3785722 Schultz Jan 1974 A
3808035 Stelter Apr 1974 A
3817211 Brown et al. Jun 1974 A
3833387 Reed et al. Sep 1974 A
3863177 Damen et al. Jan 1975 A
3865540 Loeffler Feb 1975 A
3919437 Brown et al. Nov 1975 A
3923487 Lewis Dec 1975 A
3923533 Hammel et al. Dec 1975 A
3923688 Hammel et al. Dec 1975 A
3929440 Oldfield Dec 1975 A
3951547 Fujinami et al. Apr 1976 A
3955953 Hauser May 1976 A
3972720 Hammel et al. Aug 1976 A
3972721 Hammel et al. Aug 1976 A
4021217 Bondybey et al. May 1977 A
4022602 Pavlopoulos May 1977 A
4022628 Deeg May 1977 A
4026420 Cuniberti May 1977 A
4065283 Asahara et al. Dec 1977 A
4065317 Baak et al. Dec 1977 A
4093771 Goldstein et al. Jun 1978 A
4095986 Matsuda et al. Jun 1978 A
4099883 Berger et al. Jul 1978 A
4105577 Yamashita Aug 1978 A
4106857 Snitzer Aug 1978 A
4106946 Ritze Aug 1978 A
4110245 Yamashita Aug 1978 A
4162910 Lining Jul 1979 A
4168959 Loeffler Sep 1979 A
4196837 Burkart et al. Apr 1980 A
4214972 Shintock Jul 1980 A
4247034 Burkart et al. Jan 1981 A
4261720 Helbing Apr 1981 A
4268294 Laughlin et al. May 1981 A
4288250 Yamashita Sep 1981 A
4293004 Lowe Oct 1981 A
4297142 Ritze Oct 1981 A
4303298 Yamashita Dec 1981 A
4305982 Hirsch Dec 1981 A
4323381 Matsuyama et al. Apr 1982 A
4324576 Matsuyama et al. Apr 1982 A
4347326 Iwami et al. Aug 1982 A
4363647 Bachman et al. Dec 1982 A
4382451 Lowe May 1983 A
4390357 Myers et al. Jun 1983 A
4407669 Nelson Oct 1983 A
4431692 Hofmann et al. Feb 1984 A
4439270 Powell Mar 1984 A
4445919 Cole et al. May 1984 A
4493722 Ono Jan 1985 A
4495223 Lalancette et al. Jan 1985 A
4516934 Nelson et al. May 1985 A
4519827 Jones May 1985 A
4521524 Yamashita Jun 1985 A
4524000 Clayfield et al. Jun 1985 A
4528012 Sturgill Jul 1985 A
4552578 Anderson Nov 1985 A
4586980 Hirai et al. May 1986 A
4588540 Kiefer et al. May 1986 A
4604119 Kuhl et al. Aug 1986 A
4615916 Henderson Oct 1986 A
4626071 Wada et al. Dec 1986 A
4657048 Foster Apr 1987 A
4741962 Wada et al. May 1988 A
4741963 Wada et al. May 1988 A
4769347 Cook et al. Sep 1988 A
4822392 Fachat et al. Apr 1989 A
4828597 Glascock, II et al. May 1989 A
4842620 Hammel et al. Jun 1989 A
4853001 Hammel Aug 1989 A
4853017 Eberle et al. Aug 1989 A
4871695 Seki et al. Oct 1989 A
4894303 Wu Jan 1990 A
4921519 Schinker et al. May 1990 A
4927442 Greulich et al. May 1990 A
4935094 Mixon et al. Jun 1990 A
4999071 Nakamura et al. Mar 1991 A
5007948 Araujo Apr 1991 A
5024974 Nakamura et al. Jun 1991 A
5028251 Schinker et al. Jul 1991 A
5034044 Glascock, II Jul 1991 A
5036025 Lin Jul 1991 A
5040880 Morimoto et al. Aug 1991 A
5061659 Ciolek et al. Oct 1991 A
5078771 Wu Jan 1992 A
5081953 Guthrie et al. Jan 1992 A
5087323 Park Feb 1992 A
5118371 Hori et al. Jun 1992 A
5120341 Nozawa et al. Jun 1992 A
5126006 Cronin et al. Jun 1992 A
5133791 Yagami et al. Jul 1992 A
5133795 Glascock, II Jul 1992 A
5145805 Tarumi et al. Sep 1992 A
5211734 Yagami et al. May 1993 A
5234594 Tonucci et al. Aug 1993 A
5249076 Fujiwara et al. Sep 1993 A
5234871 Krashkevich Oct 1993 A
5253258 Lawandy Oct 1993 A
5285517 Wu Feb 1994 A
5324691 Tarumi et al. Jun 1994 A
5383038 Lawandy Jan 1995 A
5383946 Naka et al. Jan 1995 A
5396080 Hannotiau et al. Mar 1995 A
5430236 de Macedo et al. Jul 1995 A
5437702 Burns Aug 1995 A
5464566 Ito et al. Nov 1995 A
5468344 Inoue et al. Nov 1995 A
5476990 Hittner et al. Dec 1995 A
5481630 Lawandy Jan 1996 A
5520855 Ito et al. May 1996 A
5524011 Lawandy Jun 1996 A
5552467 Reiter et al. Sep 1996 A
5562951 Kamen Oct 1996 A
5597614 Noguchi et al. Jan 1997 A
5614255 Kimura et al. Mar 1997 A
5616296 Hittner et al. Apr 1997 A
5616532 Heller et al. Apr 1997 A
5639517 Floch et al. Jun 1997 A
5662050 Angelo, II et al. Sep 1997 A
5665422 Endo et al. Sep 1997 A
5667888 Yoshida et al. Sep 1997 A
5679466 Noguchi et al. Oct 1997 A
5707685 Endou et al. Jan 1998 A
5711018 Hittner et al. Jan 1998 A
5717051 Hiraoka et al. Feb 1998 A
5742118 Endo et al. Apr 1998 A
5750448 Grabowski et al. May 1998 A
5792711 Roberts Aug 1998 A
5849200 Heller et al. Dec 1998 A
5851251 Kondo et al. Dec 1998 A
5854169 Heller et al. Dec 1998 A
5858541 Hiraoka et al. Jan 1999 A
5876475 Kozora Mar 1999 A
5908561 Palm et al. Jun 1999 A
5922138 Shindo et al. Jul 1999 A
5928527 Li et al. Jul 1999 A
5942793 Senoo et al. Aug 1999 A
5990060 Ohmi et al. Nov 1999 A
6020028 Kinneberg Feb 2000 A
6036735 Carter et al. Mar 2000 A
6074981 Tada et al. Jun 2000 A
6093484 Oguma Jul 2000 A
6093676 Heller et al. Jul 2000 A
6109278 Shindo et al. Aug 2000 A
6110528 Kimura et al. Aug 2000 A
6111227 Cress Aug 2000 A
6119483 Takahashi et al. Sep 2000 A
6129899 Katsuro et al. Oct 2000 A
6168835 Carter et al. Jan 2001 B1
6171652 Singh et al. Jan 2001 B1
6176702 Mohr et al. Jan 2001 B1
6187099 Blaudszun Feb 2001 B1
6192715 Orita et al. Feb 2001 B1
6194346 Tada et al. Feb 2001 B1
6206191 Singh et al. Mar 2001 B1
6211424 Powell et al. Apr 2001 B1
6211526 Huston et al. Apr 2001 B1
6214249 Li et al. Apr 2001 B1
6221268 Li et al. Apr 2001 B1
6233974 Anderson et al. May 2001 B1
6235667 Paloschi et al. May 2001 B1
6284314 Kato et al. Sep 2001 B1
6287683 Itoh et al. Sep 2001 B1
6289694 Pieper Sep 2001 B1
6301936 Ohga et al. Oct 2001 B1
6307212 Huston et al. Oct 2001 B1
6312317 Oguma Nov 2001 B1
6319331 Kume et al. Nov 2001 B1
6323585 Crane et al. Nov 2001 B1
6339940 Yamada et al. Jan 2002 B1
6342460 Akimoto et al. Jan 2002 B1
6358873 Stewart Mar 2002 B1
6387844 Fujishima et al. May 2002 B1
6392683 Hayashi May 2002 B1
6417879 Hayashi Jul 2002 B2
6427489 Eda et al. Aug 2002 B1
6430965 Eda et al. Aug 2002 B2
6468403 Shimizu et al. Oct 2002 B1
6501499 Hayashi Dec 2002 B2
6525315 Motoyama Feb 2003 B1
6527547 De Bruin et al. Mar 2003 B2
6563126 Motoyama May 2003 B1
6584805 Burns et al. Jul 2003 B1
6587136 Hayashi Jul 2003 B2
6641663 Kemmochi et al. Nov 2003 B2
6656321 Furukawa Dec 2003 B2
6677260 Crane et al. Jan 2004 B2
6696228 Muraoka et al. Feb 2004 B2
6698249 Yagi et al. Mar 2004 B1
6709518 Kojima et al. Mar 2004 B2
6716779 Lin Apr 2004 B2
6733827 Mitchell et al. May 2004 B2
6748769 Ooishi et al. Jun 2004 B2
6780516 Chen Aug 2004 B2
6783845 Zhang et al. Aug 2004 B2
6789401 Dabby et al. Sep 2004 B1
6793769 Kajino et al. Sep 2004 B2
6796144 Shepard et al. Sep 2004 B2
6828719 Huang et al. Dec 2004 B1
6844976 Firon et al. Jan 2005 B1
6849242 Koeppler et al. Feb 2005 B1
6881445 Arora Apr 2005 B1
6903036 Akimoto et al. Jun 2005 B2
6913643 Dejaiffe Jul 2005 B2
6936306 Barron et al. Aug 2005 B1
6939611 Fujishima et al. Sep 2005 B2
6942288 Paetz et al. Sep 2005 B2
7040960 Hench et al. May 2006 B2
7127918 Vitkala et al. Oct 2006 B2
7143612 Ishihara Dec 2006 B2
7144633 Zguris et al. Dec 2006 B2
7157840 Fujishima et al. Jan 2007 B2
7171973 Orii et al. Feb 2007 B2
7175833 Algar Feb 2007 B1
7186441 Mitchell et al. Mar 2007 B2
7189783 Kozawa et al. Mar 2007 B2
7327074 Fujishima et al. Feb 2008 B2
7373791 Leehr May 2008 B1
7404407 Orii et al. Jul 2008 B2
7441417 Park et al. Oct 2008 B2
7451623 Dabby et al. Nov 2008 B2
7451624 Dabby et al. Nov 2008 B2
7507618 Dunbar Mar 2009 B2
7538051 Fujiwara et al. May 2009 B2
7670974 Fujiwara et al. Mar 2010 B2
7726153 Ooishi et al. Jun 2010 B2
7891066 Aoki et al. Feb 2011 B2
8042359 Coppola et al. Oct 2011 B2
8047023 Ackerman et al. Nov 2011 B2
8079234 Yoshida Dec 2011 B2
8123970 Durante et al. Feb 2012 B2
8281620 Sudo et al. Oct 2012 B1
8298369 Maeda et al. Oct 2012 B2
8420191 Yamagata et al. Apr 2013 B2
8420192 Yamagata et al. Apr 2013 B2
8460769 Yamagata et al. Jun 2013 B2
8476353 Higashiyama et al. Jul 2013 B2
8635888 Dabby et al. Jan 2014 B2
8641829 Horita et al. Feb 2014 B2
8728338 Ohmi et al. May 2014 B2
8733127 Yamagata et al. May 2014 B2
20010003299 Furukawa Jun 2001 A1
20010028385 Hayashi Oct 2001 A1
20010028386 Hayashi Oct 2001 A1
20010028390 Hayashi Oct 2001 A1
20010037662 Kohmura et al. Nov 2001 A1
20010039810 Eda et al. Nov 2001 A1
20010040136 Wei et al. Nov 2001 A1
20010044370 Crane et al. Nov 2001 A1
20020000192 Kojima et al. Jan 2002 A1
20020006594 De Bruin et al. Jan 2002 A1
20020062666 Ooishi et al. May 2002 A1
20020072461 Akimoto et al. Jun 2002 A1
20020077243 Sircar Jun 2002 A1
20020107144 Fujishima et al. Aug 2002 A1
20020115781 Pourreau et al. Aug 2002 A1
20020150686 Mitchell et al. Oct 2002 A1
20020157421 Ackerman et al. Oct 2002 A1
20020178757 Chinn Dec 2002 A1
20030003228 Ooishi et al. Jan 2003 A1
20030010671 Orii et al. Jan 2003 A1
20030012899 Kemmochi et al. Jan 2003 A1
20030015004 Nakamura et al. Jan 2003 A1
20030024269 Shepard et al. Feb 2003 A1
20030050173 Lin Mar 2003 A1
20030061834 Vitkala et al. Apr 2003 A1
20030075694 Motoyama Apr 2003 A1
20030076487 Cannon et al. Apr 2003 A1
20030079835 Kajino et al. May 2003 A1
20030096701 Fujishima et al. May 2003 A1
20030101770 Nakamura et al. Jun 2003 A1
20030106491 Kemmochi et al. Jun 2003 A1
20030125187 Akimoto et al. Jul 2003 A1
20030126890 Orita et al. Jul 2003 A1
20030136511 Balasubramhanya et al. Jul 2003 A1
20030148113 Chen Aug 2003 A1
20030152763 Zhang et al. Aug 2003 A1
20030157801 Kozawa et al. Aug 2003 A1
20030196986 Tsung-Kuei et al. Oct 2003 A1
20030198660 Janas et al. Oct 2003 A1
20030225188 Horie Dec 2003 A1
20040006158 Horie et al. Jan 2004 A1
20040006159 Horie et al. Jan 2004 A1
20040040497 Kemmochi et al. Mar 2004 A1
20040055339 Ishihara Mar 2004 A1
20040060326 Ishihara Apr 2004 A1
20040063811 Horie et al. Apr 2004 A1
20040134236 Ishihara Jul 2004 A1
20040137827 Hench et al. Jul 2004 A1
20040162210 Dejaiffe Aug 2004 A1
20040172977 Nakamura et al. Sep 2004 A1
20040176499 Herrmann et al. Sep 2004 A1
20040183342 Paetz et al. Sep 2004 A1
20040206120 Yamamura Oct 2004 A1
20040219293 Mitchell et al. Nov 2004 A1
20040232819 Huang et al. Nov 2004 A1
20040244426 Park et al. Dec 2004 A1
20040247892 Chen Dec 2004 A1
20040251810 Hsu Dec 2004 A1
20040254265 Mizutani et al. Dec 2004 A1
20040259714 Fujiwara et al. Dec 2004 A1
20050000251 Dabby et al. Jan 2005 A1
20050032932 Salenbien Feb 2005 A1
20050095404 Schillert et al. May 2005 A1
20050109066 Dabby et al. May 2005 A1
20050143250 Fujiwara et al. Jun 2005 A1
20050148454 Hachitani Jul 2005 A1
20050148688 Mizutani et al. Jul 2005 A1
20050148689 Mizutani et al. Jul 2005 A1
20050166495 Cho et al. Aug 2005 A1
20050171236 Johnke et al. Aug 2005 A1
20050186412 Arora Aug 2005 A1
20050192380 Horie et al. Sep 2005 A1
20050199014 Nakamura et al. Sep 2005 A1
20050239918 Nakazawa et al. Oct 2005 A1
20050268408 Chin Dec 2005 A1
20060005579 Jacobsen et al. Jan 2006 A1
20060086147 Ooishi et al. Apr 2006 A1
20060099328 Waite et al. May 2006 A1
20060189713 Herrmann et al. Aug 2006 A1
20060196527 Nishimura et al. Sep 2006 A1
20060225999 Fukawa et al. Oct 2006 A1
20060238100 Miyata et al. Oct 2006 A1
20070032571 Furuno et al. Feb 2007 A1
20070054981 Yanagi et al. Mar 2007 A1
20070009579 Shinozaki et al. May 2007 A1
20070095791 Shinozaki et al. May 2007 A1
20070099787 Hayden et al. May 2007 A1
20070105379 Orii et al. May 2007 A1
20070105380 Orii et al. May 2007 A1
20070157676 Taquet et al. Jul 2007 A1
20070221615 Maeda et al. Sep 2007 A1
20070221617 Takahashi Sep 2007 A1
20070230181 Fujishima et al. Oct 2007 A1
20070271756 Aoki et al. Nov 2007 A1
20070271957 Nakamura et al. Nov 2007 A1
20080011713 Ito Jan 2008 A1
20080017502 Fukawa et al. Jan 2008 A1
20080148781 Yoshida Jun 2008 A1
20090038346 Dabby et al. Feb 2009 A1
20090038543 Dabby et al. Feb 2009 A1
20100212364 Suzuki et al. Aug 2010 A1
20110023543 Umetsu et al. Feb 2011 A1
20110079047 Suzuki et al. Apr 2011 A1
20110090933 Gibbs et al. Apr 2011 A1
20110143063 Yamagata et al. Jun 2011 A1
20110177290 Tomamoto et al. Jul 2011 A1
20110177325 Tomamoto et al. Jul 2011 A1
20110192758 Yamagata et al. Aug 2011 A1
20110200812 Tomamoto et al. Aug 2011 A1
20110240663 Yamagata et al. Oct 2011 A1
20110251293 Trummer et al. Oct 2011 A1
20110255161 Yoneda Oct 2011 A1
20110256330 Yamagata et al. Oct 2011 A1
20120024012 Yamada Feb 2012 A1
20120056106 Neumann Mar 2012 A1
20120073329 Fernald et al. Mar 2012 A1
20120118018 Orita et al. May 2012 A1
20120165178 Ritter et al. Jun 2012 A1
20120182614 Yoneda Jul 2012 A1
20120198889 Nakamura et al. Aug 2012 A1
20120207995 Shelestak et al. Aug 2012 A1
20120264872 Weiss et al. Oct 2012 A1
20120266634 Folk et al. Oct 2012 A1
20120272682 Sudo et al. Nov 2012 A1
20130227990 Yamagata et al. Sep 2013 A1
20130227991 Yamagata et al. Sep 2013 A1
20140150715 Yamagata Jun 2014 A1
20160052817 Ueda Feb 2016 A1
Foreign Referenced Citations (333)
Number Date Country
1084711 Sep 1980 CA
2137800 May 1993 CA
2137800 Jun 1993 CA
2137800 Jan 2003 CA
2483339 Oct 2004 CA
1127226 Jul 1996 CN
1899995 Jan 2007 CN
2007078876 Jul 2007 CN
101016188 Aug 2007 CN
101041556 Sep 2007 CN
101048488 Oct 2007 CN
101186424 May 2008 CN
201334433 Oct 2009 CN
101659521 Mar 2010 CN
201746462 Feb 2011 CN
101016188 Jun 2011 CN
102378925 Mar 2012 CN
102408192 Apr 2012 CN
102417294 Apr 2012 CN
202181248 Apr 2012 CN
101186424 May 2012 CN
102618170 Aug 2012 CN
102795782 Nov 2012 CN
103058502 Apr 2013 CN
202849253 Apr 2013 CN
101659521 Jul 2013 CN
102795782 Jun 2014 CN
32 33 211 Mar 1983 DE
691 03 444 Nov 1994 DE
691 22 586 Feb 1997 DE
19532800 Feb 1997 DE
698 12 251 Nov 2003 DE
4392738 Jun 2006 DE
202021012718 Sep 2013 DE
0137927 Apr 1985 EP
0148238 Jul 1985 EP
0166370 Jan 1986 EP
0166371 Jan 1986 EP
0265051 Apr 1986 EP
0399577 Nov 1990 EP
0422557 Apr 1991 EP
0 444 793 Sep 1991 EP
0447678 Sep 1991 EP
0452922 Oct 1991 EP
0456351 Nov 1991 EP
0470449 Feb 1992 EP
0 476 218 Mar 1992 EP
0504926 Sep 1992 EP
0547576 Jun 1993 EP
0598472 Aug 1993 EP
0579388 Jan 1994 EP
0636702 Feb 1995 EP
0504926 Jun 1995 EP
0454666 Nov 1995 EP
0270666 Aug 1996 EP
0464079 Oct 1996 EP
0452922 Jan 1997 EP
0547576 Mar 1997 EP
0598472 Jun 1997 EP
0823403 Feb 1998 EP
0579388 Apr 1998 EP
0854022 Jul 1998 EP
0 870 530 Oct 1998 EP
0870530 Oct 1998 EP
0871046 Oct 1998 EP
0 897 896 Feb 1999 EP
0874786 Mar 1999 EP
0905273 Apr 1999 EP
0636702 May 1999 EP
0799802 Jan 2000 EP
0963797 Mar 2000 EP
0999574 May 2000 EP
1046617 Oct 2000 EP
1065178 Jan 2001 EP
1088789 Apr 2001 EP
1103805 May 2001 EP
1136452 Sep 2001 EP
1 198 426 Apr 2002 EP
1211227 Jun 2002 EP
0905273 Oct 2002 EP
1253118 Nov 2002 EP
1 298 096 Apr 2003 EP
1 298 096 Apr 2003 EP
1298096 Apr 2003 EP
1065178 May 2003 EP
1319639 Jun 2003 EP
1319736 Jun 2003 EP
0823403 Jul 2003 EP
0999574 Jul 2003 EP
1325947 Jul 2003 EP
0963797 Aug 2003 EP
1336592 Aug 2003 EP
1340724 Sep 2003 EP
0911302 Jan 2004 EP
1375702 Jan 2004 EP
1375702 Jan 2004 EP
1392611 Mar 2004 EP
1405833 Apr 2004 EP
0725679 Sep 2004 EP
1464631 Oct 2004 EP
1468970 Oct 2004 EP
1468971 Oct 2004 EP
1468973 Oct 2004 EP
1468973 Oct 2004 EP
1046617 Dec 2004 EP
0870530 Jan 2005 EP
1211227 Jan 2005 EP
1496021 Jan 2005 EP
1510504 Mar 2005 EP
1 524 245 Apr 2005 EP
1524245 Apr 2005 EP
1392611 May 2005 EP
1198426 Aug 2005 EP
1627857 Feb 2006 EP
1634856 Mar 2006 EP
1319736 May 2006 EP
1693482 Aug 2006 EP
1714948 Oct 2006 EP
1719561 Nov 2006 EP
1731261 Dec 2006 EP
1103805 Jan 2007 EP
1173780 Mar 2007 EP
1834933 Sep 2007 EP
1 925 600 May 2008 EP
1 925 600 May 2008 EP
1925599 May 2008 EP
1925600 May 2008 EP
1298096 Jul 2008 EP
1723086 Sep 2008 EP
1925599 Jan 2009 EP
1731261 Jul 2009 EP
1925600 Mar 2010 EP
2223941 Sep 2010 EP
2248597 Nov 2010 EP
1807259 Mar 2011 EP
2305611 Apr 2011 EP
1723086 Sep 2011 EP
2414872 Feb 2012 EP
2431338 Mar 2012 EP
2436658 Apr 2012 EP
2455349 May 2012 EP
2463246 Jun 2012 EP
1634856 Aug 2012 EP
2489642 Aug 2012 EP
1136452 Apr 2013 EP
2581350 Apr 2013 EP
2305611 Dec 2013 EP
2725122 Apr 2014 EP
2 246 567 Feb 1992 GB
2284362 May 1993 GB
2239404 Jan 1994 GB
2284362 Jan 1997 GB
S51128311 Nov 1976 JP
S5577701 Jun 1980 JP
S57129832 Aug 1982 JP
A5987071 May 1984 JP
S5987071 May 1984 JP
S6028605 Feb 1985 JP
S6044941 Mar 1985 JP
S6071535 Apr 1985 JP
S6081041 May 1985 JP
S60145930 Aug 1985 JP
S60210540 Oct 1985 JP
S6158840 Mar 1986 JP
S61106438 May 1986 JP
S61146731 Jul 1986 JP
S6275402 Apr 1987 JP
S62132944 Jun 1987 JP
S6311530 Jan 1988 JP
S6364930 Mar 1988 JP
S63134539 Jun 1988 JP
S63182224 Jul 1988 JP
S63282139 Nov 1988 JP
S649830 Jan 1989 JP
S6433029 Feb 1989 JP
H01134307 May 1989 JP
H01138512 May 1989 JP
H01219038 Sep 1989 JP
H02192427 Jul 1990 JP
H02252633 Oct 1990 JP
H03202110 Sep 1991 JP
H03202111 Sep 1991 JP
H03202112 Sep 1991 JP
H03202113 Sep 1991 JP
H03202116 Sep 1991 JP
H03247524 Nov 1991 JP
H03295827 Dec 1991 JP
H0412063 Jan 1992 JP
H0465333 Mar 1992 JP
H05146615 Jun 1993 JP
05238773 Sep 1993 JP
H05306136 Nov 1993 JP
H0648745 Feb 1994 JP
H06101050 Apr 1994 JP
H06183771 Jul 1994 JP
H06219767 Aug 1994 JP
H0710594 Jan 1995 JP
H07187698 Jul 1995 JP
H07242438 Sep 1995 JP
H07300332 Nov 1995 JP
H08217480 Aug 1996 JP
H08301615 Nov 1996 JP
09071430 Mar 1997 JP
H0995133 Apr 1997 JP
H09110454 Apr 1997 JP
H09188523 Jul 1997 JP
H1081533 Mar 1998 JP
S63139032 Jun 1998 JP
H10194785 Jul 1998 JP
H10338555 Dec 1998 JP
H11123334 May 1999 JP
H11246228 Sep 1999 JP
2000044289 Feb 2000 JP
2000125075 Apr 2000 JP
2000327359 Nov 2000 JP
2001048572 Feb 2001 JP
2001151537 Jun 2001 JP
2001154016 Jun 2001 JP
2001220155 Aug 2001 JP
2001-294431 Oct 2001 JP
2001 302258 Oct 2001 JP
2002243368 Aug 2002 JP
2002267827 Sep 2002 JP
2003040626 Feb 2003 JP
2003048739 Feb 2003 JP
2003119034 Apr 2003 JP
2003160342 Jun 2003 JP
2003192355 Jul 2003 JP
2003212553 Jul 2003 JP
2003262473 Sep 2003 JP
2003347266 Dec 2003 JP
2004142976 May 2004 JP
2004321970 Nov 2004 JP
2004351358 Dec 2004 JP
2004359513 Dec 2004 JP
3735887 Jan 2006 JP
2006193361 Jul 2006 JP
2006206337 Aug 2006 JP
2006248884 Sep 2006 JP
2007131487 May 2007 JP
2007313435 Dec 2007 JP
2008127260 Jun 2008 JP
2008170143 Jul 2008 JP
2010042940 Feb 2010 JP
4424232 Mar 2010 JP
4465932 May 2010 JP
2011236071 Nov 2011 JP
2012006797 Jan 2012 JP
2012006799 Jan 2012 JP
2013020022 Jan 2012 JP
2012031034 Feb 2012 JP
2012036014 Feb 2012 JP
2012062203 Mar 2012 JP
2012116731 Jun 2012 JP
2012166992 Sep 2012 JP
2012193057 Oct 2012 JP
2012246180 Dec 2012 JP
2013006767 Jan 2013 JP
2013037217 Feb 2013 JP
5238773 Jul 2013 JP
2013173628 Sep 2013 JP
2013249213 Dec 2013 JP
2014009105 Jan 2014 JP
20000038422 Jul 2000 KR
20010060246 Jul 2001 KR
20010080860 Aug 2001 KR
20030083848 Nov 2003 KR
20080046561 May 2008 KR
20090056391 Jun 2009 KR
PA00006579 Feb 2005 MX
PA04010649 Oct 2005 MX
2007005085 Jun 2007 MX
100114 Oct 1990 RO
121337 Mar 2007 RO
2390425 May 2010 RU
2390426 May 2010 RU
1254035 May 2006 TW
8200827 Mar 1982 WO
8706927 Nov 1987 WO
8707559 Dec 1987 WO
9008334 Jul 1990 WO
9009356 Aug 1990 WO
9011540 Oct 1990 WO
9308500 Apr 1993 WO
9311077 Jun 1993 WO
9325301 Dec 1993 WO
9511751 May 1995 WO
9609260 Mar 1996 WO
9726222 Jul 1997 WO
9739988 Oct 1997 WO
9841397 Sep 1998 WO
9947236 Sep 1999 WO
9950203 Oct 1999 WO
0037385 Jun 2000 WO
0060375 Oct 2000 WO
0104065 Jan 2001 WO
0104065 Jan 2001 WO
0112567 Feb 2001 WO
0119746 Mar 2001 WO
0125503 Apr 2001 WO
0145820 Jun 2001 WO
0207181 Jan 2002 WO
02079108 Oct 2002 WO
02081388 Oct 2002 WO
02083581 Oct 2002 WO
02088036 Nov 2002 WO
02102724 Dec 2002 WO
02102724 Dec 2002 WO
03037613 May 2003 WO
2004002911 Jan 2004 WO
2004002911 Jan 2004 WO
2004029326 Apr 2004 WO
2005061400 Jul 2005 WO
2006052578 May 2006 WO
2006058517 Jun 2006 WO
2006070395 Jul 2006 WO
2006123838 Nov 2006 WO
2007136670 Nov 2007 WO
2008062448 May 2008 WO
2009093134 Jul 2009 WO
2009116300 Sep 2009 WO
2011016998 Feb 2011 WO
2011027035 Mar 2011 WO
2011061569 May 2011 WO
2011088515 Jul 2011 WO
2012112279 Aug 2012 WO
2012148744 Nov 2012 WO
2013015752 Jan 2013 WO
2013081827 Jun 2013 WO
2013081827 Jun 2013 WO
2014002666 Jan 2014 WO
2014002666 Jan 2014 WO
2014043267 Mar 2014 WO
Non-Patent Literature Citations (17)
Entry
Hahnemann, H.W. “The pressure drop for perforated plates with extremely small free opening and extremely small opening diameter” Forsch. Ing.Wes. 42 (1976) No. 3 and its English Translation.
Learn about Fluid Engineering, 1.2 Mesh to Micron Conversion Table from http_www.fluideng.com_TechInfo_MeshMicronConversion.php.
Bee, Jared S., et al.“Effects of Surfaces and Leachables on the Stability of Biopharmaceuticals” Journal of Pharmaceutical Sciences, vol. 100, No. 10, Oct. 2011.
Jiang, Jiagin “Apparatus and Techniques for Study of Unsteady Thermal/Fluid-Induced Loads on Electronic Components”, Master Thesis, San Jose State University, 1993.
“Weed Washer” What is a Micron? (Micron v/s Mesh) Micron and Mesh, ICPI Workshop 2011.
Orlov, A. N. et al. “The Main Design and Technological Features of In-Line and Sectional Machines of the IS Type Made by Mole Bros. (USA)” All-Union Scientific- Research and Planning and Design Institute of Glass Machinery. Translated from Steklo i Keramika,, No. 12, pp. 32-33, Dec. 1975.
Holdich, Richard et al. “Pore Design and Engineering for Filters and Membranes” Philosophical Transaction of the Royal Society vol. 364 pp. 161-174, 2006.
Lueger “Machine Manufacturing Bottles” vol. 8. p. 370. 1976 and its English Translation.
“International Standard: Space Systems—Surface Cleanliness of Fluid Systems Part 2: Cleanliness Levels” ISO 14952-2. Nov. 15, 2003.
“International Standard: Space Systems—Surface Cleanliness of Fluid Systems Part 3: Analytical Procedures for the Determination of Nonvolatile Residues and Particulate Contamination” ISO 14952-3. Nov. 15, 2003.
“International Standard: Space Systems—Surface Cleanliness of Fluid Systems Part 4: Rough-Cleaning Processes” ISO 14952-4. Nov. 15, 2003.
“International Standard: Space Systems—Surface Cleanliness of Fluid Systems Part 6: Precision-Cleaning Processes” ISO 14952-6. Nov. 15, 2003.
“Standard Specification for Industrial Woven Wire Cloth” Designation: E2016-11 ASTM International.
“Stainless Steel Flat Products for Building the Grades in EN 10088-4 Explained” Building Series, vol. 18. pp. 1-26. Euro Inox: The European Stainless Steel Development Association.
“Standard Specification for Passivation of Stainless Steels Using Electropolishing” Designation: B912-02. ATSM International.
“Airborne Particulate Cleanliness Classes in Cleanrooms and Clean Zones” Federal Standard 209E. U.S. General Services Administration. pp. 1-48. Sep. 11, 1992.
“Stainless Steels—Part 1: List of Stainless Steels” English Version of EN 10088-1:2014, English Translation of DIN EN 10088-1. Dec. 2014.
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20170313614 A1 Nov 2017 US
Provisional Applications (1)
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62079208 Nov 2014 US