Patent Application
20150233517
The invention relates to phenolic insulating foam sections, particularly suitable for pipe insulation.
Historically, phenolic resins have been the preferred thermosetting resin material when low smoke emission and self-extinguishing ability in fire situations is paramount. One such application is in building and pipe insulation where phenolic foams provide both thermal insulation in use, and good performance during a fire.
As conventional phenolic foam is produced using an acid catalyst, there is a perception that when this foam is in direct contact with metal, such as an insulated pipe, it could induce corrosion of the metal.
German Patent Publication DE1 272 058 discloses a composite pipe which is a steel tube with a sheath of hardened foam plastic. It is not suitable for use for retrofitting, for example to existing pipework.
French Patent Publication FR 2 388 059 describes a corrosion inhibitor mixture for pipes and ducts. The mixture is for protecting the pipe from the elements. It can be applied in an arrangement with an outer casing and an inner casing.
US Patent Publication No. 2009/0270005 describes a foamable resol type phenolic resin. Inorganic filler can be added to the resin.
According to the invention there is provided a foam body having an outer facing web and an inner facing web wherein at least one of the webs is porous and comprises a neutralising agent. The neutralising agent is desirably of limited solubility in water so that immediate reaction with the acidic catalyst species does not readily occur. Such limited solubility is typical of certain alkali metal, alkaline earth metal or aluminium carbonates, oxides or hydroxides.
The foam body is suitable for production in a continuous process. The outer and inner facing webs are attached to the foam body by curing of the foam. (No other adhesion is required.) The product thus comprises a foam body to which the outer and inner facing web are attached and the neutralising agent is present in at least the inner facing web. The product is thus provided as a complete product and does not require assembly in order to be fitted, for example to a pipe.
In one embodiment the inner facing web is porous
Alternatively or additionally the outer facing web is porous.
The neutralising agent may comprise an alkali metal, alkaline earth metal, or aluminium carbonate oxide, or hydroxide with limited water solubility.
One such neutralising agent comprises calcium carbonate.
In one aspect the foam body comprises a foam board.
In another aspect the foam body comprises an elongate shaped hollow phenolic foam body of substantially uniform cross section, the foam body having an outer facing web and an inner facing web wherein at least one of the webs is porous and comprises a neutralising agent.
In one embodiment the foam body is of curvilinear shape. The body may be slit longitudinally into section parts for wrapping around an object.
In one case section parts are linked by the outer web on one side. Facing ends of the section parts may be faced with the inner facing web on an opposite side.
In one case the foam body is generally cylindrical.
The foam body may comprise an insulating body for a pipe.
Alternatively the foam body comprises a duct or an insulating body therefor.
The foam body may be of rectilinear shape.
In one embodiment the inner web is of porous fibreglass material. The glass material may be in the form of a veil or mesh which can weigh, for example from 20 to 60 grams per square metre.
In one embodiment the outer web is of metal foil such as aluminium foil, paper, glass, thermoplastic film or combinations of two or more thereof.
The outer web may, for example be of aluminium foil.
The invention also provides an elongate shaped section comprising a hollow phenolic foam body of substantially uniform cross section, the foam body having an outer facing web and an inner facing web wherein the body is slit longitudinally into section parts for wrapping around an object, wherein the section parts are linked by the outer web on one side and wherein facing ends of the section parts are faced with the inner facing web on an opposite side and wherein at least one of the webs is porous and comprises a neutralising agent.
We describe a continuous process for producing elongate phenolic foam insulating shaped sections comprising the steps of:
The inner and outer webs may be heated to a temperature of between 45° C. and 85° C. The inner and outer webs may be heated to a temperature of between 50° C. and 70° C.
The inner web is shaped by a mandrel. The mandrel may be heated. The mandrel may be a hollow mandrel which is heated by circulating a heat exchange fluid therethrough.
The mandrel may be at least partially coated with an anti-friction agent such as polytetrafluoroethylene based product such as for example as sold under the name Teflon®.
The outer web may be shaped by a mould. The mould may be heated. The mould may be heated by radiant heat.
The process may include the step of post-curing the elongate foam insulating shaped section.
The shaped section may be post cured at a temperature of from 20° C. and 85° C. for a period of 4 to 48 hours. The shaped sections may be post cured at a temperature of from 50° C. to 85° C. for a period of from 4 to 48 hours.
The process may comprise cutting the shaped section to a desired length. The shaped section may be cut to a desired length in-line.
The elongate foam insulating shaped section may comprise a hollow foam body of substantially uniform cross section. The shaped section may be of curvilinear, preferably cylindrical shape.
The shaped section may be of rectilinear shape.
The foam body may comprise an insulating body for a pipe. Alternatively the foam body comprises a duct or an insulating body therefor. The foam body may comprise a pipe support.
We describe a process for manufacturing continuous profiled insulating phenolic foam pipe-sections using phenolic foam reactants.
The term phenolic foam reactants means a resin substantially based on phenol formaldehyde to produce a substantially closed cell foam with stabiliser, plastisicer, blowing agent, surfactant, catalyst, and/or initiator system and possibly other ingredients including polyether or polyester polyol and/or isocyanurate.
The process involves the continuous feeding of facing webs, laying down of phenolic foam pre-polymer between these webs, and shaping the section continuously entering a double-chain shaped heated conveyor which enables the pre-polymer to cure as a shaped profile section.
We describe a process for continuously producing profiled sections of phenolic foam with good retention of low thermal conductivity properties where desired. The process is capable of very low inherent waste and scrap rates as no waste section is produced, the waste being limited to cutting blade width and occasional scrap sections at machine start-up or during processing difficulties (which are naturally limited as the process can be stopped and started with ease).
We describe a continuous process for producing phenolic foam insulating pipe-sections with minimal waste involving the continuous feeding of facing webs, laying down of phenolic foam pre-polymer between these webs, and shaping the section continuously entering a double-belt shaped heated conveyor which enables the pre-polymer to cure as a shaped profile section.
Both the inner mandrel and outer mould sections may be heated to ensure adequate curing of the phenolic foam insulation in a commercially useful time at a rate exceeding 2 metres/minute, preferably exceeding 4 metres/minute.
The inner mandrel and outer mould sections enable a wide variety of sizes of pipe-section or similar continuously profiled phenolic foam insulating section to be produced.
A variety of phenolic resins and catalyst systems may be used to produce continuous pipe-section or other profiled insulating sections by this method.
The pipe sections may be post-cured at between 50 and 85° C. to produce product with good dimensional stability and stable thermal conductivity.
A variety of different facing materials including aluminium foil, paper, glass, thermoplastic film or a combination of these may be used.
The invention will be more clearly understood from the following description thereof given by way of example only with reference to the accompanying drawings, in which:
Referring to the drawings, and initially to
The inner web 3 comprises a porous material which contains/comprises and/or is impregnated with a neutralising agent. One such material is calcium carbonate. The porous material may, for example be of a veil composed of glass filaments. The neutralising agent may be incorporated into the material during manufacture or added (for example by coating) subsequently. The material typically weighs from 20 to 60 grams per square metre. A further amount of typically 10 to 50 grams per square metre of calcium carbonate is added.
In the invention, in the event that acidic moisture leaches from the foam it is neutralised by the neutralising agent (in this case calcium carbonate) before it can reach the pipework against which the product is placed. In addition, because the liner is porous, moisture can pass through which will aid drying/curing and prevent moisture from becoming trapped either within the foam or between the foam and the surface on which it rests.
The outer web 4 may be any suitable material such as an aluminium foil.
Referring now to
The outer facing 4 is led through a former 27 prior to entry to the mould 10. The mould 10 comprises a number of mould sections 28 which are interlinked as illustrated in
The mandrel/former 11 has an upwardly projecting fin 35 over which excess inner facing 3A is led. The fin 35 is used to mount the mandrel 11 in the machine. The excess inner facing 3A is guided by a guide wheel 40 and the excess outer facing 4A is guided by a guide wheel 41.
The mandrel is preferably at least partially coated with a friction reducing material such as polytetrafluoroethylene such as that sold under the name Teflon which is a Trade Mark of Du Pont. This has the effect of reducing the friction which acts between the moving web and the stationary mandrel. Such friction reducing measures are important because friction can cause the inner web to move more slowly than the outer web. The expanding foam lies between the webs and the differential movement of the webs may result in the cells of the foam becoming elongated with consequent adverse effects on the properties of the foam.
Referring to
The centre line of each mandrel is designed to have exactly the same measurement in relation to the track so that when the mandrel is changed, the centre point of the next mandrel is correctly aligned in relation to the moulds 28. Any changes to the position of the mandrel 11 are made by moving the track 40 in which it rests, thereby altering the effective position of all mandrels simultaneously.
A solution to the problem of continuous production of profiled insulated phenolic foam sections with minimal waste is provided by the invention.
In the invention, webs which form the facings 3, 4 are introduced and shaped immediately prior to laying down a pre-polymer mix onto the ‘outer’ web 4. The ‘outer’ web 4 is curled to fit inside the continuously rotated stiff mould sections 28 rotating on two chain systems either side on a central axis. These mould sections 28 form the shape of the outside of the pipe-section insulation profile, and are provided in short sections which can be readily changed to enable different outer diameter or shapes of profile. The mould sections 28 may be solid or hollow material, and may have means of electrical or liquid flow heating, or be heated separately by infra-red, conductive or air-flow means. Typically the mould sections 28 may be formed from wood, plastic, resin or metal. The upper part of the mould sections 28 grip an excess 4A of the outer web facing 4, providing the traction to pull this along the central axis of the machine. The ‘inner’ web 3 is curled continuously around a central profiled mandrel 11 which extends part way along the central axis of the machine, but does not move with the outer chains, but remains static. The central mandrel 11 may be heated, normally using a liquid (water or oil) circulation system.
Phenol-formaldehyde resin is mixed with suitable surfactant, plasticiser, and blowing agent system, and with a fast-acting catalyst immediately prior to the mix being laid down through the nozzle 25 onto a continuously moving facing web 4 shaped to hold the mixture. The whole is fed continuously between the double chain system of moulds 28 so that the outer web 4 is held to the outer mould section shape, moving continuously at the same speed as these mould sections, and the inner web 3 slides over the inner heated mandrel 11. Several metres along the central axis of the machine, at the point where the resin mix has polymerised sufficiently to be self-supporting, the mandrel section 11 finishes. The final polymerisation and partial cure of the outer section then continues along the central axis of the machine and, at the point where the outside of the pipe-section is sufficiently cured, the mould sections 28 are parted on the double chain and returned to the beginning of the process along the outer sides of the machine. If the moulds 28 are not self heating, they may be heated just prior to the front of the machine by radiators placed along the outside.
The partly cured profile emerging continuously from the machine is cut into sections of suitable length for handling (typically 1 metre), slit continuously to allow folding over pipe lengths as described above, and collected in cassettes or boxes for further heat curing, if required.
By this method phenolic foam insulating pipe sections can be made continuously with much reduced waste and productivity over conventional procedures.
Phenolic formaldehyde resole was pre-mixed with 10 parts per hundred resole (pph) of cyclo:iso pentane (85:15) blowing agent mix containing 5% perfluoroalkane type P5052. This was continuously fed into a low pressure dynamic mixer to which 65% phenol sulphonic acid was added at a rate of 25 pph. The resultant pre-polymer was fed onto a continuously moving facing web shaped to hold the mixture. The whole was fed continuously at 2.5 metres/minute between a 12 metre double chain system of moulds so that the outer web was held to the outer mould section shape (diameter 74 mm) as described above, moving continuously at the same speed as these mould sections, and the inner web slid over the inner heated mandrel (diameter 38 mm), which projected 8 metres along the central axis of the machine. The inner mandrel was heated to 60° C. and the outer mould sections to 50° C.
The partly cured profile emerging continuously from the machine was cut into sections of suitable length for handling (1 metre), slit continuously to allow folding over pipe lengths, and collected in boxes for further heat curing. The sections thus produced showed good dimensional stability and thermal conductivity suitable for use as pipe section insulation.
The invention is not limited to insulating sections for pipes or ducts. It may be used, for example, to produce short lengths (typically 50 mm to 250 mm) of similar shape with higher density for use as a support or the like. Such densities would typically lie in the range of from 50 kg/m3 to 125 kg/m3 and the material produced has sufficient compressive strength to be able to support a pipe system which may be insulated by the insulated pipe sections of the invention. Products of this type are known as pipe supports.
The invention is not limited to the embodiments hereinbefore described which may be varied in detail.
| Number | Date | Country | Kind |
|---|---|---|---|
| 12184824.6 | Sep 2012 | EP | regional |
| 2012/0407 | Sep 2012 | IE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2013/069394 | 9/18/2013 | WO | 00 |
