This invention relates to a gas adaptor which is used to reduce and regulate the pressure or flow rate of a gas or of a liquefied gas. In one aspect the gas adaptor can interconnect a source of gas such as a gas bottle or gas cylinder to apparatus which utilizes the gas such as a gas heater or gas barbeque. The gas adaptor reduces the pressure of the gas to low pressure which can be utilized in gas utilization apparatus in a safe and effective manner.
Hitherto when it was desired to connect a source of high pressure gas to a gas utilization apparatus it was necessary to use a regulator. Thus for example when it was necessary to connect a SCUBA gas cylinder to breathing apparatus it was necessary to reduce the pressure in the gas cylinder from 240 atmospheres to 1-5 atmospheres. This is achieved by a regulator which in a first stage has a high pressure chamber and an intermediate pressure chamber which are separated from each other by a valve diaphragm combination or a piston which is in contact with ambient water pressure. The high pressure chamber receives air directly from the cylinder while the intermediate pressure chamber is in contact with the ambient water pressure through the diaphragm or piston. The regulator also has a second stage which is connected to the first stage and has a chamber with an outer rubber diaphragm that is in contact with ambient water pressure. The second stage also has a purge button and an inner valve that is connected to a movable lever exhaust valve and mouthpiece. The second stage reduces the first stage pressure of 9.5 atmospheres to 1-5 atmospheres.
Reference also may be made to U.S. Pat. No. 6,796,326 which describes a pressure regulator of complicated construction having a gas-tight casing that houses an inlet side chamber and an outlet side chamber connected to each other by a passage to accommodate a valve seat to retain a valve disc that is guided through a rod and can be moved in an axial direction inside the casing wherein the rod is connected to a pressure diaphragm in contact with an adjusting spring. There is also provided a closing body connected to an armature of an electro-magnetic drive.
Reference may also be made to U.S. Pat. No. 6,769,447 which describes a regulator valve having a valve chamber which regulator valve has a cap member which holds an elongate rotatable control key in operative association with a rotatable flow regulating plug member located in the valve chamber. The plug member includes an inlet orifice which can communicate with a gas flow inlet passage and an outlet orifice. There is also provided a spring for biasing the control key. The regulator valve also includes a press member carried on the control key and retained thereon by a clip.
Reference also may be made to U.S. Pat. Nos. 6,318,407, 5,018,965, 5,566,713, 5,975,121 and 4,217,928 all of which relate to gas regulators of complicated structure and construction.
Reference may be made to WO2006/108244 which refers to catalytic oxidation of hydrocarbon gas wherein pulses of a compressed hydrocarbon from a container of the compressed hydrocarbon gas are passed into an expansion chamber and subsequently passed over a catalytic converter to oxidize the hydrocarbon gas. The hydrocarbon gas is released from the gas bottle through a porous ceramic slug mounted in a gas take off from the gas container. The porous ceramic slug has an interconnected network of interstices through which the passage of hydrocarbon gas is restricted. The hydrocarbon gas is released from the gas container without the need for a regulator by releasing the compressed hydrocarbon gas through a restrictor tube into a valve such as an electronically controlled valve and then into another restrictor tube that is connected to the expansion chamber. It is also disclosed in this reference that small amounts of hydrocarbon gas may be released in a controlled manner from the gas container by passing the hydrocarbon gas through a small diameter orifice located in an electronic valve directly attached to the gas container or via the restrictor tube which is connected to the electronic valve.
It is therefore an object of the invention to provide a gas adaptor which may replace a conventional pressure regulator or regulator valve which is effective in operation and of simple structure.
The gas adaptor of the invention is adapted in use to reduce the pressure of a gas or flow rate of liquefied gas, said gas adaptor having:
It has now been discovered that the omission of a regulator does not require the use of an electronic valve or a first and second restrictor tube as described in WO2006/108244 and that use may be made of a gas adaptor described above having the adaptor body attachable to the gas container which contains the ceramic insert in the internal bore of the adapter body which is in fluid communication with the internal bore. This is a much simpler structure than the structure described in WO2006/108244.
The invention therefore is the adoption of the ceramic insert in the internal bore of the adaptor body in combination with the capillary tube or passage which is an effective substitute for the conventional regulator.
The capillary tube is preferably an elongate tube of relatively restricted inside diameter or transverse dimension which preferably is formed from copper or material that self seals if the capillary tube is damaged or cut. In another arrangement the capillary tube may be replaced by a passage drilled or machined in an elongate body. However the capillary tube is preferred.
Preferably the gas adaptor is adapted in use to interconnect a high pressure gas source to gas utilization apparatus wherein the initial high pressure of the gas is reduced to a lower operating pressure relevant to operation of the gas utilization apparatus. In this arrangement therefore the gas adaptor may include means for connection to the gas utilization apparatus.
The means for connection to the gas utilization apparatus may involve a screw threaded connection between a low pressure end fitting and the gas utilization apparatus. Alternatively a male-female, plug socket engagement may be utilized using an interference fit. Alternatively a “snap in” or “click-in” connection may be used where the low pressure end fitting has a tail or plug that automatically engages with a socket of corresponding cross sectional shape.
Preferably the capillary tube or passage is provided with a flexible or rigid protective hose which is attached to the adaptor body and the connection means to the gas utilization apparatus.
The connection means to the high pressure gas source may involve screw threaded engagement between the adaptor body and the high pressure gas source. Thus for example the adaptor body itself may be screw threadedly engaged with the high pressure gas source or have a fitting which incorporates a screw thread rotatably mounted to the adaptor body.
The connection means in other arrangements may include a plug-socket or male-female engagement between the adaptor body or connection member mounted to the adaptor body such as by way of interference fit. However a screw threaded engagement is preferred.
The adaptor body may have a unitary or one piece construction or alternatively include two or more components which may for example be a protective sleeve which protects a high pressure end of the rigid or flexible protective hose. The protection sleeve may be screw threadedly engageable with an inner bore of the adaptor body.
In another embodiment the adaptor body may include a sealing member which engages in a high pressure end of the adaptor body which seals the ceramic insert within the internal bore of the adaptor body. There may be provided a pair of resilient members such as O rings located at each end of the ceramic insert so as to vary the gas flow rate through the ceramic insert. The degree of adjustment may be regulated by the sealing member which is preferably a screw threadedly engageable in the inner bore of the adaptor body so that tightening or loosening of the sealing screw will adjust the gas flow rate through the ceramic insert.
Reference may now be made to a preferred embodiment of the present invention wherein:
In the drawings there is shown gas adaptor 10 having a high pressure end 11 and a low pressure end 12. The gas adaptor 10 at the high pressure end 11 has a body 13 having a screw thread 14 adapted to be screw threadedly attached to a suitable source of high pressure gas. This source may include for example 200×105 Pa in relation to medical applications as described in U.S. Pat. No. 5,566,713 or may include or in the case of portable gas tanks used as oxygen sources in the medical field pressures inclusive of 2200 psig in the USA or 3000 psig in Europe. Such pressures may be reduced by the use of pressure regulators as described in U.S. Pat. No. 6,318,407 to 50 psig in the USA and 45-60 psig in Europe. In relation to gas bottles of carbon dioxide, liquid petroleum gas (LPG) or butane suitable high pressures may be 1200 psig for carbon dioxide, 240 psig for LPG and 60 psig for butane.
Body 13 is suitably made from metal inclusive of stainless steel, brass or aluminium with brass being preferred and has an O-ring 15 mounted in a mating groove 16 for connection to the high pressure gas source. There is also provided an inner sleeve 17 and an outer sleeve 18 rotatably supported on inner sleeve 17 and which has screw threaded portion 14. There is also provided nut component 20 which is an integral part of outer sleeve 18.
There is also provided a ceramic insert 21 which may correspond to the ceramic insert described in U.S. Pat. No. 5,018,965 which is totally incorporated herein by reference. However insert 21 is cylindrical and may be formed from aluminium oxide and provided with a slight taper (not shown) to facilitate insertion into internal bore 22 of body 13 which has a corresponding diameter to insert 21. Body 13 may also have a further inner bore 23 of smaller diameter than internal bore 22.
Ceramic insert 21 is suitably a mesoporous ceramic material having a pore size of 2-50 nm and may be made of metal oxides such as aluminium oxide, zirconia or non oxides such as carbides, borides, nitrides or silicides or composites of these materials. Particular examples of ceramic materials include barium titanate, bismuth strontium calcium copper oxide, boron carbide, boron nitride, ferrite, lead zirconate titanate, magnesium diboride, silicon carbide, silicon nitride, steatite, uranium oxide, yttrium barium copper oxide or zinc oxide.
However it will also be appreciated that ceramic insert 21 may be formed from non crystalline materials such as clays, cement or glass or crystalline materials inclusive of metal compounds discussed above.
A suitable method of manufacture of ceramic insert 21 is mainly based on sintering methods where the ceramic body is baked in a kiln where diffusion processes cause the ceramic body to shrink and the internal pores close up, resulting in a denser stronger product. Manufacture of high performance ceramics is described for example in “Organic Additives and Ceramic Processing” by D J Shanefield, Kluwer P which reference is totally incorporated herein by reference.
In the drawings there is also shown a capillary tube 24 which may have an inside diameter of 0.001-0.05 inches and more preferably an inside diameter of around 0.026 inch. The capillary tube 24 may be formed from any suitable material which is preferably self sealing in the event of damage or being melted by a flame. A suitable material is copper although aluminium or stainless steel may be utilized if required although they are less preferred than copper.
The capillary tube 24 has a protective sheath of stainless steel braided hose 25 and this may be pushed into open ended passage 9 of body 13 and retained therein by interference fit. The capillary tube 24 and its protective sheath or hose 25 may be of any desired length. The protective hose 25 may be formed from other suitable material such as rigid plastics material inclusive of Teflon, polyethylene or propylene but it is preferred that a flexible material such as stainless steel or Teflon braided hose be utilized.
The low pressure end 12 of capillary tube 24 extends through outlet fitting 26 and is welded thereto at 26A. Outlet fitting 26 is designed to be compatible with conventional corresponding apertures or sockets on apparatus utilizing the gas from the high pressure source and thus may be a “click-in” interconnection of plug and socket. In
In
In
In
In
In
In operation gas from gas bottle 43 is caused to flow through ceramic insert 21 or 21A which is mesoporous as described above. The ceramic insert provides a fixed pressure and flow rate for the gas although this may be adjusted as described in
In operation of the catalytic converter assembly 43 propane gas passes through gas hose 25 from gas cylinder 43 after opening of gas flow by control handle 45. The propane gas is then caused to flow through hollow bore 79 of pin 78 and is ignited by a spark from spark end 68 to be oxidised to carbon dioxide. The spark is caused by movement of actuator button 80 and the propane is catalytically converted to carbon dioxide by catalyst layer 70. The resulting carbon dioxide is a well known attractant for mosquitoes. The hollow support body 65 incorporates a conductive carbon content to avoid use of an earth wire.
In another aspect of the invention there is also provided a method of operating a gas adaptor connected to a source of gas or liquefied gas to reduce the pressure of the gas or the flow rate of the liquefied gas, said method including the steps of:
After step (ii) the gas adaptor may be connected to gas utilization apparatus as described above which is in flow communication with the capillary passage or alternatively the gas may flow to atmosphere as shown in
It will be appreciated from the foregoing that the gas adaptor of the invention is adapted to reduce an initial pressure of a gas to produce a gas at lower pressure. However it will be evident that the gas adaptor of the invention may also reduce a flow rate of a gas and this is especially applicable to a liquefied gas which flows through the ceramic insert and subsequently through the capillary tube or passage.
Reference may now be made to another embodiment of the invention shown in
When each of the components shown in exploded relationship in
The advantage of having plastics washer 94 in abutting relationship and separate from tubular end component 92 (i.e. it is not secured or connected to component 92 such as by screw threaded engagement) is that when thread 102 engages thread 103 and thus, brings washer 94 and component 92 into contact or abutting relationship there is provided a secure seal in relation to the gas so that all the gas flows through inner bore 97 and into capillary passage 24.
The advantages of locating the ceramic insert 98 inside plastics washer 94 means that fitting or assembly of the ceramic insert 98 to hose 25 is very much simplified compared to the arrangements shown in
As a result of the impurities reaching ceramic insert 21 or capillary tube 24, there was often a complete blockage and thus, gas flow through capillary tube 24 was prevented. If such was the case it was then necessary to throw away the entire gas adaptor 10 and order a new one. This was an expensive procedure. This problem was overcome by the provision of a separate component such as plastics washer or sleeve 94 wherein ceramic insert 98 could be pushed into accommodating internal bore 97 by press fit or interference fit. This made plastics sleeve or washer 94 a throwaway or disposable item and capable of being readily replaced by a fresh or substitute sleeve 94 having insert 98 already fitting thereto in bore 97.
Further embodiments of the invention are shown in
In
In
The production of restricted zone 24A is shown in
In a further embodiment as shown in
The production of restricted zone 24A of capillary tube 24 means that the diameter of restricted zone 24A may be varied to suit production of various gas flows. However, a suitable range may be from 0.005 to 0.2 mm compared to an internal diameter of the unrestricted part 25 which may vary from 0.025 to 1.25 mm in internal diameter. The restricted zone 24A may also produce a flow rate of gas through the restricted zone 24A at a flow rate of 5-30 gm of gas per day and more suitably 18 gm of gas per day.
It will also be appreciated that the production of the restricted zone 24A will greatly increase frictional contact of the gas with an internal surface of restricted zone 24A and which greatly reduces the flow of the gas. Therefore, gas flow may be produced in pulses whereby separate pulses are produced by a build up in gas pressure to pass through the zone 24A. Another factor on gas flow rate will also be the length of zone 24A which may vary from 10-125 mm in length. Obviously the greater the length of restricted zone 24A the greater reduction in gas flow that may be achieved.
It will also be appreciated that multiple restricted zones 24A may be produced but it is preferred that there is only a single restricted zone.
The major advantage that will be provided by restricted zone 24A is that a bottle of gas will last substantially longer with the substantial reduction in gas flow as discussed above. Thus, gas bottle pressure may be reduced from approximately 60-3000 psi in gas bottle 43 as described above to less than 5 psi when the gas passes through the zone 24A.
Number | Date | Country | Kind |
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AU2007903624 | Jul 2007 | AU | national |
This application claims priority and incorporates by reference co-pending and commonly assigned PCT Application No. PCT/AU2008/000989 filed Jul. 4, 2008 for Gas Adaptor and through the PCT application claims priority to and incorporates by reference Australian Patent Application No. 2007903624 filed Jul. 4, 2007.
Number | Date | Country | |
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Parent | PCT/AU2008/000989 | Jul 2008 | US |
Child | 12650992 | US |