CN101316649B - Gas generator - Google Patents
Gas generator Download PDFInfo
- Publication number
- CN101316649B CN101316649B CN2006800442176A CN200680044217A CN101316649B CN 101316649 B CN101316649 B CN 101316649B CN 2006800442176 A CN2006800442176 A CN 2006800442176A CN 200680044217 A CN200680044217 A CN 200680044217A CN 101316649 B CN101316649 B CN 101316649B
- Authority
- CN
- China
- Prior art keywords
- caltalyst
- reative cell
- gas
- wireway
- reactant liquor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007789 gas Substances 0.000 claims abstract description 67
- 239000012495 reaction gas Substances 0.000 claims abstract description 28
- 239000003054 catalyst Substances 0.000 claims abstract description 20
- 239000012295 chemical reaction liquid Substances 0.000 claims abstract description 13
- 239000000376 reactant Substances 0.000 claims description 38
- 239000007788 liquid Substances 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 12
- 229920001971 elastomer Polymers 0.000 claims description 11
- 239000000806 elastomer Substances 0.000 claims description 10
- 238000005213 imbibition Methods 0.000 claims description 6
- 230000007423 decrease Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 13
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 6
- 239000004810 polytetrafluoroethylene Substances 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 4
- -1 polytetrafluoroethylene Polymers 0.000 description 3
- 229920002635 polyurethane Polymers 0.000 description 3
- 239000004814 polyurethane Substances 0.000 description 3
- 238000012797 qualification Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 229920002379 silicone rubber Polymers 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 229910000033 sodium borohydride Inorganic materials 0.000 description 2
- 239000012279 sodium borohydride Substances 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
Images
Landscapes
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A gas generator has a reaction liquid and a catalyst body in its reaction chamber, with the catalyst body facing to the reaction liquid. At least one of the reaction chamber and the catalyst body is a flexible body. When the reaction liquid contacts with the catalyst body, it generates a reaction gas. The reaction gas pressure deforms the flexible body to realize an autocontrol of the reaction gas pressure. When the reaction gas pressure is lower, the deformation of the flexible body increases the contact area of the reaction liquid and the catalyst body to accelerate the generation of the reaction gas. When the reaction gas pressure is higher, the deformation of the flexible body decreases the contact area of the reaction liquid and the catalyst body to decelerate, even to stop the generation of the reaction gas.
Description
Technical field
The present invention relates to gas generator, particularly reactant liquor and caltalyst are by contacting the generator that produces gas.
Background technology
As everyone knows, reactant liquor and caltalyst produce gas and adopt usually and open general gas generator by contacting, and it realizes that by the balance between the pressure of the gravity of reactant liquor and the gas that produces gas pressure controls automatically, but its complex structure, poor stability uses and carries inconvenience.
Summary of the invention
The objective of the invention is to overcome above-mentioned defective, a kind of gas generator is provided, it is simple in structure, uses easy to carry, automatic pressure-controlled, safe and reliable.
The object of the present invention is achieved like this:
A kind of gas generator, comprise reative cell, it is characterized in that: liquid and caltalyst respond in the described reative cell, caltalyst orientating reaction liquid, at least one is flexible body for reative cell and caltalyst, produce reacting gas when reactant liquor contacts with caltalyst, reaction gas pressure makes the flexible body distortion, thereby the realization response gas pressure is controlled automatically:
When reaction gas pressure hour, the flexible body distortion causes reactant liquor and caltalyst contact area to strengthen, thus the generation of accelerated reaction gas;
When reaction gas pressure was big, the flexible body distortion caused reactant liquor to reduce with the caltalyst contact area even separates, and produced thereby slow down even stop reacting gas.
Described flexible body is an elastomer.
Described reative cell is the elasticity bag, reative cell is contained in the housing, the outer surface of reative cell is communicated with atmosphere by the passage on the housing, on the top cover of housing wireway is arranged, the bottom of wireway is stretched in the reative cell, and caltalyst is fixed in the lower end of wireway, wireway is communicated with reative cell by gas port, the top of wireway is connected with air supply pipe, and gas-liquid separation device is equipped with in its junction, and steam supply valve and safety valve are housed on the air supply pipe.
Described caltalyst is made of elasticity bag and the affixed catalyst of its appearance, the inner surface of elasticity bag is communicated with atmosphere by breather pipe, described reative cell has top cover, and wireway is arranged on the top cover, and the bottom of wireway is stretched in the reative cell, caltalyst is fixed in the lower end of wireway, wireway is communicated with reative cell by gas port, and wireway is not communicated with breather pipe, and the top of wireway is connected with air supply pipe, gas-liquid separation device is equipped with in its junction, and steam supply valve and safety valve are housed on the air supply pipe.
Described reative cell has the bottom surface that flexible sheet constitutes, flexible sheet is contained between reative cell sidewall and the bottom, the outer surface of flexible sheet is communicated with atmosphere by the passage on the bottom, described caltalyst is the porous catalyst body, caltalyst is contained between reative cell sidewall and the top cover, between top cover and the caltalyst gas-liquid separation device is housed, and air supply pipe is arranged on the top cover, steam supply valve is housed on the air supply pipe, on the reative cell sidewall safety valve is housed.
Porous flexible imbibition body is housed in the described reative cell.
In the inner chamber of described elasticity bag elastomer is housed.
The present invention mainly contains following actively useful effect: this gas generator is simple in structure, make reative cell or/and caltalyst distortion by reaction gas pressure, cause reactant liquor with the caltalyst contact or separate, thereby the realization response gas pressure is controlled automatically, safe and reliable, easy to use; The porous flexible imbibition body of energy absorption reaction liquid can be housed in the reative cell, emit reactant liquor when being squeezed, but this gas generator any direction is placed, easy to carry.
Summary of drawings
Fig. 1 is the structural representation of the embodiment of the invention one.
Fig. 2 is the structural representation of the embodiment of the invention two.
Fig. 3 is the structural representation of the embodiment of the invention three.
Fig. 4 is the structural representation of the embodiment of the invention four.
Fig. 5 is the structural representation of the embodiment of the invention five.
Fig. 6 is the structural representation of the embodiment of the invention six.
Embodiments of the invention
Embodiment one
Please refer to Fig. 1, the present invention is a kind of gas generator, comprise reative cell 1, liquid 101 and caltalyst 2 respond in the reative cell 1, caltalyst 2 orientating reaction liquid 101, reative cell 1 is an elastomer, it is an elasticity bag, the elasticity bag can be by silicon rubber, fluorubber or polyurethane etc. are made, and reative cell 1 is contained in the housing 3, and the outer surface of reative cell 1 is communicated with atmosphere by the passage on the housing 3 301, on the top cover 4 of housing 3 wireway 401 is arranged, the bottom of wireway 401 is stretched in the reative cell 1, and caltalyst 2 is fixed in the lower end of wireway 401, and wireway 401 is communicated with reative cell 1 by gas port 402, the top of wireway 401 is connected with air supply pipe 5, gas-liquid separation device 6 is equipped with in its junction, and it can be made of the polytetrafluoroethylene (PTFE) of micropore, and its effect is that reacting gas is separated with reactant liquor.Steam supply valve 501 and safety valve 8 are housed on the air supply pipe 5.Safety valve 8 can adopt unidirectional relief valve, and its effect is to prevent that the gas generator internal pressure is excessive, when pressure surpasses qualification pressure, and releasing pressure automatically.
Operating position: at first, open top cover 4, in reative cell 1, add an amount of reactant liquor 101, shut top cover 4 then, open steam supply valve 501, caltalyst 2 contacts with reactant liquor 101 and reacts the generation reacting gas, and reacting gas enters wireway 401 via gas port 402, through gas-liquid separation device 6, steam supply valve 501 air feed.Reaction gas pressure makes reative cell 1 distortion, cause reactant liquor with the caltalyst contact or separate, thereby the realization response gas pressure is controlled automatically:
When reaction gas pressure hour, reative cell 1 is shunk by the atmospheric pressure effect to cause reactant liquor 101 and caltalyst 2 contacts area to strengthen, thus accelerated reaction gas produces.
When reaction gas pressure was big, reative cell 1 overcame the atmospheric pressure effect and expands and cause reactant liquor 101 to reduce with caltalyst 2 contacts area even separate, and produces thereby slow down even stop reacting gas.
Embodiment two
Please refer to Fig. 2, the porous flexible imbibition body 102 of energy absorption reaction liquid 101 is housed in the reative cell 1,, discharge reactant liquor 101 when being squeezed as sponge.But this gas generator any direction is placed, and uses easy to carry, automatic pressure-controlled, safe and reliable.Operation principle is identical with embodiment one, does not repeat.
Embodiment three
Please refer to Fig. 3, the present invention is a kind of gas generator, comprise reative cell 1, liquid 101 and caltalyst 2 respond in the reative cell 1, caltalyst 2 orientating reaction liquid 101, caltalyst 2 is elastomers, and it is made of elasticity bag 201 and the affixed catalyst 202 of its appearance, and the inner surface of elasticity bag 201 is communicated with atmosphere by breather pipe 7.
Operating position: at first, open top cover 4, in reative cell 1, add an amount of reactant liquor 101, shut top cover 4 then, open steam supply valve 501, catalyst 202 contacts with reactant liquor 101 and reacts the generation reacting gas, and reacting gas enters wireway 401 via gas port 402, through gas-liquid separation device 6, steam supply valve 501 air feed.Reaction gas pressure makes elasticity bag 201 distortion, cause reactant liquor 101 with catalyst 202 contacts or separate, thereby the realization response gas pressure is controlled automatically:
When reaction gas pressure hour, elasticity bag 201 is expanded by the atmospheric pressure effect to cause reactant liquor 101 and catalyst 202 contacts area to strengthen, thus accelerated reaction gas produces.
When reaction gas pressure was big, elasticity bag 201 overcame the atmospheric pressure effect and shrinks and cause reactant liquor 101 to reduce with catalyst 202 contacts area even separate, and produces thereby slow down even stop reacting gas.
Embodiment four
Please refer to Fig. 4, elastomer 10 is housed in the elasticity bag 201, elastomer 10 can be spring, rubber, sponge etc., and elastomer 10 can increase the supply gas pressure of reacting gas.The elastic force of elastomer 10 is big more, and the supply gas pressure of reacting gas is big more.The porous flexible imbibition body 102 of energy absorption reaction liquid 101 is housed in the reative cell 1,, discharges reactant liquor 101 when being squeezed as sponge.But this gas generator any direction is placed, and uses easy to carry, automatic pressure-controlled, safe and reliable.Operation principle is identical with embodiment three, not superfluous stating.
Embodiment five
Please refer to Fig. 5, the present invention is a kind of gas generator, comprise reative cell 1, liquid 101 and caltalyst 2 respond in the reative cell 1, caltalyst 2 is the porous catalyst body, be contained between reative cell sidewall 104 and the top cover 4, reative cell 1 is an elastomer, its bottom surface is made of flexible sheet 103, flexible sheet 103 is contained between reative cell sidewall 104 and the bottom 9, the upper surface periphery of flexible sheet 103 is tightly connected by sealing ring 11 and reative cell sidewall 104, the lower surface periphery of flexible sheet 103 is tightly connected by sealing ring 12 and bottom 9, the lower surface of flexible sheet 103 is communicated with atmosphere by the passage 901 on the bottom 9, top cover 4 is tightly connected by sealing ring 13 and reative cell sidewall 104, between top cover 4 and the caltalyst 2 gas-liquid separation device 6 is housed, it can be made of the polytetrafluoroethylene (PTFE) of micropore, its effect is that reacting gas is separated with reactant liquor, wireway 401 is arranged on the top cover 4, the top of wireway 401 is connected with air supply pipe 5, and steam supply valve 501 is housed on the air supply pipe 5, and safety valve 8 is housed on the reative cell sidewall 104, safety valve 8 can adopt unidirectional relief valve, its effect is to prevent that the gas generator internal pressure is excessive, when pressure surpasses qualification pressure, and releasing pressure automatically.
Operating position: at first, take off safety valve 8, in reative cell 1, add an amount of reactant liquor 101, load onto safety valve 8 then, open steam supply valve 501, caltalyst 2 contacts with reactant liquor 101 and reacts the generation reacting gas, and reacting gas is via hole, gas-liquid separation device 6, wireway 401, air supply pipe 5, steam supply valve 501 air feed of caltalyst 2 self.Reaction gas pressure makes flexible sheet 103 distortion, cause reactant liquor 101 with caltalyst 2 contacts or separate, thereby the realization response gas pressure is controlled automatically:
When reaction gas pressure hour, flexible sheet 103 is inwardly shunk by the atmospheric pressure effect, cause reactant liquor 101 and caltalyst 2 contacts area to strengthen, thereby accelerated reaction gas produces.
When reaction gas pressure was big, flexible sheet 103 overcame the atmospheric pressure effect and outwards expands, and caused reactant liquor 101 to reduce with caltalyst 2 contacts area even separated, and produced thereby slow down even stop reacting gas.
Embodiment six
Please refer to Fig. 6, the porous flexible imbibition body 102 of energy absorption reaction liquid 101 is housed in the reative cell 1,, discharge reactant liquor 101 when being squeezed as sponge.But this gas generator any direction is placed, and uses easy to carry, automatic pressure-controlled, safe and reliable.Operation principle is identical with embodiment five, does not give unnecessary details.
Claims (3)
1. gas generator, comprise reative cell, it is characterized in that: liquid and caltalyst respond in the described reative cell, caltalyst orientating reaction liquid, at least one is flexible body for reative cell and caltalyst, produce reacting gas when reactant liquor contacts with caltalyst, reaction gas pressure makes the flexible body distortion, thereby the realization response gas pressure is controlled automatically:
When reaction gas pressure hour, the flexible body distortion causes reactant liquor and caltalyst contact area to strengthen, thus the generation of accelerated reaction gas;
When reaction gas pressure was big, the flexible body distortion caused reactant liquor to reduce with the caltalyst contact area even separates, and produced thereby slow down even stop reacting gas;
Described caltalyst is made of elasticity bag and the affixed catalyst of its appearance, the inner surface of elasticity bag is communicated with atmosphere by breather pipe, described reative cell has top cover, and wireway is arranged on the top cover, and the bottom of wireway is stretched in the reative cell, caltalyst is fixed in the lower end of wireway, wireway is communicated with reative cell by gas port, and wireway is not communicated with breather pipe, and the top of wireway is connected with air supply pipe, gas-liquid separation device is equipped with in its junction, and steam supply valve and safety valve are housed on the air supply pipe.
2. gas generator as claimed in claim 1 is characterized in that: porous flexible imbibition body is housed in the described reative cell.
3. gas generator as claimed in claim 1 is characterized in that: in the inner chamber of described elasticity bag elastomer is housed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2006800442176A CN101316649B (en) | 2006-01-27 | 2006-06-13 | Gas generator |
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200620001975.7 | 2006-01-27 | ||
CNU2006200019757U CN2863238Y (en) | 2006-01-27 | 2006-01-27 | Gas generator |
CN200620007750.2 | 2006-03-10 | ||
PCT/CN2006/001292 WO2007085144A1 (en) | 2006-01-27 | 2006-06-13 | A gas generator |
CN2006800442176A CN101316649B (en) | 2006-01-27 | 2006-06-13 | Gas generator |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101316649A CN101316649A (en) | 2008-12-03 |
CN101316649B true CN101316649B (en) | 2010-10-06 |
Family
ID=42813454
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2006800442176A Expired - Fee Related CN101316649B (en) | 2006-01-27 | 2006-06-13 | Gas generator |
Country Status (1)
Country | Link |
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CN (1) | CN101316649B (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1233525A (en) * | 1999-03-25 | 1999-11-03 | 王卫平 | Automatic pressure control type gas generator |
CN1449360A (en) * | 2000-08-28 | 2003-10-15 | 摩托罗拉公司 | Hydrogen generator utilizing ceramic technology |
-
2006
- 2006-06-13 CN CN2006800442176A patent/CN101316649B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1233525A (en) * | 1999-03-25 | 1999-11-03 | 王卫平 | Automatic pressure control type gas generator |
CN1449360A (en) * | 2000-08-28 | 2003-10-15 | 摩托罗拉公司 | Hydrogen generator utilizing ceramic technology |
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Publication number | Publication date |
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CN101316649A (en) | 2008-12-03 |
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PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101006 Termination date: 20140613 |
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EXPY | Termination of patent right or utility model |