CN114713009A - Purifier of methanol catalytic reforming hydrogen production device - Google Patents
Purifier of methanol catalytic reforming hydrogen production device Download PDFInfo
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- CN114713009A CN114713009A CN202210230970.5A CN202210230970A CN114713009A CN 114713009 A CN114713009 A CN 114713009A CN 202210230970 A CN202210230970 A CN 202210230970A CN 114713009 A CN114713009 A CN 114713009A
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- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 150
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 76
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 75
- 239000001257 hydrogen Substances 0.000 title claims abstract description 75
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 54
- 238000001833 catalytic reforming Methods 0.000 title claims abstract description 48
- 239000007789 gas Substances 0.000 claims abstract description 147
- 238000000746 purification Methods 0.000 claims abstract description 58
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 23
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 23
- 239000012295 chemical reaction liquid Substances 0.000 claims description 16
- 230000001105 regulatory effect Effects 0.000 claims description 14
- 238000004891 communication Methods 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 11
- 230000033228 biological regulation Effects 0.000 claims description 7
- 230000003750 conditioning effect Effects 0.000 claims description 6
- 238000011068 loading method Methods 0.000 claims description 6
- 239000002341 toxic gas Substances 0.000 abstract description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 22
- 238000010438 heat treatment Methods 0.000 description 15
- 229910002092 carbon dioxide Inorganic materials 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 12
- 239000001569 carbon dioxide Substances 0.000 description 11
- 230000009286 beneficial effect Effects 0.000 description 9
- 230000002349 favourable effect Effects 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000001514 detection method Methods 0.000 description 6
- 239000003245 coal Substances 0.000 description 4
- 208000002925 dental caries Diseases 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000004364 calculation method Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000003780 insertion Methods 0.000 description 2
- 230000037431 insertion Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000007096 poisonous effect Effects 0.000 description 2
- 238000002407 reforming Methods 0.000 description 2
- 238000010517 secondary reaction Methods 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/346—Controlling the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/62—Carbon oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/323—Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/502—Carbon monoxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Oil, Petroleum & Natural Gas (AREA)
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Abstract
The invention provides a purifier of a methanol catalytic reforming hydrogen production device, which comprises a first purifying device and a second purifying device, wherein the tail gas discharge end of the methanol catalytic reforming hydrogen production device is communicated with the gas inlet end of the first purifying device, and the gas outlet end of the first purifying device is communicated with the gas inlet end of the second purifying device. The first purification device is used for carrying out primary purification (can be used for reacting with gas (such as toxic gas) in the tail gas) on the tail gas discharged by the methanol catalytic reforming hydrogen production device, and the second purification device is used for carrying out secondary purification (can be used for reacting with gas (such as toxic gas) in the tail gas) on the tail gas purified by the first purification device.
Description
Technical Field
The invention relates to the technical field of air purifiers, in particular to a purifier of a methanol catalytic reforming hydrogen production device.
Background
Hydrogen is one of the most ideal energy sources in the 21 st century, the hydrogen generates the most energy under the condition of burning coal, gasoline and hydrogen with the same weight, and the combustion product is water without ash slag and waste gas, so that the environment is not polluted; the combustion of coal and oil mainly produces CO2 and SO2, which can produce greenhouse effect and acid rain, respectively. The reserves of coal and oil are limited, while hydrogen is mainly stored in water, and the only product after combustion is water, which can continuously generate hydrogen and never use up. The distribution of hydrogen is very broad and water is a large "warehouse" of hydrogen, containing 11% hydrogen. About 1.5% hydrogen in the soil; petroleum, coal, natural gas, animals and plants, etc. contain hydrogen. The bulk of hydrogen is in the form of compound water, and about 70% of the earth's surface is covered with water, which is a large storage of water, and thus hydrogen is an "inexhaustible" energy source.
With the progress of the technology, the technology of hydrogen production by reforming methanol and water gradually replaces the method of producing hydrogen from petroleum, coal and natural gas, but in the hydrogen production process of the existing methanol catalytic reforming hydrogen production device, toxic gases such as carbon monoxide and the like are often generated due to insufficient reaction and are directly discharged to pollute the environment, so that the development of a purifier of the methanol catalytic reforming hydrogen production device is urgently needed to overcome the defects in the current practical application.
Disclosure of Invention
The invention provides a purifier of a methanol catalytic reforming hydrogen production device, which is used for improving the following problems in the background technology: the existing methanol catalytic reforming hydrogen production device often generates toxic gases such as carbon monoxide and the like due to insufficient reaction in the hydrogen production process, and the direct emission can pollute the environment.
In order to solve the technical problem, the invention discloses a purifier of a methanol catalytic reforming hydrogen production device, which comprises: the tail gas exhaust end of the methanol catalytic reforming hydrogen production device is communicated with the gas inlet end of the first purification device, and the gas outlet end of the first purification device is communicated with the gas inlet end of the second purification device.
Preferably, the tail gas discharge end of the methanol catalytic reforming hydrogen production device is connected with the gas inlet end of the first purification device through a first connecting channel, and the gas outlet end of the first purification device is connected with the gas inlet end of the second purification device through a second connecting pipe.
Preferably, a plurality of fixing seats are respectively and fixedly installed at the bottom ends of the methanol catalytic reforming hydrogen production device, the first purification device and the second purification device.
Preferably, the second purifying device is connected with the gas collecting device through a third connecting pipe, a second control valve is arranged on the third connecting pipe, and a first control valve is arranged on the second connecting pipe.
Preferably, a gas regulating device is arranged in the connecting channel I.
Preferably, the gas conditioning device includes:
the air pump is arranged in the first connecting channel, and the output end of the air pump is communicated with the first through hole;
the left side of the first through hole penetrates through the first connecting channel, the first through hole is communicated with a first cavity, and the first cavity is arranged in the first connecting channel;
the inserting block is inserted at the opening on the left side of the through hole;
the first piston is connected to the inner wall of the cavity in a sliding mode;
the top end of the first connecting rod is fixedly mounted on the first piston, and the bottom end of the first connecting rod penetrates through the first cavity and is fixedly connected with the first rectangular block;
the first adjusting spring is sleeved on the first connecting rod, one end of the first adjusting spring is fixedly installed at the bottom end of the first piston, and the other end of the first adjusting spring is fixedly installed on the inner wall of the bottom end of the cavity;
the bottom end of the T-shaped block penetrates through the first through hole and the first cavity and is fixedly connected with the first piston;
and an output shaft of the electric telescopic rod II is fixedly provided with a rectangular block II, and the rectangular block II is vertically and slidably connected in the through hole I.
Preferably, the first purification device comprises:
the left end and the right end of the first box body are respectively provided with a second through hole, and the second through holes are communicated with the first connecting channel and the second connecting pipe;
the fourth connecting pipe is fixedly arranged at the top end of the first box body and is used for introducing reaction liquid;
the third control valve is arranged on the fourth connecting pipe;
and the carbon monoxide concentration detector is fixedly installed at the top end of the box body.
Preferably, the first box body is internally provided with:
the left end and the right end of the first moving plate are connected to the inner wall of the first box body in a sliding mode;
the electric telescopic rods are fixedly arranged on the inner wall of the bottom end of the box body, and the output ends of the electric telescopic rods are fixedly provided with adjusting plates;
the first motor is fixedly installed on the adjusting plate, and a push rod is fixedly installed on an output shaft of the first motor.
Preferably, the first box body is internally provided with:
the first belt pulley is fixedly arranged on an output shaft of the first motor;
the loading system, the loading system symmetry sets up both ends about motor one include:
the T-shaped sleeve is fixedly arranged on the inner wall of the bottom end of the box body;
the second pistons are connected to the inner wall of the top end of the T-shaped sleeve in a sliding mode;
one end of each long rod is fixedly arranged on the piston II, and the other end of each long rod penetrates through the T-shaped sleeve to be fixedly connected with the circular ring;
one end of the second adjusting spring is fixedly arranged on the second piston, and the other end of the second adjusting spring is fixedly arranged on the inner wall of the T-shaped sleeve;
one end of each short rod is fixedly arranged on the periphery of the inner wall of the circular ring, the other end of each short rod is rotatably connected with a rotating shaft, and a roller is fixedly arranged on each rotating shaft;
the sleeve is fixedly arranged on the inner wall of the bottom end of the box body;
the second belt pulley is connected to the sleeve in a bearing mode and is connected with the first belt pulley through a belt;
the second short rod is fixedly installed at the bottom end of the second belt pulley, and a hemisphere is fixedly installed at one end, close to the sleeve, of the second short rod;
the adjusting box is fixedly arranged on the sleeve, and a third through hole is formed in the adjusting box;
the third through hole is communicated with the interior of the sleeve, and a first check valve is further arranged on the inner wall of the third through hole;
the through hole IV is formed in the bottom end of the adjusting box;
the piston III is connected to the inner wall of the adjusting box in a sliding mode, one end of the piston III is fixedly provided with a first return spring, and the other end of the piston III is fixedly provided with a first T-shaped rod;
one end of the reset spring is fixedly arranged on the inner wall of the adjusting box, and the other end of the T-shaped rod is in contact with the hemisphere;
the top end of the T-shaped rod II is in contact with the moving plate I, and the bottom end of the T-shaped rod II is connected to the inner wall of the sleeve in a sliding mode;
the air release valve is fixedly arranged on the sleeve;
the first communicating pipe is communicated with the sleeves arranged at the left end and the right end respectively, and is further communicated with the T-shaped sleeve.
Preferably, the second purification device includes:
the bottom end of the second box body is fixedly arranged on the fixed seat, and the top end of the right side of the second box body is fixedly provided with a third connecting pipe;
the left end and the right end of the fixing plate are fixedly arranged on the inner walls of the left end and the right end of the box body II, and the top end of the fixing plate is provided with a stirring mechanism;
the stirring mechanism includes:
the driving box is arranged at the middle end of the fixing plate;
the top end of the connecting plate is fixedly arranged on the inner wall of the box body II, the bottom end of the connecting plate is fixedly arranged on the driving box, the left end and the right end of the connecting plate are respectively provided with a cavity II and a cavity III, and the cavity III is connected with the connecting pipe III;
the motor III is fixedly arranged in the driving box, and an output shaft of the motor III is connected with the long rod II through a belt assembly;
the middle end of the second long rod is rotatably connected to the connecting plate, and the left end and the right end of the second long rod are respectively arranged in the second cavity and the third cavity;
the stirring blades are fixedly arranged at the left end and the right end of the second long rod;
two ends of the third communicating pipe are respectively communicated with the second cavity and the third cavity, and a one-way valve III is fixedly installed in the third communicating pipe; and a second reaction liquid is arranged in the second cavity and the third cavity.
Preferably, the second purification device further comprises: a gas flow control mechanism;
the gas flow control mechanism includes:
the gas adjusting bin is arranged in the second cavity, and the bottom end of the gas adjusting bin is fixedly installed at the top end of the left side of the fixing plate;
the second motor is fixed at the bottom end of the gas regulation bin, a threaded rod is fixedly installed on an output shaft of the second motor, and the top end of the threaded rod is rotatably connected to the inner wall of the gas regulation bin;
the through holes are formed in the surface of the box body at the top end of the gas regulating bin, and a check valve II is fixedly installed in each through hole;
the six through holes are formed in the surface of the box body on the left side of the gas conditioning bin, the six through holes are connected with the second communicating pipe, and the other end of the third connecting pipe is communicated with the second connecting pipe;
the first supporting rod is arranged on the gas adjusting bin close to the sixth through hole, a rotating shaft at one end of the first supporting rod is connected to the gas adjusting bin, and the other end of the first supporting rod is clamped on the gas adjusting bin;
one end of the second reset spring is fixedly arranged on the first support rod, and the other end of the second reset spring is fixedly arranged on the gas adjusting bin;
the left end and the right end of the second moving plate are connected to the inner wall of the gas conditioning bin in a sliding mode respectively, and the second moving plate is in threaded connection with the threaded rod;
the through holes seven are symmetrically formed in the moving plate II at the left end and the right end of the threaded rod;
one end of each support rod II is connected to the second moving plate in a rotating mode, and the other end of each support rod II is clamped to the second moving plate;
and one end of the third reset spring is fixedly arranged on the second support rod, and the other end of the third reset spring is fixedly arranged on the second moving plate.
The technical solution of the present invention is further described in detail by the accompanying drawings and embodiments.
Drawings
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention and not to limit the invention. In the drawings:
FIG. 1 is a schematic view of the mechanism of the purifier body of the present invention.
FIG. 2 is a schematic view of the point A in FIG. 1 according to the present invention.
FIG. 3 is a schematic view of the structure of the purification apparatus of the present invention.
FIG. 4 is a left side view of the T-shaped sleeve structure of the present invention.
FIG. 5 is an enlarged view of the point B structure of FIG. 4 according to the present invention.
FIG. 6 is an enlarged view of the point C structure of FIG. 3 according to the present invention.
Fig. 7 is an enlarged view of a portion of fig. 6 according to the present invention.
Fig. 8 is a partial top view of fig. 3 in accordance with the present invention.
FIG. 9 is a schematic view of a second embodiment of the purification apparatus of the present invention.
Fig. 10 is an enlarged view of a portion of fig. 9 according to the present invention.
In the figure: 1. a second rectangular block; 2. a methanol catalytic reforming hydrogen production device; 3. a first purifying device; 4. a second purifying device; 5. connecting a first channel; 6. a second connecting pipe; 7. a first control valve; 8. an air pump; 9. a first through hole; 10. a first cavity; 11. a first piston; 12. a fixed seat; 13. a third connecting pipe; 14. a second control valve; 15. an insertion block; 16. adjusting a first spring; 17. a first connecting rod; 18. a first rectangular block; 19. a T-shaped block; 20. a first box body; 21. a second through hole; 22. a fourth connecting pipe; 23. a third control valve; 24. a carbon monoxide concentration detector; 25. moving a first plate; 26. an electric telescopic rod; 27. an adjusting plate; 28. a first motor; 29. a push rod; 30. a first belt pulley; 31. a T-shaped sleeve; 32. a second piston; 33. a first long rod; 34. a circular ring; 35. a second adjusting spring; 36. a short rod I; 37. a rotating shaft; 38. a roller; 39. a sleeve; 40. a second belt pulley; 41. a short rod II; 42. a hemisphere; 43. an adjusting box; 44. a third through hole; 45. a fourth through hole; 46. a piston III; 47. a first return spring; 48. a first T-shaped rod; 49. a belt; 50. a T-shaped rod II; 51. a first communicating pipe; 52. a second box body; 53. a second communicating pipe; 54. a connecting plate; 55. a gas conditioning bin; 56. a one-way valve I; 57. a second motor; 58. a threaded rod; 59. a deflation valve; 60. a fifth through hole; 61. a sixth through hole; 62. a first support rod; 63. a second return spring; 64. moving a second plate; 65. a seventh through hole; 66. a second support rod; 67. a third return spring; 68. a fixing plate; 69. a second cavity; 70. a second one-way valve; 71. a drive box; 72. a third motor; 73. a long rod II; 74. a third cavity; 75. a stirring blade; 76. a third communicating pipe; 77. a one-way valve III; 78. a second reaction solution; 79. and a second electric telescopic rod.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it should be understood that they are presented herein only to illustrate and explain the present invention and not to limit the present invention.
In addition, the descriptions related to the first, the second, etc. in the present invention are only used for description purposes, do not particularly refer to an order or sequence, and do not limit the present invention, but only distinguish components or operations described in the same technical terms, and are not understood to indicate or imply relative importance or implicitly indicate the number of indicated technical features. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one of the feature. In addition, technical solutions and technical features between various embodiments can be combined with each other, but must be realized by a person skilled in the art, and when the technical solutions are contradictory or cannot be realized, the combination of the technical solutions should be considered to be absent and not be within the protection scope of the present invention.
Example 1
An embodiment of the present invention provides a purifier for a methanol catalytic reforming hydrogen production device, as shown in fig. 1, including: the device comprises a first purification device 3 and a second purification device 4, wherein the tail gas discharge end of the methanol catalytic reforming hydrogen production device 2 is communicated with the gas inlet end of the first purification device 3, and the gas outlet end of the first purification device 3 is communicated with the gas inlet end of the second purification device 4.
The beneficial effects of the above technical scheme are: the first purification device 3 is used for carrying out primary purification (can be reacted with gas (such as poisonous gas) in the tail gas) on the tail gas discharged by the methanol catalytic reforming hydrogen production device 2, the second purification device 4 is used for carrying out secondary purification (can be reacted with gas (such as poisonous gas) in the tail gas) on the tail gas purified by the first purification device, the first purification device and the second purification device can be used for reacting different gases in the tail gas, and concretely, referring to the following embodiment, the toxic gas in the hydrogen production process is purified to reach the emission standard or generate the emission of the nontoxic gas through chemical reaction, so that the environment is more environment-friendly, the first purification device 3 and the second purification device 4 are arranged on the methanol catalytic reforming hydrogen production device 2, so that the problem that the existing methanol catalytic reforming hydrogen production process generates the toxic gases such as carbon monoxide and the like due to insufficient reaction is solved, the direct discharge can pollute the environment.
Example 2
On the basis of the embodiment 1, the tail gas discharge end of the methanol catalytic reforming hydrogen production device 2 is connected with the gas inlet end of the first purification device 3 through the first connecting channel 5, and the gas outlet end of the first purification device 3 is connected with the gas inlet end of the second purification device 4 through the second connecting pipe 6.
Optionally, a plurality of fixing seats 12 are respectively fixedly mounted on the left sides of the bottom ends of the methanol catalytic reforming hydrogen production device 2, the first purification device 3 and the second purification device 4.
Optionally, the second purification device 4 is connected with the gas collection device through a third connecting pipe 13, a second control valve 14 is arranged on the third connecting pipe 13, and a first control valve 7 is arranged on the second connecting pipe 6.
The beneficial effects of the above technical scheme are: the connecting channel I5 and the connecting pipe II 6 are arranged, so that the methanol catalytic reforming hydrogen production device 2, the purification device I3 and the purification device II 4 can be connected conveniently; a gas regulating device is arranged in the connecting channel I5, so that the flow of the gas entering the purifying device I3 from the methanol catalytic reforming hydrogen production device 2 can be controlled; the control valve I7 is arranged, so that the flow of the gas introduced into the second purification device 4 from the first purification device 3 can be controlled; the gas collecting device is arranged, so that the purified tail gas (containing hydrogen) can be collected; the second control valve 14 is arranged, so that the second purification device 4 is sealed; through setting up fixing base 12, be favorable to right purifier body 1 fixes.
Example 3
On the basis of embodiment 2, as shown in fig. 2, a gas regulating device is arranged inside the connecting channel-5, and the gas regulating device comprises:
the air pump 8 is arranged in the first connecting channel 5, and the output end of the air pump 8 is communicated with the first through hole 9;
the left side of the first through hole 9 penetrates through the first connecting channel 5, the first through hole 9 is communicated with a first cavity 10, and the first cavity 10 is arranged in the first connecting channel 5;
the insertion block 15 is inserted at the opening at the left side of the first through hole 9;
the first piston 11 is connected to the inner wall of the first cavity 10 in a sliding mode;
the top end of the first connecting rod 17 is fixedly mounted on the first piston 11, and the bottom end of the first connecting rod 17 penetrates through the first cavity 10 to be fixedly connected with the first rectangular block 18;
the first adjusting spring 16 is sleeved on the first connecting rod 17, one end of the first adjusting spring 16 is fixedly installed at the bottom end of the first piston 11, and the other end of the first adjusting spring 16 is fixedly installed on the inner wall of the bottom end of the first cavity 10;
the bottom end of the T-shaped block 19 penetrates through the first through hole 9 and the first cavity 10 to be fixedly connected with the first piston 11;
and the output shaft of the second electric telescopic rod 79 is fixedly provided with a second rectangular block 1, and the second rectangular block 1 is vertically and slidably connected into the first through hole 9.
The working principle of the technical scheme is as follows: when the flow of the gas introduced into the first purification device 3 by the methanol catalytic reforming hydrogen production device 2 needs to be controlled, firstly, the gas pump 8 is controlled to be started, the gas pump 8 discharges pressure gas, downward thrust is generated on the piston 11 through the first through hole 9 and the first cavity 10, the piston 11 moves downwards to extrude the first adjusting spring 16, the first connecting rod 17 further moves downwards to drive the first rectangular block 18 to move downwards, the opening size of the first connecting channel at the rectangular block 18 is adjusted, so that the gas introduced into the first purification device 3 is controlled, when the device needs to be reset, the second electric telescopic rod 79 is started, the second rectangular block 1 is driven by the second electric telescopic rod 79 to move upwards, the gas generated by the gas pump 8 cannot pass through the first through hole 9, and then the plug-in block 15 is taken out, and when the air pump 8 is damaged or fails, a user can manually press the T-shaped block 19 downwards to control the flow of the connecting channel I5.
The beneficial effects of the above technical scheme are: the air pump 8 and the T-shaped block 19 are arranged, so that manual and automatic control over the air adjusting device is facilitated; the electric telescopic rod II 79 and the rectangular block II 1 are arranged, so that the air generated by the air pump 8 can be intercepted; the first adjusting spring 16 is arranged to facilitate the resetting of the first piston 11; the rectangular block I18 is beneficial to controlling the flow of the gas introduced into the purification device I3 by the methanol catalytic reforming hydrogen production device 2.
Example 4
On the basis of any one of embodiments 1 to 3, as shown in fig. 3 to 8, the first purification device 3 includes:
the bottom end of the first box body 20 is fixedly mounted on the fixed seat 12, the left end and the right end of the first box body 20 are respectively provided with a second through hole 21, and the second through holes 21 are communicated with the first connecting channel 5 and the second connecting pipe 6;
a fourth connecting pipe 22, wherein the fourth connecting pipe 22 is fixedly installed at the top end of the first box body 20, and the fourth connecting pipe 22 is used for introducing a reaction liquid (the reaction liquid can be steam or a reaction liquid for absorbing or reacting other gases in the methanol reforming hydrogen production device);
a third control valve 23, wherein the third control valve 23 is arranged on the fourth connecting pipe 22;
and the carbon monoxide concentration detector 24 is fixedly arranged at the top end of the first box body 20.
Optionally, the first box body 20 is further provided with:
the left end and the right end of the first moving plate 25 are connected to the inner wall of the first box body 20 in a sliding mode;
the electric telescopic rods 26 are fixedly installed on the inner wall of the bottom end of the first box body 20, and the output ends of the electric telescopic rods 26 are fixedly provided with adjusting plates 27;
the first motor 28 is fixedly arranged on the adjusting plate 27, and an output shaft of the first motor 28 is fixedly provided with a push rod 29;
optionally, the first box body 20 is further provided with:
the first belt pulley 30 is fixedly arranged on an output shaft of the first motor 28;
the loading system, the loading system symmetry sets up both ends about motor 28 includes:
the T-shaped sleeve 31 is fixedly arranged on the inner wall of the bottom end of the first box body 20;
the second pistons 32 are connected to the inner wall of the top end of the T-shaped sleeve 31 in a sliding mode;
one end of each long rod 33 is fixedly installed on the corresponding piston 32, and the other end of each long rod 33 penetrates through the T-shaped sleeve 31 to be fixedly connected with the corresponding circular ring 34;
one end of the second adjusting spring 35 is fixedly mounted on the second piston 32, and the other end of the second adjusting spring 35 is fixedly mounted on the inner wall of the T-shaped sleeve 31;
one end of each short rod 36 is fixedly arranged on the periphery of the inner wall of the circular ring 34, the other end of each short rod 36 is rotatably connected with a rotating shaft 37, and a roller 38 is fixedly arranged on each rotating shaft 37;
the sleeve 39 is fixedly arranged on the inner wall of the bottom end of the first box body 20;
the second belt pulley 40 is in bearing connection with the sleeve 39, and the second belt pulley 40 is connected with the first belt pulley 30 through a belt 49;
the second short rod 41 is fixedly installed at the bottom end of the second belt pulley 40, and a hemisphere 42 is fixedly installed at one end, close to the sleeve 39, of the second short rod 41;
the adjusting box 43 is fixedly arranged on the sleeve 39, and a third through hole 44 is formed in the adjusting box 43;
a third through hole 44, wherein the third through hole 44 is communicated with the interior of the sleeve 39, and a first check valve 56 is further arranged on the inner wall of the third through hole 44;
a fourth through hole 45, wherein the fourth through hole 45 is arranged at the bottom end of the adjusting box 43;
the piston III 46 is connected to the inner wall of the adjusting box 43 in a sliding mode, one end of the piston III 46 is fixedly provided with a first return spring 47, and the other end of the piston III 46 is fixedly provided with a first T-shaped rod 48;
the other end of the first return spring 47 is fixedly arranged on the inner wall of the adjusting box 43, and the other end of the first T-shaped rod 48 is in contact with the hemispheroid 42;
the top end of the second T-shaped rod 50 is in contact with the first moving plate 25, and the bottom end of the second T-shaped rod 50 is connected to the inner wall of the sleeve 39 in a sliding mode;
the air release valve 59, the said air release valve 59 is fixedly mounted on said bush 39;
and the first communication pipe 51 is communicated with the sleeves 39 arranged at the left end and the right end of the first communication pipe 51 respectively, and the first communication pipe 51 is further communicated with the T-shaped sleeve 31.
The working principle of the technical scheme is as follows: in the hydrogen production process of the methanol catalytic reforming hydrogen production device 2, in the insufficient reaction process, a mixed gas of carbon monoxide, carbon dioxide and hydrogen is often generated, in order to eliminate the carbon monoxide gas contained in the mixed gas, a user introduces the gas generated by the methanol catalytic reforming hydrogen production device 2 into the first box body 20 through the first connecting channel 5, and then opens the third control valve 23, so that high-temperature water vapor is introduced from the fourth connecting pipe 22;
in order to make the carbon monoxide gas and the water vapor fully react, a user can start a motor I28, the motor I28 rotates to drive a belt pulley I30 to rotate, the belt pulley I30 rotates to drive a belt pulley II 40 to rotate, so that a short rod II 41 fixedly arranged on the belt pulley II 40 rotates, the short rod II 41 rotates to drive the hemispheroid 42 to extrude a T-shaped rod I48, the T-shaped rod I48 moves to drive a piston III 46 to move towards the left side, air entering from a through hole IV 45 is compressed, further air is led into the sleeve 39 from the through hole III 44, then the air pressure in the sleeve 39 is increased, upward thrust is generated on the T-shaped rod II 50, the T-shaped rod II 50 moves upwards to drive a moving plate I25 to move upwards, and thus the reaction of the water vapor and the carbon monoxide is pressurized, simultaneously, the air pressure in the sleeve 39 rises, high-pressure air enters the T-shaped sleeve 31 through the first communication pipe 51, the second piston 32 is extruded, the first long rod 33 moves towards two ends, the circular ring 34 moves towards two ends, the belt 49 is further separated from the first belt pulley 30, and then the first motor 28 is turned off;
and finally, starting the electric telescopic rod 26, wherein the electric telescopic rod 26 drives the adjusting plate 27 to move upwards, and further the push rod 29 moves upwards, so that the first moving plate 25 is pushed, secondary pressurization is realized, and the reaction is more sufficient, a user stops adding water vapor into the first box body 20 by observing the detection of the carbon monoxide concentration detector 24 when the detected carbon monoxide concentration is zero, then closes the electric telescopic rod 26, and further exhausts high-pressure gas in the sleeve 39 by opening the air exhaust valve 59, so that the second T-shaped rod 50 and the first moving plate 25 are reset.
The beneficial effects of the above technical scheme are: the carbon monoxide concentration detector 24 is arranged, so that a user can observe the concentration of the carbon monoxide in the first box body 20 conveniently; the T-shaped sleeve 31 is arranged, so that the connection relation between the belt 49 and the first belt pulley 30 is controlled, and the first motor 28 cannot control the rotation of the second belt pulley 40; the adjustment box 43 is arranged to facilitate the supply of gas to the sleeve 39; the first check valve 56 is arranged, so that gas is prevented from escaping from the third through hole 44; the arrangement of the roller 38 is beneficial to protecting the belt 49, and the friction resistance of the belt 49 is further reduced; the high-pressure gas in the sleeve 39 is discharged by arranging a vent valve 59.
Example 5
On the basis of any one of embodiments 1 to 4, as shown in fig. 9 to 10, the second purification device 4 includes:
the bottom end of the second box body 52 is fixedly arranged on the fixed seat 12, and the top end of the right side of the second box body 52 is fixedly provided with a third connecting pipe 13;
the left end and the right end of the fixing plate 68 are fixedly installed on the inner walls of the left end and the right end of the second box body 52, and the top end of the fixing plate 68 is provided with a stirring mechanism;
the stirring mechanism includes:
a driving box 71, wherein the driving box 71 is arranged at the middle end of the fixed plate 68;
the top end of the connecting plate 54 is fixedly mounted on the inner wall of the second box body 52, the bottom end of the connecting plate 54 is fixedly mounted on the driving box 71, the left end and the right end of the connecting plate 54 are respectively provided with a second cavity 69 and a third cavity 74, and the third cavity 74 is connected with the third connecting pipe 13;
the motor III 72 is fixedly arranged in the driving box 71, and an output shaft of the motor III 72 is connected with the long rod II 73 through a belt assembly;
the middle end of the second long rod 73 is rotatably connected to the connecting plate 54, and the left end and the right end of the second long rod 73 are respectively arranged in the second cavity 69 and the third cavity 74;
the stirring blades 75 are fixedly arranged at the left end and the right end of the second long rod 73;
two ends of the third communication pipe 76 are respectively communicated with the second cavity 69 and the third cavity 74, and a check valve III 77 is fixedly installed in the third communication pipe 76; a second reaction liquid 78 is arranged inside the second cavity 69 and the third cavity 74 (the second reaction liquid 78 can be a sodium hydroxide liquid, and the hydrogen gas can be purified by reacting with carbon dioxide).
The working principle of the technical scheme is as follows: when the mixed gas of the hydrogen and the carbon dioxide is introduced into the second cavity 69, the third motor 72 is started to drive the belt assembly to rotate, the second long rod 73 is further driven to rotate, the second long rod 73 rotates to drive the stirring blade 75 to rotate along with the second long rod, so that the carbon dioxide introduced into the second cavity 69 and the second reaction liquid 78 are fully reacted, after the second reaction liquid 78 in the second cavity 69 is fully reacted, the gas is discharged into the second reaction liquid 78 in the third cavity 74 from the third communicating pipe 76, then secondary reaction is carried out, the carbon dioxide in the mixed gas is fully reacted, and finally the purified hydrogen is discharged into the gas collection device from the third connecting pipe 13.
The beneficial effects of the above technical scheme are: through setting up check valve three 77, be favorable to preventing the refluence of reaction liquid two 78, through setting up stirring vane 75, be favorable to making the abundant reaction of carbon dioxide composition in the mist absorb, through setting up cavity two 69 and cavity three 74, be favorable to passing through the secondary reaction with carbon dioxide to further purify the hydrogen in the mist.
Example 6
On the basis of embodiment 5, the second purification device 4 further includes: a gas flow control mechanism;
the gas flow control mechanism includes:
the gas adjusting bin 55 is arranged in the second cavity 69, and the bottom end of the gas adjusting bin 55 is fixedly mounted at the top end of the left side of the fixing plate 68;
the second motor 57 is fixed at the bottom end of the gas regulation bin 55, a threaded rod 58 is fixedly installed on an output shaft of the second motor 57, and the top end of the threaded rod 58 is rotatably connected to the inner wall of the gas regulation bin 55;
the five through holes 60 are formed in the surface of the box body at the top end of the gas adjusting bin 55, and a second check valve 70 is fixedly installed in the five through holes 60;
the five through holes 60 are formed in the surface of the box body on the left side of the gas conditioning bin 55, the six through holes 61 are connected with the second communicating pipe 53, and the other end of the third connecting pipe 13 is communicated with the second connecting pipe 6;
the first support rod 62 is arranged on the gas adjusting bin 55 close to the six through holes 61, one end of the first support rod 62 is connected to the gas adjusting bin 55 through a rotating shaft, and the other end of the first support rod 62 is clamped on the gas adjusting bin 55;
one end of the second return spring 63 is fixedly mounted on the first support rod 62, and the other end of the second return spring 63 is fixedly mounted on the gas adjusting bin 55;
the left end and the right end of the second moving plate 64 are respectively connected to the inner wall of the gas adjusting bin 55 in a sliding mode, and the second moving plate 64 is in threaded connection with the threaded rod 58;
the through holes seven 65 are symmetrically formed in the moving plate two 64 at the left end and the right end of the threaded rod 58;
one end of each second support rod 66 is connected to the second moving plate 64 in a rotating mode, and the other end of each second support rod 66 is clamped on the second moving plate 64;
one end of the third return spring 67 is fixedly mounted on the second support rod 66, and the other end of the third return spring 67 is fixedly mounted on the second moving plate 64.
The working principle of the technical scheme is as follows: after the carbon monoxide gas in the first tank body 20 fully reacts, the control valve I7 is opened, so that the mixed gas of the hydrogen gas and the carbon dioxide gas passes through the communicating pipe II 53 and the through hole VI 61, then, a second motor 57 is started, the second motor 57 rotates to drive the threaded rod 58 to rotate, so that the second moving plate 64 moves up and down, when the second moving plate 64 moves up, the air pressure at the bottom end of the second moving plate 64 is reduced, so that the first support rod 62 at the bottom end of the second moving plate 64 rotates towards the right side, the mixed gas enters the cavity at the bottom end of the second moving plate 64 from the six through holes 61, when the second moving plate 64 moves downwards, the mixed gas of hydrogen and carbon dioxide at the bottom end of the second moving plate 64 enters the cavity at the top end of the second moving plate 64 through the seventh through hole 65, and finally is discharged into the second cavity 69 through the fifth through hole 60.
The beneficial effects of the above technical scheme are: the gas regulating bin 55 is arranged, so that the flow of the introduced mixed gas can be controlled; the resetting of the first support rod 62 and the second support rod 66 is facilitated by the arrangement of the second return spring 63 and the third return spring 67; through setting up motor two 57 is favorable to realizing the gaseous volume that lets in of automatic control, through setting up check valve two 70 is favorable to preventing two 78 refluxes of reaction liquid in the two 69 cavitys, through setting up two 62 and two 66 branches, be favorable to controlling the gaseous volume that lets in the six 61 through-holes, and can the separation gas, prevent to enter into the volume in two 69 final cavitys, keep in certain controllable state, further make the user judge according to the number of times that lets in gas that enters into two 69 cavitys, and reaction liquid 78 in timely two 69 and the three 74 cavitys of change, prevent that the concentration of sodium hydroxide reduces in the reaction liquid 78, make the reaction insufficient, unusual convenient and practical.
Example 7
On the basis of any one of embodiments 1-6, the purifier for the methanol catalytic reforming hydrogen production device further comprises a temperature adjusting device (such as a heating device), wherein the temperature adjusting device is used for adjusting the internal temperature of the first box body 20 (used for adjusting the temperature of water vapor and carbon monoxide in the first box body 20 so as to facilitate the reaction of the water vapor and the carbon monoxide);
the purifier of the methanol catalytic reforming hydrogen production device further comprises:
the flow velocity sensor is used for detecting the flow velocity of the water vapor introduced into the connecting pipe IV 22;
the first temperature sensor is used for detecting the temperature inside the first box body 20 when the temperature adjusting device does not start to operate;
controller, alarm, the controller is connected with flow sensor, temperature sensor one, alarm electricity, the controller is based on flow sensor, temperature sensor one control alarm work, including following step:
step 1: calculating the power P required by the temperature regulating device to heat the tail gas (mixed gas) of the methanol catalytic reforming hydrogen production device 2 according to the formula (1) and the detection value of the temperature sensor I1：
Wherein P is1The power m required for the temperature regulating device to heat the tail gas of the methanol catalytic reforming hydrogen production device 21Lambda is the mass of the mixed gas (mixed gas containing CO) generated by the methanol catalytic reforming hydrogen production apparatus 2 per unit time1Is the specific heat, lambda, of the carbon monoxide gas in the mixed gas2Is specific heat, lambda, of carbon dioxide gas in the mixed gas4Specific heat of hydrogen in the mixed gas, T1Is a target temperature, T, of an interior of the cabinet2Is a detected value of the temperature sensor, T0The initial temperature of the interior of the first box body 20 (when no water vapor or tail gas is introduced), S is the working time (heating time) of the temperature regulating device, alpha is the heat conductivity coefficient of carbon monoxide gas, S is the cross sectional area of the first box body 20, and h is the height of the first box body 20; wherein
Represents the heat dissipation amount of the mixed gas during the preheating process of the temperature regulation device, wherein
The power required by the temperature adjusting device for heating the mixed gas is represented; for example: get m150kg, take lambda1Is 13.8 kcal/kg.K, taking lambda43.41 kcal/kg-K, taking lambda2Is 8.93 kcal/kg.K, and T is taken1773K, take T0295K, take T2353K for S240S and 4m for S2Taking alpha as 0.59KW/(m × K), taking h as 1.3m, and calculating to obtain the power P required by the temperature regulating device1Approximately equal to 11.69 KW;
step 2: calculating the actual total heating power P of the temperature adjusting device according to a formula (2) and the detection value of the flow rate sensor, comparing the actual total heating power P of the temperature adjusting device with a preset theoretical heating power range by the controller, and controlling an alarm to give an alarm by the controller when the actual total heating power P is not in the preset theoretical heating power range;
wherein P is the total actual heating power of the temperature regulating device, m3The flow rate of the introduced water vapor is lambda3The specific heat of the water vapor is obtained, and V is the detection value of the flow rate sensor; wherein
Represents the power required for heating the thermostat after the introduction of water vapor, for example: get m330kg, V is 3.0m/s, lambda is30.47 kcal/kg-K, and the total actual heating power P of the temperature regulating device is about 57.66KW by calculation.
The beneficial effects of the above technical scheme are:
firstly, calculating the power required by the temperature adjusting device according to a formula (1) and a detection value of a temperature sensor, and comprehensively considering the mass of a mixed gas (a mixed gas containing CO) generated by the methanol catalytic reforming hydrogen production device 2 in unit time, the specific heat of carbon monoxide in the mixed gas, the specific heat of carbon dioxide in the mixed gas, the specific heat of hydrogen in the mixed gas, the initial temperature (when water vapor and tail gas are not introduced) in the box body I20, the working time (heating time) of the temperature adjusting device, the heat conductivity coefficient of the carbon monoxide gas, the cross sectional area of the box body I20 and the height of the box body I20; the calculation result is more accurate and reliable;
and then according to the formula (2) and the detection value of the flow velocity sensor, comprehensively considering the flow of the introduced water vapor in unit time, the specific heat of the water vapor and other factors, and further calculating the actual total heating power of the temperature regulating device, so that the calculation result is more accurate and reliable.
The controller controls the flow rate sensor and the temperature sensor to work, when the actual total heating power of the temperature adjusting device is not within the preset theoretical heating power range, the controller controls the alarm to give an alarm, so that a user is reminded to adjust (such as increase) the output power of the temperature adjusting device, the reaction of carbon monoxide and steam is enabled to be more sufficient, and the requirement of the user on the purifier of the methanol catalytic reforming hydrogen production device is further met.
It will be apparent to those skilled in the art that various changes and modifications may be made in the present invention without departing from the spirit and scope of the invention. Thus, if such modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalents, the present invention is also intended to include such modifications and variations.
Claims (10)
1. A purifier of a methanol catalytic reforming hydrogen production device is characterized by comprising: the device comprises a first purification device (3) and a second purification device (4), wherein the tail gas discharge end of the methanol catalytic reforming hydrogen production device (2) is communicated with the gas inlet end of the first purification device (3), and the gas outlet end of the first purification device (3) is communicated with the gas inlet end of the second purification device (4).
2. The purifier of the methanol catalytic reforming hydrogen production device as claimed in claim 1, wherein the exhaust end of the methanol catalytic reforming hydrogen production device (2) is connected with the air inlet end of the first purifying device (3) through a first connecting channel (5), and the exhaust end of the first purifying device (3) is connected with the air inlet end of the second purifying device (4) through a second connecting pipe (6).
3. The purifier of the methanol catalytic reforming hydrogen production device according to claim 1, wherein a plurality of fixing seats (12) are respectively fixedly installed at the bottom ends of the methanol catalytic reforming hydrogen production device (2), the first purification device (3) and the second purification device (4).
4. The purifier of a methanol catalytic reforming hydrogen production device as defined in claim 2, wherein the second purifying device (4) is connected with a gas collecting device through a third connecting pipe (13), the third connecting pipe (13) is provided with a second control valve (14), and the second connecting pipe (6) is provided with a first control valve (7).
5. The purifier of a methanol catalytic reforming hydrogen production device as claimed in claim 2, characterized in that the first connecting channel (5) is internally provided with a gas regulating device.
6. The purifier of a methanol catalytic reforming hydrogen production device as claimed in claim 5, wherein the gas conditioning device comprises:
the air pump (8) is arranged in the first connecting channel (5), and the output end of the air pump (8) is communicated with the first through hole (9);
the left side of the first through hole (9) penetrates through the first connecting channel (5), the first through hole (9) is communicated with a first cavity (10), and the first cavity (10) is arranged in the first connecting channel (5);
the plug-in block (15) is plugged at the left opening of the first through hole (9);
the first piston (11), the first piston (11) is connected to the inner wall of the first cavity (10) in a sliding mode;
the top end of the first connecting rod (17) is fixedly mounted on the first piston (11), and the bottom end of the first connecting rod (17) penetrates through the first cavity (10) to be fixedly connected with the first rectangular block (18);
the first adjusting spring (16) is sleeved on the first connecting rod (17), one end of the first adjusting spring (16) is fixedly installed at the bottom end of the first piston (11), and the other end of the first adjusting spring (16) is fixedly installed on the inner wall of the bottom end of the first cavity (10);
the bottom end of the T-shaped block (19) penetrates through the first through hole (9) and the first cavity (10) and is fixedly connected with the first piston (11);
and the output shaft of the second electric telescopic rod (79) is fixedly provided with a second rectangular block (1), and the second rectangular block (1) is vertically and slidably connected into the first through hole (9).
7. The purifier of a methanol catalytic reforming hydrogen production device as claimed in claim 1, wherein the first purifying means (3) comprises:
the box body I (20), the left end and the right end of the box body I (20) are respectively provided with a through hole II (21), and the through hole II (21) is communicated with the connecting channel I (5) and the connecting pipe II (6);
the fourth connecting pipe (22), the fourth connecting pipe (22) is fixedly installed at the top end of the first box body (20), and the fourth connecting pipe (22) is used for introducing reaction liquid;
a third control valve (23), wherein the third control valve (23) is arranged on the fourth connecting pipe (22);
and the carbon monoxide concentration detector (24) is fixedly arranged at the top end of the first box body (20).
8. The purifier of a methanol catalytic reforming hydrogen production device as claimed in claim 7, characterized in that the first box body (20) is internally provided with:
the left end and the right end of the first moving plate (25) are connected to the inner wall of the first box body (20) in a sliding mode;
the electric telescopic rods (26) are fixedly mounted on the inner wall of the bottom end of the first box body (20), and an adjusting plate (27) is fixedly mounted at the output end of each electric telescopic rod (26);
the first motor (28), the first motor (28) is fixedly arranged on the adjusting plate (27), and an output shaft of the first motor (28) is fixedly provided with a push rod (29);
the first belt pulley (30), the first belt pulley (30) is fixedly arranged on an output shaft of the first motor (28);
the loading system, the loading system symmetry sets up both ends about motor (28), includes:
the T-shaped sleeve (31) is fixedly arranged on the inner wall of the bottom end of the first box body (20);
the second pistons (32) are connected to the inner wall of the top end of the T-shaped sleeve (31) in a sliding mode;
one end of each long rod (33) is fixedly arranged on the piston II (32), and the other end of each long rod (33) penetrates through the T-shaped sleeve (31) to be fixedly connected with the circular ring (34);
one end of the second adjusting spring (35) is fixedly installed on the second piston (32), and the other end of the second adjusting spring (35) is fixedly installed on the inner wall of the T-shaped sleeve (31);
one end of each short rod I (36) is fixedly installed on the periphery side of the inner wall of the circular ring (34), the other end of each short rod I (36) is rotatably connected with a rotating shaft (37), and a roller (38) is fixedly installed on each rotating shaft (37);
the sleeve (39) is fixedly arranged on the inner wall of the bottom end of the first box body (20);
the second belt pulley (40), the second belt pulley (40) is connected to the sleeve (39) in a bearing mode, and the second belt pulley (40) is connected with the first belt pulley (30) through a belt (49);
the second short rod (41) is fixedly installed at the bottom end of the second belt pulley (40), and a hemispheroid (42) is fixedly installed at one end, close to the sleeve (39), of the second short rod (41);
the adjusting box (43) is fixedly arranged on the sleeve (39), and a third through hole (44) is formed in the adjusting box (43);
the through hole III (44) is communicated with the interior of the sleeve (39), and a one-way valve I (56) is further arranged on the inner wall of the through hole III (44);
the through hole IV (45) is arranged at the bottom end of the adjusting box (43);
the piston III (46) is connected to the inner wall of the adjusting box (43) in a sliding mode, one end of the piston III (46) is fixedly provided with a return spring I (47), and the other end of the piston III (46) is fixedly provided with a T-shaped rod I (48);
the other end of the first return spring (47) is fixedly arranged on the inner wall of the adjusting box (43), and the other end of the first T-shaped rod (48) is in contact with the hemispheroid (42);
the top end of the second T-shaped rod (50) is in contact with the first moving plate (25), and the bottom end of the second T-shaped rod (50) is connected to the inner wall of the sleeve (39) in a sliding mode;
the air release valve (59), the air release valve (59) is fixedly installed on the sleeve (39);
the first communication pipe (51), the sleeves (39) arranged at the left end and the right end of the first communication pipe (51) are communicated, and the first communication pipe (51) is further communicated with the T-shaped sleeve (31).
9. The purifier of a methanol catalytic reforming hydrogen production device as claimed in claim 7, wherein the second purification device (4) comprises:
the bottom end of the second box body (52) is fixedly arranged on the fixed seat (12), and the top end of the right side of the second box body (52) is fixedly provided with a third connecting pipe (13);
the left end and the right end of the fixing plate (68) are fixedly arranged on the inner walls of the left end and the right end of the second box body (52), and a stirring mechanism is arranged at the top end of the fixing plate (68);
the rabbling mechanism includes:
a driving box (71), wherein the driving box (71) is arranged at the middle end of the fixing plate (68);
the top end of the connecting plate (54) is fixedly mounted on the inner wall of the second box body (52), the bottom end of the connecting plate (54) is fixedly mounted on the driving box (71), the left end and the right end of the connecting plate (54) are respectively provided with a second cavity (69) and a third cavity (74), and the third cavity (74) is connected with the third connecting pipe (13);
the motor III (72) is fixedly arranged in the driving box (71), and an output shaft of the motor III (72) is connected with the long rod II (73) through a belt assembly;
the middle end of the second long rod (73) is rotatably connected to the connecting plate (54), and the left end and the right end of the second long rod (73) are respectively arranged in the second cavity (69) and the third cavity (74);
the stirring blades (75) are fixedly arranged at the left end and the right end of the second long rod (73);
two ends of the communication pipe III (76) are respectively communicated with the cavity II (69) and the cavity III (74), and a check valve III (77) is fixedly installed in the communication pipe III (76); and a second reaction liquid (78) is arranged in the second cavity (69) and the third cavity (74).
10. The purifier of a methanol catalytic reforming hydrogen production device as claimed in claim 9, wherein the second purification device (4) further comprises: a gas flow control mechanism;
the gas flow control mechanism includes:
the gas adjusting bin (55) is arranged in the second cavity (69), and the bottom end of the gas adjusting bin (55) is fixedly installed at the top end of the left side of the fixing plate (68);
the second motor (57), the second motor (57) is fixed at the bottom end of the gas regulation bin (55), a threaded rod (58) is fixedly installed on an output shaft of the second motor (57), and the top end of the threaded rod (58) is rotatably connected to the inner wall of the gas regulation bin (55);
the plurality of through holes five (60), the through holes five (60) are arranged on the surface of the box body at the top end of the gas adjusting bin (55), and a check valve two (70) is fixedly arranged in the through holes five (60);
the six through holes (61) are formed in the surface of the box body on the left side of the gas adjusting bin (55), the six through holes (61) are connected with the second communicating pipe (53), and the other end of the third connecting pipe (13) is communicated with the second connecting pipe (6);
the first support rod (62) is arranged on the gas adjusting bin (55) close to the position of the six through holes (61), a rotating shaft at one end of the first support rod (62) is connected to the gas adjusting bin (55), and the other end of the first support rod (62) is clamped on the gas adjusting bin (55);
one end of the second return spring (63) is fixedly arranged on the first support rod (62), and the other end of the second return spring (63) is fixedly arranged on the gas adjusting bin (55);
a second moving plate (64), wherein the left end and the right end of the second moving plate (64) are respectively connected to the inner wall of the gas adjusting bin (55) in a sliding mode, and the second moving plate (64) is in threaded connection with the threaded rod (58);
the through holes seven (65) are symmetrically formed in the moving plate II (64) at the left end and the right end of the threaded rod (58);
one end of each second support rod (66) is connected to the second moving plate (64) in a rotating mode, and the other end of each second support rod (66) is clamped on the second moving plate (64);
and one end of the third return spring (67) is fixedly arranged on the second support rod (66), and the other end of the third return spring (67) is fixedly arranged on the second moving plate (64).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210230970.5A CN114713009A (en) | 2022-03-10 | 2022-03-10 | Purifier of methanol catalytic reforming hydrogen production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210230970.5A CN114713009A (en) | 2022-03-10 | 2022-03-10 | Purifier of methanol catalytic reforming hydrogen production device |
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| Publication Number | Publication Date |
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| CN114713009A true CN114713009A (en) | 2022-07-08 |
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| CN202210230970.5A Pending CN114713009A (en) | 2022-03-10 | 2022-03-10 | Purifier of methanol catalytic reforming hydrogen production device |
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| US20170183226A1 (en) * | 2015-06-05 | 2017-06-29 | Guangdong Hydrogen Energy Science And Te | Residual gas heat exchange combustion-supporting system based on methanol-water mixture reforming hydrogen production system, and method thereof |
| CN108302245A (en) * | 2018-04-11 | 2018-07-20 | 马鞍山启元自动化技术有限责任公司 | A kind of temperature controlled operated pneumatic valve and its control method |
| CN110479073A (en) * | 2019-09-06 | 2019-11-22 | 西安交通大学医学院第一附属医院 | It anaesthetizes department and extracts device with waste gas of anesthesia |
| CN210045066U (en) * | 2019-03-12 | 2020-02-11 | 河南聚力联创环保科技有限公司 | High-efficient purifier of flue gas |
| CN111908574A (en) * | 2020-07-09 | 2020-11-10 | 深圳市飞龙云商贸有限公司 | Sedimentation tank with air purification function |
| CN112648388A (en) * | 2020-12-17 | 2021-04-13 | 利晟（杭州）科技有限公司 | A valve structure in biological deodorization case for flue gas is handled |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US4553981A (en) * | 1984-02-07 | 1985-11-19 | Union Carbide Corporation | Enhanced hydrogen recovery from effluent gas streams |
| CN1829656A (en) * | 2003-07-28 | 2006-09-06 | 犹德有限公司 | Method for extracting hydrogen from a gas containing methane, especially natural gas and system for carrying out said method |
| US20170183226A1 (en) * | 2015-06-05 | 2017-06-29 | Guangdong Hydrogen Energy Science And Te | Residual gas heat exchange combustion-supporting system based on methanol-water mixture reforming hydrogen production system, and method thereof |
| CN108302245A (en) * | 2018-04-11 | 2018-07-20 | 马鞍山启元自动化技术有限责任公司 | A kind of temperature controlled operated pneumatic valve and its control method |
| CN210045066U (en) * | 2019-03-12 | 2020-02-11 | 河南聚力联创环保科技有限公司 | High-efficient purifier of flue gas |
| CN110479073A (en) * | 2019-09-06 | 2019-11-22 | 西安交通大学医学院第一附属医院 | It anaesthetizes department and extracts device with waste gas of anesthesia |
| CN111908574A (en) * | 2020-07-09 | 2020-11-10 | 深圳市飞龙云商贸有限公司 | Sedimentation tank with air purification function |
| CN112648388A (en) * | 2020-12-17 | 2021-04-13 | 利晟（杭州）科技有限公司 | A valve structure in biological deodorization case for flue gas is handled |
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Application publication date: 20220708 |