CN115183146A - Natural gas adsorption tank body heat exchange system - Google Patents
Natural gas adsorption tank body heat exchange system Download PDFInfo
- Publication number
- CN115183146A CN115183146A CN202210893154.2A CN202210893154A CN115183146A CN 115183146 A CN115183146 A CN 115183146A CN 202210893154 A CN202210893154 A CN 202210893154A CN 115183146 A CN115183146 A CN 115183146A
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- China
- Prior art keywords
- heat exchange
- adsorption tank
- fixedly connected
- liquid inlet
- liquid
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Links
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 70
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 239000003345 natural gas Substances 0.000 title claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 89
- 230000008859 change Effects 0.000 abstract description 2
- 239000013589 supplement Substances 0.000 abstract description 2
- 230000009471 action Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007105 physical stamina Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C3/00—Vessels not under pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/28—Strainers not provided for elsewhere
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/08—Tubular elements crimped or corrugated in longitudinal section
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/01—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using means for separating solid materials from heat-exchange fluids, e.g. filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0352—Pipes
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Geometry (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
A heat exchange system of a natural gas adsorption tank body belongs to the field of natural gas adsorption equipment. Comprises an adsorption device and a circulating device; a heat exchange tube is arranged between the adsorption tank inner shell and the adsorption tank outer shell, and a liquid outlet and a liquid inlet of the heat exchange tube penetrate through the adsorption tank outer shell; the liquid inlet end of the heat exchange tube is fixedly connected with a pump body, the other end of the pump body is fixedly connected with a liquid inlet tube, and the liquid outlets of the liquid inlet tube and the heat exchange tube are arranged in the circulating device; the heat exchange tube is located the part of adsorption tank inner shell, between the adsorption tank shell and is wavy, and the spiral setting is in the outside of adsorption tank inner shell, is equipped with a plurality of spiral arrangement's limiting plate on the inner wall of heat exchange tube. The invention not only can automatically supplement liquid, but also can filter the supplemented liquid, thereby avoiding blockage caused by a large amount of sundries being blocked in the heat exchange tube; the invention can also change the running state of the liquid in the heat exchange tube, so that the liquid in the heat exchange tube can be uniformly heated.
Description
Technical Field
The invention relates to a heat exchange system of a natural gas adsorption tank body, and belongs to the field of natural gas adsorption equipment.
Background
In the gas adsorption process, can outwards release heat, lead to the temperature to rise, consequently store the ability heat through heat exchange system, but present heat exchange system in the use, the liquid evaporation after the temperature rise can appear, lead to liquid total volume to reduce to liquid in the heat exchange tube on the market at present steadily flows all the time, leads to only partial liquid physical stamina and the inner wall contact of adsorption tanks, and heat conductivility reduces.
Disclosure of Invention
The present invention is directed to solving the above problems in the background art, and provides a heat exchange system for a natural gas adsorption tank.
The invention achieves the purpose, and adopts the following technical scheme:
a heat exchange system of a natural gas adsorption tank body comprises an adsorption device and a circulation device; the adsorption device comprises an adsorption tank inner shell, a heat exchange pipe, a liquid outlet, a liquid inlet, a pump body, a liquid inlet pipe and an adsorption tank outer shell; a heat exchange tube is arranged between the adsorption tank inner shell and the adsorption tank outer shell, and a liquid outlet and a liquid inlet of the heat exchange tube penetrate through the adsorption tank outer shell; the liquid inlet end of the heat exchange tube is fixedly connected with a pump body, the other end of the pump body is fixedly connected with a liquid inlet tube, and the liquid inlet tube and the liquid outlet of the heat exchange tube are arranged in the circulating device; the heat exchange tube is located the part of adsorption tank inner shell, between the adsorption tank shell and is wavy, and the spiral setting is in the outside of adsorption tank inner shell, is equipped with a plurality of spiral arrangement's limiting plate on the inner wall of heat exchange tube.
Compared with the prior art, the invention has the beneficial effects that: the invention not only can automatically supplement liquid, but also can filter the supplemented liquid, thereby avoiding blockage caused by a large amount of sundries being blocked in the heat exchange tube; the invention can also change the running state of the liquid in the heat exchange tube, so that the liquid in the heat exchange tube can be uniformly heated.
Drawings
FIG. 1 is a front view of a natural gas adsorption tank heat exchange system of the present invention;
FIG. 2 is an adsorption unit of a heat exchange system of a natural gas adsorption tank of the present invention;
FIG. 3 isbase:Sub>A cross-sectional view taken along line A-A of FIG. 2;
FIG. 4 is an enlarged schematic view of B of FIG. 2;
FIG. 5 is a cross-sectional top view of the position of the external cartridge of a natural gas adsorption canister heat exchange system of the present invention;
FIG. 6 is a cross-sectional view of a heat exchange tube of a natural gas adsorption tank heat exchange system of the present invention;
FIG. 7 is a front view of a cycle device of a natural gas adsorption tank heat exchange system of the present invention;
FIG. 8 is a top view of a conical plate of a natural gas adsorption tank heat exchange system of the present invention;
fig. 9 is a top view of the slide bars, conical filter plates and collection troughs of a heat exchange system for a natural gas adsorber tank of the invention.
Detailed Description
The technical solutions in the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the invention, rather than all embodiments, and all other embodiments obtained by those skilled in the art without any creative work based on the embodiments of the present invention belong to the protection scope of the present invention.
The first specific implementation way is as follows: as shown in fig. 1 to 9, the present embodiment describes a heat exchange system for a natural gas adsorption tank, which includes an adsorption apparatus 1 and a circulation apparatus 2; the adsorption device 1 comprises an adsorption tank inner shell 11, a heat exchange tube 16, a liquid outlet 12, a liquid inlet 13, a pump body 14, a liquid inlet tube 15 and an adsorption tank outer shell 115; a heat exchange tube 16 is arranged between the adsorption tank inner shell 11 and the adsorption tank outer shell 115, and a liquid outlet 12 and a liquid inlet 13 of the heat exchange tube 16 penetrate through the adsorption tank outer shell 115; a pump body 14 is fixedly connected with a liquid inlet 13 end of the heat exchange tube 16, a liquid inlet tube 15 is fixedly connected with the other end of the pump body 14, and the liquid inlet tube 15 and a liquid outlet 12 of the heat exchange tube 16 are arranged in the circulating device 2; the part of the heat exchange tube 16 between the adsorption tank inner shell 11 and the adsorption tank outer shell 115 is wavy, the heat exchange tube is spirally arranged outside the adsorption tank inner shell 11, and the inner wall of the heat exchange tube 16 is provided with a plurality of limiting plates 161 which are spirally arranged.
The second embodiment is as follows: as shown in fig. 1 to 9, the present embodiment is further described with respect to the first embodiment, and the circulation device 2 includes a storage barrel 23; a through hole I24 and a through hole II 26 are arranged on the side surface of the storage barrel 23; the liquid outlet 12 end of the heat exchange tube 16 is fixedly connected in the perforation II 26, and the liquid inlet tube 15 is fixedly connected in the perforation I24.
The third concrete implementation mode: as shown in fig. 1-9, the present embodiment further illustrates the first embodiment, the liquid inlet pipe 15 is L-shaped, a through hole 17 is formed on the upper end surface of the bent portion of the L-shaped liquid inlet pipe 15, and the vertical end of the L-shaped liquid inlet pipe 15 passes through a through hole iii 25 at the bottom end of the storage barrel 23; the bottom end of the storage barrel 23 is fixedly connected with a supporting rod 22; the lower end of the supporting rod 22 is fixedly connected to the top end of the interior of the collecting barrel 21.
The fourth concrete implementation mode: as shown in fig. 1-9, the present embodiment is further described with respect to the first embodiment, wherein the inner diameter of the collection barrel 21 is larger than the outer diameter of the storage barrel 23.
The fifth concrete implementation mode: as shown in fig. 1 to 9, this embodiment is further described with respect to the first embodiment, and the adsorption device 1 further includes a stopper 18, a sliding baffle 19, an external cylinder 110, a connecting rod 111, a connecting pipe 112, a limiting ring 113, and a spring 114; a connecting rod 111 is fixedly connected to the bottom surface of the vertical end of the liquid inlet pipe 15, a connecting pipe 112 is fixedly connected to the lower end of the connecting rod 111, and a stop block 18 is fixedly connected to the inner wall of the vertical end of the liquid inlet pipe 15; two ends of the external cylinder 110 are respectively and fixedly connected to the liquid inlet pipe 15 and the connecting pipe 112, and the inner diameter of the external cylinder 110 is larger than the outer diameters of the liquid inlet pipe 15 and the connecting pipe 112; the limiting ring 113 is fixedly connected to the inner wall of the connecting pipe 112, one end of the spring 114 is fixedly connected to the upper end of the limiting ring 113, the other end of the spring 114 is fixedly connected to the lower end of the sliding baffle 19, the sliding baffle 19 is arranged at the lower end of the stop block 18, and the sliding baffle 19 is in sliding fit with the inner wall of the vertical end of the liquid inlet pipe 15.
The sixth specific implementation mode: as shown in fig. 1 to 9, this embodiment is further described as the first embodiment, and the thickness of the slide damper 19 is smaller than the height of the connecting rod 111.
The seventh embodiment: as shown in fig. 1 to 9, the embodiment is further described as the first embodiment, the circulating device 2 further comprises a fixing rod 27, a sliding rod 212 and a conical floating block 28; the fixing rod 27 is fixedly connected to the inner wall of the storage barrel 23, and a circular hole is formed in the fixing rod 27; the sliding rod 212 is in sliding fit with the round hole, and the lower end of the sliding rod 212 is fixedly connected with the conical floating block 28 floating on the liquid level.
The specific implementation mode is eight: as shown in fig. 1-9, this embodiment is further described with respect to the first embodiment, when the conical float 28 moves to the lowest point along with the liquid surface, the conical float 28 is inserted into the through hole 17, and the through hole 17 is sealed.
The specific implementation method nine: as shown in fig. 1-9, which further illustrate the first embodiment, the circulation device 2 further includes a conical plate 29, a conical filter plate 210, and a collection tank 211; the conical plate 29 is fixedly connected to the inner wall of the storage barrel 23, the conical plate 29 is positioned below the through hole II 26, and a hole is formed in the center of the conical plate 29; the outer circular surface of the slide bar 212 is fixedly connected with a conical filter plate 210, the lower end of the conical filter plate 210 is fixedly connected with a collecting groove 211, the collecting groove 211 is annular, and the outer diameter of the collecting groove 211 is equal to the aperture of the central hole of the conical plate 29.
The detailed implementation mode is ten: as shown in fig. 1-9, this embodiment is further described with respect to the first embodiment, when the conical floating block 28 moves to the lowest point, the upper end surface of the collecting groove 211 moves to the lowest point of the inner side surface of the conical plate 29.
The working principle of the invention is as follows: when the device is used, the pump body 14 is started, the pump body 14 pumps liquid in the storage barrel 23 into the heat exchange tube 16 through the through hole 17 in the liquid inlet tube 15, and the heat exchange tube 16 is wavy, so that when the liquid moves from a position far away from the adsorption tank inner shell 11 to a position close to the adsorption tank inner shell 11, as the radian of the position close to the adsorption tank inner shell 11 is larger than that of the position far away from the adsorption tank inner shell 11, when the liquid passes through a position with a large radian, the impact force of the liquid on the inner wall of the heat exchange tube 16 is increased, further more heat can be taken away, the heat exchange efficiency is increased, meanwhile, a plurality of spiral limiting plates 161 are arranged on the inner wall of the heat exchange tube 16, and therefore, the liquid can rotate under the action of the limiting plates 161 in the liquid flowing process, and the liquid can be uniformly heated;
when the liquid volume in the storage barrel 23 is reduced due to evaporation of the liquid, the conical floating block 28 moves downwards along with the liquid level, so as to drive the sliding rod 212 to move downwards, when the liquid level is lowered to the lowest point, the conical floating block 28 moves into the through hole 17 to block the through hole 17, and after the conical floating block 28 moves into the through hole 17, the buoyancy is reduced due to the reduction of the liquid level height, so that the conical floating block 28 moves downwards under the action of gravity, pushes the sliding baffle 19 to move downwards, compresses the spring 114, and after the sliding baffle 19 moves to the position of the external cylinder 110, the conical floating block 28 is limited by the through hole 17 and cannot move downwards, at this time, the pump body 14 pumps the liquid into the heat exchange tube 16 through the connecting tube 112, the external cylinder 110 and the liquid inlet tube 15, and flows into the storage barrel 23 after circulation, and when the liquid volume in the storage barrel 23 is increased, the conical floating block 28 moves upwards under the buoyancy to be separated from the through hole 17, and the sliding baffle 19 moves upwards to the original position under the action of elasticity, so as to separate the liquid inlet tube 15 from the connecting tube 112, and the liquid column is always stored in the negative pressure;
when the sliding rod 212 moves downwards, the conical filter plate 210 and the collecting tank 211 also move downwards, after the conical floating block 28 moves to the lowest point, the collecting tank 211 moves to the lowest point of the inner side surface of the conical plate 29, after the liquid flows out of the liquid outlet 12 for a circle in a circulating manner, the liquid directly washes the conical filter screen 210, the foreign matters are retained and slide into the collecting tank 211, and the foreign matters are prevented from being clamped in the heat exchange tube 16 due to repeated circulation of the foreign matters, so that the heat exchange efficiency is influenced;
the inner diameter of the collecting barrel 21 is larger than the diameter of the storage barrel 23, so that water drops formed by condensation of steam contacting the outer side wall of the storage barrel 23 can drop into the collecting barrel 21 when the water drops slide down under the action of gravity, and resources are saved.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present specification describes embodiments, not every embodiment includes only a single embodiment, and such description is for clarity purposes only, and it is to be understood that all embodiments may be combined as appropriate by one of ordinary skill in the art to form other embodiments as will be apparent to those of skill in the art from the description herein.
Claims (10)
1. The utility model provides a natural gas adsorbs a jar body heat exchange system which characterized in that: comprises an adsorption device (1) and a circulating device (2); the adsorption device (1) comprises an adsorption tank inner shell (11), a heat exchange pipe (16), a liquid outlet (12), a liquid inlet (13), a pump body (14), a liquid inlet pipe (15) and an adsorption tank outer shell (115); a heat exchange tube (16) is arranged between the adsorption tank inner shell (11) and the adsorption tank outer shell (115), and a liquid outlet (12) and a liquid inlet (13) of the heat exchange tube (16) penetrate through the adsorption tank outer shell (115); a pump body (14) is fixedly connected with a liquid inlet (13) of the heat exchange tube (16), a liquid inlet tube (15) is fixedly connected with the other end of the pump body (14), and the liquid inlet tube (15) and a liquid outlet (12) of the heat exchange tube (16) are arranged in the circulating device (2); the heat exchange tube (16) is located the part wavy between adsorption tank inner shell (11), adsorption tank outer shell (115), and the spiral setting is in the outside of adsorption tank inner shell (11), is equipped with a plurality of spiral arrangement's limiting plate (161) on the inner wall of heat exchange tube (16).
2. The natural gas adsorption tank heat exchange system of claim 1, wherein: the circulation device (2) comprises a storage tub (23); a perforation I (24) and a perforation II (26) are arranged on the side surface of the storage barrel (23); the liquid outlet (12) end of the heat exchange tube (16) is fixedly connected in the perforation II (26), and the liquid inlet tube (15) is fixedly connected in the perforation I (24).
3. The natural gas adsorption tank heat exchange system of claim 2, wherein: the liquid inlet pipe (15) is L-shaped, a through hole (17) is formed in the upper end face of the bent part of the L-shaped liquid inlet pipe (15), and the vertical end of the L-shaped liquid inlet pipe (15) penetrates through a through hole III (25) in the bottom end of the storage barrel (23); the bottom end of the storage barrel (23) is fixedly connected with a supporting rod (22); the lower end of the supporting rod (22) is fixedly connected to the top end of the inner part of the collecting barrel (21).
4. The natural gas adsorption tank heat exchange system of claim 3, wherein: the inner diameter of the collecting barrel (21) is larger than the outer diameter of the storage barrel (23).
5. The natural gas adsorption tank heat exchange system of claim 4, wherein: the adsorption device (1) further comprises a stop block (18), a sliding baffle (19), an external cylinder (110), a connecting rod (111), a connecting pipe (112), a limiting ring (113) and a spring (114); the bottom surface of the vertical end of the liquid inlet pipe (15) is fixedly connected with a connecting rod (111), the lower end of the connecting rod (111) is fixedly connected with a connecting pipe (112), and the inner wall of the vertical end of the liquid inlet pipe (15) is fixedly connected with a stop block (18); two ends of the external cylinder (110) are respectively and fixedly connected to the liquid inlet pipe (15) and the connecting pipe (112), and the inner diameter of the external cylinder (110) is larger than the outer diameters of the liquid inlet pipe (15) and the connecting pipe (112); spacing ring (113) fixed connection is on the inner wall of connecting pipe (112), the one end fixed connection of spring (114) is in the upper end of spacing ring (113), and the other end fixed connection of spring (114) is at the lower extreme of slide damper (19), and slide damper (19) set up the lower extreme at dog (18), and slide damper (19) and the inner wall sliding fit of the vertical end of feed liquor pipe (15).
6. The natural gas adsorption tank heat exchange system of claim 5, wherein: the thickness of the sliding baffle (19) is smaller than the height of the connecting rod (111).
7. The natural gas adsorption tank heat exchange system of claim 6, wherein: the circulating device (2) further comprises a fixed rod (27), a sliding rod (212) and a conical floating block (28); the fixing rod (27) is fixedly connected to the inner wall of the storage barrel (23), and a circular hole is formed in the fixing rod (27); the sliding rod (212) is in sliding fit with the round hole, and the lower end of the sliding rod (212) is fixedly connected with a conical floating block (28) floating on the liquid level.
8. The natural gas adsorption tank heat exchange system of claim 7, wherein: when the conical floating block (28) moves to the lowest point along with the liquid level, the conical floating block (28) is inserted into the through hole (17) and seals the through hole (17).
9. The natural gas adsorption tank heat exchange system of claim 8, wherein: the circulating device (2) further comprises a conical plate (29), a conical filter plate (210) and a collecting tank (211); the conical plate (29) is fixedly connected to the inner wall of the storage barrel (23), the conical plate (29) is positioned below the perforation II (26), and a hole is formed in the center of the conical plate (29); the outer disc of slide bar (212) is gone up fixedly connected with toper filter plate (210), and the lower extreme fixedly connected with collecting vat (211) of toper filter plate (210), and collecting vat (211) are the annular, and the external diameter of collecting vat (211) equals with the aperture of toper board (29) centre bore.
10. The natural gas adsorption tank heat exchange system of claim 9, wherein: when the conical floating block (28) moves to the lowest point, the upper end surface of the collecting tank (211) moves to the lowest point of the inner side surface of the conical plate (29).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210893154.2A CN115183146B (en) | 2022-07-27 | 2022-07-27 | Natural gas adsorption tank body heat exchange system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210893154.2A CN115183146B (en) | 2022-07-27 | 2022-07-27 | Natural gas adsorption tank body heat exchange system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN115183146A true CN115183146A (en) | 2022-10-14 |
| CN115183146B CN115183146B (en) | 2023-10-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210893154.2A Active CN115183146B (en) | 2022-07-27 | 2022-07-27 | Natural gas adsorption tank body heat exchange system |
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| CN (1) | CN115183146B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101832466A (en) * | 2009-03-13 | 2010-09-15 | 中国国际海运集装箱(集团)股份有限公司 | Limited charging device, low-temperature liquid container and limited charging method |
| CN204300688U (en) * | 2014-10-29 | 2015-04-29 | 郑州朗润石油设备有限公司 | LNG immersed pump pump pit level control system |
| CN209054327U (en) * | 2018-11-09 | 2019-07-02 | 云南省能源研究院有限公司 | A kind of novel Hydrogen Energy storage device |
| CN214369284U (en) * | 2020-12-16 | 2021-10-08 | 淄博安泽特种气体有限公司 | Metal hydride hydrogen storage tank |
| CN216537714U (en) * | 2021-11-12 | 2022-05-17 | 辽宁北方化学工业有限公司 | Recovery unit of VOCs in production of ethanediol |
-
2022
- 2022-07-27 CN CN202210893154.2A patent/CN115183146B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101832466A (en) * | 2009-03-13 | 2010-09-15 | 中国国际海运集装箱(集团)股份有限公司 | Limited charging device, low-temperature liquid container and limited charging method |
| CN204300688U (en) * | 2014-10-29 | 2015-04-29 | 郑州朗润石油设备有限公司 | LNG immersed pump pump pit level control system |
| CN209054327U (en) * | 2018-11-09 | 2019-07-02 | 云南省能源研究院有限公司 | A kind of novel Hydrogen Energy storage device |
| CN214369284U (en) * | 2020-12-16 | 2021-10-08 | 淄博安泽特种气体有限公司 | Metal hydride hydrogen storage tank |
| CN216537714U (en) * | 2021-11-12 | 2022-05-17 | 辽宁北方化学工业有限公司 | Recovery unit of VOCs in production of ethanediol |
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| Publication number | Publication date |
|---|---|
| CN115183146B (en) | 2023-10-24 |
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