CN202246887U - Movable large hydrogen production system device - Google Patents
Movable large hydrogen production system device Download PDFInfo
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- CN202246887U CN202246887U CN2011203452765U CN201120345276U CN202246887U CN 202246887 U CN202246887 U CN 202246887U CN 2011203452765 U CN2011203452765 U CN 2011203452765U CN 201120345276 U CN201120345276 U CN 201120345276U CN 202246887 U CN202246887 U CN 202246887U
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- Prior art keywords
- hydrogen
- cooling
- generating system
- system device
- separate
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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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model discloses a movable large hydrogen production system device of the field of chemical machinery, which comprises a container and hydrogen production equipment arranged in the container. The movable large hydrogen production system device adopts a movable box-type rectifier transformer (rectification cabinet), an integrated water electrolysis oxygen hydrogen separation and cooling dealkalization device and a special arrangement method, thereby greatly reducing space for equipment, enabling the hydrogen production system to be capable of being arranged in the container and achieving integrated and movable effects of large hydrogen production equipment.
Description
Technical field
The utility model relates to chemical machinery field, relates in particular to a kind of portable large-scale hydrogen generating system device that is mainly used in fields such as electric power, electronics, metallurgy, iron and steel, polysilicon, chemical industry, new forms of energy.
Background technology
It is existing that large-scale (per hour hydrogen output is greater than 50m
3) hydrogen producer, because volume is big, Heavy Weight and produce inflammable and explosive hydrogen, normally be fixedly mounted on indoorly, the house need be provided with corresponding anti-explosion fire measure, and keeps certain fire safety distance with other building.But along with the expansion in hydrogen applications field, provisional hydrogen user demand is more and more, and, the nonvolatil fixed buildings of the suitable construction in many places, therefore, more and more to the large-scale hydrogen producer device demand of movable type.
The utility model content
It is a kind of in limited mobile space that the purpose of the utility model is to provide, and solves the layout of large-scale hydrogen producer, the large-scale hydrogen generating system device of design production integration.
To achieve these goals, the technical scheme of the utility model employing is following:
The portable large-scale hydrogen generating system device of the utility model comprises freight container and the hydrogen producer that is arranged in this freight container.
Preferably; Described hydrogen producer adopts integrated hydro-electrolytic hydroxide to separate and cooling dealkalize device; Described integrated hydro-electrolytic hydroxide separate with cooling dealkalize device by one be used for hydrogen simultaneously, the isolating pressurized vessel of oxygen is formed; Said pressurized vessel is divided into two separate chambers through a baffle plate, is respectively hydrogen separation chamber, oxygen separation chamber, on the said baffle plate, be provided with the hole that connects two separate chambers under the electrolytic solution liquid level.
Preferably, the top in said two separate chambers is respectively arranged with refrigerating unit, and the pneumatic outlet on said hydrogen separation chamber, the oxygen separation chamber is arranged on the top of said pressurized vessel, the said refrigerating unit.
Preferably, described refrigerating unit adopts double-deck cooling structure, and is horizontally set at the top of said two separate chambers.
Preferably; Housing in the described hydrogen producer, power distribution cabinet, rectifier cabinet are arranged at an end of described freight container, and the electrolyzer group in the said hydrogen producer, NaOH solution circulating pump, alkali solution cooler, alkali lye strainer, said integrated hydro-electrolytic hydroxide separate with the arrangement mode of cooling dealkalize device, hydrogen water separator, drying tower, regeneration cooling tower, hydrogen cooler condenser, lye tank, small pump, water softening device following:
Described electrolyzer group, alkali lye strainer, integrated hydro-electrolytic hydroxide separate with cooling dealkalize device, hydrogen water separator, drying tower, regeneration cooling tower, lye tank, water softening device laterally arranges successively side by side; Described NaOH solution circulating pump, alkali solution cooler lay respectively at the both sides longitudinally of said electrolyzer group; The adjacent described integrated hydro-electrolytic hydroxide of said hydrogen water separator separates and the setting of cooling dealkalize device; Said hydrogen cooler condenser is arranged on a side longitudinally of said drying tower, and said small pump is arranged on a side longitudinally of said lye tank.
Preferably, described freight container is divided into watch-keeping cubicle and process for making hydrogen chamber.
Preferably; Said housing, power distribution cabinet, rectifier cabinet are arranged in the described watch-keeping cubicle, and said electrolyzer group, NaOH solution circulating pump, alkali solution cooler, alkali lye strainer, said integrated hydro-electrolytic hydroxide separate with cooling dealkalize device, hydrogen water separator, drying tower, regeneration cooling tower, hydrogen cooler condenser, lye tank, small pump, that water softening device is positioned at described process for making hydrogen is indoor.
The beneficial effect of the utility model is following:
The portable large-scale hydrogen generating system device of the utility model adopts portable box rectifier transformer (rectifier cabinet), incorporate hydro-electrolytic hydroxide to separate and cooling dealkalize device and special decoration form; The required space of equipment is dwindled greatly; Thereby make hydrogen generating system can be disposed in the freight container, realized integrated, the effect movably of large-scale hydrogen producer.
Description of drawings
Fig. 1 is the floor plan schematic top plan view of the portable large-scale hydrogen generating system device of the utility model;
Fig. 2 looks synoptic diagram for the floor plan master of the portable large-scale hydrogen generating system device of the utility model;
Fig. 3 is that the integrated hydro-electrolytic hydroxide in the utility model separates and an example structure synoptic diagram that cools off the dealkalize device;
Fig. 4 is the schematic side view of embodiment among Fig. 3.
Embodiment
Further describe below in conjunction with accompanying drawing and specific embodiment technical scheme and beneficial effect the utility model.
Be that hydrogen producer is provided with in the freight container 1 among the embodiment referring to the portable large-scale hydrogen generating system device shown in accompanying drawing 1, the accompanying drawing 2; Can adopt 40 chi freight containers in the actually operating; Freight container among this embodiment is divided into two portions; Watch-keeping cubicle 2 and process for making hydrogen chamber 3 also can adopt a chamber to realize certainly in other embodiment; Housing 4 in the hydrogen producer, power distribution cabinet 5, rectifier cabinet 6 are positioned at watch-keeping cubicle 2, and the electrolyzer group 8 in the hydrogen producer, NaOH solution circulating pump 7, alkali solution cooler 9, alkali lye strainer 10, integrated hydro-electrolytic hydroxide separate with the arrangement mode of cooling dealkalize device 11, hydrogen water separator 12, drying tower 13, regeneration cooling tower 15, hydrogen cooler condenser 14, lye tank 17, small pump 16, water softening device 18 following:
Integrated hydro-electrolytic hydroxide in the utility model separates some embodiment with cooling dealkalize device; Referring to accompanying drawing 3; Be made up of a pressurized vessel 19, this pressurized vessel 1 is divided into two separate chambers by baffle plate 2, respectively as oxygen separation chamber, hydrogen separation chamber; Be provided with a hole that is communicated with two separate chambers in the bottom of baffle plate 20, this hole is under electrolyte level.Top in two separate chambers is respectively arranged with refrigerating unit, and this refrigerating unit adopts refrigerating unit 22 among the embodiment as shown in the figure; The pneumatic outlet e of two separate chambers, f are separately positioned on the top of pressurized vessel 19, on refrigerating unit 22; Also be provided with alkali lye outlet i, balance port j in the pressurized vessel bottom, the cooling water inlet b of refrigerating unit, d are lower than cooling water outlet g, h, and the oxygen, the hydrogen that like this electrolysis are gone out better cool off.
The device of the utility model in use, pressurized vessel 19 is fixing through the support 21 that is fixed on the bottom, injects electrolytic solution from electrolyte entrance a, c respectively then; In the electrolytic process, the oxygen that electrolysis goes out respectively in the oxygen separation chamber, hydrogen separation chamber assembles, when hydrogen and oxygen during through apparatus for supercooling 22; The moisture that wherein carries is running into refrigerating unit 22, can meet condensation and form water droplet, is dropped in the electrolytic solution of bottom, separate chamber; Thereby reach the moisture in separating hydrogen gas and the oxygen; Reach the purpose of removing alkali, simultaneously, hydrogen and oxygen have also obtained cooling.
The portable large-scale hydrogen generating system device of the utility model changes the X-former of hydrogen generating system into can move separately cabinet type rectifier transformer by common rectifier transformer, and promptly rectifier cabinet may be moved into system and is possible.The freight container that adopts in the utility model need satisfy in the hydrogen generating system about explosion-proof, prevent fires, be incubated, start shipment, each item requirement such as equipment installation and checkout (EIC).Changed the size and the decoration form of the pressurized vessel in the hydrogen generating system in the utility model, the total system volume has been reduced and be easy to and in freight container, install, overhaul.This device interior the hydrogen-oxygen tripping device, volume is little, separation efficiency is high.The purpose that not only can reach cooling gas can also further be cleaned alkali lye, has reached the purpose of multi-use.Tightly do not saved the manufacturing expense of other containers like this, saved the space yet to whole plant.
Claims (7)
1. portable large-scale hydrogen generating system device is characterized in that, comprises freight container and the hydrogen producer that is arranged in this freight container.
2. the large-scale hydrogen generating system device of movable type according to claim 1; It is characterized in that; Described hydrogen producer adopts integrated hydro-electrolytic hydroxide to separate and cooling dealkalize device; Described integrated hydro-electrolytic hydroxide separate with cooling dealkalize device by one be used for hydrogen simultaneously, the isolating pressurized vessel of oxygen is formed; Said pressurized vessel is divided into two separate chambers through a baffle plate, is respectively hydrogen separation chamber, oxygen separation chamber, on the said baffle plate, be provided with the hole that connects two separate chambers under the electrolytic solution liquid level.
3. the large-scale hydrogen generating system device of movable type according to claim 2; It is characterized in that; Top in said two separate chambers is respectively arranged with refrigerating unit, and the pneumatic outlet on said hydrogen separation chamber, the oxygen separation chamber is arranged on the top of said pressurized vessel, the said refrigerating unit.
4. the large-scale hydrogen generating system device of movable type according to claim 3 is characterized in that described refrigerating unit adopts double-deck cooling structure, and is horizontally set at the top of said two separate chambers.
5. according to the large-scale hydrogen generating system device of the arbitrary described movable type of claim 2 to 4; It is characterized in that; Housing in the described hydrogen producer, power distribution cabinet, rectifier cabinet are arranged at an end of described freight container, and the electrolyzer group in the said hydrogen producer, NaOH solution circulating pump, alkali solution cooler, alkali lye strainer, said integrated hydro-electrolytic hydroxide separate with the arrangement mode of cooling dealkalize device, hydrogen water separator, drying tower, regeneration cooling tower, hydrogen cooler condenser, lye tank, small pump, water softening device following:
Described electrolyzer group, alkali lye strainer, integrated hydro-electrolytic hydroxide separate with cooling dealkalize device, hydrogen water separator, drying tower, regeneration cooling tower, lye tank, water softening device laterally arranges successively side by side; Described NaOH solution circulating pump, alkali solution cooler lay respectively at the both sides longitudinally of said electrolyzer group; The adjacent described integrated hydro-electrolytic hydroxide of said hydrogen water separator separates and the setting of cooling dealkalize device; Said hydrogen cooler condenser is arranged on a side longitudinally of said drying tower, and said small pump is arranged on a side longitudinally of said lye tank.
6. the large-scale hydrogen generating system device of movable type according to claim 5 is characterized in that described freight container is divided into watch-keeping cubicle and process for making hydrogen chamber.
7. the large-scale hydrogen generating system device of movable type according to claim 6; It is characterized in that; Said housing, power distribution cabinet, rectifier cabinet are arranged in the described watch-keeping cubicle, and said electrolyzer group, NaOH solution circulating pump, alkali solution cooler, alkali lye strainer, said integrated hydro-electrolytic hydroxide separate with cooling dealkalize device, hydrogen water separator, drying tower, regeneration cooling tower, hydrogen cooler condenser, lye tank, small pump, that water softening device is positioned at described process for making hydrogen is indoor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203452765U CN202246887U (en) | 2011-09-15 | 2011-09-15 | Movable large hydrogen production system device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203452765U CN202246887U (en) | 2011-09-15 | 2011-09-15 | Movable large hydrogen production system device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202246887U true CN202246887U (en) | 2012-05-30 |
Family
ID=46108157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203452765U Expired - Lifetime CN202246887U (en) | 2011-09-15 | 2011-09-15 | Movable large hydrogen production system device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202246887U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104062986A (en) * | 2014-07-16 | 2014-09-24 | 山东中实易通集团有限公司 | Hydrogen generation station liquid level ratio control system and method |
| CN108358163A (en) * | 2018-03-30 | 2018-08-03 | 苏州市彩衣真空镀膜有限公司 | A kind of container-type hydrogen generating system |
| CN110656342A (en) * | 2019-11-01 | 2020-01-07 | 南通安思卓新能源有限公司 | Capsule type movable water electrolysis hydrogen production device |
| CN111118525A (en) * | 2020-02-16 | 2020-05-08 | 中科院大连化学物理研究所张家港产业技术研究院有限公司 | Electrolytic tank suitable for pressurizing circulating pump shell and working method thereof |
| CN114411171A (en) * | 2022-02-23 | 2022-04-29 | 阳光氢能科技有限公司 | Hydrogen production system |
| CN117364113A (en) * | 2023-11-02 | 2024-01-09 | 江苏复源芥子空间新材料研究院有限公司 | Water electrolysis type hydrogen manufacturing system |
-
2011
- 2011-09-15 CN CN2011203452765U patent/CN202246887U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104062986A (en) * | 2014-07-16 | 2014-09-24 | 山东中实易通集团有限公司 | Hydrogen generation station liquid level ratio control system and method |
| CN108358163A (en) * | 2018-03-30 | 2018-08-03 | 苏州市彩衣真空镀膜有限公司 | A kind of container-type hydrogen generating system |
| CN110656342A (en) * | 2019-11-01 | 2020-01-07 | 南通安思卓新能源有限公司 | Capsule type movable water electrolysis hydrogen production device |
| CN111118525A (en) * | 2020-02-16 | 2020-05-08 | 中科院大连化学物理研究所张家港产业技术研究院有限公司 | Electrolytic tank suitable for pressurizing circulating pump shell and working method thereof |
| CN111118525B (en) * | 2020-02-16 | 2023-08-15 | 扬州乐道能源科技有限公司 | Electrolytic tank suitable for pressurizing circulating pump shell and working method thereof |
| CN114411171A (en) * | 2022-02-23 | 2022-04-29 | 阳光氢能科技有限公司 | Hydrogen production system |
| CN117364113A (en) * | 2023-11-02 | 2024-01-09 | 江苏复源芥子空间新材料研究院有限公司 | Water electrolysis type hydrogen manufacturing system |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120530 |