CN203787511U - Novel hydrogen-oxygen pile system - Google Patents
Novel hydrogen-oxygen pile system Download PDFInfo
- Publication number
- CN203787511U CN203787511U CN201420095008.6U CN201420095008U CN203787511U CN 203787511 U CN203787511 U CN 203787511U CN 201420095008 U CN201420095008 U CN 201420095008U CN 203787511 U CN203787511 U CN 203787511U
- Authority
- CN
- China
- Prior art keywords
- water separator
- oxygen
- hydrogen
- air inlet
- steam
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000001301 oxygen Substances 0.000 title claims abstract description 49
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 35
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000001257 hydrogen Substances 0.000 claims abstract description 27
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 27
- 239000007789 gas Substances 0.000 claims abstract description 26
- 238000006243 chemical reaction Methods 0.000 abstract description 8
- 238000005260 corrosion Methods 0.000 abstract description 2
- 230000007797 corrosion Effects 0.000 abstract description 2
- 230000001351 cycling effect Effects 0.000 abstract 4
- 238000007599 discharging Methods 0.000 abstract 3
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model relates to a novel hydrogen-oxygen pile system. The novel hydrogen-oxygen pile system comprises a galvanic pile, a hydrogen cycling inlet system and an oxygen cycling inlet system; the hydrogen cycling inlet system comprises a hydrogen inlet valve, a gas inlet pipeline A, a gas outlet pipeline A, a gas-water separator A and a water discharging pipeline A, wherein the gas inlet pipeline A is provided with a venturi pipe A, and the gas outlet pipeline A is also provided with the gas-water separator A; the oxygen cycling inlet system comprises an oxygen inlet valve, a gas inlet pipeline B, a gas outlet pipeline B, a gas-water separator B and a water discharging pipeline B, wherein the gas inlet pipeline B is provided with a venturi pipe B, and the gas outlet pipeline B is also provided with the gas-water separator B. The novel hydrogen-oxygen pile system has advantages that hydrogen and oxygen are separated from water by utilizing the gas-water separator, the separated hydrogen and oxygen are sent into the venturi pipes and continuously sent into the galvanic pile for reaction, and the corrosion of a circuit and the environmental pollution caused by direct discharging of the hydrogen and the oxygen can be avoided.
Description
Technical field
The utility model relates to a kind of reactor system, particularly a kind of novel hydrogen-oxygen shut-down system.
Background technology
When oxyhydrogen reaction, hydrogen and oxygen need to first carry out preheating, also need to add a certain amount of water simultaneously, and when reaction, oxyhydrogen reaction has must back pressure, produces water, the water of oxyhydrogen reaction with react before the water that adds be all the intermittent discharges of needs, and in the process of discharge, have the hydrogen of most and oxygen to be discharged away along with water.The hydrogen of discharge has certain corrosiveness to control circuit, and hydrogen arbitrarily discharge pollute the environment, hydrogen and oxygen easy firing, also exist certain potential safety hazard simultaneously.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of novel hydrogen-oxygen shut-down system that can avoid unreacted hydrogen and oxygen discharge.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of novel hydrogen-oxygen shut-down system, and its innovative point is: comprise pile, hydrogen circulation gas handling system and oxygen circulation gas handling system;
Described hydrogen circulation gas handling system comprises hydrogen gas valve, air inlet pipeline A, outlet pipe A, steam-water separator A and discharge pipe line A, air inlet place at air inlet pipeline A is provided with hydrogen gas valve, on described air inlet pipeline A, be provided with Venturi tube A, air inlet pipeline A is connected with the air inlet of pile, outlet pipe A is connected with the gas outlet of pile, one steam-water separator A is also installed on outlet pipe A, and described Venturi tube A, air inlet pipeline A, pile, outlet pipe A and steam-water separator A form a circulatory system;
Described oxygen circulation gas handling system comprises oxygen intake valve, air inlet pipeline B, outlet pipe B, steam-water separator B and discharge pipe line B, air inlet place at air inlet pipeline B is provided with oxygen intake valve, on described air inlet pipeline B, be provided with Venturi tube B, air inlet pipeline B is connected with the air inlet of pile, outlet pipe B is connected with the gas outlet of pile, one steam-water separator B is also installed on outlet pipe B, and described Venturi tube B, air inlet pipeline B, pile, outlet pipe B and steam-water separator B form a circulatory system.
Further, the pressure transmitter A that the pressure in a pair of steam-water separator A detects is installed on described steam-water separator A, described pressure transmitter A regulates the keying of hydrogen gas valve by controller.
Further, the pressure transmitter B that the pressure in a pair of steam-water separator B detects is installed on described steam-water separator B, described pressure transmitter B regulates the keying of oxygen intake valve by controller.
Further, between described steam-water separator A and Venturi tube A, unidirectional valve A is installed, between described steam-water separator B and Venturi tube B, unidirectional valve B is installed.
Further, draining valve A is also installed on the outlet pipeline of described steam-water separator A, draining valve B is also installed on the outlet pipeline of steam-water separator B.
The utility model has the advantage of: by setting up respectively steam-water separator in the exhaust ports of reaction pile, when pile draining, the unreacted hydrogen containing in water and oxygen are passed through respectively to steam-water separator, utilize steam-water separator that hydrogen is separated with water with oxygen, in hydrogen after separation is sent into Venturi tube with oxygen, continue to be fed in pile and react, avoid hydrogen and oxygen corrosion and pollution on the environment that directly discharge causes circuit, also avoided hydrogen and oxygen combustion simultaneously and the potential safety hazard brought; Separated hydrogen and oxygen, also with uniform temperature, can carry out certain preheating to the hydrogen directly passing into from air inlet pipeline and oxygen simultaneously, have reduced the consumption of the energy.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of novel hydrogen-oxygen shut-down system of the present utility model.
Embodiment
Schematic diagram is as shown in Figure 1 known, and novel hydrogen-oxygen shut-down system of the present utility model comprises pile 4, hydrogen circulation gas handling system and oxygen circulation gas handling system.
Hydrogen circulation gas handling system comprises hydrogen gas valve 1, air inlet pipeline A3, outlet pipe A16, steam-water separator A10 and discharge pipe line A18, air inlet place at air inlet pipeline A3 is provided with hydrogen gas valve 1, on air inlet pipeline A3, be provided with Venturi tube A2, air inlet pipeline A3 is connected with the air inlet of pile 4, outlet pipe A16 is connected with the gas outlet of pile 4, one steam-water separator A10 is also installed on outlet pipe A16, one unidirectional valve A8 is also installed on outlet pipe A16 between Venturi tube A2 and steam-water separator A10, the delivery port of steam-water separator A10 is connected with outlet pipeline A18, draining valve A11 is installed on outlet pipeline A18, the pressure transmitter A9 that pressure in a pair of steam-water separator A10 detects is installed on steam-water separator A10, pressure transmitter A9 regulates the keying of hydrogen gas valve 1 by controller.
Venturi tube A2, air inlet pipeline A3, pile 4, outlet pipe A16, steam-water separator A10 and unidirectional valve A8 form a circulatory system, the hydrogen for reaction in pile 4 is recycled, also the hydrogen in air inlet pipeline A3 is heated, reduce air inlet pressure simultaneously.
Oxygen circulation gas handling system comprises oxygen intake valve 7, air inlet pipeline B5, outlet pipe B17, steam-water separator B13 and discharge pipe line B19, air inlet place at air inlet pipeline B5 is provided with oxygen intake valve 7, on air inlet pipeline B5, be provided with Venturi tube B6, air inlet pipeline B5 is connected with the air inlet of pile 4, outlet pipe B17 is connected with the gas outlet of pile 4, one steam-water separator B13 is also installed on outlet pipe B17, one unidirectional valve B15 is also installed on outlet pipe B17 between Venturi tube B6 and steam-water separator B13, the delivery port of steam-water separator B13 is connected with outlet pipeline B19, draining valve B12 is installed on outlet pipeline B19, the pressure transmitter B14 that pressure in a pair of steam-water separator B13 detects is installed on steam-water separator B13, pressure transmitter B14 regulates the keying of oxygen intake valve 7 by controller.
Venturi tube B6, air inlet pipeline B5, pile 4, outlet pipe B17, steam-water separator B13 and unidirectional valve B15 form a circulatory system, the oxygen for reaction in pile 4 is recycled, also the oxygen in air inlet pipeline B5 is heated, reduce air inlet pressure simultaneously.
More than show and described basic principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (5)
1. a novel hydrogen-oxygen shut-down system, is characterized in that: comprise pile, hydrogen circulation gas handling system and oxygen circulation gas handling system;
Described hydrogen circulation gas handling system comprises hydrogen gas valve, air inlet pipeline A, outlet pipe A, steam-water separator A and discharge pipe line A, air inlet place at air inlet pipeline A is provided with hydrogen gas valve, on described air inlet pipeline A, be provided with Venturi tube A, air inlet pipeline A is connected with the air inlet of pile, outlet pipe A is connected with the gas outlet of pile, one steam-water separator A is also installed on outlet pipe A, and described Venturi tube A, air inlet pipeline A, pile, outlet pipe A and steam-water separator A form a circulatory system;
Described oxygen circulation gas handling system comprises oxygen intake valve, air inlet pipeline B, outlet pipe B, steam-water separator B and discharge pipe line B, air inlet place at air inlet pipeline B is provided with oxygen intake valve, on described air inlet pipeline B, be provided with Venturi tube B, air inlet pipeline B is connected with the air inlet of pile, outlet pipe B is connected with the gas outlet of pile, one steam-water separator B is also installed on outlet pipe B, and described Venturi tube B, air inlet pipeline B, pile, outlet pipe B and steam-water separator B form a circulatory system.
2. novel hydrogen-oxygen shut-down system according to claim 1, it is characterized in that: the pressure transmitter A that the pressure in a pair of steam-water separator A detects is installed on described steam-water separator A, and described pressure transmitter A regulates the keying of hydrogen gas valve by controller.
3. novel hydrogen-oxygen shut-down system according to claim 1, it is characterized in that: the pressure transmitter B that the pressure in a pair of steam-water separator B detects is installed on described steam-water separator B, and described pressure transmitter B regulates the keying of oxygen intake valve by controller.
4. novel hydrogen-oxygen shut-down system according to claim 1, is characterized in that: between described steam-water separator A and Venturi tube A, unidirectional valve A is installed, between described steam-water separator B and Venturi tube B, unidirectional valve B is installed.
5. novel hydrogen-oxygen shut-down system according to claim 1, is characterized in that: draining valve A is also installed on the outlet pipeline of described steam-water separator A, draining valve B is also installed on the outlet pipeline of steam-water separator B.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420095008.6U CN203787511U (en) | 2014-03-04 | 2014-03-04 | Novel hydrogen-oxygen pile system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420095008.6U CN203787511U (en) | 2014-03-04 | 2014-03-04 | Novel hydrogen-oxygen pile system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203787511U true CN203787511U (en) | 2014-08-20 |
Family
ID=51323666
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420095008.6U Expired - Fee Related CN203787511U (en) | 2014-03-04 | 2014-03-04 | Novel hydrogen-oxygen pile system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203787511U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103855418A (en) * | 2014-03-04 | 2014-06-11 | 南通百应能源有限公司 | Novel hydrogen-oxygen pile system |
| CN106252688A (en) * | 2016-08-05 | 2016-12-21 | 江苏河海新能源股份有限公司 | A kind of fuel-cell device |
-
2014
- 2014-03-04 CN CN201420095008.6U patent/CN203787511U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103855418A (en) * | 2014-03-04 | 2014-06-11 | 南通百应能源有限公司 | Novel hydrogen-oxygen pile system |
| CN106252688A (en) * | 2016-08-05 | 2016-12-21 | 江苏河海新能源股份有限公司 | A kind of fuel-cell device |
| CN106252688B (en) * | 2016-08-05 | 2019-01-25 | 江苏河海新能源股份有限公司 | A kind of fuel-cell device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203656903U (en) | Boiler blow-down drainage waste heat cascade utilization device | |
| CN203787511U (en) | Novel hydrogen-oxygen pile system | |
| CN204301574U (en) | A kind of novel hot water feeding mechanism | |
| CN103482649B (en) | Urea solution hydrolysis reactor | |
| CN103432919B (en) | A kind of liquefied ammonia ammoniacal liquor device | |
| CN103835747B (en) | A kind of system and method for low-concentration gas comprehensive utilization | |
| CN203950874U (en) | A kind of fuel cell hydrogen-oxygen enclosed complete alternation system | |
| CN205391760U (en) | Ammonia -acid process compound fertilizer production uses high -efficient liquid ammonia evaporator | |
| CN202610236U (en) | Methane production system | |
| CN105065908A (en) | Sulfur-contained natural gas collection integrated device | |
| CN103855418A (en) | Novel hydrogen-oxygen pile system | |
| CN203998986U (en) | A kind of device of controlling alumina high temperature stripping organism and sulphur | |
| CN108036193B (en) | A modular submarine natural gas pipeline hydrate anti-blocking device and process | |
| CN103335544A (en) | Pipe-in-pipe heat exchanger | |
| CN204234059U (en) | Pressure balance type reactor assembly | |
| CN204261552U (en) | A yellow phosphorus tail gas treatment system | |
| CN201292250Y (en) | Air feed system composed of multiple ammonia decomposition furnaces | |
| CN205328638U (en) | Chlorine gas treatment device | |
| CN203787092U (en) | Novel hydrogen and air reactor system cooling device | |
| CN212430815U (en) | Boiler chemical adding device | |
| CN203778054U (en) | Novel system for hydrogen-oxygen reaction water renewing circulation | |
| CN103322244A (en) | Novel U-shaped pipe gas water seal | |
| CN204283568U (en) | Off-gas recovery vaporizer | |
| CN204879446U (en) | Contain sulphur natural gas gas collection integration device | |
| CN203240016U (en) | Novel U-shaped pipe gas water seal |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140820 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |