CN202530171U - Overflow-free gas-liquid separator - Google Patents
Overflow-free gas-liquid separator Download PDFInfo
- Publication number
- CN202530171U CN202530171U CN2012200797299U CN201220079729U CN202530171U CN 202530171 U CN202530171 U CN 202530171U CN 2012200797299 U CN2012200797299 U CN 2012200797299U CN 201220079729 U CN201220079729 U CN 201220079729U CN 202530171 U CN202530171 U CN 202530171U
- Authority
- CN
- China
- Prior art keywords
- liquid
- flange
- cylindrical shell
- gas
- liquid level
- 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 - Lifetime
Links
Images
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
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model belongs to the technical field of mechanical manufacturing, and relates to a gas-liquid separator, in particular to an overflow-free gas-liquid separator. The technical scheme is that the overflow-free gas-liquid separator comprises a flange, a valve core part, a buoy, a guide tube, a barrel, a liquid control part and a lug. Through the structure, the purity of oxygen and hydrogen is ensured, and the oxygen and the hydrogen cannot infiltrate into each other; and a self-excitation floating ball sealing device is arranged in the separator, so that the separator works safely and reliably, and the defect that the liquid level of the separator continuously rises because a liquid level control system fails is thoroughly overcome.
Description
Technical field
The utility model belongs to machinery manufacturing technology field, relates to a kind of gas-liquid separator, particularly a kind of no excessive gas-liquid separator.
Background technology
In existing technology, widely used water electrolysis hydrogen producing equipment is the pressurized water electrolytic hydrogen production in the industry.It is particularly important that the control of hydrogen, oxygen separator liquid level equilibrium just seems.The groundwork flow process is: electrolytic solution electrolysis produces in electrolyzer hydrogen and oxygen get into hydrogen separator and oxygen separator respectively with electrolytic solution; Gas after the separation is discharged respectively by blow-down pipe; Liquid is got back to electrolyzer through the pipe of separator lower end, forms the water electrolysis hydrogen producing recycle system.In the work, if cause that by two trap pressure imbalances the hydrogen separator liquid level descends, then the liquid level of oxygen separator just can rise, otherwise also like this.When tank level control system was malfunctioning, hydrogen, oxygen liquid level difference just can sharply strengthen, and will cause hydrogen, oxygen infiltration aggravation in the electrolyzer, and gas purity descends, and has the danger of blast when serious.If hydrogen, oxygen liquid level difference continue to strengthen, cause the electrolytic solution in the separator all to get in another separator, will directly cause hydrogen, carrier of oxygen to mix, have the danger of blast at any time.Simultaneously, the increasing of liquid level difference also can cause electrolytic solution to overflow separator, causes gas piping to stop up, and control and analysis elements device are impaired.
The utility model content
The purpose of the utility model is to overcome the defective that exists in the prior art, designs and a kind of can guarantee hydrogen or oxygen gas purity, makes the hydrogen or oxygen gas can interpenetrative no excessive gas-liquid separator.
To achieve these goals, the technical scheme of the utility model is a kind of no excessive gas-liquid separator of design, comprises flange, valve hole part, floating drum, guide pipe, cylindrical shell, control liquid parts and flange;
Wherein, flange has centre hole;
The upper end of cylindrical shell is a hatch frame, from top to bottom has transmitter gas phase interface, gas-liquid import and transmitter liquid phase interface at the sidewall of cylindrical shell, has electrolyte outlet in the lower end of cylindrical shell;
Valve hole part is made up of spool and sealing member, and spool is the circular cone hole body, and sealing member has centre hole, and the centre hole co-axial seal of the conical bore of spool and sealing member is installed;
Floating drum is that two ends are hemispheroidal hollow cylindrical tube;
Guide pipe is made up of U type body and support, and the lower end of U type body has through hole, and an end of support and the external wall of U type are welded to connect;
Control liquid parts are cone;
Its annexation: said cylindrical shell, guide pipe, control liquid parts, valve hole part and flange are coaxial assembling; The spool of valve hole part is installed in the central hole of flange and is welded to connect with flange; Outer, upper end sealing weld at cylindrical shell is connected to flange; Flange is with the flange seal fixed installation and the sealing member of valve hole part is cooperated with the upper edge of cylindrical shell; The other end of guide pipe support is fixedly connected on the inwall of cylindrical shell; In the U of guide pipe type body, place floating drum; The upper end of floating drum is installed with control liquid parts; The spool of control liquid parts and valve hole part is complementary.
Also include liquid level meter, liquid level is counted transparent tube, and liquid level meter is connected with cylindrical shell with following pipe connecting through last pipe connecting; Liquid passes through up and down, and pipe connecting passes in and out liquid level meter so that observe the liquid level of electrolytic solution.
The transmitter gas phase interface on the cylindrical shell and the distance of flange upper surface are 132mm, and the distance of gas-liquid import and transmitter gas phase interface is 280mm, and the distance of transmitter liquid phase interface and gas-liquid import is 120mm.
The utility model is achieved in that when the liquid level of separator continues to rise; Floating drum in guide pipe with the liquid level vertical uplift; Finally separator upper end spool is blocked, thereby stoped liquid level to continue to rise, and prevent to cause electrolytic solution excessive because of liquid level continues to rise by control liquid parts; Simultaneously, also play the effect that reduces the inner hydrogen of electrolyzer, oxygen side pressure difference, stop interpenetrating of hydrogen, carrier of oxygen, prevent that gas purity from continuing to descend; When the liquid level of separator descended, floating drum vertically descended with liquid level in guide pipe, thereby opened the spool outlet of separator upper end, and the water electrolysis hydrogen producing recycle system is just recovered normal operating conditions.
The advantage and the beneficial effect of the utility model are: the present invention adopts said structure, guarantees hydrogen or oxygen gas purity, hydrogen or oxygen gas can not interpenetrated; Because indoor design has auto-excitation type ball float tightness system, and is safe and reliable, thoroughly avoided the lasting defective that rises of separator liquid level that causes because of tank level control system is malfunctioning.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Wherein, 1-flange; The 2-spool; 3-transmitter gas phase interface; The 4-floating drum; The 5-locating support; The 6-liquid level meter; The import of 7-gas-liquid; 8-transmitter liquid phase interface; The 9-cylindrical shell; The 10-electrolyte outlet; 11-control liquid parts; The last pipe connecting of 12-; Pipe connecting under the 13-.
Embodiment
Below in conjunction with accompanying drawing and embodiment the embodiment of the utility model is further described, following examples only are used for more clearly explaining the technical scheme of the utility model, and can not limit the protection domain of the utility model with this.
The technical scheme of the utility model practical implementation is: a kind of no excessive gas-liquid separator comprises flange 1, valve hole part 2, floating drum 4, guide pipe 5, cylindrical shell 9, control liquid parts 11 and flange 14;
Wherein, flange 1 has centre hole;
The upper end of cylindrical shell 9 is a hatch frame, from top to bottom has transmitter gas phase interface 3, gas-liquid import 7 and transmitter liquid phase interface 8 at the sidewall of cylindrical shell 9, has electrolyte outlet 10 in the lower end of cylindrical shell 9;
Valve hole part 2 is made up of spool and sealing member, and spool is the circular cone hole body, and sealing member has centre hole, and the centre hole co-axial seal of the conical bore of spool and sealing member is installed;
Floating drum 4 is that two ends are hemispheroidal hollow cylindrical tube;
Guide pipe 5 is made up of U type body and support, and the lower end of U type body has through hole, and an end of support and the external wall of U type are welded to connect;
Control liquid parts 11 are cone;
Its annexation: said cylindrical shell 9, guide pipe 5, control liquid parts 11, valve hole part 2 and flange 1 are coaxial assembling; The spool of valve hole part 2 is installed in the central hole of flange 1 and is welded to connect with flange 1; Outer, upper end sealing weld at cylindrical shell 9 is connected to flange 14; Flange 1 is installed with flange 14 sealing and fixing and the sealing member of valve hole part 2 is cooperated with the upper edge of cylindrical shell 9; The other end of guide pipe 5 supports is fixedly connected on the inwall of cylindrical shell 9; In the U of guide pipe 5 type body, place floating drum 4; The upper end of floating drum 4 is installed with control liquid parts 11; Control liquid parts 11 are complementary with the spool of valve hole part 2.
Also include liquid level meter 6, liquid level meter 6 is a transparent tube, and liquid level meter 6 is connected with cylindrical shell 9 with following pipe connecting 13 through last pipe connecting 12; Liquid passes through up and down, and pipe connecting passes in and out liquid level meter 6 so that observe the liquid level of electrolytic solution.
Transmitter gas phase interface 3 on the cylindrical shell 9 is 132mm with the distance of flange 1 upper surface, and gas-liquid import 7 is 280mm with the distance of transmitter gas phase interface 3, and transmitter liquid phase interface 8 is 120mm with the distance of gas-liquid import 3.
The above only is the preferential embodiment of the utility model; Should be understood that; For those skilled in the art; Under the prerequisite that does not break away from the utility model know-why, can also make some improvement and retouching, these improvement and retouching also should be regarded as the protection domain of the utility model.
Claims (3)
1. a no excessive gas-liquid separator is characterized in that: comprise flange (1), valve hole part (2), floating drum (4), guide pipe (5), cylindrical shell (9), control liquid parts (11) and flange (14);
Wherein, flange (1) has centre hole;
The upper end of cylindrical shell (9) is a hatch frame, from top to bottom has transmitter gas phase interface (3), gas-liquid import (7) and transmitter liquid phase interface (8) at the sidewall of cylindrical shell (9), has electrolyte outlet (10) in the lower end of cylindrical shell (9);
Valve hole part (2) is made up of spool and sealing member, and spool is the circular cone hole body, and sealing member has centre hole, and the centre hole co-axial seal of the conical bore of spool and sealing member is installed;
Floating drum (4) is that two ends are hemispheroidal hollow cylindrical tube;
Guide pipe (5) is made up of U type body and support, and the lower end of U type body has through hole, and an end of support and the external wall of U type are welded to connect;
Control liquid parts (11) are cone;
Its annexation: said cylindrical shell (9), guide pipe (5), control liquid parts (11), valve hole part (2) and flange (1) are coaxial assembling; The spool of valve hole part (2) is installed in the central hole of flange (1) and is welded to connect with flange (1); Outer, upper end sealing weld at cylindrical shell (9) is connected to flange (14); Flange (1) is installed with flange (14) sealing and fixing and the sealing member of valve hole part (2) is cooperated with the upper edge of cylindrical shell (9); The other end of guide pipe (5) support is fixedly connected on the inwall of cylindrical shell (9); In the U type body of guide pipe (5), place floating drum (4); The upper end of floating drum (4) is installed with control liquid parts (11); Control liquid parts (11) are complementary with the spool of valve hole part (2).
2. no excessive gas-liquid separator according to claim 1 is characterized in that: also include liquid level meter (6), liquid level meter (6) is a transparent tube, and liquid level meter (6) is connected with cylindrical shell (9) with following pipe connecting (13) through last pipe connecting (12); Liquid passes through up and down, and pipe connecting passes in and out liquid level meter (6) so that observe the liquid level of electrolytic solution.
3. no excessive gas-liquid separator according to claim 1 and 2; It is characterized in that: the transmitter gas phase interface (3) on the cylindrical shell (9) is 132mm with the distance of flange (1) upper surface; Gas-liquid import (7) is 280mm with the distance of transmitter gas phase interface (3), and transmitter liquid phase interface (8) is 120mm with the distance of gas-liquid import (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200797299U CN202530171U (en) | 2012-03-06 | 2012-03-06 | Overflow-free gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200797299U CN202530171U (en) | 2012-03-06 | 2012-03-06 | Overflow-free gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202530171U true CN202530171U (en) | 2012-11-14 |
Family
ID=47131367
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200797299U Expired - Lifetime CN202530171U (en) | 2012-03-06 | 2012-03-06 | Overflow-free gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202530171U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102560524A (en) * | 2012-03-06 | 2012-07-11 | 中国船舶重工集团公司第七一八研究所 | Gas-liquid separator without leakage |
-
2012
- 2012-03-06 CN CN2012200797299U patent/CN202530171U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102560524A (en) * | 2012-03-06 | 2012-07-11 | 中国船舶重工集团公司第七一八研究所 | Gas-liquid separator without leakage |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202530171U (en) | Overflow-free gas-liquid separator | |
| CN102560524A (en) | Gas-liquid separator without leakage | |
| CN202560301U (en) | Negative pressure automatic water-discharge device for coal-mine gas extraction pipeline | |
| CN202297794U (en) | Water electrolysis hydrogen, oxygen and liquid separation control device | |
| CN204752245U (en) | Exhaust type is sour, alkali batch meter | |
| CN103480227A (en) | Gas-water separator of hydrogen generation device | |
| CN204005263U (en) | Anti-leakage gas drainage device | |
| CN102176397B (en) | Counter weight for liquid level float switch | |
| CN201892026U (en) | Methane water separation and gas sealing tank | |
| CN208594642U (en) | A kind of proof mechanism of water at the top of external wall | |
| CN203719732U (en) | Water level detection device for solar energy water tank | |
| CN201933465U (en) | High-water-head underwater suspension floating plug | |
| CN207221396U (en) | A kind of gas-liquid two-phase separator | |
| CN202787389U (en) | Negative-pressure suppressor | |
| CN216223064U (en) | Rotary settling type gas-liquid separator | |
| CN202226929U (en) | Anode liquid discharging and storing device in the ionic membrane caustic soda manufacturing technology | |
| CN202252206U (en) | Methane throttling device | |
| CN203670961U (en) | Special valve for pressure-bearing water storage equipment | |
| CN205330866U (en) | Water pipe way self -bleeding device | |
| CN216973636U (en) | Automatic open-close negative pressure pipeline opening-closing device | |
| CN201454209U (en) | Novel filter | |
| CN203670960U (en) | Special valve for pressure bearing water storing device | |
| CN102425540A (en) | Cavitation pot | |
| CN202904385U (en) | Water tank water-feeding controller | |
| CN221235670U (en) | Miniature automatic water feeding tank with float valve |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20121114 |
|
| CX01 | Expiry of patent term |