CN201942754U - Disc separator - Google Patents

Disc separator Download PDF

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Publication number
CN201942754U
CN201942754U CN2010206204512U CN201020620451U CN201942754U CN 201942754 U CN201942754 U CN 201942754U CN 2010206204512 U CN2010206204512 U CN 2010206204512U CN 201020620451 U CN201020620451 U CN 201020620451U CN 201942754 U CN201942754 U CN 201942754U
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CN
China
Prior art keywords
separator
layer separator
lower floor
main body
upper strata
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
Application number
CN2010206204512U
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Chinese (zh)
Inventor
柯阳
李锦冠
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SUZHOU JINGLI HYDROGEN MAKING APPARATUS CO Ltd
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SUZHOU JINGLI HYDROGEN MAKING APPARATUS CO Ltd
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Publication date
Application filed by SUZHOU JINGLI HYDROGEN MAKING APPARATUS CO Ltd filed Critical SUZHOU JINGLI HYDROGEN MAKING APPARATUS CO Ltd
Priority to CN2010206204512U priority Critical patent/CN201942754U/en
Application granted granted Critical
Publication of CN201942754U publication Critical patent/CN201942754U/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen 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 provides a disc separator. The main body of the separator is in a pot type structure, and an upper-layer separator and a lower-layer separator are horizontally arranged inside the main body of the disc separator. An inlet pipe arranged at one side of the main body of the separator stretches into the cavity of the upper-layer separator, and both the upper-layer separator and the lower-layer separator are in a top open type structure. The upper-layer separator corresponds to the lower-layer separator, and opening area of the upper-layer separator is less than that of the lower-layer separator. A conduit is vertically installed at the bottom of the lower-layer separator and is communicated with the cavity of the lower-layer separator. In use, mixture of gas and liquid from an electrolytic cell enters into the top-layer separator through the inlet pipe for a first separation of the gas, then the liquid overflows from a jagged portion of the upper-layer separator and further overflows to the lower-layer separator for a second separation, afterwards the liquid enters into a liquid part through the conduit, thereby lowering the moisture content of the gas, further cooling the liquid and realizing the full cooling and separation of the gas and the liquid.

Description

The disc type separator
Technical field
The utility model relates to a kind of disc type separator that is applicable to the hydrogen in the water electrolysis hydrogen producing system (oxygen) alkali lye separation system.
Background technology
Hydrogen (oxygen) alkali lye separator is applied in the water electrolysis hydrogen producing system, the water electrolysis hydrogen producing system is by electrolyzer, hydrogen (oxygen) separator, composition such as gas cooler, alkali solution cooler, the temperature of hydrogen (oxygen) gas alkali mixed solution when electrolyzer enters hydrogen (oxygen) alkali lye separator is up to 80~90 ℃, therefore by hydrogen (oxygen) alkali separator alkali liquid temperature is reduced, separate better to reach gas-liquid, present used hydrogen (oxygen) alkali lye separator volume is all bigger, and cost is higher.
The utility model content
The purpose of this utility model is to overcome the deficiency that prior art exists, and a kind of disc type separator is provided, and is intended to increase separating area, improves separation efficiency, more effectively makes the abundant refrigerated separation of gas-liquid, and the reduction equipment volume is saved cost.
The purpose of this utility model is achieved through the following technical solutions:
The disc type separator, separator main body is the pot type structure, characteristics are: described separator main body inner horizontal is provided with upper strata separator and lower floor's separator, the inlet pipe that the separator main body side is provided with stretches in the cavity volume of upper strata separator, described upper strata separator and lower floor's separator are unenclosed construction suitable for reading, the upper strata separator is relative with the lower floor separator, the bottom vertical of lower floor's separator is equipped with conduit, conduit communicates with the cavity volume of lower floor's separator, the upper port of conduit is higher than lower floor separator bottom, and the end face of separator main body is provided with outlet pipe.
Further, above-mentioned disc type separator, wherein, the week suitable for reading edge of described upper strata separator is the band saw dentation.
Further, above-mentioned disc type separator, wherein, described lower floor separator area is greater than upper strata separator area.
Again further, above-mentioned disc type separator, wherein, the upper port of described conduit is higher than the separator bottom 30mm of lower floor.
Substantive distinguishing features and obvious improvement that technical solutions of the utility model are outstanding are mainly reflected in:
The utility model is set up two-layer refrigerated separation layer in original conventional container inside, make the abundant refrigerated separation of gas-liquid effectively, gas liquid mixture comes out to enter the upper strata separator through inlet pipe from electrolyzer, carries out the gas flash liberation, and liquid is from the band saw dentation overflow of upper strata separator, then overflow to lower floor's separator and carry out secondary separation, pass through conduit influent inside again, thereby the water capacity of gas is reduced, fluid temperature is further cooled off, equipment volume is dwindled, and saves cost.
Description of drawings
Below in conjunction with accompanying drawing technical solutions of the utility model are described further:
Fig. 1: master of the present utility model looks synoptic diagram.
The implication of each Reference numeral sees the following form among the figure:
Figure BSA00000356485400021
Embodiment
As shown in Figure 1, the disc type separator, separator main body 1 is the pot type structure, horizontally disposed, the separator main body inner horizontal is provided with upper strata separator 3 and lower floor's separator 4, the inlet pipe 2 that the separator main body side is provided with stretches in the cavity volume of upper strata separator 3, upper strata separator 3 and lower floor's separator 4 are unenclosed construction suitable for reading, the week suitable for reading edge of upper strata separator 3 is the band saw dentation, upper strata separator 3 is relative with lower floor separator 4, the uncovered area of upper strata separator 3 is less than the uncovered area of lower floor's separator 4, the bottom vertical of lower floor's separator 4 is equipped with conduit 5, and conduit 5 communicates with the cavity volume of lower floor separator 4, and the upper orifice of conduit 5 is higher than the separator bottom 30mm of lower floor, the lower nozzle of conduit 5 is positioned under the liquid level A, and the end face of separator main body is provided with outlet pipe 6.
The disc type separator is applied in the water electrolysis hydrogen producing system, gas liquid mixture comes out to enter upper strata separator 3 through inlet pipe 2 from electrolyzer, the gas flash liberation, liquid is from the band saw dentation overflow of upper strata separator 3, the band saw dentation makes liquid dispersion, then overflow to lower floor's separator 4 and carry out secondary separation, pass through conduit 5 influent inside again, gas after the separation is discharged from outlet pipe 6, the water capacity of gas is reduced, fluid temperature is further cooled off, thereby equipment volume is diminished, and saves cost.
In sum, the utility model is set up two-layer refrigerated separation layer in original conventional container inside, thereby makes the abundant refrigerated separation of gas-liquid effectively.
What need understand is: the above only is a preferred implementation of the present utility model; for those skilled in the art; under the prerequisite that does not break away from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.

Claims (4)

1. disc type separator, separator main body is the pot type structure, it is characterized in that: described separator main body inner horizontal is provided with upper strata separator and lower floor's separator, the inlet pipe that the separator main body side is provided with stretches in the cavity volume of upper strata separator, described upper strata separator and lower floor's separator are unenclosed construction suitable for reading, the upper strata separator is relative with the lower floor separator, the bottom vertical of lower floor's separator is equipped with conduit, conduit communicates with the cavity volume of lower floor's separator, the upper port of conduit is higher than lower floor separator bottom, and the end face of separator main body is provided with outlet pipe.
2. disc type separator according to claim 1 is characterized in that: the week suitable for reading of described upper strata separator is along being the band saw dentation.
3. disc type separator according to claim 1 is characterized in that: described lower floor separator area is greater than upper strata separator area.
4. disc type separator according to claim 1 is characterized in that: the upper port of described conduit is higher than the separator bottom 30mm of lower floor.
CN2010206204512U 2010-11-23 2010-11-23 Disc separator Expired - Lifetime CN201942754U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010206204512U CN201942754U (en) 2010-11-23 2010-11-23 Disc separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010206204512U CN201942754U (en) 2010-11-23 2010-11-23 Disc separator

Publications (1)

Publication Number Publication Date
CN201942754U true CN201942754U (en) 2011-08-24

Family

ID=44470102

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010206204512U Expired - Lifetime CN201942754U (en) 2010-11-23 2010-11-23 Disc separator

Country Status (1)

Country Link
CN (1) CN201942754U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102061485A (en) * 2010-11-23 2011-05-18 苏州竞立制氢设备有限公司 Disc separator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102061485A (en) * 2010-11-23 2011-05-18 苏州竞立制氢设备有限公司 Disc separator
CN102061485B (en) * 2010-11-23 2013-01-02 苏州竞立制氢设备有限公司 Disc separator

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GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20110824

Effective date of abandoning: 20130306

RGAV Abandon patent right to avoid regrant