CN204841356U - Demercuration absorbent electrolysis regenerating unit - Google Patents

Demercuration absorbent electrolysis regenerating unit Download PDF

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Publication number
CN204841356U
CN204841356U CN201520550644.8U CN201520550644U CN204841356U CN 204841356 U CN204841356 U CN 204841356U CN 201520550644 U CN201520550644 U CN 201520550644U CN 204841356 U CN204841356 U CN 204841356U
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CN
China
Prior art keywords
absorbent
electrolysis trough
electrolytic cell
type
type electrolysis
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
Application number
CN201520550644.8U
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Chinese (zh)
Inventor
沈吉兆
夏永奎
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YANGZHOU CHENGUANG SPECIAL EQUIPMENT CO Ltd
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YANGZHOU CHENGUANG SPECIAL EQUIPMENT CO Ltd
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Priority to CN201520550644.8U priority Critical patent/CN204841356U/en
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Publication of CN204841356U publication Critical patent/CN204841356U/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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Electrolytic Production Of Metals (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The utility model relates to a demercuration absorbent electrolysis regenerating unit, include H type electrolysis trough, circulation magma cistern, the former thick liquid that circulates pass through corrosion -resistant pump and connect H type electrolysis trough, and H type electrolysis trough sets up in the thermostat water bath, and the vertical cation exchange membrane that is equipped with in H type electrolysis trough bottom still is equipped with magnetic stirrers, pt piece electrode, measuring electrode in the H type electrolysis trough, and pt piece electrode is connection pressure table and ampere meter respectively, ampere meter connection DC power supply, still be equipped with conductivity tester, pH value tester and thermometer in the H type electrolysis trough. Magnetic stirrers can stir the absorbent in the electrolysis trough, and the setting of conductivity tester, pH value tester and thermometer has realized carrying out real time monitoring to the various parameters of electrolysis trough internal absorption agent, and convenient operation effectually carries out the electrolytic separation of mercury to the absorbent, separates effectually, efficient, has realized the recycle of mercury element also having realized that the recycle and regeneration of absorbent uses resources are saved simultaneously.

Description

Demercuration absorbent electrolytic regeneration device
Technical field
The utility model relates to a kind of electrolytic regeneration device, especially relates to a kind of demercuration absorbent electrolytic regeneration device.
Background technology
Coal is the topmost primary energy of China, and annual burning coal can discharge a large amount of pollutants, and therefore the improvement of pollution that caused by coal burning thing is the hot issue of association area always.Pollution that caused by coal burning owner will comprise dust, SO2, NOx, CO2, heavy metal etc., and wherein dust, SO2, NOx have had the removal methods of comparative maturity haply, and the removing sulfuldioxide of CO2 is also just in flourish process.Always out in the cold before the discharge of mercury, be not still applied to the demercuration case in actual items at present, along with environmental protection standard is day by day strict, the concentration of mercury emissions is limited, therefore needs the demercuration technology releasing a kind of high-efficiency and low-cost.The research emphasis of current mercury removal is in flue, directly spray into dry-spray removal method that pressed powder adsorbent is and the adsorbent method based on fixed bed.But in wet scrubbing demercuration, research work is also few.Wet method removes pollutant and has two advantages: first be the intensity of gas-liquid mass transfer usually above the gas solid transfer under the same terms, absorptivity is higher; Second is the environment that wet method has electrolyte solution usually, is convenient to the conversion realizing material.But if absorbent can not use by circular regeneration, the advantage of wet method removing process is difficult to play.
Utility model content
The utility model is intended to address the aforementioned drawbacks, and provides a kind of demercuration absorbent electrolytic regeneration device.
In order to overcome the defect existed in background technology, the utility model solves the technical scheme that its technical problem adopts: a kind of demercuration absorbent electrolytic regeneration device, comprise H type electrolytic cell, circulation magma liquid bath, circulation virgin pulp liquid connects H type electrolytic cell by noncorrosive pump, H type electrolytic cell is arranged in thermostat water bath, H type bottom of electrolytic tank is vertically provided with cation-exchange membrane, also magnetic stirring apparatus is provided with in H type electrolytic cell, Pt plate electrode, measurement electrode, Pt plate electrode is Bonding pressure table and ammeter respectively, ammeter connects dc source, also conductivity measurement is provided with in described H type electrolytic cell, pH value tester and thermometer.
In a preferred embodiment of the present utility model, be connected by serum recycle pipe between H type electrolytic cell with circulation magma liquid bath.
The beneficial effects of the utility model are: magnetic stirring apparatus can stir the absorbent in electrolytic cell, the setting of conductivity measurement, pH value tester and thermometer, achieve and the various parameters of electrolytic cell inner absorbent are monitored in real time, easy to operate, effectively absorbent is carried out to the electrolytic separation of mercury, good separating effect, efficiency is high, achieve the recycling of mercury element, the circular regeneration simultaneously also achieving absorbent uses, and economizes on resources.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
A kind of demercuration absorbent electrolytic regeneration device as shown in Figure 1, comprise H type electrolytic cell 1, circulation magma liquid bath 9, circulation magma liquid bath 9 connects H type electrolytic cell 1 by noncorrosive pump 8, H type electrolytic cell 1 is arranged in thermostat water bath 7, cation-exchange membrane 2 is vertically provided with bottom H type electrolytic cell 1, magnetic stirring apparatus 6, Pt plate electrode 3, measurement electrode 5 is also provided with in H type electrolytic cell 1, Pt plate electrode 3 is Bonding pressure table 10 and ammeter 11 respectively, ammeter 11 connects in dc source 14, H type electrolytic cell 1 and is also provided with conductivity measurement 12, pH value tester 13 and thermometer 4.
Be connected by serum recycle pipe 15 between H type electrolytic cell 1 with circulation magma liquid bath 9.
Magnetic stirring apparatus can stir the absorbent in electrolytic cell, the setting of conductivity measurement, pH value tester and thermometer, achieve and the various parameters of electrolytic cell inner absorbent are monitored in real time, easy to operate, effectively absorbent is carried out to the electrolytic separation of mercury, good separating effect, efficiency is high, achieve the recycling of mercury element, the circular regeneration simultaneously also achieving absorbent uses, and economizes on resources.

Claims (2)

1. a demercuration absorbent electrolytic regeneration device, it is characterized in that: comprise H type electrolytic cell, circulation magma liquid bath, described circulation virgin pulp liquid connects H type electrolytic cell by noncorrosive pump, described H type electrolytic cell is arranged in thermostat water bath, described H type bottom of electrolytic tank is vertically provided with cation-exchange membrane, also magnetic stirring apparatus is provided with in described H type electrolytic cell, Pt plate electrode, measurement electrode, described Pt plate electrode is Bonding pressure table and ammeter respectively, described ammeter connects dc source, also conductivity measurement is provided with in described H type electrolytic cell, pH value tester and thermometer.
2. demercuration absorbent electrolytic regeneration device according to claim 1, is characterized in that: described H type electrolytic cell is connected by serum recycle pipe with between circulation magma liquid bath.
CN201520550644.8U 2015-07-27 2015-07-27 Demercuration absorbent electrolysis regenerating unit Expired - Fee Related CN204841356U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520550644.8U CN204841356U (en) 2015-07-27 2015-07-27 Demercuration absorbent electrolysis regenerating unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520550644.8U CN204841356U (en) 2015-07-27 2015-07-27 Demercuration absorbent electrolysis regenerating unit

Publications (1)

Publication Number Publication Date
CN204841356U true CN204841356U (en) 2015-12-09

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520550644.8U Expired - Fee Related CN204841356U (en) 2015-07-27 2015-07-27 Demercuration absorbent electrolysis regenerating unit

Country Status (1)

Country Link
CN (1) CN204841356U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109055968A (en) * 2018-07-12 2018-12-21 芜湖职业技术学院 Organic electro-synthesis electrolysis unit

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109055968A (en) * 2018-07-12 2018-12-21 芜湖职业技术学院 Organic electro-synthesis electrolysis unit
CN109055968B (en) * 2018-07-12 2020-07-24 芜湖职业技术学院 Organic electro-synthesis electrolysis device

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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: 20151209

Termination date: 20210727

CF01 Termination of patent right due to non-payment of annual fee