CN203569215U - High-temperature high-pressure electrolyzer - Google Patents

High-temperature high-pressure electrolyzer Download PDF

Info

Publication number
CN203569215U
CN203569215U CN201320793036.0U CN201320793036U CN203569215U CN 203569215 U CN203569215 U CN 203569215U CN 201320793036 U CN201320793036 U CN 201320793036U CN 203569215 U CN203569215 U CN 203569215U
Authority
CN
China
Prior art keywords
pressure tank
electrolyzer
tank halfbody
halfbody
half body
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
CN201320793036.0U
Other languages
Chinese (zh)
Inventor
张云龙
黄炜
荆永卿
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.)
Xinhai Tianjin Electromechanical Technology Co ltd
Original Assignee
YANTAI XINHAI MINING MACHINERY CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by YANTAI XINHAI MINING MACHINERY CO Ltd filed Critical YANTAI XINHAI MINING MACHINERY CO Ltd
Priority to CN201320793036.0U priority Critical patent/CN203569215U/en
Application granted granted Critical
Publication of CN203569215U publication Critical patent/CN203569215U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The utility model relates to a high-temperature high-pressure electrolyzer, in particular to a high-temperature high-pressure electrolyzer for desorbing an electrolysis carbon gold extraction system. the high-temperature high-pressure electrolyzer comprises a rack, a fixed pressure tank half body, an electrolytic tank and a mobile pressure tank half body; the fixed pressure tank half body is welded on the rack and is movably jointed with the mobile pressure tank half body; when being closed, the fixed pressure tank half body and the mobile pressure tank half body form an integral pressure tank body; slide wheels are arranged below the mobile pressure tank half body; one end of the electrolytic tank is fixedly welded in the fixed pressure tank half body; the other end of the electrolytic tank is suspended in air and is positioned in the mobile pressure tank half body. The high-temperature high-pressure electrolyzer has the beneficial effects of shortening the time needed by an electrolysis process, improving the electrolytic capacity, improving the finished product recovery rate and effectively recovering gold mud resources.

Description

A kind of high-temp. high-pressure electrolysis groove
Technical field
The utility model relates to a kind of high-temp. high-pressure electrolysis groove, relates in particular to a kind of desorbing electrolytic carbon and carry the high-temp. high-pressure electrolysis groove of golden system.
Background technology
At present at desorbing electrolytic carbon, to put forward in the electrolytic action of golden system speed of response slower for conventional electrolyzer, and the time of conventional electrolysis reaction is longer, lower to the processing power of gold mud, has limited the efficiency of electrolytic reaction.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of high-temp. high-pressure electrolysis groove, has overcome the defect that the electrolysis activity duration is long, electrolysis ability is low.
The technical scheme that the utility model solves the problems of the technologies described above is as follows: a kind of high-temp. high-pressure electrolysis groove, comprise frame, fixation pressure tank halfbody, electrolyzer, movement pressure tank halfbody, described fixation pressure tank halfbody is welded in described frame, described movement pressure tank halfbody docks with described fixation pressure tank halfbody is movable, described fixation pressure tank halfbody and described movement pressure tank halfbody form a complete pressure-pot tank body when closed, described movement pressure tank halfbody below is provided with movable pulley, described electrolyzer one end is fixedly welded on described fixation pressure tank halfbody inside, the unsettled described movement pressure tank halfbody inside that is positioned at of the described electrolyzer the other end.
Further, described fixation pressure tank halfbody outside weldings has positive negative terminal, airline, liquidometer pipeline, safety valve pipeline, electrolyte outlet pipeline, and described positive negative terminal, described airline, described liquidometer pipeline, described safety valve pipeline, described electrolyte outlet pipeline all pass described fixation pressure tank halfbody and described fixation pressure tank halfbody internal communication.
Further, described fixation pressure tank halfbody outside weldings has stripping liquid entrance pipe, and described stripping liquid entrance pipe is linked into electrolyzer inside through fixation pressure tank halfbody.
Further, on described electrolyzer, be installed with positive plate, negative plate, described positive plate is fixed on the flat bolt through electrolyzer, described flat bolt couples together described anode upper insulation plate, described electrolyzer, described lower insulation plate, described anode electrode plate through anode upper insulation plate, electrolyzer, lower insulation plate, anode electrode plate from top to bottom successively, on described flat bolt, is arranged with insulation covering.
The beneficial effects of the utility model are: shortened the time of electrolytic process, improved electrolysis ability, improved the finished product rate of recovery, effectively reclaimed gold mud resource.
Accompanying drawing explanation
Fig. 1 is high-temp. high-pressure electrolysis groove front view of the present utility model;
Fig. 2 is high-temp. high-pressure electrolysis groove side-view of the present utility model;
Fig. 3 is the partial enlarged drawing of A in high-temp. high-pressure electrolysis groove Fig. 1 of the present utility model.
In accompanying drawing, the list of parts of each label representative is as follows:
1, frame, 2, fixation pressure tank halfbody, 3, electrolyzer, 4, movement pressure tank halfbody, 5, positive plate, 6, negative plate, 7, positive negative terminal, 8, airline, 9, liquidometer pipeline, 10, safety valve pipeline, 11, electrolyte outlet pipeline, 12, stripping liquid entrance pipe, 13, anode upper insulation plate, 14, lower insulation plate, 15, anode electrode plate, 16, insulation covering, 17, flat bolt, 18, movable pulley.
Embodiment
Below in conjunction with accompanying drawing, principle of the present utility model and feature are described, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
As shown in Figure 1, the utility model high-temp. high-pressure electrolysis groove comprises frame 1, fixation pressure tank halfbody (so-called fixation pressure tank halfbody refers to that a complete fixation pressure tank is along fixation pressure tank diameter to half fixation pressure tank after cutting apart) 2, for the electrolyzer 3 of electrolytic reaction, movement pressure tank halfbody (so-called movement pressure tank halfbody refers to that a complete movement pressure tank is along movement pressure tank diameter to half movement pressure tank after cutting apart) 4, fixation pressure tank halfbody 2 is welded in frame 1 and keeps maintaining static, movement pressure tank halfbody 4 docks with fixation pressure tank halfbody 2 is movable, when fixation pressure tank halfbody 2 and movement pressure tank halfbody 4 are closed, can form a complete pressure-pot tank body, movement pressure tank halfbody 4 belows are provided with movable pulley 18, movement pressure tank halfbody 4 by movable pulley 18 can do back and forth near or away from the slip of fixation pressure tank halfbody 2, electrolyzer 3 one end are weldingly fixed on fixation pressure tank halfbody 2 inside, the unsettled movement pressure tank halfbody 4 that is positioned at of electrolyzer 3 the other ends.
Fig. 2 is the side-view of the utility model high-temp. high-pressure electrolysis groove, as shown in Figure 2, fixation pressure tank halfbody 2 outside weldings have positive negative terminal 7, for passing into or the airline 8 of excluding air, for the liquidometer pipeline 9 of metering liquid height, safety valve pipeline 10, for discharging the electrolyte outlet pipeline 11 of electrolytic solution, positive negative terminal 7, airline 8, liquidometer pipeline 9, safety valve pipeline 10, electrolyte outlet pipeline 11 all passes fixation pressure tank halfbody 2 and realizes the pressure-controlling of fixation pressure tank halfbody 2 inside and the discharge of electrolytic solution with the internal communication of fixation pressure tank halfbody 2.
As shown in Figure 1 and Figure 2, fixation pressure tank halfbody 2 outside weldings have stripping liquid entrance pipe 12, and stripping liquid entrance pipe 12 is connected with electrolyzer 3 is inner through fixation pressure tank halfbody 2.
As shown in Figure 3, on electrolyzer 3, be installed with positive plate 5, negative plate 6, positive plate 5 is fixed on the flat bolt 17 through electrolyzer 3, flat bolt 17 is from top to bottom successively through anode upper insulation plate 13, electrolyzer 3, lower insulation plate 14, anode electrode plate 15 is by anode upper insulation plate 13, electrolyzer 3, lower insulation plate 14, positive plate battery lead plate 15 couples together, positive plate 5 can be realized with anode electrode plate 15 and being electrically connected by flat bolt 17, on flat bolt 17, cover has insulation covering 16, insulation covering 16 one end are positioned at anode upper insulation plate 13, insulation covering 16 the other ends are positioned at anode electrode plate 15 and prevent circuit conduction.
Its working process is: movement pressure tank halfbody 4 is connected with fixation pressure tank halfbody 2 close tight after, by stripping liquid entrance pipe 14, expensive desorb liquid is injected in electrolyzer 3, the amount of injecting the expensive liquid of desorb need to reach liquidometer pipeline 9 and require 2/3 of height, and then by airline 8, inject air and reach system requirements original pressure 0.2Mpa, after positive negative terminal 7 energisings, electric current enters respectively positive plate 5 and negative plate 6 by electrode, the expensive liquid of desorb in electrolyzer 3 is carried out to electrolysis and make gold precipitation, gold mud is deposited in electrolyzer 3 bottoms, when precipitation reaches a certain amount of, by electrolyte outlet pipeline 11, give off the lean electrolyte in electrolyzer 3, discharge and open movement pressure tank halfbody 4 after complete lean electrolyte and propose gold mud, realization completes the electrolytic reaction of stripping liquid under the condition of High Temperature High Pressure.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.

Claims (4)

1. a high-temp. high-pressure electrolysis groove, it is characterized in that, comprise frame (1), fixation pressure tank halfbody (2), electrolyzer (3), movement pressure tank halfbody (4), described fixation pressure tank halfbody (2) is welded in described frame (1), described movement pressure tank halfbody (4) docks with described fixation pressure tank halfbody (2) is movable, described fixation pressure tank halfbody (2) forms a complete pressure-pot tank body when closed with described movement pressure tank halfbody (4), described movement pressure tank halfbody (4) below is provided with movable pulley (18), described electrolyzer (3) one end is fixedly welded on described fixation pressure tank halfbody (2) inside, unsettled described movement pressure tank halfbody (4) inside that is positioned at of described electrolyzer (3) the other end.
2. a kind of high-temp. high-pressure electrolysis groove according to claim 1, it is characterized in that, described fixation pressure tank halfbody (2) outside weldings has positive negative terminal (7), airline (8), liquidometer pipeline (9), safety valve pipeline (10), electrolyte outlet pipeline (11), and described positive negative terminal (7), described airline (8), described liquidometer pipeline (9), described safety valve pipeline (10), described electrolyte outlet pipeline (11) all pass described fixation pressure tank halfbody (2) and described fixation pressure tank halfbody (2) internal communication.
3. a kind of high-temp. high-pressure electrolysis groove according to claim 1, it is characterized in that, described fixation pressure tank halfbody (2) outside weldings has stripping liquid entrance pipe (12), and described stripping liquid entrance pipe (12) is linked into electrolyzer (3) inside through fixation pressure tank halfbody (2).
4. according to a kind of high-temp. high-pressure electrolysis groove described in any one in claims 1 to 3, it is characterized in that, on described electrolyzer (3), be installed with positive plate (5), negative plate (6), described positive plate (5) is fixed on the flat bolt (17) through electrolyzer (3), described flat bolt (17) is from top to bottom successively through anode upper insulation plate (13), electrolyzer (3), lower insulation plate (14), anode electrode plate (15) is by described anode upper insulation plate (13), described electrolyzer (3), described lower insulation plate (14), described anode electrode plate (15) couples together, the upper cover of described flat bolt (17) has insulation covering (16).
CN201320793036.0U 2013-12-04 2013-12-04 High-temperature high-pressure electrolyzer Expired - Fee Related CN203569215U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320793036.0U CN203569215U (en) 2013-12-04 2013-12-04 High-temperature high-pressure electrolyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320793036.0U CN203569215U (en) 2013-12-04 2013-12-04 High-temperature high-pressure electrolyzer

Publications (1)

Publication Number Publication Date
CN203569215U true CN203569215U (en) 2014-04-30

Family

ID=50536957

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320793036.0U Expired - Fee Related CN203569215U (en) 2013-12-04 2013-12-04 High-temperature high-pressure electrolyzer

Country Status (1)

Country Link
CN (1) CN203569215U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103614746A (en) * 2013-12-04 2014-03-05 烟台鑫海矿山机械有限公司 High-temperature and high-pressure electrolytic tank

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103614746A (en) * 2013-12-04 2014-03-05 烟台鑫海矿山机械有限公司 High-temperature and high-pressure electrolytic tank

Similar Documents

Publication Publication Date Title
CN102453934B (en) Endoporus selective plating device
CN203536512U (en) Plug-free guiding and acid filling pot of lead-acid storage battery
CN203569215U (en) High-temperature high-pressure electrolyzer
CN205223376U (en) A recovery unit for reducing metal ion in waste water
CN106653133B (en) A kind of device based on electrochemical intercalation method disintegration spheric active anode
CN103979488B (en) Adopt the technique of MAGNESIUM METAL continuous seepage hydrogen and magnesium hydroxide
CN103614746A (en) High-temperature and high-pressure electrolytic tank
CN204289600U (en) Stereotype drenches acid and acid cycle utilizes device
CN207338572U (en) A kind of waste and old power battery brine discharge groove
CN202434651U (en) Liquid storage pot evacuating device
CN204529999U (en) A kind of swirl electrolysis device of Separation and Recovery metal composite waste
CN203546163U (en) Industrial electrolytic tank group
CN1996657A (en) Formation method for the seal of the lithium ion battery
CN202450164U (en) Device for recovering lead in waste lead storage batteries through pulse power supply
CN203938743U (en) Anonite membrane eddy flow electrowinning plant
CN203569216U (en) Anode plate sealing cover
CN204411771U (en) Tail acid gathering-device in isoleucine leaching process
CN103730695B (en) A kind of manufacture method of colloid battery
CN204385301U (en) A kind of gold electrolytic recovery device
CN110819812B (en) High-speed rail alloy treatment facility
CN205223368U (en) Zinc metal recycling mechanism
CN204162809U (en) Cyclone electrolytic cell groove
CN204257754U (en) Stereotype drenches sour device
CN213698404U (en) Hydrogen breathing machine
CN205223378U (en) Metal recovering device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CB03 Change of inventor or designer information

Inventor after: Chu Lichen

Inventor after: Huang Wei

Inventor after: Zhang Yunlong

Inventor after: Jing Yongqing

Inventor before: Zhang Yunlong

Inventor before: Huang Wei

Inventor before: Jing Yongqing

COR Change of bibliographic data
CP01 Change in the name or title of a patent holder

Address after: Xinhai high tech Industrial Area in Fushan District in Shandong province Yantai city 264006 Street No. 188

Patentee after: SHANDONG XINHAI MINING TECHNOLOGY & EQUIPMENT Inc.

Address before: Xinhai high tech Industrial Area in Fushan District in Shandong province Yantai city 264006 Street No. 188

Patentee before: YANTAI XINHAI MINING MACHINERY Co.,Ltd.

TR01 Transfer of patent right

Effective date of registration: 20181019

Address after: 300450 Tianjin eco city animation road 126 anime building C area C3 area (TG 388th)

Patentee after: Xinhai (Tianjin) Electromechanical Technology Co.,Ltd.

Address before: 264006 188 Xinhai street, high tech Industrial Zone, Fushan District, Yantai, Shandong

Patentee before: SHANDONG XINHAI MINING TECHNOLOGY & EQUIPMENT INC.

TR01 Transfer of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140430

Termination date: 20211204

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