CN207659532U - A kind of device recycling mercury from mercurial soot - Google Patents
A kind of device recycling mercury from mercurial soot Download PDFInfo
- Publication number
- CN207659532U CN207659532U CN201721925421.0U CN201721925421U CN207659532U CN 207659532 U CN207659532 U CN 207659532U CN 201721925421 U CN201721925421 U CN 201721925421U CN 207659532 U CN207659532 U CN 207659532U
- Authority
- CN
- China
- Prior art keywords
- filter
- conveyer
- mercury
- filter plate
- mercurial soot
- 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
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Electrolytic Production Of Metals (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model provides a kind of device recycling mercury from mercurial soot, it is made of water scrubber, hydraulic rotator, filter and electrolyzer, electrolyzer includes the holder composition of pedestal, electrolytic cell and its anode and cathode, deflecting roller, conveyer and fixed deflecting roller, and water scrubber includes the reciprocating filter plate, the nozzle of filter plate top setting and the waste liquid storage tank of filter plate bottom setting connected between raw material dispensing machines, at least two groups washing wheel, the fixed frame of washing wheel bottom connection, washing wheel；The hydrocyclone includes concentrator bowl and connects the driving motor of concentrator bowl, and concentrator bowl top is equipped with feed inlet, and lower part is equipped with discharge port, and feed inlet connects setting with filter plate；The filter is fixed on the discharge port lower part by rack, and the filter horizontal direction connects with the conveyer, and filter lower part is additionally provided with mercury solution collecting box；The utility model carries out tertiary treatment to mercurial soot, is suitable for the recovery processing of the mercurial soot mercury containing different impurities, improves the recovery rate of mercurial soot recycling mercury, increases equipment use scope, improve economic benefit.
Description
Technical field
The utility model belongs to mercurous waste processing arts, and in particular to a kind of application wet method recycles mercury from mercurial soot
Three-level core processing be core equipment.
Background technology
It can be generated by small globule, thin mine dust, arsenic sb oxide, hydrocarbon, moisture, mercuric sulphide, sulphur during refining mercury
The unconsolidated material of the compositions such as sour mercury, that is, mercurial soot, using the useless mercury recovery process of tradition, are steamed because the content of mercury in mercurial soot is very high
It evaporates method and waste slag containing mercury is first subjected to chemical pretreatment, then place it in retort, heating makes mercury volatilize, condensed recycling metal
Mercury.The technical maturity is high, and different preprocess methods can be taken for the form of mercury in waste residue, can gold in high efficiente callback waste residue
Belong to mercury.But there are secondary pollutions for the way of distillation.The prior art carries out mercurial soot processing recycling mercury using electrolysis wet method, because miscellaneous in mercurial soot
Matter content is high, can straight line decline for the mercurial soot electrolysis handling rate of different impurities content.
Utility model content
The purpose of this utility model is：A kind of device recycling mercury from mercurial soot is provided, is suitable for containing different impurities
The recovery processing of mercurial soot mercury, while improving the recovery rate that mercury is recycled from mercurial soot.
To achieve the goals above, the technical scheme adopted by the utility model is that：
A kind of device recycling mercury from mercurial soot, including electrolyzer, electrolyzer is by pedestal, electrolytic cell and its anode and the moon
Pole, deflecting roller, the conveyer connected on deflecting roller and fixed deflecting roller holder composition；The anode and cathode is equidistantly arranged up and down
Row, anode are arranged in upper, cathode under, and cathode and anode correspondence are positioned in cell bath, and the cathode is copper；It is flat
The transmission chain of the synchronous setting of row forms conveyer, and the conveyer is closed setting, cell wall in a ring in the periphery of electrolytic cell
On the deflecting roller of conveyer is installed, deflecting roller is fixedly connected with holder, and at least one set of material pot is hung on the conveyer
And it is set to the separator of conveyer end；Further include water scrubber, hydrocyclone and filter, the water scrubber includes raw material
Dispensing machines, at least two groups washing are taken turns, the fixed frame of bottom connection is taken turns in washing, on the reciprocating filter plate that washing connects between taking turns, filter plate
The nozzle of portion's setting and the waste liquid storage tank of filter plate bottom setting；The hydrocyclone includes concentrator bowl and connection concentrator bowl
Driving motor, concentrator bowl top is equipped with feed inlet, and lower part is equipped with discharge port, and feed inlet connects setting with filter plate；The filtering
Machine is fixed on the discharge port lower part by rack, and the filter horizontal direction connects with the conveyer, and filter lower part is also
Equipped with mercury solution collecting box.
The beneficial effects of the utility model are：Mercurial soot tertiary treatment, front and continued dispose most of flue dust, subsequent classification into
The conveyer of row processing, annular design makes the recyclable reciprocal constantly processing of mercurial soot processing, improves the applicable model of mercurial soot impurity treatment
It encloses, improves the recovery rate of mercurial soot recycling mercury, meanwhile, accelerate mercury recovery rate in mercurial soot.
Further, above-mentioned a kind of device recycling mercury from mercurial soot, the electrolyte in the electrolytic cell be sodium hydroxide,
Sodium sulphate, vulcanized sodium composite solution, because electrode plate cathode is copper, therefore solution must have the metal sprinkled than work in copper, Cai Neng
Free electron is formed in solution, sodium element belongs to more active one kind, and relative price is also cheap, and practical and economy is all preferable.
Further, a kind of above-mentioned device recycling mercury from mercurial soot, the filter surface are provided with thin layer filter plate, can
The mercury solution body recycled in hydrocyclone is filtered out, retains mercurial soot part and enters next process.
Further, a kind of above-mentioned device recycling mercury from mercurial soot, the material pot are stainless steel, material pot
Filtered mercurial soot is carry into electrolytic cell with conveyer to enter in cell bath, cell bath is alkalies
Body, stainless steel can play good corrosion-resisting function, improve product service life.
Description of the drawings
Fig. 1 is a kind of structural schematic diagram for the device recycling mercury from mercurial soot of the utility model embodiment.
Specific implementation mode
Below by the further details of explanation of specific implementation mode：
Reference numeral in Figure of description includes：Electrolyzer 1, water scrubber 2, hydrocyclone 3, filter 4, mercury solution are received
Header 5, transmission chain 6, electrolytic cell 11, anode 12, cathode 13, conveyer 14, material pot 15, holder 16, separator 17, pedestal
18, deflecting roller 19, cell bath 20, washing wheel 21, filter plate 22, fixed frame 23, nozzle 24, waste liquid storage tank 25, raw material are matched
Send machine 26, concentrator bowl 31, feed inlet 32, driving motor 33, discharge port 34, thin layer filter plate 41, rack 42.
Embodiment is substantially as shown in Fig. 1：
A kind of device recycling mercury from mercurial soot, including electrolyzer 1, electrolyzer 1 is by pedestal 18, electrolytic cell 11 and its anode
12 and cathode 13, deflecting roller 19, the conveyer 14 connected on deflecting roller 19 and fixed deflecting roller 19 holder 16 form, anode 12
It is equidistantly arranged above and below with cathode 13, anode 12 is arranged in upper, cathode 13 under, and cathode 13 and the correspondence of anode 12 are positioned over electrolytic cell
In electrolyte 20, cathode 13 is copper；The transmission chain 6 of parallel synchronous setting forms conveyer 14, and conveyer 14 is in electrolytic cell 11
Periphery be closed setting in a ring, the deflecting roller 19 of conveyer 14 is installed, deflecting roller 19 is solid with holder 16 on 11 wall of electrolytic cell
It is fixed to connect, it is hung at least one set of material pot 15 on conveyer 14 and is set to the separator 17 of 14 end of conveyer；Further include
Water scrubber 2, hydrocyclone 3 and filter 4, water scrubber 2 include raw material dispensing machines 26, at least two groups washing wheel 21, washing wheel
21 bottoms connection fixed frame 23, washing wheel 21 between connect reciprocating filter plate 22,22 top of filter plate setting nozzle 24 and
The waste liquid storage tank 25 of 22 bottom of filter plate setting；Hydrocyclone 3 includes concentrator bowl 31 and connects the driving motor of concentrator bowl 31
33,31 top of concentrator bowl is equipped with feed inlet 32, and lower part is equipped with discharge port 34, and feed inlet 32 connects setting with filter plate 22；Filter 4
It is fixed on 34 lower part of the discharge port by rack 42,4 horizontal direction of filter connects with the conveyer 14,4 lower part of filter
It is additionally provided with mercury solution collecting box 5.
The step of mercury is recycled in mercurial soot is as follows：
1, feedstock delivery to washing is taken turns on the reciprocating filter plate 22 of 21 connections by raw material dispensing machines 26,22 top of filter plate
For the nozzle 24 of setting to being sprayed by the mercurial soot of lower part, the step can remove most of impurity in mercurial soot, gradually divide
Separate out the mercury for being easy to polymerization.
2, mercurial soot is distributed to after over cleaning in 31 feed inlet 32 of concentrator bowl to connect with filter plate 22, after charging, is closed
Feed inlet 32 is closed, driving motor 33 is started, under the action of the centrifugal, small globule is broken by extruding, friction, mutually shock, film
Bad, mercury therein converges into big mercury drop and is separated.
3, after timing eddy flow, driving motor 33 is closed, opens 31 discharge port 34 of concentrator bowl of hydrocyclone 3, eddy flow is good
Material enter in filter 4, filter 4 filter out the mercury that eddy flow goes out and be thrown to bottom setting mercury solution collecting box 5 in.
4, mercurial soot is not detached to enter on the conveyer 14 of electrolyzer 1 to connect and be distributed in material pot 15, then around
The pool conveyer 14 that electrolytic cell 11 is arranged drives lower enter in cell bath 20 and after the reaction of lye, in mercurial soot
Mercury is reduced out, and precipitates in electrolytic cell 11, then extracts again.
Further increase the program：Electrolyte in electrolytic cell 11 is sodium hydroxide, sodium sulphate, vulcanized sodium composite solution,
Because electrode plate cathode 13 is copper, therefore solution must have the metal sprinkled than work in copper, could form free electron, sodium in the solution
Element belongs to more active one kind, and relative price is also cheap, and practical and economy is all preferable；4 surface of filter is provided with thin layer
Filter plate 41 may filter that the mercury solution body recycled in hydrocyclone 3, retains mercurial soot part and enters next process；Material pot 15
For stainless steel, material pot 15 carries filtered mercurial soot into electrolytic cell 11 and enters electrolytic tank electrolysis with conveyer 14
In liquid 20, cell bath 20 is akaline liquid, and stainless steel can play good corrosion-resisting function, and improving product makes
Use the service life.
Above-described is only the embodiments of the present invention, and the common sense such as well known concrete structure and characteristic are herein in scheme
It does not describe excessively.It should be pointed out that for those skilled in the art, in the premise for not departing from the utility model structure
Under, several modifications and improvements can also be made, these should also be considered as the scope of protection of the utility model, these are not all interfered with
The effect and patent practicability that the utility model is implemented.This application claims protection domain should be with the content of its claim
Subject to, the records such as specific implementation mode in specification can be used for explaining the content of claim.
Claims (4)
1. a kind of device recycling mercury from mercurial soot, including electrolyzer, electrolyzer by pedestal, electrolytic cell and its anode and cathode,
The holder composition of the conveyer and fixed deflecting roller that are connected on deflecting roller, deflecting roller；It is characterized in that：Described anode and cathode etc.
Away from being arranged above and below, anode is arranged in upper, cathode under, and cathode and anode correspondence are positioned in cell bath, the cathode
It is copper；The transmission chain of parallel synchronous setting forms conveyer, and the conveyer is closed setting in a ring in the periphery of electrolytic cell,
The deflecting roller of conveyer is installed, deflecting roller is fixedly connected with holder, and at least one is hung on the conveyer in cell wall
Group material pot and the separator for being set to conveyer end；Further include water scrubber, hydrocyclone and filter, the water scrubber
Including the reciprocating filter connected between raw material dispensing machines, at least two groups washing wheel, the fixed frame of washing wheel bottom connection, washing wheel
The waste liquid storage tank of plate, the nozzle of filter plate top setting and the setting of filter plate bottom；The hydrocyclone include concentrator bowl and
The driving motor of concentrator bowl is connected, concentrator bowl top is equipped with feed inlet, and lower part is equipped with discharge port, and feed inlet is connected with filter plate
It sets；The filter is fixed on the discharge port lower part by rack, and the filter horizontal direction connects with the conveyer, mistake
Filter lower part is additionally provided with mercury solution collecting box.
2. a kind of device recycling mercury from mercurial soot according to claim 1, it is characterised in that：Electricity in the electrolytic cell
Solution liquid is sodium hydroxide, sodium sulphate, vulcanized sodium composite solution.
3. a kind of device recycling mercury from mercurial soot according to claim 1, it is characterised in that：The filter surface is set
It is equipped with thin layer filter plate.
4. a kind of device recycling mercury from mercurial soot according to claim 1, it is characterised in that：The material pot is stainless
Steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721925421.0U CN207659532U (en) | 2017-12-29 | 2017-12-29 | A kind of device recycling mercury from mercurial soot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721925421.0U CN207659532U (en) | 2017-12-29 | 2017-12-29 | A kind of device recycling mercury from mercurial soot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207659532U true CN207659532U (en) | 2018-07-27 |
Family
ID=62944772
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721925421.0U Expired - Fee Related CN207659532U (en) | 2017-12-29 | 2017-12-29 | A kind of device recycling mercury from mercurial soot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207659532U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115011819A (en) * | 2022-08-05 | 2022-09-06 | 北京博朗德科技有限公司 | Multistage filter-pressing rupture of membranes mercury purification device |
-
2017
- 2017-12-29 CN CN201721925421.0U patent/CN207659532U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115011819A (en) * | 2022-08-05 | 2022-09-06 | 北京博朗德科技有限公司 | Multistage filter-pressing rupture of membranes mercury purification device |
| CN115011819B (en) * | 2022-08-05 | 2022-10-28 | 北京博朗德科技有限公司 | Multistage filter-pressing rupture of membranes mercury purification device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11339456B2 (en) | Separating and melting system and method for waste lead grid in waste lead acid storage battery recycling | |
| CN104282962B (en) | The recovery method of waste and old lithium ionic cell electrolyte | |
| CN102453931A (en) | Technology for treating and purifying copper electrolyte by vortex electrolysis | |
| CN108220999A (en) | A kind of device for recycling cadmium containing the method that cadmium is recycled in cadmium fumes and from cadmium-ammonia solution from metallurgy | |
| CN108910966B (en) | Method for extracting tungsten carbide and cobalt from waste hard alloy | |
| CN207659532U (en) | A kind of device recycling mercury from mercurial soot | |
| CN208104505U (en) | A kind of waste lithium cell recycling pretreatment unit | |
| CN107196005A (en) | Method for recovering waste lead storage battery | |
| CN210546969U (en) | Waste battery recycling and reusing separation equipment | |
| CN204471097U (en) | The separating cycle structure of a kind of cooling fluid and processing waste material | |
| CN1808761A (en) | Clean recovery method of lead from waste storage cells by acidic electrolyzing and in-situ deoxidation in solid phase through wet process | |
| CN106756010A (en) | The method that fluorine in solution of zinc sulfate is removed after the roasting of zinc metallurgy white residue | |
| CN104988537B (en) | The wet dust collector and leaching electrodeposition integral process of a kind of solidification disposal of waste containing zinc | |
| CN102296325B (en) | Process for treating waste lead accumulator through continuous solid phase electrolysis of rotating cathode | |
| WO2017031949A1 (en) | Method for leaching low-grade lead-zinc oxide ores by means of electrooxidation, and leaching device thereof | |
| CN212476214U (en) | Diaphragm electrolysis device for treating copper passivation waste liquid | |
| CN102676824A (en) | Electronic pin copper-tin-iron separation device and electronic pin copper-tin-iron separation method | |
| CN107217150A (en) | The method and apparatus of secondary zinc oxide removal of impurities concentration of valuable metals zinc | |
| CN101008089A (en) | Electrodeposit cobalt method for insoluble anode | |
| CN212292842U (en) | Integrated system for directly preparing mercury oxide from mercury-containing organic sludge | |
| CN212293695U (en) | System for recovering gold, silver and copper from high-silver-copper gold-loaded carbon desorption electrolysis waste liquid | |
| CN212925127U (en) | Recovery device for valuable metals in scrap copper electrolysis anode mud | |
| CN211339391U (en) | Oil product alkaline washing purification device of waste tire cracking and deslagging system | |
| CN108620229B (en) | Separating device and method for separating copper part terminals from lead ash | |
| CN216856179U (en) | Naphthalene knot piece and packaging process tail gas recovery system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180727 Termination date: 20201229 |