CN105950887A - System and method for treating cadmium-bearing solution - Google Patents

System and method for treating cadmium-bearing solution Download PDF

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Publication number
CN105950887A
CN105950887A CN201610305874.7A CN201610305874A CN105950887A CN 105950887 A CN105950887 A CN 105950887A CN 201610305874 A CN201610305874 A CN 201610305874A CN 105950887 A CN105950887 A CN 105950887A
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CN
China
Prior art keywords
cadmium
conveyance conduit
containing solution
zinc powder
pipeline
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Pending
Application number
CN201610305874.7A
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Chinese (zh)
Inventor
陆业大
戴江洪
王鸿振
赵爱君
傅建国
申美玲
聂颖
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China ENFI Engineering Corp
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China ENFI Engineering Corp
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Publication date
Application filed by China ENFI Engineering Corp filed Critical China ENFI Engineering Corp
Priority to CN201610305874.7A priority Critical patent/CN105950887A/en
Publication of CN105950887A publication Critical patent/CN105950887A/en
Priority to PCT/CN2017/078657 priority patent/WO2017193725A1/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B19/00Obtaining zinc or zinc oxide
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/02Apparatus therefor
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/44Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
    • C22B3/46Treatment or purification of solutions, e.g. obtained by leaching by chemical processes by substitution, e.g. by cementation
    • 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

Abstract

The invention discloses a system and method for treating a cadmium-bearing solution. The system for treating the cadmium-bearing solution comprises a cadmium-bearing solution storage device, a first delivery pipeline, a feeding pump, a second delivery pipeline, a pipeline reactor and a zinc powder supply device, wherein the first delivery pipeline is connected with the cadmium-bearing solution storage device; the feeding pump is connected with the first delivery pipeline; the second delivery pipeline is connected with the feeding pump; the pipeline reactor is connected with the second delivery pipeline; and the zinc powder supply device is connected with at least one of the first delivery pipeline, the second delivery pipeline and the pipeline reactor. By the adoption of the system, the technological parameters in the replacement procedure can be optimized to a great extent, the continuity of original operation is guaranteed, and electric energy consumption and equipment investment caused by extra stirring are omitted.

Description

Process the system and method for cadmium-containing solution
Technical field
The invention belongs to chemical technology field, specifically, the present invention relates to a kind of system and method processing cadmium-containing solution.
Background technology
In tradition zinc hydrometallurgy clean liquid technique, use zinc powder to carrying out except impurity such as cadmiums, in design one containing cadmium soaks supernatant As use agitator tank as reaction vessel and promote in the way of strong mixing reaction carrying out.This mode solution and solid zinc powder Although granule can be fully contacted, but agitator tank stirring intensity is limited, causes the diffusion of solid zinc powder particles surrounding ions relatively Relatively slow, response speed is relatively slow, and zinc powder utilization rate is on the low side.Meanwhile, longer to cause causing cadmium metal to return in a large number molten the response time.
Therefore, the technique of existing process cadmium-containing solution is further improved.
Summary of the invention
It is contemplated that one of technical problem solved the most to a certain extent in correlation technique.To this end, the one of the present invention Purpose is to propose a kind of system and method processing cadmium-containing solution, and this system can obtain the optimization displacement operation of high degree Middle technological parameter, not only ensure that the seriality of original operation, and eliminates power consumption and the equipment that additional stirring causes Investment.
In one aspect of the invention, the present invention proposes a kind of system processing cadmium-containing solution, according to embodiments of the invention, This system includes:
Cadmium-containing solution storage device;
First conveyance conduit, described first conveyance conduit is connected with described cadmium-containing solution storage device;
Feed pump, described feed pump is connected with described first conveyance conduit;
Second conveyance conduit, described second conveyance conduit is connected with described feed pump;
Pipeline reactor, described pipeline reactor is connected with described second conveyance conduit;And
Zinc powder feedway, described zinc powder feedway and described first conveyance conduit, described second conveyance conduit and described pipe In road reactor at least one be connected.
Thus, the system processing cadmium-containing solution according to embodiments of the present invention is by using pipeline reactor to replace agitator tank to carry out Reaction, in course of reaction, provides power by feed pump so that fluid has high flow velocities, the turbulent flow of generation and turbulent flow energy High degree reduces solid zinc powder surface diffusion layer thickness, thus improves reacting dynamics condition and improve reaction efficiency, and then Can significantly improve the displacement efficiency of cadmium in cadmium-containing solution, after using this system, in each displacement operation, technological parameter is permissible simultaneously Obtain the optimization of high degree, not only ensure that the seriality of original operation, and eliminate the electric energy that additional stirring causes and disappear Consumption and equipment investment.
It addition, the system of process cadmium-containing solution according to the above embodiment of the present invention can also have a following additional technical characteristic:
In some embodiments of the invention, described pipeline reactor is helical pipe or straight pipeline.Thus, it is possible to significantly carry The turbulent flow of high fluid and turbulent extent, thus improve the displacement efficiency of cadmium in cadmium-containing solution.
In some embodiments of the invention, the elbow of described helical pipe is steel lining PE part or steel lining F4 part.
In some embodiments of the invention, on described first conveyance conduit and described second pipe, setting independently is at least One pipe-line mixer.Thus, it is possible to improve the displacement efficiency of cadmium in cadmium-containing solution further.
In another aspect of the present invention, the present invention proposes a kind of method processing cadmium-containing solution.Enforcement according to the present invention Example, the method is that the system using above-mentioned process cadmium-containing solution is carried out.According to a particular embodiment of the invention, the method bag Include:
By the cadmium-containing solution in described cadmium-containing solution storage device successively through described first conveyance conduit, described feed pump and described In second conveyance conduit supply extremely described pipeline reactor;
Zinc powder in described zinc powder feedway is supplied to described first conveyance conduit, described second conveyance conduit and described pipe At least one in road reactor, in order to make described zinc powder and cadmium ion generation reduction reaction in described cadmium-containing solution, obtain Cadmium slag and except liquid after cadmium.
Thus, the method processing cadmium-containing solution according to embodiments of the present invention is by using pipeline reactor to replace agitator tank to carry out Reaction, in course of reaction, provides power by feed pump so that fluid has high flow velocities, the turbulent flow of generation and turbulent flow energy High degree reduces solid zinc powder surface diffusion layer thickness, thus improves reacting dynamics condition and improve reaction efficiency, and then Can significantly improve the displacement efficiency of cadmium in cadmium-containing solution, after using the method, in each displacement operation, technological parameter is permissible simultaneously Obtain the optimization of high degree, not only ensure that the seriality of original operation, and eliminate the electric energy that additional stirring causes and disappear Consumption and equipment investment.
It addition, the method for process cadmium-containing solution according to the above embodiment of the present invention can also have a following additional technical characteristic:
In some embodiments of the invention, described zinc powder is in solid form or pulp form provides.
In some embodiments of the invention, the temperature of described reduction reaction is 60~90 degrees Celsius.
In some embodiments of the invention, the time of described reduction reaction is 1~10 minute.
In some embodiments of the invention, the use level coefficient of described zinc powder is 0.9~1.15.
The additional aspect of the present invention and advantage will part be given in the following description, and part will become bright from the following description Aobvious, or recognized by the practice of the present invention.
Accompanying drawing explanation
Above-mentioned and/or the additional aspect of the present invention and advantage will be apparent from from combining the accompanying drawings below description to embodiment With easy to understand, wherein:
Fig. 1 is the system structure schematic diagram processing cadmium-containing solution according to an embodiment of the invention.
Detailed description of the invention
Embodiments of the invention are described below in detail, and the example of described embodiment is shown in the drawings, the most identical Or similar label represents same or similar element or has the element of same or like function.Retouch below with reference to accompanying drawing The embodiment stated is exemplary, it is intended to is used for explaining the present invention, and is not considered as limiting the invention.
In describing the invention, it is to be understood that term " " center ", " longitudinally ", " laterally ", " length ", " width ", " thickness ", " on ", D score, "front", "rear", "left", "right", " vertically ", " level ", " top ", " end ", " interior ", " outward ", Orientation or the position relationship of the instruction such as " clockwise ", " counterclockwise ", " axially ", " radially ", " circumferential " are based on shown in the drawings Orientation or position relationship, be for only for ease of describe the present invention and simplify describe rather than instruction or hint indication device or Element must have specific orientation, with specific azimuth configuration and operation, be therefore not considered as limiting the invention.
Additionally, term " first ", " second " are only used for describing purpose, and it is not intended that instruction or hint relative importance or Person implies the quantity indicating indicated technical characteristic.Thus, define " first ", the feature of " second " can express or Implicitly include at least one this feature.In describing the invention, " multiple " are meant that at least two, such as two, Three etc., unless otherwise expressly limited specifically.
In the present invention, unless otherwise clearly defined and limited, term " install ", " being connected ", " connection ", the art such as " fixing " Language should be interpreted broadly, and connects for example, it may be fixing, it is also possible to be to removably connect, or integral;Can be machinery Connect, it is also possible to be electrical connection;Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary, can be two units Connection within part or the interaction relationship of two elements, unless otherwise clear and definite restriction.Ordinary skill for this area For personnel, above-mentioned term concrete meaning in the present invention can be understood as the case may be.
In the present invention, unless otherwise clearly defined and limited, fisrt feature second feature " on " or D score can be One directly contacts with second feature, or the first and second features are by intermediary mediate contact.And, fisrt feature is Two features " on ", " top " and " above " but fisrt feature directly over second feature or oblique upper, or be merely representative of first Characteristic level height is higher than second feature.Fisrt feature second feature " under ", " lower section " and " below " can be fisrt feature Immediately below second feature or obliquely downward, or it is merely representative of fisrt feature level height less than second feature.
In one aspect of the invention, the present invention proposes a kind of system processing cadmium-containing solution.With reference to Fig. 1, according to this The system processing cadmium-containing solution of inventive embodiments includes: cadmium-containing solution storage device the 100, first conveyance conduit 200, Feed pump the 300, second conveyance conduit 400, pipeline reactor 500 and zinc powder feedway 600.
According to embodiments of the invention, cadmium-containing solution storage device 100 is suitable to store cadmium-containing solution.It should be noted that " cadmium-containing solution storage device " herein can be for storing the dress of any structure of cadmium-containing solution in prior art Putting, people in the art can select according to actual needs.
According to embodiments of the invention, the first conveyance conduit 200 is connected with cadmium-containing solution storage device 100, and is suitable to Cadmium-containing solution is stored in each device that the cadmium-containing solution transport in device is follow-up.
According to a particular embodiment of the invention, the first conveyance conduit 200 can be provided with at least one pipe-line mixer (not shown), such as, can arrange multiple pipe-line mixer on the first conveyance conduit, contain such that it is able to significantly improve The turbulent flow of cadmium solution and turbulent extent, and then improve the displacement efficiency of cadmium in cadmium-containing solution.
According to embodiments of the invention, feed pump 300 is connected with the first conveyance conduit 200, and is suitable to improve follow-up second defeated Send the flow velocity of cadmium-containing solution fluid in pipeline and pipeline reactor, such that it is able to significantly improve turbulent flow and the turbulent flow journey of cadmium-containing solution Degree, and then improve the displacement efficiency of cadmium in cadmium-containing solution further.It should be noted that those skilled in the art can basis Actual fluid flow rate needs to select the particular type of feed pump.
According to embodiments of the invention, the second conveyance conduit 400 is connected with feed pump 300, and is suitable to pass through feed pump Cadmium-containing solution is delivered in follow-up pipeline reactor.
According to a particular embodiment of the invention, the second conveyance conduit 400 can be provided with at least one pipe-line mixer (not shown), such as, can arrange multiple pipe-line mixer on the second conveyance conduit, contain such that it is able to significantly improve The turbulent flow of cadmium solution and turbulent extent, and then improve the displacement efficiency of cadmium in cadmium-containing solution further.
According to embodiments of the invention, pipeline reactor 500 is connected with the second conveyance conduit 400, and is adapted so that containing cadmium molten Cadmium ion in liquid and zinc powder are fully contacted generation reduction reaction, thus obtain serosity, and can use according to actual needs The means such as filter pressing isolated can remove liquid and cadmium slag after cadmium.
A specific embodiment according to the present invention, pipeline reactor can be helical pipe or straight pipeline.Thus, it is possible to it is aobvious Write turbulent flow and the turbulent extent improving cadmium-containing solution fluid, thus ensure that the cadmium ion in cadmium-containing solution is fully contacted with zinc powder, And then the displacement efficiency of cadmium in raising cadmium-containing solution.It should be noted that those skilled in the art can be the most right The length of pipeline reactor selects, as long as can guarantee that in cadmium-containing solution, cadmium ion and zinc powder fully react.
According to another specific embodiment of the present invention, the elbow of helical pipe can be steel lining PE part or steel lining F4 part.By This, can significantly improve the service life of pipeline reactor.
According to embodiments of the invention, zinc powder feedway 600 can be with first conveyance conduit the 200, second conveyance conduit 400 With in pipeline reactor 500 at least one be connected, and be suitable to first conveyance conduit the 200, second conveyance conduit 400 and In pipeline reactor 500 at least one supply zinc powder, such as shown in 1, zinc powder feedway 600 and the first conveyance conduit 200, the second conveyance conduit 400 is all connected with pipeline reactor 500.
According to one embodiment of present invention, in zinc powder feedway, the supply form of zinc powder is not particularly restricted, this area Technical staff can select according to actual needs, according to a particular embodiment of the invention, zinc powder can in solid form or Pulp form provides.Thus, it is possible to ensure that zinc powder is fully contacted with cadmium ion in cadmium-containing solution, and then improve further containing cadmium The displacement efficiency of cadmium in solution.
According to still a further embodiment, the consumption of zinc powder is not particularly restricted, and those skilled in the art are permissible Selecting according to actual needs, according to a particular embodiment of the invention, the use level coefficient of zinc powder can be 0.9~1.15. Inventor finds, if the addition of zinc powder is crossed, I haven't seen you for ages causes purification and impurity removal incomplete, and in solution, impure element is high, and if zinc Powder addition too much can be relatively complete with remove impurity, but cause can be higher containing zinc in solution, and increases zinc powder consumption, increases cost.
According to still another embodiment of the invention, zinc powder is with the temperature of cadmium ion generation reduction reaction in cadmium-containing solution not Being particularly limited, those skilled in the art can select according to actual needs, according to a particular embodiment of the invention, Zinc powder can be 60~90 degrees Celsius with the temperature of cadmium ion generation reduction reaction in cadmium-containing solution.Inventor finds, should At a temperature of can significantly improve the displacement efficiency of cadmium ion in zinc powder and cadmium-containing solution, thus after ensureing that last gained is except cadmium In liquid, cadmium content is less than 10.5mg/L.
According to still another embodiment of the invention, zinc powder is with the time of cadmium ion generation reduction reaction in cadmium-containing solution not Being particularly limited, those skilled in the art can select according to actual needs, according to a particular embodiment of the invention, Zinc powder can be 1~10 minute with the time of cadmium ion generation reduction reaction in cadmium-containing solution.Inventor finds, this time In the range of can ensure that the cadmium ion in cadmium-containing solution fully reacts with zinc powder, thus improve cadmium in cadmium-containing solution further Displacement efficiency.
The system processing cadmium-containing solution according to embodiments of the present invention replaces agitator tank to react by employing pipeline reactor, In course of reaction, providing power by feed pump so that fluid has high flow velocities, the turbulent flow of generation and turbulent flow can very big journeys Degree reduces solid zinc powder surface diffusion layer thickness, thus improves reacting dynamics condition and improve reaction efficiency, and then can show Writing and improve the displacement efficiency of cadmium in cadmium-containing solution, after using this system, in each displacement operation, technological parameter can obtain pole simultaneously The optimization of big degree, not only ensure that the seriality of original operation, and eliminates power consumption that additional stirring causes and set Standby investment.
In the second aspect of the invention, the present invention proposes a kind of method processing cadmium-containing solution.Enforcement according to the present invention Example, the method is to use the above-mentioned system processing cadmium-containing solution to carry out.According to a particular embodiment of the invention, the method Including: cadmium-containing solution is stored the cadmium-containing solution in device and supplies through the first conveyance conduit, feed pump and the second conveyance conduit successively Give to pipeline reactor;Zinc powder in zinc powder feedway is supplied to the first conveyance conduit, the second conveyance conduit and pipeline At least one in reactor, in order to make zinc powder and cadmium ion generation reduction reaction in cadmium-containing solution, obtain cadmium slag and except cadmium Rear liquid.Inventor finds, by using pipeline reactor to replace agitator tank to react, in course of reaction, passes through feed pump Thering is provided power so that fluid has high flow velocities, the turbulent flow of generation and turbulent flow energy high degree reduce solid zinc powder diffusion into the surface Layer thickness, thus improve reacting dynamics condition and improve reaction efficiency, and then putting of cadmium in cadmium-containing solution can be significantly improved Changing efficiency, after using the method, in each displacement operation, technological parameter can obtain the optimization of high degree, not only ensures simultaneously The seriality of original operation, and eliminate power consumption and the equipment investment that additional stirring causes.It should be noted that The above-mentioned method being equally applicable to this process cadmium-containing solution for the feature and advantage described by the system of process cadmium-containing solution, this Place repeats no more.
According to one embodiment of present invention, the supply form of zinc powder is not particularly restricted, and those skilled in the art can root Select according to being actually needed, according to a particular embodiment of the invention, zinc powder can with in solid form or pulp form provide. Thus, it is possible to ensure that zinc powder is fully contacted with cadmium ion in cadmium-containing solution, and then improve the displacement of cadmium in cadmium-containing solution further Efficiency.
According to one embodiment of present invention, in zinc powder feedway, the supply form of zinc powder is not particularly restricted, this area Technical staff can select according to actual needs, according to a particular embodiment of the invention, zinc powder can in solid form or Pulp form provides.Thus, it is possible to ensure that zinc powder is fully contacted with cadmium ion in cadmium-containing solution, and then improve further containing cadmium The displacement efficiency of cadmium in solution.
According to still a further embodiment, the consumption of zinc powder is not particularly restricted, and those skilled in the art are permissible Selecting according to actual needs, according to a particular embodiment of the invention, the use level coefficient of zinc powder can be 0.9~1.15. Inventor finds, if the addition of zinc powder is crossed, I haven't seen you for ages causes purification and impurity removal incomplete, and in solution, impure element is high, and if zinc Powder addition too much can be relatively complete with remove impurity, but cause can be higher containing zinc in solution, and increases zinc powder consumption, increases cost.
According to still another embodiment of the invention, zinc powder is with the temperature of cadmium ion generation reduction reaction in cadmium-containing solution not Being particularly limited, those skilled in the art can select according to actual needs, according to a particular embodiment of the invention, Zinc powder can be 60~90 degrees Celsius with the temperature of cadmium ion generation reduction reaction in cadmium-containing solution.Inventor finds, should At a temperature of can significantly improve the displacement efficiency of cadmium ion in zinc powder and cadmium-containing solution, thus after ensureing that last gained is except cadmium In liquid, cadmium content is less than 10.5mg/L.
According to still another embodiment of the invention, zinc powder is with the time of cadmium ion generation reduction reaction in cadmium-containing solution not Being particularly limited, those skilled in the art can select according to actual needs, according to a particular embodiment of the invention, Zinc powder can be 1~10 minute with the time of cadmium ion generation reduction reaction in cadmium-containing solution.Inventor finds, this time In the range of can ensure that the cadmium ion in cadmium-containing solution fully reacts with zinc powder, thus improve cadmium in cadmium-containing solution further Displacement efficiency.
Below with reference to specific embodiment, present invention is described, it should be noted that these embodiments are the most descriptive , and limit the present invention never in any form.
Embodiment 1
By 1m3Two-stage nitration passes sequentially through the first conveyance conduit, feed pump and the second conveying pipe except the gained cadmium-containing solution after nickel cobalt Road supplies to pipeline reactor, simultaneously anti-to the first conveyance conduit, the second conveyance conduit and pipeline by zinc powder feedway Answer supply zinc powder in device so that zinc powder and the cadmium ion in cadmium-containing solution occur reduction reaction, reaction temperature in pipeline reactor Degree is 80 DEG C, and the response time is 5min, and zinc powder use level coefficient is 0.9, and reaction gained serosity is carried out filter pressing process, To except in liquid after cadmium cadmium content less than 1mg/L.
Embodiment 2
By 1m3Two-stage nitration passes sequentially through the first conveyance conduit, feed pump and the second conveying pipe except the gained cadmium-containing solution after nickel cobalt Road supplies to pipeline reactor, simultaneously anti-to the first conveyance conduit, the second conveyance conduit and pipeline by zinc powder feedway Answer supply zinc powder in device so that zinc powder and the cadmium ion in cadmium-containing solution occur reduction reaction, reaction temperature in pipeline reactor Degree is 80 DEG C, and the response time is 2min, and zinc powder use level coefficient is 0.9, and reaction gained serosity is carried out filter pressing process, To except in liquid after cadmium cadmium content less than 10.2mg/L.
In the description of this specification, reference term " embodiment ", " some embodiments ", " example ", " concrete example ", Or specific features, structure, material or the feature bag that the description of " some examples " etc. means to combine this embodiment or example describes It is contained at least one embodiment or the example of the present invention.In this manual, to the schematic representation of above-mentioned term necessarily It is directed to identical embodiment or example.And, the specific features of description, structure, material or feature can be arbitrary Individual or multiple embodiment or example combine in an appropriate manner.Additionally, in the case of the most conflicting, the skill of this area The feature of the different embodiments described in this specification or example and different embodiment or example can be combined by art personnel And combination.
Although above it has been shown and described that embodiments of the invention, it is to be understood that above-described embodiment is exemplary, Being not considered as limiting the invention, those of ordinary skill in the art within the scope of the invention can be to above-described embodiment It is changed, revises, replaces and modification.

Claims (9)

1. the system processing cadmium-containing solution, it is characterised in that including:
Cadmium-containing solution storage device;
First conveyance conduit, described first conveyance conduit is connected with described cadmium-containing solution storage device;
Feed pump, described feed pump is connected with described first conveyance conduit;
Second conveyance conduit, described second conveyance conduit is connected with described feed pump;
Pipeline reactor, described pipeline reactor is connected with described second conveyance conduit;And
Zinc powder feedway, described zinc powder feedway and described first conveyance conduit, described second conveyance conduit and described pipe In road reactor at least one be connected.
System the most according to claim 1, it is characterised in that described pipeline reactor is helical pipe or straight pipeline.
System the most according to claim 2, it is characterised in that the elbow of described helical pipe is steel lining PE part or steel Lining F4 part.
4. according to the system according to any one of right 1-3, it is characterised in that described first conveyance conduit and described second pipe On road independently at least one pipe-line mixer is set.
5. utilize the method that the system processing cadmium-containing solution according to any one of claim 1-4 processes cadmium-containing solution, It is characterized in that, including:
By the cadmium-containing solution in described cadmium-containing solution storage device successively through described first conveyance conduit, described feed pump and described In second conveyance conduit supply extremely described pipeline reactor;
Zinc powder in described zinc powder feedway is supplied to described first conveyance conduit, described second conveyance conduit and described pipe At least one in road reactor, in order to make described zinc powder and cadmium ion generation reduction reaction in described cadmium-containing solution, obtain Cadmium slag and except liquid after cadmium.
Method the most according to claim 5, it is characterised in that described zinc powder is in solid form or pulp form provides.
7. according to the method described in claim 5 or 6, it is characterised in that the temperature of described reduction reaction is 60~90 Celsius Degree.
Method the most according to claim 7, it is characterised in that the time of described reduction reaction is 1~10 minute.
Method the most according to claim 6, it is characterised in that the use level coefficient of described zinc powder is 0.9~1.15.
CN201610305874.7A 2016-05-10 2016-05-10 System and method for treating cadmium-bearing solution Pending CN105950887A (en)

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PCT/CN2017/078657 WO2017193725A1 (en) 2016-05-10 2017-03-29 System and method for treating cadmium-containing solution

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CN102719671A (en) * 2012-07-06 2012-10-10 中南大学 Method and device for deeply removing copper of nickel thiocarbonate from nickel-containing solution
CN202658207U (en) * 2012-07-06 2013-01-09 中南大学 Device for deeply removing copper from nickel-containing solution by nickel thiocarbonate

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WO2017193725A1 (en) * 2016-05-10 2017-11-16 中国恩菲工程技术有限公司 System and method for treating cadmium-containing solution

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