CN1923711A - Method of eliminating lead from nickel chloride solution - Google Patents

Method of eliminating lead from nickel chloride solution Download PDF

Info

Publication number
CN1923711A
CN1923711A CN 200610152789 CN200610152789A CN1923711A CN 1923711 A CN1923711 A CN 1923711A CN 200610152789 CN200610152789 CN 200610152789 CN 200610152789 A CN200610152789 A CN 200610152789A CN 1923711 A CN1923711 A CN 1923711A
Authority
CN
China
Prior art keywords
resin
chloride solution
nickel chloride
lead
solution
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.)
Pending
Application number
CN 200610152789
Other languages
Chinese (zh)
Inventor
范春龙
崔芸
梁承宇
李书山
田洪梅
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.)
Jinchuan Group Co Ltd
Original Assignee
Jinchuan Group 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 Jinchuan Group Co Ltd filed Critical Jinchuan Group Co Ltd
Priority to CN 200610152789 priority Critical patent/CN1923711A/en
Publication of CN1923711A publication Critical patent/CN1923711A/en
Pending legal-status Critical Current

Links

Abstract

The invention discloses a lead removing method in the nickel chloride solution through resin, which makes nickel chloride solution and D318 resin exchange ion to remove lead.

Description

A kind of method of eliminating lead from nickel chloride solution
Technical field
A kind of method of eliminating lead from nickel chloride solution relates to the method for removing impurity in a kind of chlorination medium, particularly removes method plumbous in the nickel chloride solution with resin.
Background technology
Usually adopt the chemical precipitation method deleading in the traditional technology, but this method is only applicable to the higher solution of lead content, and post precipitation still has a spot of lead (about 0.2g/l) to exist in solution, influence the quality of the finished product.Existing degree of depth method for removing lead adopts ion exchange resin usually, and FPA90, the FPA98 resin deleading effect in nickel chloride solution is bad, does not reach the production needs; The deleading of D363, D296 resin can produce a desired effect, but capacity is little, and qualifying liquid only is the twice of resin volume; D318, D331 resin capacity are big, and effect is better, but the D331 resin regeneration is when handling, and when adopting washing or washing back use acid treatment, effect is all undesirable, and regeneration is difficult, so D331 should not operate.
Summary of the invention
Purpose of the present invention is exactly the deficiency that exists at above-mentioned prior art, and a kind of method that can effectively reduce the lead in the nickelous chloride production system is provided.
The objective of the invention is to be achieved through the following technical solutions.
A kind of method of eliminating lead from nickel chloride solution is characterized in that nickel chloride solution and D318 resin carry out ion exchange lead removal.
The D318 resin is a Zeo-karb, and when nickel chloride solution process resin-column, lead ion in the solution and the hydrogen ion in the resin exchange, and the lead ion in the solution is adsorbed on the resin, thereby reaches the effect that reduces plumbum ion concentration in the solution.Lead can be reduced to below the 0.08g/l through the nickel chloride solution behind the D318 resin deleading.
The parsing of D318 resin is divided into washes nickel and two processes of regeneration, wash HCL solution that nickel adopts 0.1mol/L with 3 times of resin volumes/hour flow velocity through ion exchange column, the time of carrying out this operation is 2 hours; Use pure water or water of condensation during regeneration, with 4 times of resin volumes/hour flow velocity by resin-column, regeneration in 2 hours finishes.
The inventive method has realized the purpose of deleading from nickel chloride solution, makes that lead content satisfies the accuracy electroplate requirement in the nickelous chloride finished product.Resin regeneration is easy, and cost is low, can not cause environmental pollution.
Embodiment
A kind of method of nickel chloride solution resin deleading, sodium hydroxide solution with 4N passes through resin-column earlier, is alkalescence until solution, uses the pure water washing resin to neutral then, hydrochloric acid soln washing resin with 4N is acid until effusive solution again, uses the pure water washing resin to neutral again.With purify good nickel chloride solution with 1 times of resin volume/hour flow velocity by ion exchange column, the lead ion in the solution is adsorbed, adsorption cycle is 8 hours.After absorption finishes, the deleading resin is washed nickel operation, the HCL solution of 0.1mol/L with 3 times of resin volumes/hour flow velocity through ion exchange column, the time of carrying out this operation is 2 hours.The resin of washing behind the nickel will carry out regenerative operation, uses pure water or water of condensation during regeneration, with 4 times of resin volumes/hour flow velocity by resin-column, 2 hours these EOs, regeneration finishes.
Embodiment 1
Carry out ion-exchange through pretreated D318 resin and nickel chloride solution, nickel chloride solution is with the flow velocity process resin-column of 1 times of resin volume, and adsorption cycle is 8 hours.Wash the nickel operation then, the hydrochloric acid soln of 0.1mol/L approximately through two hours, is washed the nickel end of processing with the flow velocity process resin-column of 3 times of resin volumes.At last resin is regenerated, pure water is used in resin regeneration, and through resin-column, resin regeneration in about 2 hours finishes with 4 times of resin volumetric flow rates.
Liquid contrast g/l behind liquid, the deleading before the deleading
Liquid before the deleading Liquid behind the deleading Liquid before the deleading Liquid behind the deleading
0.065 0.0072 0.039 0.024
0.031 0.034 0.024 0.025
0.036 0.012 0.056 0.015
0.039 0.0024 0.078 0.042
0.030 0.019 0.0090 0.036
0.047 0.032 0.022 0.0017
0.026 0.0030 0.044 0.0065
0.034 0.0081 0.047 0.011
0.054 0.016 0.040 0.043
0.040 0.0044 0.0036 0.026
0.033 0.011 0.050 0.0082
0.038 0.0038 0.051 0.066
0.0072 0.0016 0.047 0.041
0.037 0.015 0.035 0.043
0.082 0.0017

Claims (1)

1. the method for an eliminating lead from nickel chloride solution is characterized in that nickel chloride solution and D318 resin carry out ion exchange lead removal.
CN 200610152789 2006-09-29 2006-09-29 Method of eliminating lead from nickel chloride solution Pending CN1923711A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200610152789 CN1923711A (en) 2006-09-29 2006-09-29 Method of eliminating lead from nickel chloride solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200610152789 CN1923711A (en) 2006-09-29 2006-09-29 Method of eliminating lead from nickel chloride solution

Publications (1)

Publication Number Publication Date
CN1923711A true CN1923711A (en) 2007-03-07

Family

ID=37816560

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200610152789 Pending CN1923711A (en) 2006-09-29 2006-09-29 Method of eliminating lead from nickel chloride solution

Country Status (1)

Country Link
CN (1) CN1923711A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100554168C (en) * 2007-09-07 2009-10-28 金川集团有限公司 A kind of method of removing iron from nickel chloride leachate
CN106587178A (en) * 2016-12-21 2017-04-26 金川集团股份有限公司 Zinc removing method of nickel chloride solution
CN110812888A (en) * 2019-10-23 2020-02-21 金川集团股份有限公司 Method for removing silicon by nickel solution adsorption

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100554168C (en) * 2007-09-07 2009-10-28 金川集团有限公司 A kind of method of removing iron from nickel chloride leachate
CN106587178A (en) * 2016-12-21 2017-04-26 金川集团股份有限公司 Zinc removing method of nickel chloride solution
CN110812888A (en) * 2019-10-23 2020-02-21 金川集团股份有限公司 Method for removing silicon by nickel solution adsorption

Similar Documents

Publication Publication Date Title
CN102417194B (en) Method for deeply removing magnesium through chelating resin for extracting lithium from salt lake brine
CN107324448B (en) Method for selective separation and comprehensive recovery of nickel in alkaline chemical nickel wastewater
CN101502742A (en) Method for removing thermostable salt in amine liquid for desulphurization
CN101519724A (en) Method for recovering nickel from low-nickel waste water
KR101806823B1 (en) METHOD FOR PRODUClNG AQUEOUS SOLUTION OF TETRAALKYL AMMONIUM SALT
CN102321802B (en) New method for extracting gallium from Bayer mother liquor through chelating resin
JP6185924B2 (en) Desalination method for boron-containing solution
CN104229859A (en) Method for removing iron impurities and gathering cupric ions in copper sulfate solution
CN203429003U (en) Tetramethyl ammonium hydroxide (TMAH) recycling device
CN1923711A (en) Method of eliminating lead from nickel chloride solution
CN101245486A (en) Method for removing aging copper foil plating solution detrimental impurities
CN101176565B (en) Method for reducing heavy metal plumbi content in sha ji fruit juice raw material by ion exchange process
CN1923345A (en) Process for removal of sulfate ions from organic amine absorbent
CN101618898A (en) Method for recovering gold, platinum and porpezite from acidic waste water by ion exchange
CN109929998A (en) A kind of regeneration method of copper-molybdenum saturated resin
CN101121550A (en) Method for removing anion surfactant from waste water
CN207376097U (en) A kind of electronickelling retracting device
TWI423836B (en) Process for recovering and purifying tetraalkyl ammonium hydroxide from waste solution containing the same
CN205999182U (en) Special Resin trundle bed acid-restoring plant
CN212127781U (en) Nickel recovery device for waste battery wastewater
CN209940667U (en) System for recycling acid liquor in acidic wastewater
CN110643818B (en) Method for recovering nickel from electroplating wastewater
CN203429267U (en) Tetramethyl ammonium hydroxide (TMAH) recycling device
CN1792819A (en) Process for purifying separating eliminating vanadium from ammonium molybdate solution
CN103961901B (en) A kind of method removing long-chain carboxylic acid's salt and hydrocarbon in alkanolamine solution

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication