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CN114836624A - Calcium removal method for chloride or sulfate solution - Google Patents

Calcium removal method for chloride or sulfate solution Download PDF

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Publication number
CN114836624A
CN114836624A CN202210417031.1A CN202210417031A CN114836624A CN 114836624 A CN114836624 A CN 114836624A CN 202210417031 A CN202210417031 A CN 202210417031A CN 114836624 A CN114836624 A CN 114836624A
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additive
solution
sulfate
chloride
calcium
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许开华
胡意
彭亚光
刘炼
肖汀汀
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Jingmen GEM New Material Co Ltd
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Jingmen GEM New Material Co Ltd
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    • 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
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0063Hydrometallurgy
    • C22B15/0084Treating solutions
    • C22B15/0089Treating solutions by chemical methods
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0453Treatment or purification of solutions, e.g. obtained by leaching
    • C22B23/0461Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B47/00Obtaining manganese

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

本发明公开了一种氯化盐或者硫酸盐溶液的除钙方法,包括:向氯化盐或者硫酸盐溶液中加入稀碱控制pH2‑5,加热至85℃‑95℃;向溶液中加入添加剂A和添加剂B或者只加入添加剂B,所述添加剂A为无水硫酸钠,所述添加剂B为无水硫酸钙;通过保温蒸发浓缩20%‑30%的水后固液分离。在处理该含钙溶液时能高效的去除溶液中的钙,且有价金属无损失,处理过程简单、安全、环保、无危害、成本低。The invention discloses a method for removing calcium from chloride salt or sulfate solution, comprising: adding dilute alkali to the chloride salt or sulfate solution to control pH 2-5, heating to 85°C-95°C; adding additives to the solution A and additive B or only add additive B, the additive A is anhydrous sodium sulfate, and the additive B is anhydrous calcium sulfate; the solid-liquid separation is performed after concentrating 20%-30% of water by thermal insulation evaporation. When the calcium-containing solution is processed, the calcium in the solution can be efficiently removed, and the valuable metal is not lost, and the processing process is simple, safe, environmentally friendly, harmless, and low in cost.

Description

一种氯化盐或者硫酸盐溶液的除钙方法A kind of calcium removal method of chloride salt or sulfate solution

技术领域technical field

本发明涉及化学除杂技术领域,具体涉及一种氯化盐或者硫酸盐溶液的除钙方法。The invention relates to the technical field of chemical impurity removal, in particular to a method for removing calcium from chloride or sulfate solution.

背景技术Background technique

目前含镍、钴、锰或者铜的氯化盐溶液或者硫酸盐溶液除钙方法,采取先加硫酸钠初除钙然后再加氟化钠精除钙,该方法会导致废水以及成品液中氟离子超标,溶液无法达到下游质量要求,同时给废水处理带来很大困难和排放废水氟超标风险。此外,CN113023751A公开了一种从氯化盐水中回收钙的方法,首先通过控制溶液的酸碱度,针对不同氢氧化物的沉淀区间,在不同的pH范围条件下实现对Mg(OH)2和Ca(OH)2的分离,再采用反渗透或蒸发结晶等方法,对溶液进行浓缩,达到氯化盐水中脱除钙的目的,该方法工艺过程复杂、成本高。At present, the calcium removal method of chloride salt solution or sulfate solution containing nickel, cobalt, manganese or copper is to add sodium sulfate to remove calcium first and then add sodium fluoride to remove calcium. This method will lead to fluorine in wastewater and finished liquid. If the ions exceed the standard, the solution cannot meet the downstream quality requirements, and at the same time, it brings great difficulties to the wastewater treatment and the risk of fluorine exceeding the standard in the discharged wastewater. In addition, CN113023751A discloses a kind of method for recovering calcium from chlorinated brine. First, by controlling the pH of the solution, for the precipitation interval of different hydroxides, under different pH range conditions, Mg(OH) 2 and Ca ( The separation of OH) 2 , and then adopt methods such as reverse osmosis or evaporative crystallization to concentrate the solution to achieve the purpose of removing calcium in the chlorinated brine, which is complicated in process and high in cost.

发明内容SUMMARY OF THE INVENTION

针对上述已有技术存在的不足,本发明提供一种氯化盐或者硫酸盐溶液的除钙方法,是满足不引入氟离子,以及后续要求的低成本除钙方法。In view of the deficiencies in the above-mentioned prior art, the present invention provides a method for removing calcium from chloride or sulfate solution, which is a low-cost method for removing calcium without introducing fluoride ions and subsequent requirements.

本发明是通过以下技术方案实现的。The present invention is achieved through the following technical solutions.

一种氯化盐或者硫酸盐溶液的除钙方法,其特征在于,所述方法包括:A method for removing calcium from chloride or sulfate solution, wherein the method comprises:

(1)向氯化盐或者硫酸盐溶液中加入稀碱控制pH2-5,加热搅拌至85℃-95℃;(1) adding dilute alkali to the chloride salt or sulfate solution to control pH 2-5, heating and stirring to 85 ℃-95 ℃;

(2)向经步骤(1)得到的溶液中加入添加剂A和添加剂B或者只加入添加剂B,所述添加剂A为无水硫酸钠,所述添加剂B为无水硫酸钙;(2) Add additive A and additive B or only add additive B to the solution obtained through step (1), and described additive A is anhydrous sodium sulfate, and described additive B is anhydrous calcium sulfate;

(3)通过保温蒸发浓缩20%-30%的水后固液分离。(3) Solid-liquid separation after concentrating 20%-30% of water by thermal insulation evaporation.

进一步地,所述氯化盐溶液为氯化锰、氯化钴、氯化镍、氯化铜溶液中的一种;所述硫酸盐溶液为硫酸镍、硫酸铜、硫酸锰、硫酸钴溶液中的一种。Further, the chloride salt solution is one of manganese chloride, cobalt chloride, nickel chloride, and cupric chloride solution; the sulfate solution is nickel sulfate, copper sulfate, manganese sulfate, and cobalt sulfate solution. a kind of.

进一步地,所述稀碱浓度为4-16%。Further, the dilute alkali concentration is 4-16%.

进一步地,所述步骤(2)添加剂A、添加剂B分别的加入量为50-80g/L、2-8g/L(即添加剂A的加入量为每升氯化盐或者硫酸盐溶液加入50-80g,添加剂B的加入量为每升氯化盐或者硫酸盐溶液加入2-8g)。Further, the respective additions of the additive A and the additive B in the step (2) are 50-80g/L, 2-8g/L (that is, the addition of the additive A is that every liter of chloride or sulfate solution adds 50- 80g, the addition amount of additive B is 2-8g per liter of chloride salt or sulfate solution).

进一步地,所述步骤(2)向经步骤(1)得到的氯化盐溶液中加入添加剂A和添加剂B,其添加的过程为:先加入添加剂A反应10-30min后,再加入添加剂B。Further, in the step (2), the additive A and the additive B are added to the chloride salt solution obtained in the step (1).

进一步地,所述步骤(2)向经步骤(1)得到的硫酸盐溶液中只加入添加剂B。Further, in the step (2), only the additive B is added to the sulfate solution obtained in the step (1).

本发明的有益技术效果,本发明提供了一种氯化盐或者硫酸盐溶液的除钙方法,处理后液中Ca小于100mg/L,在处理该含钙溶液时能高效的去除溶液中的钙,且有价金属无损失,处理过程简单、安全、环保、无危害、成本低。The beneficial technical effect of the present invention is that the present invention provides a method for removing calcium from a chloride or sulfate solution. The Ca in the treated solution is less than 100 mg/L, and the calcium in the solution can be efficiently removed when the calcium-containing solution is treated. , and there is no loss of valuable metals, the treatment process is simple, safe, environmentally friendly, harmless, and low in cost.

具体实施方式Detailed ways

下面结合具体实施方式对本发明进行详细说明。The present invention will be described in detail below with reference to specific embodiments.

实施例1Example 1

取氯化锰溶液1L,加浓度为16%稀碱回调至pH3.5,稳定pH后继续加热搅拌30分钟,其中,溶液加热升温至85℃,加入无水硫酸钠80g反应10min后,再加入无水硫酸钙8g,继续搅拌,溶液经保温蒸发浓缩至800ml,过滤,取样检测前后溶液钙含量,前液钙6.33g/l,后液钙31.1mg/l。Take 1 L of manganese chloride solution, add 16% dilute alkali to adjust to pH 3.5, and continue heating and stirring for 30 minutes after stabilizing the pH, wherein the solution is heated to 85 ° C, and 80 g of anhydrous sodium sulfate is added to react for 10 minutes, and then add Anhydrous calcium sulfate 8g, continue to stir, the solution is evaporated and concentrated to 800ml by thermal insulation, filtered, and the calcium content of the solution before and after sampling is detected.

实施例2Example 2

取氯化锰溶液1L,加浓度为8%稀碱回调至pH 5.0,稳定pH后继续加热搅拌30分钟,其中,溶液加热升温至95℃,加入无水硫酸钠70g反应25min后,再加入无水硫酸钙3g,继续搅拌,溶液经保温蒸发浓缩至700ml,过滤,取样检测前后溶液钙含量,前液钙4.38g/l,后液钙54.9mg/l。Take 1 L of manganese chloride solution, add 8% dilute alkali to adjust to pH 5.0, and continue to heat and stir for 30 minutes after stabilizing the pH, wherein the solution is heated to 95 ° C, and 70 g of anhydrous sodium sulfate is added to react for 25 minutes. Water calcium sulfate 3g, continue to stir, the solution is evaporated and concentrated to 700ml by thermal insulation, filtered, the calcium content of the solution before and after sampling is detected, the calcium content of the front liquid is 4.38g/l, and the calcium content of the rear liquid is 54.9mg/l.

实施例3Example 3

取硫酸镍溶液1L,加浓度为4%稀碱回调至pH4.2,稳定pH后继续加热搅拌30分钟,其中,溶液加热升温至90℃,加入无水硫酸钙4g,继续搅拌,溶液经保温蒸发浓缩至750ml,过滤,取样检测前后溶液钙,前液钙2.11g/l,后液钙98.6mg/l。Take 1 L of nickel sulfate solution, add 4% dilute alkali to adjust to pH 4.2, and continue to heat and stir for 30 minutes after stabilizing the pH, wherein, the solution is heated to 90 ° C, 4 g of anhydrous calcium sulfate is added, and stirring is continued. Evaporate and concentrate to 750ml, filter, and take samples to detect the calcium in the solution before and after.

实施例4Example 4

取硫酸锰溶液1L,加浓度为4%稀碱回调至pH4.8,稳定pH后继续加热搅拌30分钟,其中,溶液加热升温至87℃,加入无水硫酸钙2g,继续搅拌,溶液经保温蒸发浓缩至700ml,过滤,取样检测前后溶液钙,前液钙3.11g/l,后液钙78.9mg/l。Take 1 L of manganese sulfate solution, add 4% dilute alkali to adjust to pH 4.8, and continue to heat and stir for 30 minutes after stabilizing the pH, wherein the solution is heated to 87 ° C, 2 g of anhydrous calcium sulfate is added, and stirring is continued. Evaporate and concentrate to 700ml, filter, take samples to detect the calcium in the solution before and after, the calcium in the former solution is 3.11g/l, and the calcium in the latter solution is 78.9mg/l.

实施例5Example 5

取硫酸铜溶液1L,加浓度为16%稀碱回调至pH2.0,稳定pH后继续加热搅拌30分钟,其中,溶液加热升温至92℃,加入无水硫酸钙5g,继续搅拌,溶液经保温蒸发浓缩至800ml,过滤,取样检测前后溶液钙,前液钙1.95g/l,后液钙30.9mg/l。Take 1 L of copper sulfate solution, add 16% dilute alkali to adjust to pH 2.0, stabilize the pH and continue to heat and stir for 30 minutes, wherein the solution is heated to 92 ° C, add 5 g of anhydrous calcium sulfate, continue to stir, the solution is kept warm Evaporate and concentrate to 800ml, filter, take samples to detect the calcium in the solution before and after, the calcium in the former solution is 1.95g/l, and the calcium in the latter solution is 30.9mg/l.

实施例6Example 6

取氯化钴溶液1L,加浓度为8%稀碱回调至pH3.7,稳定pH后继续加热搅拌30分钟,其中,溶液加热升温至95℃,加入无水硫酸钠50g反应15min后,再加入无水硫酸钙3g,继续搅拌,溶液经保温蒸发浓缩至700ml,过滤,取样检测前后溶液钙,前液钙2.63g/l,后液钙30.9mg/l。Take 1 L of cobalt chloride solution, add 8% dilute alkali to adjust to pH 3.7, and continue to heat and stir for 30 minutes after stabilizing the pH, wherein the solution is heated to 95 ° C, and 50 g of anhydrous sodium sulfate is added to react for 15 minutes, and then add Anhydrous calcium sulfate 3g, continue to stir, the solution is evaporated and concentrated to 700ml by heat preservation, filtered, sampled to detect the calcium in the solution before and after, the calcium in the front liquid is 2.63g/l, and the calcium in the rear liquid is 30.9mg/l.

以上所述的仅是本发明的较佳实施例,并不局限发明。应当指出对于本领域的普通技术人员来说,在本发明所提供的技术启示下,还可以做出其它等同改进,均可以实现本发明的目的,都应视为本发明的保护范围。The above descriptions are only preferred embodiments of the present invention, and do not limit the invention. It should be pointed out that for those of ordinary skill in the art, under the technical inspiration provided by the present invention, other equivalent improvements can also be made, all of which can achieve the purpose of the present invention and should be regarded as the protection scope of the present invention.

Claims (6)

1. A method for decalcifying a chloride or sulfate solution, said method comprising:
(1) adding dilute alkali into the chloride or sulfate solution to control the pH value of 2-5, and heating and stirring to 85-95 ℃;
(2) adding an additive A and an additive B into the solution obtained in the step (1) or only adding the additive B, wherein the additive A is anhydrous sodium sulfate, and the additive B is anhydrous calcium sulfate;
(3) concentrating 20-30% water by heat preservation and evaporation, and then carrying out solid-liquid separation.
2. The method of claim 1, wherein the chloride solution is one of manganese chloride, cobalt chloride, nickel chloride and copper chloride; the sulfate solution is one of nickel sulfate, copper sulfate, manganese sulfate and cobalt sulfate solution.
3. The method of claim 1, wherein the dilute alkali concentration is 4-16%.
4. The method for removing calcium from a chloride or sulfate solution according to claim 1, wherein the additive A and the additive B are added in an amount of 50-80g/L and 2-8g/L respectively in step (2).
5. The method for removing calcium from a chloride or sulfate solution according to claim 1, wherein the step (2) comprises adding the additive A and the additive B to the chloride solution obtained in the step (1) by the following steps: adding the additive A to react for 10-30min, and then adding the additive B.
6. The method for removing calcium from a chloride or sulfate solution according to claim 1, wherein the step (2) is performed by adding only the additive B to the sulfate solution obtained in the step (1).
CN202210417031.1A 2022-04-20 2022-04-20 Calcium removal method for chloride or sulfate solution Pending CN114836624A (en)

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Citations (12)

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Publication number Priority date Publication date Assignee Title
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US20040089103A1 (en) * 2001-03-09 2004-05-13 Panu Talonen Method for the removal of calcium from a zinc process sulfate solution
US20080206126A1 (en) * 2007-02-28 2008-08-28 Robert Benson Higher than 30% concentration lime slurries, preparation and uses thereof
CN103397185A (en) * 2013-06-24 2013-11-20 中南大学 Method for calcium removal during iron precipitation of nickel sulfate solution containing iron and free sulfuric acid
CN105296754A (en) * 2015-11-30 2016-02-03 北方工业大学 Method for separating copper, cobalt and manganese from impurity-removed solution of copper, manganese, cobalt, calcium and zinc chloride
CN105755296A (en) * 2016-03-29 2016-07-13 云南华联锌铟股份有限公司 Method for removing calcium from zinc sulfate solution of zinc hydrometallurgy production
CN105838879A (en) * 2016-03-29 2016-08-10 云南华联锌铟股份有限公司 Method and apparatus for removing calcium and magnesium from solution after indium precipitation in zinc smelting
CN107794372A (en) * 2017-10-25 2018-03-13 湖南水口山有色金属集团有限公司 A kind of dearsenification selective from lead anode slurry and the method for zero emission of wastewater treatment
CN109633021A (en) * 2018-12-29 2019-04-16 上海微谱化工技术服务有限公司 The detection method of additive in a kind of sufentanil drug
CN110306054A (en) * 2018-03-20 2019-10-08 荆门市格林美新材料有限公司 A kind of recovery method of old circuit board valuable metal
CN112760482A (en) * 2019-11-05 2021-05-07 格林美股份有限公司 Method for reducing calcium sulfate deposition in P204 extraction impurity removal process
CN113106536A (en) * 2021-03-11 2021-07-13 山东创领新材料科技有限公司 Method for preparing calcium sulfate whiskers from calcium chloride solution and sodium sulfate as phosphoric acid byproducts

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2638123A1 (en) * 1976-08-25 1978-03-09 Ruthner Eng Gmbh Calcium ions removed from magnesium chloride soln. - by pptn. as calcium sulphate, e.g. prior to mfg. magnesia and hydrochloric acid
US20040089103A1 (en) * 2001-03-09 2004-05-13 Panu Talonen Method for the removal of calcium from a zinc process sulfate solution
US20080206126A1 (en) * 2007-02-28 2008-08-28 Robert Benson Higher than 30% concentration lime slurries, preparation and uses thereof
CN103397185A (en) * 2013-06-24 2013-11-20 中南大学 Method for calcium removal during iron precipitation of nickel sulfate solution containing iron and free sulfuric acid
CN105296754A (en) * 2015-11-30 2016-02-03 北方工业大学 Method for separating copper, cobalt and manganese from impurity-removed solution of copper, manganese, cobalt, calcium and zinc chloride
CN105755296A (en) * 2016-03-29 2016-07-13 云南华联锌铟股份有限公司 Method for removing calcium from zinc sulfate solution of zinc hydrometallurgy production
CN105838879A (en) * 2016-03-29 2016-08-10 云南华联锌铟股份有限公司 Method and apparatus for removing calcium and magnesium from solution after indium precipitation in zinc smelting
CN107794372A (en) * 2017-10-25 2018-03-13 湖南水口山有色金属集团有限公司 A kind of dearsenification selective from lead anode slurry and the method for zero emission of wastewater treatment
CN110306054A (en) * 2018-03-20 2019-10-08 荆门市格林美新材料有限公司 A kind of recovery method of old circuit board valuable metal
CN109633021A (en) * 2018-12-29 2019-04-16 上海微谱化工技术服务有限公司 The detection method of additive in a kind of sufentanil drug
CN112760482A (en) * 2019-11-05 2021-05-07 格林美股份有限公司 Method for reducing calcium sulfate deposition in P204 extraction impurity removal process
CN113106536A (en) * 2021-03-11 2021-07-13 山东创领新材料科技有限公司 Method for preparing calcium sulfate whiskers from calcium chloride solution and sodium sulfate as phosphoric acid byproducts

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Application publication date: 20220802