CN102115138A - Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag - Google Patents

Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag Download PDF

Info

Publication number
CN102115138A
CN102115138A CN 201010615456 CN201010615456A CN102115138A CN 102115138 A CN102115138 A CN 102115138A CN 201010615456 CN201010615456 CN 201010615456 CN 201010615456 A CN201010615456 A CN 201010615456A CN 102115138 A CN102115138 A CN 102115138A
Authority
CN
China
Prior art keywords
barium
chloride
solution
sulfate
potassium chloride
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 201010615456
Other languages
Chinese (zh)
Inventor
谢善情
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 201010615456 priority Critical patent/CN102115138A/en
Publication of CN102115138A publication Critical patent/CN102115138A/en
Pending legal-status Critical Current

Links

Landscapes

  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The invention provides a method for preparing barium sulfate and coproducing potassium chloride by using barium chloride waste residues, wherein the barium chloride waste residues are waste residues obtained by preparing thiourea through the reaction of hydrochloric acid and barium sulfide, the barium chloride waste residues are fully dissolved in water and are mixed with the hydrochloric acid for reaction to obtain a solution containing barium chloride; mixing the solution containing barium chloride with potassium sulfate for reaction to obtain barium sulfate and potassium chloride; filtering to obtain a barium sulfate filter cake and a solution containing potassium chloride; washing, crushing and drying the barium sulfate filter cake to obtain a barium sulfate product; distilling the obtained solution containing potassium chloride to obtain supersaturated solution of potassium chloride, and crystallizing and separating out potassium chloride to obtain potassium chloride product. The method has simple operation and less equipment investment, converts the effective components in the barium sulfide waste residue into industrially usable substances, and is an economical and applicable method.

Description

The method for preparing barium sulfate and co-produced Repone K with the bariumchloride waste residue
Technical field
The present invention relates to the disposal of three wastes of inorganic chemical industry thiocarbamide manufacturing and utilize technical field, especially prepare the method for barium sulfate and co-produced Repone K with the bariumchloride waste residue, described is the waste residue of hydrochloric acid and barium sulphide prepared in reaction thiocarbamide gained with the bariumchloride waste residue.
Background technology
The production method of thiocarbamide is a lot, wherein traditional method is to utilize barium sulphide and hydrochloric acid reaction to generate hydrogen sulfide and bariumchloride precipitation, hydrogen sulfide absorbs through the milk of lime negative pressure and makes the hydrogen sulfide calcium solution, then react with calcium cyanamide again, the mol ratio of calcium sulfhydrate and calcium cyanamide is 1: 5, under constantly stirring, temperature of reaction is (80 ± 5) ℃, reaction times is 3h, through negative pressure filtration, can generate thiocarbamide liquid, again through evaporation, filtration, cooling, crystallization, promptly get the crystal thiocarbamide, centrifugal drying gets product.Reaction equation is as follows:
BaS+2HCl→BaC12+H2S↑
CaO+H2O→Ca(OH)2
2H 2S+Ca(OH) 2→Ca(SH) 2+2H 2O
2CaCN 2+Ca(SH 2) 2+6H 2O→2(NH 2) 2CS+3Ca(OH) 2
Aforesaid method is produced thiocarbamide, and its main industrial residue is exactly the bariumchloride waste residue, according to one's analysis, also contains a large amount of barium sulphides in the bariumchloride waste residue.
Summary of the invention
The waste residue of hydrochloric acid and barium sulphide prepared in reaction thiocarbamide gained is bariumchloride waste residue of the present invention, and its main component is a bariumchloride, also contains a large amount of barium sulphides, the invention provides the method for preparing common barium sulfate and Repone K with above-mentioned bariumchloride waste residue.This method is simple to operate, and facility investment is few, and the effective constituent in the bariumchloride waste residue is converted into industrial utilizable material, is an economic and practical method.
Technical scheme of the present invention is as follows: prepare the method for barium sulfate and co-produced Repone K with the bariumchloride waste residue, described is the waste residue of hydrochloric acid and barium sulphide prepared in reaction thiocarbamide gained with the bariumchloride waste residue, comprises following concrete steps:
Steps A: the bariumchloride waste residue fully is dissolved in water, is mainly contained the solution of bariumchloride and barium sulphide, convert the wherein molar content of barium sulphide;
Step B: with the steps A gained mainly contain bariumchloride and barium sulfide solution mixes with excessive hydrochloric acid, the molar content that makes barium sulphide is 1:1.6-2.4 with the ratio of the molar content of hydrogenchloride, hydrochloric acid and barium sulphide reaction generate bariumchloride and hydrogen sulfide, after hydrogen sulfide is overflowed from solution, obtain containing the solution of bariumchloride, the effusion hydrogen sulfide feeds in the sodium hydroxide solution and absorbs, in order to avoid contaminate environment;
Step C: the solution that contains bariumchloride and small amount of hydrochloric acid of step B gained is mixed with vitriolate of tartar, and making the bariumchloride and the ratio of the molar content of the material of vitriolate of tartar is 1:0.8-1.2; Vitriolate of tartar and bariumchloride reaction generate barium sulfate and Repone K; After filtration, obtain barium sulfate filter cake and the solution that contains Repone K;
Step D: after barium sulfate filter cake washing, pulverizing and drying, obtain barium sulfate product;
Step e: with the solution distillation that contains Repone K of step C gained is the Repone K supersaturated solution, and the Repone K crystallization is separated out, and obtains the Repone K product.
Of the present inventionly prepare the method for barium sulfate and co-produced ammonia chloride with the bariumchloride waste residue, related chemical principle is:
BaS+2HCl=====BaCl 2+H 2S
BaCl 2+K 2SO 4=====BaSO 4↓+2?KCl
Beneficial effect of the present invention is: the method for preparing barium sulfate and co-produced Repone K with the bariumchloride waste residue of the present invention, this method is simple to operate, facility investment is few, and the effective constituent in the bariumchloride waste residue is converted into industrial utilizable material, is an economic and practical method.
Embodiment
Embodiment 1:
Prepare the method for barium sulfate and co-produced Repone K with the bariumchloride waste residue, described is the waste residue of hydrochloric acid and barium sulphide prepared in reaction thiocarbamide gained with the bariumchloride waste residue, comprises following concrete steps:
Steps A: 500kg bariumchloride waste residue fully is dissolved in water, is mainly contained the solution of bariumchloride and barium sulphide, convert the wherein molar content of barium sulphide;
Step B: the steps A gained mainly contained bariumchloride and barium sulfide solution and mixed in hydrochloric acid, the molar content that makes barium sulphide is 1:1.6 with the ratio of the molar content of hydrogenchloride, hydrochloric acid and barium sulphide reaction generate bariumchloride and hydrogen sulfide, after hydrogen sulfide is overflowed from solution, obtain containing the solution of bariumchloride, the effusion hydrogen sulfide feeds in the sodium hydroxide solution and absorbs, in order to avoid contaminate environment;
Step C: the solution that contains bariumchloride and small amount of hydrochloric acid of step B gained is mixed with vitriolate of tartar, and making the bariumchloride and the ratio of the molar content of the material of vitriolate of tartar is 1:1.2; Vitriolate of tartar and bariumchloride reaction generate barium sulfate and Repone K; After filtration, obtain barium sulfate filter cake and the solution that contains Repone K;
Step D: after barium sulfate filter cake washing, pulverizing and drying, obtain barium sulfate product;
Step e: with the solution distillation that contains Repone K of step C gained is the Repone K supersaturated solution, and the Repone K crystallization is separated out, and obtains the Repone K product.
Embodiment 2:
Prepare the method for barium sulfate and co-produced Repone K with the bariumchloride waste residue, described is the waste residue of hydrochloric acid and barium sulphide prepared in reaction thiocarbamide gained with the bariumchloride waste residue, comprises following concrete steps:
Steps A: 500kg bariumchloride waste residue fully is dissolved in water, is mainly contained the solution of bariumchloride and barium sulphide, convert the wherein molar content of barium sulphide;
Step B: the steps A gained mainly contained bariumchloride and barium sulfide solution and mixed in hydrochloric acid, the molar content that makes barium sulphide is 1:2 with the ratio of the molar content of hydrogenchloride, hydrochloric acid and barium sulphide reaction generate bariumchloride and hydrogen sulfide, after hydrogen sulfide is overflowed from solution, obtain containing the solution of bariumchloride, the effusion hydrogen sulfide feeds in the sodium hydroxide solution and absorbs, in order to avoid contaminate environment;
Step C: the solution that contains bariumchloride and small amount of hydrochloric acid of step B gained is mixed with vitriolate of tartar, and making the bariumchloride and the ratio of the molar content of the material of vitriolate of tartar is 1:1; Vitriolate of tartar and bariumchloride reaction generate barium sulfate and Repone K; After filtration, obtain barium sulfate filter cake and the solution that contains Repone K;
Step D: after barium sulfate filter cake washing, pulverizing and drying, obtain barium sulfate product;
Step e: with the solution distillation that contains Repone K of step C gained is the Repone K supersaturated solution, and the Repone K crystallization is separated out, and obtains the Repone K product.
Embodiment 3:
Prepare the method for barium sulfate and co-produced Repone K with 500kg bariumchloride waste residue, described is the waste residue of hydrochloric acid and barium sulphide prepared in reaction thiocarbamide gained with the bariumchloride waste residue, comprises following concrete steps:
Steps A: the bariumchloride waste residue fully is dissolved in water, is mainly contained the solution of bariumchloride and barium sulphide, convert the wherein molar content of barium sulphide;
Step B: the steps A gained mainly contained bariumchloride and barium sulfide solution and mixed in hydrochloric acid, the molar content that makes barium sulphide is 1:2.4 with the ratio of the molar content of hydrogenchloride, hydrochloric acid and barium sulphide reaction generate bariumchloride and hydrogen sulfide, after hydrogen sulfide is overflowed from solution, obtain containing the solution of bariumchloride, the effusion hydrogen sulfide feeds in the sodium hydroxide solution and absorbs, in order to avoid contaminate environment;
Step C: the solution that contains bariumchloride and small amount of hydrochloric acid of step B gained is mixed with vitriolate of tartar, and making the bariumchloride and the ratio of the molar content of the material of vitriolate of tartar is 1:0.8; Vitriolate of tartar and bariumchloride reaction generate barium sulfate and Repone K; After filtration, obtain barium sulfate filter cake and the solution that contains Repone K;
Step D: after barium sulfate filter cake washing, pulverizing and drying, obtain barium sulfate product;
Step e: with the solution distillation that contains Repone K of step C gained is the Repone K supersaturated solution, and the Repone K crystallization is separated out, and obtains the Repone K product.
Above content be in conjunction with concrete preferred implementation to further describing that the present invention did, can not assert that concrete enforcement of the present invention is confined to these explanations.For the general technical staff of the technical field of the invention, without departing from the inventive concept of the premise, its framework form can be flexible and changeable, can the subseries product.Just make some simple deduction or replace, all should be considered as belonging to the scope of patent protection that the present invention is determined by claims of being submitted to.

Claims (1)

1.用氯化钡废渣制备硫酸钡联产氯化钾的方法,其特征在于,所述用氯化钡废渣为盐酸与硫化钡反应制备硫脲所得的废渣,包括如下具体步骤:1. prepare the method for barium sulfate co-production Repone K with barium chloride waste residue, it is characterized in that, described use barium chloride waste residue to prepare the waste residue of thiourea gained for hydrochloric acid and barium sulfide reaction, comprise following concrete steps: 步骤A:将氯化钡废渣充分溶解于水,得到主要含氯化钡和硫化钡的溶液,折算其中硫化钡的摩尔含量;Step A: the barium chloride waste residue is fully dissolved in water to obtain a solution mainly containing barium chloride and barium sulfide, and convert the molar content of barium sulfide wherein; 步骤B:将步骤A所得的主要含氯化钡和硫化钡溶液与盐酸混合,使硫化钡的摩尔含量与氯化氢的摩尔含量之比为1:1.6-2.4,盐酸与硫化钡反应生成氯化钡和硫化氢,硫化氢气体从溶液中逸出后,得到含氯化钡的溶液,逸出硫化氢气体通入氢氧化钠溶液中吸收,以免污染环境;Step B: the main solution containing barium chloride and barium sulfide obtained in step A is mixed with hydrochloric acid, so that the ratio of the molar content of barium sulfide to the molar content of hydrogen chloride is 1:1.6-2.4, and hydrochloric acid reacts with barium sulfide to generate barium chloride And hydrogen sulfide, after the hydrogen sulfide gas escapes from the solution, a solution containing barium chloride is obtained, and the escaped hydrogen sulfide gas is passed into the sodium hydroxide solution for absorption, so as not to pollute the environment; 步骤C:将步骤B所得的含氯化钡和少量盐酸的溶液与硫酸钾混合,使氯化钡与硫酸钾的物质的摩尔含量之比为1:0.8-1.2;硫酸钾与氯化钡反应,生成硫酸钡和氯化钾;经过滤,得到硫酸钡滤饼和含氯化钾的溶液;Step C: the solution containing barium chloride and a small amount of hydrochloric acid obtained in step B is mixed with potassium sulfate, so that the ratio of the molar content of barium chloride and potassium sulfate is 1:0.8-1.2; potassium sulfate reacts with barium chloride , generate barium sulfate and potassium chloride; After filtering, obtain barium sulfate filter cake and the solution containing potassium chloride; 步骤D:将硫酸钡滤饼洗涤、粉碎和干燥后,得到硫酸钡产品;Step D: after the barium sulfate filter cake is washed, pulverized and dried, the barium sulfate product is obtained; 步骤E:将步骤C所得的含氯化钾的溶液蒸馏为氯化钾过饱和溶液,使氯化钾结晶析出,得到氯化钾产品。Step E: Distill the potassium chloride-containing solution obtained in step C into a supersaturated potassium chloride solution to crystallize potassium chloride to obtain a potassium chloride product.
CN 201010615456 2010-12-31 2010-12-31 Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag Pending CN102115138A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201010615456 CN102115138A (en) 2010-12-31 2010-12-31 Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201010615456 CN102115138A (en) 2010-12-31 2010-12-31 Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag

Publications (1)

Publication Number Publication Date
CN102115138A true CN102115138A (en) 2011-07-06

Family

ID=44214080

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201010615456 Pending CN102115138A (en) 2010-12-31 2010-12-31 Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag

Country Status (1)

Country Link
CN (1) CN102115138A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113371750A (en) * 2021-06-08 2021-09-10 龙蟒佰利联集团股份有限公司 Method for preparing barium sulfate by combining titanium white waste acid obtained by chlorination process and titanium white waste acid obtained by sulfuric acid process

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
《河北化工》 19990131 郭斌等 含钡废渣酸浸法制取硫酸钡 第1、2、3.1节 1 , 第1期 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113371750A (en) * 2021-06-08 2021-09-10 龙蟒佰利联集团股份有限公司 Method for preparing barium sulfate by combining titanium white waste acid obtained by chlorination process and titanium white waste acid obtained by sulfuric acid process

Similar Documents

Publication Publication Date Title
CN101508447B (en) Method for processing phosphogypsum
CN102115136B (en) Method for co-production of barium sulfate and manganese chloride from barium chloride waste
CN102115048B (en) Method for preparing barium phosphate and co-producing potassium chloride by using barium chloride waste residues
CN102059038A (en) Treatment process and device of waste gas containing hydrogen sulfide and carbon dioxide
CN102115050B (en) Method for preparing barium phosphate and co-producing industrial salt by using barium chloride waste residues
CN110407180A (en) The method of high-purity calcium thiosulfate and sulfur dioxide is prepared under the conditions of wet process
CN102115138A (en) Method for preparing barium sulfate and co-producing potassium chloride with barium chloride waste slag
CN102167383A (en) Method for preparing ordinary barium sulfate by using barium sulfide waste residue to co-produce soda sulfide and industrial salt
CN102115140A (en) Method for preparing barium sulfate and co-producing industrial salt with barium chloride waste residues
CN102115112A (en) Method for preparing barium carbonate and co-producing zinc chloride with barium chloride waste residue
CN102115049B (en) Method for preparing barium phosphate and co-producing ammonium chloride by using barium chloride waste residues
CN101993107A (en) Method for preparing micronic barium sulfate and co-generating alkali sulfide and industrial salt from barium sulfate waste slag
CN102115135A (en) Method for preparing barium sulfate and co-producing ferrous chloride with barium chloride waste residue
CN102115109A (en) Method for co-production of barium carbonate and ammonium chloride from barium chloride waste
CN102115113A (en) Method for preparing barium carbonate and co-producing potassium chloride with barium chloride waste slag
CN102115137B (en) Method for preparing barium sulfate and co-producing zinc chloride by using barium chloride waste residues
CN102115110A (en) Method for co-production of barium carbonate and industrial salt from barium chloride waste
CN102115107B (en) Method for preparing barium carbonate and potassium chloride by using barium chloride waste residue
CN102115111A (en) Method for preparing barium carbonate and co-producing manganese chloride with barium chloride waste residue
CN102115139B (en) Method for producing barium sulfate and ammonia chloride by using barium chloride waste residue
CN85107743B (en) Hydrochloric acid circulation method for co-production of barium sulfate and magnesium oxide
CN102107901A (en) Method for preparing ultra-fine barium sulfate by using barium sulfide waste residue to co-produce soda sulfide and industrial salt
CN102115125A (en) Method for preparing carbonate and lithium sulfate mixed product with manganese-containing waste liquid
CN101913643A (en) Method for preparing strontium hydroxide and coproducing calcium sulfate dihydrate from barium sulfide waste residue
CN104925830B (en) A chemical treatment method for extracting sodium thiocyanate from coking desulfurization waste liquid

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20110706