CN102115249A - Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone - Google Patents

Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone Download PDF

Info

Publication number
CN102115249A
CN102115249A CN2010106166712A CN201010616671A CN102115249A CN 102115249 A CN102115249 A CN 102115249A CN 2010106166712 A CN2010106166712 A CN 2010106166712A CN 201010616671 A CN201010616671 A CN 201010616671A CN 102115249 A CN102115249 A CN 102115249A
Authority
CN
China
Prior art keywords
manganese
gained
filtrate
suction filtration
production
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
CN2010106166712A
Other languages
Chinese (zh)
Inventor
何云
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 CN2010106166712A priority Critical patent/CN102115249A/en
Publication of CN102115249A publication Critical patent/CN102115249A/en
Pending legal-status Critical Current

Links

Landscapes

  • Removal Of Specific Substances (AREA)

Abstract

The invention belongs to the technical field of utilization of manganese-containing waste liquor obtained in the production of hydroquinone and particularly relates to a method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with the manganese-containing waste liquor obtained in the production of hydroquinone. The method mainly comprises the following steps: the manganese-containing waste liquor obtained in the production of hydroquinone is filter through a filter to obtain a filtrate; the filtrate is distilled and filtered to obtain a filter cake; the filter cake is deeply processed to obtain manganese hydroxide; and then the filtrate is distilled under reduced pressure and then further deeply processed to obtain cobaltous sulfate and aqueous ammonia. The waste liquor can be fully utilized, so that environmental pollutions are reduced; valuable manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia products can be prepared; and the method not only has remarkable social and economical benefits, but also is simple in process and production equipment, and is classified as a more practical treatment and utilization method.

Description

A kind of with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced
Technical field
The present invention relates to produce the technical field that contains the manganese waste water utilization that Resorcinol produces, particularly a kind of with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced.
Technical background
Resorcinol is important organic intermediate, and China has also dropped into suitability for industrialized production in the development seventies in 20th century.Advantages such as at present domestic mainly taking used aniline-Manganse Dioxide explained hereafter Resorcinol, and this technology is compared with external phenol-hydrogen peroxide process, has the product purity height, and impurity is few.But its shortcoming is that the quantity discharged of waste liquid is big.Under the common state, one ton of Resorcinol of every production has 40 tons of Mn-bearing waste waters approximately.The chemical composition that contains manganese waste liquid the inside of Resorcinol is the content 11~12% of manganous sulfate, and ammonium sulfate content is 1.4~1.6%, and sulfuric acid content is 1.8~2.2%, simple substance element residue 5~6%.At present domestic factories' utilizations contain the manganese waste liquid and produce crystal manganous sulfate or common carbonate, and high-purity manganese carbonate etc.High-purity manganese carbonate is an ideal high performance strong magneticsubstance, is the main raw material of the manganese-silicon that developed rapidly modern age, mangal, high-performance manganese dioxide product.High-purity manganese carbonate mainly is as soft magnet oxygen magneticsubstance at present, is that raw material is produced with electrolytic manganese or manganous sulfate, bicarbonate of ammonia etc. generally.But do not have a kind of at present with producing the relevant report that the manganese waste liquid is made the method for manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced yet.
Summary of the invention
The invention provides that a kind of this method not only technology is simple with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced, and can also make multiple value product when can effectively dispose waste liquid.
To achieve the above object, technical scheme of the present invention is:
A kind of with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced, comprise being prepared as follows step:
Steps A, will produce the waste liquid that Resorcinol produces and carry out suction filtration with the suction filtration machine;
Step B, suction filtration gained simple substance residual filter cake in the steps A is used to develop other products;
Step C, suction filtration gained filtrate in the steps A is transferred in the reactor, drops into cobaltous hydroxide solution simultaneously and react, the mass ratio between described filtrate and the cobaltous hydroxide solution is 1: 0.42~0.82; Reaction generates the mixture I of manganous hydroxide and rose vitriol and ammoniacal liquor;
Step D, the mixture I of gained among the step C is filtered with strainer;
Step e, with filter among the step D gained filter cake through wash drying, crushing packing becomes the manganous hydroxide product;
Step F, the clarifying filtrate of sulphur of gained among the step D is packaged to be the ammoniacal liquor product through underpressure distillation, condensation;
Step G, with the remaining liquid of underpressure distillation in the step e distill, cooling, crystallization, packing become the rose vitriol crystal product.
The present invention carries out suction filtration with the waste liquid that Resorcinol produced with the suction filtration machine earlier, obtains filtrate and carries out distillating filtering, and the filter cake deep processing obtains the manganous hydroxide product; Further respectively deep processing obtained rose vitriol and ammoniacal liquor product respectively after filtrate was carried out underpressure distillation again; The present invention can as clean as a pennyly gulp down waste liquid, alleviates the pollution of waste liquid to environment; Can make valuable manganous hydroxide, rose vitriol and ammoniacal liquor product again, not only have remarkable social benefit and economic benefit, and technology and production unit are simple, be a kind of relatively actual processing and utilize method.
Its chemical equation is:
MnSO 4+Co(OH) 2=====Mn(OH) 2+CoSO 4
(NH 4) 2SO 4+Co(OH) 2=====2NH 4OH+CoSO 4
H 2SO 4+Co(OH) 2=====CoSO 4+H 2O
Concrete embodiment
Embodiment 1
A kind of with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced, comprise being prepared as follows step:
Steps A, will produce the 1000kg waste liquid (wherein, comprising the 120kg manganous sulfate, 15kg ammonium sulfate and 20kg sulfuric acid) that Resorcinol produces and carry out suction filtration with the suction filtration machine;
Step B, suction filtration gained simple substance residual filter cake in the steps A is used to develop other products;
Step C, suction filtration gained filtrate in the steps A is transferred in the reactor, drops into cobaltous hydroxide solution simultaneously and react, the mass ratio between described filtrate and the cobaltous hydroxide solution is 1: 0.42; Reaction generates the mixture I of manganous hydroxide and rose vitriol and ammoniacal liquor;
Step D, the mixture I of gained among the step C is filtered with strainer;
Step e, with filter among the step D gained filter cake through wash drying, crushing packing becomes 48.38kg manganous hydroxide product;
Step F, the clarifying filtrate of sulphur of gained among the step D is packaged to be 4.73kg ammoniacal liquor product through underpressure distillation, condensation;
Step G, with the remaining liquid of underpressure distillation in the step e distill, cooling, crystallization, packing become 108.66kg rose vitriol crystal product.
Embodiment 2
A kind of with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced, comprise being prepared as follows step:
Steps A, will produce the 1000kg waste liquid (wherein, comprising the 120kg manganous sulfate, 15kg ammonium sulfate and 20kg sulfuric acid) that Resorcinol produces and carry out suction filtration with the suction filtration machine;
Step B, suction filtration gained simple substance residual filter cake in the steps A is used to develop other products;
Step C, suction filtration gained filtrate in the steps A is transferred in the reactor, drops into cobaltous hydroxide solution simultaneously and react, the mass ratio between described filtrate and the cobaltous hydroxide solution is 1: 0.62; Reaction generates the mixture I of manganous hydroxide and rose vitriol and ammoniacal liquor;
Step D, the mixture I of gained among the step C is filtered with strainer;
Step e, with filter among the step D gained filter cake through wash drying, crushing packing becomes 71.42kg manganous hydroxide product;
Step F, the clarifying filtrate of sulphur of gained among the step D is packaged to be 6.98kg ammoniacal liquor product through underpressure distillation, condensation;
Step G, with the remaining liquid of underpressure distillation in the step e distill, cooling, crystallization, packing become 144.99kg rose vitriol crystal product.
Embodiment 3
A kind of with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced, comprise being prepared as follows step:
Steps A, will produce the 1000kg waste liquid (wherein, comprising the 120kg manganous sulfate, 15kg ammonium sulfate and 20kg sulfuric acid) that Resorcinol produces and carry out suction filtration with the suction filtration machine;
Step B, suction filtration gained simple substance residual filter cake in the steps A is used to develop other products;
Step C, suction filtration gained filtrate in the steps A is transferred in the reactor, drops into cobaltous hydroxide solution simultaneously and react, the mass ratio between described filtrate and the cobaltous hydroxide solution is 1: 0.82; Reaction generates the mixture I of manganous hydroxide and rose vitriol and ammoniacal liquor;
Step D, the mixture I of gained among the step C is filtered with strainer;
Step e, with filter among the step D gained filter cake through wash drying, crushing packing becomes 94.46kg manganous hydroxide product;
Step F, the clarifying filtrate of sulphur of gained among the step D is packaged to be 9.23kg ammoniacal liquor product through underpressure distillation, condensation;
Step G, with the remaining liquid of underpressure distillation in the step e distill, cooling, crystallization, packing become 212.15kg rose vitriol crystal product.
The foregoing description is preferred embodiment of the present invention, is not to be used for limiting the scope of the present invention, so all equivalences of being done with described feature of claim of the present invention and principle change or modify, all should be included within the claim scope of the present invention.

Claims (1)

1. one kind with producing the method that the manganese waste liquid is made manganous hydroxide co-producing sulfuric acid cobalt and ammoniacal liquor that contains that Resorcinol produced, and it is characterized in that, comprises being prepared as follows step:
Steps A, will produce the waste liquid that Resorcinol produces and carry out suction filtration with the suction filtration machine;
Step B, suction filtration gained simple substance residual filter cake in the steps A is used to develop other products;
Step C, suction filtration gained filtrate in the steps A is transferred in the reactor, drops into cobaltous hydroxide solution simultaneously and react, the mass ratio between described filtrate and the cobaltous hydroxide solution is 1: 0.42~0.82; Reaction generates the mixture I of manganous hydroxide and rose vitriol and ammoniacal liquor;
Step D, the mixture I of gained among the step C is filtered with strainer;
Step e, with filter among the step D gained filter cake through wash drying, crushing packing becomes the manganous hydroxide product;
Step F, the clarifying filtrate of sulphur of gained among the step D is packaged to be the ammoniacal liquor product through underpressure distillation, condensation;
Step G, with the remaining liquid of underpressure distillation in the step e distill, cooling, crystallization, packing become the rose vitriol crystal product.
CN2010106166712A 2010-12-30 2010-12-30 Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone Pending CN102115249A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010106166712A CN102115249A (en) 2010-12-30 2010-12-30 Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010106166712A CN102115249A (en) 2010-12-30 2010-12-30 Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone

Publications (1)

Publication Number Publication Date
CN102115249A true CN102115249A (en) 2011-07-06

Family

ID=44214192

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010106166712A Pending CN102115249A (en) 2010-12-30 2010-12-30 Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone

Country Status (1)

Country Link
CN (1) CN102115249A (en)

Similar Documents

Publication Publication Date Title
CN102115193A (en) Method for producing manganese hydrate and co-producing magnesium sulfate and ammonia water by using manganese-containing waste liquid generated by producing hydroquinone
CN102115196A (en) Method for producing manganese hydroxide and ammonium sulfate by using manganese-containing waste liquid from production of hydroquinone
CN102120621A (en) Method for preparing manganese sulfate and co-producing ammonia water by utilizing manganese-containing waste liquid generated in hydroquinone production
CN102115249A (en) Method for preparing manganese hydroxide, as well as cobaltous sulfate and aqueous ammonia with manganese-containing waste liquor obtained in production of hydroquinone
CN102115191A (en) Method for co-production of manganese hydroxide, sodium sulfate and ammonia water from manganese-containing waste liquid generated during hydroquinone production
CN102115185A (en) Method for co-production of manganese carbonate and ammonium sulfate from manganese-containing waste liquid generated during hydroquinone production
CN102120620A (en) Method for preparing manganese nitrate and coproducing lithium sulfate and ammonium nitrate by using manganese-containing waste liquor generated in production of hydroquinone
CN102115187A (en) Method for preparing manganese sulfide coproduced with strontium sulfate and ammonium sulfide by using manganese-containing waste liquor produced during production of hydroquinone
CN102115182A (en) Method for co-production of manganese carbonate, magnesium sulfate and ammonium carbonate from manganese-containing waste liquid generated during hydroquinone production
CN102115178A (en) Method for co-production of manganese sulfide, magnesium sulfate and ammonium sulfide from manganese-containing waste liquid generated during hydroquinone production
CN102115246A (en) Method for preparing co-product of manganese hydroxide and potassium sulfate as well as ammonia water by manganese-containing waste liquid obtained by producing hydroquinone
CN102115195A (en) Method for preparing manganese hydroxide coproduced with zinc sulfate and ammonia water by using manganese-containing waste liquor produced during production of hydroquinone
CN102115186A (en) Method for preparing co-product of manganese carbonate and zinc sulfate as well as ammonium carbonate by manganese-containing waste liquid obtained by producing hydroquinone
CN102115177A (en) Method for co-production of manganese carbonate, cobalt sulfate and ammonium carbonate from manganese-containing waste liquid generated during hydroquinone production
CN102115192A (en) Method for producing manganese hydroxide, and co-producing lithium sulfate and ammonia water by using manganese-containing waste liquid from production of hydroquinone
CN102115176A (en) Method for producing manganese sulfide, cobalt sulfate and ammonium sulfate by using manganese-containing waste liquid from production of hydroquinone
CN102115061A (en) Method for co-production of manganese phosphate, magnesium sulfate and ammonium phosphate from manganese-containing waste liquid generated during hydroquinone production
CN102115194A (en) Method for producing manganese hydroxide, strontium sulfate and ammonia water by using manganese-containing waste liquid from production of hydroquinone
CN102115190A (en) Method for producing manganese carbonate and co-producing strontium sulfate and ammonium carbonate by using manganese-containing waste liquid generated by producing hydroquinone
CN102180452A (en) Method for producing manganese phosphate as well as sodium sulfate and ammonium phosphate with manganese-containing waste liquid generated in production of hydroquinone
CN102115184A (en) Method for preparing co-product of manganese sulfide and ammonium sulfate as well as ammonium sulfide by manganese-containing waste liquid obtained by producing hydroquinone
CN102115199A (en) Method for preparing co-product of manganese nitrate and ammonium sulfate as well as nitric acid by manganese-containing waste liquid obtained by producing hydroquinone
CN102115198A (en) Method for co-production of manganese nitrate, cobalt sulfate and ammonium nitrate from manganese-containing waste liquid generated during hydroquinone production
CN102115181A (en) Method for co-production of manganese carbonate, lithium sulfate and ammonium carbonate from manganese-containing waste liquid generated during hydroquinone production
CN102115202A (en) Method for producing manganese nitrate, strontium sulfate and ammonium nitrate by using manganese-containing waste liquid from production of hydroquinone

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

Application publication date: 20110706