GB760653A - Method of separating solids from aqueous suspensions - Google Patents

Method of separating solids from aqueous suspensions

Info

Publication number
GB760653A
GB760653A GB30380/54A GB3038054A GB760653A GB 760653 A GB760653 A GB 760653A GB 30380/54 A GB30380/54 A GB 30380/54A GB 3038054 A GB3038054 A GB 3038054A GB 760653 A GB760653 A GB 760653A
Authority
GB
United Kingdom
Prior art keywords
suspension
per cent
acrylamide
vinyl
hydrolytes
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.)
Expired
Application number
GB30380/54A
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.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
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 Dow Chemical Co filed Critical Dow Chemical Co
Publication of GB760653A publication Critical patent/GB760653A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Hydrology & Water Resources (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

An aqueous suspension of a finely-divided mineral has mixed with it an acrylamide polymer hydrolyte having a specified minimum viscosity and having from 0.8 to 10 per cent of its amide groups replaced by carboxyl groups, the addition being an amount sufficient to accomplish the flocculation and sedimentation of the suspended solids. The preferred reagents are the hydrolytes of the homopolymer of acrylamide, but hydrolytes of water-soluble copolymers of acrylamide with up to 15 per cent by weight of monomers such as alkyl esters of acrylic acid and methacrylic acid, methacrylamide, styrene, vinyl acetate, acrylonitrile, methacrylonitrile, vinyl alkyl ethers and vinyl and vinylidene chloride. The reagent is mixed with water and agitated vigorously, preferably at room temperature, and added to and dispersed through the suspension held in a tank, or introduced into a pipe conveying the suspension where mixing is accomplished by turbulent flow. Preferred solution concentrations lie in the range from 0.003 to 0.1 per cent by weight of reagent, but may be as high as 0.5 per cent. The solution is used in an amount of from 0.001 lbs. to 2 lbs. per short ton of suspended solids. The pH of the suspension should be adjusted to lie in the range 1 to 11.5, and its temperature maintained below 60 DEG C. Examples are given demonstrating improved filtration or settling rates. Reference has been directed by the Comptroller to Specification 725,460.ALSO:In a method for concentrating a finely divided solid mineral in an aqueous suspension and separating it from the suspension, there is mixed with the suspension an acrylamide polymer hydrolyte having a specified minimum viscosity and having from 0,8 to 10 per cent of its amide groups replaced by carboxyl groups, in an amount sufficient to accomplish the flocculation and sedimentation of the suspended solids. The preferred reagents are the hydrolytes of the homopolymer of acrylamide, but hydrolytes of water-soluble copolymers of acrylamide with up to 15 per cent by weight of monomers such as alkyl esters of acrylic acid and metha-crylic acid, methacrylamide, styrene, vinyl acetate, acrylonitrile, methacrylonitrile, vinyl alkyl ethers and vinyl and vinylidene chloride. The reagent is mixed with water and agitated vigorously, preferably at room temperature, and added to and dispersed through the suspension held in a tank, or introduced into a pipe conveying the suspension where mixing is accomplished by turbulent flow. Preferred solution concentrations lie in the range from 0,003 to 0,1 per cent by weight of reagent, but may be as high as 0,5 per cent. The solution is used in an amount of from 0,001 lbs. to 2 lbs. per short ton of suspended solids. The pH of the suspension should be adjusted to lie in the range 1 to 11,5 and its temperature maintained below 60 DEG C. Examples are given demonstrating improved filtration or settling rates. Reference has been directed by the Comptroller to Specification 725,460.ALSO:An aqueous suspension of a finely-divided mineral has mixed with it an acrylamide polymer hydrolyte having a specified minimum viscosity and having from 0.8 to 10 per cent of its amide groups replaced by carboxyl groups, the addition being an amount sufficient to accomplish the flocculation and sedimentation of the suspended solids. The preferred reagents are the hydrolytes of the homopolymer of acrylamide, but hydrolytes of water-soluble copolymers of acrylamide with up to 15 per cent by weight of monomers such as alkyl esters of acrylic acid, and methacrylic acid, methacrylamide, styrene, vinyl acetate, acrylonitrile, methacrylonitrile, vinyl alkyl ethers and vinyl and vinylidene chloride. The reagent is mixed with water and agitated vigorously, preferably at room temperature, and added to and dispersed through the suspension held in a tank, or introduced into a pipe conveying the suspension where mixing is accomplished by turbulent flow. Preferred solution concentrations lie in the range from 0.003 to 0.1 per cent by weight of reagent, but may be as high as 0.5 per cent. The solution is used in an amount of from 0.001 lbs. to 2 lbs. per short ton of suspended solids. The pH of the suspension should be adjusted to lie in the range 1 to 11.5 and its temperature maintained below 60 DEG C. Examples are given demonstrating improved filtration or settling rates. Reference has been directed by the Comptroller to Specification 725,460.
GB30380/54A 1954-06-22 1954-10-21 Method of separating solids from aqueous suspensions Expired GB760653A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US760653XA 1954-06-22 1954-06-22

Publications (1)

Publication Number Publication Date
GB760653A true GB760653A (en) 1956-11-07

Family

ID=22129724

Family Applications (1)

Application Number Title Priority Date Filing Date
GB30380/54A Expired GB760653A (en) 1954-06-22 1954-10-21 Method of separating solids from aqueous suspensions

Country Status (1)

Country Link
GB (1) GB760653A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3017351A (en) * 1958-11-06 1962-01-16 Pan American Petroleum Corp Shale hydration inhibitors for clear water drilling fluids
US3025236A (en) * 1959-04-10 1962-03-13 Phillips Petroleum Co Flocculation of solids
US3146193A (en) * 1960-04-04 1964-08-25 Dow Chemical Co Aqueous suspension clarification method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3017351A (en) * 1958-11-06 1962-01-16 Pan American Petroleum Corp Shale hydration inhibitors for clear water drilling fluids
US3025236A (en) * 1959-04-10 1962-03-13 Phillips Petroleum Co Flocculation of solids
US3146193A (en) * 1960-04-04 1964-08-25 Dow Chemical Co Aqueous suspension clarification method

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