ES258101A1 - Process and apparatus for the purification of brine - Google Patents

Process and apparatus for the purification of brine

Info

Publication number
ES258101A1
ES258101A1 ES0258101A ES258101A ES258101A1 ES 258101 A1 ES258101 A1 ES 258101A1 ES 0258101 A ES0258101 A ES 0258101A ES 258101 A ES258101 A ES 258101A ES 258101 A1 ES258101 A1 ES 258101A1
Authority
ES
Spain
Prior art keywords
brine
zone
lime
sludge
reaction zone
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
ES0258101A
Other languages
Spanish (es)
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.)
Novartis AG
Original Assignee
Ciba Geigy AG
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
Priority claimed from CH7325559A external-priority patent/CH396858A/en
Application filed by Ciba Geigy AG filed Critical Ciba Geigy AG
Publication of ES258101A1 publication Critical patent/ES258101A1/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00Halides of sodium, potassium or alkali metals in general
    • C01D3/04Chlorides
    • C01D3/06Preparation by working up brines; seawater or spent lyes
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00Halides of sodium, potassium or alkali metals in general
    • C01D3/14Purification
    • C01D3/16Purification by precipitation or adsorption

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

A two step process for continuously purifying brine by consecutively adding lime and an alkali-metal carbonate to continuously upward-flowing brine, whereby flakes are formed that settle out, the velocity of the brine flowing upwardly through the first reaction zone decreasing on account of the cross-section of the zone widening, the addition of the brine occurring where the flakes begin to form a sludge, comprises the steps of (1) continuously adding to the upward flowing brine in a first reaction zone and at a temperature between 50 DEG C. and 100 DEG C., lime in countercurrent flow, (2) regulating the lime feed rate to maintain the pH of the brine at at least 10.0 at the place where it leaves the first reaction zone, (3) regulating the flow velocity of the brine and removal rate of the sludge to prevent sludge or flakes carrying over to the second reaction zone, (4) adding, in a second reaction zone, an alkali metal carbonate in excess of that required for purification, and (5) regulating the flow velocity in the second zone to prevent flake or sludge removal therefrom. The lime may be in the form of calcined lime or milk of lime. Sodium sulphate may be added to the brine prior to entering the second zone to reduce the alkali metal carbonate requirement, for example in the form of a mother liquor obtained by the evaporation of a sodium sulphate containing brine. There may be added before or simultaneously with the alkali metal carbonate, alkali bicarbonate in an amount such that the hydroxyl ion concentration remains at at least 10-6 g/l. Similarly CO2 may be introduced between the two zones for the same purpose. The second zone may be situated above the first zone, and the sludge precipitated in the second zone may pass through the first zone.
ES0258101A 1959-05-15 1960-05-14 Process and apparatus for the purification of brine Expired ES258101A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH7325559A CH396858A (en) 1959-05-15 1959-05-15 Method of purifying brine
CH402860 1960-04-08

Publications (1)

Publication Number Publication Date
ES258101A1 true ES258101A1 (en) 1960-12-01

Family

ID=25694465

Family Applications (1)

Application Number Title Priority Date Filing Date
ES0258101A Expired ES258101A1 (en) 1959-05-15 1960-05-14 Process and apparatus for the purification of brine

Country Status (2)

Country Link
ES (1) ES258101A1 (en)
GB (1) GB951643A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3463814A (en) * 1967-03-24 1969-08-26 Us Interior Chemical cycle for evaporative water desalination plant
ZA852131B (en) * 1984-04-17 1985-11-27 Dampier Salt Ltd Process for producing high grade sodium chloride
US4636376A (en) * 1985-09-30 1987-01-13 Ppg Industries, Inc. Sulfate removal from alkali metal chlorate solutions
DE3738573C1 (en) * 1987-11-10 1989-02-09 Mannesmann Ag Process and device for processing waste solutions from flue gas cleaning plants
CN104326490A (en) * 2014-11-12 2015-02-04 中盐工程技术研究院有限公司 Method and device for continuously purifying brine through lime-mirabilite-flue gas process

Also Published As

Publication number Publication date
GB951643A (en) 1964-03-11

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