GB910541A - Improvements relating to the recovery of boron values from alkaline liquors - Google Patents

Improvements relating to the recovery of boron values from alkaline liquors

Info

Publication number
GB910541A
GB910541A GB2831860A GB2831860A GB910541A GB 910541 A GB910541 A GB 910541A GB 2831860 A GB2831860 A GB 2831860A GB 2831860 A GB2831860 A GB 2831860A GB 910541 A GB910541 A GB 910541A
Authority
GB
United Kingdom
Prior art keywords
solution
polyol
ether
boric acid
phenyl
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
GB2831860A
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.)
American Potash and Chemical Corp
Original Assignee
American Potash and Chemical Corp
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 American Potash and Chemical Corp filed Critical American Potash and Chemical Corp
Publication of GB910541A publication Critical patent/GB910541A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
    • C01B35/08Compounds containing boron and nitrogen, phosphorus, oxygen, sulfur, selenium or tellurium
    • C01B35/10Compounds containing boron and oxygen
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
    • C01B35/06Boron halogen compounds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
    • C01B35/08Compounds containing boron and nitrogen, phosphorus, oxygen, sulfur, selenium or tellurium
    • C01B35/10Compounds containing boron and oxygen
    • C01B35/12Borates

Abstract

Boron values are recovered from aqueous alkaline solutions containing boron ions derived from an alkali metal borate or boric acid, by contacting the solution with 1,8-naphthalene diol or with an aromatic polyol in which two hydroxyl groups are separated by not more than three carbon atoms of which, when there are three carbon atoms, at least one is extra nuclear, to form a boron-containing complex of the polyol, separating the complex from the solution and decomposing it to recover the polyol and recover the boron values. The polyol may be a phenylglycol, an aromatic mono-ether of glycerol, an aromatic compound having hydroxyl groups in the 1,2 positions, or a methylol phenol or naphthol. The solution containing boron ions may be a brine derived from a natural source and may contain sodium or potassium metaborates, tetraborates or pentaborates, and other salts, e.g. sodium and potassium chlorides, sulphates, carbonates, phosphates, sulphides and arsenates; these other salts remain in the aqueous solution. The polyol alone may be mixed with the aqueous solution, or may be added as a solution in a water-immiscible solvent, e.g. benzene, isopropyl ether, diethyl ether, tributyl phosphate, kerosene or a monohydric alcohol having 8 to 17 carbon atoms. The complex appears as a precipitate or as a solution in the organic phase. The complex is reacted with an acid, e.g. sulphuric acid, to obtain an aqueous solution of boric acid and sodium and potassium sulphates, and to regenerate the polyol which is either separated in the organic solvent phase, when present, or is stripped with an organic solvent. The aqueous solution is then evaporated sufficiently to crystallize boric acid at 35 DEG C. but to leave sodium and potassium sulphates in solution. After removal of boric acid crystals the solution is evaporated still further to cause the sulphates to crystallize at a higher temperature leaving the boric acid in solution. Other acids which may be used to decompose the complex are sulphurous, hydrochloric, nitric and perchloric acids. In examples brines containing borax are contacted with 1,8-naphthalenediol, phenyl-glycol in iso-octanol, 4-isooctyl-6-chloro-saligenin in kerosene, and 2,3-naphthalene-diol in a mixture of octanol and tributyl phosphate, and boric acid is recovered by reacting the complexes formed with sulphuric acid. Other polyols mentioned are 1,2-diphenyl glycol, methyl phenyl glycol, 3,5-xylenyl ether of p-tertiary-amyl-phenyl-ether of glycerol, octyl-, nonyl-, dinonyl, phenyl- and dodecyl-saligenins, 2,6-dimethylol-4-octyl phenol and methylolnaphthol. The above-mentioned boron-containing complexes may be added to gasoline together with tetraethyl lead and a halide scavenging agent. The boron compound is added in an amount sufficient to provide from 0,002 to 0,1% by weight based on the gasoline. Specification 625,216 is referred to.ALSO:Boron-containing complexes are prepared from aqueous alkaline solutions containing boron ions derived from an alkali metal borate or boric acid, by contacting the solution with 1,8-naphthalene diol or with an aromatic polyol in which two hydroxyl groups are separated by not more than three carbon atoms of which, when there are three carbon atoms, at least one is extra nuclear. The polyol may be a phenylglycol, an aromatic mono-ether of glycerol, an aromatic compound having hydroxyl groups in the 1,2 positions, or a methylol phenol or naphthol. The solution containing boron ions may be a brine derived from a natural source and may contain sodium or potassium metaborates, tetraborates or pentaborates, and other salts, e.g. sodium and potassium chlorides, sulphates, carbonates, phosphates, sulphides and arsenates; these other salts remain in the aqueous solution. The polyol alone may be mixed with the aqueous solution, or may be added as a solution in a water-immiscible solvent, e.g. benzene, isopropyl ether, diethyl ether, tributyl phosphate, kerosene or a monohydric alcohol having 8 to 17 carbon atoms. The complex appears as a precipitate or as a solution in the organic phase. The complex may be reacted with an acid e.g. sulphuric acid, to obtain an aqueous solution of boric acid and sodium and potassium sulphates, and to regenerate the polyol. In examples brines containing borax are contacted with 1,8-naphthalenediol, phenyl-glycol in isooctanol, 4-isooctyl-6-chloro-saligenin in kerosene, and 2,3-naphthalenediol in a mixture of octanol and tributyl phosphate, and boric acid is recovered by reacting the complexes formed with sulphuric acid. Other polyols mentioned are 1,2-diphenyl glycol, methyl phenyl glycol, 3,5-xylenyl ether of glycerol, p-tertiary-butyl phenyl ether of glycerol, p-tertiary-amyl-phenyl-ether of glycerol, octyl-, nonyl-, dinonyl-, phenyl- and dodecyl-saligenins, 2,6-dimethylol - 4 - octyl phenol and methylolnaphthol. 4-Iso-octyl-6-chlorosaligenin is prepared by chlorinating 4-iso-octyl-phenol to obtain isooctyl-chloro-phenol, which is then reacted with formaldehyde and aqueous sodium hydroxide. Specification 625,216 is referred to.
GB2831860A 1959-08-18 1960-08-16 Improvements relating to the recovery of boron values from alkaline liquors Expired GB910541A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US83450759A 1959-08-18 1959-08-18

Publications (1)

Publication Number Publication Date
GB910541A true GB910541A (en) 1962-11-14

Family

ID=25267085

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2831860A Expired GB910541A (en) 1959-08-18 1960-08-16 Improvements relating to the recovery of boron values from alkaline liquors

Country Status (1)

Country Link
GB (1) GB910541A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3424563A (en) * 1966-02-03 1969-01-28 Dow Chemical Co Selective extraction of boron from aqueous solutions
US3433604A (en) * 1965-09-22 1969-03-18 Dow Chemical Co Calcium chloride and boric acid extraction from magnesium chloride brines using diols and catechols
US3855392A (en) * 1970-09-29 1974-12-17 Norsk Hydro As Method of removing boric acid and boric acid salts from aqueous magnesium chloride solutions
US4261961A (en) * 1979-11-30 1981-04-14 Kerr-Mcgee Chemical Corporation Process for the extraction of potassium from aqueous alkaline solution

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3433604A (en) * 1965-09-22 1969-03-18 Dow Chemical Co Calcium chloride and boric acid extraction from magnesium chloride brines using diols and catechols
US3424563A (en) * 1966-02-03 1969-01-28 Dow Chemical Co Selective extraction of boron from aqueous solutions
US3855392A (en) * 1970-09-29 1974-12-17 Norsk Hydro As Method of removing boric acid and boric acid salts from aqueous magnesium chloride solutions
US4261961A (en) * 1979-11-30 1981-04-14 Kerr-Mcgee Chemical Corporation Process for the extraction of potassium from aqueous alkaline solution

Similar Documents

Publication Publication Date Title
US3111383A (en) Boron extractants
GB907465A (en) Improvements in or relating to the recovery of molybdenum and/or vanadium values
Kumar et al. Dicyclohexano 18 crown 6 in butanol-octanol mixture: a promising extractant of Sr (II) from nitric acid medium
GB910541A (en) Improvements relating to the recovery of boron values from alkaline liquors
US5939038A (en) Process for removing boron from brines
GB798856A (en) Process for separating and recovering carbon dioxide from gaseous mixtures
US5676916A (en) Process for extracting the boron content in the brine of natural or industrial salt mines
US4051219A (en) Method of preparing fluorine-free rare earth metal compounds from such compounds containing fluorine
US6322702B1 (en) Solvent and process for recovery of hydroxide from aqueous mixtures
US3424563A (en) Selective extraction of boron from aqueous solutions
US1991329A (en) Alkali-metal trichlorophenolates
US3943204A (en) Method for improving the extraction properties of a tributyl phosphate solution
US3302993A (en) Process of recovering strontium, cesium, cerium and rare earth values from radioactive solutions
US1961073A (en) Manufacture of potassium borate
US4261961A (en) Process for the extraction of potassium from aqueous alkaline solution
US3011871A (en) Process for treating ammonium borates
US2893824A (en) Uranium recovery process
US1724549A (en) Manufacture of xanthates
US3212850A (en) Preparation of alkali metal peroxides
US3812237A (en) Beryllium hydride containing stabilizing agents
US3049402A (en) Solvent extraction process for separating actinide and lanthanide metal values
US2863892A (en) Separation of plutonium from lanthanum by chelation-extraction
MX3021E (en) PROCEDURE FOR THE PRODUCTION OF POTASSIUM DIACIDE PHOSPHATE
Tewes et al. Thermal Exchange between Vanadyl and Pervanadyl Ions1
US3022134A (en) Separation of curium and americium