ES414069A1 - Purification of phosphoric acid - Google Patents

Purification of phosphoric acid

Info

Publication number
ES414069A1
ES414069A1 ES414069A ES414069A ES414069A1 ES 414069 A1 ES414069 A1 ES 414069A1 ES 414069 A ES414069 A ES 414069A ES 414069 A ES414069 A ES 414069A ES 414069 A1 ES414069 A1 ES 414069A1
Authority
ES
Spain
Prior art keywords
phosphoric acid
ketone
phase
contact
brought
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
ES414069A
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.)
Solvay Solutions UK Ltd
Original Assignee
Albright and Wilson Ltd
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 Albright and Wilson Ltd filed Critical Albright and Wilson Ltd
Publication of ES414069A1 publication Critical patent/ES414069A1/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
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/46Preparation involving solvent-solvent extraction
    • C01B25/461Preparation involving solvent-solvent extraction the phosphoric acid present in the medium obtained after reaction being first extracted from the liquid phase formed or separated then re-extracted as free acid by using water or as a phosphate by using a basic compound
    • C01B25/463Preparation involving solvent-solvent extraction the phosphoric acid present in the medium obtained after reaction being first extracted from the liquid phase formed or separated then re-extracted as free acid by using water or as a phosphate by using a basic compound the extracting agent being a ketone or a mixture of ketones
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/18Phosphoric acid
    • C01B25/22Preparation by reacting phosphate-containing material with an acid, e.g. wet process
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/18Phosphoric acid
    • C01B25/234Purification; Stabilisation; Concentration
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/18Phosphoric acid
    • C01B25/234Purification; Stabilisation; Concentration
    • C01B25/2343Concentration concomitant with purification, e.g. elimination of fluorine

Abstract

The novel process is employed to produce purified phosphoric acid or purified phosphate from a phosphoric acid obtained according to the wet process. This involves bringing the acid into contact with a dialkyl ketone having 5 or 6 carbon atoms. Essentially, the weight ratio is from 0.5:1 to 2:1. The phosphoric acid is then extracted into the organic phase, so that a ketone phase is formed in which the H3PO4 concentration is from 28 to 40% by weight. The organic phase is then brought into contact with water or an aqueous solution of a base. An aqueous phase is thus obtained which contains phosphoric acid or a phosphate with a purity higher than that of the phosphoric acid employed obtained from the wet process. If a ketone having 5 carbon atoms is used, the ketone phase is brought into contact in counter-current with water in at least two stages.
ES414069A 1972-04-26 1973-04-25 Purification of phosphoric acid Expired ES414069A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB1947672A GB1436113A (en) 1972-04-26 1972-04-26 Purification of phosphoric acid
GB4538072 1972-10-02

Publications (1)

Publication Number Publication Date
ES414069A1 true ES414069A1 (en) 1976-05-16

Family

ID=26254071

Family Applications (1)

Application Number Title Priority Date Filing Date
ES414069A Expired ES414069A1 (en) 1972-04-26 1973-04-25 Purification of phosphoric acid

Country Status (20)

Country Link
JP (1) JPS4999993A (en)
AU (1) AU8599475A (en)
BE (1) BE798737A (en)
CA (1) CA1004828A (en)
CH (1) CH613916A5 (en)
DD (1) DD109362A5 (en)
DE (1) DE2320877B2 (en)
ES (1) ES414069A1 (en)
FI (1) FI59077C (en)
FR (3) FR2182055B1 (en)
GB (1) GB1436113A (en)
IE (1) IE37549B1 (en)
IN (1) IN140334B (en)
MY (1) MY7800085A (en)
NL (1) NL7305765A (en)
NO (1) NO137082C (en)
OA (1) OA04403A (en)
RO (2) RO69802A (en)
SE (1) SE395263B (en)
TR (1) TR18445A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IL48207A (en) * 1974-10-07 1978-12-17 Pennzoil Co Production of fluoride-free phosphates
CA1139956A (en) * 1978-10-10 1983-01-25 Mark A. Rose Process for extracting uranium from crude phosphoric acids
DE3246416A1 (en) * 1982-12-15 1984-06-20 Hoechst Ag, 6230 Frankfurt METHOD FOR PURIFYING WET METAL PHOSPHORIC ACID
DE3246415A1 (en) * 1982-12-15 1984-06-20 Hoechst Ag, 6230 Frankfurt METHOD FOR PURIFYING WET METHOD PHOSPHORIC ACID
JP2512429Y2 (en) * 1993-07-12 1996-10-02 北陸電気工業株式会社 High voltage resistance pack
IT1285694B1 (en) * 1996-05-08 1998-06-18 Azionaria Costruzioni Acma Spa METHOD AND UNIT FOR THE TRAINING AND CONVEYANCE OF GROUPS OF PRODUCTS
DE19703884C2 (en) 1997-02-03 1999-04-29 Bk Giulini Chem Gmbh & Co Ohg Process for purifying wet process phosphoric acid

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL298968A (en) 1963-10-08
GB1142719A (en) * 1968-10-24 1969-02-12 Israel Mining Ind Inst For Res Phosphoric acid recovery
DE2334019C3 (en) * 1973-07-04 1982-11-04 Hoechst Ag, 6000 Frankfurt Process for the purification of contaminated aqueous phosphoric acid

Also Published As

Publication number Publication date
DD109362A5 (en) 1974-11-05
NL7305765A (en) 1973-10-30
NO137082C (en) 1977-12-28
BE798737A (en) 1973-10-26
IE37549B1 (en) 1977-08-17
FI59077B (en) 1981-02-27
RO67820A (en) 1980-01-15
FR2289442B1 (en) 1979-02-02
RO69802A (en) 1983-07-07
IN140334B (en) 1976-10-16
CH613916A5 (en) 1979-10-31
FR2182055A1 (en) 1973-12-07
DE2320877A1 (en) 1973-11-15
GB1436113A (en) 1976-05-19
IE37549L (en) 1973-10-26
CA1004828A (en) 1977-02-08
DE2320877B2 (en) 1980-03-20
RO69802B (en) 1983-06-30
FI59077C (en) 1981-06-10
FR2289442A1 (en) 1976-05-28
FR2289441B1 (en) 1979-02-02
FR2182055B1 (en) 1977-01-07
AU5488473A (en) 1974-10-31
OA04403A (en) 1980-02-29
JPS4999993A (en) 1974-09-20
SE395263B (en) 1977-08-08
NO137082B (en) 1977-09-19
AU8599475A (en) 1975-12-18
FR2289441A1 (en) 1976-05-28
TR18445A (en) 1977-02-16
MY7800085A (en) 1978-12-31

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