Claims
- 1. In a process for producing phosphoric acid wherein phosphate rock is acidulated with a mineral acid and crystals of calcium sulphate hemihydrate are formed, separated off from the phosphoric acid and thereafter washed, the improvement which comprises washing the calcium sulphate hemihydrate crystals with an aqueous wash liquor which prior to contact with the crystals, contains P.sub.2 O.sub.5 in amounts less than 30% and H.sub.2 SO.sub.4 in amounts of less than 10 parts by weight per 100 parts by weight of H.sub.3 PO.sub.4 present in the aqueous wash liquor and contains from 0.0002 to 1.0% by weight of an additive selected from the group consisting of compounds of the empirical general formula:
- R.sup.1 R.sup.2 S(O).sub.n I
- wherein n has a value of 3 or 4 and when n is 3 R.sup.2 is hydrogen and R.sup.1 is an alkyl or aralkyl group and when n is 4 R.sup.1 is an alkyl or aralkyl group and R.sup.2 is hydrogen or an R.sup.1 group; alkylene oxide condensates of an alcohol, phenol or an alkyl phenol and mixtures and salts, esters and amides of said compounds whereby the deposition of calcium sulphate dihydrate scale due to the recrystallisation of the calcium sulphate hemihydrate to calcium sulfate dihydrate is reduced; the total contact time between the calcium sulphate hemihydrate crystals and the wash liquor during washing being less than 10 minutes.
- 2. A process as claimed in claim 1 wherein the additive comprises a mixture of an alkylbenzene sulphonic acid, or alkali-metal salt thereof, with an ethylene oxide condensate of an alkylphenol.
- 3. A process as claimed in claim 2 wherein the mixture comprises from 50 to 80 parts by weight of the sulphonic acid or salt thereof and from 50 to 20 parts by weight of the condensate.
- 4. A process as claimed in claim 3 wherein the alkyl group in the alkylbenzene sulphonic acid contains from 9 to 11 carbon atoms and the condensate is a condensate of from 5 to 15 molar proportions of ethylene oxide with octyl- or nonylphenol.
- 5. A process according to claim 1 wherein the additive is used in the form of an alkali-metal or ammonium salt thereof.
- 6. A process as claimed in claim 1 wherein R.sup.1 is an alkyl group containing from 8 to 18 carbon atoms, optionally interrupted by one or more ether linkages.
- 7. A process as claimed in claim 1 wherein the additive is an ethylene oxide condensate of an alkyl phenol or of a monohydric or dihydric alkanol.
- 8. A process as claimed in claim 1 wherein the compound of formula 1 is selected from alkylbenzene sulphonic acids; monoalkyl sulphate esters; dialkyl sulphate esters; sulphate mono-esters of alkylene oxide condensates with alcohols, glycols or alkylphenols; alkane sulphonates; and mixtures of these.
- 9. A process as claimed in claim 1 wherein the washing is carried out in a number of stages and the additive is added to the wash liquors in two or more of the wash stages.
- 10. A process as claimed in claim 1 wherein the crystals are washed in situ on the filter in which the crystals are separated from the phosphoric acid.
Priority Claims (7)
Number |
Date |
Country |
Kind |
53869/70 |
Nov 1970 |
UK |
|
2225/71 |
Jan 1971 |
UK |
|
44560/71 |
Sep 1971 |
UK |
|
50564/71 |
Oct 1971 |
UK |
|
20966/72 |
May 1972 |
UK |
|
20967/72 |
May 1972 |
UK |
|
22176/72 |
May 1972 |
UK |
|
Parent Case Info
The present invention relates to a process for reducing scale formation, and is a continuation-in-part of our copending Application No. 300,575, filed 10/25/72 itself a continuation-in-part of our earlier, abandoned Application No. 198,425 filed 11/21/71.
US Referenced Citations (8)
Foreign Referenced Citations (4)
Number |
Date |
Country |
539,641 |
Jan 1931 |
DD |
391,901 |
Feb 1964 |
JA |
1,356,586 |
Jun 1974 |
UK |
236,435 |
Nov 1969 |
SU |
Continuation in Parts (2)
|
Number |
Date |
Country |
Parent |
300575 |
Oct 1972 |
|
Parent |
198425 |
Nov 1971 |
|