GB437833A - Improvements in or relating to the manufacture of phosphoric acid-containing fertilisers - Google Patents
Improvements in or relating to the manufacture of phosphoric acid-containing fertilisersInfo
- Publication number
- GB437833A GB437833A GB19040/34A GB1904034A GB437833A GB 437833 A GB437833 A GB 437833A GB 19040/34 A GB19040/34 A GB 19040/34A GB 1904034 A GB1904034 A GB 1904034A GB 437833 A GB437833 A GB 437833A
- Authority
- GB
- United Kingdom
- Prior art keywords
- phosphate
- phosphoric acid
- stage
- sulphuric acid
- raw
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B1/00—Superphosphates, i.e. fertilisers produced by reacting rock or bone phosphates with sulfuric or phosphoric acid in such amounts and concentrations as to yield solid products directly
- C05B1/02—Superphosphates
Abstract
<PICT:0437833/III/1> Phosphoric acid containing fertilizers, i.e. superphosphates, are prepared by reacting sulphuric acid and a part of the phosphoric acid containing material to produce phosphoric acid but no monocalcium phosphate and reacting the resulting product with a further quantity of the same or a different phosphoric acid-containing material whereby super phosphate is formed, the reactions being carried out at different times and in different vessels without substantial quantities of the compounds formed during the process being separated. The initial material reacting with sulphuric acid may be tricalcium phosphate or monocalcium phosphate, say in the form of a portion of the superphosphate previously prepared by the process. The two steps may be carried out continuously, the first in a container provided with stirring means and the second in a mixing apparatus such as a mixed screw device. An excess of sulphuric acid may be employed in the first stage corresponding additional phosphate material being added in the second stage. The first stage may be so conducted that the phosphate material first comes into contact with phosphoric acid only. This may be effected by bringing the raw material into the upper part of the decomposition container and the sulphuric acid into the lower part thereof. Either or both of the two steps may themselves be divided into several stages, by introducing the corresponding quantities of the phosphoric-acid containing raw materials in portions and if desired also at different places. According to one example sulphuric acid is fed from a container 9 into the lower part of a reaction vessel 6 and raw phosphate is introduced into the same vessel from a container 10 and a distributer 11. The mass proceeds via a tube 12 to a vessel 7 in which the reaction continues. The paste passes via an overflow 8 into a mixing apparatus 13 where the residual portion of the phosphate flows in from the distributing device 11. The product leaves via 14 and is removed on a conveyer belt 15. The Specification as open to inspection under Sect. 91 describes also a modification of the process in which both raw phosphate and superphosphate previously prepared by the process are reacted with sulphuric acid in the first stage, the resulting product being reacted with further raw phosphate in the second stage. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE437833X | 1933-06-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB437833A true GB437833A (en) | 1935-11-06 |
Family
ID=20309939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB19040/34A Expired GB437833A (en) | 1933-06-29 | 1934-06-27 | Improvements in or relating to the manufacture of phosphoric acid-containing fertilisers |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB437833A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2767045A (en) * | 1952-10-03 | 1956-10-16 | Robert F Mccullough | Treatment of phosphate rock to recover phosphorus and uranium values |
US2769686A (en) * | 1952-12-08 | 1956-11-06 | Robert F Mccullough | Recovery of mineral values from leached zone material overlying florida pebble phosphate deposits |
US2819145A (en) * | 1952-10-15 | 1958-01-07 | Robert F Mccullough | Metal value recovery from leached zone material |
US2830872A (en) * | 1952-10-03 | 1958-04-15 | Robert F Mccullough | Recovery of uranium values from phosphate rock |
US2849278A (en) * | 1952-10-03 | 1958-08-26 | Charles A Feldt | Metal value recovery from phosphate rock |
-
1934
- 1934-06-27 GB GB19040/34A patent/GB437833A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2767045A (en) * | 1952-10-03 | 1956-10-16 | Robert F Mccullough | Treatment of phosphate rock to recover phosphorus and uranium values |
US2830872A (en) * | 1952-10-03 | 1958-04-15 | Robert F Mccullough | Recovery of uranium values from phosphate rock |
US2849278A (en) * | 1952-10-03 | 1958-08-26 | Charles A Feldt | Metal value recovery from phosphate rock |
US2819145A (en) * | 1952-10-15 | 1958-01-07 | Robert F Mccullough | Metal value recovery from leached zone material |
US2769686A (en) * | 1952-12-08 | 1956-11-06 | Robert F Mccullough | Recovery of mineral values from leached zone material overlying florida pebble phosphate deposits |
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