GB453646A - Improvements in the treatment of raw phosphates - Google Patents
Improvements in the treatment of raw phosphatesInfo
- Publication number
- GB453646A GB453646A GB4346/35A GB434635A GB453646A GB 453646 A GB453646 A GB 453646A GB 4346/35 A GB4346/35 A GB 4346/35A GB 434635 A GB434635 A GB 434635A GB 453646 A GB453646 A GB 453646A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fluorine
- retort
- gases
- phosphate
- flame
- 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
-
- D—TEXTILES; PAPER
- D05—SEWING; EMBROIDERING; TUFTING
- D05C—EMBROIDERING; TUFTING
- D05C13/00—Auxiliary devices incorporated in embroidering machines, not otherwise provided for; Ancillary apparatus for use with embroidering machines
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B13/00—Fertilisers produced by pyrogenic processes from phosphatic materials
- C05B13/02—Fertilisers produced by pyrogenic processes from phosphatic materials from rock phosphates
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
<PICT:0453646/III/1> <PICT:0453646/III/2> <PICT:0453646/III/3> In decomposing raw phosphates by heat treatment at above 1000 DEG C. in the presence of silica, but in the absence of alkalis, whilst scouring with gases containing steam, the fluorine containing-waste gases are carried off from the main reaction zone, and further contact with the material to be or being decomposed is avoided. The production of an undesirable easily-fusible enamel-like compound from the silicon fluoride of the gases and the lime of the phosphate is thereby avoided. In Fig. 1, the phosphate is fed through orifice e through an inclined rotary retort m, and is heated at one end by a powdered coal, oil or gas flame k. Fluorine-containing gases are drawn off through a tube c secured on struts d. The phosphate is preheated by this tube. The phosphate may be fed to the retort through tube c, the gases being withdrawn on the outside of this tube. Fans may be disposed at the end a of the retort. The decomposed material is discharged at orifice f. In another retort, a cooled suction pipe enters in the same direction as, and immediately below, the flame. In Fig. 3, powdered coal or gas n and air o produce the flame k. The lower part q contacting with the material is sucked back by fans through outlet r, carrying with it the fluorine escaping from the decomposing material. The decomposed material is discharged at orifice s. In a modification, the firing of the retort may be so controlled and the main reaction zone may be moved so far in the direction of the gas outlet that the temperature is higher than that at which fluorine is reabsorbed by the material. The hot gases, after removal of fluorine by treatment with basic substances, may be used for preheating the charge. In Fig. 4, the material is preheated in a retort m<1>, care being taken that no sintering occurs. Fluorine is removed to some extent in this retort. The material passes through a short channel 8<1> to a second retort m<11>, wherein the temperature is maintained above that at which fluorine is absorbed. The material may be preheated by means of a travelling grate similar to that used in the Dwight-Lloyd method. The reaction mixture should be finely ground, for instance, to pass through a 2500 mesh sieve, or even so as to leave a 10 per cent residue on a 10,000 mesh sieve. Grain sizes of 0,3 mm. or over are also referred to. The total amount of silica present should not be less than 15 per cent and may amount to one third of the phosphate. Up to 15 per cent of sulphuric, nitric, hydrochloric or phosphoric acid or an acid calcium phosphate may be added. When a product having a composition 5CaO.P2O5.SiO2 is desired, lime may be added. Heating is preferably effected in two operations, first at 1000--1200 DEG C., then at 1300--1450 DEG C. The product is soluble in citric acid and ammonium citrate. The Specification as open to inspection under Sect. 91 comprises also melting of the furnace charge at 1600--1650 DEG C. The melt is cooled by allowing it to fall in drops into a sheet metal chamber. The mixed charge may be wet ground. Precipitated silicic acid, clay, kaolin, blast furnace slag, sand or quartz are specified as sources of silica. This may, however, be replaced by compounds of aluminium, iron, titanium, boron, molybdenum, chromium, vanadium, nickel, &c., producing volatile fluorides. Aluminium fluoride subliming, for example, may be used in the ceramic industry, or for producing artificial cryolite. An oxyhydrogen or acetylene flame may be employed. The reaction mixture may be admixed with powdered coal and blown into the flame. If the fluorine-containing waste gases are allowed to contact with the material to be decomposed, the fluorine concentration is reduced by dilution with inert gases, or by removal with basic absorbents. Basic substances specified for extraction of fluorine from the gases are slaked lime, sodium hydroxide and alumina. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE453646X | 1934-08-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB453646A true GB453646A (en) | 1936-09-11 |
Family
ID=6538805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4346/35A Expired GB453646A (en) | 1934-08-15 | 1935-02-11 | Improvements in the treatment of raw phosphates |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR453646A (en) |
GB (1) | GB453646A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2565351A (en) * | 1947-02-28 | 1951-08-21 | Int Minerals & Chem Corp | Production of defluorinated tricalcium phosphate |
US2754191A (en) * | 1952-05-08 | 1956-07-10 | Smith Douglass Company Inc | Defluorination of phosphate rock |
US2839377A (en) * | 1951-02-28 | 1958-06-17 | Smith Douglass Company Inc | Edfluorination of phosphate rock |
CN106669647A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Titanium-containing alumina dry gel powder and preparation method thereof |
CN113527994A (en) * | 2021-07-31 | 2021-10-22 | 立邦涂料(重庆)化工有限公司 | Soaking type low-temperature drying chromium-free fingerprint resistant agent |
-
1913
- 1913-01-27 FR FR453646D patent/FR453646A/en not_active Expired
-
1935
- 1935-02-11 GB GB4346/35A patent/GB453646A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2565351A (en) * | 1947-02-28 | 1951-08-21 | Int Minerals & Chem Corp | Production of defluorinated tricalcium phosphate |
US2839377A (en) * | 1951-02-28 | 1958-06-17 | Smith Douglass Company Inc | Edfluorination of phosphate rock |
US2754191A (en) * | 1952-05-08 | 1956-07-10 | Smith Douglass Company Inc | Defluorination of phosphate rock |
CN106669647A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Titanium-containing alumina dry gel powder and preparation method thereof |
CN106669647B (en) * | 2015-11-09 | 2019-09-10 | 中国石油化工股份有限公司 | A kind of titanium-contained aluminum oxide dry glue powder and preparation method thereof |
CN113527994A (en) * | 2021-07-31 | 2021-10-22 | 立邦涂料(重庆)化工有限公司 | Soaking type low-temperature drying chromium-free fingerprint resistant agent |
Also Published As
Publication number | Publication date |
---|---|
FR453646A (en) | 1913-06-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2093176A (en) | Treatment of raw phosphates | |
DE3785919T2 (en) | Conversion of calcium compounds into solid and gaseous compounds. | |
JP4313936B2 (en) | Method and apparatus for producing fired product | |
JP2022509411A (en) | Glass manufacturing method and industrial glass manufacturing equipment | |
GB453646A (en) | Improvements in the treatment of raw phosphates | |
US2446978A (en) | Defluorination of phosphate rock | |
US2189248A (en) | Process for the production of phosphatic fertilizers | |
US2252279A (en) | Manufacture of sulphur dioxide and portland cement from calcium sulphate and the usual additions containing aluminum silicate | |
GB284661A (en) | A process for preparing pure alumina | |
US1605098A (en) | Manufacture of aluminum chloride | |
US1931944A (en) | Extraction of tin from ores | |
US2442674A (en) | Deleading zinc-lead fume | |
US1268015A (en) | Process of making aluminum chlorid. | |
US1220735A (en) | Method for the production of hydraulic lime and cement from combustion residues of sewage, canal-sludge, or the like. | |
US1837935A (en) | Process for the obtention of sodium or potassium metals | |
US2684296A (en) | Reduction of iron ores | |
US2117301A (en) | Apparatus for producing phosphorus | |
US2036221A (en) | Method of purifying zirconium silicates | |
NO126986B (en) | ||
US7594952B2 (en) | Treatment of smelting by-products | |
US2474831A (en) | Method for defluorinating phosphate rock | |
US1963546A (en) | Process for making pigments | |
US833406A (en) | Method of smelting ores. | |
US1418527A (en) | Production of beryllium compounds | |
US1959086A (en) | Process of treating phosphates |