SU800132A1 - Method of producing aluminium phosphate fluoride - Google Patents
Method of producing aluminium phosphate fluoride Download PDFInfo
- Publication number
- SU800132A1 SU800132A1 SU792771540A SU2771540A SU800132A1 SU 800132 A1 SU800132 A1 SU 800132A1 SU 792771540 A SU792771540 A SU 792771540A SU 2771540 A SU2771540 A SU 2771540A SU 800132 A1 SU800132 A1 SU 800132A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- fluoride
- aluminum
- fluorine
- compounds
- phosphoric acid
- Prior art date
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- BSBYUILAJHHGCA-UHFFFAOYSA-K aluminum;phosphate;hydrofluoride Chemical compound [F-].[Al+3].OP([O-])([O-])=O BSBYUILAJHHGCA-UHFFFAOYSA-K 0.000 title claims description 5
- 238000000034 method Methods 0.000 title claims description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 14
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 7
- DDFHBQSCUXNBSA-UHFFFAOYSA-N 5-(5-carboxythiophen-2-yl)thiophene-2-carboxylic acid Chemical compound S1C(C(=O)O)=CC=C1C1=CC=C(C(O)=O)S1 DDFHBQSCUXNBSA-UHFFFAOYSA-N 0.000 claims description 4
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 4
- 229910052731 fluorine Inorganic materials 0.000 claims description 4
- 239000011737 fluorine Substances 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 2
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims 1
- 238000010790 dilution Methods 0.000 claims 1
- 239000012895 dilution Substances 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 230000008020 evaporation Effects 0.000 claims 1
- 150000002222 fluorine compounds Chemical class 0.000 claims 1
- 239000012452 mother liquor Substances 0.000 claims 1
- 239000002244 precipitate Substances 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000000243 solution Substances 0.000 description 9
- 239000012429 reaction media Substances 0.000 description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 229920002313 fluoropolymer Polymers 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- FQKMRXHEIPOETF-UHFFFAOYSA-N F.OP(O)(O)=O Chemical compound F.OP(O)(O)=O FQKMRXHEIPOETF-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
(54) СПОСОБ ПОЛУЧЕНИЯ ФОСФАТ-ФТОРИДА (54) METHOD FOR PRODUCING PHOSPHATE-FLUORIDE
Xl в состав ближайшей координационной сферы ионов М вход т и ионы, и ,при мольнсил соотношении компонентов FlPOl 1:1:1 образуютс комплексы типа АС-Р (HjPCijJt Содержание фтора в .реакционной ; среде составл ет 0,7-1,5 масс.%,т.е. соответствует концентрации фтора в экстракционной .фосфорной кислоте (ЭФ. Это позвол ет вести частичную очистку ЭФК от фтора путем осаждени последнего в виде AEHPO,j.F aHjO.Xl and the nearest coordination sphere of M ions include ions and, at a molar ratio of the components of FlPOl 1: 1: 1, complexes of the AC-P type are formed (HjPCijJt. The fluorine content in the reaction medium; the medium is 0.7-1.5 mass .%, i.e., corresponds to the concentration of fluorine in the extraction phosphoric acid (ESP. This allows partial purification of EPA from fluorine by precipitating the latter in the form of AEHPO, jF aHjO.
и м е р 1. 100 г 6,9%-ного раствора фосфорной кислоты (5 г Р О помещают в полиэтиленовый реактор с фторпластовой ; мешалкой в термостат. К те1; лостатированному при 75 С раствору фосфорной кислоты одновременно приливают 72,0 г 16,4%-ного раствора сульфата алк мини (з,52 г AtjO) и;22 .1г 11,5%-ного раствора фторида аммони 1, 31 г дл установлени в реакционной среде мольного соотнсшеии компонентов Р and meper 1. 100 g of a 6.9% phosphoric acid solution (5 g of P O are placed in a polyethylene fluoroplastic reactor; a stirrer in a thermostat. K te1; a solution of phosphoric acid simultaneously poured at 75 C at the same time 72.0 g 4% aqueous solution of alkali sulphate (C, 52 g AtjO) and; 22.11 11.5% ammonium fluoride solution 1, 31 g to establish in the reaction medium the molar ratio of the components P
«110,98:1,96. Затем реакционную смесь пеЕюмешивгиот при указанных услови х в течение 4 ч, фильтруют, промывают водой и сушат при . Выход фосфатфторида алюмини составл ет 7,ЗЙ г (73,80%).“110.98: 1.96. Then the reaction mixture is mixed under these conditions for 4 hours, filtered, washed with water and dried at. The yield of aluminum phosphate fluoride is 7, D3 g (73.80%).
Теоретическое: Р 10,67%; А1,0,-. 28,65% Рз,0539,89%.Theoretical: R 10.67%; A1.0, -. 28.65% Pz, 0539.89%.
Экспериментальное: F 10,20%; Al20i 28,50f P,,60%.Experimental: F 10.20%; Al20i 28.50f P ,, 60%.
П р и м е р 2. 100 г 13,8%-ного раствора фосфорной кислоты (10 г Р О помещают в полиэтиленовый реактор с фторпластовой мешалкой в термостат. К термостатированному при 80 С раствору фосфорной кислоты одновременно приливают 96,8 г 24,8%-ного раствора сульфата алюмини (7,16 г ) иPRI mme R 2. 100 g of a 13.8% phosphoric acid solution (10 g of P O are placed in a polyethylene reactor with a fluoroplastic agitator in a thermostat. 96.8 g 24 are simultaneously added to a solution of phosphoric acid that is temperature-controlled at 80 C, 8% aqueous solution of aluminum sulfate (7.16 g) and
25.2г 20,6%-ного раствора фторида аммони (2,67 г Р) дл установлени 25.2 g of a 20.6% ammonium fluoride solution (2.67 g P) to establish
в реакционной среде мольного соотношени компонентов F. 1:1:2. Затем реакционную смесь перемэшивают при указанных услови х в течение 5ч, фильтруют, промывают водой и сушат при 80 С. Выход фосфатфторида алюмини составл ет 13,41 г (67,05%)in the reaction medium, the molar ratio of the components F. 1: 1: 2. Then the reaction mixture was mixed under the above conditions for 5 hours, filtered, washed with water and dried at 80 ° C. The yield of aluminum phosphate fluoride was 13.41 g (67.05%)
Теоретическое: Р 10,67%} А I;j0j28 ,65%; ,89%.Theoretical: P 10.67%} A I; j0j28, 65%; 89%.
Экспериментальное: F 10,13%; MjQ4 29,15%i Р5;0539,40%.Experimental: F 10.13%; MjQ4 29.15% i P5; 0539.40%.
Примерз. 100 г 27,7%-ного раствора фосфорной кислоты(20 г Pj С помещают в полиэтиленовый реактор с фторпластовой мешалкой в термостат. К термостатированному при 85С раствору фосфорной кислоты одновременно приливают 168,9 г 29,4%-ного раствора сульфата алюмини (14,81 г Аб,( () и 41,6 г 25,8%-ного раствора фторида аммони (5,51 г Р) дл установлени в реакционной среде мольного соотнотени компонентов 05: А 1,0 :2,06. Затем реакционную смесь перемешивают при указанных услови х в течение 5 ч,фильтруют,промывсцот водой и сушат при 8бс.Выход фосфат-фторйда алюмини составл ет 22,34 г(56,20Froze 100 g of a 27.7% phosphoric acid solution (20 g of Pj C is placed in a polyethylene reactor with a fluoroplastic stirrer in a thermostat. 168.9 g of a 29.4% solution of aluminum sulfate (14 , 81 g of Ab, (() and 41.6 g of a 25.8% solution of ammonium fluoride (5.51 g of P) to establish the molar ratio of components 05: A 1.0: 2.06 in the reaction medium. Then the reaction the mixture is stirred under the above conditions for 5 hours, filtered, washed with water and dried at 8 bs. The output of aluminum phosphate-fluoride is 22.34 g (56.20
Теоретическое: Р 10,67%, AlaOj ,28,65;. Pj05-39, 85%. Экспериментальное: :р 10,92%; ,00%-, PjOj- 40,10%.Theoretical: P 10.67%, AlaOj, 28.65; Pj05-39, 85%. Experimental: p-10.92%; , 00% -, PjOj- 40.10%.
Предложенный способ позвол ет сократить врем проведени процесса до 4-6 ч, исключить в аппаратурном оформлении антикоррозионные материалы и улучшить санитарные услови труда.The proposed method allows to reduce the time of the process to 4-6 hours, to exclude anticorrosive materials in hardware design and to improve the sanitary conditions of labor.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU792771540A SU800132A1 (en) | 1979-04-23 | 1979-04-23 | Method of producing aluminium phosphate fluoride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU792771540A SU800132A1 (en) | 1979-04-23 | 1979-04-23 | Method of producing aluminium phosphate fluoride |
Publications (1)
Publication Number | Publication Date |
---|---|
SU800132A1 true SU800132A1 (en) | 1981-01-30 |
Family
ID=20829990
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU792771540A SU800132A1 (en) | 1979-04-23 | 1979-04-23 | Method of producing aluminium phosphate fluoride |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU800132A1 (en) |
-
1979
- 1979-04-23 SU SU792771540A patent/SU800132A1/en active
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