SU414268A1 - - Google Patents
Info
- Publication number
- SU414268A1 SU414268A1 SU1513450A SU1513450A SU414268A1 SU 414268 A1 SU414268 A1 SU 414268A1 SU 1513450 A SU1513450 A SU 1513450A SU 1513450 A SU1513450 A SU 1513450A SU 414268 A1 SU414268 A1 SU 414268A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- mixture
- phosphoric acid
- phosphate
- mol
- catalyst
- Prior art date
Links
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 14
- 238000000034 method Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 229910019142 PO4 Inorganic materials 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 4
- 239000010452 phosphate Substances 0.000 description 4
- 235000021317 phosphate Nutrition 0.000 description 4
- 239000000047 product Substances 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 239000004327 boric acid Substances 0.000 description 2
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 2
- 230000032050 esterification Effects 0.000 description 2
- 238000005886 esterification reaction Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- WRKCIHRWQZQBOL-UHFFFAOYSA-N octyl dihydrogen phosphate Chemical compound CCCCCCCCOP(O)(O)=O WRKCIHRWQZQBOL-UHFFFAOYSA-N 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 101100287595 Caenorhabditis elegans kin-2 gene Proteins 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- MMCPOSDMTGQNKG-UHFFFAOYSA-N anilinium chloride Chemical compound Cl.NC1=CC=CC=C1 MMCPOSDMTGQNKG-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- HTDKEJXHILZNPP-UHFFFAOYSA-N dioctyl hydrogen phosphate Chemical class CCCCCCCCOP(O)(=O)OCCCCCCCC HTDKEJXHILZNPP-UHFFFAOYSA-N 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 150000004702 methyl esters Chemical class 0.000 description 1
- 150000002903 organophosphorus compounds Chemical class 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- 238000003918 potentiometric titration Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
Description
1one
Изобретение относитс к способу иолученн фосфорорганических соединеиий, а именно смесн МОНО- и диалкиловых эфиров фосфорной кислоты, которые наход т применение в качестве экстрагентов, антиокислителей, новерхностно-активных веществ и т. д.This invention relates to a method for the preparation of organophosphorus compounds, namely the mixture of MONO- and dialkyl phosphate esters, which are used as extractants, antioxidants, surface-active substances, etc.
Известен способ получени смеси моно- и диалкиловых эфиров фосфорной кпслоты взаимодействием фосфорной кислоты со сниртами в присутствии в качестве катализатора борной кислоты ири иаргевании.A method is known for producing a mixture of mono- and dialkyl esters of phosphoric acid by reacting phosphoric acid with snartami in the presence of boric acid and sintering as a catalyst.
Недостатком известного способа вл етс использование борной кислоты, что усложн ет технологию процесса.The disadvantage of this method is the use of boric acid, which complicates the process technology.
С пелью устранени указанного недостатка предлагаетс иснольозвать в качестве катализатора ионообменную смолу кислотного типа, вл ющуюс промышлеппым катализатором, который легко регенерируетс и может быть ,л ногократно использован.With the elimination of this drawback, it is proposed to withdraw the acid-type ion-exchange resin as a catalyst, which is an industrial catalyst that is easily regenerated and can be successfully used.
При siTOM аппаратура практически ие подвергаетс коррозии, а процесс можно вести непрерывно.With siTOM, the equipment is practically corroded and the process can be carried out continuously.
Реакпню обычно ведут при нагревании, предпочтительио до температуры кииени смеСП исходных веществ, с последующим выделением целевого продукта пзвестпымп приемами .The reaction is usually carried out with heating, preferably up to the temperature of the hip and the mixture of starting materials, followed by isolation of the target product using methods.
Пример 1. Этерификаци фосфорной кпслоты октиловым спиртом.Example 1. Esterification of phosphoric acid with octyl alcohol.
Смесь 71,5 г (0,55 г-моль) октилового спирта , 57,6 г (0,5 г-моль) 85%-iioi i фосфорной кислоты ,10 г катионита КУ-2 в И-форме и 500 мл толуола кип т т в приборе Дина-Старка до прекращени выделени воды (13 час), охлаждают , отфильтровывают КУ-2, из фильтрата после удалени растворите.т получают 104,8 г сырого продукта, содержаи1.его по данным потенпиометрнческого титровани 56,2% моноалкилфосфата и 31,8% диалкилфосфата. Выход смеси моно- и диоктилфосфатов в расчете на исходный спирт 89,6%. Смесь фосфатов обрабатывают анилином, перекристаллпзовывают из этилового сппрта и получают анилиновую соль монооктилфосфата, т. пл. 129-131 °С. (по литературным даннылг т. пл. 129-130°С).A mixture of 71.5 g (0.55 g-mol) of octyl alcohol, 57.6 g (0.5 g-mol) of 85% -iioi i phosphoric acid, 10 g of cation exchanger KU-2 in the I-form and 500 ml of toluene boil in a Dean-Stark device until water stops (13 hours), cool, filter KU-2, from the filtrate after removing the solvent. 104.8 g of crude product are obtained; its content according to potentiometric titration is 56.2% monoalkyl phosphate and 31.8% dialkyl phosphate. The yield of the mixture of mono- and dioctyl phosphates, based on the starting alcohol, is 89.6%. The phosphate mixture is treated with aniline, recrystallized from ethyl alumina, and the aniline salt of monooctyl phosphate is obtained, m.p. 129-131 ° C. (according to literature data, pl. 129-130 ° С).
Найдено, %: С 55,7; Н 8,9; N 4,8; Р 10,5.Found,%: C 55.7; H 8.9; N 4.8; R 10.5.
СиП.б NO4P.NO4P Sib.
Вычислено, %: С 55,4; Н 8,62; N 4,6; Р 10,2.Calculated,%: C 55.4; H 8.62; N 4,6; R 10.2.
Пример 2. Этерификаци фосфорной кислоты додециловым спиртом.Example 2. Esterification of phosphoric acid with dodecyl alcohol.
Смесь 39 г (0,5 моль) додепилового сппрта, 69,0 г (0,6 моль) 85%-ной фосфорной кислоты , 10 г катинпона КУ-2 и 500 мл толуола кнп т т в приборе Дина-Старка до прекращени выделени воды (15 час), охлаждают, отфильтровывают КУ-2 и из фильтрата после удалени растворител получают 124 г продукта , содержащего по данным потенциомет3 рмческого титроваипп 89,5% мо |одолои.пл(|)осфата и 7,56% Д1 додоцил(|;осфата. Выход смоси M0110-II дидодсцилфосфата в расчете на исходный спирт 94,1 %. . -. , Предмет и з о о р е т е н и 1. Способ получени смеси мопо- п дткалкиловых эфиров фосфорпой кислоты взаимодействием фосфориой кислоты ео спиртами при 4 Г1лгпгг-;пиии к присутствии катализатора с последующим выдг-лпнлем пслг иого продукта игиестньлми методам;:, о т л и ч а ю iii, и ii с и тем, что, с целью упроиктш способа, в качестве катализатора используют попооблшипУю смо .,. ,„слотпого т ппа. 2. Способ по п. 1, от л и ч а ю ш и й-с г тем, что процесс ведут при темцератур.е кнпеци смеси исходиых реагентов.A mixture of 39 g (0.5 mol) of a pre-dopil acid solution, 69.0 g (0.6 mol) of 85% phosphoric acid, 10 g of Kin-2 KU-2 and 500 ml of toluene at a Dean-Stark device until the release of water (15 hours), cooled, KU-2 is filtered off and from the filtrate, after removal of the solvent, 124 g of product are obtained, containing, according to potentiometer 3 of the titrea, 89.5% of my ophthalate and | () Dopedyl ( ос; osfate. The yield of M0110-II didodoscyl phosphate based on the initial alcohol is 94.1%. -., Subject and rectification 1. The method of obtaining a mixture of phospholipopropyl methyl esters isosta by the interaction of phosphoric acid eo with alcohols at 4 Glpfg-; piii to the presence of a catalyst followed by extraction of the Pslg product from the ingest methods; iii, and ii c and the fact that 2. The method according to claim 1, dated by the fact that the process is carried out at temcerature. There is an injection of a mixture of starting reagents.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1513450A SU414268A1 (en) | 1969-12-23 | 1969-12-23 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1513450A SU414268A1 (en) | 1969-12-23 | 1969-12-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
SU414268A1 true SU414268A1 (en) | 1974-02-05 |
Family
ID=20461250
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1513450A SU414268A1 (en) | 1969-12-23 | 1969-12-23 |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU414268A1 (en) |
-
1969
- 1969-12-23 SU SU1513450A patent/SU414268A1/ru active
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