SU385977A1 - METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^ - Google Patents

METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^

Info

Publication number
SU385977A1
SU385977A1 SU1679476A SU1679476A SU385977A1 SU 385977 A1 SU385977 A1 SU 385977A1 SU 1679476 A SU1679476 A SU 1679476A SU 1679476 A SU1679476 A SU 1679476A SU 385977 A1 SU385977 A1 SU 385977A1
Authority
SU
USSR - Soviet Union
Prior art keywords
ionite
uni
great
obtaining
phosphorus
Prior art date
Application number
SU1679476A
Other languages
Russian (ru)
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to SU1679476A priority Critical patent/SU385977A1/en
Application granted granted Critical
Publication of SU385977A1 publication Critical patent/SU385977A1/en

Links

Landscapes

  • Treatment Of Water By Ion Exchange (AREA)

Description

,1,one

Известен споСоб получени  ионитов путем обработки полиаминостирола метилольНьШИ производными фосфора (триметилолфосфин, тетраметилолфосфонийхлорид и т. п.). Однако получение метилолкных производных фосфора в промышленном масштабе вызывает целый р д технологических трудностей, поэтому получение ионитов с группами а-аминометилфосфоновых кислот в (Насто щее врем  «е представл етс  возможным по этому способу. It is known for the preparation of ion exchangers by treating polyaminostyrene with methylol phosphorus derivatives (trimethylolphosphine, tetramethylolphosphonium chloride, etc.). However, the preparation of methylalkol derivatives of phosphorus on an industrial scale causes a whole range of technological difficulties, therefore, the preparation of ion exchangers with a-aminomethylphosphonic acid groups is now (Presently, e seems possible by this method.

Предлагаетс  способ получени  ионита с Группами амиНометнлфосфанОВой кислоты Hai основе сшитого макропористого аминополистирола обработкой формалином (параформом ) и фосфорноватистой кислотой (гипофосфит Na в избытке НС1) в среде этиленгликол . Этиленгликоль примен ют дл  повышени  температуры кипени  реакционной смеси. Реакци  протекает через стадию образовани  метилольного производного полиамина с последующим присоединением и окислением фосфориоватистой кислоты.A method is proposed for the preparation of an ion exchanger with the Hai groups of Aminomethylene Phosphate Acid based on a cross-linked macroporous aminopolystyrene by treatment with formalin (paraform) and hypophosphorous acid (Na hypophosphite in excess of HCl) in ethylene glycol. Ethylene glycol is used to raise the boiling point of the reaction mixture. The reaction proceeds through the stage of formation of the methylol derivative of the polyamine, followed by addition and oxidation of hypophosphorous acid.

Предложенный способ по сравнению с существующим более прост и может быть выполней на ти.повой ап.паратуре дл  синтеза ионообменных смол. Гипофосфит Na в качестве фосфорсодержащего компонента имеет низкую стоимость и более доступен, чем другиеThe proposed method in comparison with the existing one is simpler and can be performed on a standard equipment for the synthesis of ion exchange resins. Na hypophosphite as a phosphorus-containing component has a low cost and is more accessible than others.

фосфорсодержашие компоненты (ди- и триалкилфосфиты , эфиры аминофосфоновых кислот ).phosphorus-containing components (di- and trialkylphosphites, aminophosphonic acid esters).

Иониты, полученные по предлагаемому способу , имеют высокие значени  предельнЫьХ коэффициентов распределени  () и значительные величины емкостей по ионамIonites, obtained by the proposed method, have high values of limiting distribution coefficients () and significant values of capacities for ions

voi+.voi +.

Пример 1.2е амимопол«стирола макропористой структуры (20% дивинилбензола, 80% гептана) с СОЕ по 0,1 н. НС1 5,0мг-экв/г обрабатывают смесью 8,8 г NaH2PO2 (6 моль), 10 мл 37%-iHoro формалина (6 моль) и 10 мл концентрированной НС1 (10 моль) в 25 мл этиленглИКол  при 120°С в течение 8 час. После охлаждени  смесь отфильтровывают , промывают водой, 5%-ным раствором NaOH, водой, 5%-ным раствором ПС1 и вод&й до отсутстви  С1-1Иона в фильтрате . Ионит высушивают и анализируют. Содержание Р 7,0%.Example 1.2e amimopol "styrene of a macroporous structure (20% divinylbenzene, 80% heptane) with SOY of 0.1 n. HC1 5.0 mg-eq / g is treated with a mixture of 8.8 g of NaH2PO2 (6 mol), 10 ml of 37% -iHoro formalin (6 mol) and 10 ml of concentrated HC1 (10 mol) in 25 ml of ethylene glycol at 120 ° C for 8 o'clock After cooling, the mixture is filtered, washed with water, with a 5% solution of NaOH, with water, with a 5% solution of P1 and with water # until there is no C1-1Ion in the filtrate. The ion exchanger is dried and analyzed. The content of R is 7.0%.

Пример 2. ,5 г амийополистирола обрабатывают по Примеру 1, замен   формалин параформом . Содержание Р 9,0%. СОЕ по 0,1 н. NaOH 4,6 мг-экв/г. Степень превращени  по аминогруппам 80%. Кр пред. 7500 дл  VO2 в 1 Н. HNOa. Обменна1Я емкость по иону VO2 При сорбции из раствора с коицентрацией 5 мг1мл в 1 н. мг V/г сухого ионита. ПримерЗ. 2г аминополистирола обрабатывают ПО примеру 1, добавл   формалин в течение 30 мин после достил ени  температуры 120°С. Содержание Р 9,0%. Обменна1Я емкость по иону услови х примера 2 равна 80 мг-экв/г сухого ионита. 4 Предмет изобретени  Способ получени  июнита, содержащего грутапы аминометилфосфоновой кислоты путем обработки сшитого макропористого полиаминостирола фосфорсодержап1.им реагентом, отличающийс  тем, что, с целью упрощени  технологии, в .качестве фосфорсодержащего реагента примен ют смесь формальдегида и фосфориоватийтой кислоты.Example 2. 5 g of amiopolistirol treated with Example 1, replacing formalin with paraform. The content of P is 9.0%. SOY 0.1 n. NaOH 4.6 mEq / g. Amino conversion is 80%. Cr before. 7500 for VO2 in 1 N. HNOa. Exchange capacity for VO2 ion During sorption from solution with a concentration of 5 mg1 ml in 1 n. mg V / g dry ion exchanger. Example 2 g of aminopolystyrene are treated according to example 1, by adding formalin within 30 minutes after reaching a temperature of 120 ° C. The content of P is 9.0%. The ion exchange capacity of the conditions of Example 2 is 80 mEq / g dry ion exchanger. 4 Subject of the Invention A method for producing junit containing aminomethylphosphonic acid grooves by treating a crosslinked macroporous polyaminoexpanol phosphorus containing I. reagent, characterized in that, in order to simplify the technology, a mixture of formaldehyde and phosphoric acid is used as a phosphorus containing reagent.

SU1679476A 1971-07-01 1971-07-01 METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^ SU385977A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1679476A SU385977A1 (en) 1971-07-01 1971-07-01 METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1679476A SU385977A1 (en) 1971-07-01 1971-07-01 METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^

Publications (1)

Publication Number Publication Date
SU385977A1 true SU385977A1 (en) 1973-06-14

Family

ID=20482341

Family Applications (1)

Application Number Title Priority Date Filing Date
SU1679476A SU385977A1 (en) 1971-07-01 1971-07-01 METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^

Country Status (1)

Country Link
SU (1) SU385977A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4818773A (en) * 1983-02-24 1989-04-04 Rohm And Haas Company Alkylaminophosphonic chelating resins, their preparation and use in purifying brines
EP0355007A2 (en) * 1988-08-18 1990-02-21 Bayer Ag Process for the manufacture of ion exchange resins containing aminoalkylene phosphonic-acid groups
US5278193A (en) * 1988-07-18 1994-01-11 The Dow Chemical Company Ion exchange resin beads having aminoalkylphosphonic groups and processes for preparing them

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4818773A (en) * 1983-02-24 1989-04-04 Rohm And Haas Company Alkylaminophosphonic chelating resins, their preparation and use in purifying brines
US5278193A (en) * 1988-07-18 1994-01-11 The Dow Chemical Company Ion exchange resin beads having aminoalkylphosphonic groups and processes for preparing them
EP0355007A2 (en) * 1988-08-18 1990-02-21 Bayer Ag Process for the manufacture of ion exchange resins containing aminoalkylene phosphonic-acid groups

Similar Documents

Publication Publication Date Title
SU385977A1 (en) METHOD OF OBTAINING IONITE} THE GREAT UNI \\\\\\\\\\\\\\ ^^^
Miller et al. P1, P1-Diethyl pyrophosphate
ATE37808T1 (en) INORGANIC CATION EXCHANGER AND PROCESS FOR THEIR PRODUCTION.
US3156531A (en) Hydrogen peroxide purification
US2583549A (en) Preparation of pentaerythrityl phosphates
US3321521A (en) Regeneration of chelating solutions
US2938770A (en) Process for the purification of alkali metal hypophosphite solutions containing alkali metal phosphites
US3776957A (en) Method for removing copper from aqueous solutions of acrylamide
US1998182A (en) Production of di-sodium phosphate
SU724528A1 (en) Method of producing cation-exchange resins
US2890180A (en) Anion exchangers from polyvinyl alcohol, thiourea and formaldehyde
SU441265A1 (en) The method of obtaining phosphorus-containing sorbents
SU425922A1 (en) METHOD FOR OBTAINING PHOSPHORUS CONTAINING CATIONITES
US4035271A (en) Method of removing acids from reaction liquid of dimethyl dioxane synthesis
SU1213038A1 (en) Method of producing phosphorus-containing cationite
SU528260A1 (en) Extraction phosphoric acid purification method
SU431184A1 (en) METHOD OF OBTAINING PHOSPHORUS AND NITROGEN-CONTAINING SYNTHESIS
SU1039935A1 (en) Process for preparing phosphate-containing cationite
SU999535A1 (en) Method of obtaining phosphonic-acid polyelectrolyte
SU401692A1 (en) METHOD FOR OBTAINING WATER-SOLUBLE AMPHOTERIC
JP3173836B2 (en) Manufacturing method of activated carbon adsorbent
SU568263A1 (en) Method of obtaining cationites
SU1161178A1 (en) Method of obtaining crystalline boron phosphate
SU531815A1 (en) Method for preparing complexing ion exchanger
SU1086758A1 (en) Method of obtaining cation exchanger