SU545650A1 - The method of producing cation exchanger - Google Patents

The method of producing cation exchanger

Info

Publication number
SU545650A1
SU545650A1 SU2183023A SU2183023A SU545650A1 SU 545650 A1 SU545650 A1 SU 545650A1 SU 2183023 A SU2183023 A SU 2183023A SU 2183023 A SU2183023 A SU 2183023A SU 545650 A1 SU545650 A1 SU 545650A1
Authority
SU
USSR - Soviet Union
Prior art keywords
cation exchanger
producing cation
hours
temperature
granules
Prior art date
Application number
SU2183023A
Other languages
Russian (ru)
Inventor
Мирходжи Аскарович Аскаров
Тулкун Мирамилович Миркамилов
Зоя Петровна Корнеева
Мухаббат Сагдуллаевна Миркамилова
Original Assignee
Ташкентский Политехнический Институт Им.Беруни
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 by Ташкентский Политехнический Институт Им.Беруни filed Critical Ташкентский Политехнический Институт Им.Беруни
Priority to SU2183023A priority Critical patent/SU545650A1/en
Application granted granted Critical
Publication of SU545650A1 publication Critical patent/SU545650A1/en

Links

Description

рола. Через 0,5 час образуетс  смола в виде сферических гранул, постепенно повыша  температуру до 70°С, их выдерживают 0,5 час. Гранулы обрабатывают сразу гор чей дистиллированной водой (80-90°С), сушат на воздухе 24 час, затем 5 час ири темиературе 100- 110°С. Далее гранулы сульфируют в трехгорлой колбе концеитрироваипой сериой кислотой (d 1,83 г/см) в течение 5 час ири температуре 90°С.rola. After 0.5 hour, a resin in the form of spherical granules is formed, gradually raising the temperature to 70 ° C, they are kept for 0.5 hour. The granules are treated immediately with hot distilled water (80-90 ° C), dried in air for 24 hours, then for 5 hours at a temperature of 100-110 ° C. Next, the granules are sulphurized in a three-necked flask with a final nitrile seric acid (d 1.83 g / cm) for 5 hours at a temperature of 90 ° C.

Получениый в виде гранул катион гг и)омывают до нейтральной реакции и перевод т в Н-форму согласно ГОСТУ 10895-64.The cation gg and) obtained in the form of granules is washed until neutral and converted to the H-form according to GOST 10895-64.

Основные иоказатели катионита следующие:The main indications of cation exchanger are as follows:

Насыпной вес в воздушносухом состо нии, ,55Bulk density in air-dry condition,, 55

Статическа  обмеииа  емкость ио 0,1 н. раствору NaOH, мг-экв/г5Static capacity of 0.1 n. NaOH solution, mEq / g5

ХемостойкостьСтойкийChemical resistance Resistant

Статическа  обменна  емкость (в мг-экв/г) иосле обработки:Static exchange capacity (in mEq / g) after treatment:

5 н. H2S045,15 n. H2S045.1

5 н. NaOH55 n. NaOH5

ТермостойкостьСтойкийHeat Resistant Resistant

При кип чении получеииого катнонита в дистиллированной воде в течение 20 час емкостьDuring boiling of the potent catnonite in distilled water for 20 hours

не мен етс . Свойства катиоиита ие меи ютс  при температуре 150-250°С.does not change. The properties of the catalyst are metered at a temperature of 150-250 ° C.

Катионит, иолучаемый согласно известному способу, имеет статистическую обменную емкость по 0,1 н. раствору NaOH 4 мг-экв/г, после обработки 0,5 н. H2SO4-3,8 мг-экв/г. Технико-экономическа  эффективность способа, согласно изобретению, обусловлеиа сокрашением времени проведени  процесса и полным исключеиием расхода органического растворител  дл  промывки получепного иоликоиденсаиионного продукта.The cation exchanger, which is obtained according to a known method, has a statistical exchange capacity of 0.1 n. a solution of NaOH 4 mEq / g, after treatment with 0.5 n. H2SO4-3.8 mg-eq / g. Technical and economic efficiency of the method according to the invention, due to the shortening of the time of the process and the complete elimination of the consumption of organic solvent for washing the obtained iolic condensate and ionic product.

Claims (2)

1.Авторское свидетельство СССР ЛЬ 196302, кл. С 08g 5/18, 1967.1. USSR author's certificate L 196302, cl. From 08g 5/18, 1967. 2.Авторское свидетельство СССР № 362851, кл. С 08g 5/18, 1973.2. USSR author's certificate number 362851, cl. From 08g 5/18, 1973.
SU2183023A 1975-10-17 1975-10-17 The method of producing cation exchanger SU545650A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU2183023A SU545650A1 (en) 1975-10-17 1975-10-17 The method of producing cation exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU2183023A SU545650A1 (en) 1975-10-17 1975-10-17 The method of producing cation exchanger

Publications (1)

Publication Number Publication Date
SU545650A1 true SU545650A1 (en) 1977-02-05

Family

ID=20635232

Family Applications (1)

Application Number Title Priority Date Filing Date
SU2183023A SU545650A1 (en) 1975-10-17 1975-10-17 The method of producing cation exchanger

Country Status (1)

Country Link
SU (1) SU545650A1 (en)

Similar Documents

Publication Publication Date Title
SU545650A1 (en) The method of producing cation exchanger
US2702795A (en) Anion exchange resin restoration process
US1906873A (en) Method for the reduction of furfural and furan derivatives
US2706143A (en) Process for treating feathers
DE1916107B2 (en) Process for the production of basic ion exchangers based on agarose
US2142324A (en) Method and process for preparing a catalytic material
SU434790A1 (en) The method of modification of natural and chemical fibers
SU133863A1 (en) Method of preparation of phosphate catalyst for the polymerization of olefins
CN102125873A (en) Phenolic resin based solid acid, preparation method and application thereof
SU138229A1 (en) The method of preparation of a spherical, mechanically strong iron-chromium catalyst for the conversion of carbon monoxide with water vapor in suspension
CN114773265B (en) Synthesis process of rubber antioxidant RD
US2485352A (en) Method of making an ion-exchange material from light oil acid sluidges
SU92123A1 (en) A method of manufacturing catalysts based on artificial resin ion exchangers
SU377018A1 (en) Method for producing glycolic esters of aromatic cicarboxylic acids
SU467054A1 (en) The method of obtaining 1,4-dichlorobutane
SU442188A1 (en) The method of obtaining anion exchange resin
SU407906A1 (en) METHOD OF OBTAINING AMINOEPOXIDE OLIGOMERS 1 omerov by reacting epichlorohydrin with aromathedyum diamines, HanpMMeip II2NsBH4CH2SbN4YN2, followed by dehydrochlorination of the product / mixture with pheloch.
US1641281A (en) Process for producing active carbon
SU586207A1 (en) Method of obtaining ion-exchange polyacrylonitrile fibre
ES432369A1 (en) Process for spinning acrylic polymers
SU417447A1 (en) WAY OF OBTAINING ANIOPITIS
SU129017A1 (en) Method of producing polyether acrylates
SU396350A1 (en) METHOD OF OBTAINING FURFUROLACACETONE
US1665233A (en) Process for making furfural resins
SU444783A1 (en) The method of obtaining electron-ion exchangers