SU502909A1 - Method of coagulation of divinyl nitrile rubbers - Google Patents

Method of coagulation of divinyl nitrile rubbers

Info

Publication number
SU502909A1
SU502909A1 SU1987186A SU1987186A SU502909A1 SU 502909 A1 SU502909 A1 SU 502909A1 SU 1987186 A SU1987186 A SU 1987186A SU 1987186 A SU1987186 A SU 1987186A SU 502909 A1 SU502909 A1 SU 502909A1
Authority
SU
USSR - Soviet Union
Prior art keywords
coagulation
nitrile rubbers
rubber
divinyl
divinyl nitrile
Prior art date
Application number
SU1987186A
Other languages
Russian (ru)
Inventor
Федор Иванович Ядреев
Инна Ивановна Полякова
Вячеслав Николаевич Лохмачев
Иван Николаевич Лынов
Original Assignee
П/Я А-7345
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 П/Я А-7345 filed Critical П/Я А-7345
Priority to SU1987186A priority Critical patent/SU502909A1/en
Application granted granted Critical
Publication of SU502909A1 publication Critical patent/SU502909A1/en

Links

Description

ДивинилDivinyl

Нитрил акриловой кислотыAcrylic Nitrile

Алкилсульфонат натри Sodium alkyl sulfonate

Калиевое мыло диспропорционированной канифолиPotassium Disproportionate Soap Rosin

Лейканол Сульфат натри  Трилон „БLeukanol sodium sulfate Trilon B

Сульфат двухвалентного железа семиводныйFerrous sulphate of semivalent

РонгалитRongalite

ГиперизHyperies

ДипрокслдDiproksld

трет. Додецилмеркаптанtert Dodecyl mercaptan

ВодаWater

Стоппер: диметилдитиокарбамат натри Stopper: sodium dimethyldithiocarbamate

Температура реакции 5±2°. Глубина полимеризации 65% достигаетс  за 10-12 ч. После отгонки незаполимеризовавшихс  мономеров латексы с рН 8-10 и степенью адсорбционной насыщенности 46-49% заправл ют синтанолом ДС-10 в количестве 0,3- 0,4 вес. % на каучук и подщелачивают до рН 11 - 12.The reaction temperature is 5 ± 2 °. A polymerization depth of 65% is reached in 10-12 hours. After the non-polymerized monomers are distilled off, latexes with a pH of 8-10 and a degree of adsorption saturation of 46-49% are charged with DS-10 syntanol in an amount of 0.3-0.4 wt. % rubber and alkalinized to a pH of 11 - 12.

Коагул цию латексов провод т по каскадной схеме в пвух коагул ционных аппаратах.The coagulation of the latexes is carried out in a cascade scheme in two coagulation devices.

МономерMonomer

В первый аппарат каскада подаютс  латекс и очищенный раствор хлористого натри . Здесь производ т коагул цию латекса при температуре 50-65°С. Второй аппарат каскада служит дозревателем крошки каучука. Величина крощки каучука легко регулируетс  изменением температуры коагул ции и варьированием числа оборотов мешалок в аппаратах каскада.Latex and purified sodium chloride solution are supplied to the first cascade apparatus. The latex is coagulated at a temperature of 50-65 ° C. The second unit of the cascade serves as a rubber crumbler. The amount of rubber crumb is easily controlled by varying the coagulation temperature and varying the number of revolutions of the agitators in the cascade apparatus.

Таблица ITable I

Промывку крошки каучука провод т в двух коагул ционных аппаратах при 40-50°С. Затем крошка каучука поступает на предварительный отжим, где отжимаетс  до остаточпой влаги 8-10%. Сушку каучука осуш;ествл ют в одноходовой ленточной сушилке.Washing of rubber crumbs is carried out in two coagulation devices at 40-50 ° C. Then the rubber crumbs are fed to the preliminary spin, where they are pressed to a residual moisture of 8-10%. The drying of the rubber was dried; it was set up in a one-way belt dryer.

Химический состав и физико-механические свойства каучуков СКН-26АС, СКН-40АС и их вулканизаторов приведены в табл. 1.The chemical composition and physico-mechanical properties of SKN-26AS, SKN-40AS rubbers and their vulcanizers are given in table. one.

Данные о вли нии различных способов коагул ции латекса СКН-26 на чистоту получаемого каучука приведены в табл. 2.Data on the effect of various methods of coagulation of SKN-26 latex on the purity of the obtained rubber are given in Table. 2

Таблица 2table 2

Таблица 3Table 3

SU1987186A 1974-01-21 1974-01-21 Method of coagulation of divinyl nitrile rubbers SU502909A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU1987186A SU502909A1 (en) 1974-01-21 1974-01-21 Method of coagulation of divinyl nitrile rubbers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU1987186A SU502909A1 (en) 1974-01-21 1974-01-21 Method of coagulation of divinyl nitrile rubbers

Publications (1)

Publication Number Publication Date
SU502909A1 true SU502909A1 (en) 1976-02-15

Family

ID=20572990

Family Applications (1)

Application Number Title Priority Date Filing Date
SU1987186A SU502909A1 (en) 1974-01-21 1974-01-21 Method of coagulation of divinyl nitrile rubbers

Country Status (1)

Country Link
SU (1) SU502909A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003022891A1 (en) * 2001-09-13 2003-03-20 Lg Chem, Ltd. Process for preparing polymer latex resin powder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003022891A1 (en) * 2001-09-13 2003-03-20 Lg Chem, Ltd. Process for preparing polymer latex resin powder
US7064149B2 (en) * 2001-09-13 2006-06-20 Lc Chem, Ltd. Process for preparing polymer latex resin powder

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