SU502909A1 - Method of coagulation of divinyl nitrile rubbers - Google Patents
Method of coagulation of divinyl nitrile rubbersInfo
- 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
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
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)
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 |
-
1974
- 1974-01-21 SU SU1987186A patent/SU502909A1/en active
Cited By (2)
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
FI56970B (en) | SAETT ATT FRAMSTAELLA VAESENTLIGEN EMULGATORFRI LATEX | |
CH510067A (en) | Process for the preparation of fluorine-containing block and graft copolymers | |
GB1034228A (en) | Process for the recovery of emulsion polymerized polymer from the latex in which it is prepared | |
GB351508A (en) | Improvements in the manufacture and production of artificial masses and articles therefrom | |
BRPI0410042A (en) | hydrophilic resin and its production process | |
SU502909A1 (en) | Method of coagulation of divinyl nitrile rubbers | |
GB648900A (en) | Improvements in or relating to plasticized vinyl resin compositions and to methods of preparing the same | |
CN111961768A (en) | Preparation method of amphoteric polyacrylic acid retanning agent | |
SE7500671L (en) | ||
CN107337763B (en) | Production process of high styrene rubber | |
SE7608013L (en) | SET FOR POLYMERIZATION OF VINYL CHLORIDE | |
KR830004087A (en) | Bonding rubber and textile cords by immersion coating using polymers containing N-methylol groups | |
SU523124A1 (en) | Polyvinyl chloride composition | |
SU1423561A1 (en) | Polymeric compound based on styrene-butadiene latex | |
US1098882A (en) | Manufacture of rubber compounds. | |
SU486676A1 (en) | Method of preparing chloroprene latexes | |
SU439494A1 (en) | Method for producing latex | |
KR900001724A (en) | Recovery method of rubber crumb prepared by emulsion polymerization | |
US2684356A (en) | Synthetic rubber and preparation thereof | |
US2973345A (en) | Vinylcyclohexanethiol modified polymers | |
SU406848A1 (en) | In P i b | |
SU168415A1 (en) | The method of manufacture of rubber compounds | |
SU366722A1 (en) | Method of obtaining divinylnitrile rubbers | |
SU730706A1 (en) | Method of producing chloroprene latex | |
SU528333A1 (en) | CLE SHA MASTIC |