SU593673A3 - Method of bonding materials together - Google Patents
Method of bonding materials togetherInfo
- Publication number
- SU593673A3 SU593673A3 SU752176641A SU2176641A SU593673A3 SU 593673 A3 SU593673 A3 SU 593673A3 SU 752176641 A SU752176641 A SU 752176641A SU 2176641 A SU2176641 A SU 2176641A SU 593673 A3 SU593673 A3 SU 593673A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- bonding materials
- materials together
- copolymer
- ethylene
- autoclave
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/02—Ethene
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Paints Or Removers (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Laminated Bodies (AREA)
Description
(54) СПОСОБ СКЛЕИВАНИЯ МАТЕРИАЛОВ(54) METHOD OF GLUING MATERIALS
в пересчете, на полимеризуемый этилен. Кроме того, как таковые или в смеси могут быть использованы и перекиси и другие -образователи радикалов, например пёрбензоат, перекись дилаурила, перекись дидеканоила, перекись ди-грёт -бу- тила , динитрил азоизомасл ной кислоты , в количествах мол.ч. на милл он в пересчете на полимеризуемый этиЛен,in terms of polymerized ethylene. In addition, peroxides and other radical-forming agents, such as perbenzoate, dilauryl peroxide, didecanoyl peroxide, di-tert-butyl peroxide, dinitrile of azo-isobutyric acid, in amounts of mol. on the mill it is in terms of polymerized etilen,
Полимеризацию можно проводить в присут- .ствии замедлителей таких, как например,Polymerization can be carried out in the presence of retarders such as, for example,
алифатические спирты, насыщенные и иена сыщенные углеводороды, хлорированные уг леводороды, а также водород. Полимеризацию можно проводить непрерывно или прерывно причем предпочитают непрерывный способ. .aliphatic alcohols, saturated and yen, saturated hydrocarbons, chlorinated hydrocarbons, and hydrogen. The polymerization can be carried out continuously or discontinuously, with the continuous method being preferred. .
При этом сополимер выдел ют из реактора и часть мономера, инициатора и не участвующего в реакции, модификатора оп т возвращают в реа:ктор.In this case, the copolymer is separated from the reactor and a part of the monomer, the initiator and the one not participating in the reaction, is again returned to the reagent.
Получают сополимер :в установке автоклавов непрерывного действи , главным -элементом которой вл етс снабженный магнитной мешалкой и электрическим к гревом автоклав. ,A copolymer is obtained: in a continuous autoclave installation, the main element of which is a autoclave equipped with a magnetic stirrer and electric to heating. ,
До введени в автоклав к этилену добавл ют газообразные добавки, например кислород как инициатор и в случае необходимости пропан как замедлитель, и сгущают его до давлени реакции. Реакционна смесь проходит через предварительный подо Треватедь и затем поступает в автоклав. Одновременно сополимеры в случае необхо. димости в растворенном или разбавленном Prior to introduction into the autoclave, gaseous additives, such as oxygen as an initiator and, if necessary, propane as a moderator, are added to the ethylene and condensed it up to the reaction pressure. The reaction mixture passes through a preliminary under Trevatedi and then enters the autoclave. At the same time copolymers if necessary. dissolved or diluted
виде подают в реактор с помощью двух дозирующих насосов высокого давлени , имеющих различную мощность. Особенно выгодными растворител ми вл ютс низком лекул рные , пол рные органические соединени , например метанол, этанол и бутанол. Определение адгезионной прочности производ т на алюминиевых образцах Ър следующей методикеThe form is fed to the reactor by means of two high-pressure metering pumps having different capacities. Particularly advantageous solvents are low-molecular, polar organic compounds, such as methanol, ethanol and butanol. Determination of adhesion strength is carried out on aluminum specimens with the following procedure
Очищенные алюминиевые полосы.имеющиеPeeled aluminum strips.
длину 100мм,ширину 100 мм и толщину 1,5 мм, по длине 70 мм склеивают под прессова- /1ием (давление 3 кгс/см, выдержка при прессовании 30-4О с температурой прессовани 180 с) с помощью пленок из соответствующих сополимеров этилeнaj которые дмевэт толщину 0,2 мм и получаютс путем прессовани или экструзии через щелевую головку. В другом случае имеющие100 mm long, 100 mm wide and 1.5 mm thick, 70 mm long are glued together under a press (1 kgf / cm pressure, 30-4 O pressing time with a pressing temperature of 180 s) with the help of films of corresponding ethylene copolymers The dummy is 0.2 mm thick and is obtained by extrusion or extrusion through a slit die. In another case, having
одинаковые размеры алюминиевые полосы в одинаковых услови х соедин ют с плитой из полиэтилена: высокого давлени котора имеет толщину 4.ММ, Не склеенные участки алюминиевых полос под пр мым угломThe same dimensions of aluminum strips under the same conditions are connected to a plate made of polyethylene: high pressure which is 4. mm thick, non-glued sections of aluminum strips at a right angle
отгибшот в противоположные направлени .fold back in opposite directions.
Состав сополимеров и результаты испытаний приведены в табл. 1, из которой видно, что введение в состав сонолимернодого кле -расплава гфостых винильных групп значительно увеличивает адгезионную прочНООЬ . .The composition of the copolymers and the test results are given in table. 1, from which it can be seen that the introduction of soft vinyl groups into the composition of the sonolimer-glue melt significantly increases the adhesive strength. .
Данные по примерам состава сополимера , и Данные по сопротивдению на отслаивание 35 ;:приведены .в; таб - 2.Data for examples of the composition of the copolymer, and Data on the resistance to peeling 35;: are given. tab - 2.
ТаблицаTable
13,613.6
2,92.9
13,113.1
2,42.4
13,313.3
2,72.7
0,40.4
3,23.2
Недостаточна адгези Insufficient adhesion
3,80,53,80,5
14,014.0
3,03.0
13,013.0
2,82.8
13,513.5
2,72.7
11,211.2
2,72.7
1О,61O, 6
3,03.0
(N(N
аbut
ftft
чэChe
asas
НH
СОWITH
WW
0000
Claims (2)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2448342A DE2448342C3 (en) | 1974-10-10 | 1974-10-10 | Process for the production of copolymers of ethylene and their use |
Publications (1)
Publication Number | Publication Date |
---|---|
SU593673A3 true SU593673A3 (en) | 1978-02-15 |
Family
ID=5928005
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU752176641A SU593673A3 (en) | 1974-10-10 | 1975-10-01 | Method of bonding materials together |
Country Status (15)
Country | Link |
---|---|
JP (2) | JPS51125176A (en) |
AT (1) | AT335584B (en) |
BE (1) | BE834240A (en) |
CA (1) | CA1050363A (en) |
DE (1) | DE2448342C3 (en) |
DK (1) | DK145719C (en) |
ES (1) | ES441497A1 (en) |
FR (1) | FR2287457A1 (en) |
GB (1) | GB1480565A (en) |
IT (1) | IT1056145B (en) |
NL (1) | NL158513B (en) |
RO (1) | RO66795A (en) |
SE (1) | SE424329B (en) |
SU (1) | SU593673A3 (en) |
ZA (1) | ZA756294B (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54114889U (en) * | 1978-01-31 | 1979-08-11 | ||
JPS59142130A (en) * | 1983-02-03 | 1984-08-15 | 湊紙器株式会社 | Method of processing carton material |
JPS6178620U (en) * | 1984-10-30 | 1986-05-26 | ||
JPS6178621U (en) * | 1984-10-30 | 1986-05-26 | ||
JPS61106230A (en) * | 1984-10-30 | 1986-05-24 | 積水化成品工業株式会社 | Size changing device for mold for molding set-up box |
JPH0357466Y2 (en) * | 1985-09-20 | 1991-12-27 | ||
JPS6268734A (en) * | 1985-09-20 | 1987-03-28 | 積水化成品工業株式会社 | Box making device |
JPS6253133U (en) * | 1985-09-20 | 1987-04-02 | ||
DE10343901A1 (en) * | 2003-09-19 | 2005-04-14 | Basf Ag | Amide group-containing ethylene terpolymers and their use |
EP3181599A1 (en) * | 2015-12-18 | 2017-06-21 | Borealis AG | Novel process for producing a polar ethylene copolymer with low melt flow rate |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL126214C (en) * | 1961-06-21 | 1900-01-01 | ||
FR1471882A (en) * | 1963-09-18 | 1967-03-03 | Permutit Co Ltd | Film forming terpolymer |
US3405200A (en) * | 1965-07-08 | 1968-10-08 | Toyo Boseki | Polyolefin composition containing a copolymer of ethylene-acrylamide-ethylenically unsaturated compound |
DE1645018A1 (en) * | 1965-08-02 | 1970-05-14 | Monsanto Co | Copolymers and processes for making the same |
US3451982A (en) * | 1965-08-04 | 1969-06-24 | Monsanto Co | Terpolymers of ethylene,a vinyl ester and an unsaturated amide |
US3458487A (en) * | 1965-08-12 | 1969-07-29 | Monsanto Co | Interpolymers of ethylene,an unsaturated amide,and a vinyl ether |
DE1569907A1 (en) * | 1966-01-19 | 1969-08-14 | Basf Ag | Process for bonding molded structures made of polyolefins |
DE1669638B2 (en) * | 1966-03-08 | 1972-09-07 | Badische Anilin & Soda Fabrik AG, 6700 Ludwigshafen | MOLDING COMPOUNDS BASED ON BITUMEN, ETHYLENE MIXED POLYMERIZES AND POLYISOBUTYLENE |
DE1745001B2 (en) * | 1967-10-12 | 1979-07-12 | Imhico Ag, Zuerich (Schweiz) | Copolymers of ethylene suitable for film production and processes for their production |
-
1974
- 1974-10-10 DE DE2448342A patent/DE2448342C3/en not_active Expired
- 1974-10-29 AT AT867774A patent/AT335584B/en not_active IP Right Cessation
-
1975
- 1975-09-26 NL NL7511390.A patent/NL158513B/en not_active IP Right Cessation
- 1975-10-01 SU SU752176641A patent/SU593673A3/en active
- 1975-10-01 FR FR7530100A patent/FR2287457A1/en active Granted
- 1975-10-02 SE SE7511065A patent/SE424329B/en unknown
- 1975-10-02 RO RO7583506A patent/RO66795A/en unknown
- 1975-10-03 GB GB40626/75A patent/GB1480565A/en not_active Expired
- 1975-10-03 JP JP50119675A patent/JPS51125176A/en active Granted
- 1975-10-03 ZA ZA00756294A patent/ZA756294B/en unknown
- 1975-10-03 ES ES441497A patent/ES441497A1/en not_active Expired
- 1975-10-03 DK DK447975A patent/DK145719C/en not_active IP Right Cessation
- 1975-10-06 BE BE160732A patent/BE834240A/en unknown
- 1975-10-09 CA CA237,321A patent/CA1050363A/en not_active Expired
- 1975-10-09 IT IT51723/75A patent/IT1056145B/en active
-
1977
- 1977-07-13 JP JP8401577A patent/JPS5388835A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
SE424329B (en) | 1982-07-12 |
NL158513B (en) | 1978-11-15 |
JPS5388835A (en) | 1978-08-04 |
JPS5646504B2 (en) | 1981-11-04 |
DK447975A (en) | 1976-04-11 |
NL7511390A (en) | 1976-04-13 |
SE7511065L (en) | 1976-04-12 |
GB1480565A (en) | 1977-07-20 |
ZA756294B (en) | 1976-09-29 |
ATA867774A (en) | 1976-07-15 |
BE834240A (en) | 1976-04-06 |
IT1056145B (en) | 1982-01-30 |
FR2287457B1 (en) | 1980-05-30 |
DK145719B (en) | 1983-02-07 |
JPS5249027B2 (en) | 1977-12-14 |
DK145719C (en) | 1983-07-25 |
FR2287457A1 (en) | 1976-05-07 |
RO66795A (en) | 1980-03-15 |
JPS51125176A (en) | 1976-11-01 |
DE2448342A1 (en) | 1976-04-22 |
DE2448342C3 (en) | 1984-05-30 |
CA1050363A (en) | 1979-03-13 |
AT335584B (en) | 1977-03-25 |
DE2448342B2 (en) | 1980-02-07 |
ES441497A1 (en) | 1977-04-01 |
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