GB932075A - Improvements in the preparation of petroleum resin emulsions - Google Patents
Improvements in the preparation of petroleum resin emulsionsInfo
- Publication number
- GB932075A GB932075A GB2744661A GB2744661A GB932075A GB 932075 A GB932075 A GB 932075A GB 2744661 A GB2744661 A GB 2744661A GB 2744661 A GB2744661 A GB 2744661A GB 932075 A GB932075 A GB 932075A
- Authority
- GB
- United Kingdom
- Prior art keywords
- resin
- weight
- emulsions
- plasticizer
- petroleum
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
- C08J3/03—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2357/00—Characterised by the use of unspecified polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C08J2357/02—Copolymers of mineral oil hydrocarbons
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Paper (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Polyaromatic petroleum resin emulsions of improved stability are prepared by plasticizing the resin in the melted state with a hydrocarbon plasticizer, adding a non-ionic emulsifier to the plasticized resin, cooling the mixture to a temperature below 100 DEG C. but above the softening point of the plasticized resin, maintaining the temperature, while adding water until the emulsion is changed from the water-in-oil type to the oil-in-water type. The polyaromatic petroleum resins are defined as the thermoplastic resins obtained by the distillation of tar produced in the steam cracking of petroleum fractions. The preferred petroleum resins have a softening point within the range 70 DEG -100 DEG C., an acid index of less than 1 and a saponification index of less than 1. Plasticizers used include oily liquid hydrocarbons having a viscosity above 120 centi-stokes at 50 DEG C. and liquid polymers or copolymers of conjugated diolefines containing 4-6 carbon atoms in the molecule. Polymers derived from steam cracked petroleum resins may also be used. The molecular weight of the plasticizers may be in the range 500-15,000. Non-ionic emulsifiers used are a mixture of from 30-5% by weight of a lipophilic emulsifier and from 70-95% by weight of a hydrophilic emulsifier. Specified lipophilic emulsifiers are (a) Condensation products of compounds of formula R-CO-NH2 where R is a C3-C18 alkyl radical, wherein a molecule of the fatty amide has been condensed with 1-15 molecules of an alkylene oxide containing 2-6 carbon atoms; (b) Condensation products of monoesters of polyglycols with diethanolamine; (c) Condensation products of tertiary dodecyl mercaptans and ethylene oxide. Hydrophilic emulsifiers used are condensation products of cresol, xylol, or alkyl phenols, where the alkyl chain contains 3-18 carbon atoms with 1-25 molecules of an alkylene oxide containing 2-6 carbon atoms. Preferably the petroleum polyaromatic resin is plasticized at 100 DEG -150 DEG C., the plasticizer being used in proportions of 10-50% by weight per 90-50% by weight of the polyaromatic resin based on the plasticized mixture. The melted mixture of plasticizer and resin is cooled with stirring to 85 DEG -95 DEG C. and 1-20% by weight in relation to the total weight of the mixture of resin and plasticizer thereafter added in portions. Mixing is continued and water is added at the same temperature to form a water in resin emulsion which reverses to form a resin in water emulsion having a p mean particle dimension of 1 micron, a pH range of 8-10 and a solids content of about 50%. The emulsions have high stability mechanically and are also stable to acids, bases or electrolytes. They may be used for impregnating or coating paper board and fibrous material to improve gloss or finish, resistance to adhesion, wear or colour change, moisture and grease; and to give sound proofing properties by applying them to a metal surface, thereafter applying a paste of fibre and these emulsions and then drying. They may be mixed with other thermoplastic or thermosetting polymers.ALSO:Aqueous emulsions comprising a thermoplastic resin obtained by the distillation of tar produced in the steam-cracking of petroleum fractions, plasticizer and non-ionic emulsifier (see Group III) are used for impregnating paper board and fibrous p materials of a similar type to improve gloss or finish as well as resistance to adhesion, wear or colour change and to give the property of withstanding moisture and grease. The emulsions may be mixed with other thermoplastic or thermo-setting polymers. Specified plasticizers are of hydrocarbon type and specified emulsifiers are mixtures of polyether type.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR836042A FR1272571A (en) | 1960-08-17 | 1960-08-17 | Process for preparing emulsions of petroleum resins |
Publications (1)
Publication Number | Publication Date |
---|---|
GB932075A true GB932075A (en) | 1963-07-24 |
Family
ID=8737564
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2744661A Expired GB932075A (en) | 1960-08-17 | 1961-07-28 | Improvements in the preparation of petroleum resin emulsions |
Country Status (4)
Country | Link |
---|---|
BE (1) | BE607267A (en) |
DE (1) | DE1444821A1 (en) |
FR (1) | FR1272571A (en) |
GB (1) | GB932075A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0085471A2 (en) * | 1982-01-15 | 1983-08-10 | Exxon Research And Engineering Company | Aqueous emulsions of hydrocarbon resins and process for preparing the same |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115894894B (en) * | 2022-11-10 | 2023-12-01 | 宇昂科技有限公司 | Petroleum resin emulsifier and preparation method and application thereof |
-
0
- BE BE607267D patent/BE607267A/xx unknown
-
1960
- 1960-08-17 FR FR836042A patent/FR1272571A/en not_active Expired
-
1961
- 1961-07-28 GB GB2744661A patent/GB932075A/en not_active Expired
- 1961-08-04 DE DE19611444821 patent/DE1444821A1/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0085471A2 (en) * | 1982-01-15 | 1983-08-10 | Exxon Research And Engineering Company | Aqueous emulsions of hydrocarbon resins and process for preparing the same |
EP0085471A3 (en) * | 1982-01-15 | 1984-05-02 | Exxon Research And Engineering Company | Aqueous emulsions of hydrocarbon resins and process for preparing the same |
Also Published As
Publication number | Publication date |
---|---|
DE1444821A1 (en) | 1969-01-30 |
BE607267A (en) | |
FR1272571A (en) | 1961-09-29 |
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