GB829912A - Apparatus and process for making cellular rubber - Google Patents
Apparatus and process for making cellular rubberInfo
- Publication number
- GB829912A GB829912A GB33985/56A GB3398556A GB829912A GB 829912 A GB829912 A GB 829912A GB 33985/56 A GB33985/56 A GB 33985/56A GB 3398556 A GB3398556 A GB 3398556A GB 829912 A GB829912 A GB 829912A
- Authority
- GB
- United Kingdom
- Prior art keywords
- rubber
- conveyer
- composition
- carbon black
- butadiene
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/20—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length
- B29C44/28—Expanding the moulding material on continuous moving surfaces without restricting the upwards growth of the foam
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
A continuous sheet of gas-expanded cellular rubber is produced by continuously forming a rubber composition containing a blowing agent into a sheet, heating the sheet to cause the blowing agent to evolve a gas and expand the rubber composition, intermittently breaking contact between the composition and the surface supporting it during expansion, and vulcanizing the expanded composition. In one form of apparatus (not shown), the extruded rubber composition is conveyed continuously into a first heating chamber where it is partially vulcanized below a temperature high enough to cause the blowing agent to evolve a gas. It then passes on to a vibrator conveyer and advances through a second heating chamber where the composition, whilst bouncing on the vibrating conveyer to break contact therewith, is expanded and vulcanization completed. If desired expansion and vulcanization can be effected in different chambers. Instead of a vibrator conveyer, a series of air jets positioned below an open mesh conveyer belt can be employed to direct streams of air against the underside of the rubber composition thereby causing it to break contact with the conveyer. Partial vulcanization before expansion is omitted when an open cell rather than a closed cell sponge is required. Rubbers employed may be natural, e.g. caoutchouc, or synthetic, e.g. polymers and copolymers of butadiene-1,3; 2,3-dimethyl butadiene-1,3; and 1,4-dimethyl butadiene-1,3; copolymers thereof with styrene, methyl and ethyl acrylate, methyl and ethyl methacrylate, acrylonitrile and isobutylene, and polychloroprene. Blowing agents specified are sodium bicarbonate, ammonium carbonate, diazoaminobenzene, dinitrozo pentamethylenetetramine, 1,3-bis-(o-zenyl)-triazene, and p,p1-oxybis-(benzene sulphonyl hydrazide). In examples, the following compositions are blown and vulcanized: (1) and (3) natural rubber, carbon black, hydrocarbon oil; (2) GR-S rubber, natural rubber, paraffin oil, zinc oxide stearic acid, carbon black, naphthenic hydrocarbon plasticizer, finely-divided urea; (4) butadiene-acrylonitrile polymer, coumarone-indene polymer, naphthenic hydrocarbon plasticizer, carbon black, zinc oxide; (5) polychloroprene, natural rubber, GR-S, paraffin oil, naphthenic hydrocarbon plasticizer, carbon black, zinc oxide, magnesia, stearic acid. Proportions of the various ingredients are given. Both open and closed cell products are produced.ALSO:A continuous sheet of gas-expanded cellular rubber is produced by continuously forming a rubber composition containing a blowing agent into a sheet, heating the sheet to cause the blowing agent to evolve a gas and expand the rubber composition, intermittently breaking contact between the composition and the surface supporting it during expansion, and vulcanizing the expanded composition. In one form of apparatus, (not shown), the extruded rubber composition is conveyed continuously into a first heating chamber where it is partially vulcanized below a temperature high enough to cause the blowing agent to evolve a gas. It then passes on to a vibrator conveyer and advances through a second heating chamber where the composition, whilst bouncing on the vibrating conveyer to break contact therewith, is expanded and vulcanization completed. If desired expansion and vulcanization can be effected in different chambers. Instead of a vibrator conveyer, a series of air jets positioned below an open mesh conveyer belt can be employed to direct streams of air against the underside of the rubber composition thereby causing it to break contact with the conveyer. Partial vulcanization before expansion is omitted when an open cell rather than a closed cell sponge is required. Rubbers employed may be natural, e.g. caoutchouc, or synthetic, e.g. polymers and copolymers of butadiene-1, 3; 2, 3- dimethyl butadiene -1, 3; and 1, 4- dimethyl butadiene -1, 3; copolymers thereof with styrene, methyl and ethyl acrylate, methyl and ethyl methacrylate, acrylonitrile and isobutylene, and polychloroprene. Blowing agents specified are sodium bicarbonate, ammonium carbonate, diazoaminobenzene, dinitrozo pentamethylenetetramine, 1, 3- bis (o - zenyl) -triazene, and p, p1 oxybis (benzene sulphonyl hydrazide). In examples the following compositions are blown and vulcanized: (1) and (3) natural rubber, carbon black, hydrocarbon oil; (2) GR-S, natural rubber, paraffin oil, zinc oxide, stearic acid, carbon black, naphthenic hydrocarbon plasticizer finely divided urea; (4) butadiene-acrylonitrile polymer, coumarone-indene polymer, naphthenic hydrocarbon plasticizer, carbon black, zinc oxide; (5) polychloroprene, natural rubber, GR-S, paraffin oil, naphthenic hydrocarbon plasticizer, carbon black, zinc oxide, magnesia, stearic acid. Proportions of the various ingredients are given. Both open and closed cell products are produced.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US829912XA | 1955-11-08 | 1955-11-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB829912A true GB829912A (en) | 1960-03-09 |
Family
ID=22174733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB33985/56A Expired GB829912A (en) | 1955-11-08 | 1956-11-07 | Apparatus and process for making cellular rubber |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB829912A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3210449A (en) * | 1963-04-08 | 1965-10-05 | Goodrich Co B F | Process and apparatus for making a cylindrical-shaped cellular rubber strip |
US3239585A (en) * | 1962-05-11 | 1966-03-08 | Dow Chemical Co | Shock treatment of plastic foams |
US3346247A (en) * | 1965-07-27 | 1967-10-10 | Goodrich Co B F | Heating apparatus for rubber or rubber-like strip material |
DE1252984B (en) * | 1960-04-20 | 1967-10-26 | Aeroquip Ag | End fitting for hoses or flexible lines |
US3393260A (en) * | 1965-04-27 | 1968-07-16 | Baker Perkins Inc | Process for preparing foam products |
US3946096A (en) * | 1970-04-23 | 1976-03-23 | Phillips Petroleum Company | Securing a filamentous extrudate into a base material matrix at least one of which is expandable |
WO2010074727A2 (en) | 2008-12-22 | 2010-07-01 | The Gates Corporation | Method of making composite article with expandable elastomer in compression |
-
1956
- 1956-11-07 GB GB33985/56A patent/GB829912A/en not_active Expired
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1252984B (en) * | 1960-04-20 | 1967-10-26 | Aeroquip Ag | End fitting for hoses or flexible lines |
US3239585A (en) * | 1962-05-11 | 1966-03-08 | Dow Chemical Co | Shock treatment of plastic foams |
US3210449A (en) * | 1963-04-08 | 1965-10-05 | Goodrich Co B F | Process and apparatus for making a cylindrical-shaped cellular rubber strip |
US3393260A (en) * | 1965-04-27 | 1968-07-16 | Baker Perkins Inc | Process for preparing foam products |
US3346247A (en) * | 1965-07-27 | 1967-10-10 | Goodrich Co B F | Heating apparatus for rubber or rubber-like strip material |
US3946096A (en) * | 1970-04-23 | 1976-03-23 | Phillips Petroleum Company | Securing a filamentous extrudate into a base material matrix at least one of which is expandable |
WO2010074727A2 (en) | 2008-12-22 | 2010-07-01 | The Gates Corporation | Method of making composite article with expandable elastomer in compression |
US8246872B2 (en) | 2008-12-22 | 2012-08-21 | The Gates Corporation | Method for making composite article with expandable elastomer in compression |
US9731438B2 (en) | 2008-12-22 | 2017-08-15 | Gates Corporation | Composite article with expandable elastomer in compression |
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