WO1991012287A1 - Procede de production de mousses n=c=o et leur pre- et post-expansions regulees - Google Patents
Procede de production de mousses n=c=o et leur pre- et post-expansions regulees Download PDFInfo
- Publication number
- WO1991012287A1 WO1991012287A1 PCT/US1991/000845 US9100845W WO9112287A1 WO 1991012287 A1 WO1991012287 A1 WO 1991012287A1 US 9100845 W US9100845 W US 9100845W WO 9112287 A1 WO9112287 A1 WO 9112287A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- blowing agent
- foam
- process according
- expansion
- mixing zone
- Prior art date
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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
- C08J9/149—Mixtures of blowing agents covered by more than one of the groups C08J9/141 - C08J9/143
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/127—Mixtures of organic and inorganic blowing agents
-
- 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
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/14—Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
-
- 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
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/14—Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
- C08J2203/142—Halogenated saturated hydrocarbons, e.g. H3C-CF3
-
- 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
- C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2375/04—Polyurethanes
Definitions
- Polyurethanes and other associated polymers based on diisocyanate chemistry are foamed for use in thermal insulation, floatation, and rigidizing applications.
- these foam products can be employed in refrigeration systems, building materials, storage tanks, truck and railway tankers and cars which form the bulk of the thermal insulation industry.
- these foams can be used in a flotation environment which encompasses, the filling of cavities in boats, barges, drilling platforms, etc., with low- density foams to prevent sinking of the vessel when accidents occur.
- These foams have also been used to rigidize aircraft, helicopter blades, automobiles, and the like.
- the reactants which are reacted with diisocyanates vary greatly depending on the desired end product.
- the most widely used reactants are those compounds which terminate with an -OH group, -NH group or a -SH group.
- the other reactant employed in the reaction is selected from diamines, water, dimethylol urea, and even dimethylol elamine, with the diamine being more preferred.
- the "modified" phenolics are so called, since the reaction is not an acid cure, as in production of pure phenolics.
- the isocyanates employed in such reactions range in functionality from about 2.0 to about 2.9.
- the polymers can be prepared using prepolymers which have a functionality well above 3.0.
- blowing agents In order to foam these polymers into low- density materials, blowing agents are used. In the past, the chlorofluorocarbons were the preferred blowing agents. However, due to the world-wide limitations on, and upcoming elimination of these products, alternative blowing agents must be found.
- U.S. Patent 4,337,318 to Doyle is an example illustrating alternate blowing agents which have been used to replace the chlorofluorocarbons.
- liquid carbon dioxide is used to achieve complete and immediate foaming of the polyurethane as it emerges from a mixing zone. This technique is known as "pre-expansion" of the foam. The process occurs in the absence of "post-expansion", i.e., the expansion of the foam which occurs over time after the foam leaves the mixing zone.
- any desired percentage of pre-expansion and post-expansion may be obtained, where liquid C0 2 is preferably employed as the principal blowing agent, with the further use of co-blowing agents and other techniques such as altering the pressure to the mixing zone that allow for the controlled pre- and post-expansion of the foamed polymer.
- the process of the present invention comprises:
- the equipment employed in preforming the above process is essentially the same as the standard equipment employed with conventional processes.
- either positive-displacement piston-type pumps, or variable-speed gear or vane type pumps may be employed.
- the only requirement is that the equipment must be capable of producing pressures to the mixing zone on the order of about 300 to about 5000 psi.
- each pump pumping a separate component to the mixing zone.
- two or more of the components may be pre- blended and then pumped to the mixing zone a ⁇ a separate stream.
- formulation ⁇ may be altered, modified, and changed almost instantaneously.
- the blowing agent(s) may be introduced at any point prior to the mixing zone, e.g., into one or more of the reactant streams, or it may be introduced directly into the mixing zone.
- the preferred principal blowing agent is liquid carbon dioxide / because of low cost, high gas production, and good stability associated with its use.
- any liquid gas having a boiling point below approximately -100"F may be used, such as nitrogen, helium, argon, tetrafluoromethane, fluoroform, hexafluoroethane, chlorotrifluoromethane, or mixtures thereof.
- One technique for controlling the amount of pre- and post-expansion of the foam involves the use of co- blowing agents.
- Other co-blowing agents include higher- boiling solvents, such as methylene chloride, ethyl chloride, chloroform, methyl chloroform, and hydrochlorofluorocarbons, such as Freon 21, 22, 113, 114 and the like.
- non-halogenated hydrocarbons such as hexane, heptane, butene-1, butane, and the like may be used.
- the co-blowing agents may be introduced as a separate stream(s) to the mixing zone, or may be pre- blended into one or more of the other components prior to the mixing zone.
- the co-blowing agent would compri ⁇ e a minor amount of the total blowing agent, in an amount ⁇ ufficient to provide the desirable amount of post-expansion.
- water employed as the co-blowing agent
- about 1 lb. of water provides the same amount of foaming as about 7 lbs. of the liquid carbon dioxide.
- approximately 3 lbs. of Freon 22 would provide the same amount of foaming as about 2 lbs. of the liquid carbon dioxide.
- controlled amounts of post expansion of the foam can be obtained by lowering the pressure at which the ingredients are subjected to at the mixing zone.
- the use of pressures at the mixing zone of about 300-500 psi provides for considerable amounts of post- expansion.
- the higher the pressure at the mixing zone the lesser the amount of post-expan ⁇ ion i ⁇ derived from the liquid carbon dioxide.
- the degree of po ⁇ t-expansion is related to the percentage of C0 2 in the mixture. In particular, the higher the percentage of carbon dioxide in the total mix, the lesser the amount of post- expansion that may be obtained.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US47924690A | 1990-02-13 | 1990-02-13 | |
US479,246 | 1990-02-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1991012287A1 true WO1991012287A1 (fr) | 1991-08-22 |
Family
ID=23903220
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1991/000845 WO1991012287A1 (fr) | 1990-02-13 | 1991-02-12 | Procede de production de mousses n=c=o et leur pre- et post-expansions regulees |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0517858A4 (fr) |
CA (1) | CA2075975A1 (fr) |
WO (1) | WO1991012287A1 (fr) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996014354A2 (fr) * | 1994-11-02 | 1996-05-17 | Solvay Fluor Und Derivate Gmbh | Agents d'expansion contenant du dioxyde de carbone liquide |
EP0722975A1 (fr) * | 1994-11-28 | 1996-07-24 | Bayer Ag | Procédé de dissolution de dioxyde de carbone dans un polymère liquide |
US5620710A (en) * | 1993-07-14 | 1997-04-15 | Foaming Technologies Cardio Bv | Froth system for continuous manufacture of polyurethane foam slab-stocks |
US5665287A (en) * | 1993-07-14 | 1997-09-09 | Foaming Technologies Cardio Bv | Froth process for continous manufacture of polyurethane foam slab-stocks |
US5831004A (en) * | 1994-10-27 | 1998-11-03 | Affymax Technologies N.V. | Inhibitors of metalloproteases, pharmaceutical compositions comprising same and methods of their use |
US5840698A (en) * | 1994-10-27 | 1998-11-24 | Affymax Technologies N.V. | Inhibitors of collagenase-1 and stormelysin-I metalloproteases, pharmaceutical compositions comprising same and methods of their use |
USRE37012E1 (en) * | 1993-07-14 | 2001-01-09 | Foaming Technologies, Cardio BV | Froth system for continuous manufacture of polyurethane foam slab-stocks |
DE19502708C2 (de) * | 1995-01-28 | 2003-10-23 | Solvay Fluor & Derivate | Verfahren zur Herstellung von Ein- oder Mehrkomponenten-Polyurethanschaumstoffen |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4337318A (en) * | 1980-09-30 | 1982-06-29 | Doyle Earl N | Process for the total pre-expansion of polyurethane foam |
US4853417A (en) * | 1987-06-19 | 1989-08-01 | Sumitomo Bayer Urethane Co., Ltd | Process for manufacturing rigid polyurethane foam |
US4931487A (en) * | 1988-03-04 | 1990-06-05 | Dow Chemical Company | Chain extenders for polyurethanes |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB904003A (en) * | 1958-02-06 | 1962-08-22 | Dunlop Rubber Co | Method and apparatus for the production of cellular synthetic rubber |
GB2116574A (en) * | 1982-03-19 | 1983-09-28 | Ici Plc | Method of manufacturing polyurethane foams |
GB8329628D0 (en) * | 1983-11-05 | 1983-12-07 | Rubber & Plastic Res Ass | Polyurethanes |
DE3916873C2 (de) * | 1988-05-27 | 2003-01-09 | Elastogran Gmbh | Verfahren zur Herstellung von zellhaltigen Kunststoffen nach dem Polyisocyanat-polyadditionsverfahren und eine Katalysatorkombination hierfür |
US4906672A (en) * | 1988-07-29 | 1990-03-06 | Pmc, Inc. | Blowing agents for polyurethane foam |
-
1991
- 1991-02-12 WO PCT/US1991/000845 patent/WO1991012287A1/fr active Search and Examination
- 1991-02-12 CA CA 2075975 patent/CA2075975A1/fr not_active Abandoned
- 1991-02-12 EP EP19910907521 patent/EP0517858A4/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4337318A (en) * | 1980-09-30 | 1982-06-29 | Doyle Earl N | Process for the total pre-expansion of polyurethane foam |
US4853417A (en) * | 1987-06-19 | 1989-08-01 | Sumitomo Bayer Urethane Co., Ltd | Process for manufacturing rigid polyurethane foam |
US4931487A (en) * | 1988-03-04 | 1990-06-05 | Dow Chemical Company | Chain extenders for polyurethanes |
Non-Patent Citations (1)
Title |
---|
See also references of EP0517858A4 * |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE37115E1 (en) * | 1993-07-14 | 2001-03-27 | Foaming Technologies Cardio Bv | Froth system for continuous manufacture of polyurethane foam slab-stocks |
USRE37012E1 (en) * | 1993-07-14 | 2001-01-09 | Foaming Technologies, Cardio BV | Froth system for continuous manufacture of polyurethane foam slab-stocks |
USRE37075E1 (en) * | 1993-07-14 | 2001-02-27 | Carlo Fiorentini | Froth system for continuous manufacture of polyurethane foam slab-stocks |
US5620710A (en) * | 1993-07-14 | 1997-04-15 | Foaming Technologies Cardio Bv | Froth system for continuous manufacture of polyurethane foam slab-stocks |
US5629027A (en) * | 1993-07-14 | 1997-05-13 | Foaming Technologies Cardio Bv | Froth system for continuous manufacture of polyurethane foam slab-stocks |
US5639483A (en) * | 1993-07-14 | 1997-06-17 | Foaming Technologies Cardio Bv | Froth system for continuous manufacture of polyurethane foam slab-stocks |
US5665287A (en) * | 1993-07-14 | 1997-09-09 | Foaming Technologies Cardio Bv | Froth process for continous manufacture of polyurethane foam slab-stocks |
US5840698A (en) * | 1994-10-27 | 1998-11-24 | Affymax Technologies N.V. | Inhibitors of collagenase-1 and stormelysin-I metalloproteases, pharmaceutical compositions comprising same and methods of their use |
US5929278A (en) * | 1994-10-27 | 1999-07-27 | Affymax Technologies N.V. | Inhibitors of metalloproteases, pharmaceutical compositions comprising same and methods of their use |
US5831004A (en) * | 1994-10-27 | 1998-11-03 | Affymax Technologies N.V. | Inhibitors of metalloproteases, pharmaceutical compositions comprising same and methods of their use |
US6307101B1 (en) | 1994-10-27 | 2001-10-23 | David A. Campbell | Inhibitors of metalloproteases, pharmaceutical compositions comprising same and methods of their use |
WO1996014354A3 (fr) * | 1994-11-02 | 1997-02-13 | Solvay Fluor & Derivate | Agents d'expansion contenant du dioxyde de carbone liquide |
WO1996014354A2 (fr) * | 1994-11-02 | 1996-05-17 | Solvay Fluor Und Derivate Gmbh | Agents d'expansion contenant du dioxyde de carbone liquide |
US6303667B1 (en) | 1994-11-02 | 2001-10-16 | Solvay Fluor Und Derivate | Foaming agents containing liquid carbon dioxide |
EP0722975A1 (fr) * | 1994-11-28 | 1996-07-24 | Bayer Ag | Procédé de dissolution de dioxyde de carbone dans un polymère liquide |
DE19502708C2 (de) * | 1995-01-28 | 2003-10-23 | Solvay Fluor & Derivate | Verfahren zur Herstellung von Ein- oder Mehrkomponenten-Polyurethanschaumstoffen |
Also Published As
Publication number | Publication date |
---|---|
EP0517858A4 (en) | 1993-07-28 |
CA2075975A1 (fr) | 1991-08-14 |
EP0517858A1 (fr) | 1992-12-16 |
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