Method for producing foamed molded bodies

US9758613B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9758613-B2
Application numberUS-201314397513-A
CountryUS
Kind codeB2
Filing dateApr 26, 2013
Priority dateApr 30, 2012
Publication dateSep 12, 2017
Grant dateSep 12, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The invention relates to a method for producing foamed molded bodies comprising the steps of A) providing a mold, and B) introducing a foam-forming reaction mixture into the mold under variable pressure of injection, wherein the method is characterized in that the foam-forming reaction mixture has a fiber time of ≧20 s to ≦60 s.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method for producing foamed molded bodies comprising the steps of A) providing a mold, and B) introducing a foam-forming reaction mixture from a mixing head into the mold under variable pressure of injection, wherein the foam-forming reaction mixture exits the mixing head at a speed which decreases over time from an initial exit speed to a decreased exit speed, wherein the initial exit speed and the decreased exit speed are each in the range of >1 m/s to <5 m/s, and wherein the foam-forming reaction mixture has a fiber time at 20° C. of ≧20 s to ≦60 s wherein the foam-forming reaction mixture comprises an emulsion, and wherein the emulsion contains the following constituents: (I) an isocyanate-reactive composition A containing a polyol mixture A1 of at least three polyols A1a, A1 and A1e as continuous phase and (II) at least one physical blowing agent T as disperse phase, wherein: (i) A1a is a polyether polyol having a hydroxyl number of 15 mg KOH/g to 550 mg KOH/g and having a functionality of 1.5 to 6.0, obtained by addition reaction of an epoxide onto one or more starter compounds selected from the group consisting of carbohydrates and di- or higher-functional alcohols; (ii) A1b is a polyether polyol having a hydroxyl number of 100 mg KOH/g to 550 mg KOH/g and having a functionality of 1.5 to 5.0, obtained by addition reaction of an epoxide onto an aromatic amine; and (iii) A1e is a polyester polyether polyol having a hydroxyl number of 100 mg KOH/g to 450 mg KOH/g and having a functionality of 1.5 to 3.5, obtained by addition reaction of an epoxide onto the esterification product of an aromatic dicarboxylic acid derivative and a di- or more highly functional alcohol. 2. The method as claimed in claim 1 , wherein the foam-forming reaction mixture is introduced into the mold at a temporally variable rate. 3. The method as claimed in claim 1 , wherein the ratio of the time in which the foam-forming reaction mixture is introduced into the mold at a temporally variable rate to the cream time of the foam-forming reaction mixture is in the range from 0.1 to 10. 4. The method as claimed in claim 1 , wherein the temporal variation of the introduction rate and/or injection pressure of the foam-forming reaction mixture is effected by varying the power output of a pump motor acting on the reaction mixture. 5. The method as claimed in claim 1 , wherein the foam-forming reaction mixture is obtained from the reaction of a first reaction component comprising said emulsion and a second reaction component and the a first reaction component comprising said emulsion and a second reaction component are each introduced via nozzles into a mixing chamber in said mixing head. 6. The process as claimed in claim 1 , wherein the foam-forming reaction mixture has a fiber time of ≧25 s to ≦55 s. 7. The method as claimed in 1 , wherein the injection pressure is reduced over time in step B). 8. The method as claimed in claim 1 , wherein the injection pressure in step B) is varied by at least 15 bar/s. 9. The method as claimed in claim 1 , wherein the mold in cross section comprises a horizontally disposed floor volume and also vertically disposed volumes in communication with the floor volume. 10. The method as claimed in claim 1 , wherein the mold comprises a pipework line on the outside and a pipework line disposed therein on the inside and the foam-forming reaction mixture is introduced between the inside and outside pipework lines. 11. The method as claimed in claim 1 , wherein the mold comprises two spaced-apart areal elements and the foam-forming reaction mixture is introduced between these areal elements. 12. The method as claimed in claim 1 , wherein the foam-forming reaction mixture is introduced by the mixing head having a mixing chamber and wherein furthermore the outflow cross section of the mixing chamber is varied during the introducing. 13. The method as claimed in claim 1 , wherein the at least one physical blowing agent T is at least one member selected from the group consisting of hydrocarbons, halogenated ethers and perfluorinated hydrocarbons having from 1 to 8 carbon atoms each. 14. A foamed molded body obtainable by a method as claimed in claim 1 . 15. A refrigerator, a freezer or a fridge-freezer combination comprising a foamed molded body as claimed in claim 14 . 16. The method as claimed in claim 2 , wherein the time during which the foam-forming reaction mixture is introduced into the mold at a temporally variable rate is ≧1 s to ≦20 s. 17. The method according to claim 3 , wherein the ratio of the time in which the foam-forming reaction mixture is introduced into the mold at a temporally variable rate to the cream time of the foam-forming reaction mixture is in the range from 0.5 to 5. 18. The method as claimed in claim 4 , wherein the power output of the pump motor is effected by varying the rotary speed of the motor using a frequency converter. 19. The method as claimed in claim 5 , wherein the foam-forming reaction mixture is selected so as to obtain a rigid polyurethane foam. 20. The process as claimed in claim 6 , wherein the foam-forming reaction mixture has a fiber time of ≧30 s to ≦50 s. 21. The method as claimed in 7 , wherein the injection pressure is reduced over time in step B) in a very substantially linear manner. 22. The method as claimed in claim 8 , wherein the injection pressure in step B) is varied by at least 20 bar/s. 23. The refrigerator, freezer or fridge-freezer combination as claimed in claim 15 , wherein the provided mold is a housing component of the refrigerator, of the freezer or of the fridge-freezer combination.

Assignees

Inventors

Classifications

  • B29C44/18Primary

    Filling preformed cavities {(B29C44/1204 takes precedence)} · CPC title

  • organic · CPC title

  • Gate valves; Sliding valves; Cocks (B05B1/326 takes precedence) · CPC title

  • Rigid foams · CPC title

  • using pressure difference, e.g. by injection or by vacuum · CPC title

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What does patent US9758613B2 cover?
The invention relates to a method for producing foamed molded bodies comprising the steps of A) providing a mold, and B) introducing a foam-forming reaction mixture into the mold under variable pressure of injection, wherein the method is characterized in that the foam-forming reaction mixture has a fiber time of ≧20 s to ≦60 s.
Who is the assignee on this patent?
Covestro Deutschland Ag
What technology area does this patent fall under?
Primary CPC classification B29C44/18. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Sep 12 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).