Method for producing skin-covered foamed molded article and resulting product
US-2015360401-A1 · Dec 17, 2015 · US
US9758613B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9758613-B2 |
| Application number | US-201314397513-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2013 |
| Priority date | Apr 30, 2012 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
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.
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.
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
Related publications grouped by family.
Answers are generated from the same data shown on this page.