Insulation boards and methods for their manufacture
First Claim
Patent Images
1. A method for producing isocyanurate insulation foams, the method comprising:
- (i) forming a B-side stream of reactants including a polyol and a blowing agent blend, where the blowing agent blend includes isopentane and n-pentane at a weight ratio of isopentane to n-pentane of about 1;
1 to about 2.7;
1 in the substantial absence of cyclopentane, where said step of forming includes introducing the polyol and the blowing agent within a pin mixer under a pressure in excess of about 80 psi and a temperature in excess of about 10°
C.;
(ii) increasing the temperature of the B-side stream of reactants to a temperature of about 16°
C. to about 29°
C. and a pressure of about 1800 psi to about 2400 psi;
(iii) after said step of increasing, delivering the B-side stream of reactants to a mix head, where the temperature of the B-side stream of reactants is increased to about 27°
C. to about 35°
C.;
(iv) introducing an A-side stream of reactants to the mix head at a temperature of about 29°
C. to about 35°
C. and a pressure of about 1800 to about 2400 psi to thereby mix with the B-side stream and form a mixture of polyisocyanurate ingredients;
(v) depositing the mixture of polyisocyanurate ingredients onto a laminator and allowing the mixture of polyisocyanurate ingredients to form a developing foam.
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Abstract
A method for producing polyisocyanurate insulation foams, the method comprising contacting an A-side stream of reactants that includes an isocyanate with a B-side stream of reactants that include a polyol and a blowing agent, where the blowing agent includes isopentane and n-pentane in a substantial absence of cyclopentane.
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Citations
4 Claims
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1. A method for producing isocyanurate insulation foams, the method comprising:
-
(i) forming a B-side stream of reactants including a polyol and a blowing agent blend, where the blowing agent blend includes isopentane and n-pentane at a weight ratio of isopentane to n-pentane of about 1;
1 to about 2.7;
1 in the substantial absence of cyclopentane, where said step of forming includes introducing the polyol and the blowing agent within a pin mixer under a pressure in excess of about 80 psi and a temperature in excess of about 10°
C.;(ii) increasing the temperature of the B-side stream of reactants to a temperature of about 16°
C. to about 29°
C. and a pressure of about 1800 psi to about 2400 psi;(iii) after said step of increasing, delivering the B-side stream of reactants to a mix head, where the temperature of the B-side stream of reactants is increased to about 27°
C. to about 35°
C.;(iv) introducing an A-side stream of reactants to the mix head at a temperature of about 29°
C. to about 35°
C. and a pressure of about 1800 to about 2400 psi to thereby mix with the B-side stream and form a mixture of polyisocyanurate ingredients;(v) depositing the mixture of polyisocyanurate ingredients onto a laminator and allowing the mixture of polyisocyanurate ingredients to form a developing foam. - View Dependent Claims (2, 3, 4)
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Specification