CN101948563A - Pentane type composite polyether and composition containing same, rigid polyurethane rigid foam and application thereof - Google Patents

Pentane type composite polyether and composition containing same, rigid polyurethane rigid foam and application thereof Download PDF

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CN101948563A
CN101948563A CN2010102639007A CN201010263900A CN101948563A CN 101948563 A CN101948563 A CN 101948563A CN 2010102639007 A CN2010102639007 A CN 2010102639007A CN 201010263900 A CN201010263900 A CN 201010263900A CN 101948563 A CN101948563 A CN 101948563A
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pentane
polyether
preferable
type combined
combined polyether
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CN101948563B (en
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李心强
李欣
郑广朋
于楠
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SHANGHAI DONGDA POLYURETHANE CO Ltd
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SHANGHAI DONGDA POLYURETHANE CO Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/20Climate change mitigation technologies for sector-wide applications using renewable energy

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Abstract

The invention provides pentane type composite polyether, which comprises the following components: polyether polyol 8210H, polyether polyol SA460, foam stabilizer, polyurethane synthesis catalyst, pentane foaming agent and water. In the pentane type composite polyether, pentane is used as the foaming agent; the pentane foaming agent has the advantages of low GWP value and zero ODP value and completely conforms to the environmental protection requirements for replacing HCFC-141B in the industry of a solar water heater, while the cost is low. The composite polyether overcomes the shortcoming of low compatibility between pentane and polyether and has high compatibility with pentane, high flow property and good foaming effect; and the viscosity of the composite polyether is suitable for the production technology of the solar water heater. The composite polymer has obvious advantages on application in the industry of solar water heater. The rigid polyurethane foam prepared by the action between the composite polymer and isocyanate has high heat conductivity and size stability.

Description

Pentane type combined polyether and contain its composition, hard polyurethane foam and application thereof
Technical field
The present invention relates to hard polyurethane foam foaming field, relate in particular to a kind of pentane type combined polyether, the invention still further relates to a kind of composition that contains this pentane type combined polyether, and the hard polyurethane foam and the application thereof that make by this pentane type combined polyether.
Background technology
Along with the widespread use of hard polyurethane foams, its negative impact to environment also more and more is subject to people's attention.The refrigerator ice cabinet industry of China has been transferred to the cyclopentane type combined polyether from HCFC-141B type combined polyether substantially.But in the sun power industry, still based on the HCFC-141B combined polyether.Yet HCFC-141B still can damage atmospheric ozone layer as a kind of transitional product.Under the catalysis of low-carbon economy, " green " the hard polyurethane foam cry with latent value (GWP) value of low global greenhouse effect and the latent value (ODP) of zero ozone depletion is more and more higher.
According to statistics, in order to substitute the HCFC-141B whipping agent, domestic had only several producers of a line brand to attempt having carried out foaming experiments such as HFC-245fa HFC-365mfc Quan Shui after 2007, and carried out the short run popularization.
The big urethane company in east is by the adjustment to the polyethers system, with HFC-245fa, HFC-365mfc is the insulation requirement that the polyurethane foam of whipping agent all can reach the solar water heater product, compressive strength is greater than 150kpa, thermal conductivity 17-19mW/mK, but such whipping agent higher cost has restricted its development, and its GWP value is much higher than pentane (HC) whipping agent, is the whipping agent of relative environmental protection in the greenhouse gases.
Take all factors into consideration for environmental protection, foaming properties each side, by a large amount of evidences, the HC whipping agent can solve hydrogen fluorohydrocarbon (HFC) and full water foamed shortcoming.Tool using value is three kinds of pentamethylene, Skellysolve A and iso-pentane in the HC foaming, is referred to as pentane class whipping agent, and it is owing at room temperature be all liquid state, and it is zero that ODP value is, and the GWP value is very low, and is nontoxic, minimum and come into one's own to environmental influence.
At present, also do not adopt the reason of HC whipping agent to be because the HC whipping agent belongs to inflammable volatile organic compounds in the solar water heater industry, can explode under finite concentration and condition with air, for guaranteeing safety, need existing metering, storage and foaming machine are carried out bigger improvement and increase the safe handling facility, and operative technique needs strict control, thereby equipment cost is high than HCFC, HFC foamed system.But having given the HC whipping agent, present domestic refrigerator industry proves that well safety problem is solved comprehensively.And can use the cheap HC whipping agent that is easy to get by once improvement input, obtain better controlled for production cost to equipment.But because the technology of sun power industry and to urethane flowing property, foaming density etc. require inconsistent, pentane type combined polyether in the refrigerator field is not suitable for the sun power industry, therefore needs badly and seeks a kind of pentane type combined polyether that can be applicable to the solar water heater field.
Summary of the invention
Technical problem to be solved by this invention is in order to have overcome existing combined polyether and the pentane foaming agent consistency is poor, and existing pentane type combined polyether is not suitable for the shortcoming in solar water heater field, a kind of pentane type combined polyether, a kind of composition that is used to prepare hard polyurethane foam are provided, a kind of hard polyurethane foam and application thereof.Pentane type combined polyether of the present invention as whipping agent, has zero odp value, low GWP value, environmental protection and low cost and other advantages with pentane.Combined polyether of the present invention can satisfy the requirement of solar water heater field to hard polyurethane foam performance of heat protective material and manufacturing process well, can make all very excellent hard polyurethane foams of various aspects of performance such as dimensional stability, thermal conductivity, compressive strength.
The invention provides a kind of pentane type combined polyether, it comprises following compositions: polyether glycol 8210H, polyether glycol SA460, suds-stabilizing agent, urethane synthetic catalyst, pentane foaming agent and water.
Wherein, what the mass fraction of each composition was preferable in the pentane type combined polyether of the present invention is: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, suds-stabilizing agent 0.2-0.3 part, urethane synthetic catalyst 0.2-0.35 part, pentane foaming agent 1-1.3 part and water 0.05-0.1 part; What wherein, described urethane synthetic catalyst was preferable is 0.22-0.3 part.
In the present invention's one preferred implementation, described pentane type combined polyether is grouped into by the one-tenth of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, suds-stabilizing agent 0.2-0.3 part, urethane synthetic catalyst 0.2-0.35 part, pentane foaming agent 1.0-1.3 part and water 0.05-0.1 part; What wherein, described urethane synthetic catalyst was preferable is 0.22-0.3 part.
Wherein, described polyether glycol 8210H is the polyether glycol of the special screening for pentane type combined polyether.Described polyether glycol 8210H is the commercially available prod, and its viscosity is 3000-4000mpa.s (25 ℃), and functionality is 4.3, and number-average molecular weight is 560, and hydroxyl value is 400-450mgKOH/g, and moisture is less than 0.1wt%.
Wherein, described polyether glycol SA460 is the commercially available prod, and its viscosity is 12000-15000mpa.s (25 ℃), and functionality is 6, and number-average molecular weight is 730, and hydroxyl value is 440-480mgKOH/g, and moisture is less than 0.1wt%.
Wherein, described suds-stabilizing agent is the conventional all kinds of suds-stabilizing agents that use in hard polyurethane foam field, and preferable is the silicone suds-stabilizing agent, and that better is the B8462 of goldschmidt chemical corporation and/or the L6900 of U.S. Mitugao New Material Group company etc.
Wherein, described urethane synthetic catalyst is the catalyzer that is used for the hard polyurethane foam foaming, can be amines catalyst and/or organo-metallic class catalyzer, and more satisfactory is to unite to use amines catalyst and organo-metallic class catalyzer.Wherein, what described amines catalyst was preferable is tertiary amine catalyst, and that better is N, N, N`, N``, N```-five methyl diethylentriamine and/or triethylenediamine.Described organo-metallic class catalyzer is preferable is in isocaprylic acid potassium, Potassium ethanoate and the potassium oleate one or more.Comprise triethylenediamine and isocaprylic acid potassium in the time of urethane synthetic catalyst the best of the present invention, what wherein the mass ratio of triethylenediamine and isocaprylic acid potassium was preferable is 1: 1-2.5: 1.
Wherein, pentane foaming agent of the present invention can be selected in this area various pentane foaming agents commonly used for use, and as in pentamethylene, Skellysolve A and the iso-pentane one or more, preferable is the mixture or the pentamethylene of pentamethylene and iso-pentane.In described mixture, the mixing quality of pentamethylene and iso-pentane than preferable be 6: 4~8: 2.
What wherein, described water was preferable is deionized water.
In the preferable example of the present invention one, pentane type combined polyether of the present invention comprises the composition of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, silicone suds-stabilizing agent B8462 or L69000.2-0.3 part, N, N, N`, N``, N```-five methyl diethylentriamine 0.02-0.03 part, triethylenediamine 0.1-0.2 part, isocaprylic acid potassium, Potassium ethanoate or potassium oleate 0.08-0.12 part, pentamethylene 0.7-0.13 part, iso-pentane 0-0.3 part, and deionized water 0.05-0.10 part.
In another preferred implementation of the present invention, pentane type combined polyether of the present invention is grouped into by the one-tenth of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, silicone suds-stabilizing agent B8462 or L69000.2-0.3 part, N, N, N`, N``, N```-five methyl diethylentriamine 0.02-0.03 part, triethylenediamine 0.1-0.2 part, isocaprylic acid potassium, Potassium ethanoate or potassium oleate 0.08-0.12 part, pentamethylene 0.7-0.13 part, iso-pentane 0-0.3 part, and deionized water 0.05-0.10 part.
Preferably, as required, also can contain other conventional additives of this area in the pentane type combined polyether of the present invention, as long as it does not influence the technique effect of pentane type combined polyether of the present invention substantially.
The preparation method of pentane type combined polyether of the present invention is: with above-mentioned each composition by mass fraction having the uniform mixing in the still of puddling of security device, promptly obtain pentane type combined polyether.Described mixing is preferably carried out in stainless steel is puddled still, and what mixing time was preferable is 2-5 hour.
Pentane type combined polyether of the present invention is mainly used in the polyurethane insulation coating of solar water heater, and than present industry present situation, it possesses tangible environment-friendly advantage, excellent flowability energy, excellent size stability and excellent thermal conductivity.Pentane type combined polyether of the present invention directly places itself and isocyanic ester between the shell of solar water heater and the inner bag and foams in use, can obtain hard polyurethane foam, thereby play the effect of filling and being incubated.
Therefore, the present invention also provides a kind of composition that is used to prepare polyurethane foam, it comprises pentane type combined polyether of the present invention and isocyanic ester, and the mass ratio of wherein said pentane type combined polyether and isocyanic ester is 1: 1-1: 1.3, and preferable is 1: 1-1: 1.2.What described isocyanic ester was preferable is polymeric MDI (having another name called polyphenyl polymethylene polyisocyanates or thick MDI), polymeric MDI among the present invention adopts the 44V20 of Bayer (BAYER) company, 5005 of the M20S of BASF AG or U.S.'s Hensel graceful (huntsman) urethane company limited.If the consideration cost factor, what the mass ratio of pentane type combined polyether of the present invention and isocyanic ester was preferable is 1: 1-1: 1.2.If do not consider cost factor, preferable is more than 1: 1.2, can improve the foamy quality well.Composition of the present invention before use, wherein pentane type combined polyether and isocyanic ester do not contact all the time, therefore form that can suit is sold and is preserved said composition, during use pentane type combined polyether and isocyanic ester is mixed according to the above ratio foaming.
The present invention also provides a kind of hard polyurethane foam, and it is made by following method: is 1 with described pentane type combined polyether and isocyanic ester in mass ratio: 1-1: 1.3 ratio is mixed post-foaming, gets final product.What described isocyanic ester was preferable is polymeric MDI (having another name called polyphenyl polymethylene polyisocyanates or thick MDI), and the polymeric MDI among the present invention adopts the 44V20 of Bayer (BAYER) company, the M20S of BASF AG or the U.S..
What wherein, described blowing temperature was preferable is 20-25 ℃.Preferably adopt the high pressure machine to foam.
The present invention also provides the application of a kind of described hard polyurethane foam as the polyurethane insulation coating of solar water heater.
Among the present invention, above-mentioned optimum condition can be on the basis that meets this area general knowledge arbitrary combination, promptly obtain the preferable example of the present invention.
The raw material that the present invention uses and reagent is all commercially available gets.
Positive progressive effect of the present invention is:
1, as whipping agent, pentane foaming agent has the advantage of low GWP value and zero odp value to pentane type combined polyether of the present invention with pentane, meet the environmental requirement that substitutes HCFC-141B in the solar water heater industry fully, and cost is low.
2, pentane type combined polyether of the present invention has overcome the shortcoming of pentane and polyethers consistency difference, filters out product with pentane consistency excellence as main body polyethers of the present invention from the polyether glycol with excellent properties.The combined polyether that obtains thus has that not only the consistency with pentane is good, and good flowing properties have excellent foaming effect, and the viscosity of combined polyether is applicable to the production technique of solar water heater.Application in the solar water heater industry has remarkable advantages.
3, the hard polyurethane foam that obtains after pentane type combined polyether of the present invention and the isocyanic ester effect has excellent thermal conductivity, dimensional stability.
Embodiment
Further specify the present invention with embodiment below, but the present invention is not limited.
Polyether glycol 8210H, the SA460 that uses among the following embodiment is Shanghai Dongda Polyurethane Co., Ltd's product.Polyether glycol NT403 purchases in the big chemical industry limited liability company in Shandong blue star east.
Silicone suds-stabilizing agent B8462 purchases in goldschmidt chemical corporation, and L6900 purchases the Mitugao New Material Group company in the U.S..
The whipping agent pentamethylene is purchased in the Beijing Dongfang Yakeli Chemical Science Co., Ltd.
Isocyanic ester is a polymeric MDI, purchases in Bayer A.G, and model is 44V20.
Embodiment 1
One, the prescription of ring/iso-pentane type combined polyether:
7 parts of polyether glycol 8210H, polyether glycol SA4603 part, silicone suds-stabilizing agent B84620.2 part, N, N, N`, N``, 0.02 part of N```-five methyl diethylentriamine, 0.20 part of triethylenediamine, 0.08 part in isocaprylic acid potassium, 0.7 part of pentamethylene, 0.10 part of 0.3 part of iso-pentane and deionized water.
Two, the preparation method of ring/iso-pentane type combined polyether: the prescription according to ring/iso-pentane type combined polyether stirs above-mentioned each composition speed with 500 rev/mins under room temperature 2 hours, and blowing promptly.
Three, the preparation of hard polyurethane foam lagging material: will encircle/iso-pentane combined polyether and isocyanic ester in 20 ℃ react to such an extent that foam density be 35kg/m by mass ratio at 1: 1.15 3Sun power hard polyurethane foam lagging material, the physical and chemical performance of this hard polyurethane foam sees Table 1.
Four, the preparation of contrast 1 hard polyurethane foam lagging material:
1, HCFC-141B combined polyether preparation method: with 41109 parts of polyether glycols, polyether glycol NT4031 part, silicone suds-stabilizing agent B84620.2 part, N, N, N`, N``, 0.02 part of N```-five methyl diethylentriamine, 0.1 part of triethylenediamine, 0.1 part in isocaprylic acid potassium, 0.10 part of 1.5 parts of HCFC-141B and the deionized water speed with 500 rev/mins under room temperature stirred 2 hours, and blowing promptly gets the HCFC-141B combined polyether.
2, the preparation of contrast 1 hard polyurethane foam lagging material: 1: 1.15 in 20 ℃ react to such an extent that foam density be 35.2kg/m by mass ratio HCFC-141B combined polyether and isocyanic ester 3Sun power hard polyurethane foam lagging material, this physical and chemical performance that contrasts 1 hard polyurethane foam sees Table 1.
Table 1
Figure BSA00000245458800071
Embodiment 2
One, the prescription of cyclopentane type combined polyether:
8 parts of polyether glycol 8210H, polyether glycol SA4602 part, silicone suds-stabilizing agent L69000.3 part, N, N, N`, N``, 0.05 part of 0.03 part of N```-five methyl diethylentriamine, 0.15 part of triethylenediamine, 0.12 part of Potassium ethanoate, 1.0 parts of pentamethylene and deionized water.
Two, the preparation method of cyclopentane type combined polyether: the prescription according to the cyclopentane type combined polyether stirs above-mentioned each composition speed with 500 rev/mins under room temperature 2 hours, and blowing promptly.
Three, the preparation of hard polyurethane foam lagging material: 1: 1.0 in 25 ℃ react to such an extent that foam density be 37kg/m by mass ratio pentamethylene combined polyether and isocyanic ester 3Sun power hard polyurethane foam lagging material, the physical and chemical performance of this hard polyurethane foam sees Table 2.
Four, the preparation of contrast 2 hard polyurethane foam lagging materials:
1, HCFC-141B combined polyether preparation method: with 41109 parts of polyether glycols, polyether glycol NT4031 part, silicone suds-stabilizing agent L69000.3 part, N, N, N`, N``, 0.03 part of N```-five methyl diethylentriamine, 0.15 part of triethylenediamine, 0.12 part of Potassium ethanoate, 0.05 part of 1.8 parts of HCFC-141B and the deionized water speed with 500 rev/mins under room temperature stirred 2 hours, and blowing promptly gets the HCFC-141B combined polyether.
2, the preparation of contrast 2 hard polyurethane foam lagging materials: 1: 1.0 react to such an extent that foam density be 37.2kg/m by mass ratio HCFC-141B combined polyether and isocyanic ester 3Sun power hard polyurethane foam lagging material, this physical and chemical performance that contrasts 2 hard polyurethane foams sees Table 2.
Table 2
Figure BSA00000245458800081
Embodiment 3
One, the prescription of cyclopentane type combined polyether:
6 parts of polyether glycol 8210H, polyether glycol SA4604 part, silicone suds-stabilizing agent L69000.2 part, N, N, N`, N``, 0.08 part of 0.02 part of N```-five methyl diethylentriamine, 0.1 part of triethylenediamine, 0.1 part of potassium oleate, 1.3 parts of pentamethylene and deionized water.
Two, the preparation method of cyclopentane type combined polyether: the prescription according to the cyclopentane type combined polyether stirs above-mentioned each composition speed with 500 rev/mins under room temperature 2 hours, and blowing promptly.
Three, the preparation of hard polyurethane foam lagging material: with above-mentioned cyclopentane type combined polyether and isocyanic ester mass ratio is to react to such an extent that foam density be 38kg/m at 1: 1.30 3Sun power hard polyurethane foam lagging material.
Four, the preparation of contrast 3 hard polyurethane foam lagging materials:
1, HCFC-141B combined polyether preparation method: with 41109 parts of polyether glycols, polyether glycol NT4031 part, silicone suds-stabilizing agent L69000.2, N, N, N`, N``, 0.02 part of N```-five methyl diethylentriamine, 0.10 part of triethylenediamine, 0.10 part of potassium oleate, 0.08 part of 2.0 parts of HCFC-141B and the deionized water speed with 500 rev/mins under room temperature stirred 2 hours, and blowing promptly gets the HCFC-141B combined polyether.
2, the preparation of contrast 3 hard polyurethane foam lagging materials: 1: 1.30 react to such an extent that foam density be 38kg/m by mass ratio HCFC-141B combined polyether and isocyanic ester 3Sun power hard polyurethane foam lagging material, this physical and chemical performance that contrasts 3 hard polyurethane foams sees Table 3.
Table 3
Figure BSA00000245458800091

Claims (10)

1. a pentane type combined polyether is characterized in that it comprises following compositions: polyether glycol 8210H, polyether glycol SA460, suds-stabilizing agent, urethane synthetic catalyst, pentane foaming agent and water.
2. pentane type combined polyether as claimed in claim 1, it is characterized in that: described pentane type combined polyether comprises the composition of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, suds-stabilizing agent 0.2-0.3 part, urethane synthetic catalyst 0.2-0.35 part, pentane foaming agent 1-1.3 part and water 0.05-0.1 part; What wherein, described urethane synthetic catalyst was preferable is 0.22-0.3 part;
Preferable, described pentane type combined polyether is grouped into by the one-tenth of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, suds-stabilizing agent 0.2-0.3 part, urethane synthetic catalyst 0.20-0.35 part, pentane foaming agent 1.0-1.3 part and water 0.05-0.10 part; What wherein, described urethane synthetic catalyst was preferable is 0.22-0.3 part.
3. pentane type combined polyether as claimed in claim 1 or 2 is characterized in that: described suds-stabilizing agent is the silicone suds-stabilizing agent, and that described silicone suds-stabilizing agent is preferable is silicone suds-stabilizing agent B8462 and/or L6900.
4. as each described pentane type combined polyether in the claim 1~3, it is characterized in that: described urethane synthetic catalyst is amines catalyst and/or organo-metallic class catalyzer, what described amines catalyst was preferable is tertiary amine catalyst, that better is N, N, N`, N``, N```-five methyl diethylentriamine and/or triethylenediamine; Described organo-metallic class catalyzer is preferable is in isocaprylic acid potassium, Potassium ethanoate and the potassium oleate one or more.
5. pentane type combined polyether as claimed in claim 4 is characterized in that: described urethane synthetic catalyst comprises triethylenediamine and isocaprylic acid potassium, and what wherein the mass ratio of triethylenediamine and isocaprylic acid potassium was preferable is 1: 1-2.5: 1.
6. as each described pentane type combined polyether in the claim 1~5, it is characterized in that: described pentane foaming agent is one or more in pentamethylene, Skellysolve A and the iso-pentane, and preferable is the mixture or the pentamethylene of pentamethylene and iso-pentane; In described mixture, the mixing quality of pentamethylene and iso-pentane than preferable be 6: 4~8: 2.
7. as each described pentane type combined polyether in the claim 1~6, it is characterized in that: described pentane type combined polyether comprises the composition of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, silicone suds-stabilizing agent B8462 or L69000.2-0.3 part, N, N, N`, N``, N```-five methyl diethylentriamine 0.02-0.03 part, triethylenediamine 0.1-0.2 part, isocaprylic acid potassium, Potassium ethanoate or potassium oleate 0.08-0.12 part, pentamethylene 0.7-0.13 part, iso-pentane 0-0.3 part, and deionized water 0.05-0.10 part;
Preferable, described pentane type combined polyether is grouped into by the one-tenth of following mass fraction: polyether glycol 8210H 6-8 part, polyether glycol SA4602-4 part, silicone suds-stabilizing agent B8462 or L69000.2-0.3 part, N, N, N`, N``, N```-five methyl diethylentriamine 0.02-0.03 part, triethylenediamine 0.1-0.2 part, isocaprylic acid potassium, Potassium ethanoate or potassium oleate 0.08-0.12 part, pentamethylene 0.7-0.13 part, iso-pentane 0-0.3 part, and deionized water 0.05-0.10 part.
8. composition that is used to prepare polyurethane foam, it is characterized in that: it comprises as each described pentane type combined polyether and isocyanic ester in the claim 1~7, the mass ratio of wherein said pentane type combined polyether and isocyanic ester is 1: 1-1: 1.3, and preferable is 1: 1-1: 1.2; What described isocyanic ester was preferable is polymeric MDI.
9. hard polyurethane foam, it is characterized in that: it is made by following method: is 1 with each described pentane type combined polyether and isocyanic ester in the claim 1~7 in mass ratio: 1-1: 1.3 ratio is mixed post-foaming, gets final product; What wherein, the temperature of described foaming was preferable is 20-25 ℃; Preferable in the high pressure machine, the carrying out of foaming; What described isocyanic ester was preferable is polymeric MDI.
10. hard polyurethane foam as claimed in claim 9 is as the application of the polyurethane insulation coating of solar water heater.
CN2010102639007A 2010-08-24 2010-08-24 Pentane type composite polyether and composition containing same, rigid polyurethane rigid foam and application thereof Expired - Fee Related CN101948563B (en)

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CN103570902A (en) * 2012-07-18 2014-02-12 上海东大聚氨酯有限公司 High density polyurethane and raw material composition, combined polyether, preparation method and application thereof
CN104387559A (en) * 2014-11-27 2015-03-04 山东一诺威新材料有限公司 Half-pored sound-absorbing and heat-insulating premixed polyether for spraying and preparation method thereof
CN107266700A (en) * 2017-07-18 2017-10-20 成都新柯力化工科技有限公司 A kind of stability pentane system environment-friendly foaming agent for polyurethane foam

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