WO2017063255A1 - Biomass-based polyurethane spray foam plastic and method for preparation thereof - Google Patents

Biomass-based polyurethane spray foam plastic and method for preparation thereof Download PDF

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WO2017063255A1
WO2017063255A1 PCT/CN2015/096026 CN2015096026W WO2017063255A1 WO 2017063255 A1 WO2017063255 A1 WO 2017063255A1 CN 2015096026 W CN2015096026 W CN 2015096026W WO 2017063255 A1 WO2017063255 A1 WO 2017063255A1
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bio
polyurethane spray
component
spray foam
polyol
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PCT/CN2015/096026
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French (fr)
Chinese (zh)
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崔爱华
林永飞
魏建辉
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江苏绿源新材料有限公司
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Publication of WO2017063255A1 publication Critical patent/WO2017063255A1/en

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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
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    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
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    • C08G18/36Hydroxylated esters of higher fatty acids
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
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    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
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    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4804Two or more polyethers of different physical or chemical nature
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
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    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6633Compounds of group C08G18/42
    • C08G18/6662Compounds of group C08G18/42 with compounds of group C08G18/36 or hydroxylated esters of higher fatty acids of C08G18/38
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6666Compounds of group C08G18/48 or C08G18/52
    • C08G18/6696Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/36 or hydroxylated esters of higher fatty acids of C08G18/38
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    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
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    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-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
    • C08J9/14Working-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
    • C08J9/143Halogen containing compounds
    • C08J9/144Halogen containing compounds containing carbon, halogen and hydrogen only
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/52Phosphorus bound to oxygen only
    • C08K5/521Esters of phosphoric acids, e.g. of H3PO4
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    • C08G2110/00Foam properties
    • C08G2110/0025Foam properties rigid
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    • C08G2110/00Foam properties
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    • C08G2110/005< 50kg/m3
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/14Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
    • C08J2203/142Halogenated saturated hydrocarbons, e.g. H3C-CF3
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04Polyurethanes
    • C08J2375/06Polyurethanes from polyesters
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04Polyurethanes
    • C08J2375/08Polyurethanes from polyethers
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-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
    • C08J9/14Working-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
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    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/014Additives containing two or more different additives of the same subgroup in C08K

Definitions

  • Bio-based polyurethane spray foam plastic and preparation method thereof are Bio-based polyurethane spray foam plastic and preparation method thereof.
  • the present invention relates to a polyurethane spray foam, and more particularly to a bio-based polyol preparation polyurethane spray foam and a process for the preparation thereof.
  • Polyurethane rigid foam is widely used in many fields of the national economy such as refrigerators, freezers, cold storage plates, sandwich panels, pipe insulation, refrigerated containers, building energy conservation, etc. due to its excellent thermal insulation properties.
  • Polyurethane spray foam molding is The two-component polyurethane foam composition is directly sprayed onto the surface of the object for foam molding, and has the advantages of: strong adhesion to the substrate; easy processing, no matter what shape surface can be formed by spraying to form a thermal insulation layer, thereby greatly improving Labor productivity; at the same time, it has the functions of waterproof, sound absorption and sound insulation.
  • a polyether compound of a prior art polyurethane rigid foam whose main component is a petroleum-removed product, is a non-renewable resource, and has a complicated processing process, high cost, and environmental pollution, and its price is also Fluctuating with fluctuations in oil prices.
  • Bio-based polyether polyols are polyol compounds synthesized from soybean oil, rapeseed oil, cottonseed oil or palm oil. They are environmentally friendly, renewable resources and have been industrially produced. From the perspective of environmental protection and resource recycling, the use of bio-based polyether polyols is the main direction of future research.
  • bio-based polyether polyols have a relatively large molecular weight and a low hydroxyl value, they are mainly used in the modification of soft foams and polyisocyanate foams in polyurethanes.
  • rigid foams and sprayed polyurethanes with lower indices or the introduction of bio-based polyether polyols, which still require a large amount of petroleum-based polyesters and polyester polyols.
  • polyurethane rigid foam in polyurethane spray foam that has both high levels of bio-based materials and similar performance characteristics to foams made from existing petroleum-based materials.
  • a bio-based polyurethane spray foam characterized in that a polyurethane spray composition white component prepared by using at least one bio-based polyether polyol as a raw material is mixed with an isocyanate component to be foamed and polymerized.
  • the composition of the polyurethane composite white material is a polyol component of at least one bio-based polyether polyol, an amine and/or metal salt catalyst, a physical and/or chemical foaming agent, and a foam stabilization And optional flame retardant.
  • the bio-based polyol has a weight ratio of the entire polyol component of from 5 to 75%, preferably from 20% to 50%.
  • the bio-based polyether polyol can be produced from various bio-based materials, including but not limited to: soybean oil, jatropha oil, palm oil, corn oil, peanut oil, cottonseed oil, rapeseed oil, olive oil, and a mixture of them.
  • a particularly preferred bio-based polyether polyol is a soybean oil polyol.
  • the isocyanate component is a crude polymerized diphenylformamidine diisocyanate (PMDI) or an improved crude polymethylene polyphenylene having an average functionality between 2. 5-3.
  • the ratio of the mass ratio of the polyurethane component to the isocyanate component is 1: 1-1. 5, preferably a ratio of 1:1.
  • the spray foam has an average density of from 30 to 80 kg/m 3 , preferably a density of from 35 to 55 kg/m 3 .
  • the catalyst for bio-based polyurethane spray foam comprises an amine and/or metal salt catalyst, wherein the amine catalyst is a tertiary amine catalyst including pentamethyldiethylenetriamine, N,N-dimethyl ring One or more of hexylamine, triethylenediamine, triethylamine, and didimethylaminoethyl ether; the metal salt catalyst includes potassium isooctanoate, quaternary ammonium formate, potassium acetate, Two or more kinds of dibutyltin dilaurate, stannous octoate and potassium oleate. Since the polyurethane spray foam reacts very quickly, the solidification molding is normally completed in a dozen seconds. The amount of catalyst added is much larger than that required for other polyurethane foams, accounting for 5% to 15% of the polyurethane spray composition white component. The amount used.
  • a combination of water and a low boiling point compound is used as the blowing agent of the present invention.
  • Low boiling point fluorine-containing compounds such as HFC-245fa, HFC-365mfc and HFC_134a, which are used singly or in combination.
  • Particularly preferred blowing agents for use in the present invention are 1,1-dichloro-1-fluoroethane (HCFC-141B), 1, 1, 1, 3, 3_pentafluoropropene (HFC-245fa) and 1 1, 1, 3, 3-pentafluorobutyrate (HFC-365) and mixtures thereof.
  • HCFC-141B 1, 1, 1, 1, 3, 3_pentafluoropropene
  • HFC-365 1 1, 1, 3, 3-pentafluorobutyrate
  • a small amount of foam stabilizer which is advantageous for foaming can be used in the polyurethane spray foaming to stabilize the foaming reaction mixture in the initial stage of polymerization, which helps to adjust the pore diameter and produce closed pores, thereby improving the heat insulating property.
  • the foam stabilizer used is one or two of a non-hydrolyzed silicon-carbon surfactant and a non-silicone surfactant. Since the speed of spray foaming is rapid, the cells of the foam are relatively good. Therefore, the foam stabilizer used plays a more important role in the storage stability of the polyurethane sprayed white component before foaming.
  • Suitable flame retardants include phosphonates/salts, phosphites/salts and phosphates/salts (eg, dimethyl methylphosphonate, ammonium polyphosphate, and various cyclic phosphates and phosphonates) It is applied to bio-based polyurethane spray foam. Since polyurethane spray foam molding is formed by atomization and mixing foaming of foaming gun head, when flame retardant is selected, it is more liquid-oriented and has relatively good storage stability.
  • tris(2-chloroethyl) phosphate TCEP
  • tris(2-chloropropyl) phosphate TCPP
  • triethyl phosphate TEP
  • dimethyl methylphosphonate DMMP
  • tris(2-chloropropyl)phosphate TCPP
  • triethyl phosphate TEP
  • DMMP dimethyl methylphosphonate
  • the preparation method of the bio-based polyurethane spray foam comprises the following steps: (1) mixing a polyol combination, a catalyst, a foaming agent, a foam stabilizer and an optional flame retardant in a ratio, thereby preparing Polyurethane composite white component; (2) The combined white component and the isocyanate component obtained in the step (1) are sprayed on a wooden board or a cement board by a high-pressure sprayer at a fixed ratio, and the two components are rapidly reacted and solidified. Formed to form a bio-based polyurethane spray foam.
  • the product of the present invention has a high content of bio-based material for use in thermal insulation and water-repellent spraying of walls or roofs, so that the foam has properties similar to those produced with all petroleum-based materials.
  • polyether polyol A sucrose starting refined polyether polyol, hydroxyl value 380mgK0H / g, viscosity at 25 ° C is about 10000 centipoise, hydroxyl functionality is 6;
  • polyether polyol B ethylenediamine starting polyether polyol, hydroxyl value 760mgK0H / g, viscosity at 25 ° C is about 25000 centipoise, hydroxyl functionality is 4;
  • bio-based polyol E epoxidized soybean oil-based vegetable oil polyol, hydroxyl value 380mgK0H / g, viscosity at 25 ° C is about 5000 centipoise, the functionality is 4. 5;
  • Reference example 1 is a common formulation for polyurethane spray foams used in GB50404-2007.
  • the moiety is replaced with one or two bio-based polyols. If you want to adjust the foaming speed, you can adjust the amount of catalyst; if you want to adjust the foam density, you can adjust the amount of water and physical foaming agent.
  • the bio-based polyol is combined with an aliphatic polyol to ensure the basic properties of the polyurethane spray foam and maximize the amount of bio-based polyol in combination with a high-functionality aliphatic polyol.
  • different amounts should be used according to the characteristics of different products.
  • Select Example 4 to carry out on-site foaming, and prepare the polyurethane sprayed white component according to Table 2, and then spray the prepared white component and isocyanate component in a fixed ratio on a wooden board by a high-pressure sprayer. The reaction solidifies and forms a bio-based polyurethane spray foam.
  • the foam properties obtained by the foaming mechanism are better than the laboratory foaming properties.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

Disclosed is a biomass-based polyurethane spray foam plastic, characterized as a polyurethane spray produced through foam polymerization by mixing a white material component, prepared with at least one biomass-based polyether polyol as a raw ingredient, with an isocyanate component. The product of the present invention has a high content of biomass-based materials, and when used as insulation and water-proofing spray for walls and roofs, the foam material has similar performance to fully petroleum-based foams.

Description

生物基聚氨酯喷涂泡沬塑料及其制备方法 技术领域  Bio-based polyurethane spray foam plastic and preparation method thereof
[0001] 本发明涉及聚氨酯喷涂泡沫塑料, 具体涉及一种生物基多元醇制备聚氨酯喷涂 泡沫及其制备方法。  [0001] The present invention relates to a polyurethane spray foam, and more particularly to a bio-based polyol preparation polyurethane spray foam and a process for the preparation thereof.
背景技术  Background technique
[0002] 聚氨酯硬质泡沫因其优良的绝热性能被广泛应用于冰箱、 冷柜、 冷库板、 夹心 板、 管道保温、 冷藏集装箱、 建筑节能等国民经济的多个领域, 聚氨酯喷涂泡 沫发泡成型是将双组分聚氨酯泡沫组合料直接喷射到物体表面发泡成型, 其优 点是: 与基材粘接力强; 加工简易, 无论何种形状表面都可以通过喷涂形成保 温隔热层, 因而大大提高了劳动生产率; 同时兼具防水、 吸音、 隔音等功能。  [0002] Polyurethane rigid foam is widely used in many fields of the national economy such as refrigerators, freezers, cold storage plates, sandwich panels, pipe insulation, refrigerated containers, building energy conservation, etc. due to its excellent thermal insulation properties. Polyurethane spray foam molding is The two-component polyurethane foam composition is directly sprayed onto the surface of the object for foam molding, and has the advantages of: strong adhesion to the substrate; easy processing, no matter what shape surface can be formed by spraying to form a thermal insulation layer, thereby greatly improving Labor productivity; at the same time, it has the functions of waterproof, sound absorption and sound insulation.
[0003] 现有技术的聚氨酯硬质泡沫的组合白料的多羟基化合物, 其主要的成分为石油 提制产品, 是不可再生资源, 其加工生产过程复杂, 成本高且污染环境, 其价 格也随石油价格的波动而波动。 生物基聚醚多元醇是大豆油、 菜籽油、 棉籽油 或棕榈油为起始原料合成的多元醇化合物, 是种环保的、 可再生的资源, 并且 已经实现了工业化生产。 从环保以及资源循环利用角度来看, 采用生物基聚醚 多元醇是今后研究的主要方向。  [0003] A polyether compound of a prior art polyurethane rigid foam, whose main component is a petroleum-removed product, is a non-renewable resource, and has a complicated processing process, high cost, and environmental pollution, and its price is also Fluctuating with fluctuations in oil prices. Bio-based polyether polyols are polyol compounds synthesized from soybean oil, rapeseed oil, cottonseed oil or palm oil. They are environmentally friendly, renewable resources and have been industrially produced. From the perspective of environmental protection and resource recycling, the use of bio-based polyether polyols is the main direction of future research.
[0004] 由于生物基聚醚多元醇的分子量较大, 羟值偏低, 在聚氨酯方面主要应用在软 质泡沫和聚异氰酸酯泡沫的改性方面。 对于指数较低的硬质泡沫及喷涂聚氨酯 中的应用于还相对较少, 或者所引入的生物基聚醚多元醇的含量极低, 仍然需 要大量的石油基聚酯和聚酯多元醇。 在聚氨酯喷涂泡沫塑料仍然需要一种聚氨 酯硬质泡沫材料, 该材料既具有高含量生物基材料, 又具有与现有石油基原料 制备的泡沫材料类似的性能特性。  [0004] Since bio-based polyether polyols have a relatively large molecular weight and a low hydroxyl value, they are mainly used in the modification of soft foams and polyisocyanate foams in polyurethanes. There are still relatively few applications for rigid foams and sprayed polyurethanes with lower indices, or the introduction of bio-based polyether polyols, which still require a large amount of petroleum-based polyesters and polyester polyols. There is still a need for a polyurethane rigid foam in polyurethane spray foam that has both high levels of bio-based materials and similar performance characteristics to foams made from existing petroleum-based materials.
发明概述  Summary of invention
技术问题  technical problem
[0005] 本发明的目的在于提供一种具有高含量的生物基材料, 应用在墙面或屋顶的保 温防水喷涂中, 使泡沫材料具有与用全部石油基材料生产的泡沫类似的性能的 生物基聚氨酯喷涂泡沫塑料及其制备方法。 [0005] It is an object of the present invention to provide a bio-based material having a high content, which is applied to thermal insulation and water-repellent spraying of a wall or a roof, so that the foam has properties similar to those of foams produced from all petroleum-based materials. Bio-based polyurethane spray foam and preparation method thereof.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0006] 本发明的技术解决方案是:  The technical solution of the present invention is:
[0007] 一种生物基聚氨酯喷涂泡沫塑料, 其特征在于由以至少一种生物基聚醚多元醇 为原料制备的聚氨酯喷涂组合白料组分与异氰酸酯组分混合发泡聚合生成的。  [0007] A bio-based polyurethane spray foam, characterized in that a polyurethane spray composition white component prepared by using at least one bio-based polyether polyol as a raw material is mixed with an isocyanate component to be foamed and polymerized.
[0008] 所述的聚氨酯组合白料的组分为至少一种生物基聚醚多元醇的多元醇组分, 胺 类和 /或金属盐类催化剂、 物理和 /或化学发泡剂、 泡沫稳定剂以及任选阻燃剂 。 其中所述的生物基多元醇占整个多元醇组分的重量比为 5-75%, 其中优选 20%- 50%。  [0008] The composition of the polyurethane composite white material is a polyol component of at least one bio-based polyether polyol, an amine and/or metal salt catalyst, a physical and/or chemical foaming agent, and a foam stabilization And optional flame retardant. The bio-based polyol has a weight ratio of the entire polyol component of from 5 to 75%, preferably from 20% to 50%.
[0009] 所述的生物基聚醚多元醇可由各种生物基原料生产, 包括但不限于: 大豆油、 麻风树油、 棕榈油、 玉米油、 花生油、 棉籽油、 菜籽油、 橄榄油和它们的混合 物。 特别优选的生物基聚醚多元醇是由大豆油多元醇。  [0009] The bio-based polyether polyol can be produced from various bio-based materials, including but not limited to: soybean oil, jatropha oil, palm oil, corn oil, peanut oil, cottonseed oil, rapeseed oil, olive oil, and a mixture of them. A particularly preferred bio-based polyether polyol is a soybean oil polyol.
[0010] 所述的异氰酸酯组分为平均官能度在 2. 5-3. 5之间的粗制聚合二苯基甲垸二异 氰酸酯 (PMDI) 或改进的粗制多亚甲基多苯基多异氰酸酯; 所述的聚氨酯喷涂组 合白料组分与异氰酸酯组分的质量比为 1 : 1-1. 5, 优选比例 1 : 1。 所述的喷涂 泡沫塑料的平均密度在 30-80kg/m 3, 优选密度在 35-55 kg/m 3[0010] The isocyanate component is a crude polymerized diphenylformamidine diisocyanate (PMDI) or an improved crude polymethylene polyphenylene having an average functionality between 2. 5-3. The ratio of the mass ratio of the polyurethane component to the isocyanate component is 1: 1-1. 5, preferably a ratio of 1:1. The spray foam has an average density of from 30 to 80 kg/m 3 , preferably a density of from 35 to 55 kg/m 3 .
[0011] 用于生物基聚氨酯喷涂泡沫塑料的催化剂包括胺类和 /或金属盐类催化剂, 其 中胺类催化剂为叔胺类催化剂包括五甲基二乙烯三胺、 N,N-二甲基环己胺、 三 乙烯二胺、 三乙胺、 双二甲胺基乙基醚中的一种两种或多种; 所述金属盐类催 化剂为包括异辛酸钾、 甲酸季铵盐、 醋酸钾、 二月桂酸二丁基锡、 辛酸亚锡和 油酸钾的一种两种或多种。 由于聚氨酯喷涂泡沫反应非常迅速, 固化成型正常 在十几秒内完成, 因些所添加的催化剂的量较其它聚氨酯泡沫所需用量要大的 多, 占聚氨酯喷涂组合白料组分 5%_15%的用量。  [0011] The catalyst for bio-based polyurethane spray foam comprises an amine and/or metal salt catalyst, wherein the amine catalyst is a tertiary amine catalyst including pentamethyldiethylenetriamine, N,N-dimethyl ring One or more of hexylamine, triethylenediamine, triethylamine, and didimethylaminoethyl ether; the metal salt catalyst includes potassium isooctanoate, quaternary ammonium formate, potassium acetate, Two or more kinds of dibutyltin dilaurate, stannous octoate and potassium oleate. Since the polyurethane spray foam reacts very quickly, the solidification molding is normally completed in a dozen seconds. The amount of catalyst added is much larger than that required for other polyurethane foams, accounting for 5% to 15% of the polyurethane spray composition white component. The amount used.
[0012] 水和低沸点化合物的组合用作本发明的发泡剂。 低沸点含氟化合物, 例如 HFC- 245fa、 HFC-365mfc 和 HFC_134a, 它们单独使用或者组合使用。 特别优选用于 本发明的发泡剂是 1, 1-二氯 -1-氟乙垸 (HCFC-141B)、 1, 1, 1, 3, 3_五氟丙垸 (HFC -245fa) 和 1, 1, 1, 3, 3-五氟丁垸 (HFC-365 ) 和它们的混合物。 正常垸类发泡剂 因为安全问题很少用于聚氨酯喷涂泡沫中, 比如环戊垸、 异戊垸等。 [0012] A combination of water and a low boiling point compound is used as the blowing agent of the present invention. Low boiling point fluorine-containing compounds such as HFC-245fa, HFC-365mfc and HFC_134a, which are used singly or in combination. Particularly preferred blowing agents for use in the present invention are 1,1-dichloro-1-fluoroethane (HCFC-141B), 1, 1, 1, 3, 3_pentafluoropropene (HFC-245fa) and 1 1, 1, 3, 3-pentafluorobutyrate (HFC-365) and mixtures thereof. Normal anthraquinone blowing agent Because safety issues are rarely used in polyurethane spray foams, such as cyclopentamidine, isovalerone, and the like.
[0013] 聚氨酯喷涂发泡中可用到有利于发泡的少量泡沫稳定剂, 以在聚合初始阶段稳 定发泡反应混合物, 有助于调节孔径, 产生闭合的孔, 从而改进绝热性能。 所 用的泡沫稳定剂为非水解硅碳类表面活性剂和非硅酮类表面活性剂中一种或两 种。 由于喷涂发泡的速度迅速, 所以泡沫的泡孔相对较好, 因此, 所用的泡沫 稳定剂所起的作用更偏向于聚氨酯喷涂组合白料组分在发泡之前的储存稳定性  [0013] A small amount of foam stabilizer which is advantageous for foaming can be used in the polyurethane spray foaming to stabilize the foaming reaction mixture in the initial stage of polymerization, which helps to adjust the pore diameter and produce closed pores, thereby improving the heat insulating property. The foam stabilizer used is one or two of a non-hydrolyzed silicon-carbon surfactant and a non-silicone surfactant. Since the speed of spray foaming is rapid, the cells of the foam are relatively good. Therefore, the foam stabilizer used plays a more important role in the storage stability of the polyurethane sprayed white component before foaming.
[0014] 合适的阻燃剂包括膦酸酯 / 盐、 亚磷酸酯 / 盐和磷酸酯 / 盐( 例如甲基膦酸二 甲酯、 多磷酸铵、 和各种环磷酸酯和膦酸酯可应用于生物基聚氨酯喷涂泡沫中 。 由于聚氨酯喷涂发泡成型是通过发泡枪头雾化混合发泡成型, 因而在选用阻 燃剂时更偏向于液态的, 储存稳定性相对较好的原料, 比如三 (2-氯乙基) 磷 酸酯 (TCEP) 、 三 (2-氯丙基) 磷酸酯 (TCPP) 、 磷酸三乙酯(TEP)和甲基膦酸 二甲酯(DMMP)的一种或多种, 其中优选三 (2-氯丙基) 磷酸酯 (TCPP) 和磷酸 三乙酯(TEP)。 [0014] Suitable flame retardants include phosphonates/salts, phosphites/salts and phosphates/salts (eg, dimethyl methylphosphonate, ammonium polyphosphate, and various cyclic phosphates and phosphonates) It is applied to bio-based polyurethane spray foam. Since polyurethane spray foam molding is formed by atomization and mixing foaming of foaming gun head, when flame retardant is selected, it is more liquid-oriented and has relatively good storage stability. Such as tris(2-chloroethyl) phosphate (TCEP), tris(2-chloropropyl) phosphate (TCPP), triethyl phosphate (TEP) and dimethyl methylphosphonate (DMMP) Or more, among which tris(2-chloropropyl)phosphate (TCPP) and triethyl phosphate (TEP) are preferred.
[0015] 所述的生物基聚氨酯喷涂泡沫塑料的制备方法, 包括以下步骤: (1 ) 将多元 醇组合、 催化剂、 发泡剂、 泡沫稳定剂以及任选阻燃剂按照比例混合均匀, 制 得聚氨酯组合白料组分; (2 ) 将步骤 (1 ) 中制得的组合白料组分与异氰酸酯 组分按固定比例, 通过高压喷涂机喷在木板或者水泥板上, 两组分快速反应固 化成形, 生成生物基聚氨酯喷涂泡沫塑料。  [0015] The preparation method of the bio-based polyurethane spray foam comprises the following steps: (1) mixing a polyol combination, a catalyst, a foaming agent, a foam stabilizer and an optional flame retardant in a ratio, thereby preparing Polyurethane composite white component; (2) The combined white component and the isocyanate component obtained in the step (1) are sprayed on a wooden board or a cement board by a high-pressure sprayer at a fixed ratio, and the two components are rapidly reacted and solidified. Formed to form a bio-based polyurethane spray foam.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0016] 本发明产品具有高含量的生物基材料, 应用在墙面或屋顶的保温防水喷涂中, 使泡沫材料具有与用全部石油基材料生产的泡沫类似的性能。  [0016] The product of the present invention has a high content of bio-based material for use in thermal insulation and water-repellent spraying of walls or roofs, so that the foam has properties similar to those produced with all petroleum-based materials.
实施该发明的最佳实施例  BEST MODE FOR CARRYING OUT THE INVENTION
本发明的最佳实施方式  BEST MODE FOR CARRYING OUT THE INVENTION
[0017] 通过以下实施例进一步说明本发明, 但本发明不限于以下实施例, 除非另有说 明, 否则, 所有以 "份数"和 "百分比"给出的量都应该理解为是以重量计的 。 以下材料用于生产实施例的聚氨酯泡沫材料: [0018] 表 1 聚氨酯原料简介[0017] The invention is further illustrated by the following examples, but the invention is not limited to the following examples, unless otherwise indicated, all amounts given by "parts" and "percents" should be understood as being by weight. of. The following materials were used to produce the polyurethane foam of the examples: [0018] Table 1 Introduction to Polyurethane Raw Materials
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[表 1] 序号 原料 备注 [Table 1] No. Material Remarks
1 聚醚多元醇 A 蔗糖起始的精制聚醚多元 醇, 羟值 380mgK0H/g, 在 25°C的粘度约为 10000厘 泊, 羟基官能度为 6; 1 polyether polyol A sucrose starting refined polyether polyol, hydroxyl value 380mgK0H / g, viscosity at 25 ° C is about 10000 centipoise, hydroxyl functionality is 6;
2 聚醚多元醇 B 乙二胺起始的聚醚多元醇 , 羟值 760mgK0H/g, 在 25 °C的粘度约为 25000厘泊 , 羟基官能度为 4; 2 polyether polyol B ethylenediamine starting polyether polyol, hydroxyl value 760mgK0H / g, viscosity at 25 ° C is about 25000 centipoise, hydroxyl functionality is 4;
3 阻燃聚醚多元醇 C 含溴起始的阻燃聚醚多元 醇, 羟值 200mgK0H/g, 在 25 °C的粘度约为 15000厘 泊, 羟基官能度为 2; 3 flame retardant polyether polyol C bromine-containing flame retardant polyether polyol, hydroxyl value 200mgK0H / g, viscosity at 25 ° C is about 15000 centipoise, hydroxyl functionality is 2;
4 聚酯多元醇 D 邻苯二甲酸酯的芳族聚酯 多元醇, 羟值 310mgK0H/g , 25 °C的粘度约为 3000厘 泊, 官能度为 2; 4 Polyester polyol D phthalate aromatic polyester polyol, hydroxyl value 310mgK0H / g, viscosity at 25 ° C is about 3000 centipoise, functionality is 2;
5 生物基多元醇 E 环氧大豆油基植物油多元 醇, 羟值 380mgK0H/g, 在 25 °C的粘度约为 5000厘泊 , 官能度为 4. 5;  5 bio-based polyol E epoxidized soybean oil-based vegetable oil polyol, hydroxyl value 380mgK0H / g, viscosity at 25 ° C is about 5000 centipoise, the functionality is 4. 5;
6 生物基多元醇 F 植物油多元醇, 羟值 60mg  6 Bio-based polyol F vegetable oil polyol, hydroxyl value 60mg
KOH/g, 25°C的粘度约为 6 00厘泊, 官能度为 3, 依 据中国专利申请号 201110 054557. X制得 7 催化剂 A 五甲基二乙烯三胺 KOH/g, viscosity at 25 ° C of about 600 cps, functionality of 3, according to Chinese patent application number 201110 054557. X 7 Catalyst A pentamethyldiethylenetriamine
8 催化剂 B 三乙烯二胺  8 Catalyst B Triethylenediamine
9 催化剂 c 二月桂酸二丁基锡  9 Catalyst c Dibutyltin dilaurate
10 泡沫稳定剂 硅氧垸表面活性剂  10 Foam Stabilizer Silicon Oxide Surfactant
11 阻燃剂 A 三 (2-氯丙基) 磷酸酯 (  11 flame retardant A tris(2-chloropropyl) phosphate (
TCPP)  TCPP)
12 阻燃剂 B 磷酸三乙酯(TEP) 12 Flame Retardant B Triethyl Phosphate (TEP)
13 发泡剂 1, 1-二氯 -1-氟乙垸(HCFC 13 blowing agent 1, 1-dichloro-1-fluoroacetamidine (HCFC
-141B)  -141B)
14 异氰酸酯 聚合二苯基甲垸二异氰酸 酯(PMDI), NC0基含量约 为 32. 4, 25°C的粘度约为 25厘泊 14 Isocyanate Polymerized diphenylformamidine diisocyanate (PMDI), NC0 content of about 32. 4, viscosity at 25 ° C is about 25 centipoise
[0019] 按下表 2中所列的重量份数的各组分混合, 并异氰酸酯组分与白料组合重量比 为 1 : 1的情况下反应, 产生自由发泡的泡沫材料。 使用本领域普通技术人员已 知的手动混合步骤制备这些泡沫材料, 在泡沫固化成型后, 检测泡沫性能。 [0019] The components in the parts by weight listed in Table 2 below were mixed, and the weight ratio of the isocyanate component to the white component was 1:1, resulting in a free-foamed foam. These foams were prepared using a manual mixing procedure known to those skilled in the art to determine foam properties after the foam was cured.
[0020] 表 2 聚氨酯泡沫组分配参数 (重量份)  Table 2 Polyurethane Foam Group Distribution Parameters (Parts by Weight)
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实倒 实例 細 实 細 細Actually, the example is fine and detailed.
1 2 3 4 5 6 7 S1 2 3 4 5 6 7 S
1 聚離 A 25 25 25 25 25 25 25 1 Separation A 25 25 25 25 25 25 25
2 鰣多元 15 15 15 15 15 15 15 20 2 鲥Multi 15 15 15 15 15 15 15 20
Hj^lSl 多元 Hj^lSl multiple
3 10 10 10 10 10 10 10 藤 C  3 10 10 10 10 10 10 10 Vine C
4 50 10 10 20 4 50 10 10 20
5 50 40 35 49 40 20 5 50 40 35 49 40 20
E  E
6 10 15 10  6 10 15 10
¥  ¥
7 2 2 2 2 2 2 2 2 7 2 2 2 2 2 2 2 2
S 23 25 25 25 25 23 25 25S 23 25 25 25 25 23 25 25
9 1 1 1 1 1 I I 19 1 1 1 1 1 I I 1
10 25 25 25 25 25 25 25 2510 25 25 25 25 25 25 25 25
11 15 15 15 15 15 15 35 3511 15 15 15 15 15 15 35 35
12 10 10 10 10 10 10 12 10 10 10 10 10 10
Ϊ3 水 iJ» LO 13 1J3 LO iJO LO ID Ϊ3 water iJ» LO 13 1J3 LO iJO LO ID
H 25 25 25 25 25 20 20 20H 25 25 25 25 25 20 20 20
15 159 m 150 150 ISO 159 15» 150 参考例 1是用于 GB50404-2007的聚氨酯喷涂泡沫的常用配方。 在实施例中, 用 一种或两种生物基多元醇替代部分。 如需调节发泡速度, 可调节催化剂用量; 如需调节泡沫密度, 可调节水和物理发泡剂的用量。 15 159 m 150 150 ISO 159 15» 150 Reference example 1 is a common formulation for polyurethane spray foams used in GB50404-2007. In an embodiment, the moiety is replaced with one or two bio-based polyols. If you want to adjust the foaming speed, you can adjust the amount of catalyst; if you want to adjust the foam density, you can adjust the amount of water and physical foaming agent.
将密度、 导热系数、 氧指数这样关键的泡沫性能与对照泡沫材料对比, 有的好 一些, 有的差一些。 但是通过各组合料的配比的调整可以达到的最为合适的原 配比, 性能达标, 成本最优化, 生物基聚醚多元醇使用量最佳。  Comparing the key foam properties such as density, thermal conductivity, and oxygen index with the control foam, some are better or worse. However, the most suitable original ratio can be achieved by adjusting the ratio of each compound, the performance is up to standard, the cost is optimized, and the bio-based polyether polyol is used in the best amount.
表 3 喷涂泡沫各项性能参数 Table 3 Performance parameters of spray foam
Figure imgf000009_0001
Figure imgf000009_0001
从表 3可以看出, 生物基多元醇与脂肪族多元醇组合, 在高官能度的脂肪族多 元醇的配合下, 保证聚氨酯喷涂泡沫的各项基本性能, 将生物基多元醇的用量 最大化, 同时, 在使用不同生物基多元醇时要根据不同的产品的特性使用不同 的量。 选取实例 4进行喷涂现场发泡, 根据表 2制得聚氨酯喷涂组合白料组分, 然后通过高压喷涂机将制得的组合白料组分与异氰酸酯组分按固定比例, 喷在 木板上, 快速反应固化成形, 生成生物基聚氨酯喷涂泡沫塑料。 通过发泡机制 得的泡沫性能较实验室发泡性能更佳。  As can be seen from Table 3, the bio-based polyol is combined with an aliphatic polyol to ensure the basic properties of the polyurethane spray foam and maximize the amount of bio-based polyol in combination with a high-functionality aliphatic polyol. At the same time, when using different bio-based polyols, different amounts should be used according to the characteristics of different products. Select Example 4 to carry out on-site foaming, and prepare the polyurethane sprayed white component according to Table 2, and then spray the prepared white component and isocyanate component in a fixed ratio on a wooden board by a high-pressure sprayer. The reaction solidifies and forms a bio-based polyurethane spray foam. The foam properties obtained by the foaming mechanism are better than the laboratory foaming properties.
Figure imgf000009_0002
Figure imgf000009_0002
前述的本发明的实施例是为了说明而非限制性的目的。 文中所述的实施方式可 在不背离本发明精神和范围的前提下进行各种变化或修改, 这对本领域技术人 员而言是显而易见的。 本发明的范围由所附权利要求限定。  The foregoing embodiments of the invention have been presented for purposes of illustration It will be apparent to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention. The scope of the invention is defined by the appended claims.

Claims

权利要求书 Claim
[权利要求 1] 一种生物基聚氨酯喷涂泡沫塑料, 其特征是: 由至少一种生物基聚醚 多元醇为原料制备的聚氨酯喷涂组合白料组分与异氰酸酯组分混合发 泡聚合生成的。  [Claim 1] A bio-based polyurethane spray foam, characterized in that: a polyurethane spray composition white component prepared from at least one bio-based polyether polyol is mixed with an isocyanate component to form a foaming polymerization.
[权利要求 2] 根据权利要求 1所述的生物基聚氨酯喷涂泡沫塑料, 其特征是: 所述 的至少一种生物基聚醚多元醇为原料制备的聚氨酯喷涂组合白料的组 分为至少一种生物基聚醚多元醇的多元醇组分, 胺类和 /或金属盐类 催化剂, 物理和 /或化学发泡剂, 泡沫稳定剂以及任选阻燃剂。  [Claim 2] The bio-based polyurethane spray foam according to claim 1, wherein: the at least one bio-based polyether polyol is prepared by using at least one component of the polyurethane sprayed composite white material. A polyol component of a bio-based polyether polyol, an amine and/or metal salt catalyst, a physical and/or chemical blowing agent, a foam stabilizer, and optionally a flame retardant.
[权利要求 3] 根据权利要求 2所述的生物基聚氨酯喷涂泡沫塑料, 其特征是: 所述 的至少一种生物基聚醚多元醇的多元醇组分中生物基多元醇的重量比 为 5-75%。  [Claim 3] The bio-based polyurethane spray foam according to claim 2, wherein: the weight ratio of the bio-based polyol in the polyol component of the at least one bio-based polyether polyol is 5 -75%.
[权利要求 4] 根据权利要求 1、 2或 3所述的生物基聚氨酯喷涂泡沫塑料, 其特征是 : 所述的生物基聚醚多元醇选自大豆油、 麻风树油、 棕榈油、 玉米油 、 花生油、 棉籽油、 菜籽油、 橄榄油或它们的混合物。  [Claim 4] The bio-based polyurethane spray foam according to claim 1, 2 or 3, wherein: the bio-based polyether polyol is selected from the group consisting of soybean oil, jatropha oil, palm oil, and corn oil. , peanut oil, cottonseed oil, rapeseed oil, olive oil or a mixture thereof.
[权利要求 5] 根据权利要求 1、 2或 3所述的生物基聚氨酯喷涂泡沫塑料, 其特征是 : 所述的异氰酸酯组分为平均官能度在 2. 5-3. 5之间的聚合多苯基多 异氰酸酯; 生物基聚醚多元醇为原料制备的聚氨酯喷涂组合白料组分 与异氰酸酯组分的质量比为 1 : 1-1. 5。  The polymerization between 2. 5-3. 5 is more than 5. 5-3. 5。 The phenyl polyisocyanate; the ratio of the mass ratio of the polyurethane component to the isocyanate component is 1: 1-1.
[权利要求 6] 根据权利要求 1所述的生物基聚氨酯喷涂泡沫塑料, 其特征是: 所述 的喷涂泡沫塑料的平均密度在 30-80kg/m 3[Claim 6] The bio-based polyurethane spray foam according to claim 1, wherein: the spray foam has an average density of 30 to 80 kg/m 3 .
[权利要求 7] 根据权利要求 2所述的生物基聚氨酯喷涂泡沫塑料, 其特征是: 所述 的胺类和 /或金属盐类催化剂中胺类催化剂为叔胺类催化剂包括五甲 基二乙烯三胺、 N,N-二甲基环己胺、 三乙烯二胺、 三乙胺、 双二甲胺 基乙基醚中的一种两种或多种; 所述金属盐类催化剂为包括异辛酸钾 、 甲酸季铵盐、 醋酸钾、 二月桂酸二丁基锡、 辛酸亚锡和油酸钾的一 种两种或多种; 所述的物理发泡剂为水; 所述的化学发泡剂为 1, 1-二 氯 -1-氟乙垸、 1, 1, 1, 3, 3-五氟丙垸、 1, 1, 1, 3, 3-五氟丁垸中的一种 或多种。 [Claim 7] The bio-based polyurethane spray foam according to claim 2, wherein: the amine catalyst in the amine and/or metal salt catalyst is a tertiary amine catalyst including pentamethyldivinyl Two or more kinds of triamine, N,N-dimethylcyclohexylamine, triethylenediamine, triethylamine, didimethylaminoethyl ether; the metal salt catalysts include Two or more kinds of potassium octoate, quaternary ammonium formate, potassium acetate, dibutyltin dilaurate, stannous octoate and potassium oleate; the physical foaming agent is water; the chemical foaming agent One or more of 1,1-dichloro-1-fluoroethane, 1, 1, 1, 3, 3-pentafluoropropane, 1, 1, 1, 3, 3-pentafluoropyrene .
[权利要求 8] 根据权利要求 2所述的生物基聚氨酯喷涂泡沫塑料, 其特征是: 所述 的泡沫稳定剂为非水解硅碳类表面活性剂和非硅酮类表面活性剂中一 种或两种; 所述的阻燃剂为三 (2-氯乙基) 磷酸酯、 三 (2-氯丙基) 磷酸酯、 磷酸三乙酯和甲基膦酸二甲酯的一种或多种。 [Claim 8] The bio-based polyurethane spray foam according to claim 2, wherein: the foam stabilizer is one of a non-hydrolyzed silicon-carbon surfactant and a non-silicone surfactant or Two; the flame retardant is one or more of tris(2-chloroethyl)phosphate, tris(2-chloropropyl)phosphate, triethyl phosphate and dimethyl methylphosphonate .
[权利要求 9] 一种权利要求 1所述的生物基聚氨酯喷涂泡沫塑料的制备方法, 其特 征是: 包括以下步骤: (1 ) 将多元醇组合、 催化剂、 发泡剂、 泡沫 稳定剂以及任选阻燃剂按照比例混合均匀, 制得聚氨酯喷涂组合白料 组分; (2) 将步骤 (1 ) 中制得的组合白料组分与异氰酸酯组分按固 定比例, 通过高压喷涂机喷在木板或者水泥板上, 两组分快速反应固 化成形, 生成生物基聚氨酯喷涂泡沫塑料。  [Claim 9] A method for preparing a bio-based polyurethane spray foam according to claim 1, comprising the steps of: (1) combining a polyol, a catalyst, a foaming agent, a foam stabilizer, and The flame retardant is uniformly mixed in proportion to obtain a polyurethane spray composition white component; (2) the combined white component and the isocyanate component obtained in the step (1) are sprayed at a fixed ratio through a high pressure spray machine. On the wood or cement board, the two components are rapidly reacted and solidified to form a bio-based polyurethane spray foam.
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