CN105295018A - Modified cardanol-based polyether polyol and high-fire-resistant hard polyurethane foam prepared by modified cardanol-based polyether polyol and preparation method thereof - Google Patents

Modified cardanol-based polyether polyol and high-fire-resistant hard polyurethane foam prepared by modified cardanol-based polyether polyol and preparation method thereof Download PDF

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CN105295018A
CN105295018A CN201510798040.XA CN201510798040A CN105295018A CN 105295018 A CN105295018 A CN 105295018A CN 201510798040 A CN201510798040 A CN 201510798040A CN 105295018 A CN105295018 A CN 105295018A
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cardanol
polyether polyol
reaction
mannich
warming
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郭亚莉
钟东南
孙志武
陈志强
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TENGZHOU CHEMTECH MATERIAL SCIENCE Co Ltd
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TENGZHOU CHEMTECH MATERIAL SCIENCE Co Ltd
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Abstract

The invention discloses a modified cardanol-based polyether polyol and high-fire-resistant hard polyurethane foam prepared by the modified cardanol-based polyether polyol and a preparation method thereof. The polyether polyol takes cardanol, paraformaldehyde, diethanolamine, diethylenetriamine, tribromoaniline, melamine, oxirane and epoxypropane as raw materials, the raw materials are reacted for synthesis of cardanol Mannich polyether polyol, a hydroxyl value is 200-700mg/gKOH, the moisture is less than or equal to 1.0%, the viscosity is 1000-12000 mPa.s (at 25 DEG C), and the cardanol-based polyether polyol can be taken as a polyhydric alcohol component which can be used in the hard polyurethane foam. The product has advantage of adjustable functionality, contains a flame-retardant group, and has good compatibility with a cyclopentane foaming agent.

Description

A kind of modification cardanol based polyether polyol and with its high flame retardant hard polyurethane foams prepared and preparation method thereof
Technical field
The present invention relates to a kind of modification cardanol based polyether polyol and with its high flame retardant hard polyurethane foams prepared and preparation method thereof.
Background technology
In recent years, the fire disaster caused by architecture exterior wall insulating materials especially rigid polyurethane foam (RPUF) happens occasionally, cause great loss of life and personal injury and property damage, create severe social influence, this seriously constrains the development of polyurethane heat insulation material, and fire-retardant research is extremely urgent." GB8624-2012 material of construction and the product burns grading performance " that come into effect on October 1st, 2013 is inner, explicitly call for for metope insulation foamed plastic, B1 level material must meet limiting oxygen index(LOI) LOI >=30%, and B2 level material must meet LOI >=26%." GB50016-2014 Code for fire protection design of buildings " different fire ratings to architecture exterior wall insulating materials that on May 1st, 2015 formally implements have made specified in more detail (see table 1), for common polyurethane heat insulation material, generally can reach B2 grade standard, be only applicable to lower level building, and for the even A grade standard of the B1 required by middle-high building, this type of polyurethane material that can realize real large-scale application have not been reported.
In urethane, adding fire retardant or in polyether structure, introduce ignition-proof element or structure, is realize two fire-retardant main paties, is called additive flame retardant and structure-type (response type) is fire-retardant.Although it is simpler directly to add fire retardant technique in foaming raw material, cost is also minimum, but there is easily precipitation, affect the defects such as foam monolith performance, and due to the consumption of fire retardant limited, the RPUF of simple interpolation fire retardant generally only can reach about LOI25%, structure-type fire retardant (flame retarding polyether) does not have this misgivings, and it is present in polyurethane structural, can not separate out; Participate in the foamable reaction of urethane, generally do not affect the overall performance of foam; In formula, it even can also be added to 100 parts.In the flame retardant area of RPUF, the flame retarding polyether seeking excellent performance has more potential competitive power.
The gordian technique of flame retarding polyether is the preparation of flame retardant type initiator and the synthesis of polyethers, and the initiator developed at present is based on Halogen system (Br, Cl), phosphorus system and nitrogen series elements, and each series elements system cross development, interpenetrates.Comparatively speaking, nitrogen series elements is due to the low cigarette of low toxicity, and flame retarding efficiency is good and cheap, and world in recent years flame retardant area obtains extensive concern.Containing nitrogen compound as Dyhard RU 100, trimeric cyanamide, cyanogen urea acid trimeric cyanamide etc.; necessarily applied; it has been generally acknowledged that nitrogenous flame ratardant plays multiple flame retardant efficiency at condensed phase and gas phase simultaneously; as heat absorption, generate rare gas element, promote into charcoal, form expansion barrier layer and melting and move heat etc.; fire-retardant mechanism is unique, is consistent with the current requirement of preserving the ecological environment.
At present, at structure-type flame retarding polyether preparing technical field, research emphasis both domestic and external and difficult point are structure design and the synthesis of initiator.
Summary of the invention
The object of this invention is to provide that functionality is adjustable, flame retardant effect be good, well dissolve each other with pentamethylene whipping agent, a kind of modification cardanol based polyether polyol of stable mechanical property and with its high flame retardant hard polyurethane foams prepared and preparation method thereof;
To achieve these goals, technical scheme of the present invention is:
A kind of modification cardanol based polyether polyol, it is characterized in that: after one or both in cardanol, trimeric cyanamide and bromamide, paraformaldehyde mixing, drip in diethanolamine and diethylenetriamine one or both, the mol ratio wherein between cardanol, diethanolamine and/or diethylenetriamine, paraformaldehyde is 1:1 ~ 4:1 ~ 4; Modification cashew nut phenolic group Mannich alkali intermediate is obtained by reacting by Mannich, obtain with oxyethane and propylene oxide alkoxide more further, oxyethane and propylene oxide total mole number are 3 ~ 16 times of cardanol, trimeric cyanamide and/or bromamide total mole number, its viscosity 25 DEG C is 1000-12000mPas, hydroxyl value is 200-700mg/gKOH, moisture≤1%wt; The reaction conditions of obtained modification cashew nut phenolic group Mannich alkali intermediate is 50-120 DEG C, and diethanolamine/triethylene diamine time for adding is 1-2h, and the reaction times is 2-5h; React the water of complete removing reaction system, when water-content is less than 1.0%wt, carry out alkoxide reaction, temperature of reaction is 130-150 DEG C, and the reaction times is 2-6h.
It is characterized in that: on four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, trimeric cyanamide 25g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 470mg/gKOH, 25 DEG C of viscosity are 5500mPas.
It is characterized in that: comprise the following steps: step (1) is on four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, bromamide 66g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 ~ 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 402mg/gKOH, 25 DEG C of viscosity are 6500mPas,
Step (2) takes above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N according to mass parts, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.1g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 32.3%.
It is characterized in that: on four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, bromamide 66g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 402mg/gKOH, 25 DEG C of viscosity are 6500mPas, then above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N is taken according to mass parts, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.1g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 32.3%.
Further: after cardanol, the mixing of liquefaction trimeric cyanamide, bromamide and paraformaldehyde, drip diethanolamine and diethylenetriamine, modification cashew nut phenolic group Mannich alkali intermediate is obtained by reacting by Mannich, obtain with oxyethane and propylene oxide alkoxide more further, its viscosity 25 DEG C is 1000-12000mPas, hydroxyl value is 200-700mg/gKOH, moisture≤1%wt; Wherein cardanol, diethanolamine or diethylenetriamine and formaldehyde mole ratio are 1:1:1-1:4:4, oxyethane and propylene oxide total mole number are 3-16 times of cardanol, trimeric cyanamide and bromamide total mole number, the reaction conditions of obtained modification cashew nut phenolic group Mannich alkali intermediate is 50-120 DEG C, diethanolamine/triethylene diamine time for adding is 1-2h, and the reaction times is 2-5h; React the water of complete removing reaction system, when water-content is less than 1.0%wt, carry out alkoxide reaction, temperature of reaction is 130-150 DEG C, and the reaction times is 2-6h.By the impact of the factor such as initiator structure, oxyethane, propylene oxide quality in research reaction process on polyether glycol structure and performance, Optimizing Technical.
tool of the present invention has the following advantages:
(1) raw material adopts biological material cardanol to substitute petrochemical material, inexpensive abundant, renewable;
(2) constructional feature of cardanol makes it have a lot of excellent properties, and rigidity benzene ring structure makes cardanol have resistance to elevated temperatures; Between phenyl ring, position can increase the toughness of system containing carbon 15 long alkyl chain of unsaturated carbon-carbon double bond and reduce the viscosity of system;
(3) utilize Mannich to react, structure and the adjustable polyether glycol of functionality can be obtained;
(4) add trimeric cyanamide, bromamide carries out modification, improve polyvalent alcohol nitrogen heterocyclic and bromo element content, improve intrinsic flame-retarding characteristic.Obtained rigid urethane foam abscess is fine and smooth, and good, the fire-retardant rank of mechanical stability is high, high insulating effect;
(5) introduce phenyl ring rigid structure, introduce the ignition-proof elements such as N, Br and make it have excellent mechanics, heat-resisting, flame retardant properties; Between phenyl ring, position is carbon 15 long alkyl chain containing unsaturated carbon-carbon double bond, can be well compatible with pentamethylene whipping agent, can also increase the toughness of system and reduce the viscosity of system.It is characterized in that in Mannich reaction system by adding trimeric cyanamide or bromamide carries out modification, obtained polyether glycol is containing ignition-proof elements such as N, Br, it is characterized in that passing through hydroxylating, liquefaction trimeric cyanamide, and the H activated in melamine molecule structure, the intermolecular polymerization reaction occurred after adopting Mannich reaction to stop trimeric cyanamide liquefaction, obtains the adjustable trimeric cyanamide Mannich polyvalent alcohol of functionality by changing feed ratio; The application of modification cardanol based polyether polyol in the flame-retardant hard polyurethane foam board preparing pentamethylene foaming system.Modification cardanol based polyether polyol, itself and catalyzer, pentamethylene whipping agent, foam stabilizer, fire retardant, water etc. are hybridly prepared into premixed systems, react with the many phenyl isocyanate of polymethine and prepare hard polyurethane foams, isocyanate index 200-400, coordinate modification cardanol based polyether polyol, obtained hard polyurethane foams good flame resistance, stable mechanical property, excellent thermal insulation performance.
Embodiment
Embodiment 1
On four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, trimeric cyanamide 25g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 470mg/gKOH, 25 DEG C of viscosity are 5500mPas.Then according to mass parts take above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.9g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 31.2%.
Embodiment 2
On four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, bromamide 66g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 402mg/gKOH, 25 DEG C of viscosity are 6500mPas.Then according to mass parts take above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.1g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 32.3%.
Embodiment 3
On four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, trimeric cyanamide 25g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethylenetriamine 230g, time for adding is 2h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 509mg/gKOH, 25 DEG C of viscosity are 5700mPas.Then according to mass parts take above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.9g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 31.5%.

Claims (4)

1. a modification cardanol based polyether polyol, it is characterized in that: after one or both in cardanol, trimeric cyanamide and bromamide, paraformaldehyde mixing, drip in diethanolamine and diethylenetriamine one or both, the mol ratio wherein between cardanol, diethanolamine and/or diethylenetriamine, paraformaldehyde is 1:1 ~ 4:1 ~ 4; Modification cashew nut phenolic group Mannich alkali intermediate is obtained by reacting by Mannich, obtain with oxyethane and propylene oxide alkoxide more further, oxyethane and propylene oxide total mole number are 3 ~ 16 times of cardanol, trimeric cyanamide and/or bromamide total mole number, its viscosity 25 DEG C is 1000-12000mPas, hydroxyl value is 200-700mg/gKOH, moisture≤1%wt; The reaction conditions of obtained modification cashew nut phenolic group Mannich alkali intermediate is 50-120 DEG C, and diethanolamine/triethylene diamine time for adding is 1-2h, and the reaction times is 2-5h; React the water of complete removing reaction system, when water-content is less than 1.0%wt, carry out alkoxide reaction, temperature of reaction is 130-150 DEG C, and the reaction times is 2-6h.
2. a kind of modification cardanol based polyether polyol according to claim 1, it is characterized in that: on four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, trimeric cyanamide 25g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 470mg/gKOH, 25 DEG C of viscosity are 5500mPas.
3. high flame retardant hard polyurethane foams prepared by the modification cardanol based polyether polyol described in a right to use 1 ~ 2, it is characterized in that: comprise the following steps: step (1) is on four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, bromamide 66g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 ~ 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 402mg/gKOH, 25 DEG C of viscosity are 6500mPas,
Step (2) takes above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N according to mass parts, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.1g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 32.3%.
4. prepare the method for high flame retardant hard polyurethane foams as claimed in claim 3 for one kind, it is characterized in that: on four-necked bottle, load onto reflux condensing tube, 302g cardanol is added in four-necked bottle, paraformaldehyde 72g, bromamide 66g stirred under nitrogen atmosphere mixes, be warming up to 80 DEG C, drip diethanolamine 200g, time for adding is 1h, then at 90 DEG C, 4h is reacted, continue to be warming up to 110 DEG C, decompression dehydration makes moisture be less than 1.0%, pass into 80g oxyethane and 162g propylene oxide reaction continuously, temperature controls at about 130 DEG C, still internal pressure remains on 0.4 1 0.6MPa, when pressure cooling is for normal pressure, polyreaction terminates, at 110 DEG C of insulation 2h, vacuumize 30min, obtain modification cardanol Mannich polyether glycol, its hydroxyl value is 402mg/gKOH, 25 DEG C of viscosity are 6500mPas, then above-mentioned polyether glycol 60g, polyester polyol 40g, foam stabilizer (AK-8805) 3g, amines catalyst (N is taken according to mass parts, N-dimethylcyclohexylamine) 0.76g, metal-based catalysts isocaprylic acid potassium 0.75g, Potassium ethanoate 0.5g, water 1.5g, pentamethylene 15g mixing and stirring be mixed with combined polyether, then in cup, add aforesaid combination polyethers 11.6g, polymethine polyphenyl polyisocyanate 20.1g successively, mechanical stirring 10s under rotating speed 3000-3500r/min condition, obtained urethane foam oxygen index is 32.3%.
CN201510798040.XA 2015-11-19 2015-11-19 Modified cardanol-based polyether polyol and high-fire-resistant hard polyurethane foam prepared by modified cardanol-based polyether polyol and preparation method thereof Pending CN105295018A (en)

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CN107141466A (en) * 2017-06-19 2017-09-08 于天荣 A kind of Mannich polyethers and preparation method thereof
CN109134803A (en) * 2018-06-25 2019-01-04 青岛海尔股份有限公司 Glycol composition and its polyurethane rigid foam plastic of preparation
CN110862526A (en) * 2019-11-01 2020-03-06 上海应用技术大学 Preparation method of high-activity flame-retardant polyether polyol
CN111511791A (en) * 2017-12-21 2020-08-07 巴斯夫欧洲公司 Method for producing rigid polyurethane foam composite elements using mannich polyols
CN112646163A (en) * 2020-12-14 2021-04-13 山东一诺威新材料有限公司 Preparation method of cardanol polyether polyol with high pentane intersolubility
CN113501930A (en) * 2021-06-23 2021-10-15 四川东树新材料有限公司 Cast polyurethane resin for wind power blade and preparation method thereof
CN114395108A (en) * 2022-02-18 2022-04-26 山东蓝天新材料科技有限公司 Flame-retardant bio-based polyurethane foam and preparation method thereof
CN114524927A (en) * 2022-03-08 2022-05-24 上海回天新材料有限公司 Preparation method of cardanol bio-based polyol and application of cardanol bio-based polyol in flexible packaging adhesive
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Publication number Priority date Publication date Assignee Title
CN107141466A (en) * 2017-06-19 2017-09-08 于天荣 A kind of Mannich polyethers and preparation method thereof
CN111511791A (en) * 2017-12-21 2020-08-07 巴斯夫欧洲公司 Method for producing rigid polyurethane foam composite elements using mannich polyols
CN109134803A (en) * 2018-06-25 2019-01-04 青岛海尔股份有限公司 Glycol composition and its polyurethane rigid foam plastic of preparation
CN110862526B (en) * 2019-11-01 2022-12-06 上海应用技术大学 A kind of preparation method of highly active flame retardant polyether polyol
CN110862526A (en) * 2019-11-01 2020-03-06 上海应用技术大学 Preparation method of high-activity flame-retardant polyether polyol
CN112646163A (en) * 2020-12-14 2021-04-13 山东一诺威新材料有限公司 Preparation method of cardanol polyether polyol with high pentane intersolubility
CN113501930A (en) * 2021-06-23 2021-10-15 四川东树新材料有限公司 Cast polyurethane resin for wind power blade and preparation method thereof
CN113501930B (en) * 2021-06-23 2022-04-01 四川东树新材料有限公司 Cast polyurethane resin for wind power blade and preparation method thereof
JP2023092020A (en) * 2021-12-21 2023-07-03 株式会社イノアックコーポレーション POLYURETHANE FOAM, ITS MANUFACTURING METHOD AND SEALING MATERIAL
CN114395108B (en) * 2022-02-18 2023-06-16 山东蓝天新材料科技有限公司 Flame-retardant bio-based polyurethane foam and preparation method thereof
CN114395108A (en) * 2022-02-18 2022-04-26 山东蓝天新材料科技有限公司 Flame-retardant bio-based polyurethane foam and preparation method thereof
CN114524927A (en) * 2022-03-08 2022-05-24 上海回天新材料有限公司 Preparation method of cardanol bio-based polyol and application of cardanol bio-based polyol in flexible packaging adhesive
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CN115584028B (en) * 2022-10-21 2023-08-25 江苏美思德化学股份有限公司 Bio-based polyether organic silicon copolymer, preparation method thereof, foam stabilizer and polyurethane foam
CN116836349A (en) * 2022-11-17 2023-10-03 江苏长能节能新材料科技有限公司 Preparation method of melamine resin with good pentane compatibility
WO2024119648A1 (en) * 2022-12-08 2024-06-13 安徽扬子地板股份有限公司 Substrate for waterproof wall floor board and preparation method for substrate
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Application publication date: 20160203