CN105860051A - 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 - Google Patents
聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 Download PDFInfo
- Publication number
- CN105860051A CN105860051A CN201610487179.7A CN201610487179A CN105860051A CN 105860051 A CN105860051 A CN 105860051A CN 201610487179 A CN201610487179 A CN 201610487179A CN 105860051 A CN105860051 A CN 105860051A
- Authority
- CN
- China
- Prior art keywords
- polyurethane foam
- low
- polyether
- parts
- odor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920000570 polyether Polymers 0.000 title claims abstract description 43
- 239000004721 Polyphenylene oxide Substances 0.000 title claims abstract description 22
- 229920005830 Polyurethane Foam Polymers 0.000 title claims abstract description 18
- 239000011496 polyurethane foam Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims abstract description 8
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 40
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 39
- 238000002360 preparation method Methods 0.000 claims abstract description 12
- 239000003054 catalyst Substances 0.000 claims abstract description 11
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000003463 adsorbent Substances 0.000 claims abstract description 9
- 239000003999 initiator Substances 0.000 claims abstract description 6
- 238000007151 ring opening polymerisation reaction Methods 0.000 claims abstract description 5
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical group CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 24
- 239000001294 propane Substances 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 238000010792 warming Methods 0.000 claims description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims 1
- 229910001948 sodium oxide Inorganic materials 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 abstract 2
- 235000011187 glycerol Nutrition 0.000 abstract 2
- 239000002984 plastic foam Substances 0.000 abstract 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 6
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 5
- 230000002159 abnormal effect Effects 0.000 description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000035943 smell Effects 0.000 description 3
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical group C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229920005862 polyol Polymers 0.000 description 2
- 150000003077 polyols Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- IMNIMPAHZVJRPE-UHFFFAOYSA-N triethylenediamine Chemical compound C1CN2CCN1CC2 IMNIMPAHZVJRPE-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/26—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
- C08G65/2603—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen
- C08G65/2606—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen containing hydroxyl groups
- C08G65/2609—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen containing hydroxyl groups containing aliphatic hydroxyl groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4829—Polyethers containing at least three hydroxy groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/30—Post-polymerisation treatment, e.g. recovery, purification, drying
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyethers (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
本发明公开了一种聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用,该方法以甘油为起始剂;氢氧化钠为催化剂;与环氧丙烷在低温下开环聚合反应制备;制备方法是由以下重量份数的原料制成:甘油5‑10;氢氧化钠0.5‑0.8;环氧丙烷200‑300,三乙醇胺:3‑5;制备过程中采用精制吸附剂来吸附氢氧化钠。采用该聚醚制备的聚氨酯泡沫塑料泡沫质量更好,气味更低。
Description
技术领域
本发明属于有机高分子化合物的制备方法,具体地说是一种聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用。
背景技术
随着聚醚多元醇生产工艺的不断改进,产品的质量也在不断提高,但聚醚产品的气味问题还是没有得到很好的解决,尤其是应用于家具、汽车、服装等行业,与人们的日常生活直接相关气味问题显得尤为突出。
发明内容
本发明的目的是提供一种聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用,采用该聚醚制备的聚氨酯泡沫塑料泡沫质量更好,气味更低。
本发明的目的是通过以下技术方案来实现的:
一种聚氨酯泡沫用低气味聚醚的制备方法,其特征在于:该方法以甘油为起始剂;氢氧化钠为催化剂;与环氧丙烷在低温下开环聚合反应制备;采用精制吸附剂去除催化剂氢氧化钠;加入三乙醇胺与聚醚中的醛类物质反应成为不易挥发的大分子,包括如下步骤:
1)将甘油、氢氧化钠投入到反应器中,重量份数为:甘油5-10;氢氧化钠0.5-0.8;
2)然后在120-130℃温度下通过氮气流脱水,水份合格后,降低温度至100-110℃缓慢通入重量份数为200-300的环氧丙烷,环氧丙烷投加结束后,搅拌1-3小时,使体系充分反应,然后抽真空,冷却后制得粗聚醚;水份合格是指水份质量分数低于0.05%;
3)将粗聚醚投入到反应器中,加入占粗聚醚重量份数1%精制吸附剂(精制吸附剂生产厂家为枣阳市永华化工有限公司,牌号为ZH-AD100S),控制温度在80-90℃,搅拌1-2小时后升温至110-120℃,进行抽真空2小时,然后经过过滤,再加入重量份数为3-5的三乙醇胺,控制温度在80-90℃,搅拌2小时后得到聚氨酯泡沫用低气味聚醚。
聚醚常规生产工艺路线是采用磷酸加入到粗聚醚中与碱性催化剂发生中和反应来去除催化剂,这个过程中会磷酸与聚醚接触有副反应产生低分子醛类物质,使得聚醚气味变大:本发明不采用中和反应的工艺路线,而是使用精制吸附剂直接通过吸附去除碱性催化剂,避免了使用磷酸与聚醚接触产生低分子醛类的环节,然后采用过量的三乙醇胺和聚醚中微量的低分子醛类反应成为不易挥发的大分子,从而达到降低聚醚气味的效果,而且反应后的大分子仍含有羟基,不影响聚氨酯发泡应用。
具体实施方式
下面通过具体实施例对本发明作进一步的说明,但各实施例均不是对本发明的具体限制。
实施例1
一种聚氨酯泡沫用低气味聚醚的制备方法,以甘油为起始剂;氢氧化钠为催化剂;与环氧丙烷在低温下开环聚合反应制备,采用三乙醇胺消除低分子醛类。包括如下步骤:
①原料重量份数为:甘油(JOC GREAT WALLCO.LTD)5份;氢氧化钠(南京化学试剂厂)0.6份;环氧丙烷(利安德)200份;三乙醇胺3份;
②将甘油、氢氧化钠投入到反应器中,然后在120-130℃温度下通过氮气流脱水,水份低于0.05%(质量分数)后,降低温度至110℃缓慢通入环氧丙烷,环氧丙烷投加结束后,搅拌1-3小时,使体系充分反应,然后抽真空,冷却后制得粗聚醚。
③将粗聚醚投入到反应器中,加入占粗聚醚重量份数0.3%精制吸附剂(精制吸附剂生产厂家为枣阳市永华化工有限公司,牌号为ZH-AD100NS),控制温度在80-90℃,搅拌1-2小时后升温至110-120℃,进行抽真空2小时,然后经过过滤,再加入三乙醇胺,控制温度在80-90℃,搅拌2小时后得到低气味聚醚。
实施例2
一种聚氨酯泡沫用低气味聚醚的制备方法,以甘油为起始剂;氢氧化钠为催化剂;与环氧丙烷在低温下开环聚合反应制备。包括如下步骤:
①原料重量份数为:甘油(JOC GREAT WALLCO.LTD)5份;氢氧化钠(南京化学试剂厂)0.6份;环氧丙烷(利安德)200份;三乙醇胺5份
②将甘油、氢氧化钠投入到反应器中,然后在120-130℃温度下通过氮气流脱水,水份合格后,降低温度至100℃缓慢通入环氧丙烷,环氧丙烷投加结束后,搅拌1-3小时,使体系充分反应,然后抽真空,冷却后制得粗聚醚。
③将粗聚醚投入到反应器中,加入占粗聚醚重量份数1%精制吸附剂(精制吸附剂生产厂家为枣阳市永华化工有限公司,牌号为ZH-AD100NS),控制温度在80-90℃,搅拌1-2小时后升温至110-120℃,进行抽真空2小时,然后经过过滤,再加入三乙醇胺,控制温度在80-90℃,搅拌2小时后得到低气味聚醚。
实施例3
一种上述制备方法制得的低气味聚醚的应用,取聚氨酯泡沫用聚醚多元醇100份,硅油2份,三乙烯二胺催化剂0.2份,水3份,异氰酸酯110份,高速搅拌混合后发泡制得聚氨酯泡沫制品。
Claims (3)
1.一种聚氨酯泡沫用低气味聚醚的制备方法,其特征在于:该方法以甘油为起始剂;氢氧化钠为催化剂;与环氧丙烷在低温下开环聚合反应制备;包括如下步骤:
1)将甘油、氢氧化钠投入到反应器中,重量份数为:甘油5-10;氢氧化钠0.5-0.8;
2)然后在120-130℃温度下通过氮气流脱水,水份合格后,降低温度至100-110℃缓慢通入重量份数为200-300的环氧丙烷,环氧丙烷投加结束后,搅拌1-3小时,使体系充分反应,然后抽真空,冷却后制得粗聚醚;
3)将粗聚醚投入到反应器中,加入占粗聚醚质量份数1%精制吸附剂,控制温度在80-90℃,搅拌1-2小时后升温至110-120℃,进行抽真空2小时,然后经过过滤,再加入重量份数为3-5的三乙醇胺,控制温度在80-90℃,搅拌2小时后得到聚氨酯泡沫用低气味聚醚。
2.根据权利要求1所述的聚氨酯泡沫用低气味聚醚的制备方法,其特征在于:水份合格是指水份质量分数低于0.05%。
3.一种权利要求1所述制备方法制得的低气味聚醚在聚氨酯泡沫中的应用。
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610487179.7A CN105860051A (zh) | 2016-06-29 | 2016-06-29 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
| PCT/CN2016/096470 WO2018000556A1 (zh) | 2016-06-29 | 2016-08-24 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610487179.7A CN105860051A (zh) | 2016-06-29 | 2016-06-29 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105860051A true CN105860051A (zh) | 2016-08-17 |
Family
ID=56656015
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610487179.7A Pending CN105860051A (zh) | 2016-06-29 | 2016-06-29 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN105860051A (zh) |
| WO (1) | WO2018000556A1 (zh) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018000556A1 (zh) * | 2016-06-29 | 2018-01-04 | 句容宁武新材料股份有限公司 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
| CN112608447A (zh) * | 2020-12-15 | 2021-04-06 | 无锡吉兴木桥高分子材料科技有限公司 | 一种高透气性半硬质聚氨酯泡沫及其制备方法 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113773486B (zh) * | 2020-06-09 | 2024-06-28 | 中国石油化工股份有限公司 | 一种聚醚多元醇的精制方法及其产物与应用 |
| CN116082619A (zh) * | 2021-11-05 | 2023-05-09 | 万华化学集团股份有限公司 | 一种低气味聚醚多元醇生产方法 |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1660918A (zh) * | 2005-01-31 | 2005-08-31 | 锦化化工(集团)有限责任公司 | 耐高温聚氨酯硬泡用聚醚多元醇的制备方法 |
| CN101392054A (zh) * | 2008-10-31 | 2009-03-25 | 句容市宁武化工有限公司 | 一种甘油基聚醚多元醇的制备方法 |
| CN101775132A (zh) * | 2010-02-03 | 2010-07-14 | 山东蓝星东大化工有限责任公司 | 低气味聚醚多元醇的精制方法 |
| CN104262610A (zh) * | 2014-10-11 | 2015-01-07 | 淄博德信联邦化学工业有限公司 | 阻燃聚醚多元醇的制备方法 |
| CN105111428A (zh) * | 2015-08-31 | 2015-12-02 | 句容宁武新材料发展有限公司 | 一种低气味聚醚多元醇的制备方法 |
| CN105315453A (zh) * | 2015-11-25 | 2016-02-10 | 山东一诺威新材料有限公司 | 聚合甘油基聚醚多元醇及其制备方法 |
| CN105315450A (zh) * | 2015-11-25 | 2016-02-10 | 山东一诺威新材料有限公司 | 全水型聚氨酯硬泡用聚醚多元醇的制备方法 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102005015894A1 (de) * | 2005-04-06 | 2006-10-12 | Basf Ag | Verfahren zur Herstellung von Polyetheralkoholen |
| TW200838838A (en) * | 2006-12-22 | 2008-10-01 | Dow Technology Investments Llc | Process for reducing side-reactions during alkylene glycol and poly-alkylene glycol manufacturing |
| EP2444444A1 (en) * | 2009-06-16 | 2012-04-25 | Asahi Glass Company, Limited | Process for producing polyether polyol and process for producing rigid foamed synthetic resin using same |
| CN102942666B (zh) * | 2012-12-04 | 2015-04-15 | 苏州井上高分子新材料有限公司 | 一种聚氨酯半硬质泡沫组合物及其制备方法 |
| CN105860051A (zh) * | 2016-06-29 | 2016-08-17 | 句容宁武新材料股份有限公司 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
-
2016
- 2016-06-29 CN CN201610487179.7A patent/CN105860051A/zh active Pending
- 2016-08-24 WO PCT/CN2016/096470 patent/WO2018000556A1/zh not_active Ceased
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1660918A (zh) * | 2005-01-31 | 2005-08-31 | 锦化化工(集团)有限责任公司 | 耐高温聚氨酯硬泡用聚醚多元醇的制备方法 |
| CN101392054A (zh) * | 2008-10-31 | 2009-03-25 | 句容市宁武化工有限公司 | 一种甘油基聚醚多元醇的制备方法 |
| CN101775132A (zh) * | 2010-02-03 | 2010-07-14 | 山东蓝星东大化工有限责任公司 | 低气味聚醚多元醇的精制方法 |
| CN104262610A (zh) * | 2014-10-11 | 2015-01-07 | 淄博德信联邦化学工业有限公司 | 阻燃聚醚多元醇的制备方法 |
| CN105111428A (zh) * | 2015-08-31 | 2015-12-02 | 句容宁武新材料发展有限公司 | 一种低气味聚醚多元醇的制备方法 |
| CN105315453A (zh) * | 2015-11-25 | 2016-02-10 | 山东一诺威新材料有限公司 | 聚合甘油基聚醚多元醇及其制备方法 |
| CN105315450A (zh) * | 2015-11-25 | 2016-02-10 | 山东一诺威新材料有限公司 | 全水型聚氨酯硬泡用聚醚多元醇的制备方法 |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018000556A1 (zh) * | 2016-06-29 | 2018-01-04 | 句容宁武新材料股份有限公司 | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 |
| CN112608447A (zh) * | 2020-12-15 | 2021-04-06 | 无锡吉兴木桥高分子材料科技有限公司 | 一种高透气性半硬质聚氨酯泡沫及其制备方法 |
| CN112608447B (zh) * | 2020-12-15 | 2022-09-09 | 无锡吉兴汽车部件有限公司 | 一种高透气性半硬质聚氨酯泡沫及其制备方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2018000556A1 (zh) | 2018-01-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105860051A (zh) | 聚氨酯泡沫用低气味聚醚的制备方法及制得产品的应用 | |
| CN106589345B (zh) | 一种降低voc含量及气味的聚醚多元醇精制方法 | |
| JP5716382B2 (ja) | ポリアルキレングリコールの製造方法 | |
| CN102453253A (zh) | 高伯羟基聚醚多元醇制备工艺 | |
| CN101125919A (zh) | 用于制备环戊烷型聚氨酯泡沫的植物油聚醚多元醇及其制法 | |
| EP2495259A4 (en) | METHOD FOR THE PRODUCTION OF CATIONIC HYDROXYPROPYL CELLULOSE | |
| CN105237759B (zh) | 高拉伸弹性体用聚醚多元醇及其制备方法 | |
| KR20160021270A (ko) | 탄닌 함유 폴리올, 이의 제법 및 이의 용도 | |
| CN106928425A (zh) | 一种抗菌除臭聚氨酯泡沫及其加工方法 | |
| CN115975203A (zh) | 一种长效抗菌剂、硅橡胶及其制备方法 | |
| CN102167809A (zh) | 由植物油制备生物基聚醚多元醇的方法 | |
| CN104130389B (zh) | 降低聚醚多元醇voc含量的方法 | |
| CN104592480A (zh) | 聚氨酯改性聚硫橡胶的制备方法 | |
| CN111518322A (zh) | 一种纤维素改性乳胶材料及其制备方法和应用 | |
| CN103613620B (zh) | 木薯淀粉制备十二烷基糖苷的方法 | |
| CN115340452B (zh) | 一种由赤藓糖醇、甘露醇或山梨醇催化转化制备羟基乙酸的方法 | |
| CN105906798A (zh) | 一种低粘度硬泡聚醚的制备方法 | |
| CN108997552A (zh) | 一种低气味高回弹聚氨酯泡沫的制备方法 | |
| CN110256242B (zh) | 一种甘油在酸性条件下直接制备乳酸的方法 | |
| CN117258841B (zh) | 环三磷腈衍生基硅基固态胺材料及其催化二氧化碳与环氧化物耦合制备环状碳酸酯的应用 | |
| CN106187678B (zh) | 一种(r)-3-氯-1,2-丙二醇的制备方法 | |
| CN102040826B (zh) | 一种汽车止滑垫用聚氨酯弹性体组合物 | |
| CN110479355A (zh) | 一种用于合成环己基苯的催化剂的制备方法 | |
| CN109321192A (zh) | 一种汽车内饰顶棚用环保湿固化聚氨酯胶黏剂 | |
| CN106117537A (zh) | 聚氨酯泡沫用低易挥发物聚醚的制法及制得产品的应用 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160817 |