JPH04501284A - Method of manufacturing plastic from raw material oils and fats - Google Patents
Method of manufacturing plastic from raw material oils and fatsInfo
- Publication number
- JPH04501284A JPH04501284A JP2511716A JP51171690A JPH04501284A JP H04501284 A JPH04501284 A JP H04501284A JP 2511716 A JP2511716 A JP 2511716A JP 51171690 A JP51171690 A JP 51171690A JP H04501284 A JPH04501284 A JP H04501284A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- manufacturing
- fats
- oils
- oxidized
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 18
- 239000004033 plastic Substances 0.000 title claims description 16
- 229920003023 plastic Polymers 0.000 title claims description 16
- 235000014593 oils and fats Nutrition 0.000 title claims description 8
- 239000002994 raw material Substances 0.000 title claims description 6
- 239000003921 oil Substances 0.000 claims description 23
- 239000003925 fat Substances 0.000 claims description 19
- 235000019197 fats Nutrition 0.000 claims description 19
- 150000001875 compounds Chemical class 0.000 claims description 15
- 238000006243 chemical reaction Methods 0.000 claims description 13
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 12
- 230000003647 oxidation Effects 0.000 claims description 9
- 238000007254 oxidation reaction Methods 0.000 claims description 9
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 8
- 150000002009 diols Chemical class 0.000 claims description 8
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 8
- 150000004670 unsaturated fatty acids Chemical class 0.000 claims description 7
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 claims description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000007858 starting material Substances 0.000 claims description 6
- 150000004985 diamines Chemical class 0.000 claims description 5
- 125000005442 diisocyanate group Chemical group 0.000 claims description 5
- 150000004665 fatty acids Chemical group 0.000 claims description 5
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims description 5
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 4
- 239000004593 Epoxy Substances 0.000 claims description 4
- 235000019253 formic acid Nutrition 0.000 claims description 4
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 4
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 3
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 3
- LJGHYPLBDBRCRZ-UHFFFAOYSA-N 3-(3-aminophenyl)sulfonylaniline Chemical compound NC1=CC=CC(S(=O)(=O)C=2C=C(N)C=CC=2)=C1 LJGHYPLBDBRCRZ-UHFFFAOYSA-N 0.000 claims description 3
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 3
- 239000005642 Oleic acid Substances 0.000 claims description 3
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 3
- 125000003700 epoxy group Chemical group 0.000 claims description 3
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 3
- 239000011541 reaction mixture Substances 0.000 claims description 3
- 150000002440 hydroxy compounds Chemical class 0.000 claims description 2
- 235000021081 unsaturated fats Nutrition 0.000 claims description 2
- 240000003291 Armoracia rusticana Species 0.000 claims 1
- 235000011330 Armoracia rusticana Nutrition 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims 1
- 240000000528 Ricinus communis Species 0.000 claims 1
- 235000004443 Ricinus communis Nutrition 0.000 claims 1
- 238000010276 construction Methods 0.000 claims 1
- 235000019198 oils Nutrition 0.000 description 19
- 150000003626 triacylglycerols Chemical class 0.000 description 15
- 238000000034 method Methods 0.000 description 9
- 239000002253 acid Substances 0.000 description 5
- -1 hydroxy fatty acid triglycerides Chemical class 0.000 description 5
- 150000004965 peroxy acids Chemical class 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 125000001931 aliphatic group Chemical group 0.000 description 3
- 150000001414 amino alcohols Chemical class 0.000 description 3
- 239000004359 castor oil Substances 0.000 description 3
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- GLUUGHFHXGJENI-UHFFFAOYSA-N Piperazine Chemical compound C1CNCCN1 GLUUGHFHXGJENI-UHFFFAOYSA-N 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 235000019438 castor oil Nutrition 0.000 description 2
- 150000001805 chlorine compounds Chemical class 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000002118 epoxides Chemical class 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 2
- 239000005056 polyisocyanate Substances 0.000 description 2
- 229920001228 polyisocyanate Polymers 0.000 description 2
- 229920000307 polymer substrate Polymers 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- XFNJVJPLKCPIBV-UHFFFAOYSA-N trimethylenediamine Chemical compound NCCCN XFNJVJPLKCPIBV-UHFFFAOYSA-N 0.000 description 2
- JOYRKODLDBILNP-UHFFFAOYSA-N urethane group Chemical group NC(=O)OCC JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ZLYYJUJDFKGVKB-UPHRSURJSA-N (z)-but-2-enedioyl dichloride Chemical compound ClC(=O)\C=C/C(Cl)=O ZLYYJUJDFKGVKB-UPHRSURJSA-N 0.000 description 1
- PWGJDPKCLMLPJW-UHFFFAOYSA-N 1,8-diaminooctane Chemical compound NCCCCCCCCN PWGJDPKCLMLPJW-UHFFFAOYSA-N 0.000 description 1
- JCEZOHLWDIONSP-UHFFFAOYSA-N 3-[2-[2-(3-aminopropoxy)ethoxy]ethoxy]propan-1-amine Chemical compound NCCCOCCOCCOCCCN JCEZOHLWDIONSP-UHFFFAOYSA-N 0.000 description 1
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 1
- IGSBHTZEJMPDSZ-UHFFFAOYSA-N 4-[(4-amino-3-methylcyclohexyl)methyl]-2-methylcyclohexan-1-amine Chemical compound C1CC(N)C(C)CC1CC1CC(C)C(N)CC1 IGSBHTZEJMPDSZ-UHFFFAOYSA-N 0.000 description 1
- 244000067602 Chamaesyce hirta Species 0.000 description 1
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- 244000020551 Helianthus annuus Species 0.000 description 1
- 235000003222 Helianthus annuus Nutrition 0.000 description 1
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 1
- AVXURJPOCDRRFD-UHFFFAOYSA-N Hydroxylamine Chemical compound ON AVXURJPOCDRRFD-UHFFFAOYSA-N 0.000 description 1
- WUGQZFFCHPXWKQ-UHFFFAOYSA-N Propanolamine Chemical compound NCCCO WUGQZFFCHPXWKQ-UHFFFAOYSA-N 0.000 description 1
- 235000019486 Sunflower oil Nutrition 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- PWAXUOGZOSVGBO-UHFFFAOYSA-N adipoyl chloride Chemical compound ClC(=O)CCCCC(Cl)=O PWAXUOGZOSVGBO-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000003158 alcohol group Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 150000004984 aromatic diamines Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000001588 bifunctional effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- DLDJFQGPPSQZKI-UHFFFAOYSA-N but-2-yne-1,4-diol Chemical compound OCC#CCO DLDJFQGPPSQZKI-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- XLJMAIOERFSOGZ-UHFFFAOYSA-M cyanate Chemical compound [O-]C#N XLJMAIOERFSOGZ-UHFFFAOYSA-M 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- SSRPXSRFVKUAKH-UHFFFAOYSA-N decane-1,10-diol;hexane-1,6-diol Chemical compound OCCCCCCO.OCCCCCCCCCCO SSRPXSRFVKUAKH-UHFFFAOYSA-N 0.000 description 1
- 125000004420 diamide group Chemical group 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 125000001033 ether group Chemical group 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 1
- 239000010655 horseradish oil Substances 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 125000000468 ketone group Chemical group 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 125000001971 neopentyl group Chemical group [H]C([*])([H])C(C([H])([H])[H])(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 150000004967 organic peroxy acids Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 125000003538 pentan-3-yl group Chemical group [H]C([H])([H])C([H])([H])C([H])(*)C([H])([H])C([H])([H])[H] 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 125000005471 saturated fatty acid group Chemical group 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 125000001174 sulfone group Chemical group 0.000 description 1
- 239000002600 sunflower oil Substances 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
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- 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
- C08G59/00—Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
- C08G59/02—Polycondensates containing more than one epoxy group per molecule
- C08G59/027—Polycondensates containing more than one epoxy group per molecule obtained by epoxidation of unsaturated precursor, e.g. polymer or monomer
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/38—Compounds containing oxirane rings with hydrocarbon radicals, substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
- C07D303/40—Compounds containing oxirane rings with hydrocarbon radicals, substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals by ester radicals
- C07D303/42—Acyclic compounds having a chain of seven or more carbon atoms, e.g. epoxidised fats
-
- 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
- C08G18/30—Low-molecular-weight compounds
- C08G18/36—Hydroxylated esters of higher fatty acids
-
- 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
- C08G59/00—Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
- C08G59/18—Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
- C08G59/40—Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the curing agents used
- C08G59/50—Amines
-
- 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
- C08G59/00—Polycondensates containing more than one epoxy group per molecule; Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups
- C08G59/18—Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing
- C08G59/40—Macromolecules obtained by polymerising compounds containing more than one epoxy group per molecule using curing agents or catalysts which react with the epoxy groups ; e.g. general methods of curing characterised by the curing agents used
- C08G59/62—Alcohols or phenols
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Fats And Perfumes (AREA)
- Polyurethanes Or Polyureas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Epoxy Compounds (AREA)
- Polyesters Or Polycarbonates (AREA)
- Epoxy Resins (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 原料油脂からプラスチックを製造する方法本発明は原料油脂から得られるプラス チックと、プラスチックの添加剤を製造する方法に関するものである。[Detailed description of the invention] Method for producing plastics from raw material oil It relates to a method for producing additives for plastics and plastics.
油脂は人の栄養に役立つばかりでなく、工業技術的に重要な多数の基本物質製造 の出発物質として利用される。しかしこれまで油脂は、一定条件下のごく限られ た範囲でのみ、ポリマーおよびプラスチック製造の出発物質として使用されてき た。Oils and fats are not only useful for human nutrition, but also for the production of many basic substances of industrial importance. used as a starting material. However, up until now, oils and fats have only been available under certain conditions. It has been used as a starting material for the production of polymers and plastics only to the extent that Ta.
ヒドロキシ脂肪酸トリグリセライドとそれらの誘導体を含む天然油脂は、特に有 用な工業製品を製造するに適している。例えば、トリグリセライド分子当たり2 個以上のアルコール基を優勢的に含む特定の油脂は、適当な反応性化合物、例え ばジイソシアネートとの反応により、これらのヒドロキシル基を経て、ポリマー 構造を形成でき、有利に熱硬化性プラスチックが生成される。Natural fats and oils containing hydroxy fatty acid triglycerides and their derivatives are particularly Suitable for manufacturing industrial products. For example, 2 per triglyceride molecule Certain fats and oils containing predominantly 1 or more alcohol groups can be treated with suitable reactive compounds, e.g. By reaction with diisocyanates, polymers are formed via these hydroxyl groups. Structures can be formed, advantageously thermosetting plastics being produced.
これらの変換反応に適した物質としては、例えばひまし油、または水素添加した ひまし油があり、それらはトリグリセライドとして直接使用できる。しかしこの 方法の応用範囲は、入手可能なヒドロキシル基含有油脂の数により極度に制限さ れる。さらにその欠点は、望ましくない副生物、特に、望ましくない着色成分を 除くために、反応前に油脂を精製しなければならないことである。Suitable materials for these transformation reactions include, for example, castor oil or hydrogenated There are castor oils and they can be used directly as triglycerides. But this The scope of application of the method is extremely limited by the number of hydroxyl group-containing fats and oils available. It will be done. Further disadvantages are the production of undesirable by-products, especially undesirable color components. In order to remove them, the fats and oils must be purified before the reaction.
本発明の目的は、従来は工業的重要度が低かった油脂をかなりの損失を見込む複 雑な精製工程を要しないで、プラスチックおよびプラスチックコモノマー製造の 出発物質にできる方法を提供するにある。It is an object of the present invention to convert oils and fats, which have hitherto been of low industrial importance, into complexes that are expected to result in considerable losses. for the production of plastics and plastic comonomers without the need for complex purification steps. The purpose is to provide a method that can be used as a starting material.
本発明は、プラスチックコモノマーと、請求項1に記されるように、不飽和脂肪 酸から成る油脂からプラスチックを製造する方法である。The present invention relates to a plastic comonomer and an unsaturated fat as defined in claim 1. This is a method of manufacturing plastics from oils and fats consisting of acids.
純不飽和脂肪酸およびそれらの誘導体が有機過酸と反応して、エポキシ化合物ま たはヒドロキシ化合物を生成することは知られている。Pure unsaturated fatty acids and their derivatives react with organic peracids to form epoxy compounds or It is known to produce hydroxy compounds.
驚くべきことに、原料油脂で表わされるような未精製トリグリセライドでさえ、 この方法によると問題なく酸化でき、しかも出発物質中に常に存在する随伴物を 予め除去しなくても問題なく酸化し得ることが見出された。別の予期し得なかっ た効果は、生成物の品質およびそれによる後の反応に望ましくない逆効果をもた らす、着色剤と香料がこの反応により完全に破壊され、全く無色の反応生成物が 得られることである。Surprisingly, even unrefined triglycerides, such as those expressed in raw oils and fats, This method allows for problem-free oxidation and eliminates accompanying substances that are always present in the starting material. It has been found that oxidation can be carried out without problems even without prior removal. another unexpected effects that have undesirable adverse effects on product quality and therefore subsequent reactions The colorants and fragrances are completely destroyed by this reaction, leaving a completely colorless reaction product. That's what you get.
基本的に、不飽和脂肪酸のグリセライドを含むどんな種類の原料油脂でも、本発 明による方法に適している。しかしこの種の油脂では、脂肪酸全量に対する、不 飽和脂肪酸残基の割合が既知で、少なくとも50%に達するものが有利である。Basically, any type of raw material oil or fat that contains glycerides of unsaturated fatty acids can be used with this product. It is suitable for the method according to the present invention. However, with this type of fat, the amount of fatty acids It is advantageous if the proportion of saturated fatty acid residues is known and amounts to at least 50%.
望ましい油類は、その中である。特に望ましいのはトウダイグサ油および新しい 「高オレイン」のひまわり油である。Desirable oils are among them. Particularly desirable are spurge oil and fresh It is a "high oleic" sunflower oil.
原料油脂は通常の方法、例えばスクリュー押出し機またはスピンドルプレス、ま たは加圧抽出により得られる。木材または植物残滓などの、含有する可能性のあ る固形成分を除去した後は、直接使用できる。Raw material fats and oils can be prepared using conventional methods such as screw extruders or spindle presses, or or by pressure extraction. Contains materials such as wood or plant residues that may contain After removing the solid components, it can be used directly.
本発明によれば、原料油脂は、ギ酸または酢酸などの適当な溶媒を使用して、好 ましくは、−5℃と+80℃との間の温度で、過ギ酸または過酢酸と反応させて 、酸化トリグリセライドに変換される。According to the present invention, the raw oil or fat is prepared using a suitable solvent such as formic acid or acetic acid. Preferably, by reacting with performic acid or peracetic acid at a temperature between -5°C and +80°C. , converted to oxidized triglycerides.
反応機構は、脂肪酸残基の二重結合が先ず反応してエポキシドを作り、それから 高温でジオールを生成する。The reaction mechanism is that the double bonds of fatty acid residues first react to form an epoxide, and then Produces diols at high temperatures.
一5℃と+20℃との間の低い温度と短い反応時間では、エポキシドが主として 生成する。一方ジオールは、幾つかの二重結合、ポリオールの存在で、有利には 一5℃と+80℃との間の温度で生成する。At low temperatures between -5°C and +20°C and short reaction times, epoxides are predominantly generate. Diols, on the other hand, have several double bonds, the presence of polyols, and advantageously It forms at temperatures between -5°C and +80°C.
どれだけ多くの過酸が使用されるかは、出発トリグリセライドの不飽和の程度お よび望ましい酸化程度に依存する。特にポリ不飽和トリグリセライドの場合には 、酸化された基の数に選択的に影響されるので、低分量が望ましい。How much peracid is used depends on the degree of unsaturation of the starting triglyceride. and the degree of oxidation desired. Especially in the case of polyunsaturated triglycerides , is selectively influenced by the number of oxidized groups, so low amounts are desirable.
この場合、望ましくない付随物は、トリグリセライドを酸化する前に常に除去さ れるので、例え二重結合がほんの部分的に酸化されたとしても、望ましくない着 色成分は反応混合物中には残らない。In this case, undesired concomitants are always removed before oxidizing the triglycerides. Even if the double bond is only partially oxidized, undesirable adhesion can occur. No color component remains in the reaction mixture.
過酸を直接添加する代りに、トリグリセライドを酢酸またはギ酸中に溶解してか ら、有利には過酸化水素を市販の30%溶液の形で滴下して、油脂を酸化するこ とも可能である。この場合、過酸化水素と溶媒の反応により過酸が形成され、そ れが更に酸化されるべき油脂と反応する。Instead of adding peracid directly, triglycerides can be dissolved in acetic or formic acid. The fats and oils can be oxidized by adding hydrogen peroxide dropwise, advantageously in the form of a commercially available 30% solution. Both are possible. In this case, the reaction between hydrogen peroxide and the solvent forms a peracid; This reacts with the fats and oils to be further oxidized.
反応が完結すると、過剰の過酸または過酸化水素は、通常の方法例えば触媒また は還元剤により除去される。次いで反応混合物中の大部分の水および溶媒が減圧 除去される。Once the reaction is complete, excess peracid or hydrogen peroxide can be removed by conventional methods, e.g. is removed by a reducing agent. Most of the water and solvent in the reaction mixture are then removed under reduced pressure. removed.
全ての随伴する着色剤は原料油脂の酸化工程で破壊されるので、結果として得ら れる酸化生成物は透明水溶液または無色の粘稠溶液として高収率で分離できる。All accompanying colorants are destroyed in the oxidation process of the raw oil and fat, so the resulting The oxidation products can be isolated in high yields as clear aqueous solutions or colorless viscous solutions.
酸化したトリグリセライドは、同等追加の精製工程なしに、余分の過酸、水、溶 媒を簡単に除去した後に、直ちに使用できる、架橋剤またはコモノマーとして、 例えば古典的なポリエステルおよびポリウレタン系中で使用されるものは、プラ スチックの性質を変え゛るので、純粋な形では非常に高価で、加圧油の形で使用 できない、ひまし油の低コスト代替物となる。Oxidized triglycerides can be purified without additional purification steps by removing excess peracid, water, and solvent. As a crosslinking agent or comonomer, ready for use after simple removal of the medium, For example, those used in classic polyester and polyurethane systems Because it changes the properties of the stick, it is very expensive in its pure form and used in the form of pressurized oil. It is a low-cost alternative to castor oil.
例えばジオールまたはジイソシアネートからのポリウレタン樹脂の場合に、ジオ ールの一部は、ジイソシアネートとの反応に先立って、酸化されたトリグリセラ イドにより置換される。これはポリマーを生成するが、その工程で、ジオールお よび酸化トリグリセライドは共に、ウレタン基を経て結合される。For example, in the case of polyurethane resins from diols or diisocyanates, A portion of the oxidized triglycerate is added to the oxidized triglycerate prior to reaction with the diisocyanate. replaced by the id. This produces polymers, but in the process, diols and and oxidized triglyceride are both attached via a urethane group.
さらに、酸化された油脂は、直接ヒドロキシ基またはエポキシ基と反応能力を持 つ二官能性または多官能性化合物と反応して、透明なポリマーとプラスチックを 得る。Additionally, oxidized fats and oils have the ability to directly react with hydroxyl or epoxy groups. transparent polymers and plastics by reacting with di- or polyfunctional compounds. obtain.
その脂肪酸組成中に約50%のオレイン酸を持つ獣脂のような、不飽和脂肪酸の 量が約50%の油脂を使用すると、一つの不飽和脂肪酸残基をも含まないトリグ リセライド分子の比率は相対的に低いが、これは大抵の完全酸化されたトリグリ セライド分子が、少なくとも2111のOH基を含むためである。このように酸 化された油脂は完全に反応し、実際には全量のトリグリセライドを含む。of unsaturated fatty acids, such as tallow, which has about 50% oleic acid in its fatty acid composition. When using approximately 50% fat and oil, triglycerides that do not contain even a single unsaturated fatty acid residue Although the proportion of lyceride molecules is relatively low, this is the case for most fully oxidized triglycerides. This is because the ceride molecule contains at least 2111 OH groups. In this way acid The converted fats and oils are fully reacted and actually contain the entire amount of triglycerides.
本発明による酸化は、基本的に不飽和脂肪酸の分割を起こさないので、全脂肪量 がポリマー生成に反応する。これは技術の重要な進歩である。The oxidation according to the present invention basically does not cause the splitting of unsaturated fatty acids, so the total fat content reacts with polymer formation. This is an important advance in technology.
ヒドロキシル基含有トリグリセライドと反応するための、二官能性または多官能 性化合物には、例えば、プラスチック製造に公知の、ジまたはポリイソシアネー トがある。Difunctional or polyfunctional for reacting with hydroxyl-containing triglycerides Compounds include, for example, di- or polyisocyanates known for plastics production. There is a
ヘキサメチレンジイソシアネート、メチレンジフェニルジイソシアネート(MD I)は有利に使用される0例えば商品名Desmodur E14またはT2O の名前で入手されるDesmodurクラスのジイソシアネートまたはポリイソ シアネートを使用する時は、いずれも何等の問題も起こさない、他の適当な二官 能性化合物には、ジカルボン酸またはそれらの活性誘導体、例えば酸塩化物、エ ステルおよび無水物がある。このような二官能性化合物の望ましい代表は、フタ ル酸ジクロライド、アジピン酸ジクロライド、マレイン酸ジクロライド、フォス ゲンである。このような化合物を用いると、トリグリセライドはウレタン結合か 、エステル結合を経て互いに結合される。Hexamethylene diisocyanate, methylene diphenyl diisocyanate (MD I) is preferably used, for example under the trade name Desmodur E14 or T2O Desmodur class diisocyanates or polyisocyanates available under the name When using cyanate, use other suitable secondary agents, none of which will cause any problems. Functional compounds include dicarboxylic acids or their active derivatives, such as acid chlorides, acid chlorides, etc. There are stellate and anhydrous. A desirable representative of such difunctional compounds is the lid adipic dichloride, maleic dichloride, phos It's Gen. When such compounds are used, triglycerides are bonded to urethane. , are bonded to each other via ester bonds.
エポキシ基含有トリグリセライドは、例えば、ジオール、ジアミン、アミノアル コールを経て結合される。この反応のための適当なジアミンまたはアミノアルコ ールは、望ましくは2〜44個の炭素原子を持つ、−級および二級の脂肪族、環 状−脂肪族、脂肪−芳香族および芳香族ジアミン、またはアミノアルコールであ る。さらに中でもダイマー性脂肪酸からのアミンが含まれる。Epoxy group-containing triglycerides include, for example, diols, diamines, aminoalcohols, Combined via call. Suitable diamine or aminoalcohol for this reaction - and secondary aliphatic, cyclic, preferably having 2 to 44 carbon atoms. aliphatic, aliphatic-aromatic and aromatic diamines, or amino alcohols. Ru. Also included are amines from dimeric fatty acids, among others.
追加の構成要素、または別の機能性基、例えば、エーテル基、ジアミド基、アミ ノ基、ケト基、またはスルフォン基が、炭化水素鎖の中のジアミンの二つのアミ ン官能基の間に配位されてもよいし、または環状脂肪族または芳香族残基に付加 されていてもよい。Additional components or other functional groups, such as ether groups, diamide groups, amino groups, etc. , a keto group, or a sulfone group connects two amino acids of the diamine in the hydrocarbon chain. may be coordinated between functional groups or attached to cycloaliphatic or aromatic residues. may have been done.
望ましいジアミンは、1.2−ジアミノエタン、1.3−ジアミノプロパン、1 .6−ジアミツヘキサン、1.8−ジアミノオクタン、ピペラジン、ジエチレン トリアミン、4,7.10−トリオキサトリデカン−1,13−ジアミン、3, 3°−ジアミノジフェニルスルフォン、3.3′−ジメチル−4,4′−ジアミ ノジシクロヘキシルメタンおよび次の式を持つ市販のエーテルジアミンである: ここでnは1から2000までの整数であるel+2−ジアミノエタン、および 1.6−ジアミツヘキサンが特に望ましい、望ましいアミノアルコールは2−ア ミノエタノールおよび3−アミノプロパツールである。Preferred diamines include 1,2-diaminoethane, 1,3-diaminopropane, 1 .. 6-diamithexane, 1,8-diaminooctane, piperazine, diethylene triamine, 4,7.10-trioxatridecane-1,13-diamine, 3, 3°-diaminodiphenylsulfone, 3,3'-dimethyl-4,4'-diami Nodicyclohexylmethane and a commercially available ether diamine with the formula: el+2-diaminoethane, where n is an integer from 1 to 2000, and 1.6-diamithexane is particularly preferred; preferred amino alcohols include 2-alcohols. minoethanol and 3-aminopropanol.
本反応に適当なジオールは、望ましくは2〜44個の炭素原子を持つ、−級およ び二級脂肪族、環状−脂肪族、脂肪−芳香族および芳香族ジオールである。有利 にはグリコール、1.4ブタンジオール、2−ブチン−1,4ジオール、2−ブ テン−1,4−ジオール、1.5−ベンタンジオール、1.6−ヘキサンジオー ル、1.10デカンジオール、ネオペンチルグリコール、N、N−ジエチルアミ ノプロパンジオール−2,3、またはヒドロキシビバリック酸ネオペンチルグリ コールエステルである。特に望ましいのは、1゜4ブタンジオール、および1, 10−デカンジオールである。Suitable diols for this reaction include -class and -class diols, preferably having 2 to 44 carbon atoms. and secondary aliphatic, cycloaliphatic, aliphatic-aromatic and aromatic diols. advantageous contains glycol, 1.4-butanediol, 2-butyne-1,4diol, 2-butanediol, Thene-1,4-diol, 1,5-bentanediol, 1,6-hexanediol 1.10 decanediol, neopentyl glycol, N,N-diethylamide Nopropanediol-2,3, or neopentyl glycylate hydroxybivaric acid It is a coal ester. Particularly desirable are 1.4 butanediol and 1. 10-decanediol.
反応は20℃と200℃の間の温度範囲で有利に行われる。通常プラスチック製 造に使用されるような触媒と安定剤が反応混合物に添加できる0反応は溶液また は溶融体のいずれかで行われる。不活性ガス中で実施すると好都合である。The reaction is advantageously carried out in a temperature range between 20°C and 200°C. Usually made of plastic Catalysts and stabilizers, such as those used in is carried out either in the melt. It is convenient to carry out under an inert gas.
本発明による方法で得られたプラスチックは透明で熱硬化性である。それらの性 質は、本質的に出発油脂の種類、酸化および架橋の程度、および使用した二官能 性または多官能性化合物のタイプ、それらの酸化されたトリグリセライドに対す るモル混合比に依存する。The plastics obtained by the method according to the invention are transparent and thermosetting. their gender The quality depends essentially on the type of starting fat, the degree of oxidation and crosslinking, and the difunctionality used. types of functional or polyfunctional compounds, their oxidized triglycerides Depends on the molar mixing ratio.
ここでは全く一般的に、古典的ポリマー化学のルールが考慮されるべきである。Quite generally, the rules of classical polymer chemistry should be considered here.
二官能性または多官能性化合物の望ましい量は、この化合物中の反応基の割合が トリグリセライド中のヒ・ ドロキシまたはエポキシ基に対して、0.5〜1. 5の間にあるものが選ばれる。The desired amount of difunctional or polyfunctional compound is determined by the proportion of reactive groups in this compound. 0.5 to 1. The one between 5 is selected.
とうだいぐさ油、またはオレイン酸含量が85%もの高オレイン酸型のひまわり 油から得られるような、高度に酸化されたトリグリセライドを使用すると、プラ スチックの性質を容易に変更できる。何故なら、この場合、二官能性または多官 能性化合物に対する、酸化されたトリグリセライドのポリマー生成混合比率の可 能範囲は特に広いからである。Horseradish oil or sunflower with a high oleic acid content of 85% Using highly oxidized triglycerides, such as those obtained from oils, The properties of the stick can be easily changed. Because in this case, bifunctional or polyfunctional Possible polymer-forming mixing ratios of oxidized triglycerides to functional compounds This is because the range of abilities is particularly wide.
それ故に、酸化の程度はより高くあるべきで、二官能性または多官能性含量の部 分がより多い程、結合は一層強くなる。さらに親水性および吸着能力は、ヒドロ キシル基の数が増加するに応じて増加する。これはプラスチック材料が、硝子、 フェスおよび金属のような他物質に一層良く付着するに適することを意味する。Therefore, the degree of oxidation should be higher and the proportion of di- or polyfunctional content should be higher. The more minutes there are, the stronger the bond will be. Furthermore, the hydrophilicity and adsorption capacity are It increases as the number of xyl groups increases. This is plastic material, glass, This means that it is better suited for adhering to surfaces and other materials such as metals.
本発明による方法は、このような油脂を、従来望ましくない随伴物のために使用 できなかった油脂をプラスチック工程に利用し易くする。こうして本発明は、工 業的に有用な製品と中間物を、簡単な方法で、しかも低コストで加工できるよう にする。The method according to the invention eliminates the use of such fats and oils for traditionally undesirable accompaniments. To make it easier to use oils and fats that cannot be used in plastic processes. In this way, the present invention Industrially useful products and intermediates can be processed easily and at low cost. Make it.
国際調査報告 −1,−絢一=−11−mPcT/EP 90101259国際調査報告international search report -1, -Kenichi=-11-mPcT/EP 90101259 International Investigation Report
Claims (8)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3926285.5 | 1989-08-09 | ||
| DE3926285 | 1989-08-09 |
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|---|---|
| JPH04501284A true JPH04501284A (en) | 1992-03-05 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2511716A Pending JPH04501284A (en) | 1989-08-09 | 1990-08-01 | Method of manufacturing plastic from raw material oils and fats |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0437592A1 (en) |
| JP (1) | JPH04501284A (en) |
| CA (1) | CA2038936A1 (en) |
| DE (1) | DE4024364A1 (en) |
| WO (1) | WO1991001980A2 (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4119295C2 (en) * | 1991-06-12 | 1994-12-01 | Frische Gmbh | Environmentally safe composite material made of natural fibers or products and plastics of the polyurethane-polyester and / or polyurethane-polyamide type and process for its production |
| EP0724613B1 (en) * | 1993-10-20 | 2002-02-20 | Henkel Kommanditgesellschaft auf Aktien | Binders based on fat chemical reaction products |
| NZ312082A (en) * | 1995-07-05 | 2000-04-28 | Preform Raumgliederungssysteme | Polymer material comprising the reaction product of a triglyceride having at least two epoxide groups and a polycarboxylic acid anhydride, process for its production and use thereof |
| DE19646424A1 (en) | 1996-11-11 | 1998-05-14 | Henkel Kgaa | Use of polyols for isocyanate casting resins and coating compositions |
| DE19834048A1 (en) * | 1998-07-30 | 2000-02-03 | Cognis Deutschland Gmbh | Composites based on renewable raw materials |
| EP0992569A1 (en) * | 1998-10-05 | 2000-04-12 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | Preservation/lubricant/primercomposition for metallic surfaces |
| DE10015913A1 (en) * | 1999-04-16 | 2000-10-19 | Henkel Kgaa | Adducts used as binders for adhesives or as tackifiers are obtained from unsaturated natural fats or oils by ene or Diels-Alder reactions followed by radical or oxidative treatment |
| DE19930770A1 (en) | 1999-07-03 | 2001-01-04 | Cognis Deutschland Gmbh | Process for the production of fiber composite materials |
| DE102006003762A1 (en) * | 2006-01-25 | 2007-07-26 | Dracowo Forschungs- Und Entwicklungs Gmbh | Fiber composite materials are made using natural epoxide resins matrices obtained by acid reaction of ethoxylated linseed oil epoxides or other highly ethoxylated fatty acid epoxides without use of comonomers |
| DE102008014558A1 (en) | 2008-03-15 | 2009-09-17 | Dracowo Forschungs- Und Entwicklungs Gmbh | Polycarboxylic acid modified native epoxides with a specific ratio of epoxide-polycarboxylic acid in glycidyl ester epoxide, useful for preparing polyether and polyester |
| DE102010040601A1 (en) | 2009-09-11 | 2011-03-17 | Dracowo Forschungs- Und Entwicklungs Gmbh | Technical production of carboxylic acid-modified epoxide from native oils, useful e.g as food preservative, comprises epoxidating the native oil, separating the epoxide phase, reacting the separated epoxide phase with polycarboxylic acid |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2569502A (en) * | 1945-02-07 | 1951-10-02 | Swern Daniel | Epoxidized oils |
| FR1129495A (en) * | 1954-03-23 | 1957-01-22 | Fmc Corp | Epoxidation process for natural unsaturated oils |
| US3051729A (en) * | 1957-09-10 | 1962-08-28 | Archer Daniels Midland Co | Method of preparing epoxidized oils and the like |
| FR1295619A (en) * | 1961-05-09 | 1962-06-08 | Swift & Co | Process for the production of a prepolymer of highly epoxidized fatty oils and polyamines and prepolymer obtained by this process |
| FR1335729A (en) * | 1961-08-22 | 1963-08-23 | Mobay Chemical Corp | Polyurethane plastics |
| NL302305A (en) * | 1962-12-20 | 1900-01-01 | British Celanese | |
| DE1645539C3 (en) * | 1965-02-17 | 1973-10-25 | Unilever N.V., Rotterdam (Niederlande) | Process for the production of water-thinnable or emulsifiable binders |
| US3843391A (en) * | 1969-11-10 | 1974-10-22 | Ciba Geigy Ag | Process for finishing textiles |
| DE3246612A1 (en) * | 1982-12-16 | 1984-06-20 | Henkel KGaA, 4000 Düsseldorf | METHOD FOR PRODUCING MODIFIED TRIGLYCERIDES WITH MEDIUM EPOXY AND HYDROXYL AND ETHER GROUPS |
| DE3246615A1 (en) * | 1982-12-16 | 1984-06-20 | Henkel KGaA, 4000 Düsseldorf | ALKYD RESIN CONTAINING FUNCTIONAL EPOXIES |
| DE3307421A1 (en) * | 1983-03-03 | 1984-09-06 | Rhein-Chemie Rheinau Gmbh, 6800 Mannheim | PRODUCTION AND USE OF CROSS-LINKED, EPOXIDIZED FAT OILS |
| DE3320219A1 (en) * | 1983-06-03 | 1984-12-06 | Henkel KGaA, 4000 Düsseldorf | CONTINUOUS, CATALYTIC EPOXIDATION OF DOUBLE OLEFINIC BINDINGS WITH HYDROGEN PEROXIDE AND FORMIC ACID |
-
1990
- 1990-08-01 DE DE19904024364 patent/DE4024364A1/en not_active Withdrawn
- 1990-08-01 EP EP19900912681 patent/EP0437592A1/en not_active Withdrawn
- 1990-08-01 WO PCT/EP1990/001259 patent/WO1991001980A2/en not_active Ceased
- 1990-08-01 JP JP2511716A patent/JPH04501284A/en active Pending
- 1990-08-01 CA CA 2038936 patent/CA2038936A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
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| WO1991001980A2 (en) | 1991-02-21 |
| EP0437592A1 (en) | 1991-07-24 |
| WO1991001980A3 (en) | 1991-03-21 |
| CA2038936A1 (en) | 1991-02-10 |
| DE4024364A1 (en) | 1991-02-14 |
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