JPH04257536A - Diol compound having cyclohexane ring and its production - Google Patents
Diol compound having cyclohexane ring and its productionInfo
- Publication number
- JPH04257536A JPH04257536A JP3018613A JP1861391A JPH04257536A JP H04257536 A JPH04257536 A JP H04257536A JP 3018613 A JP3018613 A JP 3018613A JP 1861391 A JP1861391 A JP 1861391A JP H04257536 A JPH04257536 A JP H04257536A
- Authority
- JP
- Japan
- Prior art keywords
- cyclohexane
- diol compound
- propyl
- hydroxy
- compound
- 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.)
- Granted
Links
- -1 Diol compound Chemical class 0.000 title claims abstract description 22
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 26
- 239000003960 organic solvent Substances 0.000 claims abstract description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 6
- 239000001257 hydrogen Substances 0.000 claims abstract description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims abstract description 3
- 238000006243 chemical reaction Methods 0.000 abstract description 24
- 150000001875 compounds Chemical class 0.000 abstract description 17
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 abstract description 6
- 229920000642 polymer Polymers 0.000 abstract description 4
- 150000002978 peroxides Chemical class 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 abstract description 2
- 239000003381 stabilizer Substances 0.000 abstract description 2
- 239000004094 surface-active agent Substances 0.000 abstract description 2
- 241000283690 Bos taurus Species 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 10
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 10
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 8
- 238000006722 reduction reaction Methods 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- UGPWRRVOLLMHSC-UHFFFAOYSA-N 2-[3-(2-hydroxypropan-2-yl)phenyl]propan-2-ol Chemical compound CC(C)(O)C1=CC=CC(C(C)(C)O)=C1 UGPWRRVOLLMHSC-UHFFFAOYSA-N 0.000 description 5
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 5
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 5
- 229910052707 ruthenium Inorganic materials 0.000 description 5
- QLAJIFRXKTVJRX-UHFFFAOYSA-N 2-[3-(2-hydroxypropan-2-yl)cyclohexyl]propan-2-ol Chemical compound CC(C)(O)C1CCCC(C(C)(C)O)C1 QLAJIFRXKTVJRX-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- 208000012839 conversion disease Diseases 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- 238000004817 gas chromatography Methods 0.000 description 4
- 229910052703 rhodium Inorganic materials 0.000 description 4
- 239000010948 rhodium Substances 0.000 description 4
- LEARFTRDZQQTDN-UHFFFAOYSA-N 2-[4-(2-hydroxypropan-2-yl)phenyl]propan-2-ol Chemical compound CC(C)(O)C1=CC=C(C(C)(C)O)C=C1 LEARFTRDZQQTDN-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 229910052763 palladium Inorganic materials 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- AZQRXYPICCDFKX-UHFFFAOYSA-N 2-[3-(1-hydroxyethyl)cyclohexyl]propan-2-ol Chemical compound CC(O)C1CCCC(C1)C(C)(C)O AZQRXYPICCDFKX-UHFFFAOYSA-N 0.000 description 2
- YBIUTEHXBIHTDE-UHFFFAOYSA-N 2-[4-(2-hydroxypropan-2-yl)cyclohexyl]propan-2-ol Chemical compound CC(C)(O)C1CCC(C(C)(C)O)CC1 YBIUTEHXBIHTDE-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910052702 rhenium Inorganic materials 0.000 description 2
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- XULVUKHIJXQUDO-UHFFFAOYSA-N 1-[2-(1-hydroxyethyl)cyclohexyl]ethanol Chemical compound CC(O)C1CCCCC1C(C)O XULVUKHIJXQUDO-UHFFFAOYSA-N 0.000 description 1
- WNQZLDLHFMYGFB-UHFFFAOYSA-N 1-[2-(1-hydroxyethyl)phenyl]ethanol Chemical compound CC(O)C1=CC=CC=C1C(C)O WNQZLDLHFMYGFB-UHFFFAOYSA-N 0.000 description 1
- JYFLNNVENRPSEI-UHFFFAOYSA-N 1-[3-(1-hydroxyethyl)cyclohexyl]ethanol Chemical compound CC(O)C1CCCC(C(C)O)C1 JYFLNNVENRPSEI-UHFFFAOYSA-N 0.000 description 1
- JXGTYKDVCCARGA-UHFFFAOYSA-N 1-[3-(1-hydroxyethyl)phenyl]ethanol Chemical compound CC(O)C1=CC=CC(C(C)O)=C1 JXGTYKDVCCARGA-UHFFFAOYSA-N 0.000 description 1
- SUFNMUXAUBJEHK-UHFFFAOYSA-N 1-[4-(1-hydroxyethyl)cyclohexyl]ethanol Chemical compound CC(O)C1CCC(C(C)O)CC1 SUFNMUXAUBJEHK-UHFFFAOYSA-N 0.000 description 1
- BHCGGVIVFXWATI-UHFFFAOYSA-N 1-[4-(1-hydroxyethyl)phenyl]ethanol Chemical compound CC(O)C1=CC=C(C(C)O)C=C1 BHCGGVIVFXWATI-UHFFFAOYSA-N 0.000 description 1
- 125000004066 1-hydroxyethyl group Chemical group [H]OC([H])([*])C([H])([H])[H] 0.000 description 1
- SBASXUCJHJRPEV-UHFFFAOYSA-N 2-(2-methoxyethoxy)ethanol Chemical compound COCCOCCO SBASXUCJHJRPEV-UHFFFAOYSA-N 0.000 description 1
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 description 1
- ZZKGDTNQFLOKLN-UHFFFAOYSA-N 2-[1-(2-hydroxypropan-2-yl)cyclohexyl]propan-2-ol Chemical compound CC(C)(O)C1(C(C)(C)O)CCCCC1 ZZKGDTNQFLOKLN-UHFFFAOYSA-N 0.000 description 1
- MUTDMJAPYVRYFV-UHFFFAOYSA-N 2-[2-(1-hydroxyethyl)cyclohexyl]propan-2-ol Chemical compound OC(C)C1C(CCCC1)C(C)(C)O MUTDMJAPYVRYFV-UHFFFAOYSA-N 0.000 description 1
- RMLRJGODYWIDJZ-UHFFFAOYSA-N 2-[2-(2-hydroxypropan-2-yl)cyclohexyl]propan-2-ol Chemical compound OC(C)(C)C1C(CCCC1)C(C)(C)O RMLRJGODYWIDJZ-UHFFFAOYSA-N 0.000 description 1
- KSMBFKMHJGVFQO-UHFFFAOYSA-N 2-[2-(2-hydroxypropan-2-yl)phenyl]propan-2-ol Chemical compound CC(C)(O)C1=CC=CC=C1C(C)(C)O KSMBFKMHJGVFQO-UHFFFAOYSA-N 0.000 description 1
- FVFIGQIPPFRMLP-UHFFFAOYSA-N 2-[4-(1-hydroxyethyl)cyclohexyl]propan-2-ol Chemical compound CC(O)C1CCC(CC1)C(C)(C)O FVFIGQIPPFRMLP-UHFFFAOYSA-N 0.000 description 1
- ZNQVEEAIQZEUHB-UHFFFAOYSA-N 2-ethoxyethanol Chemical compound CCOCCO ZNQVEEAIQZEUHB-UHFFFAOYSA-N 0.000 description 1
- FJCMBINIICRZGV-UHFFFAOYSA-N CC(O)c1cccc(c1)C(C)(C)O Chemical compound CC(O)c1cccc(c1)C(C)(C)O FJCMBINIICRZGV-UHFFFAOYSA-N 0.000 description 1
- QFYTVLMFCCRECV-UHFFFAOYSA-N CC(O)c1ccccc1C(C)(C)O Chemical compound CC(O)c1ccccc1C(C)(C)O QFYTVLMFCCRECV-UHFFFAOYSA-N 0.000 description 1
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- GIVPVFUIMGNQMZ-UHFFFAOYSA-N OC(C)(C)C1=CC=C(C=C1)C(C)O Chemical compound OC(C)(C)C1=CC=C(C=C1)C(C)O GIVPVFUIMGNQMZ-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- POLCUAVZOMRGSN-UHFFFAOYSA-N dipropyl ether Chemical compound CCCOCCC POLCUAVZOMRGSN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000007327 hydrogenolysis reaction Methods 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 238000001819 mass spectrum Methods 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
- 239000003607 modifier Substances 0.000 description 1
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- HBEQXAKJSGXAIQ-UHFFFAOYSA-N oxopalladium Chemical compound [Pd]=O HBEQXAKJSGXAIQ-UHFFFAOYSA-N 0.000 description 1
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical compound [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 description 1
- SJLOMQIUPFZJAN-UHFFFAOYSA-N oxorhodium Chemical compound [Rh]=O SJLOMQIUPFZJAN-UHFFFAOYSA-N 0.000 description 1
- 229910003445 palladium oxide Inorganic materials 0.000 description 1
- 229910003446 platinum oxide Inorganic materials 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229910003450 rhodium oxide Inorganic materials 0.000 description 1
- 229910001925 ruthenium oxide Inorganic materials 0.000 description 1
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- JOKPITBUODAHEN-UHFFFAOYSA-N sulfanylideneplatinum Chemical compound [Pt]=S JOKPITBUODAHEN-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、前記一般式(1)で表
わされる新規なシクロヘキサン環を有するジオール化合
物に関するもの、及び前記一般式(3)で表わされるシ
クロヘキサン環を有するジオール化合物の製造方法に関
するものである。本発明のシクロヘキサン環を有するジ
オール化合物は、ポリマー、ポリマーの改質剤、界面活
性剤、各種安定剤、過酸化物等の製造用原料として極め
て有用である。[Field of Industrial Application] The present invention relates to a novel diol compound having a cyclohexane ring represented by the above general formula (1), and a method for producing a diol compound having a cyclohexane ring represented by the above general formula (3). It is related to. The diol compound having a cyclohexane ring of the present invention is extremely useful as a raw material for producing polymers, polymer modifiers, surfactants, various stabilizers, peroxides, and the like.
【0002】0002
【従来の技術】前記一般式(1)で表わされるシクロヘ
キサン環を有するジオール化合物は、知られていない。
また、前記一般式(3)で表わされるシクロヘキサン環
を有するジオール化合物は、上記のとおり有用な化合物
であるにもかかわらず、工業的にも実施可能な優れた製
造方法は見い出されていない。BACKGROUND OF THE INVENTION A diol compound having a cyclohexane ring represented by the general formula (1) is not known. Further, although the diol compound having a cyclohexane ring represented by the general formula (3) is a useful compound as described above, no excellent manufacturing method that is industrially practicable has been found.
【0003】0003
【発明が解決しようとする課題】かかる現状に鑑み、本
発明の目的は、前記一般式(1)で表わされる新規なシ
クロヘキサン環を有するジオール化合物を提供すると共
に、前記一般式(3)で表わされるシクロヘキサン環を
有するジオール化合物の製造方法であって、工業的にも
実施可能で、かつ高転化率及び高選択率を実現できる、
優れた製造方法を提供することにある。SUMMARY OF THE INVENTION In view of the current situation, an object of the present invention is to provide a novel diol compound having a cyclohexane ring represented by the above general formula (1), and to provide a diol compound having a novel cyclohexane ring represented by the above general formula (3). A method for producing a diol compound having a cyclohexane ring, which is industrially feasible and capable of achieving high conversion and high selectivity.
Our goal is to provide an excellent manufacturing method.
【0004】0004
【課題を解決するための手段】本発明者らは、上記の目
的を達成すべく、鋭意検討の結果、本発明に到達したも
のである。すなわち、本発明のうち、一の発明は、前記
一般式(1)で表わされるシクロヘキサン環を有するジ
オール化合物に係るものである。また、他の発明は、前
記一般式(2)で表わされるベンゼン環を有するジオー
ル化合物を、有機溶媒及び還元用触媒の存在下、水素還
元することにより、前記一般式(3)で表わされるシク
ロヘキサン環を有するジオール化合物とするシクロヘキ
サン環を有するジオール化合物の製造方法に係るもので
ある。[Means for Solving the Problems] In order to achieve the above object, the present inventors have arrived at the present invention as a result of intensive studies. That is, one aspect of the present invention relates to a diol compound having a cyclohexane ring represented by the general formula (1). Further, in another invention, a diol compound having a benzene ring represented by the general formula (2) is reduced with hydrogen in the presence of an organic solvent and a reduction catalyst, thereby producing cyclohexane represented by the general formula (3). The present invention relates to a method for producing a diol compound having a cyclohexane ring, which is a diol compound having a ring.
【0005】以下、詳細に説明する。本発明の一般式(
1)で表わされる化合物は、具体的には、1,3−ジ(
1−ヒドロキシエチル)シクロヘキサン、1,3−ジ(
2−ヒドロキシ−2−プロピル)シクロヘキサン、又は
1−(1−ヒドロキシエチル)−3−(2−ヒドロキシ
−2−プロピル)シクロヘキサンである。[0005] This will be explained in detail below. General formula of the present invention (
Specifically, the compound represented by 1) is 1,3-di(
1-hydroxyethyl)cyclohexane, 1,3-di(
2-hydroxy-2-propyl)cyclohexane, or 1-(1-hydroxyethyl)-3-(2-hydroxy-2-propyl)cyclohexane.
【0006】本発明の一般式(2)で表わされる化合物
は、具体的には、1,2−ジ(1−ヒドロキシエチル)
ベンゼン、1,2−ジ(2−ヒドロキシ−2−プロピル
)ベンゼン、1−(1−ヒドロキシエチル)−2−(2
−ヒドロキシ−2−プロピル)ベンゼン、1,3−ジ(
1−ヒドロキシエチル)ベンゼン、1,3−ジ(2−ヒ
ドロキシ−2−プロピル)ベンゼン、1−(1−ヒドロ
キシエチル)−3−(2−ヒドロキシ−2−プロピル)
ベンゼン、1,4−ジ(1−ヒドロキシエチル)ベンゼ
ン、1,4−ジ(2−ヒドロキシ−2−プロピル)ベン
ゼン、又は1−(1−ヒドロキシエチル)−4−(2−
ヒドロキシ−2−プロピル)ベンゼンである。Specifically, the compound represented by the general formula (2) of the present invention is 1,2-di(1-hydroxyethyl)
Benzene, 1,2-di(2-hydroxy-2-propyl)benzene, 1-(1-hydroxyethyl)-2-(2
-hydroxy-2-propyl)benzene, 1,3-di(
1-hydroxyethyl)benzene, 1,3-di(2-hydroxy-2-propyl)benzene, 1-(1-hydroxyethyl)-3-(2-hydroxy-2-propyl)
Benzene, 1,4-di(1-hydroxyethyl)benzene, 1,4-di(2-hydroxy-2-propyl)benzene, or 1-(1-hydroxyethyl)-4-(2-
hydroxy-2-propyl)benzene.
【0007】本発明の一般式(3)で表わされる化合物
は、具体的には、1,2−ジ(1−ヒドロキシエチル)
シクロヘキサン、1,2−ジ(2−ヒドロキシ−2−プ
ロピル)シクロヘキサン、1−(1−ヒドロキシエチル
)−2−(2−ヒドロキシ−2−プロピル)シクロヘキ
サン、1,3−ジ(1−ヒドロキシエチル)シクロヘキ
サン、1,3−ジ(2−ヒドロキシ−2−プロピル)シ
クロヘキサン、1−(1−ヒドロキシエチル)−3−(
2−ヒドロキシ−2−プロピル)シクロヘキサン、1,
4−ジ(1−ヒドロキシエチル)シクロヘキサン、1,
4−ジ(2−ヒドロキシ−2−プロピル)シクロヘキサ
ン、又は1−(1−ヒドロキシエチル)−4−(2−ヒ
ドロキシ−2−プロピル)シクロヘキサンである。Specifically, the compound represented by the general formula (3) of the present invention is 1,2-di(1-hydroxyethyl)
Cyclohexane, 1,2-di(2-hydroxy-2-propyl)cyclohexane, 1-(1-hydroxyethyl)-2-(2-hydroxy-2-propyl)cyclohexane, 1,3-di(1-hydroxyethyl) ) cyclohexane, 1,3-di(2-hydroxy-2-propyl)cyclohexane, 1-(1-hydroxyethyl)-3-(
2-hydroxy-2-propyl)cyclohexane, 1,
4-di(1-hydroxyethyl)cyclohexane, 1,
4-di(2-hydroxy-2-propyl)cyclohexane or 1-(1-hydroxyethyl)-4-(2-hydroxy-2-propyl)cyclohexane.
【0008】一般式(2)で表わされる化合物の製法は
、特に限定されないが、下記一般式(4)で表わされる
化合物を空気酸化して得ることができ、又は下記一般式
(5)又は(6)で表わされる化合物を、亜硫酸ソーダ
、触媒存在下の水素等による還元反応に付すことにより
得ることができる。The method for producing the compound represented by the general formula (2) is not particularly limited, but it can be obtained by air oxidation of the compound represented by the following general formula (4), or the compound represented by the following general formula (5) or ( The compound represented by 6) can be obtained by subjecting it to a reduction reaction using sodium sulfite, hydrogen, etc. in the presence of a catalyst.
【0009】[0009]
【0010】(式中、R1、R2は、H及びCH3 基
のうちから選ばれる同一又は異なる基である。)(In the formula, R1 and R2 are the same or different groups selected from H and CH3 groups.)
【00
11】本発明の方法において使用される還元用触媒とし
ては、パラジウム黒、酸化パラジウム、コロイドパラジ
ウム、パラジウム/活性炭、パラジウム/アルミナ、パ
ラジウム/硫酸バリウム、パラジウム/炭酸バリウムな
どのパラジウム触媒、白金黒、コロイド白金、白金海綿
、酸化白金、硫化白金、白金/活性炭などの白金触媒、
レニウム/活性炭などのレニウム触媒、酸化ロジウム、
ロジウム/活性炭、ロジウム/アルミナなどのロジウム
触媒、酸化ルテニウム、ルテニウム/活性炭、ルテニウ
ム/アルミナなどのルテニウム触媒などを例示でき、こ
れらの金属触媒は、各々単独で、又は二種類以上の多元
系の触媒として用いることができ、更にこれらの触媒に
他の金属類を少量加えて変性させたものを使用してもよ
い。これらの還元用触媒のうちでは、ロジウム触媒、ル
テニウム触媒を使用することが好ましく、特に活性炭又
はアルミナに担持したロジウム触媒、ルテニウム触媒を
使用することが好ましい。00
11] Reduction catalysts used in the method of the present invention include palladium catalysts such as palladium black, palladium oxide, colloidal palladium, palladium/activated carbon, palladium/alumina, palladium/barium sulfate, palladium/barium carbonate, platinum black, Platinum catalysts such as colloidal platinum, platinum sponge, platinum oxide, platinum sulfide, platinum/activated carbon,
Rhenium catalysts such as rhenium/activated carbon, rhodium oxide,
Examples include rhodium catalysts such as rhodium/activated carbon and rhodium/alumina, ruthenium catalysts such as ruthenium oxide, ruthenium/activated carbon, and ruthenium/alumina. Furthermore, these catalysts may be modified by adding small amounts of other metals. Among these reduction catalysts, it is preferable to use a rhodium catalyst or a ruthenium catalyst, and it is particularly preferable to use a rhodium catalyst or a ruthenium catalyst supported on activated carbon or alumina.
【0012】還元用触媒の使用量は、一般式(2)で表
わされる化合物1重量部あたり、触媒全重量として、0
.005 〜0.2 重量部が好ましい。The amount of the reduction catalyst used is 0 as the total weight of the catalyst per 1 part by weight of the compound represented by the general formula (2).
.. 0.05 to 0.2 parts by weight is preferred.
【0013】本発明の実施においては、有機溶媒が使用
される。有機溶媒としては、一般式(2)の化合物を溶
解し、かつ水素還元反応に不活性な溶媒であれば特に限
定されないが、具体的には、エチレングリコールモノメ
チルエーテル、エチレングリコールモノエチルエーテル
、エチレングリコールジメチルエーテル、ジエチレング
リコールモノメチルエーテル、ジオキサン、ジプロピル
エーテル、ジフェニルエーテルなどのエーテル類、メタ
ノール、エタノール、イソプロパノール、シクロヘキサ
ノール、エチレングリコール、ジエチレングリコールな
どのアルコール類などを例示することができ、中でも、
メタノール、エタノール、イソプロパノール、シクロヘ
キサノールが好ましい。有機溶媒の使用量は、通常、一
般式(2)の化合物1重量部あたり、0.5 〜20重
量部が用いられる。[0013] In the practice of this invention, organic solvents are used. The organic solvent is not particularly limited as long as it dissolves the compound of general formula (2) and is inert to the hydrogen reduction reaction, but specific examples include ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, and ethylene. Examples include ethers such as glycol dimethyl ether, diethylene glycol monomethyl ether, dioxane, dipropyl ether, and diphenyl ether; alcohols such as methanol, ethanol, isopropanol, cyclohexanol, ethylene glycol, and diethylene glycol; among others,
Methanol, ethanol, isopropanol and cyclohexanol are preferred. The amount of organic solvent used is usually 0.5 to 20 parts by weight per 1 part by weight of the compound of general formula (2).
【0014】本発明の反応温度は、30〜250 ℃、
好ましくは50〜200 ℃の範囲であり、反応圧力は
1〜50kg/cm2G 、好ましくは5〜30kg/
cm2G である。反応は、通常、オートクレーブによ
るスラリー反応、固定床の流通反応の方式がとられる。
上記のとおり、触媒量、反応温度及び反応圧力に対する
好ましい範囲を定めた理由は、次のとおりである。すな
わち、触媒量が多すぎる、反応温度が高過ぎる、又は反
応圧力が高すぎる場合には、目的の反応以外の副反応、
例えば水素化分解反応等を生じ、副生物が増加する。一
方、触媒量が少なすぎる、反応温度が低すぎる、又は反
応圧力が低すぎる場合には、目的の反応の反応速度が遅
い。なお、有機溶媒の量が少なすぎる場合は除熱の制御
の点で、また、多すぎる場合はエネルギー消費の点で好
ましくない。[0014] The reaction temperature of the present invention is 30 to 250°C;
Preferably the temperature is in the range of 50 to 200°C, and the reaction pressure is 1 to 50 kg/cm2G, preferably 5 to 30 kg/cm2G.
cm2G. The reaction usually takes the form of a slurry reaction using an autoclave or a fixed bed flow reaction. As mentioned above, the reason for determining the preferable ranges for the amount of catalyst, reaction temperature, and reaction pressure is as follows. That is, if the amount of catalyst is too large, the reaction temperature is too high, or the reaction pressure is too high, side reactions other than the desired reaction,
For example, hydrogenolysis reactions occur, resulting in an increase in by-products. On the other hand, if the amount of catalyst is too small, the reaction temperature is too low, or the reaction pressure is too low, the reaction rate of the desired reaction will be slow. Incidentally, if the amount of the organic solvent is too small, it is undesirable from the viewpoint of heat removal control, and when it is too large, it is undesirable from the viewpoint of energy consumption.
【0015】かくして得られる反応混合物から、目的の
化合物(3)を分離、回収する好ましい方法は次のとお
りである。すなわち、反応終了後、触媒をろ過分離し、
次いで蒸留により有機溶媒を除去し、引き続いて生成物
を蒸留で留出させ、固化させて目的の化合物(3)を取
得するか、又は蒸留で有機溶媒を除いた後の缶出液、又
は缶出液から蒸留によって得た留出液をヘキサン、トル
エン、クロルベンゼン、水等を単独又は混合した溶媒で
晶析して、目的の化合物(3)を取得することができる
。A preferred method for separating and recovering the target compound (3) from the reaction mixture thus obtained is as follows. That is, after the reaction is completed, the catalyst is separated by filtration,
Next, the organic solvent is removed by distillation, and the product is subsequently distilled off and solidified to obtain the target compound (3), or the bottoms or cans after removing the organic solvent by distillation are used. The target compound (3) can be obtained by crystallizing the distillate obtained by distillation from the extract using a solvent such as hexane, toluene, chlorobenzene, water, etc. alone or in combination.
【0016】[0016]
【実施例】次に、実施例をあげて、本発明を更に詳細に
説明するが、本発明は、これに限定されるものではない
。
実施例1
かくはん機付SUS製 200ccオートクレーブに、
1,3−ジ(2−ヒドロキシ−2−プロピル)ベンゼン
48.6g (0.25 モル)、エタノール48.6
g 、5%ロジウム担持活性炭触媒2.43g を仕込
み、水素圧力15kg/cm2G の一定圧力下に75
℃で、還元反応を実施した。2 時間の反応後、所定量
のH2吸収が認められたので、反応を停止し、触媒を瀘
過した後、反応液を取得した。ガスクロマトグラフィー
分析(以下「GC分析」と略す。)の結果、1,3−ジ
(2−ヒドロキシ−2−プロピル)ベンゼンの反応転化
率は99.6%であり、1,3−ジ(2−ヒドロキシ−
2−プロピル)シクロヘキサンの選択率は85.3%で
あった。上記の取得した反応液から、蒸留によってエタ
ノールを除去し、引き続いて減圧下に蒸留して1,3−
ジ(2−ヒドロキシ−2−プロピル)シクロヘキサンを
主成分とする留出液を得、これをトルエンで再結晶して
、融点91.5℃、沸点135 ℃/2mmHgの1,
3−ジ(2−ヒドロキシ−2−プロピル)シクロヘキサ
ンを得た。なお、上記化合物については、マススペクト
ル、NMRスペクトル及び元素分析により、分子量 2
00の1,3−ジ(2−ヒドロキシ−2−プロピル)シ
クロヘキサンであることを確認した。[Examples] Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto. Example 1 In a SUS 200cc autoclave with a stirrer,
1,3-di(2-hydroxy-2-propyl)benzene 48.6g (0.25 mol), ethanol 48.6
g, 2.43 g of 5% rhodium-supported activated carbon catalyst were charged, and 75 g was charged under a constant hydrogen pressure of 15 kg/cm2G.
The reduction reaction was carried out at °C. After 2 hours of reaction, a predetermined amount of H2 absorption was observed, so the reaction was stopped and the reaction solution was obtained after filtering the catalyst. As a result of gas chromatography analysis (hereinafter abbreviated as "GC analysis"), the reaction conversion rate of 1,3-di(2-hydroxy-2-propyl)benzene was 99.6%, and the reaction conversion rate of 1,3-di(2-hydroxy-2-propyl)benzene was 99.6%. 2-hydroxy-
The selectivity of 2-propyl)cyclohexane was 85.3%. Ethanol was removed from the reaction solution obtained above by distillation, and then 1,3-
A distillate containing di(2-hydroxy-2-propyl)cyclohexane as the main component was obtained, and this was recrystallized with toluene to obtain 1,000 g
3-di(2-hydroxy-2-propyl)cyclohexane was obtained. The above compound has a molecular weight of 2 by mass spectrum, NMR spectrum, and elemental analysis.
00 1,3-di(2-hydroxy-2-propyl)cyclohexane.
【0017】実施例2
1,3−ジ(2−ヒドロキシ−2−プロピル)ベンゼン
のかわりに1,4−ジ(2−ヒドロキシ−2−プロピル
)ベンゼンを使用したほかは実施例1と同様にして反応
を実施した。GC分析の結果、1,4−ジ(2−ヒドロ
キシ−2−プロピル)ベンゼンの反応転化率は99.0
%、1,4−ジ(2−ヒドロキシ−2−プロピル)シク
ロヘキサンの選択率は82.1%であった。Example 2 Same as Example 1 except that 1,4-di(2-hydroxy-2-propyl)benzene was used instead of 1,3-di(2-hydroxy-2-propyl)benzene. The reaction was carried out. As a result of GC analysis, the reaction conversion rate of 1,4-di(2-hydroxy-2-propyl)benzene was 99.0.
%, the selectivity for 1,4-di(2-hydroxy-2-propyl)cyclohexane was 82.1%.
【0018】実施例−3
5%ロジウム担持活性炭触媒のかわりに5%ルテニウム
担持活性炭触媒を使用した他は、実施例−1と同様にし
て反応を実施した。GC分析の結果、1,3−ジ(2−
ヒドロキシ−2−プロピル)ベンゼンの反応転化率は、
92.5%、1,3−ジ(2−ヒドロキシ−2−プロピ
ル)シクロヘキサンの選択率は、80.6%であった。Example 3 A reaction was carried out in the same manner as in Example 1, except that a 5% ruthenium-supported activated carbon catalyst was used instead of the 5% rhodium-supported activated carbon catalyst. As a result of GC analysis, 1,3-di(2-
The reaction conversion rate of hydroxy-2-propyl)benzene is
The selectivity for 92.5% and 1,3-di(2-hydroxy-2-propyl)cyclohexane was 80.6%.
【0019】[0019]
【発明の効果】以上、説明したとおり、本発明により、
前記一般式(1)で表わされる新規なシクロヘキサン環
を有するジオール化合物を提供すると共に、前記一般式
(3)で表わされるシクロヘキサン環を有するジオール
化合物の製造方法であって、工業的にも実施可能で、か
つ高転化率及び高選択率を実現できる、優れた製造方法
を提供することができた。[Effect of the invention] As explained above, according to the present invention,
Provided is a novel diol compound having a cyclohexane ring represented by the general formula (1), and a method for producing a diol compound having a cyclohexane ring represented by the general formula (3), which is also industrially practicable. We were able to provide an excellent manufacturing method that can achieve high conversion and high selectivity.
Claims (2)
サン環を有するジオール化合物。 (ただし、R1、R2は、H又はCH3 基のうちから
選ばれる同一又は異なる基である。)1. A diol compound having a cyclohexane ring represented by the following general formula (1). (However, R1 and R2 are the same or different groups selected from H or CH3 groups.)
を有するジオール化合物を、有機溶媒及び還元用触媒の
存在下、水素還元することにより、下記一般式(3)で
表わされるシクロヘキサン環を有するジオール化合物と
するシクロヘキサン環を有するジオール化合物の製造方
法。 (ただし、R1、R2は、H又はCH3 基のうちから
選ばれる同一又は異なる基である。)[Claim 2] By reducing a diol compound having a benzene ring represented by the following general formula (2) with hydrogen in the presence of an organic solvent and a reducing catalyst, a cyclohexane ring represented by the following general formula (3) can be obtained. A method for producing a diol compound having a cyclohexane ring. (However, R1 and R2 are the same or different groups selected from H or CH3 groups.)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03018613A JP3089672B2 (en) | 1991-02-12 | 1991-02-12 | Diol compound having cyclohexane ring and method for producing diol compound having cyclohexane ring |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03018613A JP3089672B2 (en) | 1991-02-12 | 1991-02-12 | Diol compound having cyclohexane ring and method for producing diol compound having cyclohexane ring |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04257536A true JPH04257536A (en) | 1992-09-11 |
JP3089672B2 JP3089672B2 (en) | 2000-09-18 |
Family
ID=11976482
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03018613A Expired - Lifetime JP3089672B2 (en) | 1991-02-12 | 1991-02-12 | Diol compound having cyclohexane ring and method for producing diol compound having cyclohexane ring |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3089672B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004024934A1 (en) * | 2002-09-09 | 2004-03-25 | Nippon Kayaku Kabushiki Kaisha | Process for producing optically active erythro 3-cyclohexylserines |
JP2021080343A (en) * | 2019-11-15 | 2021-05-27 | 旭化成株式会社 | Hydrogenated polyphenylene ether and production method of the same |
-
1991
- 1991-02-12 JP JP03018613A patent/JP3089672B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004024934A1 (en) * | 2002-09-09 | 2004-03-25 | Nippon Kayaku Kabushiki Kaisha | Process for producing optically active erythro 3-cyclohexylserines |
JP2021080343A (en) * | 2019-11-15 | 2021-05-27 | 旭化成株式会社 | Hydrogenated polyphenylene ether and production method of the same |
Also Published As
Publication number | Publication date |
---|---|
JP3089672B2 (en) | 2000-09-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2841261B2 (en) | Method for producing ether alcohols | |
JPS61109782A (en) | Manufacture of 1-alkyl- or 1-cycloalkyl- piperazine | |
JP6372771B2 (en) | Process for producing trans-cyclohexanedicarboxylate bis (2-hydroxyalkyl) | |
JPH04257536A (en) | Diol compound having cyclohexane ring and its production | |
JP3089772B2 (en) | Method for producing diol compound having cyclohexane ring | |
JP3579923B2 (en) | Method for producing alicyclic diketone compound | |
US6881865B2 (en) | Method for preparing cyclohexyl phenyl ketone from 1,3-butadiene and acrylic acid | |
JP4243448B2 (en) | Novel 4- (4 '-(4 "-hydroxyphenyl) cyclohexyl) -1-hydroxybenzenes | |
JP3904854B2 (en) | Method for producing fluorine-containing alicyclic dicarboxylic acid compound | |
JP3535637B2 (en) | Method for producing cis-3,3,5-trimethylcyclohexanol | |
JPH10298144A (en) | Production of trans-4-alkylcyclohexanecarboxylic ester | |
JPH09194433A (en) | Production of tricyclodecanecarboxylic acid ethyl ester | |
JP3154598B2 (en) | N- (4'-nonylcyclohexyl) -4-nonylaniline and method for producing the same | |
JP4472063B2 (en) | Method for producing dicyclohexane derivative | |
JP3103451B2 (en) | Method for producing 7-octen-1-al | |
WO2018078961A1 (en) | Production method for trans-bis(2-hydroxyalkyl) cyclohexanedicarboxylate, and bis(2-hydroxyalkyl) cyclohexanedicarboxylate | |
JP3177350B2 (en) | Method for producing dinonyldiphenylamine | |
JP2523140B2 (en) | Method for producing (4-hydroxyphenyl) -cyclohexanecarboxylic acid | |
JP2002179609A (en) | Method for producing bis(4-oxocyclohexyl) compound | |
JP3008296B2 (en) | Method for producing diaryl glycolic acid | |
JP2008273975A (en) | New 4-(4'-(4"-hydroxyphenyl)cyclohexyl)-1-hydroxybenzenes | |
JP2010126464A (en) | Method for producing amino group-containing imidazoles | |
JPH10237046A (en) | Production of hexahydropyridazine and tetrahydropyridazine | |
JPS6396166A (en) | Production of aromatic hydrazo compound | |
JPH03240746A (en) | Production of o-alkoxyphenols |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080721 Year of fee payment: 8 |
|
RD05 | Notification of revocation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: R3D05 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090721 Year of fee payment: 9 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100721 Year of fee payment: 10 |