JPH0368538A - Production of octahydrodimethanonaphthalene ring-containing compound - Google Patents
Production of octahydrodimethanonaphthalene ring-containing compoundInfo
- Publication number
- JPH0368538A JPH0368538A JP20550889A JP20550889A JPH0368538A JP H0368538 A JPH0368538 A JP H0368538A JP 20550889 A JP20550889 A JP 20550889A JP 20550889 A JP20550889 A JP 20550889A JP H0368538 A JPH0368538 A JP H0368538A
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- cyclopentadiene
- formula
- compound
- compound represented
- 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
- 150000001875 compounds Chemical class 0.000 title claims abstract description 48
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- RAPZOMPOJASZJS-UHFFFAOYSA-N tetracyclo[6.4.0.02,4.05,7]dodec-1(12)-ene Chemical group C12=CCCCC2C2CC2C2C1C2 RAPZOMPOJASZJS-UHFFFAOYSA-N 0.000 title description 3
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000006243 chemical reaction Methods 0.000 claims abstract description 42
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 5
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 abstract description 14
- 239000002994 raw material Substances 0.000 abstract description 7
- -1 fumaric acid diester Chemical class 0.000 abstract description 6
- 229920000642 polymer Polymers 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 4
- 150000002148 esters Chemical class 0.000 abstract description 3
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 abstract description 3
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Natural products OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 abstract description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 abstract 1
- 239000001530 fumaric acid Substances 0.000 abstract 1
- 239000011976 maleic acid Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 11
- 239000011541 reaction mixture Substances 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 description 6
- 239000007810 chemical reaction solvent Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 125000004177 diethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 4
- LDCRTTXIJACKKU-ONEGZZNKSA-N dimethyl fumarate Chemical compound COC(=O)\C=C\C(=O)OC LDCRTTXIJACKKU-ONEGZZNKSA-N 0.000 description 4
- 229960004419 dimethyl fumarate Drugs 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 230000035484 reaction time Effects 0.000 description 4
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 238000005698 Diels-Alder reaction Methods 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- GXDVEXJTVGRLNW-UHFFFAOYSA-N [Cr].[Cu] Chemical compound [Cr].[Cu] GXDVEXJTVGRLNW-UHFFFAOYSA-N 0.000 description 2
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 2
- IEPRKVQEAMIZSS-AATRIKPKSA-N diethyl fumarate Chemical compound CCOC(=O)\C=C\C(=O)OCC IEPRKVQEAMIZSS-AATRIKPKSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000008204 material by function Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- PMJHHCWVYXUKFD-SNAWJCMRSA-N (E)-1,3-pentadiene Chemical compound C\C=C\C=C PMJHHCWVYXUKFD-SNAWJCMRSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- IEPRKVQEAMIZSS-UHFFFAOYSA-N Di-Et ester-Fumaric acid Natural products CCOC(=O)C=CC(=O)OCC IEPRKVQEAMIZSS-UHFFFAOYSA-N 0.000 description 1
- IEPRKVQEAMIZSS-WAYWQWQTSA-N Diethyl maleate Chemical compound CCOC(=O)\C=C/C(=O)OCC IEPRKVQEAMIZSS-WAYWQWQTSA-N 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- ZVQOOHYFBIDMTQ-UHFFFAOYSA-N [methyl(oxido){1-[6-(trifluoromethyl)pyridin-3-yl]ethyl}-lambda(6)-sulfanylidene]cyanamide Chemical compound N#CN=S(C)(=O)C(C)C1=CC=C(C(F)(F)F)N=C1 ZVQOOHYFBIDMTQ-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- LDCRTTXIJACKKU-ARJAWSKDSA-N dimethyl maleate Chemical compound COC(=O)\C=C/C(=O)OC LDCRTTXIJACKKU-ARJAWSKDSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229940049920 malate Drugs 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N malic acid Chemical compound OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 125000001570 methylene group Chemical group [H]C([H])([*:1])[*:2] 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- UMRZSTCPUPJPOJ-KNVOCYPGSA-N norbornane Chemical group C1C[C@H]2CC[C@@H]1C2 UMRZSTCPUPJPOJ-KNVOCYPGSA-N 0.000 description 1
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はオクタヒドロジメタノナフタレン環を有する化
合物の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a compound having an octahydrodimethanonaphthalene ring.
本発明の方法によシ製造される化合物は各種の構造材料
1機能材料として有用な高分子化合物の原料化合物とし
て用いられる。The compounds produced by the method of the present invention are used as raw material compounds for polymeric compounds useful as various structural materials and functional materials.
従来、 1.2.3.4.4a、 5.8.88−オク
タヒドロ−14:5.8−ジメタノナレタレンー2,3
−ジカルボン酸エステルから誘導されるベルヒドロ−1
,4:5.8−ジメタノナフタレン−2,3−ジカルボ
ン酸エステルまたはペルヒトl:I−1,4:5,8−
ジメタノナフタレン−2,3−ジメタノールを原料に用
いて得られるポリエステルはガラス転移温度が高く、寸
法安定性に優れ、写真用フィルムのベースなどに用いら
れることが知られている(米国防#特許第896,03
3号明細書釦よびジャーナル・オブ・ポリマー・サイエ
ンス:ポリマー・ケミストリイ−エデイシE 7 (J
ournal of Polymer 5cience
:Polymer Chemistry Editi
on )、10巻、atc++’1(1972年)参照
)。これらの文献には、フマル酸ジエチルとシクロペン
メジエンかラティールスーアルダー(Diels−Al
der )反応により1.2.3.4.4a。Conventionally, 1.2.3.4.4a, 5.8.88-octahydro-14:5.8-dimethanonaretalene-2,3
-berhydro-1 derived from dicarboxylic acid ester
,4:5.8-dimethanonaphthalene-2,3-dicarboxylic acid ester or perhythmyl:I-1,4:5,8-
Polyester obtained using dimanonaphthalene-2,3-dimethanol as a raw material has a high glass transition temperature, excellent dimensional stability, and is known to be used as a base for photographic films (U.S. National Defense Agency). Patent No. 896,03
No. 3 specification button and Journal of Polymer Science: Polymer Chemistry Editorial E 7 (J
internal of Polymer 5science
:Polymer Chemistry Editi
on), vol. 10, atc++'1 (1972)). These documents include diethyl fumarate and cyclopenmediene or Diels-Alder.
der) 1.2.3.4.4a by reaction.
5、8.8a−オクタヒドロ−1,4:5,8−ジメタ
ノナフタレン−2,3−ジカルボン酸ジエチルを得る方
法が開示されている。A method for obtaining diethyl 5,8.8a-octahydro-1,4:5,8-dimethanonaphthalene-2,3-dicarboxylate is disclosed.
フマル酸ジエチルとシクロペンタジェンカラ1゜2、3
.4.4a、 5.8.8a−オクタヒトO−1,4:
5,8−ジメタノナフタレン−2,3−ジカルボン酸
エステルを製造する上記の方法にふ・いては、反応温度
180℃で18時間という長い反応時間を要し、かつ目
的の収率は僅か22%と低い。このように、従来提案さ
れている方法では反応を長時間行う必要があり、かつ目
的とする化合物の収率が低い。Diethyl fumarate and cyclopentadiene color 1゜2, 3
.. 4.4a, 5.8.8a-octahyto O-1,4:
The above method for producing 5,8-dimethanonaphthalene-2,3-dicarboxylic acid ester requires a long reaction time of 18 hours at a reaction temperature of 180°C, and the desired yield is only 22 % is low. As described above, in the conventionally proposed methods, it is necessary to carry out the reaction for a long time, and the yield of the target compound is low.
本発明の目的は、オクタヒドロジメタノナフタレン骨格
を有するジカルボン酸エステルを工J[に有利に製造す
るための方法を提供することにあるO
〔課題を解決するための手段〕
本発明によれば、上記の目的は、下記一般式(I)%式
%)
(式中、R1によびR2はそれぞれアルキル基を表す。An object of the present invention is to provide a method for advantageously producing a dicarboxylic acid ester having an octahydrodimethanonaphthalene skeleton. , the above object is achieved by the following general formula (I) (% formula %) (wherein R1 and R2 each represent an alkyl group).
)
で示される化合物とシクロペンタジェン曾たはジシクロ
ペンタジェンを反応させるに際し、反応温度を200℃
〜250℃の範囲内に保ち、該シクロペンタジェンまた
ハシシクロペンタジェンをシクロペンタジェンに換算し
た債で一般式(1)で示される化合物に対して最終的に
2モル倍以上の芥とシクロペンタジエン豊たはシンクロ
ペンタジエンを反応させるに際し、反応系に仕込むこと
を特徴とする下記−形式(tl)(式中、R1j?よび
R2は上記に定積したと釦りである。〕
で示される化合物の製造方法を提供することによって達
成される。) When reacting the compound represented by cyclopentadiene or dicyclopentadiene, the reaction temperature is set at 200°C.
The temperature is maintained within the range of ~250°C, and the cyclopentadiene or hasycyclopentadiene is converted into cyclopentadiene, and the compound represented by the general formula (1) is finally mixed with more than 2 moles of soybean and cyclopentadiene. When reacting pentadiene enrichment or synchropentadiene, the reaction system is charged with the following formula (tl) (wherein R1j? and R2 are the constant product of the above.) This is accomplished by providing a method for producing the compound.
一般式(1)&よび一般式(Il)におけるR1および
R2が表すアルキル基としては、炭素数1〜8のアルキ
ル基が好筐しく1その具体例としては次のものが挙げら
れる。The alkyl group represented by R1 and R2 in general formula (1) & general formula (Il) is preferably an alkyl group having 1 to 8 carbon atoms.Specific examples include the following.
CHa CHa
CH3
−CH2(CI(2)5CH3,−CH2−とH(CH
2)3CH3一般式(1)で示される化合物はトランス
体、シス体またはそれらの混合物であってもよい。また
。CHa CHa CH3 -CH2(CI(2)5CH3, -CH2- and H(CH
2) 3CH3 The compound represented by the general formula (1) may be a trans form, a cis form, or a mixture thereof. Also.
−形式(りで示される化合物としては1硅の化合物であ
ってもよいし、2種以上の化合物であってもよい。- The compound represented by the form (ri) may be one compound or two or more types of compounds.
本発明の方法にpいては、シクロペンメジエンまたはジ
シクロペンタジェンの仕込み量は、シクロペンタジェン
に換算した量で一般式(1)で示される化合物に対して
2モル倍以上である必要がある。In the method of the present invention, the amount of cyclopenmediene or dicyclopentadiene charged must be at least 2 times the amount of the compound represented by general formula (1) in terms of cyclopentadiene. There is.
その仕込み量は2〜6モル倍の範囲が好1しく、2〜4
モル倍の範囲がより好オしい。シクロペンタジェン筐た
はジシクロペンタジェンの仕込み量が一般式(1)で示
される化合物に対して2モル倍よす少ない場合は、シク
ロペンタジェンと一般式(1)で示される化合物の1対
1の付加生成物、すなわち5−ノルボルネン−2,3−
ジカルボン酸エステルの生成量が増える結果、−形式(
II)で示される化合物の収率が低下する。一方、その
仕込み量が例えば6モル倍を超えて多い場合には、シク
ロペンタジェンと一般式(1)で示される化合物の3対
】の付加生成物、すなわち1.2.3.4.4&、 5
.8.8a、 9.9a。The amount to be charged is preferably in the range of 2 to 6 times the mole, and 2 to 4 times the mole.
A range of multiple moles is more preferable. When the amount of cyclopentadiene or dicyclopentadiene charged is less than 2 moles relative to the compound represented by general formula (1), 1 mole of cyclopentadiene and the compound represented by general formula (1) The addition product of pair 1, i.e. 5-norbornene-2,3-
As a result of the increase in the amount of dicarboxylic acid ester produced, - form (
The yield of the compound represented by II) decreases. On the other hand, if the amount charged is more than 6 moles, for example, an addition product of 3 pairs of cyclopentadiene and the compound represented by the general formula (1), that is, 1.2.3.4.4 & , 5
.. 8.8a, 9.9a.
10.1011−ドデカヒトel−1,4 : 5,8
: 9.1 (+−)リメタノアントラセンー2,3
−ジカルボン識エステルの生成量が増える結果、−形式
(fl)で示される化合物の収率が低下し、さらにシク
ロペンタジエンオリゴマーの生成量が増えるために反応
液の粘度上昇または沈殿物生成が起こる結果、反応操作
が困難になる場合があり好さしくない。−紋穴(1)で
示される化合物に対して2モル倍以上のCI+Eのシク
ロペンタジェンまたはジシクロペンタ・ジエンを反応開
始時に一度に仕込むのではなく1反応容器の内温か所定
の温度に達したのち、断続的捷たはシンクロペンタジエ
ンを反応させるに際し、反応系に仕込むことによシ、一
般式([[)で示される化合物の収率を高めることがで
きる。仕込み時間は約10分間ないし10時間のa曲内
が好1しく、約10分間ないし8時間の範囲内がより好
ましく、特に約10分間ないし6時間の範囲内が好まし
い。仕込み時間が10時間よりも長い場合には、生成し
た一般式([[lで示される化合物が重合筐たは分解に
よって一部失われることがあり好ましくない。シクロペ
ンタジェン箇たはシンクロペンタジェンの一部を反応開
始時に予め反応容器内に仕込んで釦いてもよい。この仕
込み−)上はシクロペンタジェンまたはシンクロペンタ
ジェンの全仕込み景の90%程度以下が好ましい。シク
ロペンタジェンまたはシンクロペンタジェンの仕込みを
シンクロペンタジエンを反応させるに際し、実施する場
合は、その仕込み速度を一定に保ってもよいし、変化さ
せてもよい。仕込みには適当な送液ボンダを使用すれば
よい。断続的に仕込む場合は、シクロベンメジエン′!
たはシンクロペンタジェンの全仕込み量を2以上の適当
な数のフラクションに分け、それを上記の仕込み時間内
に仕込めがよい。この場合、仕込みには適当な送液ポン
プを用いればよい。反応容器の内温を室温程度にまで冷
却したのちにすることもできる。反応時間は通常約30
分間ないし15時間。10.1011-dodecahyte el-1,4: 5,8
: 9.1 (+-) Rimetanoanthracene-2,3
- As a result of the increase in the amount of dicarboxylic ester produced, the yield of the compound represented by the - format (fl) decreases, and the increase in the amount of cyclopentadiene oligomer produced increases the viscosity of the reaction solution or the formation of precipitates. , which is not preferable as it may make the reaction operation difficult. - Cyclopentadiene or dicyclopentadiene with a CI+E of 2 moles or more of the compound shown by Monka (1) is not charged all at once at the start of the reaction, but after the internal temperature of one reaction vessel reaches a predetermined temperature. When reacting with intermittent fractionation or synchropentadiene, the yield of the compound represented by the general formula ([[) can be increased by charging it to the reaction system. Preparation time is preferably about 10 minutes to 10 hours, more preferably about 10 minutes to 8 hours, particularly preferably about 10 minutes to 6 hours. If the preparation time is longer than 10 hours, it is not preferable that the generated compound represented by the general formula A part of the cyclopentadiene or synchropentadiene may be charged in advance into the reaction vessel at the start of the reaction and then turned off.This charge is preferably about 90% or less of the total charge of cyclopentadiene or synchropentadiene. When cyclopentadiene or synclopentadiene is charged when reacting syncropentadiene, the rate of feeding may be kept constant or may be varied. An appropriate liquid feeding bonder may be used for the preparation. If you use it intermittently, use cyclobenmadiene'!
Alternatively, it is preferable to divide the total charge amount of synchropentagene into two or more appropriate number of fractions and charge them within the above-mentioned charge time. In this case, an appropriate liquid feeding pump may be used for charging. This can also be done after the internal temperature of the reaction vessel has been cooled to about room temperature. Reaction time is usually about 30
minutes to 15 hours.
好筐しくに30分間ないし10時間、より好1しくは1
時間ないし10時間の範囲である。Preferably for 30 minutes to 10 hours, more preferably for 1 hour.
The duration ranges from 1 hour to 10 hours.
本発明の方法にpいては1反応源度が反応速度pよび一
般式(n)で示される化合物の収率に大きな影響を与え
る。反応は200℃〜250℃の範囲の温度で行われる
。反応温度は200℃〜240℃の範囲が好ましく、2
10℃〜240℃の範囲がより好ましい。反応源が25
0℃を超えて高い場合には、生成した一般式(It)で
示される化合物が重合または分解によシ消費され、また
原料であるシクロペンタジェンまたはシンクロペンタジ
ェンが重合するため、その損失が大となる。一方、反応
温度が200℃よシも低い場合には1反応速度が著しく
低下し、かつ目的とする一般式(■)で示される化合物
の収率が低下する。In the method of the present invention, the degree of reaction p has a large effect on the reaction rate p and the yield of the compound represented by the general formula (n). The reaction is carried out at a temperature ranging from 200<0>C to 250<0>C. The reaction temperature is preferably in the range of 200°C to 240°C, and 2
The range of 10°C to 240°C is more preferable. The reaction source is 25
If the temperature is higher than 0°C, the generated compound represented by the general formula (It) is consumed by polymerization or decomposition, and the raw material cyclopentadiene or synclopentadiene is polymerized, resulting in its loss. Becomes large. On the other hand, if the reaction temperature is lower than 200° C., the reaction rate will drop significantly and the yield of the target compound represented by the general formula (■) will drop.
シクロペンタジェンまたはシンクロペンタジェンと一般
式(1)で示される化合物との反応は溶媒の不存在下で
行うことも可能であるが、適当な反応溶媒の存在下で行
うのが一般式((1)で示される化合物の収率が良好と
なる点で好ましい。反応溶媒としてはベンゼン、トルエ
ン、キシレン等の芳香族炭化水素;ヘキサン、ヘプタン
等の脂肪族炭化水素;テトラヒドロフラン、1,4−ジ
オキサン等のエーテル;メタノール、エタノール、プロ
パノール、ブタノール等のアルコール:塩化メチレン、
クロロホルム等のハロゲン化炭化水素;N、N−ジメチ
ルホルムアミド、N−メチルピロリドン等ノ含窒素化合
物などが用いられるが、これらのうちで芳香族炭化水素
嘔よび脂肪族炭化水素が一般式(n)で示される化合物
の収率が良好となる点で好ましく、特に芳香族炭化水素
が好筐しい。反応溶媒は通常、全原料化合物に対して0
.1〜100重景倍の範囲の量で用いられる。反応溶媒
の使用量は全原料化合物に対して0.2〜50重量倍の
範囲が好筐しく、0.2〜10重量倍の範囲がより好!
しい。反応mtsの使用量が0.1重量倍より少ない場
合には、−紋穴(n)で示される化合物の収率が低下す
ることがあり、オたその使用量が100重量倍を超える
場合には1反応速度が低下することがあり、いずれの場
合も好普しくない。Although the reaction between cyclopentadiene or synclopentadiene and the compound represented by the general formula (1) can be carried out in the absence of a solvent, it is preferable to carry out the reaction in the presence of a suitable reaction solvent. It is preferable in that the yield of the compound shown in 1) is good.As the reaction solvent, aromatic hydrocarbons such as benzene, toluene and xylene; aliphatic hydrocarbons such as hexane and heptane; tetrahydrofuran and 1,4-dioxane. Ethers such as; alcohols such as methanol, ethanol, propanol, butanol; methylene chloride,
Halogenated hydrocarbons such as chloroform; nitrogen-containing compounds such as N,N-dimethylformamide and N-methylpyrrolidone are used; among these, aromatic hydrocarbons and aliphatic hydrocarbons are represented by the general formula (n). It is preferable in that the yield of the compound represented by is good, and aromatic hydrocarbons are particularly preferable. The reaction solvent is usually 0% for all raw material compounds.
.. It is used in amounts ranging from 1 to 100 magnifications. The amount of reaction solvent to be used is preferably in the range of 0.2 to 50 times the weight of the total raw material compounds, and more preferably in the range of 0.2 to 10 times the weight!
Yes. If the amount of reaction mts used is less than 0.1 times by weight, the yield of the compound indicated by -monya (n) may decrease, and if the amount used exceeds 100 times by weight, 1 reaction rate may decrease, and either case is unfavorable.
本発明の方法における反応は通常のディールス−アルダ
−反応の場合に準じて行うことができる。The reaction in the method of the present invention can be carried out in accordance with the usual Diels-Alder reaction.
すなわち、金属製または耐圧ガラス製の反応容器に一般
式(1)で示される化合物、シクロベンメジエンまたは
ジシクロペンタジェン、および必要に応じて適当な反応
溶媒を仕込み、所定のa度に加熱して反応させる。反応
は空気中で行うこともできるが、窒素、アルゴン、二酸
化炭素等の不活性ガス中で行う、のが好筐しい。また1
通常は機械的な攪拌を行うのがよい。なか、本発明の製
造方法の温度条件下ではジシクロペンタジェンは容易に
シクロペンタジェンに分解して反応することから。That is, a reaction vessel made of metal or pressure-resistant glass is charged with the compound represented by the general formula (1), cyclobenmediene or dicyclopentadiene, and an appropriate reaction solvent if necessary, and heated to a predetermined temperature of a degree. and react. Although the reaction can be carried out in air, it is preferably carried out in an inert gas such as nitrogen, argon or carbon dioxide. Also 1
Mechanical stirring is usually preferred. Among these, dicyclopentadiene easily decomposes into cyclopentadiene and reacts under the temperature conditions of the production method of the present invention.
必ずしもシクロペンタジェンを原料として用いる必要は
ない。反応終了後1反応混合物からの一般式1■>で示
される化合物の単離は1反応混合物を蒸留するか、′ま
たは使用する反応溶媒の種類によっては反応混合物から
析出する一般式(n)で示される化合物を濾別すること
により行われる。It is not necessarily necessary to use cyclopentadiene as a raw material. After completion of the reaction, the compound represented by the general formula 1■> can be isolated from the reaction mixture by distilling the reaction mixture, or by precipitating the compound represented by the general formula (n) from the reaction mixture depending on the type of reaction solvent used. This is done by filtering off the indicated compound.
本発明の方法によシ得られる一般式(U)で示される化
合物を二重結合の水添反応に付することによジベルヒド
ロ−1,4: 5.8−ジメタノナフタレン−2,3−
ジカルボン酸エステルが製造され、このベルヒドロ−1
,4:5.8−ジメタノナフタレン−2,3−ジカルボ
ン酸エステルをエステル部分の還元反応に付することに
よりベルヒドロ−1,4: 5゜8−ジメタノナフタレ
ン−2,3−ジメタノールが製造される。この場合、一
般式(II)で示される化合物を例えば、銅−クロム触
媒の存在下、加圧水素雰囲気中で反応させることによル
ベルヒドロ−1゜4二5.8−ジメタノナフタレン−2
,3−ジメタノールを直接製造することもできる。こう
して得られたベルヒドロ−1,4:5.8−ジメタノナ
フタレン−2,3−ジカルボン酸エステルtiはベルヒ
ドロ−1,4:5,8−ジメタノナフタレン−2,3−
ジメタノールは公知の方法に従って各種の構造材料。By subjecting the compound represented by the general formula (U) obtained by the method of the present invention to a double bond hydrogenation reaction, diberhydro-1,4: 5,8-dimethanonaphthalene-2,3-
A dicarboxylic acid ester is produced, and this perhydro-1
, 4:5.8-dimethanonaphthalene-2,3-dicarboxylic acid ester is subjected to a reduction reaction of the ester moiety to produce behydro-1,4:5゜8-dimethanonaphthalene-2,3-dimethanol. Manufactured. In this case, by reacting the compound represented by the general formula (II) in a pressurized hydrogen atmosphere in the presence of a copper-chromium catalyst, for example, rubberhydro-1°425.8-dimethanonaphthalene-2
, 3-dimethanol can also be produced directly. The thus obtained perhydro-1,4:5.8-dimethanonaphthalene-2,3-dicarboxylic acid ester ti is perhydro-1,4:5,8-dimethanonaphthalene-2,3-
Dimethanol is extracted into various structural materials according to known methods.
機能材料として有用なポリエステル、ポリカーボネート
またはポリエステルカーボネートに容易に誘導すること
ができる。筐た。一般式(■)で示される化合物はビニ
ル重合により単独重合体となり。It can be easily derived into polyester, polycarbonate or polyester carbonate useful as functional materials. It was a cabinet. The compound represented by the general formula (■) becomes a homopolymer through vinyl polymerization.
また二重結合を有する他の化合物1例えば無水マレイン
酸、酢酸ビニル、アクリロニトリル等と共重合体を形成
することも可能である。It is also possible to form a copolymer with other compounds having double bonds, such as maleic anhydride, vinyl acetate, acrylonitrile, etc.
以下、実施例により本発明を具体的に説明するが5本発
明はこれらの実施例によって何ら限定されるものではな
い。EXAMPLES Hereinafter, the present invention will be specifically explained with reference to Examples, but the present invention is not limited to these Examples in any way.
実施例1
電磁攪拌装置を備えた内容11のオートクレープニ7マ
ル酸ジプチル171f(0,75モル)。Example 1 Autoclaved diptyl 7malate 171f (0.75 mol) of content 11 with a magnetic stirrer.
ジシクロペンタジェン99ノ(0,75モル)&!ヒp
−キシレン300fを仕込み、窒素ガスで系内を置換し
た。次いで、オートクレーブの内温を230℃に昇温し
、同温度で攪拌下に2時間反応させた。この時点で定量
ポンプを用いてジシクロペンタジェン92f(0,70
モル)を30分かけて添加し、ここからさらに1時間3
0分反応させた。Dicyclopentadiene 99 (0.75 mol) &! hip
- 300f of xylene was charged and the system was replaced with nitrogen gas. Next, the internal temperature of the autoclave was raised to 230°C, and the mixture was reacted at the same temperature for 2 hours with stirring. At this point, using a metering pump, dicyclopentadiene 92f (0,70
mol) over 30 minutes, and then for an additional hour 3
It was allowed to react for 0 minutes.
反応終了後1反応混合液をガスクロマトグラフィーによ
り分析した結果、1.2.3.4.4a、 5.8.8
1!L−オクタヒドロ−1,4:5,8−ジメタノナフ
タレン−トランス−2,3−ジカルボン酸ジブチルが1
81を生成していることが確認された。この反応混合物
から減圧蒸留により、 1.2.3.4.4&、 5.
8.8a−オクタヒドロ−1,4二5,8−ジメタノナ
フタレン−トランス−2,3−ジカルボン酸ジブチル1
43tを得た。フマル酸ジプチルに基づく収率は53嘩
であった。After the completion of the reaction, the reaction mixture was analyzed by gas chromatography, and the results were as follows: 1.2.3.4.4a, 5.8.8
1! L-octahydro-1,4:5,8-dimethanonaphthalene-trans-2,3-dicarboxylic acid dibutyl is 1
It was confirmed that 81 was generated. From this reaction mixture, 1.2.3.4.4&, 5.
8.8a-octahydro-1,425,8-dimethanonaphthalene-trans-2,3-dicarboxylic acid dibutyl 1
43t was obtained. The yield based on diptyl fumarate was 53%.
実施例2
実施例1で用いたオートクレーブに7マル酸ジメチル1
08F(0,75モル)釦よびp−キシレン3002を
仕込み%窒素ガスで系内金置換した。Example 2 In the autoclave used in Example 1, 1 dimethyl 7 malate was added.
08F (0.75 mol) and p-xylene 3002 were charged and the gold in the system was replaced with nitrogen gas.
次いで、オートクレーブの内温を210℃に昇温し、攪
拌下で定量ポンプによりジシクロペンタジェン99F(
0,75モル)を1時間かけて添加したのち、1時間反
応させた。その後、再びジシクロペンタジェン50り(
0,38モル)を定量ポンプを用いて1時間かけて添加
し、1時間反応させた。Next, the internal temperature of the autoclave was raised to 210°C, and dicyclopentadiene 99F (
After adding 0.75 mol) over 1 hour, the mixture was reacted for 1 hour. After that, 50 ml of dicyclopentadiene (
0.38 mol) was added over 1 hour using a metering pump, and the mixture was reacted for 1 hour.
反応終了後、反応混合物をガスクロマトグラフィーによ
り分析した結果、1.2.3.4.4&、 5.8.8
&−オクタヒドロ−1,4:5.8−ジメタノナフタレ
ン−トランス−2,3−ジカルボン酸ジメチルが122
f生成していることが確認された。この反応混合物から
減圧蒸留により、1.2.3.4.4&、 5.8.8
a−オクタヒドロ−1,4:5,8−ジメタノナフタレ
ン−トランス−2,3−ジカルボン酸ジメチル103f
を得た。フマル酸ジメチルに基づく収率は50%であっ
た。After the reaction was completed, the reaction mixture was analyzed by gas chromatography, and the results were as follows: 1.2.3.4.4&, 5.8.8
&-octahydro-1,4:5.8-dimethanonaphthalene-trans-2,3-dicarboxylic acid dimethyl is 122
It was confirmed that f was being generated. From this reaction mixture, 1.2.3.4.4 &, 5.8.8
a-octahydro-1,4:5,8-dimethanonaphthalene-trans-2,3-dicarboxylic acid dimethyl 103f
I got it. The yield based on dimethyl fumarate was 50%.
実施例3
実施例1で用いたオートクレーブにマレイン酸ジエチル
129f(0,75モル)%シシクロベンタシェフ99
F(0,75モル)&!びp−キシレン300Fを仕込
み、窒素ガスで系内を置換した。Example 3 Diethyl maleate 129f (0.75 mol)% cyclobentashev 99 was added to the autoclave used in Example 1.
F (0,75 mol) &! and p-xylene 300F, and the system was purged with nitrogen gas.
次いで、オートクレーブの内温を220℃に昇温し、同
温度で攪拌下に2時間反応させた。その後。Next, the internal temperature of the autoclave was raised to 220°C, and the reaction was carried out at the same temperature for 2 hours with stirring. after that.
ジシクロペンタジェン30F(0,23モ/’)を定量
ポンプを用いて30分かけて添加し、1時間反応させた
。さらにジシクロペンタジェン2Qf(0,15モル)
を定量ポンプを用いて30分かけて添加し。Dicyclopentadiene 30F (0.23 mo/') was added over 30 minutes using a metering pump and reacted for 1 hour. Furthermore, dicyclopentadiene 2Qf (0.15 mol)
was added over 30 minutes using a metering pump.
1時間30分反応させた。反応終了後1反応混合物をガ
スクロマトグラフィーにより分析した結果。The reaction was carried out for 1 hour and 30 minutes. Results of analyzing one reaction mixture by gas chromatography after the completion of the reaction.
1、2.3.4.4a、 5.8.8a−オクタヒドロ
−1,4:5,8−シメタノナフタレンーシス−2,3
−ジカルボン酸ジエチルが1122生成していることが
確認された。な釦、同時に1.2.3.4.4a、 5
.8. ga −オクタヒドロ−1,4:5.8−ジメ
タノナフタレン−トランス−2,3−ジカルボン酸ジエ
チルが13f生成していることが認められた。この反応
混合物から減圧蒸留によシs 1+ 2+ 3+ 4+
48. り、 s、 sa−オクタヒドロ−1,4:
5.8−ジメタノナフタレン−シス−2,3−ジカルボ
ン酸ジエチル94fを得た。マレイン酸ジメチルに基づ
く収率は41%であった。1, 2.3.4.4a, 5.8.8a-octahydro-1,4:5,8-simethanonaphthalenesis-2,3
It was confirmed that 1122 diethyl dicarboxylates were produced. buttons, 1.2.3.4.4a, 5 at the same time
.. 8. It was observed that 13f of diethyl ga-octahydro-1,4:5.8-dimethanonaphthalene-trans-2,3-dicarboxylate was produced. This reaction mixture is distilled under reduced pressure. s 1+ 2+ 3+ 4+
48. ri, s, sa-octahydro-1,4:
Diethyl 5.8-dimethanonaphthalene-cis-2,3-dicarboxylate 94f was obtained. Yield based on dimethyl maleate was 41%.
比較例1
実施例1で用いたオートクレーブにフマル酸ジメチル1
08f(0,75モル)、シンクロペンタジェン189
F(1,43モル)pよびp−キシレン300Fを仕込
み、窒素ガスで系内を置換した。Comparative Example 1 Dimethyl fumarate 1 was added to the autoclave used in Example 1.
08f (0.75 mol), synchropentadiene 189
F (1,43 mol) p and p-xylene 300F were charged, and the system was purged with nitrogen gas.
次いで、オートクレーブの内温を180℃に昇温し、同
温度で攪拌下に4時間反応させた。反応終了後1反応混
合液を減圧蒸留に付すことにより、1、2.3.4.4
B、 5.8.88−オクタヒトl:’−1,4:5,
8−ジメタノナフタレン−トランス−2,3−)hルー
ボン酸ジメチル14tを得た。フマル酸ジメチルに基づ
く収率は7多であった。なお1反応時間を24時間にす
る以外は上記と同様にして反応によび蒸留を実施したと
ころ、この場合のフマル酸ジメチルに基づ(1,2,3
,4,4&、 5.8.8a−オクタヒドロ−1,4:
5.8−ジメタノナフタレン−トランス−2,3−ジ
カルボン酸ジメチルの収率は25%であった。Next, the internal temperature of the autoclave was raised to 180°C, and the reaction was carried out at the same temperature for 4 hours with stirring. After the reaction is completed, 1, 2.3.4.4 is obtained by subjecting the reaction mixture to vacuum distillation.
B, 5.8.88-octahito l:'-1,4:5,
14 t of dimethyl 8-dimethanonaphthalene-trans-2,3-)h rubonate was obtained. The yield based on dimethyl fumarate was 7.5%. The reaction and distillation were carried out in the same manner as above except that one reaction time was 24 hours. Based on dimethyl fumarate in this case, (1, 2, 3
,4,4&,5.8.8a-octahydro-1,4:
The yield of dimethyl 5.8-dimethanonaphthalene-trans-2,3-dicarboxylate was 25%.
参考クリ
実施例1で用いたオートクレーブに、実施例1で得られ
た1、 2.3.4.4&、 5.8.8&−オクタヒ
ドロ−1,4:5.8−ジメタノナフタレン−トランス
−2゜3−ジカルボン酸ジプチル40’、1.4−ジオ
キサン400dおよび銅−クロム触媒21を仕込み。1, 2.3.4.4&, 5.8.8&-octahydro-1,4:5.8-dimethanonaphthalene-trans- obtained in Example 1 was placed in the autoclave used in Reference Example 1. Diptyl 2°3-dicarboxylate 40', 1,4-dioxane 400d and copper-chromium catalyst 21 were charged.
万円を水素ガスで十分置換したのち、水素ガスを250
気圧仕込み、200℃で24時間攪拌した。After fully replacing 10,000 yen with hydrogen gas, replace 250 yen with hydrogen gas.
The mixture was charged at atmospheric pressure and stirred at 200°C for 24 hours.
冷却後、反応液を取り出し、触媒を濾別したのち。After cooling, the reaction solution was taken out and the catalyst was filtered off.
1.4−ジオキサンを除去した。残漬をアセトンより再
結晶することにより、白色結晶15ft−得た。1.4-Dioxane was removed. The residue was recrystallized from acetone to obtain 15 ft of white crystals.
得られた結晶のIH−NMRスペクトルは次の通りであ
り、この結晶はベルヒドロ−1,4:5,8−ジメタノ
ナフタレン−トランス−2,3−ジメタノールであるこ
とが確かめられた。The IH-NMR spectrum of the obtained crystal was as follows, and it was confirmed that this crystal was berhydro-1,4:5,8-dimethanonaphthalene-trans-2,3-dimethanol.
0.8〜2.0 ppm: 12H
2,0〜2.3ppm: 4H(ノルボルナン骨格橋
頭位のプロトン)
3、0〜3.8 ppm : 6 H(酸素原子に結
合t、、*メチレン基のプロトン訃よび
水酸基のプロトン)
〔発明の効果〕
不発明の方法によれば、従来提案されている方法に比し
て短い反応時間でかつ良好な収率で1.2゜3、4.4
.a、 5.8.8a−オクタヒトI:I−1.4:5
.8−ジメタノナフタレン−2,3−ジカルボン酸エス
テルが製造される。0.8-2.0 ppm: 12H 2,0-2.3 ppm: 4H (proton at the bridgehead position of the norbornane skeleton) 3,0-3.8 ppm: 6 H (bond t to the oxygen atom, *of the methylene group) [Effects of the Invention] According to the uninvented method, the reaction time was shorter and the yield was better than that of the conventionally proposed method.
.. a, 5.8.8a-octahuman I:I-1.4:5
.. 8-dimethanonaphthalene-2,3-dicarboxylic acid ester is produced.
Claims (1)
、R^1およびR^2はぞれぞれアルキル基を表す。)
で示される化合物とシクロペンタジエンまたはシンクロ
ペンタジエンを反応させるに際し、反応温度を200℃
〜250℃の範囲内に保ち、該シクロペンタジエンまた
はシンクロペンタジエンをシクロペンタジエンに換算し
た量で一般式( I )で示される化合物に対して最終的
に2モル倍以上の量となるように断続的または連続的に
反応系に仕込むことを特徴とする下記一般式(II) ▲数式、化学式、表等があります▼ (式中、R^1およびR^2は上記に定義したとおりで
ある。) で示される化合物の製造方法。[Claims] The following general formula (I) R^OOC-CH=CH-COOR^2 (I) (In the formula, R^1 and R^2 each represent an alkyl group.)
When reacting the compound represented by cyclopentadiene or synchlopentadiene, the reaction temperature is set at 200°C.
The temperature is maintained within a range of ~250°C, and the cyclopentadiene or syncropentadiene is intermittently heated in an amount equivalent to cyclopentadiene so that the final amount is at least 2 times the mole of the compound represented by general formula (I). Or the following general formula (II), which is characterized by being continuously charged into the reaction system ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (In the formula, R^1 and R^2 are as defined above.) A method for producing a compound represented by
Priority Applications (1)
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---|---|---|---|
JP20550889A JP2733325B2 (en) | 1989-08-07 | 1989-08-07 | Method for producing octahydrodimethanonaphthalene ring-containing compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20550889A JP2733325B2 (en) | 1989-08-07 | 1989-08-07 | Method for producing octahydrodimethanonaphthalene ring-containing compound |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0368538A true JPH0368538A (en) | 1991-03-25 |
JP2733325B2 JP2733325B2 (en) | 1998-03-30 |
Family
ID=16508027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20550889A Expired - Lifetime JP2733325B2 (en) | 1989-08-07 | 1989-08-07 | Method for producing octahydrodimethanonaphthalene ring-containing compound |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2733325B2 (en) |
-
1989
- 1989-08-07 JP JP20550889A patent/JP2733325B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
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JP2733325B2 (en) | 1998-03-30 |
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