JPS5817173B2 - Method for producing tricyclo(5.2.1.0↑2'↑6)-3-decene-8 (or 9)ol - Google Patents
Method for producing tricyclo(5.2.1.0↑2'↑6)-3-decene-8 (or 9)olInfo
- Publication number
- JPS5817173B2 JPS5817173B2 JP4064780A JP4064780A JPS5817173B2 JP S5817173 B2 JPS5817173 B2 JP S5817173B2 JP 4064780 A JP4064780 A JP 4064780A JP 4064780 A JP4064780 A JP 4064780A JP S5817173 B2 JPS5817173 B2 JP S5817173B2
- Authority
- JP
- Japan
- Prior art keywords
- dicyclopentadiene
- oxygen
- amount
- hydroxylated
- distillation
- 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.)
- Expired
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 20
- 239000001301 oxygen Substances 0.000 claims description 20
- 229910052760 oxygen Inorganic materials 0.000 claims description 20
- 238000004821 distillation Methods 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 6
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical class C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 description 28
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 6
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000004042 decolorization Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000006703 hydration reaction Methods 0.000 description 4
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000001577 simple distillation Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 238000005886 esterification reaction Methods 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000005698 Diels-Alder reaction Methods 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 229920001429 chelating resin Polymers 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical class C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000000887 hydrating effect Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 125000001174 sulfone group Chemical group 0.000 description 1
- 229920006337 unsaturated polyester resin Polymers 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明は精製されたトリシクロ(5,2,1,02j6
)−3−デセン−8(または9)オールの製造法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention provides purified tricyclo(5,2,1,02j6
)-3-Decene-8 (or 9)ol.
トリシクロ(5,2,1,02j6) −3−デセン−
8(または9)オール(以下これをヒドロキシル化ジシ
クロペンタジェンと言う。Tricyclo(5,2,1,02j6) -3-decene-
8 (or 9)ol (hereinafter referred to as hydroxylated dicyclopentadiene).
)は、不飽和ポリエステル樹脂を始めとし、その他各種
樹脂、香料、樹脂安定剤または可塑剤の原料として有用
なものである。) is useful as a raw material for unsaturated polyester resins as well as various other resins, perfumes, resin stabilizers, and plasticizers.
このヒドロキシル化ジシクロペンタジェンは鉱酸あるい
はカチオン交換樹脂などの酸性触媒を使用して、ジシク
ロペンタジェンの水和反応によって製造される。This hydroxylated dicyclopentadiene is produced by a hydration reaction of dicyclopentadiene using an acidic catalyst such as a mineral acid or a cation exchange resin.
このようにして得られたヒドロキシル化ジシクロペンタ
ジェンは黄色ないし黄褐色に着色しており、蒸留精製時
に空気を除去し、熱履歴を短くして注意深く蒸留操作を
行なっても未だ黄色ないしは黄褐色に着色している。The hydroxylated dicyclopentadiene obtained in this way is colored yellow to yellowish brown, and even if air is removed during distillation purification, the thermal history is shortened, and distillation is carried out carefully, the color remains yellow or yellowish brown. It is colored in.
ゆえに、その用途は極めて限られていた。Therefore, its use was extremely limited.
特公昭47−39106号公報によれば着色の原因は原
料ジシクロペンクジエン中の微量の不純物(メチルジシ
クロペンクジエン)によるもので、製品ヒドロキシル化
ジシクロペンタジェンの脱色方法として次の方法が提案
されていた。According to Japanese Patent Publication No. 47-39106, the cause of the coloring is due to a trace amount of impurity (methyldicyclopencdiene) in the raw material dicyclopencdiene, and the following method is used to decolorize the product hydroxylated dicyclopentadiene. It had been proposed.
すなわち、着色したヒドロキシ化ジシクロペンタジェン
にディールス・アルダ−反応の際にジェノフィルとして
作用する化合物、例えば無水マレイン酸あるいはp−ベ
ンゾキノンを添加混合したのち蒸留する方法である。That is, a compound that acts as a genophile during the Diels-Alder reaction, such as maleic anhydride or p-benzoquinone, is added to and mixed with colored hydroxylated dicyclopentadiene, and then distilled.
この方法は確かに製品の脱色に対して効果があるが、経
済的な方法ではない。Although this method is certainly effective for decolorizing products, it is not an economical method.
すなわち、無水マレイン酸の場合ヒドロキシル化ジシク
ロペンタジェンに対して2重素条を添加し、加熱攪拌後
蒸留することによってハーゼン色相で10〜20の製品
が得られるが、蒸留残渣が13%程度と多量に生成する
ために製品のロスが著しい。That is, in the case of maleic anhydride, a product with a Hazen hue of 10 to 20 can be obtained by adding double hydrogen to hydroxylated dicyclopentadiene, heating and stirring, and then distilling it, but the distillation residue is about 13%. Because large quantities are produced, product loss is significant.
これは無水マレイン酸が単に脱色に使用される以外にヒ
ドロキシル化ジシクロペンタジェンが無水マレイン酸と
エステル化反応を起こしたためと考えられる。This is thought to be because maleic anhydride is not only used for decolorization, but also because hydroxylated dicyclopentadiene undergoes an esterification reaction with maleic anhydride.
また、エステル化反応を起こさないp−ベンゾキノンを
使用した場合も脱色が可能であり、無水マレイン酸の場
合に比べて蒸留残渣量も少ない。Further, decolorization is also possible when p-benzoquinone, which does not cause an esterification reaction, is used, and the amount of distillation residue is smaller than when maleic anhydride is used.
しかし、p−ベンゾキノンは高価な試薬であり汎用でな
く、工業的には利用しがたいものである。However, p-benzoquinone is an expensive reagent, is not commonly used, and is difficult to use industrially.
本発明は、このような問題点を解決するものであり、従
来と異なる新規な方法を提供するものである。The present invention solves these problems and provides a novel method different from the conventional method.
すなわち、本発明はジシクロペンタジェンを酸性触媒の
存在下に水利反応させて得られる粗製ヒドロキシル化ジ
シクロペンタジェンを130〜220℃の温度下に酸素
または酸素含有気体と接触させたのち蒸留することを特
徴とする精製ヒドロキシル化ジシクロペンタジェンの製
造法に関する。That is, in the present invention, crude hydroxylated dicyclopentadiene obtained by subjecting dicyclopentadiene to a water conservation reaction in the presence of an acidic catalyst is brought into contact with oxygen or an oxygen-containing gas at a temperature of 130 to 220°C, and then distilled. The present invention relates to a method for producing purified hydroxylated dicyclopentadiene, which is characterized by the following.
上記ジシクロペンタジェンを酸性触媒の存在下に水和反
応させて得られる粗製ヒドロキシル化ジシクロペンタジ
ェンとは、水和反応後、水層と分離した油層またはこの
油層を蒸留して得られたヒドロキシル化ジシクロペンタ
ジェン留分てあり、これは前述したとおり黄色または黄
褐色に着色しているものである。The crude hydroxylated dicyclopentadiene obtained by hydrating the above dicyclopentadiene in the presence of an acidic catalyst is the oil layer separated from the water layer after the hydration reaction, or the oil layer obtained by distilling this oil layer. There is a hydroxylated dicyclopentadiene fraction, which is colored yellow or tan as described above.
あるいは蒸留後において無色透明の場合であっても貯蔵
中に黄色または黄褐色に着色してしまう。Alternatively, even if it is colorless and transparent after distillation, it will turn yellow or yellowish brown during storage.
上記粗製ヒドロキシル化ジシクロペンタジェンは、通常
ジシクロペンタジェンを酸性触媒例えば硫酸またはイオ
ン交換樹脂の存在下80〜120℃の温度で水和反応さ
せることによって得られる。The above-mentioned crude hydroxylated dicyclopentadiene is usually obtained by subjecting dicyclopentadiene to a hydration reaction in the presence of an acidic catalyst such as sulfuric acid or an ion exchange resin at a temperature of 80 to 120°C.
この粗製ヒドロキシル化ジシクロペンタジェンは、常識
的には空気を除去し、真空で蒸留して精製されるが、本
発明はまったく逆に酸素または酸素含有気体と接触させ
たのち蒸留す・るだけでなく、蒸留中にも、酸素または
酸素含有気体と接触させテモよい。Conventionally, this crude hydroxylated dicyclopentadiene is purified by removing air and distilling it in a vacuum, but in the present invention, the crude hydroxylated dicyclopentadiene is purified by simply distilling it after contacting it with oxygen or an oxygen-containing gas. However, during distillation, it may be brought into contact with oxygen or an oxygen-containing gas.
即ち、粗製ヒドロキシル化ジシクロペンタジェンを13
0〜220°Cに加熱攪拌した状態にし、これに酸素ま
たは酸素含有気体を吹込み接触させる。That is, 13 crude hydroxylated dicyclopentadiene
The mixture is heated and stirred at 0 to 220°C, and oxygen or an oxygen-containing gas is blown into the mixture.
この時の酸素または酸素含有気体の量は酸素量で試料1
1に対して0.021/、−以上、好ましくは0.1〜
i i 7yyinであり、接触させる時間は上記二つ
の条件によって変化するが通常は0.5〜10時間であ
る。The amount of oxygen or oxygen-containing gas at this time is the amount of oxygen in sample 1.
0.021/- or more, preferably 0.1 to 1
The contact time varies depending on the above two conditions, but is usually 0.5 to 10 hours.
このように加熱空気処理した試料を単蒸留することによ
って、ガードナー色相1の実質上無色透明であり、貯蔵
中にも着色しないヒドロキシル化ジシクロペンタジェン
が得られる。By simple distillation of the sample treated with heated air in this way, hydroxylated dicyclopentadiene is obtained which is substantially colorless and transparent and has a Gardner hue of 1 and does not become colored during storage.
この時の蒸留残渣量は3〜4重量係素条る。The amount of distillation residue at this time is 3 to 4 weight factors.
上記の温度、酸素量及び処理時間の範囲設定の理由は、
次のとおりである。The reason for setting the above temperature, oxygen amount, and treatment time ranges is as follows.
It is as follows.
温度に関しては、100℃未満であると、接触時間を長
く取らなければ無色透明の製品が得られないこと、また
250°Cを越えると蒸留残渣が著しく多くなることか
ら、温度は100°C〜250℃、好ましくは130°
C〜220℃の範囲である。Regarding the temperature, if it is less than 100°C, a colorless and transparent product cannot be obtained unless the contact time is long, and if it exceeds 250°C, there will be a significant amount of distillation residue, so the temperature should be between 100°C and above. 250°C, preferably 130°
It is in the range of C to 220C.
次に、酸素量に関しても温度の場合と同様に、空気量が
試料11に対して0.021/*’n未満となると、接
触時間が長くなる。Next, regarding the amount of oxygen, as in the case of temperature, when the amount of air is less than 0.021/*'n with respect to the sample 11, the contact time becomes longer.
逆に多すぎるとなると、蒸留残渣量が増大する。On the other hand, if it is too large, the amount of distillation residue will increase.
好ましい酸素量の範囲は試料llに対して0.1〜11
/−である。The preferred range of oxygen amount is 0.1 to 11 per liter of sample.
/-.
接触させる時間に関しては、上記の温度、酸素量によっ
て決まる。The contact time is determined by the above temperature and oxygen amount.
即ち、加熱温度が高く、酸素量が多い場合は、残渣量の
増大を抑えるため接触時間は短くなり、温度が低く、酸
素量も少ない場合は、接触時間を長く取って脱色を進め
るが、通常は0.5〜10時間である。In other words, when the heating temperature is high and the amount of oxygen is high, the contact time is shortened to suppress the increase in the amount of residue, and when the temperature is low and the amount of oxygen is low, the contact time is increased to proceed with decolorization, but normally is 0.5 to 10 hours.
以下、実施例及び比較例によってより詳細に述べる。Hereinafter, it will be described in more detail with reference to Examples and Comparative Examples.
実施例 1
ジシクロペンタジェンをスルホン基を有するイオン交換
樹脂〔ロームアンドバース製、アンバーライトIR−2
0003の存在下、水和反応させたのち、ただちに減圧
蒸留して、ヒト’oキシル化ジシクロペンタジェン留分
を採取した。Example 1 Ion exchange resin containing dicyclopentadiene and sulfone group [manufactured by Rohm & Birth, Amberlite IR-2]
After a hydration reaction in the presence of 0003, the mixture was immediately distilled under reduced pressure to collect a human'oxylated dicyclopentadiene fraction.
得られた粗製ヒドロキシル化ジシクロペンタジェンは黄
褐色(ガードナー色相6)に着していた。The crude hydroxylated dicyclopentadiene obtained had a tan color (Gardner hue 6).
コノ黄褐色に着色した粗製ヒドロキシル化ジシクロペン
タジェン300CC(320iを還流冷却管を付けた四
ツロフラスコに入れ攪拌しながら、オイルバスで加熱す
る。Crude hydroxylated dicyclopentadiene 300CC (320i) colored yellowish brown is placed in a four-way flask equipped with a reflux condenser and heated in an oil bath while stirring.
試料が200°Cに達した時点で、シリカゲルの筒を通
して乾燥させた空気を60 (Iff/111tかの速
度で試料中に吹込み、加熱攪拌を2時間続ける。When the temperature of the sample reaches 200°C, dry air is blown into the sample through a silica gel cylinder at a rate of 60 (Iff/111t), and heating and stirring are continued for 2 hours.
反応液は暗赤色に変化した。この試料をクライゼン形の
連結管を付けたフラスコで4〜5MHg(この時のオイ
ルパス温度は125℃)で減圧蒸留し、留出液を集めた
ところ、液は無色透明の粘性液体(ヒドロキシル化ジシ
クロペンタジェン)で得量は、316.2.Fであった
。The reaction solution turned dark red. This sample was distilled under reduced pressure at 4 to 5 MHg (the oil path temperature at this time was 125°C) in a flask equipped with a Claisen-type connecting tube. When the distillate was collected, the liquid was a colorless and transparent viscous liquid (hydroxylated dicyclopentadiene), the yield was 316.2. It was F.
このものの着色度はガードナー色相で1、ハーゼン色相
で30であった。The coloring degree of this product was 1 in Gardner hue and 30 in Hazen hue.
また、蒸留の残渣は12.9gであった。Moreover, the residue from the distillation was 12.9 g.
従って残渣割合い(残渣量/仕込量)は4.0%であっ
た。Therefore, the residue ratio (residue amount/charged amount) was 4.0%.
得られた精製ヒドロキシル化ジシクロペンタジェンは実
質的に無色であり、長期間保存しても着色しなかった。The purified hydroxylated dicyclopentadiene obtained was virtually colorless and did not become colored even after long-term storage.
実施例2〜3および比較例1〜2
実施例1に準じて実施例1の試料(粗製ヒドロキシル化
シクロペンタジェン)および装置を使用し、温度及び空
気量を変えて行なった。Examples 2 to 3 and Comparative Examples 1 to 2 Experiments were carried out in the same manner as in Example 1, using the sample (crude hydroxylated cyclopentadiene) and apparatus, and varying the temperature and amount of air.
表にその時の処理条件及び結果を示した。The treatment conditions and results are shown in the table.
比較例 3
実施例1で用いた試料を、加熱及び空気接触す・ること
なしに、単にクライゼン形のフラスコで単蒸留した結果
を表に示した。Comparative Example 3 The sample used in Example 1 was subjected to simple distillation in a Claisen-type flask without heating or contact with air, and the results are shown in the table.
比較例 4
実施例1で用いた試料を、150°Cで2時間加熱し、
この間空気の代りに窒素を実施例1と同量吹込んだ結果
を示した。Comparative Example 4 The sample used in Example 1 was heated at 150°C for 2 hours,
The results are shown in which the same amount of nitrogen as in Example 1 was blown in instead of air during this time.
以上より明らかなように、単蒸留あるいは加熱窒素処理
ではほとんど脱色されていないが、酸素と接触させるこ
とによって実質的に無色透明のヒドロキシル化ジシクロ
ペンタジェンが得られ、この時の蒸留残渣量は少量に抑
えることができる。As is clear from the above, there is almost no decolorization in simple distillation or heated nitrogen treatment, but substantially colorless and transparent hydroxylated dicyclopentadiene can be obtained by contacting it with oxygen, and the amount of distillation residue at this time is It can be kept to a small amount.
本発明による方法によって、安価に無色透明のヒドロキ
シル化ジシクロペンタジェンの製造が可能となった。By the method according to the present invention, it has become possible to produce colorless and transparent hydroxylated dicyclopentadiene at low cost.
Claims (1)
応させて得られる粗製トリシクロ(5,2,1゜()2
,6) 3−デセン−8(または9)オールを130
〜220°Cの温度下に、酸素または酸素含有気体と接
触させたのち蒸留することを特徴とする精製トリシクロ
(5,2,1,02j6)−3−デセン−8(またはり
)オールの製造法。1 Crude tricyclo(5,2,1°()2
,6) 3-decene-8 (or 9)ol at 130
Production of purified tricyclo(5,2,1,02j6)-3-decen-8(or)ol, characterized by distillation after contact with oxygen or an oxygen-containing gas at a temperature of ~220°C Law.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4064780A JPS5817173B2 (en) | 1980-03-28 | 1980-03-28 | Method for producing tricyclo(5.2.1.0↑2'↑6)-3-decene-8 (or 9)ol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4064780A JPS5817173B2 (en) | 1980-03-28 | 1980-03-28 | Method for producing tricyclo(5.2.1.0↑2'↑6)-3-decene-8 (or 9)ol |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56138132A JPS56138132A (en) | 1981-10-28 |
| JPS5817173B2 true JPS5817173B2 (en) | 1983-04-05 |
Family
ID=12586342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4064780A Expired JPS5817173B2 (en) | 1980-03-28 | 1980-03-28 | Method for producing tricyclo(5.2.1.0↑2'↑6)-3-decene-8 (or 9)ol |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5817173B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6255465U (en) * | 1985-09-26 | 1987-04-06 |
-
1980
- 1980-03-28 JP JP4064780A patent/JPS5817173B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6255465U (en) * | 1985-09-26 | 1987-04-06 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56138132A (en) | 1981-10-28 |
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