JPS6039275B2 - Method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-ol - Google Patents
Method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-olInfo
- Publication number
- JPS6039275B2 JPS6039275B2 JP2930177A JP2930177A JPS6039275B2 JP S6039275 B2 JPS6039275 B2 JP S6039275B2 JP 2930177 A JP2930177 A JP 2930177A JP 2930177 A JP2930177 A JP 2930177A JP S6039275 B2 JPS6039275 B2 JP S6039275B2
- Authority
- JP
- Japan
- Prior art keywords
- ttph
- tetramethyltetrahydropyran
- crude
- purifying
- acetone
- 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
Landscapes
- Pyrane Compounds (AREA)
Description
【発明の詳細な説明】
本発明は、2,2,6,6−テトラメチルテトラヒドロ
ピラン−4ーオールの精製方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-ol.
式
で示される2,2,6,6ーテトラメチルテトラヒドロ
ピランー4ーオール(以後、TTPHと略称する)は、
融点約85〜8がCの化合物で、有機合成原料や高沸点
溶剤などに有用な化合物である。2,2,6,6-tetramethyltetrahydropyran-4-ol (hereinafter abbreviated as TTPH) represented by the formula:
It is a C compound with a melting point of about 85 to 8, and is a compound useful as a raw material for organic synthesis and a high boiling point solvent.
TTPHは、アセトンのアルドール縮合、それに次ぐ脱
水さらに水素添加の工程を経て製造することが可能であ
る。例えば、アセトンのァルドール縮合につてトリアセ
トンジアルコールを合成し、次いで脱水塚化によって2
,2,6,6−テトラメチルテトラヒドロピランー4ー
オン(以後、TTPKと略称する)を合成し、これを水
素添加することによってTTPHを製造する方法、アセ
トンの縮合、脱水によってホロンを製造し、次いで水和
と環化を行わせてTTPKを合成し、同様の水素添加に
よってTTPHとする方法などがある。又、上記何れの
反応を経るか明確でないが、アセトンの縮合、脱水およ
び水素添加によってメチルィソブチルケトン(MIBK
)やメチルイソブチルビノール(MIBC)を製造する
場合にも副生物としてTTPH又はTTPKが得られる
ので、TTPKは同様に水素添加することによってTT
PHとすることができる。このような方法によて製造さ
れるTTPHは、通常不純物を含む形で得られるので、
用途によっては一層純度を高める必要がある。TTPH can be produced through aldol condensation of acetone, followed by dehydration and hydrogenation. For example, triacetone dialcohol is synthesized by aldol condensation of acetone, and then 2
, 2,6,6-tetramethyltetrahydropyran-4-one (hereinafter abbreviated as TTPK), a method for producing TTPH by hydrogenating it, a method for producing holon by condensation of acetone, dehydration, There is a method in which TTPK is then synthesized by hydration and cyclization, and TTPH is produced by similar hydrogenation. Although it is not clear which of the above reactions takes place, methyl isobutyl ketone (MIBK
) and methylisobutylvinol (MIBC), TTPH or TTPK is obtained as a by-product, so TTPK can be converted to TTPH by hydrogenating in the same way.
It can be PH. TTPH produced by such a method is usually obtained in a form containing impurities, so
Depending on the application, it may be necessary to further increase the purity.
本発明者らは前記粗TTPHの精製方法について鋭意研
究した結果、炭化水素溶媒を用いる再結晶法を見出すに
至った。すなわち本発明は、アセトンの縮合、脱水およ
び水素添加によって得られる粗TTPHを、炭化水素溶
媒を用いて再結晶を行うことを特徴とするTTPHの精
製方法である。本発明において用いられる再結晶溶媒は
、炭化水素溶媒であり、好適には炭素数5なし、し12
のものである。The inventors of the present invention conducted intensive research on the method for purifying the crude TTPH, and as a result, discovered a recrystallization method using a hydrocarbon solvent. That is, the present invention is a method for purifying TTPH, which is characterized by recrystallizing crude TTPH obtained by condensation, dehydration, and hydrogenation of acetone using a hydrocarbon solvent. The recrystallization solvent used in the present invention is a hydrocarbon solvent, preferably having 5 carbon atoms, 12 carbon atoms, and 12 carbon atoms.
belongs to.
具体的には、nーベンタン、nーヘキサン、イソヘキサ
ン、n−へブタン、nーオクタン、ィソオクタン、nー
デカン、灯油などの脂肪族炭化水素、シクロベンタン、
シクロヘキサンのような脂環族炭化水素、ベンゼン、ト
ルェン、キシレソのような芳香族炭化水素を例示するこ
とができる。これら再結晶溶剤は、単一化合物である必
要はなく、2種以上の混合物であってもよい。また、少
量であれば他の有機溶剤を含んでいてもよい。これらの
中で特に好ましいものは脂肪族炭化水素である。本発明
の原料として用いられる粗TTPH‘ま、前記したよう
にアセトンの縮合、脱水、水素添加の工程を経て製造さ
れるもので、通常、純度約80%以上、好ましくは約9
0%以上で、不純物としてTTPKその他のアセトン議
導体を含んでいる。Specifically, aliphatic hydrocarbons such as n-bentane, n-hexane, isohexane, n-hebutane, n-octane, isooctane, n-decane, kerosene, cyclobentane,
Examples include alicyclic hydrocarbons such as cyclohexane, and aromatic hydrocarbons such as benzene, toluene, and xylene. These recrystallization solvents do not need to be a single compound, and may be a mixture of two or more. In addition, other organic solvents may be included as long as they are in small amounts. Particularly preferred among these are aliphatic hydrocarbons. The crude TTPH' used as the raw material of the present invention is produced through the steps of condensation of acetone, dehydration, and hydrogenation as described above, and usually has a purity of about 80% or more, preferably about 9.
At 0% or more, it contains TTPK and other acetone conductors as impurities.
粗TTPHの再結晶に際して、溶媒の使用量は、粗TT
PHの熔解させる温度や溶媒の種類によって異なるが、
一般には、溶媒100のと当り、TTPHを5なし、し
5雌程度用い、30なし、し100oo程度の温度で溶
解させた後、一20ないし十30午0程度に冷却させる
方法が採用される。晶出の方法として、所定温度に保た
れた結晶晶出槽に、粗TTPH溶液を連続的に供給し、
その一方でスラリーを結晶晶出槽から連続的に排出させ
る連続法、結晶晶出槽に粗TTPH溶液を仕込んだ後冷
却してTTPHを晶出させる回分法、あるいはこれらの
変形方式を採用することができる。結晶を単離するには
、炉過や遠心分離など通常の結晶分離方法として採用さ
れている方法を用いることができる。必要に応じ、再結
晶操作を2回以上行ってもよい。本発明によれば、TT
PHの回収率が非常に高く、かつ高純度品を容易に得る
ことができる。実施例 1
アセトンの縮合、脱水および水素添加の工程を経てMI
BKを主成分とする反応混合物を得た。When recrystallizing crude TTPH, the amount of solvent used is
The pH varies depending on the melting temperature and type of solvent, but
In general, a method is adopted in which TTPH is dissolved at a temperature of about 100°C to 100°C per 100°C of solvent, and then cooled to about 120° to 130°C. . As a crystallization method, a crude TTPH solution is continuously supplied to a crystallization tank maintained at a predetermined temperature,
On the other hand, a continuous method in which the slurry is continuously discharged from the crystallization tank, a batch method in which the crude TTPH solution is charged into the crystallization tank and then cooled to crystallize TTPH, or a modified method thereof may be adopted. I can do it. In order to isolate the crystals, methods employed as ordinary crystal separation methods such as filtration and centrifugation can be used. If necessary, the recrystallization operation may be performed two or more times. According to the invention, T.T.
The recovery rate of PH is very high, and high purity products can be easily obtained. Example 1 MI through the steps of acetone condensation, dehydration and hydrogenation
A reaction mixture containing BK as a main component was obtained.
MIBKを蒸留除去したものを水素添加したのち、ジィ
ソブチルケトンおよびそれより低沸点物を蒸留除去した
。残留物を冷却し、析出した結晶を炉週により採取して
純度92.8%の粗TTPHを得た。三井へキサン(三
井石油化学社製)100私に、上記粗TTPH9.暖を
加え50つ0で溶解した後、0℃まで冷却し結晶を得た
。ガラスフィルターで炉過し減圧乾燥することによって
純度99.9%の精製TTPH4.7gを得た (富虫
点85.1℃)。実施例 2シクロヘキサン100叫に
、実施例1で用いた粗TTPH40gを加え50こ0で
溶解した後、2000まで冷却した。After MIBK was distilled off, the mixture was hydrogenated, and diisobutyl ketone and lower boiling point substances were distilled off. The residue was cooled, and the precipitated crystals were collected in a furnace to obtain crude TTPH with a purity of 92.8%. Mitsui Hexane (manufactured by Mitsui Petrochemical Co., Ltd.) 100, and the above crude TTPH9. After heating to dissolve at 50° C., the mixture was cooled to 0° C. to obtain crystals. By filtering through a glass filter and drying under reduced pressure, 4.7 g of purified TTPH with a purity of 99.9% was obtained (Fumushi point: 85.1°C). Example 2 40 g of crude TTPH used in Example 1 was added to 100 g of cyclohexane, dissolved at 50 g, and then cooled to 2000 g.
Claims (1)
れる粗2,2,6,6−テトラメチルテトラヒドロピラ
ン−4−オールを炭化水素溶媒を用いて再結晶を行うこ
とを特徴とする2,2,6,6−テトラメチルテトラヒ
ドロピラン−4−オールの精製方法。 2 炭化水素溶媒として、炭素数5ないし12のものを
用いる特許請求の範囲1記載の方法。 3 炭化水素溶媒として、脂肪族炭化水素を用いる特許
請求の範囲1又は2記載の方法。[Claims] 1. Recrystallization of crude 2,2,6,6-tetramethyltetrahydropyran-4-ol obtained by condensation, dehydration and hydrogenation of acetone using a hydrocarbon solvent. A characterized method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-ol. 2. The method according to claim 1, wherein a hydrocarbon solvent having 5 to 12 carbon atoms is used. 3. The method according to claim 1 or 2, wherein an aliphatic hydrocarbon is used as the hydrocarbon solvent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2930177A JPS6039275B2 (en) | 1977-03-18 | 1977-03-18 | Method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-ol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2930177A JPS6039275B2 (en) | 1977-03-18 | 1977-03-18 | Method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-ol |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53116375A JPS53116375A (en) | 1978-10-11 |
| JPS6039275B2 true JPS6039275B2 (en) | 1985-09-05 |
Family
ID=12272396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2930177A Expired JPS6039275B2 (en) | 1977-03-18 | 1977-03-18 | Method for purifying 2,2,6,6-tetramethyltetrahydropyran-4-ol |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6039275B2 (en) |
-
1977
- 1977-03-18 JP JP2930177A patent/JPS6039275B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53116375A (en) | 1978-10-11 |
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