JPH05201889A - Production of 1,3-dimethylnaphthalene - Google Patents

Production of 1,3-dimethylnaphthalene

Info

Publication number
JPH05201889A
JPH05201889A JP4034033A JP3403392A JPH05201889A JP H05201889 A JPH05201889 A JP H05201889A JP 4034033 A JP4034033 A JP 4034033A JP 3403392 A JP3403392 A JP 3403392A JP H05201889 A JPH05201889 A JP H05201889A
Authority
JP
Japan
Prior art keywords
dimethylnaphthalene
platinum
methylpropene
dimethylphenyl
reaction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP4034033A
Other languages
Japanese (ja)
Inventor
Shiro Aizawa
史朗 相澤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eneos Corp
Original Assignee
Nippon Mining Co Ltd
Nikko Kyodo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Mining Co Ltd, Nikko Kyodo Co Ltd filed Critical Nippon Mining Co Ltd
Priority to JP4034033A priority Critical patent/JPH05201889A/en
Publication of JPH05201889A publication Critical patent/JPH05201889A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Abstract

PURPOSE:To enable selective synthesis of 1,3-dimethylnaphthalene and industrially improve the yield at a low cost. CONSTITUTION:The objective method for producing 1,3-dimethylnaphthalene comprises the cyclodehydrogenation of 1-(2,4-dimethylphenyl)-2-methylpropene in the presence of a platinum-alumina catalyst.

Description

【発明の詳細な説明】Detailed Description of the Invention

【産業上の利用分野】本発明は、1-(2,4-ジメチルフ
ェニル)-2-メチルプロペンを環化脱水素して1,3-ジ
メチルナフタレンを製造する方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing 1,3-dimethylnaphthalene by cyclodehydrogenation of 1- (2,4-dimethylphenyl) -2-methylpropene.

【0002】1,3-ジメチルナフタレンはこれを酸化し
て1,3-ナフタレンジカルボン酸とすることができ、こ
れは耐熱性に優れた高性能ポリエステルの原料として有
用でる。
1,3-Dimethylnaphthalene can be oxidized to give 1,3-naphthalenedicarboxylic acid, which is useful as a raw material for high-performance polyester having excellent heat resistance.

【0003】さらに、1,3-ジメチルナフタレンはこれ
を異性化することにより2,3-ジメチルナフタレンある
いは1,4-ジメチルナフタレンとなり、これらも同様に
耐熱性樹脂原料として有用であるとともに、医薬、農
薬、染料、顔料などの合成原料としても有用である。
Further, 1,3-dimethylnaphthalene is isomerized into 2,3-dimethylnaphthalene or 1,4-dimethylnaphthalene, which are also useful as raw materials for heat-resistant resins, and are It is also useful as a synthetic raw material for agricultural chemicals, dyes and pigments.

【0004】[0004]

【従来の技術】ジメチルナフタレン類は従来、タール留
分から分離されていた。また、近年ジメチルナフタレン
類のうち、特に2,6-ジメチルナフタレンについては種
々の原料からこれを合成する方法が提案(例えば、特開
昭62−238222号公報、特開平2-167237
号公報参照)されており、これらの副生成物として1,3
-ジメチルナフタレンが得られる。しかし、その選択率
は極めて小さく、これから1,3-ジメチルナフタレンを
高濃度で得るためには異性体の分離を行う必要があるた
め、工業的に実施できるものではなかった。
2. Description of the Related Art Conventionally, dimethylnaphthalenes have been separated from tar fractions. Further, in recent years, among dimethylnaphthalenes, especially for 2,6-dimethylnaphthalene, a method of synthesizing this from various raw materials has been proposed (for example, JP-A-62-238222 and JP-A-2-167237).
(See Japanese Laid-Open Patent Publication No. 3-1), and these by-products are 1,3
-Dimethylnaphthalene is obtained. However, its selectivity is extremely low, and in order to obtain 1,3-dimethylnaphthalene at a high concentration from this, it is necessary to separate the isomers, so that it cannot be industrially carried out.

【0005】[0005]

【発明が解決しようとする課題】本発明者は、かかる問
題を解決すべく、1-(2,4-ジメチルフェニル)-2-メ
チルプロペンの環化脱水素反応につき鋭意研究を進め
た。一般に、ポリアルキル置換ベンゼン類を環化脱水素
反応させると、側鎖アルキル基がベンゼン核と炭素-炭
素結合する場合と、側鎖アルキル基同士が炭素-炭素結
合する場合とが起こる。したがって、1-(2,4-ジメチ
ルフェニル)-2-メチルプロペンを環化脱水素させる
と、2-メチルプロペニル基がベンゼン核と炭素-炭素結
合した場合には1,3-ジメチルナフタレンが生成し、2
-メチルプロペニル基が側鎖メチル基と炭素-炭素結合し
た場合には2,6-ジメチルナフタレンが生成する。しか
しながら、この種の環化脱水素反応は、通常、400℃
〜550℃の高温条件下に行われるので、上記の環化脱
水素反応以外に分解、異性化、水素化などの種々の反応
が併発し、多くの副生成物が生じるという問題があっ
た。
DISCLOSURE OF THE INVENTION In order to solve such a problem, the present inventor has conducted earnest research on a cyclization dehydrogenation reaction of 1- (2,4-dimethylphenyl) -2-methylpropene. In general, when a polyalkyl-substituted benzene is subjected to a cyclodehydrogenation reaction, a side chain alkyl group forms a carbon-carbon bond with a benzene nucleus and a side chain alkyl group forms a carbon-carbon bond between them. Therefore, cyclodehydrogenation of 1- (2,4-dimethylphenyl) -2-methylpropene produces 1,3-dimethylnaphthalene when the 2-methylpropenyl group is carbon-carbon bonded to the benzene nucleus. Then 2
When the -methylpropenyl group is carbon-carbon bonded to the side chain methyl group, 2,6-dimethylnaphthalene is produced. However, this type of cyclodehydrogenation reaction is usually performed at 400 ° C.
Since it is carried out under a high temperature condition of ˜550 ° C., various reactions such as decomposition, isomerization, hydrogenation, etc. occur in addition to the above cyclodehydrogenation reaction, and there is a problem that many by-products are produced.

【0006】本発明はかかる問題を解決したもので、本
発明の目的は、脱水素環化反応以外の反応を抑制し、極
めて選択良く1,3-ジメチルナフタレンの製造方法を提
供することにある。
The present invention has solved the above problems, and an object of the present invention is to provide a method for producing 1,3-dimethylnaphthalene with excellent selectivity while suppressing reactions other than the dehydrocyclization reaction. ..

【0007】[0007]

【課題を解決するための手段】すなわち、本発明は1-
(2,4-ジメチルフェニル)-2-メチルプロペンを白金-
アルミナ触媒の存在下に環化脱水素反応させることから
なる1,3-ジメチルナフタレンの製造方法である。
That is, the present invention is 1-
(2,4-Dimethylphenyl) -2-methylpropene is platinum-
A method for producing 1,3-dimethylnaphthalene, which comprises reacting a cyclodehydrogenation reaction in the presence of an alumina catalyst.

【0008】上記1-(2,4-ジメチルフェニル)-2-メ
チルプロペンは、m-キシレンとイソブチルアルデヒドの
グリニヤール反応またはフリーデルクラフツ反応等によ
り合成することができる。
The above-mentioned 1- (2,4-dimethylphenyl) -2-methylpropene can be synthesized by the Grignard reaction of m-xylene and isobutyraldehyde or the Friedel-Crafts reaction.

【0009】脱水素環化反応を行う場合は、上記1-
(2,4-ジメチルフェニル)-2-メチルプロペンをそのま
ま、或いはベンゼン、トルエン、o-キシレン、m-キシレ
ン、p-キシレン、エチルベンゼン等の有機溶剤で5〜9
5%になるように希釈して反応させても良い。
When carrying out the dehydrocyclization reaction, the above 1-
5-9 for (2,4-dimethylphenyl) -2-methylpropene as it is or with organic solvents such as benzene, toluene, o-xylene, m-xylene, p-xylene, ethylbenzene
You may make it react so that it may be diluted so that it may become 5%.

【0010】本発明で用いられる白金-アルミナ触媒
は、アルミナ担体上に0.1〜0.6重量%の白金を担持
したもので、ナフサのリホーミング用に用いられている
市販の触媒を用いると簡便で好ましい。この白金-アル
ミナ触媒は、白金以外の、例えば、レニウム、パラジウ
ム、ロジウム、ルテニウム等の周期率表第VII、VIII族
から選定された金属を0.1〜1.0重量%の範囲で担持
したものでも良い。しかし、カリウム等の担持は選択性
を低下させるため好ましくない。
The platinum-alumina catalyst used in the present invention is a carrier in which 0.1 to 0.6% by weight of platinum is supported on an alumina carrier, and a commercially available catalyst used for reforming naphtha is used. It is simple and preferable. This platinum-alumina catalyst supports a metal other than platinum, such as rhenium, palladium, rhodium, or ruthenium, selected from the group VII and VIII of the periodic table in the range of 0.1 to 1.0% by weight. Anything is fine. However, supporting potassium or the like is not preferable because it lowers the selectivity.

【0011】この反応は、450〜600℃の温度、0
〜50kg/cm2の圧力、0.1〜5.0Hr-1の液容量空間速
度(LHSV)の条件下に、窒素、水素、スチーム、ヘリウ
ム、アルゴン等当該反応に対し活性なガスの雰囲気中で
行うことが好ましく、触媒床としては固定床、移動床、
流動床等のいずれの方式でも良い。
This reaction is carried out at a temperature of 450 to 600 ° C.
In a gas atmosphere active for the reaction such as nitrogen, hydrogen, steam, helium, and argon under the conditions of pressure of -50 kg / cm 2 and liquid volume space velocity (LHSV) of 0.1-5.0 Hr -1. Preferably, the catalyst bed is a fixed bed, a moving bed,
Any method such as a fluidized bed may be used.

【0012】この方法で得られた生成物は、蒸留、晶
析、抽出、カラムクロマト、錯体分離等の手段により単
離、精製できる。
The product obtained by this method can be isolated and purified by means such as distillation, crystallization, extraction, column chromatography and complex separation.

【0013】以下に、実施例により本発明を具体的に説
明する。
The present invention will be specifically described below with reference to examples.

【0014】[0014]

【実施例】【Example】

(実施例1)市販のアルミナ担体に塩化白金酸を白金含
有量が0.2%になるように含浸し、乾燥、焼成して調
製したものを触媒として用いた。1-(2,4-ジメチルフ
ェニル)-2-メチルプロペンの10重量%エチルベンゼ
ン溶液を原料として窒素気流下で530℃の温度、常圧
下、1Hr-1のLHSV条件下で、固定床により環化脱水素さ
せた。この結果を表1に示す。
(Example 1) A commercially available alumina carrier was impregnated with chloroplatinic acid to a platinum content of 0.2%, dried, and calcined to prepare a catalyst. Cyclization with 1- (2,4-dimethylphenyl) -2-methylpropene in a 10 wt% ethylbenzene solution as a raw material under a nitrogen stream at a temperature of 530 ° C. under atmospheric pressure and an LHSV of 1 Hr −1 under a fixed bed. It was dehydrogenated. The results are shown in Table 1.

【0015】(実施例2)触媒として、市販の白金-ア
ルミナ系触媒(R-32、UOP製)を用いた以外は実施
例1と同様の操作を行った。この結果を表1に示す。
(Example 2) The same operation as in Example 1 was carried out except that a commercially available platinum-alumina catalyst (R-32, manufactured by UOP) was used as the catalyst. The results are shown in Table 1.

【0016】(比較例1)触媒として市販のクロミア-
アルミナ系触媒(N-401、日揮製)を用いた以外は実
施例1と同様の操作を行った。結果を表1に示す。
Comparative Example 1 Commercially available chromia as a catalyst
The same operation as in Example 1 was performed except that an alumina catalyst (N-401, manufactured by JGC) was used. The results are shown in Table 1.

【0017】(比較例2)触媒として、実施例1で調製
した白金-アルミナに含浸法によりカリウムを0.2wt
%担持したものを用いた以外は実施例1と同様の操作を
行った。結果を表1に示す。
(Comparative Example 2) As a catalyst, platinum-alumina prepared in Example 1 was impregnated with 0.2 wt% of potassium.
% The same operation as in Example 1 was performed except that the supported one was used. The results are shown in Table 1.

【表1】 [Table 1]

【0018】[0018]

【発明の効果】本発明は、1,3-ジメチルナフタレンを
選択的に合成でき、工業的に、安価に、しかも収率良く
1,3-ジメチルナフタレンを製造できる効果を有する。
INDUSTRIAL APPLICABILITY The present invention has the effect that 1,3-dimethylnaphthalene can be selectively synthesized, and that 1,3-dimethylnaphthalene can be produced industrially, inexpensively, and in good yield.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 1-(2,4-ジメチルフェニル)-2-メチ
ルプロペンを白金-アルミナ触媒の存在下に環化脱水素
反応させることを特徴とする1,3-ジメチルナフタレン
の製造方法。 【0001】
1. A process for producing 1,3-dimethylnaphthalene, which comprises subjecting 1- (2,4-dimethylphenyl) -2-methylpropene to a cyclodehydrogenation reaction in the presence of a platinum-alumina catalyst. [0001]
JP4034033A 1992-01-27 1992-01-27 Production of 1,3-dimethylnaphthalene Pending JPH05201889A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4034033A JPH05201889A (en) 1992-01-27 1992-01-27 Production of 1,3-dimethylnaphthalene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4034033A JPH05201889A (en) 1992-01-27 1992-01-27 Production of 1,3-dimethylnaphthalene

Publications (1)

Publication Number Publication Date
JPH05201889A true JPH05201889A (en) 1993-08-10

Family

ID=12403032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4034033A Pending JPH05201889A (en) 1992-01-27 1992-01-27 Production of 1,3-dimethylnaphthalene

Country Status (1)

Country Link
JP (1) JPH05201889A (en)

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