JPH0453851B2 - - Google Patents

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Publication number
JPH0453851B2
JPH0453851B2 JP59246135A JP24613584A JPH0453851B2 JP H0453851 B2 JPH0453851 B2 JP H0453851B2 JP 59246135 A JP59246135 A JP 59246135A JP 24613584 A JP24613584 A JP 24613584A JP H0453851 B2 JPH0453851 B2 JP H0453851B2
Authority
JP
Japan
Prior art keywords
hours
reaction
catalyst
ethylene
benzene
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 - Lifetime
Application number
JP59246135A
Other languages
Japanese (ja)
Other versions
JPS61126041A (en
Inventor
Hiroshi Ishida
Hitoshi Nakajima
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.)
KEISHITSU RYUBUN SHINYOTO KAIHATSU GIJUTSU KENKYU KUMIAI
Original Assignee
KEISHITSU RYUBUN SHINYOTO KAIHATSU GIJUTSU KENKYU KUMIAI
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 KEISHITSU RYUBUN SHINYOTO KAIHATSU GIJUTSU KENKYU KUMIAI filed Critical KEISHITSU RYUBUN SHINYOTO KAIHATSU GIJUTSU KENKYU KUMIAI
Priority to JP59246135A priority Critical patent/JPS61126041A/en
Publication of JPS61126041A publication Critical patent/JPS61126041A/en
Publication of JPH0453851B2 publication Critical patent/JPH0453851B2/ja
Granted legal-status Critical Current

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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

Landscapes

  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

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、スチレンの原料として有用なエチル
ベンゼンを選択的に製造する方法に関するもので
ある。 (従来の技術) ベンゼンを気相においてエチル化する方法に関
しては、近年、モビール社が開発した触媒として
結晶性アルミノシリケートZSM−5を用いる方
法(特公昭56−44050号参照)が知られている。
しかし、ZSM−5をそのまま触媒として使用し
た場合、トルエン、エチルトルエン等の副生が多
いため、モービル社では、ZSM−5をリン酸化
物で処理した触媒を用いる方法(特開昭51−
57688号参照)を提案しており、実際に、これら
の触媒を用いてモービリーバジヤー法として知ら
れるプロセスが企素化されている。 (発明が解決しようとする問題点) しかしながら、リンの酸化物で処理したZSM
−5を用いる方法は、確かにエチルベンゼン、ジ
エチルベンゼンへの選択率は高く、97%に達する
ものもあるが、98%以上という極めて高い選択率
の実現は困難であり、また、活性が低いという問
題があつた。さらに、本反応は反応中に触媒上へ
炭素質の析出を生じるため、活性の経時的な低下
を伴なう。それを防ぐために、水素を共存させる
ことが考えられるが、リンの酸化物で処理した
ZSM−5の場合、水素を共存させるとトルエン、
エチルトルエン等の副生が多く、選択率が低下す
るという問題のあることがわかつた。 (問題点を解決するたの手段) 本発明者らは、エチルベンゼン、ジエチルベン
ゼンへの選択率が98%以上で高活性を有し、しか
も、水素共存下でも選択性の低下しない触媒を開
発すべく鋭意検討を重ねた結果、X線回折図にお
いて表1の回折パターンを有する結晶性アルミノ
シリケートを触媒として用いる場合に、目的を満
足する結果が得られることを見い出し、本発明を
完成するに至つた。
(Industrial Application Field) The present invention relates to a method for selectively producing ethylbenzene, which is useful as a raw material for styrene. (Prior art) Regarding the method of ethylating benzene in the gas phase, a method using crystalline aluminosilicate ZSM-5 as a catalyst developed by Mobil Corporation in recent years (see Japanese Patent Publication No. 56-44050) is known. .
However, if ZSM-5 is used as a catalyst as it is, many by-products such as toluene and ethyltoluene are generated.
57688), and in fact, a process known as the Mobile Bazier process has been proposed using these catalysts. (Problem to be solved by the invention) However, ZSM treated with phosphorus oxide
The method using -5 does have a high selectivity to ethylbenzene and diethylbenzene, reaching 97% in some cases, but it is difficult to achieve an extremely high selectivity of 98% or more, and there is also the problem of low activity. It was hot. Furthermore, this reaction causes precipitation of carbonaceous matter on the catalyst during the reaction, which is accompanied by a decrease in activity over time. In order to prevent this, it is possible to coexist with hydrogen, but if treated with phosphorus oxide,
In the case of ZSM-5, when hydrogen coexists, toluene,
It was found that there were many by-products such as ethyltoluene, which caused a problem in which the selectivity decreased. (Means for solving the problem) The present inventors aimed to develop a catalyst that has high activity with a selectivity to ethylbenzene and diethylbenzene of 98% or more, and that does not lose selectivity even in the coexistence of hydrogen. As a result of extensive studies, the inventors discovered that when a crystalline aluminosilicate having the diffraction pattern shown in Table 1 in an X-ray diffraction diagram is used as a catalyst, results satisfying the objective can be obtained, and the present invention has been completed. .

【表】 X線回折分析はCuKα線を用いて測定する。た
だし、8.7±0.2と8.9±0.2の回折線のどちらかを
相対強度100とする。 すなわち、本発明は、ベンゼンを水素共存下で
気相においてエチレンと反応させる際に、触媒と
してX線回折図において表1に示される回折パタ
ーンを有する結晶性アルミノシリケートを用いる
ことを特徴とするベンゼンのエチル化法を提供す
るものである。 本発明に用いられる表1に示される回折パター
ンを有する結晶性アルミノシリケートとは、AZ
−1(特開昭59−128210号参照)と呼ばれる得意
な結晶構造を有する結晶性アルミノシリケートで
ある。 本発明における反応温度は200〜600℃、好まし
くは300〜500℃の範囲である。また、圧力は常圧
または加圧で行なわれるが、好ましい範囲は、常
圧〜20Kg/cm2の範囲である。 本発明は、気相流通法で行なわれるが、その際
のベンゼン/エチレンモル比は1〜20、好ましく
は2〜10の範囲、水素/エチレンモル比は0.5〜
20、好ましくは1〜10の範囲で行なわれる。 (発明の効果) 本発明の方法によれば、従来のリンの酸化物で
処理したZSM−5を触媒として用いる方法に比
べて、水素共存下で高収率で、しかも、極めて高
い選択率でエチルベンゼンおよびジエチルベンゼ
ンを得ることができる。このことは、工業的に実
施する際に極めて有利になる。 (実施例) 実施例 1 1,8−ジアミノ−4−アミノメチルオクタン
100g、硫酸アルミニウム(Al2(SO43・18H2O)
5g、水酸化ナトリウム5gを水150gにとかし、
さらにイシリカゾル(30%SiO2)200gを加えて
均質な溶液を得た。この溶液に、かきまぜながら
20%硫酸30gを滴下して均質なゲルを得た。さら
に、このゲルをホモジナイザーに入れ、
10000rpmで10分間混合した。このゲルをテフロ
ン内張りステンレス製耐圧容器中で、180℃、45
時間静置して結晶化を行つた。 得られた生成物を過、洗浄したのち、120℃
で6時間乾燥して、さらに500℃で6時間焼成し
た。 この生成物のX線回折パターンを図面に示す。
この回折パターンより、この生成物は、AZ−1
と同定された。また、螢光X線分析から求めたシ
リカ/アルミナモル比は80であつた。 この結晶性アルミノシリケートAZ−1を触媒
として用い、ベンゼンとエチレンの反応を行つ
た。実験条件は、ベンゼン/エチレン/H2モル
比=4/1/4、WHSV(ベンゼン基準)=
4.0hr-1、反応温度400℃、圧力3.0Kg/cm2で行つ
た。 反応開始後、2時間、6時間、20時間の結果を
表2に示す。
[Table] X-ray diffraction analysis is performed using CuKα radiation. However, the relative intensity of either the 8.7±0.2 or 8.9±0.2 diffraction lines is set to 100. That is, the present invention is characterized in that when benzene is reacted with ethylene in a gas phase in the presence of hydrogen, a crystalline aluminosilicate having a diffraction pattern shown in Table 1 in an X-ray diffraction diagram is used as a catalyst. The present invention provides a method for ethylating. The crystalline aluminosilicate having the diffraction pattern shown in Table 1 used in the present invention is AZ
It is a crystalline aluminosilicate with a unique crystal structure called JP-A-1 (see Japanese Patent Application Laid-Open No. 59-128210). The reaction temperature in the present invention is in the range of 200 to 600°C, preferably 300 to 500°C. Further, the pressure may be normal pressure or increased pressure, and a preferable range is normal pressure to 20 kg/cm 2 . The present invention is carried out by a gas phase flow method, in which the benzene/ethylene molar ratio is in the range of 1 to 20, preferably 2 to 10, and the hydrogen/ethylene molar ratio is in the range of 0.5 to 20.
20, preferably in the range of 1 to 10. (Effects of the Invention) According to the method of the present invention, compared to the conventional method using ZSM-5 treated with phosphorus oxide as a catalyst, a high yield can be achieved in the coexistence of hydrogen, and an extremely high selectivity can be achieved. Ethylbenzene and diethylbenzene can be obtained. This becomes extremely advantageous in industrial implementation. (Example) Example 1 1,8-diamino-4-aminomethyloctane
100g, aluminum sulfate (Al 2 (SO 4 ) 3・18H 2 O)
Dissolve 5g of sodium hydroxide in 150g of water,
Furthermore, 200 g of isilica sol (30% SiO 2 ) was added to obtain a homogeneous solution. Add to this solution while stirring.
30 g of 20% sulfuric acid was added dropwise to obtain a homogeneous gel. Furthermore, put this gel in a homogenizer,
Mixed for 10 minutes at 10000 rpm. This gel was stored at 180℃ and 45℃ in a Teflon-lined stainless steel pressure container.
The mixture was allowed to stand for a period of time for crystallization. After filtering and washing the obtained product, it was heated to 120℃.
The mixture was dried at 500°C for 6 hours and then fired at 500°C for 6 hours. The X-ray diffraction pattern of this product is shown in the drawing.
From this diffraction pattern, this product is AZ-1
was identified. Furthermore, the silica/alumina molar ratio determined from fluorescent X-ray analysis was 80. Using this crystalline aluminosilicate AZ-1 as a catalyst, benzene and ethylene were reacted. The experimental conditions were: benzene/ethylene/H 2 molar ratio = 4/1/4, WHSV (benzene standard) =
The reaction time was 4.0 hr -1 , the reaction temperature was 400°C, and the pressure was 3.0 Kg/cm 2 . Table 2 shows the results at 2 hours, 6 hours, and 20 hours after the start of the reaction.

【表】 実施例 2 実施例1で得られた触媒を用いて、ベンゼン/
エチレン/H2モル比=5/1/4、WHSV=
4.0hr-1、反応温度430℃、圧力5.0.Kg/cm2で反応
を行つた。 反応開始後、3時間、40時間、120時間の成績
を表3に示す。
[Table] Example 2 Using the catalyst obtained in Example 1, benzene/
Ethylene/ H2 molar ratio=5/1/4, WHSV=
The reaction was carried out at a reaction time of 4.0 hr -1 , a reaction temperature of 430°C, and a pressure of 5.0 kg/cm 2 . Table 3 shows the results at 3 hours, 40 hours, and 120 hours after the start of the reaction.

【表】【table】

【表】 実施例 3 1,8−ジアミノ−4−アミノメチルオクタン
2000g、硫酸アルミニウム150g、水酸化ナトリ
ウム150gを水5000gにとかし、さらにシリカゾ
ル(30%SiO2)4000gを加えて均質な流液を得
た。この溶液に、かきまぜながら20%硫酸500g
を加えて均質なゲルを得た。さらに、このゲルを
ホモジナイザーに入れ、10000rpmで20分間混合
した。このゲルをテフロン内張りステンレス製耐
圧容器中で、165℃、60時間静置して結晶化を行
つた。 得られた生成物を過、洗浄したのち、120℃
で6時間乾燥して、さらに500℃で6時間焼成し
た。 この生成物のX線回折パターンより、この生成
物は、AZ−1と同定された。また、螢光X線分
析から求めたシリカ/アルミナモル比は80であつ
た。 このAZ−1を触媒に用いてベンゼンとエチレ
ンの反応を行つた。実験条件は、ベンゼン/エチ
レンH2モ比=3/1/2、WHSV=5.2hr-1、反
応温度420℃、圧力=4.0Kg/cm2で行つた。 反応開始後、3時間、25時間の成績を表4に示
す。
[Table] Example 3 1,8-diamino-4-aminomethyloctane
2,000 g of aluminum sulfate, 150 g of aluminum sulfate, and 150 g of sodium hydroxide were dissolved in 5,000 g of water, and 4,000 g of silica sol (30% SiO 2 ) was added to obtain a homogeneous liquid. Add 500 g of 20% sulfuric acid to this solution while stirring.
was added to obtain a homogeneous gel. Furthermore, this gel was placed in a homogenizer and mixed at 10,000 rpm for 20 minutes. This gel was crystallized by standing at 165° C. for 60 hours in a Teflon-lined stainless steel pressure container. After filtering and washing the obtained product, it was heated to 120℃.
The mixture was dried at 500°C for 6 hours and then fired at 500°C for 6 hours. Based on the X-ray diffraction pattern of this product, this product was identified as AZ-1. Furthermore, the silica/alumina molar ratio determined from fluorescent X-ray analysis was 80. Using this AZ-1 as a catalyst, a reaction between benzene and ethylene was carried out. The experimental conditions were: benzene/ethylene H 2 mo ratio = 3/1/2, WHSV = 5.2 hr -1 , reaction temperature 420°C, and pressure = 4.0 Kg/cm 2 . Table 4 shows the results 3 hours and 25 hours after the start of the reaction.

【表】【table】

【表】 実施例 4 実施例3で得られた触媒を用いてベンゼン/エ
チレン/H2モル比=6/1/3、WHSV=
6.0hr-1、反応温度440℃、圧力=4.0Kg/cm2で反応
を行つた。 反応開始後、2時間、30時間、150時間の成績
を表5に示す。
[Table] Example 4 Using the catalyst obtained in Example 3, benzene/ethylene/H 2 molar ratio = 6/1/3, WHSV =
The reaction was carried out at a reaction time of 6.0 hr -1 , a reaction temperature of 440°C, and a pressure of 4.0 Kg/cm 2 . Table 5 shows the results at 2 hours, 30 hours, and 150 hours after the start of the reaction.

【表】 比較例 水550gに硫酸アルミニウム5gとテトラプロ
ピルアンモニウムブロミド10gを溶かし、さらに
Q brandケイ酸塩水溶液(Na2O=8.9重量%、
SiO2=28.9重量%、H2O=62.2重量%)150gを
加え、かきまぜて均質なゲルを得た。このゲル
に、20%H2SO450gをかきまぜながら滴下して
ゲル化を促進させた。このゲルをテフロン内張り
オートクレーブに入れ、150℃で20時間撹拌しな
がら結晶化させた。 得られた生成物を過洗浄後、120℃で3時間
乾燥し、500℃で4時間空気中で焼成を行つた。 この生成物のX線回折パターンは、ZSM−5
の回折パターンと一致した。また、螢光X線回折
より求めたシリカ/アルミナモル比は50であつ
た。 このZSM−5を、1N塩化アンモニウム水溶液
で60℃、24時間イオン交換を行つた後、過、洗
浄、120℃で6時間乾燥後、500℃で5時間空気焼
成してH−ZSM−5を得た。 得られたH−ZSM−5 10gをフラスコで、
n−オクタン50c.c.にトリメチルフオスフアイト4
c.c.を溶解した溶液に加えた。窒素を徐々に流しな
がら、この混合物を還流温度で80時間加熱した。
その後、この混合物を蒸発乾固して、得られた固
体をペンタンで焼成した後、120℃で10時間乾燥、
500℃で3時間焼成した。 得られた生成物のリン酸化物の担持量は8.2重
量%であつた。 このリン含有H−ZSM−5を触媒に用いて、
ベンゼン/エチレン/H2=4/1/4、WHSV
=4.0hr-1、反応温度400℃、圧力=3.0Kg/cm2で行
つた。 反応開始後、6時間の成績を表6に示す。
[Table] Comparative example Dissolve 5 g of aluminum sulfate and 10 g of tetrapropylammonium bromide in 550 g of water, and add Q brand silicate aqueous solution (Na 2 O = 8.9% by weight,
150 g of SiO 2 =28.9% by weight, H 2 O = 62.2% by weight) was added and stirred to obtain a homogeneous gel. 50 g of 20% H 2 SO 4 was added dropwise to this gel while stirring to promote gelation. This gel was placed in a Teflon-lined autoclave and crystallized with stirring at 150°C for 20 hours. After over-washing the obtained product, it was dried at 120°C for 3 hours and calcined in air at 500°C for 4 hours. The X-ray diffraction pattern of this product is ZSM-5
It matched the diffraction pattern of Furthermore, the silica/alumina molar ratio determined by fluorescent X-ray diffraction was 50. This ZSM-5 was ion-exchanged with a 1N ammonium chloride aqueous solution at 60℃ for 24 hours, filtered, washed, dried at 120℃ for 6 hours, and air-calcined at 500℃ for 5 hours to obtain H-ZSM-5. Obtained. 10g of the obtained H-ZSM-5 was placed in a flask.
Trimethyl phosphorite 4 in n-octane 50 c.c.
cc was added to the solution. The mixture was heated at reflux temperature for 80 hours with a gradual flow of nitrogen.
Thereafter, this mixture was evaporated to dryness, the resulting solid was calcined with pentane, and then dried at 120°C for 10 hours.
It was baked at 500°C for 3 hours. The amount of phosphoric oxide supported in the obtained product was 8.2% by weight. Using this phosphorus-containing H-ZSM-5 as a catalyst,
Benzene/ethylene/H 2 =4/1/4, WHSV
The reaction time was 4.0 hr -1 , the reaction temperature was 400°C, and the pressure was 3.0 Kg/cm 2 . Table 6 shows the results 6 hours after the start of the reaction.

【表】【table】

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

図面は実施例1で得られた結晶性アルミノシリ
ケートAZ−1のX線回折パターンを示す。
The drawing shows the X-ray diffraction pattern of the crystalline aluminosilicate AZ-1 obtained in Example 1.

Claims (1)

【特許請求の範囲】 1 ベンゼンを水素共存下で気相においてエチレ
ンと反応させる際に、触媒としてX線回折図にお
いて下表の回折パターンを有する結晶性アルミノ
シリケートを用いることを特徴とするベンゼンの
エチル化法。 【表】 X線回折分析はCuKα線を用いて測定する。た
だし、8.7±と8.9±0.20.2の回折線のどちらかを
相対強度100とする。
[Claims] 1. A method for reacting benzene with ethylene in the gas phase in the presence of hydrogen, using as a catalyst a crystalline aluminosilicate having a diffraction pattern shown in the table below in an X-ray diffraction diagram. Ethylation method. [Table] X-ray diffraction analysis is performed using CuKα radiation. However, either the diffraction line of 8.7± or 8.9±0.20.2 is taken as a relative intensity of 100.
JP59246135A 1984-11-22 1984-11-22 Ethylation of benzene Granted JPS61126041A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59246135A JPS61126041A (en) 1984-11-22 1984-11-22 Ethylation of benzene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59246135A JPS61126041A (en) 1984-11-22 1984-11-22 Ethylation of benzene

Publications (2)

Publication Number Publication Date
JPS61126041A JPS61126041A (en) 1986-06-13
JPH0453851B2 true JPH0453851B2 (en) 1992-08-27

Family

ID=17144000

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59246135A Granted JPS61126041A (en) 1984-11-22 1984-11-22 Ethylation of benzene

Country Status (1)

Country Link
JP (1) JPS61126041A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NZ178543A (en) * 1974-09-23 1978-04-03 Mobil Oil Corp Conversion catalyst, crystalline alumin osilicate zeolite containing phosphorus
JPS59128210A (en) * 1982-12-30 1984-07-24 Asahi Chem Ind Co Ltd Crystalline aluminosilicate, its manufature, and catalyst for alkylating monoalkylbenzene made of said aluminosilicate

Also Published As

Publication number Publication date
JPS61126041A (en) 1986-06-13

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