JPS6041622A - Separation of p-xylene from p-xylene-containing mixture - Google Patents

Separation of p-xylene from p-xylene-containing mixture

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Publication number
JPS6041622A
JPS6041622A JP12505084A JP12505084A JPS6041622A JP S6041622 A JPS6041622 A JP S6041622A JP 12505084 A JP12505084 A JP 12505084A JP 12505084 A JP12505084 A JP 12505084A JP S6041622 A JPS6041622 A JP S6041622A
Authority
JP
Japan
Prior art keywords
xylene
compound
metacyclophane
containing mixture
inclusion
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
Application number
JP12505084A
Other languages
Japanese (ja)
Other versions
JPS6128647B2 (en
Inventor
Yataro Ichikawa
市川 弥太郎
Hideki Tsuruta
英樹 鶴田
Kenichi Kato
憲一 加藤
Yoshiyuki Yamanaka
山中 義之
Aoi Yamamoto
葵 山本
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP12505084A priority Critical patent/JPS6041622A/en
Publication of JPS6041622A publication Critical patent/JPS6041622A/en
Publication of JPS6128647B2 publication Critical patent/JPS6128647B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To separate p-xylene from a p-xylene-containing mixture in high selectivity in high recovery ratio advantageously, by preparing an inclusion compound of p-xylene and metacyclophane. CONSTITUTION:Preferably 0.01-100mol compound shown by the formula based on 1mol p-xylene in a p-xylene-containing mixture is brought into contact with the p-xylene-containing mixture preferably at 0-200 deg.C so that p-xylene is included in the compound shown by the formula, and the formed inclusion compound is separated by solid-liquid separation. The compound is heated preferably at 120-280 deg.C so that p-xylene is separated and recovered from the inclusion compound. The compound shown by the formula has merits of improved performance, its inexpensive synthesis, free selection of economic process, etc., and advantageously the inclusion compound can easily desorb p-xylene by various processes in high purity.

Description

【発明の詳細な説明】 本発明は、下記式 で表わされるメタシクロファンを利用したp −キシレ
ン含有混合物からのP−キシレンの分離法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating p-xylene from a p-xylene-containing mixture using metacyclophane represented by the following formula.

従来、P−キシレンの包接化合物に関しては、例えば (1)トリー〇−チモチドとの包接体;アメリカン・ケ
ミカル働ンサアテイー (Am+ Chem、Soc、) 3747(1952)及び同2339(1958)参照 (11) α−サイクpデキストリンとの包接体;米国
特許第3,456,028明細1F参照OiD 天然又
は合成ゼオライトとの包接体;特公昭37−5155号
公報参照 本発明者らは、これら公知のP−キシレンの包接体とは
異なる包接体及びその利用について、種々研究した結果
本発明に到達した。
Conventionally, regarding clathrate compounds of P-xylene, for example, (1) clathrates with tri-thymotide; see Am+ Chem, Soc. 3747 (1952) and 2339 (1958) ( 11) Inclusion complex with α-cyc p-dextrin; see US Pat. No. 3,456,028 Specification 1F OiD Inclusion complex with natural or synthetic zeolite; see Japanese Patent Publication No. 37-5155. The present invention was achieved as a result of various studies on inclusion bodies different from known inclusion bodies of P-xylene and their uses.

すなわち、本発明は下記式(I) で表わされるメタシクロファンとP−キシレン含有混合
物とを接触せしめて、前記メタシクロファンKP−キシ
レンを包接せしめた包接化合物を形成せしめ、該包接化
合物を分離し、該包接化合物からP−キシレンを分離回
収することを特徴とするP−キシレン含有混合物からの
P−キシレンの分離法である。
That is, the present invention involves contacting metacyclophane represented by the following formula (I) with a P-xylene-containing mixture to form an inclusion compound containing the metacyclophane KP-xylene, and forming an inclusion compound containing the metacyclophane KP-xylene. This is a method for separating P-xylene from a mixture containing P-xylene, which is characterized by separating the compound and separating and recovering P-xylene from the clathrate compound.

かかる本発明において、前記メタシクロファンにP−キ
シレンが包接し、包接組成物を形成することは、従来全
く知られてなく、またこの現象に基いて、P−キシレン
含有混合物からP−キシレンを高選択率、高回収率で分
離し得ることができる。
In the present invention, it has never been known that P-xylene is included in the metacyclophane to form an inclusion composition, and based on this phenomenon, P-xylene is included from a P-xylene-containing mixture. can be separated with high selectivity and high recovery rate.

以下本発明について詳述する。The present invention will be explained in detail below.

本発明のメタンクロファンは前記式CI)で表わされる
環状化合物であればよく、それは種々の製造法によって
得ることができる。例えばその製造法としては、 (a)ヘルベチ力、キミカ、γフタ(He lve t
i ca。
The methanecrophane of the present invention may be any cyclic compound represented by the above formula CI), and can be obtained by various production methods. For example, the manufacturing methods include (a) Helvet's force, Kimika, γ-futa (Helvet's force),
i ca.

Chimica Acta ) 50巻F25cicu
lus 7(1967)No、204 (b)シンセシス(Symthesis ) 424 
(1974)等に記載されている。
Chimica Acta) 50 volumes F25cicu
lus 7 (1967) No. 204 (b) Synthesis 424
(1974) and others.

本発明において、前記一般式CI)のメタシクIffフ
ァンとP−キシレンとの包接化合物を得るには種々の方
法が適用される。
In the present invention, various methods can be applied to obtain the clathrate compound of metasic Iff fan and P-xylene of the general formula CI).

例えば、P−キシレン含有混合物中に前記メタシクロフ
ァンを添加してもよいし、また包接化を完全に行なわし
めるために上記の如くメタシクロファンを添加して得ら
れる混合物を加温し完全に溶解した溶液とし、これを冷
却して生じた結晶を分離することによっても得られる。
For example, the metacyclophane may be added to a mixture containing P-xylene, or the mixture obtained by adding metacyclophane as described above may be heated to completely achieve inclusion. It can also be obtained by preparing a solution dissolved in water, cooling the solution, and separating the resulting crystals.

いずれの方法によっても容易にメタシクロファンにP−
キシレンが包接した包接化合物を得ることができる。
Metacyclophane can be easily converted to P- by either method.
A clathrate compound containing xylene can be obtained.

前記式CI)のメタシクロファンの使用分は、P −−
1’−シレン含有混合物中の■〕−キシレン1モル当り
、0.01〜100モル、好ましくは0.1〜10モル
、就中0.2〜2モルの割合が有利である。
The amount of metacyclophane of formula CI) used is P --
Proportions of from 0.01 to 100 mol, preferably from 0.1 to 10 mol, in particular from 0.2 to 2 mol, are advantageous per mole of [1]-xylene in the mixture containing 1'-silene.

約述の如(してメタシクロファンにP−キシレンを包接
させる場合、一般に一50〜350℃、好ましくは0〜
200℃、特に20〜150℃の範囲の温度で行なわれ
る。かくして形成された包接化合物をそれを含有する混
合物から分離するには、通常固液分離(例えば1過、遠
心分離、沈降等)によるか或は溶媒成分を蒸留により蒸
発除去する方法が好ましく利用出来る。
As mentioned above, when P-xylene is included in metacyclophane, the temperature is generally -50 to 350°C, preferably 0 to 350°C.
It is carried out at a temperature of 200°C, especially in the range from 20 to 150°C. In order to separate the clathrate compound thus formed from a mixture containing it, it is usually preferable to use solid-liquid separation (for example, filtration, centrifugation, sedimentation, etc.) or to remove the solvent component by evaporation by distillation. I can do it.

いずれの方法であってもその繰作温夏は一50〜120
℃、好ましくは0〜90℃の範囲が望ましく・。
No matter which method is used, the temperature for repeated cultivation is between 150 and 120.
℃, preferably in the range of 0 to 90℃.

本発明において、P−キシレンを分離する”P−キシレ
ン含有混合物”としては、P−キシレンを含有している
ものであればよ<、p−キシレン以外の成分として包接
化を阻害したり、生成した包接化合物から、P−キシレ
ンを容易に脱着したりしないものであればよく、殊に包
接化合物を容易に溶解したりしないものが好適である。
In the present invention, the "P-xylene-containing mixture" from which P-xylene is separated may be one that contains P-xylene, or contains components other than p-xylene that inhibit inclusion. Any material may be used as long as it does not easily desorb P-xylene from the generated clathrate compound, and in particular, one that does not easily dissolve the clathrate compound is preferred.

P−キシレン含有混合物中のP−キシレンの含有量は、
P−キシレンの含有量が極めて低い場合であっても包接
化合物をイ5ることができるので、広い範囲でよい。例
えば、P−キシレン含有混合物としてC8芳香族炭化水
素類を用いた場合、これにメタシクロファンを添加し包
接化せしめることにより容易にC8芳香族炭化水素類か
らP−キシレン包接化合物を分離することができる。
The content of P-xylene in the P-xylene-containing mixture is
Even if the content of P-xylene is extremely low, the clathrate compound can be removed, so a wide range may be used. For example, when C8 aromatic hydrocarbons are used as a P-xylene-containing mixture, the P-xylene clathrate compound can be easily separated from the C8 aromatic hydrocarbons by adding metacyclophane to clathrate it. can do.

″C8芳香族炭化水素類”とは、O−キシレンm−キシ
レン、P−キシレンの3種のキシレン類とエチルベンゼ
ンを意味し、これら4種の08芳香族炭化水素類はそれ
らの沸点が極めて接近しており工業的に蒸留分離を行う
ことは非常に困難である。特にm−キシレンとP−キシ
レンとの沸点差は小さく通常の実験室的精密蒸留をもっ
てしても、これらを単離することは極めて難しい。
"C8 aromatic hydrocarbons" means three types of xylenes, O-xylene, m-xylene, and P-xylene, and ethylbenzene, and these four types of 08 aromatic hydrocarbons have very close boiling points. Therefore, it is extremely difficult to carry out distillation separation industrially. In particular, the difference in boiling point between m-xylene and p-xylene is small and it is extremely difficult to isolate them even by ordinary laboratory precision distillation.

マタ、エチルベンゼンとP−キシレンとの沸点差も不さ
くこれらを蒸留分離するのは容易でない。
However, the difference in boiling points between ethylbenzene and P-xylene is also small, making it difficult to separate them by distillation.

現在工業的には、P−キシレンの異常に高い融点を利用
した結晶化分離法、HP−BF、とm−キシレンの錯化
合物の形成を利用した分離法等が知られているが、いず
れも原料油の深冷化、結晶体の取扱い、装置の腐蝕等の
問題があった。
Currently, industrially known methods include a crystallization separation method that utilizes the abnormally high melting point of P-xylene, and a separation method that utilizes the formation of a complex compound of HP-BF and m-xylene. There were problems such as deep cooling of raw oil, handling of crystals, and corrosion of equipment.

また近年ゼオライトによる吸着分離法が工業化されてい
る。この方法は結晶化分離法における共晶点と溶解度の
問題がないためKP−キシレンの回収率の向上、ユーテ
ィリティーの改善。
In recent years, adsorption separation methods using zeolites have been industrialized. Since this method does not have the problems of eutectic point and solubility in the crystallization separation method, it improves the recovery rate of KP-xylene and improves its utility.

装置の小屋化等が期待されている。しかしその反面、高
価な吸着剤の使用、経時的吸着能(装置能力)の低下、
複雑な脱着機構、脱着剤とキシレンの分離等の問題があ
り必ずしも有利なプロセスとは言えない。
It is expected that the equipment will be converted into a shed. However, on the other hand, the use of expensive adsorbents, the decline in adsorption capacity (equipment capacity) over time,
It is not necessarily an advantageous process because of problems such as a complicated desorption mechanism and separation of the desorbent and xylene.

しかし本発明において使用するメタシクロファンは、そ
の性能もさることながら、まず安価に合成出来ること、
経済的なプロセスを自由に選択しうろことなどの有利な
点を有している。
However, the metacyclophane used in the present invention has not only excellent performance, but also the fact that it can be synthesized at low cost.
It has advantages such as being able to freely choose economic processes.

またメタシクロファンとP−キシレンとの包接組成物は
、種々の方法により容易にP−キシレンを脱着させるこ
とが出来、純粋なP−キシレンを得ることが出来る。
Further, in the inclusion composition of metacyclophane and P-xylene, P-xylene can be easily desorbed by various methods, and pure P-xylene can be obtained.

本発明においてメタシク+:+77ノとP−キシレンと
の包接化合物からP−キシレンを分離スる場合には、種
々の方法が採用されるが、例えば(a)包接化合物を9
0〜350℃、好ましくは120〜280℃の範囲の温
度に加熱しP−キシレンを分離する方法、(b)包接化
合物に、例えばn−へキサン、ベンゼン、シクロヘキサ
ン。
In the present invention, when separating P-xylene from the clathrate compound of metasic+:+77 and P-xylene, various methods are employed, for example, (a) separating the clathrate compound from 9
A method for separating P-xylene by heating to a temperature in the range of 0 to 350°C, preferably 120 to 280°C, (b) inclusion compounds such as n-hexane, benzene, and cyclohexane.

アセトン等の溶媒を接触させてP−キシレンを分離する
方法等が有利に適用される。
A method of separating P-xylene by bringing it into contact with a solvent such as acetone is advantageously applied.

以下本発明の包接化合物について説明すると、分離され
た結晶(包接化合物)を真空乾燥し、付着物を除いた後
分析した結果は次の通りであった。
The clathrate compound of the present invention will be explained below. The isolated crystal (clathrate compound) was vacuum dried to remove deposits, and the results of analysis were as follows.

+11 赤外分析; メタシクロファン 3050〜2850.1610.1590゜1490 
+1455 1Los’o +890 +790 。
+11 Infrared analysis; Metacyclophane 3050-2850.1610.1590°1490
+1455 1 Los'o +890 +790.

700、・460α−1 P−キシレン 3050〜2850 +1515.790.485cm
−’包接組成物 3050〜2850,1610.1590゜1515.
1490,1453,1080,890゜790 +7
00.485 +460cm ”従ってメタシクロファ
ン及びP−キシレンによる吸収(15151485)以
外の吸収は認められなかった。
700, 460α-1 P-xylene 3050-2850 +1515.790.485cm
-'Inclusion composition 3050-2850, 1610.1590°1515.
1490, 1453, 1080, 890°790 +7
00.485 +460cm ”Therefore, no absorption other than that due to metacyclophane and P-xylene (15151485) was observed.

(2) ガスクロ分析: 結晶(包接化合物)を力′スクμ分析したところ結晶中
に包接されているP−キシレンの他の成分に対する濃度
は約95%以上であり、大部分がP−キシレンであるこ
とが關められた。
(2) Gas chromatography analysis: When the crystal (clathrate compound) was subjected to force μ analysis, the concentration of P-xylene clathrated in the crystal relative to other components was approximately 95% or more, and the majority was P-xylene. It was suspected that it was xylene.

+31 示差熱分析; 結晶(包接化合物)を示差熱分析したところ、90〜1
15℃において重量減少が認められ、その減少量から包
接率(P−キシレン/メタシクロファン=0.99Cモ
ル比)〕であることがわかった。この〕結果P−キシレ
ン:メタシクロファン中11(モル比)テ包接している
ことを示している。
+31 Differential thermal analysis; Differential thermal analysis of the crystal (clathrate compound) revealed that it was 90-1
A weight loss was observed at 15° C., and the amount of weight loss was found to be due to the inclusion ratio (P-xylene/metacyclophane = 0.99 C molar ratio). This result shows that P-xylene: 11 (molar ratio) is included in metacyclophane.

以上の結果は、実施例に示される如く、P−キシレン混
合物としてP−キシレン以外の他の成分が1種又はそれ
以上任意の割合で含有されていても、本発明の包接化合
物が得られ、このことは、メタシクロファンの使用によ
りP−キシレン含有混合物からP−キシレンを選択的に
包接させることが出来、分離させることが出来ることを
示している。
The above results show that even if the P-xylene mixture contains one or more components other than P-xylene in arbitrary proportions, the clathrate compound of the present invention can be obtained. This shows that P-xylene can be selectively included and separated from a P-xylene-containing mixture by using metacyclophane.

以下実施例を揚げて本発明を詳述する。The present invention will be described in detail below with reference to Examples.

なお実施例中meとあるのはメタシクロファン、pxと
あるのはP−キシレン、mxとあるのはm−キシレン、
 EBとあるのはエチルベンゼンを示す。
In the examples, "me" means metacyclophane, "px" means P-xylene, "mx" means m-xylene,
EB indicates ethylbenzene.

また実施例中選択度(八)は下記式に基づいて鍔出され
た値である。
In addition, the selectivity (8) in Examples is a value determined based on the following formula.

実施例1 me 0.05部を0.5部ずつのPX+mx+EBに
各々室温で添加する。この時PXだけが白濁するがmx
 + FBは完全に溶解する。この液を各々80℃まで
昇温し約2分間保持し各溶液を完全に溶解せしめてから
室温までさげるとPX溶液のみから針状結晶が多量生成
する。他のmX+EB溶液は溶解状態であり長時間放置
しても結晶は生成しなかった。
Example 1 0.05 part of me is added to 0.5 parts of each PX+mx+EB at room temperature. At this time, only PX becomes cloudy, but mx
+ FB is completely dissolved. When each of these solutions is heated to 80° C. and maintained for about 2 minutes to completely dissolve each solution, and then cooled to room temperature, a large amount of needle-shaped crystals are generated from only the PX solution. The other mX+EB solutions were in a dissolved state and no crystals were formed even after being left for a long time.

実施例2 me 0.2部を、PX 、rnX + EB各々1部
の混合溶液3部に添加し、100℃まで昇温し、完全に
溶解してから室温までさげると針状結晶が生成する。こ
の混合物を濾過し、得られた結晶な室温100 mll
gobsで1時間乾燥し付着したキシレンを除去して、
0.22部の白色、針状結晶を得た。この結゛晶の一部
をガスクpで分析したところ、選択度はβPX/mX−
24.βPX/EB= 68であり、結晶中のPX濃度
はPX/ (PX+mX+F B )=0.95なので
結晶中には、mX T EBがほとんど含まれていない
ことがわかった。さらにこの結晶の赤外分析のデータは
、 3050〜2850.1610+1590.1515゜
1490.1453,1080,890.790 +7
00+485.460ロー1 でありmcによる吸収及びPXによる吸収(1515,
485)以外(mX + eB )の吸収は認められな
かった。
Example 2 0.2 part of me is added to 3 parts of a mixed solution of 1 part each of PX, rnX + EB, heated to 100°C, completely dissolved, and then lowered to room temperature to form needle-shaped crystals. . This mixture was filtered, resulting in 100 ml of crystalline room temperature
Dry with gobs for 1 hour to remove attached xylene,
0.22 parts of white, needle-shaped crystals were obtained. When a part of this crystal was analyzed using Gask p, the selectivity was βPX/mX-
24. Since βPX/EB=68 and the PX concentration in the crystal is PX/(PX+mX+F B )=0.95, it was found that mX T EB was hardly contained in the crystal. Furthermore, the infrared analysis data of this crystal is: 3050~2850.1610+1590.1515°1490.1453,1080,890.790 +7
00+485.460 low 1, absorption by mc and absorption by PX (1515,
No absorption of (mX + eB) other than 485) was observed.

これらの結果から、この結晶にはキシレン類の付着物は
なくほとんど純粋なPX包接体と考えられる。
From these results, this crystal is considered to be an almost pure PX clathrate with no xylenes deposits.

次にこの白色針状結晶0.0083部を示着熱天瓶によ
り分析したところ、90〜115℃において0.001
2部の重量減少が認められ、その減少量から包接率(p
x +mx+FB ) / me (モル比)= 0.
99の値が得られた。
Next, when 0.0083 part of this white needle-like crystal was analyzed using an indicative thermostat, it was found that 0.001 part at 90-115°C.
A weight loss of 2 parts was observed, and the inclusion rate (p
x+mx+FB)/me (molar ratio)=0.
A value of 99 was obtained.

実施例3 nicO,2部をpX+ mX各々1部からなる混合溶
液2部に添加し、実施例2と同様な操作を行い、0.2
1部の白色針状結晶を得た。この結晶をガスクpで分析
したところβpx/mx=1.9 の値が得られた。
Example 3 2 parts of nicO was added to 2 parts of a mixed solution consisting of 1 part each of pX + mX, and the same operation as in Example 2 was performed to obtain 0.2 parts of nicO.
One part of white needle-like crystals was obtained. When this crystal was analyzed using gask p, a value of βpx/mx=1.9 was obtained.

実施例4〜9 me 0.1部を下記の溶媒1.0部とpx 1.0部
の混合溶液に添加し、70〜130℃で加熱溶解した後
、室温まで徐冷し、結晶を生成する、その結晶を室温で
吸引濾過により、溶液と分離した後室温0.3x+Hg
の減圧下で1時間乾燥する。かくして得られた白色結晶
を他の溶媒に溶かしてガスクロ分析を行い、分離係数β
px/5olvとして、下表に示す結果を得た。
Examples 4 to 9 0.1 part of me was added to a mixed solution of 1.0 part of the following solvent and 1.0 part of px, and after heating and dissolving at 70 to 130°C, it was slowly cooled to room temperature to form crystals. After separating the crystals from the solution by suction filtration at room temperature,
Dry under reduced pressure for 1 hour. The white crystals thus obtained were dissolved in another solvent and subjected to gas chromatography analysis to determine the separation factor β.
The results shown in the table below were obtained as px/5olv.

実施例工0 実施例2で得られた白色針状結晶0.1部をメタノール
2部に添加し、10℃で10分攪拌1別して0.09部
の白色針状結晶を得た。この結晶の一部をガスクロ分析
を行ったところ、px/(px+mx +EB ) =
 0.94 であり、メタノールと接触する前と同様で
あった。
Example 0 0.1 part of the white needle-like crystals obtained in Example 2 was added to 2 parts of methanol, and the mixture was stirred for 10 minutes at 10° C. to obtain 0.09 part of white needle-like crystals. When a part of this crystal was subjected to gas chromatography analysis, px/(px+mx +EB) =
0.94, which was the same as before contact with methanol.

実施例11 実施例2と同様にして得られた白色針状結晶(組#::
 (px +mx +EB )/mc= 0.99 (
rno//mo/’ ) 、pxlCpx+mx十FB
 ) = 0.95 (moIV/moA! ))0.
2部にベンゼン1.0部を加え、封管に仕込み、130
℃まで加熱し、結晶を完全に溶解した後、室温まで冷却
し、再度針状結晶を形成させた。
Example 11 White needle-like crystals obtained in the same manner as in Example 2 (set #::
(px +mx +EB)/mc= 0.99 (
rno//mo/'), pxlCpx+mxtenFB
) = 0.95 (moIV/moA!))0.
Add 1.0 part of benzene to 2 parts and place in a sealed tube, 130
After heating to ℃ to completely dissolve the crystals, the mixture was cooled to room temperature to form needle-shaped crystals again.

該混合物から、濾過によりケークを分離した残液、及び
該ケークを0.5部のベンゼンで洗浄した洗浄液との合
計(以後、F液という)は1.1部であった。
The total amount of the residual liquid obtained by separating the cake from the mixture by filtration and the washing liquid obtained by washing the cake with 0.5 part of benzene (hereinafter referred to as liquid F) was 1.1 parts.

このP液をガスクロで分析した所Cpx−1−mχ十E
B)/ベンゼン= 2.1 (wt%) 、 px/(
px+mx+EB)−0,95(moJ/moJ ) 
であった。かくしてf液からベンゼンを蒸発、除去する
ことによ0px(微量のmx + EBを含有)を80
%の回収率で得ることができた。
When this P liquid was analyzed by gas chromatography, Cpx-1-mχ1E
B)/benzene = 2.1 (wt%), px/(
px+mx+EB)-0,95(moJ/moJ)
Met. In this way, by evaporating and removing benzene from the f liquid, 0px (containing a trace amount of mx + EB) was reduced to 80
% recovery rate.

特許出肢人 帝人株式会社、ど−・ 〆・1・、・・Patent creator Teijin Ltd. 〆・1・、・・

Claims (1)

【特許請求の範囲】 下記式 で表わされるメタシクロファンとP−キシレン含有混合
物とを接触せしめて、前記メタシクロファンにP−キシ
レンを包接せしめた包接化合物を形成せしめ、該包接化
合切を分離し、該包接化合物からP−キシレンを分離回
収することを特徴とするP−キシレン含有混合物からの
P−キシレンの分離法。
[Scope of Claims] Metacyclophane represented by the following formula and a P-xylene-containing mixture are brought into contact to form an inclusion compound in which P-xylene is included in the metacyclophane, and the inclusion compound is 1. A method for separating P-xylene from a P-xylene-containing mixture, the method comprising separating the clathrate and recovering P-xylene from the clathrate.
JP12505084A 1984-06-20 1984-06-20 Separation of p-xylene from p-xylene-containing mixture Granted JPS6041622A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12505084A JPS6041622A (en) 1984-06-20 1984-06-20 Separation of p-xylene from p-xylene-containing mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12505084A JPS6041622A (en) 1984-06-20 1984-06-20 Separation of p-xylene from p-xylene-containing mixture

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP12625975A Division JPS604805B2 (en) 1975-10-22 1975-10-22 Production method of clathrate compounds

Publications (2)

Publication Number Publication Date
JPS6041622A true JPS6041622A (en) 1985-03-05
JPS6128647B2 JPS6128647B2 (en) 1986-07-01

Family

ID=14900588

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12505084A Granted JPS6041622A (en) 1984-06-20 1984-06-20 Separation of p-xylene from p-xylene-containing mixture

Country Status (1)

Country Link
JP (1) JPS6041622A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4940832A (en) * 1988-06-13 1990-07-10 Tsutomu Miyashi Process for separating 2,6-dimethylnaphthalene
KR100914024B1 (en) 2008-06-12 2009-08-28 경희대학교 산학협력단 Method for separation of p-xylene from xylene mixture by guanidinium 4-chlorophenethyl monosulfonate host
KR100916287B1 (en) 2007-12-26 2009-09-10 경희대학교 산학협력단 Separation of xylene isomer from xylene mixture by selective inclusion using guanidinium ortho¡ªterphenyl 4,4¡¯¡ªdisulfonate host compound
KR100916286B1 (en) 2007-12-26 2009-09-10 경희대학교 산학협력단 Selective separatin of xylene isomer from xylene mixture by inclusion using guanidinium biphenyl¡ª2,2¡¯¡ªdiyldimethanesulfonate host compound
KR100984798B1 (en) 2008-06-12 2010-10-04 경희대학교 산학협력단 Method for separation of p-xylene from xylene mixture by guanidinium 2-chlorophenethyl monosulfonate host

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62182744U (en) * 1986-05-09 1987-11-19
JPS62182754U (en) * 1986-05-09 1987-11-19

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4940832A (en) * 1988-06-13 1990-07-10 Tsutomu Miyashi Process for separating 2,6-dimethylnaphthalene
KR100916287B1 (en) 2007-12-26 2009-09-10 경희대학교 산학협력단 Separation of xylene isomer from xylene mixture by selective inclusion using guanidinium ortho¡ªterphenyl 4,4¡¯¡ªdisulfonate host compound
KR100916286B1 (en) 2007-12-26 2009-09-10 경희대학교 산학협력단 Selective separatin of xylene isomer from xylene mixture by inclusion using guanidinium biphenyl¡ª2,2¡¯¡ªdiyldimethanesulfonate host compound
KR100914024B1 (en) 2008-06-12 2009-08-28 경희대학교 산학협력단 Method for separation of p-xylene from xylene mixture by guanidinium 4-chlorophenethyl monosulfonate host
KR100984798B1 (en) 2008-06-12 2010-10-04 경희대학교 산학협력단 Method for separation of p-xylene from xylene mixture by guanidinium 2-chlorophenethyl monosulfonate host

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