JPS604805B2 - Production method of clathrate compounds - Google Patents
Production method of clathrate compoundsInfo
- Publication number
- JPS604805B2 JPS604805B2 JP12625975A JP12625975A JPS604805B2 JP S604805 B2 JPS604805 B2 JP S604805B2 JP 12625975 A JP12625975 A JP 12625975A JP 12625975 A JP12625975 A JP 12625975A JP S604805 B2 JPS604805 B2 JP S604805B2
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- Prior art keywords
- xylene
- metacyclophane
- crystals
- compound
- mixture
- 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.)
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
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アンにpーキシレンで包嬢せ
しめた包嬢化合物の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a encapsulated compound in which metacyclophane represented by the following formula is encapsulated with p-xylene.
従来、pーキシレンの包嬢化合物に関しては、例えば(
i)トリー○ーチモチドとの包薮体;
アメリカン・ケミカル・ソサアテイー
(Am,Chem.Soc.)
3747(1952)及び同2339(1958)参照
(i;)Q−サイクロデキストリンとの包蟻体;米国特
許第3,450 028明細書参照(iii)天然又は
合成ゼオラィトとの包嬢体;特公昭37−5155号公
報参照本発明者らは、これら公知のp−キシレンの包俊
体とは異なる包蚤体の製造法について、種々研究した結
果本発明に到達した。Conventionally, regarding p-xylene cladding compounds, for example (
i) Encapsulation with tri-timotide; see American Chemical Society (Am, Chem. Soc.) 3747 (1952) and Am. 2339 (1958) (i;) Encapsulation with Q-cyclodextrin; United States See Japanese Patent No. 3,450-028 (iii) Encapsulation with natural or synthetic zeolite; see Japanese Patent Publication No. 37-5155. The present invention was arrived at as a result of various research into methods for producing flea bodies.
すなわち、本発明は下記式(1)
で表わされるメタシクロフアンにpーキシレンを包倭せ
しめた包接化合物である。That is, the present invention is an inclusion compound in which p-xylene is enclosed in a metacyclophane represented by the following formula (1).
かかる本発明において、前記メタシクロフアンにpーキ
シレンが包接し、包嬢化合物を形成することは、従来全
く知られてなく、またこの化合物を用いて、pーキシレ
ン含有混合物からpー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 not been previously known that p-xylene is included in the metacyclophane to form an inclusion compound, and this compound can be used to remove p-xylene from a p-xylene-containing mixture with high selectivity. , can be separated with high recovery.
以下本発明について詳述する。The present invention will be explained in detail below.
本発明のメタシクロフアンは前記式(1)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。The metacyclophane of the present invention may be a cyclic compound represented by the above formula (1), and it can be obtained by various production methods.
例えばその製造法としては、‘a} へルベチ力、キミ
力、アクタ(Helvetica,ChimicaAc
ね)50巻 F2scicul雌7(1967)No.
204(b} シンセシス(Shm仇esis)424
(1974)等に記載されている。For example, the manufacturing methods include 'a} Helvetica, Chimica Ac
) Volume 50 F2scicul Female 7 (1967) No.
204(b} Synthesis (Shm-esis) 424
(1974) and others.
本発明において、前記一般式(1)のメタシクロフアン
とpーキシレンとの包酸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 encapsulated compound of metacyclophane and p-xylene represented by the general formula (1).
例えば、p−キシレン含有混合物中に前記メタシクロフ
アンを添加してもよいし、また包嬢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アンを添加して得ら
れる混合物を加溢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 the p-xylene-containing mixture, or the mixture obtained by adding metacyclophane as described above may be overflowed to completely encapsulate the mixture. 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アンにP−
キシレンが包接した包嬢化合物を得ることができる。前
記式(1)のメタシクロフアンの使用量は、pーキシレ
ン含有混合物中のpーキシレン1モル当り、o.ol〜
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。前述の如くしてメタシク
ロフアンにp−キシレンを包接させる場合、一般に−5
0〜35000、好ましくは0〜200午0、特に20
〜15000の範囲の温度で行なわれる。Either method can easily convert P- into metacyclophane.
A compound containing xylene can be obtained. The amount of metacyclophane of formula (1) used is o. ol~
100 mol, preferably 0.1 to 10 mol, especially 0.2
Proportions of ˜2 mol are advantageous. When p-xylene is included in metacyclophane as described above, generally -5
0 to 35,000, preferably 0 to 200 o'clock, especially 20
It is carried out at temperatures in the range of ~15,000 °C.
かくして形成された包酸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(例えば炉過、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。いずれの方法であっ
てもその操作温度は−50〜120oo、好ましくは0
〜90℃の範囲が望ましい。本発明の方法を用いて、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く、
p−キシレン以外の成分として包薮化を阻害したり、生
成した包嬢化合物から、pーキシレンを容易に脱着した
りしないものであればよく、殊に包授化合物を容易に溶
解したりしないものが好適である。In order to separate the encapsulated acid compound thus formed from the mixture containing it, it is usually preferable to use solid-liquid separation (e.g., filtration, centrifugation, sedimentation, etc.) or to remove the solvent component by evaporation by distillation. I can do it. In either method, the operating temperature is -50 to 120 oo, preferably 0.
A range of ~90°C is desirable. Using the method of the invention, p
- The "p-xylene-containing mixture" from which xylene is separated may be any mixture containing p-xylene;
Any component other than p-xylene may be used as long as it does not inhibit encapsulation or easily desorb p-xylene from the generated encapsulation compound, and in particular, it does not easily dissolve the encapsulation compound. is suitable.
p−キシレン含有混合物中のp−キシレンの含有量は、
pーキシレンの含有量が極めて低い場合であっても包酸
化合物を得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アンを添加し包嬢
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ーキシレン包援化合物を分離することができる。“C
8芳香族炭化水素類”とは、oーキシレン、mーキシレ
ン、pーキシレンの3種のキシレン類のエチルベンゼン
を意味し、これら4種のC8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。The content of p-xylene in the p-xylene-containing mixture is
Since an encapsulated acid compound can be obtained even when the content of p-xylene is extremely low, a wide range may be used. For example, when C8 aromatic hydrocarbons are used as the p-xylene-containing mixture, the p-xylene inclusion compound can be easily separated from the C8 aromatic hydrocarbons by adding metacyclophane to make it encapsulated. be able to. “C
"8 aromatic hydrocarbons" means ethylbenzene of three types of xylenes, o-xylene, m-xylene, and p-xylene, and these four types of C8 aromatic hydrocarbons have very close boiling points. It is very difficult to carry out distillation separation industrially.
特にmーキシレンとpーキシレンとの沸点差は4・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。また、エチルベンゼンとpー
キシレンとの沸点差も小さくこれらを蒸留分離するのは
容易でない。現在工業的には、pーキシレンの異常に高
い融点を利用した結晶化分離法、HF−BF3とm−キ
シレンの緒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。In particular, the difference in boiling point between m-xylene and p-xylene is 4.5 mm, making it extremely difficult to isolate them even with ordinary laboratory precision distillation. Furthermore, the difference in boiling points between ethylbenzene and p-xylene is small, making it difficult to separate them by distillation. 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 compound of HF-BF3 and m-xylene, but both of these methods use raw material oil. There were problems such as deep cooling, 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
問題がないためにpーキシレンの回収率の向上、ユーテ
ィリティーの改善、装置の小型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。しかし本発明において使用するメタシクロフアン
は、その性能もさることながち、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。またメタシクロフアンとp−キ
シレンとの包薮組成物は、種々の方法により容易にpー
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。本発明においてメタシクロフアン
とpーキシレンとの包俵化合物からp−キシレンを分離
する場合には、種々の方法が採用されるが、例えば‘a
)包嬢化合物を90〜350℃、好ましくは120〜2
80qoの範囲の温度に加溢しpーキシレンを分離する
方法、【bー包接化合物に、例えばn−へキサン、ベン
ゼン、シクロヘキサン、アセトン等の溶媒を接触させて
pーキシレンを分離する方法等が有利に適用される。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 crystallization separation methods, it is expected to improve the recovery rate of p-xylene, improve utility, and downsize the equipment.
However, on the other hand, the use of expensive adsorbents and the adsorption capacity over time (
It is not necessarily an advantageous process because of problems such as a decrease in equipment capacity, a complicated desorption mechanism, and separation of the desorbent and xylene. However, the metacyclophane used in the present invention has advantages such as not only its performance but also the fact that it can be synthesized at a low cost and that an economical process can be freely selected. Further, from the enveloping composition of metacyclophane and p-xylene, p-xylene can be easily desorbed by various methods, and pure p-xylene can be obtained. In the present invention, when p-xylene is separated from a packaged compound of metacyclophane and p-xylene, various methods are employed.
) The compound is heated at 90 to 350°C, preferably 120 to 2
A method of separating p-xylene by flooding the b-clathrate with a solvent such as n-hexane, benzene, cyclohexane, acetone, etc. Advantageously applied.
以下本発明の包嬢化合物について説明すると、分離され
た結晶(包酸化合物)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 encapsulated compound of the present invention will be explained below. The separated crystals (encapsulated acid compound) were vacuum dried to remove deposits, and then analyzed. The results were as follows.
m 赤外分析;
メタシクロフアン、
3050〜2850,1610,1590,1490,
1455,1雌0,890,790,700,460伽
‐lpーキシレン3050〜2850,1515,79
0,485狐‐1包薮化合物、3050〜2850,1
610,1590,1515,1490,1453,1
080,890”790,700,485,460Cの
一1従ってメタシクロフアン及びp−キシレンによる吸
収(1515,485)以外の吸収は認められなかつた
。m infrared analysis; metacyclophane, 3050-2850, 1610, 1590, 1490,
1455,1 female 0,890,790,700,460 ka-lp-xylene 3050-2850,1515,79
0,485 fox-1 envelope compound, 3050-2850,1
610,1590,1515,1490,1453,1
080,890''790,700,485,460C, no absorption other than that due to metacyclophane and p-xylene (1515,485) was observed.
■ ガスクロ分析;
結晶(包懐化合物)をガスクロ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ーキシレンであること
が認められた。■ Gas chromatography analysis: Gas chromatography analysis of the crystals (clathral compounds) revealed that the concentration of p-xylene clathrated in the crystals relative to other components was approximately 95% or more, and the majority was found to be p-xylene. It was done.
{3’示差熱分析:
結晶(包懐化合物)を示差熱分析したところ、90〜1
15qoにおいて重量減少が認められ、その減少量から
包嬢率〔p−キシレン/メタシクロフアン=0.99(
モル比)〕であることがわかった。{3' Differential thermal analysis: Differential thermal analysis of the crystal (encyclopedia compound) revealed that it was 90-1
A weight decrease was observed at 15qo, and from the amount of decrease, the inclusion ratio [p-xylene/metacyclophane = 0.99 (
molar ratio)].
この結果p−キシレン:メタシクロファン≠1:1(モ
ル比)で包接していることを示している。以上の結果は
、実施例に示される如く、pー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、メタシクロフアンの使用により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。This result shows that p-xylene:metacyclophane is included at a molar ratio of ≠1:1. As shown in the examples, the above results indicate that p-xylene mixture
- Even if one or more components other than xylene are contained in any proportion, 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mcとあるのはメタシクロフアン、p×と
あるのはpーキシレン、mはとあるのはmーキシレン、
EBとあるのはエチルベンゼンを示す。In the examples, mc means metacyclophane, px means p-xylene, m means m-xylene,
EB indicates ethylbenzene.
また実施例中選択度(B芸)は下記式に基づいて算出さ
れた値である。In addition, the selectivity (B trick) in the example is a value calculated based on the following formula.
(但しC,/C2は成分1.2のモル比を表わす。(However, C and /C2 represent the molar ratio of component 1.2.
)実施例 1mco.05部を0.5部ずつのpx、m
K,EBに各々室温で添加する。) Example 1mco. 05 parts by 0.5 parts px, m
K and EB respectively at room temperature.
この時pxだけが白濁するがpx,EBは完全に溶解す
る。この液を各々8000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。実施例 2mco.2部を、px,mは,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。At this time, only px becomes cloudy, but px and EB are completely dissolved. When the temperature of each solution is raised to 8,000 and held for about 2 minutes to completely dissolve each solution, the temperature is lowered to room temperature, and a large amount of needle-shaped crystals are generated from the px solution alone. The other mx and EB solutions were in a dissolved state and no crystals were formed even if they were left for a long time. Example 2mco. 2 parts of px, m were added to 3 parts of a mixed solution of 1 part of EB each, and the temperature was raised to 100°C.
When completely dissolved and cooled to room temperature, needle-shaped crystals will form.
この混合物を炉過し、得られた結晶を室温100脚Hg
o広で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
クロで分析したところ、選択度は8px/mK=2ム
6px/EB=68であり、結晶中のpx濃度はpx/
(px+mは十EB):0.95なので結晶中には、m
K,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折のデータは、3050〜285
0,1610,1590,1515,1490,145
31080,890,790,700,485,460
肌‐1であり、mcによる吸収及びpxによる吸収(1
515 485)以外(mK,EB)の吸収は認められ
なかつた。This mixture was filtered, and the obtained crystals were collected at room temperature at 100 feet Hg.
Dry for 1 hour in an oven to remove attached xylene.
22 parts of white, needle-shaped crystals were obtained. When a part of this crystal was analyzed by gas chromatography, the selectivity was 8 px/mK = 2 mu
6px/EB=68, and the px concentration in the crystal is px/
(px+m is 10EB): 0.95, so in the crystal there is m
It was found that K and EB were hardly included. Furthermore, the infrared spectroscopy data of this crystal is 3050-285
0,1610,1590,1515,1490,145
31080,890,790,700,485,460
Skin-1, absorption by mc and absorption by px (1
515 485) (mK, EB) was not 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包俊体と考えられる。From these results, this crystal is considered to be an almost pure px enclosing body with no xylenes deposits.
次にこの白色針状結晶0.0083部を示着熱夫瓶によ
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+mは十EB)/mc(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 heat exchanger, it was found that 0.001 part at 90-115°C.
A weight loss of 2 parts was observed, and the inclusion rate (p
A value of x+m (10 EB)/mc (molar ratio) = 0.99 was obtained.
実施例 3
mco.2部もpx,mは各々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、0.21部
の白色針状結晶を得た。Example 3 mco. 2 parts px, m each 1 part mixed solution 2
The same procedure as in Example 2 was carried out to obtain 0.21 part of white needle-like crystals.
この結晶を、ガスクロで分析したところ8px/mx=
1.9の値が得られた。実施例 4〜9
mco.1部を下記の溶媒1.碇郡とpxl.悦郎の混
合溶液に添加し、70〜130qoで加熱溶解した後、
室温まで徐冷し、結晶を生成する。When this crystal was analyzed by gas chromatography, 8px/mx=
A value of 1.9 was obtained. Examples 4-9 mco. One part was added to the following solvent 1. Ikari county and pxl. After adding it to Etsuro's mixed solution and dissolving it by heating at 70 to 130 qo,
Cool slowly to room temperature to form crystals.
その結果を室温で吸引炉過により、溶液と分離した後室
温0.3肌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8px/solvとして、下表に示す結果
を得た。実施例 10
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分鷹幹炉別して0.0$部
の白色針状結晶を得た。The resultant was separated from the solution by filtration in a suction oven at room temperature, and then dried for 1 hour under a reduced pressure of 0.3 skin Hg at room temperature. The thus obtained white crystals were dissolved in another solvent and subjected to gas chromatography analysis, and the results shown in the table below were obtained with a separation factor of 8 px/solv. Example 10 0.1 part of the white needle-like crystals obtained in Example 2 was added to 2 parts of methanol, and the mixture was separated in an oven at 10° C. for 10 minutes to obtain 0.0 part of white needle-like crystals.
この結晶の一部を、ガスクロ分析を行ったところ、px
/(px+mは十EB)=0.94であり、メタノール
と接触する前と同機であった。実施例 11実施例2と
同様にした得られた白色針状結晶(組成:(px+mx
+EB)/mc=0.99(mol/mol),px/
(px十mx+EB)=0.95(mol/mol))
0.2織こベンゼン1.碇都を加え、振替に仕込み、1
30午0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。When a part of this crystal was subjected to gas chromatography analysis, px
/(px+m is 10 EB) = 0.94, which was the same as before contact with methanol. Example 11 White needle-like crystals obtained in the same manner as in Example 2 (composition: (px+mx
+EB)/mc=0.99 (mol/mol), px/
(px 10 mx + EB) = 0.95 (mol/mol))
0.2 Oriko Benzene 1. Add Ikarito, prepare for transfer, 1
After heating until 1:30 AM to completely dissolve the crystals, the mixture was cooled to room temperature to form needle-like crystals again.
該混合物から、炉過によりケ−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、炉液という)は1.1部であった。この炉液
をガスクロで分析した所(px+mx+EB)/ベンゼ
ン=2.1(M%)、pxノ(px十mK+EB)=0
.95(mol/mol)であった。The total amount of the residual liquid obtained by separating the cake from the mixture by furnace filtration and the washing liquid obtained by washing the cake with 0.5 part of benzene (hereinafter referred to as furnace liquid) was 1.1 parts. When this furnace liquid was analyzed by gas chromatography, (px + mx + EB)/benzene = 2.1 (M%), px no (px 10 mK + EB) = 0
.. It was 95 (mol/mol).
Claims (1)
物とを接触せしめることを特徴とする前記メタシクロフ
アンにp−キシレンを包接せしめた包接化合物の製造法
。[Claims] 1. A metacyclophane represented by the following formula ▲There are mathematical formulas, chemical formulas, tables, etc.▼ and a p-xylene-containing mixture are brought into contact with each other. Method for producing clathrate compounds.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12625975A JPS604805B2 (en) | 1975-10-22 | 1975-10-22 | Production method of clathrate compounds |
US05/735,549 US4153630A (en) | 1975-10-22 | 1976-10-26 | Inclusion compounds, process for preparation thereof, and process for separating isomers using the inclusion compounds |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12625975A JPS604805B2 (en) | 1975-10-22 | 1975-10-22 | Production method of clathrate compounds |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12505084A Division JPS6041622A (en) | 1984-06-20 | 1984-06-20 | Separation of p-xylene from p-xylene-containing mixture |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5251329A JPS5251329A (en) | 1977-04-25 |
JPS604805B2 true JPS604805B2 (en) | 1985-02-06 |
Family
ID=14930743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12625975A Expired JPS604805B2 (en) | 1975-10-22 | 1975-10-22 | Production method of clathrate compounds |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS604805B2 (en) |
-
1975
- 1975-10-22 JP JP12625975A patent/JPS604805B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5251329A (en) | 1977-04-25 |
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