JPH0713085B2 - Sequential extraction and separation device for crystalline polymer - Google Patents

Sequential extraction and separation device for crystalline polymer

Info

Publication number
JPH0713085B2
JPH0713085B2 JP61210714A JP21071486A JPH0713085B2 JP H0713085 B2 JPH0713085 B2 JP H0713085B2 JP 61210714 A JP61210714 A JP 61210714A JP 21071486 A JP21071486 A JP 21071486A JP H0713085 B2 JPH0713085 B2 JP H0713085B2
Authority
JP
Japan
Prior art keywords
extraction
solvent
crystalline polymer
storage tank
container
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 - Fee Related
Application number
JP61210714A
Other languages
Japanese (ja)
Other versions
JPS6369501A (en
Inventor
浅沼  正
貢 伊藤
Original Assignee
三井東圧化学株式会社
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 三井東圧化学株式会社 filed Critical 三井東圧化学株式会社
Priority to JP61210714A priority Critical patent/JPH0713085B2/en
Publication of JPS6369501A publication Critical patent/JPS6369501A/en
Publication of JPH0713085B2 publication Critical patent/JPH0713085B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Extraction Or Liquid Replacement (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ポリマーの逐次抽出分離装置に関する。詳し
くは、結晶性ポリマーを逐次抽出して結晶性、組成など
の異なる各成分に分離するために好適に使用できる装置
に関する。
TECHNICAL FIELD The present invention relates to an apparatus for sequential extraction and separation of polymers. More specifically, the present invention relates to an apparatus that can be suitably used for sequentially extracting a crystalline polymer and separating each component having different crystallinity, composition and the like.

〔従来の技術〕[Conventional technology]

ポリマーを種々の溶媒を用いて逐次抽出して結晶性、組
成、分子量などの異なる各成分に分離することは良く知
られている。中でもポリプロピレン、ポリエチレンなど
の結晶性ポリマーを逐次抽出して各成分に分離すること
は広く行なわれており、沸点の異なる炭化水素溶媒を用
いてその溶剤の還流状態で抽出する方法(Bull.Chemica
l Society Japan,37巻,909ページ(1964年))、良溶媒
である炭化水素化合物と貧溶媒であるアルコール類など
との混合溶媒を用いて逐次抽出する方法(中部化学関係
学協会支部連合秋期大会第13回講演予稿集3A,20(1982
年))などがある。
It is well known that a polymer is sequentially extracted with various solvents to separate each component having different crystallinity, composition, molecular weight and the like. Among them, it is widely practiced to sequentially extract crystalline polymers such as polypropylene and polyethylene to separate them into respective components, and a method of extracting in a reflux state of a hydrocarbon solvent having different boiling points (Bull.Chemica
l Society Japan, vol. 37, p. 909 (1964), Method of sequential extraction using a mixed solvent of a hydrocarbon compound which is a good solvent and alcohols which is a poor solvent (Chubu Chemical Association Society Branch Autumn) Conference 13th Lecture Proceedings 3A, 20 (1982
Year)) etc.

〔発明が解決すべき問題点〕[Problems to be solved by the invention]

ポリマーの物性改良などの目的で重合法−物性−組成の
3者の関係を検討することは重要であり、この目的のた
め上記逐次抽出を実施することは広く行われているが、
混合溶媒を用いる方法は分離性能は優れているが操作に
熟練を要するという問題があり、また沸点の異なる炭化
水素溶媒を用いる方法は簡単であるが抽出分離の再現性
等の精度に難があるという問題があった。
For the purpose of improving the physical properties of the polymer, it is important to examine the relationship among the three factors of the polymerization method-physical properties-composition, and it is widely practiced to carry out the above sequential extraction for this purpose,
The method using a mixed solvent has excellent separation performance but has a problem that it requires skill in operation. Also, the method using a hydrocarbon solvent having a different boiling point is simple, but accuracy such as reproducibility of extraction separation is difficult. There was a problem.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者は上記問題点を解決し、しかも簡単な自動搬送
手段などを利用することで自動逐次抽出をも可能にせし
める装置について鋭意検討し、本発明を完成した。
The present inventor has conducted intensive studies on an apparatus that solves the above-mentioned problems and that also enables automatic sequential extraction by utilizing a simple automatic conveying means, and completed the present invention.

即ち、本発明は、抽出溶剤貯槽、該貯槽に連結された計
量器及び抽出部への導管よりなる溶剤貯槽部B、上部に
還流冷却器、還流冷却器下方に被抽出結晶性ポリマーを
入れる少なくとも下部にフィルターを設けてなる抽出容
器、さらに下方に加熱部及び抽出溶剤の取り出し用ノズ
ルを設けてなる抽出部Aより構成されることを特徴とす
る結晶性ポリマーの逐次抽出分離装置である。
That is, according to the present invention, at least a solvent storage tank section B comprising an extraction solvent storage tank, a meter connected to the storage tank and a conduit to the extraction section, a reflux condenser on the upper side, and a crystalline polymer to be extracted on the lower side of the reflux condenser are placed at least. A sequential extraction / separation apparatus for a crystalline polymer, characterized in that it comprises an extraction container having a filter in the lower part, and an extraction part A having a heating part and an extraction solvent extraction nozzle below the extraction container.

本発明の装置の概要を図面を用いて説明する。The outline of the device of the present invention will be described with reference to the drawings.

第1図に抽出部A及び溶剤貯槽部Bの概要を示し、第2
図に抽出容器の詳細を示す。
FIG. 1 shows an outline of the extraction section A and the solvent storage tank section B, and
The figure shows the details of the extraction container.

装置の材質としてはガラス或いは金属が好ましく用いら
れる。
Glass or metal is preferably used as the material of the device.

抽出部Aは、還流冷却器1、抽出容器2、加熱部31及び
32(31は溶剤が入れられる部分、32は加熱用装置、例え
ば加熱媒入ジャケット或いは電気ヒーターなどであ
る。)および抽出溶剤取り出しノズル41及び42(これ
は、必要に応じ上抜き、下抜きの2本、或いはどちらか
1本が取りつけられる。)から構成され、抽出溶剤取り
出しノズルには弁5が設けられており、また、還流冷却
器には冷媒導入口11及び冷媒導出口12が設けられてい
る。
The extraction unit A includes a reflux condenser 1, an extraction container 2, a heating unit 31, and
32 (31 is a portion into which a solvent is put, 32 is a heating device, for example, a heating medium containing jacket or an electric heater) and extraction solvent extraction nozzles 41 and 42 (this is a top extraction and a bottom extraction as necessary. 2 or one of them is attached.), The extraction solvent extraction nozzle is provided with a valve 5, and the reflux condenser is provided with a refrigerant inlet 11 and a refrigerant outlet 12. ing.

この抽出部Aは、還流冷却器1を取り外すことで抽出容
器2が容易に出し入れ可能な構造と成っている。
The extraction unit A has a structure in which the extraction container 2 can be easily put in and taken out by removing the reflux condenser 1.

溶剤貯槽部Bは、第1図では3種の溶剤が使用できるよ
うに貯槽61、62、63の3槽が設けられ、計量器7を経
て、導管8を通ってそれぞれ一定量の抽出溶剤が抽出部
Aに送られる。溶剤の選択、計量はそれぞれの貯槽に設
けられた弁5を開閉することによって行われる。なお、
貯槽は使用する抽出溶剤の種類に応じて適宜の個数設け
ておけばよく、3槽に限定されるものではない。
In FIG. 1, the solvent storage tank portion B is provided with three storage tanks 61, 62, and 63 so that three kinds of solvents can be used. It is sent to the extraction unit A. The solvent is selected and measured by opening and closing the valve 5 provided in each storage tank. In addition,
An appropriate number of storage tanks may be provided according to the type of extraction solvent used, and the number of storage tanks is not limited to three.

具体的には、結晶性ポリマーの抽出は以下のようにして
行われる。
Specifically, the extraction of the crystalline polymer is performed as follows.

後述の方法で結晶性ポリマーは抽出容器2に入れられ、
抽出部Aの還流冷却器1の下方にある2の位置に還流冷
却器を外してセットされる。次いで抽出溶剤抜き出しノ
ズル41、42の弁5が閉の状態で計量器7で計量された一
定量の溶剤が導管8を経て加熱部31に入れられ、加熱装
置32で加熱される。蒸発した蒸気は還流器1に冷媒を通
すことによって冷却凝縮され、凝縮した溶剤が抽出容器
2に滴下して連続的に抽出される。一定時間抽出された
後、抽出されたポリマーを含有する溶液はノズル41又は
42を用いて系外に取り出され、必要に応じ溶剤で加熱部
31が洗浄された後、次に抽出する溶剤が計量器7、導管
8を経て加熱部31に供給され、上記と同様の操作が繰り
返される。
The crystalline polymer is put in the extraction container 2 by the method described below,
The reflux condenser is removed and set at a position 2 below the reflux condenser 1 of the extraction section A. Next, with the valves 5 of the extraction solvent extraction nozzles 41 and 42 closed, a fixed amount of solvent measured by the measuring device 7 is introduced into the heating section 31 via the conduit 8 and heated by the heating device 32. The evaporated vapor is cooled and condensed by passing the refrigerant through the reflux device 1, and the condensed solvent is dropped into the extraction container 2 and continuously extracted. After being extracted for a certain period of time, the solution containing the extracted polymer is discharged from the nozzle 41 or
It is taken out of the system using 42 and heated with a solvent if necessary.
After 31 is washed, the solvent to be extracted next is supplied to the heating unit 31 via the meter 7 and the conduit 8, and the same operation as above is repeated.

抜き出されたポリマー溶液は、溶剤を溜去するか、多量
のポリマーの貧溶媒中に投入することで分離され、各種
分析に供される。
The extracted polymer solution is separated by distilling off the solvent or by pouring it into a large amount of a poor solvent for the polymer, and used for various analyses.

上述の一連の操作を例えば弁5を電磁弁としタイマーと
連動させることで、抽出溶剤の抽出部Aへの導入・取り
出しを自動化でき、また、加熱装置32の加熱量をタイマ
ーおよび温度制御器を連動させてコントロールすること
で一定条件で抽出することが可能となる。さらに、抽出
容器2の取り出し・セットを簡単なロボットに行わせる
ことにより、完全に上記一連の操作を自動化することも
可能である。
By introducing the extraction solvent to and from the extraction section A by using the valve 5 as an electromagnetic valve and interlocking with a timer in the above-mentioned series of operations, the heating amount of the heating device 32 can be controlled by a timer and a temperature controller. It is possible to extract under a certain condition by controlling in conjunction. Furthermore, it is possible to completely automate the above series of operations by causing a simple robot to take out and set the extraction container 2.

本発明の装置を有効に結晶性ポリマーの逐次抽出に利用
するのに重要な抽出容器の形状及び使用方について以下
に詳述する。
The shape and usage of the extraction container, which is important for effectively utilizing the apparatus of the present invention for the sequential extraction of crystalline polymer, will be described in detail below.

第2図に抽出容器2の一例の断面図を示す。FIG. 2 shows a sectional view of an example of the extraction container 2.

21は焼結フィルター、金網などでできたフィルターであ
り、通常円形で円筒に密着した構造であり、該フィルタ
ーは円筒にフィルター押さえ22によって脱着可能となっ
ている。勿論、融着せしめてたものでもかまわない。23
は結晶性ポリマーの溶解時に用いる回転攪拌子を示して
いる。また、24は蓋、25は蓋の押さえであり、26は被抽
出結晶性ポリマーを入れる空間である。
Reference numeral 21 is a filter made of a sintered filter, a wire mesh or the like, which is usually circular and has a structure in which it is closely attached to a cylinder, and the filter can be attached to and detached from the cylinder by a filter retainer 22. Of course, it does not matter if they are fused together. twenty three
Indicates a rotary stirrer used when the crystalline polymer is dissolved. Further, 24 is a lid, 25 is a lid retainer, and 26 is a space for containing the crystalline polymer to be extracted.

好ましい実際の使用法について以下に示す。The preferred practical use is shown below.

結晶性ポリマーは第2図に示す抽出容器2の26部分に入
れられ、次いで結晶性ポリマーを加熱下に溶解しうる溶
剤によって加熱下に実質的に溶解され、次いで冷却して
ポリマーを結晶化析出させゲル状物とする。この状態で
抽出部Aにセットして逐次抽出操作に供される。
The crystalline polymer was placed in the 26 part of the extraction vessel 2 shown in FIG. 2 and then substantially dissolved under heating by a solvent capable of dissolving the crystalline polymer under heating, followed by cooling to crystallize and precipitate the polymer. Let it be a gel. In this state, it is set in the extraction unit A and subjected to sequential extraction operation.

本発明の装置を用いて逐次抽出を適用するに好適な結晶
性ポリマーとしては、例えば沸点の異なる溶剤によって
組成の異なる成分に抽出分離が容易なポリα−オレフィ
ンが挙げられ、抽出溶剤としては沸点の異なる炭化水素
化合物或いは溶解度パラメーターの異なるハロゲン化炭
化水素、エステル類、エーテル類、ケトン類が用いら
れ、抽出は結晶性ポリマーの融点以下で行われる。
Suitable crystalline polymers for applying sequential extraction using the apparatus of the present invention include, for example, poly α-olefins that are easily extracted and separated into components having different compositions by solvents having different boiling points, and the extraction solvent has a boiling point. Different hydrocarbon compounds or halogenated hydrocarbons having different solubility parameters, esters, ethers and ketones are used, and the extraction is carried out below the melting point of the crystalline polymer.

〔実施例〕〔Example〕

以下、実施例により本発明をさらに説明する。 Hereinafter, the present invention will be further described with reference to examples.

実施例 第2図に示す形状のステンレス製容器(内径30mm、長さ
60mm、フィルター200メッシュの金網2枚重ね、下方の
蓋はテーパー付でテフロンパッキンでシールされてい
る。また、金網はネジ込み式の押さえでシールされてい
る。)に市販のプロピレンのブロック共重合体(三井東
圧化学(株)製、三井ノーブレンBJHH−G)3gを入れ、
灯油10mlを加え、130℃で攪拌処理して完全に溶解し
た。その後25℃で24時間保持してゲル状物を析出せしめ
た。
Example A stainless steel container having the shape shown in FIG. 2 (inner diameter 30 mm, length
Two wire meshes of 60 mm and filter 200 mesh are stacked, and the lower lid is tapered and sealed with Teflon packing. In addition, the wire mesh is sealed by a screw-in type presser. 3) of a commercially available propylene block copolymer (Mitsui Toatsu Chemicals, Inc., Mitsui Noblene BJHH-G),
Kerosene (10 ml) was added, and the mixture was stirred at 130 ° C to completely dissolve it. Then, the mixture was kept at 25 ° C. for 24 hours to precipitate a gel.

抽出部は内径60mm、長さ30cmのガラス製の円筒状容器で
あり、下端より10cmの位置に抽出溶剤取り出し用ノズル
が設けられてあり、そのノズルの先端は容器底より5mm
のところにある。また、下端より20cmの位置に抽出容器
2をフィルターを下にして取りつけ可能なように内側に
突起が設けられている。さらに、ガラス製の還流冷却器
とはスリ合わせで連結されている。そして、下端より15
cmの位置に溶剤貯槽部からの導管と接続されるノズルを
設けた構造となっている。溶剤貯槽としては内容積1
のガラス容器2個が用いられ、計量器は100mlのガラス
容器であり、第1図に示すようにテフロン製の管および
コックで連結した。
The extraction section is a glass cylindrical container with an inner diameter of 60 mm and a length of 30 cm.A nozzle for extracting the extraction solvent is provided at a position 10 cm from the lower end, and the tip of the nozzle is 5 mm from the container bottom.
Is there. Further, a projection is provided on the inner side at a position 20 cm from the lower end so that the extraction container 2 can be attached with the filter downward. Further, it is connected to the reflux condenser made of glass with a slot. And 15 from the bottom
It has a structure in which a nozzle connected to the conduit from the solvent storage tank is provided at the position of cm. 1 volume for solvent storage
2 glass containers were used, the weighing machine was a 100 ml glass container, and they were connected with a Teflon tube and a cock as shown in FIG.

抽出容器をセットした後、貯槽61に入れたイソペンタン
20mlを加熱部31に入れ、6時間還流抽出し、次いでノズ
ル41より抽出溶剤を取り出し、さらにイソペンタン100m
lで洗浄した。次いで貯槽62よりn−ヘプタンを加熱部3
1に導き、以下同様に抽出操作を行った。
After setting the extraction container, put isopentane in the storage tank 61.
20 ml was put into the heating part 31 and subjected to reflux extraction for 6 hours, then the extraction solvent was taken out from the nozzle 41, and further 100 m of isopentane
washed with l. Next, the n-heptane from the storage tank 62 is heated by the heating unit 3
This was led to 1, and the extraction operation was performed in the same manner as below.

得られた溶液を多量のアセトンに投入し、ポリマーを析
出分離した。イソペンタン抽出部は、抽出量8.3wt%、1
35℃テトラリン溶液の極限粘度4.65、エチレン含量40.5
wt%であり、、n−ヘプタン抽出部はそれぞれ7.8wt
%、1.08、13.2wt%であった。
The obtained solution was poured into a large amount of acetone to precipitate and separate the polymer. The isopentane extraction part has an extraction amount of 8.3 wt%, 1
Intrinsic viscosity of tetralin solution at 35 ℃ 4.65, ethylene content 40.5
wt%, and the n-heptane extraction part is 7.8 wt.
%, 1.08, 13.2 wt%.

〔発明の効果〕〔The invention's effect〕

本発明の装置は結晶性ポリマーの逐次抽出分離に好適に
利用可能であり、しかも全自動化することが可能であ
り、工業的に極めて価値がある。
INDUSTRIAL APPLICABILITY The apparatus of the present invention can be suitably used for sequential extraction and separation of crystalline polymers, and can be fully automated, which is extremely valuable industrially.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の装置の系統説明図であり、第2図は抽
出容器の1例の断面図である。
FIG. 1 is a system diagram of the apparatus of the present invention, and FIG. 2 is a sectional view of an example of an extraction container.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】抽出溶剤貯槽、該貯槽に連結された計量器
及び抽出部への導管よりなる溶剤貯槽部B、上部に還流
冷却器、還流冷却器下方に被抽出結晶性ポリマーを入れ
る少なくとも下部にフィルターを設けてなる抽出容器、
さらに下方に加熱部及び抽出溶剤の取り出し用ノズルを
設けてなる抽出部Aより構成されることを特徴とする結
晶性ポリマーの逐次抽出分離装置。
1. A solvent storage tank B comprising an extraction solvent storage tank, a meter connected to the storage tank, and a conduit to the extraction section, a reflux condenser on the upper side, and a crystalline polymer to be extracted at least on the lower side of the reflux condenser. An extraction container with a filter on the
A crystalline polymer sequential extraction / separation device, further comprising an extraction unit A having a heating unit and an extraction solvent take-out nozzle provided below.
【請求項2】抽出容器が円筒の一端に脱着可能な蓋を設
け、他端に又はその内側に円筒に密着したフィルターを
設けたものである特許請求の範囲第1項記載の結晶性ポ
リマーの逐次抽出分離装置。
2. The crystalline polymer according to claim 1, wherein the extraction container is provided with a detachable lid at one end of the cylinder and a filter closely attached to the cylinder at the other end or inside thereof. Sequential extraction and separation device.
JP61210714A 1986-09-09 1986-09-09 Sequential extraction and separation device for crystalline polymer Expired - Fee Related JPH0713085B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61210714A JPH0713085B2 (en) 1986-09-09 1986-09-09 Sequential extraction and separation device for crystalline polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61210714A JPH0713085B2 (en) 1986-09-09 1986-09-09 Sequential extraction and separation device for crystalline polymer

Publications (2)

Publication Number Publication Date
JPS6369501A JPS6369501A (en) 1988-03-29
JPH0713085B2 true JPH0713085B2 (en) 1995-02-15

Family

ID=16593884

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61210714A Expired - Fee Related JPH0713085B2 (en) 1986-09-09 1986-09-09 Sequential extraction and separation device for crystalline polymer

Country Status (1)

Country Link
JP (1) JPH0713085B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2610061B2 (en) * 1990-10-06 1997-05-14 株式会社日本ワックスポリマー開発研究所 Method for producing fractionated wax having narrow crystal melting temperature range from solid wax

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60149434A (en) * 1984-01-18 1985-08-06 Mitsui Toatsu Chem Inc Biaxially stretched polypropylene film

Also Published As

Publication number Publication date
JPS6369501A (en) 1988-03-29

Similar Documents

Publication Publication Date Title
EP0521886B1 (en) Cryogenic apparatus
NO116936B (en)
JP2003502466A (en) Method for separating a mixture of polyolefin-based compounds
JPS63269976A (en) Continuous removal of tartar and apparatus therefor
CN106279477A (en) The production method of a kind of modified PVC and process units
GB705029A (en) Improved process and device for the continuous preparation of highly polymeric compounds
US20200001201A1 (en) Resinous compound crystallization using non-polar solvent sequence
EP0681698A1 (en) Crystallization analysis fractionization
JPH0713085B2 (en) Sequential extraction and separation device for crystalline polymer
CA2372416A1 (en) Investigating different physical and/or chemical forms of materials
JPH04314706A (en) Method and apparatus for industrially fractionating polymer
CN106381226A (en) Rue extract extraction device
US4086414A (en) Steam stripping polyvinyl chloride resins
JPH0750105B2 (en) Sequential extraction separation method of crystalline polymer
US2328891A (en) Apparatus for the treatment of crude oleoresins
JP2798902B2 (en) Batch continuous extraction device
US2304610A (en) Process of washing resins
CN109126225A (en) A kind of rotational flow settlement device
CN206837571U (en) A kind of rotational flow settlement device
KR20140004144U (en) A device for preparing and transferring mixture or solution
CN214437159U (en) Refining device for collecting moisture and recovering solvent
SU963536A1 (en) Liquid dispersion separating apparatus
CA2139967A1 (en) Closed system multistage superpurification recrystallization
CN1036847C (en) Method for leaching carotene from dunaliella and the equipment thereof
CN209771430U (en) Oil-water separation treatment equipment

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees