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JPH0662490B2 - Separation of oil and water layers - Google Patents
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JPH0662490B2 - Separation of oil and water layers - Google Patents

Separation of oil and water layers

Info

Publication number
JPH0662490B2
JPH0662490B2 JP62048700A JP4870087A JPH0662490B2 JP H0662490 B2 JPH0662490 B2 JP H0662490B2 JP 62048700 A JP62048700 A JP 62048700A JP 4870087 A JP4870087 A JP 4870087A JP H0662490 B2 JPH0662490 B2 JP H0662490B2
Authority
JP
Japan
Prior art keywords
methacrylic acid
aqueous
separation
oil
layer
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
JP62048700A
Other languages
Japanese (ja)
Other versions
JPS63216840A (en
Inventor
範和 吉田
儀昭 木村
進 松本
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.)
Nippon Kayaku Co Ltd
Original Assignee
Nippon Kayaku 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 Kayaku Co Ltd filed Critical Nippon Kayaku Co Ltd
Priority to JP62048700A priority Critical patent/JPH0662490B2/en
Publication of JPS63216840A publication Critical patent/JPS63216840A/en
Publication of JPH0662490B2 publication Critical patent/JPH0662490B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はメタクリル酸水溶液から有機溶媒にてメタクリ
ル酸を抽出する際に、油層と水層との分離速度を速め又
はエマルジョンの生成を防止して抽出操作を容易にする
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention accelerates the separation rate between an oil layer and an aqueous layer or prevents the formation of an emulsion when methacrylic acid is extracted from an aqueous methacrylic acid solution with an organic solvent. And a method for facilitating the extraction operation.

(従来の技術) 従来メタクリル酸を含む水溶液からメタクリル酸を溶媒
にて抽出する時、油層と水層との分離が悪く、著しい時
はエマルジョンが生成して抽出塔が運転不能になること
がある。
(Prior Art) When extracting methacrylic acid from a conventional aqueous solution containing methacrylic acid with a solvent, the separation of the oil layer and the aqueous layer is poor, and when it is remarkable, an emulsion may be formed and the extraction tower may become inoperable. .

これを防止する一般的対策としては(1)塩の添加(特公
昭49−36209)、(2)陽イオン界面活性剤の添加
(特開昭54−66617)、(3)操作温度の上昇等が
ある。
As a general measure to prevent this, (1) addition of salt (Japanese Patent Publication No. 49-36209), (2) addition of cationic surfactant (JP-A-54-66617), (3) increase in operating temperature, etc. There is.

(発明が解決しようとする問題点) しかしながらこれらの方法は不利な点も有しており、充
分満足な結果を提供するものではない。塩添加の方法に
ついては、添加量が多い(0.1〜5%)と同時に、重
合ロスを生じやすい。陽イオン界面活性剤の添加は、析
出した固形物が塔内に付着して安定運転を妨げやすい。
操作温度の上昇は二層間の相互溶解度を増加させその結
果抽出成績を下げることになりやすい。いずれにしても
多くの問題点を有し、根本的な解決には至ってない。
(Problems to be Solved by the Invention) However, these methods also have disadvantages and do not provide sufficiently satisfactory results. Regarding the method of salt addition, the addition amount is large (0.1 to 5%), and at the same time, polymerization loss is likely to occur. The addition of the cationic surfactant tends to hinder stable operation because the precipitated solid matter adheres to the inside of the tower.
Increasing the operating temperature tends to increase the mutual solubility between the two layers and consequently lower the extraction performance. In any case, there are many problems and no fundamental solution has been reached.

(問題点を解決する為の手段) 本発明者らはかかる問題を解決するために鋭意検討した
結果、抽出時に脂肪酸エステル系又はポリアルキレング
リコール系の消泡剤を添加することにより油層と水層と
の分離速度を速め又はエマルジョン生成を防止できるこ
とを見出して本発明を完成した。
(Means for Solving Problems) As a result of intensive investigations by the present inventors in order to solve such problems, as a result, an oil layer and an aqueous layer were obtained by adding a fatty acid ester-based or polyalkylene glycol-based defoaming agent during extraction. The present invention has been completed by finding that it is possible to speed up the separation rate from or to prevent emulsion formation.

本発明は炭素数4の化合物を気相接触酸化して得られる
メタクリル酸水溶液から有機溶媒を用いてメタクリル酸
の抽出を行う際に脂肪酸エステル系又はポリアルキレン
グリコール系の消泡剤を添加することを特徴とする油層
と水層の分離法であり、この消泡剤を添加することによ
り油層と水層との分離速度が速くなり又はエマルジョン
の生成を防止することが出来る。
The present invention adds a fatty acid ester-based or polyalkylene glycol-based defoaming agent when extracting methacrylic acid from an aqueous methacrylic acid solution obtained by vapor-phase catalytic oxidation of a compound having 4 carbon atoms using an organic solvent. The method for separating an oil layer and an aqueous layer is characterized by adding the antifoaming agent to increase the separation speed between the oil layer and the aqueous layer or prevent the formation of an emulsion.

イソブチレン、t−ブタノール、イソブチルアルデヒド
又はメタクロレインの気相接触酸化反応により得られる
メタクリル酸水溶液中にはメタクロレイン及び/又はメ
タクリル酸から生成した重合物が溶解している。その量
はプロセスによって当然異なるが、通常はメタクリル酸
に対して0.1〜5重量%である。このメタクリル酸水
溶液からメタクリル酸を分離するため、有機溶媒による
抽出が通常行われる。この際、メタクリル酸の抽出が進
行するに伴い水層及び油層の中に溶解しきれなくなった
重合物は二層の界面その他の個所に析出してくる。析出
した重合物(以下スカムと略称する)は適度の粘着性を
有しており、従って抽出操作において油層と水層が接触
し終えた時に両層の分離を妨げたり、場合によってはエ
マルジョンが生成する。そこで本発明者らはこの問題解
決のため種々実験的検討を行った結果、メタクリル酸の
抽出操作時に、脂肪酸エステル系又はポリアルキレング
リコール系の消泡剤を添加することにより、油層と水層
との分離速度を速め又はエマルジョンの生成を防止する
ことを可能にした。
A polymer produced from methacrolein and / or methacrylic acid is dissolved in an aqueous solution of methacrylic acid obtained by a gas phase catalytic oxidation reaction of isobutylene, t-butanol, isobutyraldehyde or methacrolein. The amount naturally varies depending on the process, but is usually 0.1 to 5% by weight based on methacrylic acid. In order to separate methacrylic acid from this methacrylic acid aqueous solution, extraction with an organic solvent is usually performed. At this time, as the extraction of methacrylic acid progresses, the polymer that cannot be completely dissolved in the water layer and the oil layer is deposited at the interface between the two layers and other places. The deposited polymer (hereinafter referred to as scum) has an appropriate tackiness, and therefore, when the oil layer and the water layer are completely in contact with each other during the extraction operation, the separation of the two layers may be hindered or an emulsion may be formed in some cases. To do. Therefore, as a result of various experimental studies to solve this problem, the present inventors have found that an oil layer and a water layer can be formed by adding a fatty acid ester-based or polyalkylene glycol-based defoaming agent during the extraction operation of methacrylic acid. It was possible to speed up the separation rate of or to prevent the formation of emulsions.

本発明で使用される有機溶媒としては、公知のものはい
ずれも使用でき、特に限定されない。例えば、ヘキサ
ン、ヘプタン、オクタン、リグロイン、シクロヘキサ
ン、ベンゼン、トルエン、キシレン等の脂肪族、脂環
式、芳香族炭化水素、酢酸エチル、酢酸イソプロピル、
酢酸ブチル、メチルエチルケトン、メチルイソブチルケ
トン、ジイソプロピルエーテル等のエステル、ケトン、
エーテル等が使用できる。
As the organic solvent used in the present invention, any known organic solvent can be used and is not particularly limited. For example, hexane, heptane, octane, ligroin, cyclohexane, benzene, toluene, xylene and other aliphatic, alicyclic, aromatic hydrocarbons, ethyl acetate, isopropyl acetate,
Esters, ketones such as butyl acetate, methyl ethyl ketone, methyl isobutyl ketone, diisopropyl ether,
Ether or the like can be used.

本発明で使用されるポリアルキレングリコール系消泡剤
としては、ニッサンディスホームCC−118(日本油
脂(株)、平均分子量1800、分子量分布1200〜3
000)、PEG400(平均分子量400)等がある
が、これに限定されるものではない。
As the polyalkylene glycol antifoaming agent used in the present invention, Nissan Dishome CC-118 (NOF CORPORATION, average molecular weight 1800, molecular weight distribution 1200 to 3)
000), PEG 400 (average molecular weight 400) and the like, but are not limited thereto.

消泡剤の添加量はメタクリル酸水溶液の性状により左右
されるが、メタクリル酸水溶液中に5〜500ppm加
えるのが好ましく、10〜100ppm加えるのが特に
好ましい。
The addition amount of the defoaming agent depends on the properties of the methacrylic acid aqueous solution, but it is preferably 5 to 500 ppm, and particularly preferably 10 to 100 ppm, in the methacrylic acid aqueous solution.

添加方法は、抽出塔に送入される前工程のメタクリル酸
水溶液に対し、いずれの場所で添加してもよく、又、抽
出塔に直接添加してもよく、特にこだわらない。
The addition method is not particularly limited, and may be added at any place to the methacrylic acid aqueous solution of the previous step fed into the extraction tower, or may be added directly to the extraction tower.

(実施例) 次に実施例をあげて本発明を具体的に説明する。(Example) Next, the present invention will be specifically described with reference to examples.

実施例1 リン−モリブデン系の酸化触媒を用いてメタクロレイン
を気相接触酸化して得られたメタクリル酸水溶液を用い
て次の実験を行なった。
Example 1 The following experiment was conducted using an aqueous methacrylic acid solution obtained by subjecting methacrolein to gas phase catalytic oxidation using a phosphorus-molybdenum-based oxidation catalyst.

この水溶液の組成は次の通りである。The composition of this aqueous solution is as follows.

メタクリル酸 26wt% 酢 酸 5wt% ポリマー等不揮発成分 0.3wt% 水分、その他 68.7wt% 500mlの分液ロートにメタクリル水溶液100gをとり、こ
れに表1に示す量の消泡剤を添加し、これに溶媒として
ヘプタン100gを加えて30秒間強く撹拌し、静置してか
ら二層が分離するまでの時間を測定した。
Methacrylic acid 26 wt% Acetic acid 5 wt% Non-volatile components such as polymer 0.3 wt% Water, other 68.7 wt% Take a 100 ml methacrylic aqueous solution in a 500 ml separating funnel, and add the defoamer in the amount shown in Table 1 to it. To this, 100 g of heptane was added as a solvent, vigorously stirred for 30 seconds, and the time from the standing to the separation of the two layers was measured.

比較のため、シリコン系消泡剤についてもテストした。
結果は表1の通りであり、本発明の消泡剤の効果が確認
された。
For comparison, a silicone antifoam was also tested.
The results are shown in Table 1, and the effect of the defoaming agent of the present invention was confirmed.

実施例2 実施例1と同じメタクリル酸水溶液について、消泡剤と
してニッサンディスホームCC−118を添加し、表2
に示した有機溶媒を用いて実施例1と同様に実験を行な
った。
Example 2 With respect to the same aqueous methacrylic acid solution as in Example 1, Nissan Dishome CC-118 was added as an antifoaming agent, and Table 2
An experiment was conducted in the same manner as in Example 1 using the organic solvent shown in.

結果は表2の通り。消泡剤の効果は、有機溶媒の種類に
はほとんど無関係とみなせた。
The results are shown in Table 2. The effect of the defoamer could be regarded as almost independent of the type of organic solvent.

(発明の効果) 本発明によればメタクリル酸水溶液から有機溶媒を用い
てメタクリル酸を抽出する際に油層と水層の分離速度が
早くなり、エマルジョンの生成が防止できる。
(Effects of the Invention) According to the present invention, when methacrylic acid is extracted from an aqueous methacrylic acid solution using an organic solvent, the separation rate between the oil layer and the aqueous layer is increased, and the formation of an emulsion can be prevented.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】炭素数4の化合物を気相接触酸化して得ら
れるメタクリル酸水溶液から有機溶媒を用いてメタクリ
ル酸の抽出を行う際に、ポリアルキレングリコール系の
消泡剤をメタクリル酸水溶液中に5〜500ppmとな
るよう添加することを特徴とする油層と水層の分離法。
1. When a methacrylic acid is extracted from an aqueous methacrylic acid solution obtained by vapor-phase catalytic oxidation of a compound having 4 carbon atoms using an organic solvent, a polyalkylene glycol antifoaming agent is used in the aqueous methacrylic acid solution. The method for separating an oil layer and an aqueous layer is characterized by adding 5 to 500 ppm.
JP62048700A 1987-03-05 1987-03-05 Separation of oil and water layers Expired - Lifetime JPH0662490B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62048700A JPH0662490B2 (en) 1987-03-05 1987-03-05 Separation of oil and water layers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62048700A JPH0662490B2 (en) 1987-03-05 1987-03-05 Separation of oil and water layers

Publications (2)

Publication Number Publication Date
JPS63216840A JPS63216840A (en) 1988-09-09
JPH0662490B2 true JPH0662490B2 (en) 1994-08-17

Family

ID=12810583

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62048700A Expired - Lifetime JPH0662490B2 (en) 1987-03-05 1987-03-05 Separation of oil and water layers

Country Status (1)

Country Link
JP (1) JPH0662490B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5899433A (en) * 1981-12-09 1983-06-13 Nippon Shokubai Kagaku Kogyo Co Ltd Purification of methacrylic acid

Also Published As

Publication number Publication date
JPS63216840A (en) 1988-09-09

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