JPS61145137A - Production of polyglycerol - Google Patents

Production of polyglycerol

Info

Publication number
JPS61145137A
JPS61145137A JP26629584A JP26629584A JPS61145137A JP S61145137 A JPS61145137 A JP S61145137A JP 26629584 A JP26629584 A JP 26629584A JP 26629584 A JP26629584 A JP 26629584A JP S61145137 A JPS61145137 A JP S61145137A
Authority
JP
Japan
Prior art keywords
acid
polyglycerol
polyglycerin
product
glycidol
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
JP26629584A
Other languages
Japanese (ja)
Other versions
JPH0469621B2 (en
Inventor
Shinzo Uda
宇田 真三
Etsuo Takemoto
竹本 悦夫
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.)
Daicel Corp
Original Assignee
Daicel Chemical Industries 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 Daicel Chemical Industries Ltd filed Critical Daicel Chemical Industries Ltd
Priority to JP26629584A priority Critical patent/JPS61145137A/en
Publication of JPS61145137A publication Critical patent/JPS61145137A/en
Publication of JPH0469621B2 publication Critical patent/JPH0469621B2/ja
Granted legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To produce a polyglycerol having light color in an easily purifiable state, by adding glycidol of a molar number corresponding to the polymerization degree of the objective compound to a carboxylic acid such as formic acid, acetic acid, etc., and hydrolyuzing and decarboxylating the addition product. CONSTITUTION:Glycidol of a molar number corresponding to the polymerization degree of the polyglycerol to be produced is added to a carboxylic acid of formula RCOOH (R is H or 1-5C alkyl) (e.g. formic acid, acetic acid, propionic acid, butyric acid, isobutyric acid, valeric acid, caproic acid, etc.), and the obtained polyglycerol carboxylate is hydrolyzed with water and then decarboxylated to obtain a polyglycerol. The product can be purified easily by neutralizing the residual carboxylic acid completely with an alkali, dehydrating and precipitating the product, adsorbing the precipitate to diatomaceous earth, etc., and filtering the adsorbed product. USE:Emulsifier for food, humectant for cosmetic, and raw material of plasticizer, surfactant, etc.

Description

【発明の詳細な説明】 本発明は、着色の少ないポリグリセリンの製造法に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing polyglycerin with little coloring.

ポリグリセリンは、食品用乳化剤、化粧品の保湿剤、可
塑剤、界面活性剤等の原料として使用されている。
Polyglycerin is used as a raw material for food emulsifiers, cosmetic moisturizers, plasticizers, surfactants, etc.

従来、ポリグリセリンは、グリセリンの蒸留残渣よりの
回収、グリセリンの脱水縮合、あるし・はエピクロルヒ
ドリンからの直接合成等により製造されているが、これ
らの方法では製造されたポリグリセリンは精製が難しく
、又、着色がはげしいこと、重合度分布が広い範囲に亘
っていること等の欠点があった。
Conventionally, polyglycerin has been produced by recovering glycerin from distillation residue, dehydration condensation of glycerin, or direct synthesis from epichlorohydrin, but polyglycerin produced by these methods is difficult to purify. Further, there were drawbacks such as severe coloring and a wide range of polymerization degree distribution.

又、グリセリンにグリシドールを付加重合させる方法で
は、一般にエポキシ基の開環触媒である水酸化アルカリ
、アミン等が使用されているが、この方法も製造された
ポリグリセリンは、精製が難しく、着色がはげしいとい
う欠点があった。
In addition, in the addition polymerization of glycidol to glycerin, alkali hydroxide, amine, etc., which are ring-opening catalysts for epoxy groups, are generally used, but polyglycerin produced by this method is also difficult to purify and tends to be colored. It had the disadvantage of being harsh.

そこで、本発明者達は着色が少なく、精製が簡単なポリ
グリセリンの製造法を確立すべく、鋭意検討した結果、
本発明を完成させるに至った。
Therefore, the inventors of the present invention conducted extensive research to establish a method for producing polyglycerin that is less colored and easier to purify.
The present invention has now been completed.

本発明は次の通りである。即ち、 l) 下記一般式穴のカルボン酸に、目的物の重合度に
相当するモル数のグリシドールを付加反応させて、ポリ
グリセリンカルボキシレートを合成し、次いで加水分解
させた後、脱カルボン酸を行うことを特徴とするポリグ
リセリンの製造法。
The present invention is as follows. That is, l) Addition reaction of glycidol in the number of moles corresponding to the degree of polymerization of the target product to the carboxylic acid in the general formula below to synthesize polyglycerol carboxylate, followed by hydrolysis, followed by decarboxylation. A method for producing polyglycerin, characterized in that:

RCOOH・・・・・・・・(A) ここで、Rは水素または炭素数1〜5個をもつアルキル
基を表わす。
RCOOH (A) Here, R represents hydrogen or an alkyl group having 1 to 5 carbon atoms.

2) 一般式穴のカルボン酸がギ酸、酢酸、プロピオン
ば、酪酸、イソ酪酸、吉草酸、カプロン酸から選ばれる
1種以上の酸であることを特徴とする特許請求の範囲第
1項記載の方法■、付加反応工程(エステル化) 使用するカルボン酸の仕込量は、得ようとするポリグリ
セリンの重合度により、グリシドールとの比率で決定さ
れる。即ち、ル量体のポリグリセリンを得ようとすれば
、カルボン版1モルに対し、グリシドールルモルが必要
である。
2) The carboxylic acid of the general formula is one or more acids selected from formic acid, acetic acid, propionic acid, butyric acid, isobutyric acid, valeric acid, and caproic acid. Method ①, Addition Reaction Step (Esterification) The amount of carboxylic acid used is determined by the ratio to glycidol depending on the degree of polymerization of the polyglycerin to be obtained. That is, in order to obtain polyglycerin in the monomeric form, 1 mol of glycidol is required for 1 mol of carbonate.

付加反応は、通常、反応器中に前記カルボ/酸を入れ、
攪拌下グリシドールを少量づつ添加する方法で行う。
The addition reaction usually involves placing the carb/acid in a reactor;
This is done by adding glycidol little by little while stirring.

反応温度はグリシドールの添加量が所定量の%までは8
0〜IIQ”Cとし、その後110〜230℃、好まし
くは120〜140”Cで行う。
The reaction temperature is 8% until the amount of glycidol added is a specified amount.
0 to IIQ"C, and then at 110 to 230"C, preferably 120 to 140"C.

前段に反応温度を110’C以上にすると製品ポリグリ
セリンの着色がひどく、又、80℃以下では反応速度が
遅い。後段の反応温度が110℃未満では、ジグリセリ
ン等が増加し、重合度が広範囲になり、又230 ”C
を越えるとグリシドールの分解により副反応を起し、好
ましくない。
If the reaction temperature is 110'C or higher in the first stage, the product polyglycerin will be severely colored, and if it is 80C or lower, the reaction rate will be slow. If the reaction temperature in the latter stage is less than 110°C, diglycerin etc. will increase, the degree of polymerization will range over a wide range, and the temperature will exceed 230"C.
If it exceeds this amount, side reactions occur due to decomposition of glycidol, which is not preferable.

反応終了は、グリシドールの転化率が99%以上で判断
される。又、触媒としてリン酸等の酸触媒を添加すれば
更に反応速度を上げることができる。
The completion of the reaction is judged when the conversion rate of glycidol is 99% or more. Furthermore, the reaction rate can be further increased by adding an acid catalyst such as phosphoric acid as a catalyst.

■、加水分解工程(脱カルボンば) 加水分解は、通常、次いで該ポリグリセリンカルボキシ
レートに水を加えて、加水分解した後、減圧処理にて水
及びカルボン酸を留出する方法で行う。
(2) Hydrolysis step (decarboxylation) Hydrolysis is usually carried out by adding water to the polyglycerol carboxylate, hydrolyzing it, and then distilling water and carboxylic acid off under reduced pressure.

水添加量は中間体に対し、05〜2.0重量部であり、
又、反応温度は100〜120’C1時間は3〜5時間
時間が適当である。
The amount of water added is 0.5 to 2.0 parts by weight based on the intermediate,
Further, the reaction temperature is 100 to 120°C, and the appropriate time for 1 hour is 3 to 5 hours.

又、こ−れらの反応は窒素ガス等不活性ガス下で行うこ
とが好ましく、必要に応じて加圧してもよい。
Further, these reactions are preferably carried out under an inert gas such as nitrogen gas, and may be pressurized if necessary.

斯様にして得られた生成物は、残留カルボン酸をアルカ
リにて完全中和し、脱水析出後、析出物を珪藻上等に吸
着させて戸別することにより、簡単に精製することがで
き、目的物ポリグリセリンは非常に着色が少な(、目的
に適ったより高重合度である。しかし、目的によって製
品ポリグリセリンにポリグリセリンカルボン酸エステル
が混在しても問題ない場合は、精製する必要はない。
The product thus obtained can be easily purified by completely neutralizing the residual carboxylic acid with an alkali, dehydrating and precipitating the product, adsorbing the precipitate onto diatoms, etc., and distributing it from house to house. The target polyglycerin has very little coloration (and has a higher degree of polymerization than is suitable for the purpose. However, depending on the purpose, there is no need to purify it if there is no problem with the mixture of polyglycerin carboxylic acid esters in the product polyglycerin. .

本発明によれば、カルボ/酸を土台とした上で、グリシ
ドールのみの添加によって目的物ポリグリセリンの1合
度を決め、さらに中間体、ポリグリセリンカルボキシレ
ートを経ることによって悪い影響物質を消すことができ
る。
According to the present invention, it is possible to determine the concentration of the target polyglycerin by adding only glycidol on the basis of carb/acid, and further to eliminate harmful substances by passing through the intermediate polyglycerin carboxylate. can.

次に、本発明を例をあげて説明するが、これらによって
本発明を限定するものではない。
Next, the present invention will be explained by giving examples, but the present invention is not limited to these.

実施例1゜ 500dの攪拌機付フラスコに、42grの酢酸(0,
7mol )をとり、窒素ガスで置換して、攪拌しなが
ら昇温し、90’Cで3時間、その後徐々に昇温し13
0℃で2.5時間、合計5.5時間で311grのグリ
シドール(4,2mol ) 全滴下した。さらに2時
間上記温度に保った。
Example 1 42g of acetic acid (0,
7 mol) was replaced with nitrogen gas, heated to 90'C for 3 hours with stirring, and then gradually heated to 13
All of 311 gr of glycidol (4.2 mol) was added dropwise at 0°C for 2.5 hours, for a total of 5.5 hours. The temperature was maintained for an additional 2 hours.

次いで、i o o ℃に冷却して、170gr+7)
水を加え、3.5時間攪拌し、加水分解させた後、水及
び酢酸を減圧にて除去したところ、粗製ポリグリセリン
339grが得られ、その色相は、はとんど無色透明で
、ガードナー1以下であった。
Then cooled to io o °C to 170 gr + 7)
After adding water and stirring for 3.5 hours to cause hydrolysis, water and acetic acid were removed under reduced pressure to obtain 339g of crude polyglycerin, which was mostly colorless and transparent, Gardner 1 It was below.

次に、上記粗製ポリグリセリン200grをとり、10
%水酸化す) IJウム水溶液35grを加えて90℃
で1時間攪拌した後、20〜5 Torr100〜11
0℃で脱水した。90°Cに冷却して、吸着剤として0
.16 g rの珪藻土を加え、1時間攪拌した後、濾
過して190grの精製ポリグリセリンを得た。その色
相は殆んど無色透明でガードナー1以下、ヒドロキシル
価966、平均重合度6であった。
Next, take 200g of the above crude polyglycerin and
% hydroxide) Add 35g of IJum aqueous solution and heat at 90°C.
After stirring for 1 hour at 20-5 Torr100-11
Dehydrated at 0°C. Cool to 90°C and remove as adsorbent.
.. After adding 16 g of diatomaceous earth and stirring for 1 hour, it was filtered to obtain 190 g of purified polyglycerin. The hue was almost colorless and transparent, Gardner was less than 1, the hydroxyl value was 966, and the average degree of polymerization was 6.

比較例 50071!/攪拌機付きフラスコに、9.2 g r
 (1,0mol )のグリセリンと2.4grの50
%水酸化ナトリウム水溶液をとり、窒素ガスで置換し9
0℃に加熱攪拌しながら、減圧下で脱水を行った。
Comparative example 50071! / In a flask with a stirrer, 9.2 g r
(1,0 mol) of glycerin and 2.4 gr of 50
Take a % sodium hydroxide aqueous solution and replace it with nitrogen gas.
Dehydration was performed under reduced pressure while heating and stirring at 0°C.

続いて、115℃〜125℃に保ち、370gr(5,
0mol)のグリシドールを3時間で画工した。さらに
2時間上記温度に保った後、未反応のグリシドールを減
圧にて除去したところ、粗製ポリグリセリン456gr
を得た。その色相は淡褐色で、ガードナー8であった。
Subsequently, the temperature was maintained at 115°C to 125°C and 370gr (5,
0 mol) of glycidol was used in 3 hours. After keeping the above temperature for another 2 hours, unreacted glycidol was removed under reduced pressure, resulting in 456g of crude polyglycerin.
I got it. Its hue was light brown and Gardner 8.

次に、上記粗製ポリグリセリンに10%酢酸水溶液25
grを加え、80℃〜90℃に加熱して1時間攪拌した
後、10〜5 Torr、  110℃〜120℃で1
時間脱水した。90℃に冷却して、吸着剤として0.2
grの珪藻土を加え、1時間攪拌した後、濾過して33
4grの精製ポリグリセリンを得た。その色相は淡褐色
で、ガードナー7、ヒドロキシル価965、平均重合度
6であった。
Next, add 25% of a 10% acetic acid aqueous solution to the above crude polyglycerin.
gr, heated to 80°C to 90°C and stirred for 1 hour, then heated at 10 to 5 Torr and 110°C to 120°C for 1 hour.
Dehydrated for hours. Cool to 90°C and use as an adsorbent for 0.2
Add gr of diatomaceous earth, stir for 1 hour, and filter.
4 gr of purified polyglycerin was obtained. Its hue was light brown, Gardner was 7, hydroxyl value was 965, and average degree of polymerization was 6.

実施例2゜ 61.6grの酪酸(0,7mol)を使用した以外、
実施例1と同様に反応させ、精製した。
Example 2: Except for using 61.6 gr of butyric acid (0.7 mol),
It was reacted and purified in the same manner as in Example 1.

得られた精製ポリグリセリン190grの色相は殆んど
無色透明で、ガードナー1以下、ヒト゛しキシル価96
4、平均重合度6であった。
The hue of the obtained purified polyglycerin 190g is almost colorless and transparent, Gardner is less than 1, and the human xyl value is 96.
4, average degree of polymerization was 6.

Claims (1)

【特許請求の範囲】 1)下記一般式(A)のカルボン酸に、目的物の重合度
に相当するモル数のグリシドール を付加反応させて、ポリグリセリンカルボ キシレートを合成し、次いで加水分解させ た後、脱カルボン酸を行うことを特徴とす るポリグリセリンの製造法。 RCOOH・・・(A) ここで、Rは水素または炭素数1〜5個を もつアルキル基を表わす。 2)一般式(A)のカルボン酸が、ギ酸、酢酸、プロピ
オン酸、酪酸、イソ酪酸、吉草酸、 カプロン酸から選ばれる1種以上の酸であ ることを特徴とする特許請求の範囲第1項 記載の方法。
[Claims] 1) Polyglycerin carboxylate was synthesized by adding glycidol in a molar number corresponding to the degree of polymerization of the target product to a carboxylic acid represented by the following general formula (A), and then hydrolyzed. A method for producing polyglycerin, which is then subjected to decarboxylation. RCOOH...(A) Here, R represents hydrogen or an alkyl group having 1 to 5 carbon atoms. 2) Claim 1, wherein the carboxylic acid of general formula (A) is one or more acids selected from formic acid, acetic acid, propionic acid, butyric acid, isobutyric acid, valeric acid, and caproic acid. The method described in section.
JP26629584A 1984-12-19 1984-12-19 Production of polyglycerol Granted JPS61145137A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26629584A JPS61145137A (en) 1984-12-19 1984-12-19 Production of polyglycerol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26629584A JPS61145137A (en) 1984-12-19 1984-12-19 Production of polyglycerol

Publications (2)

Publication Number Publication Date
JPS61145137A true JPS61145137A (en) 1986-07-02
JPH0469621B2 JPH0469621B2 (en) 1992-11-06

Family

ID=17428956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26629584A Granted JPS61145137A (en) 1984-12-19 1984-12-19 Production of polyglycerol

Country Status (1)

Country Link
JP (1) JPS61145137A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0758641B1 (en) 1995-08-11 2000-08-30 Daicel Chemical Industries, Ltd. A fatty acid esters composition of a polyglycerine, a process for the preparation thereof, a process for the preparation of a highly-purified fatty acid esters composition of a polyglycerine, a highly-purified fatty acid esters composition of a polyglycerine, an additive for food-stuffs, a resin composition, and a composition for cosmetics or detergents

Also Published As

Publication number Publication date
JPH0469621B2 (en) 1992-11-06

Similar Documents

Publication Publication Date Title
JP4977353B2 (en) Cyclobutanetetracarboxylate compound and process for producing the same
JPH051291B2 (en)
JPS58198429A (en) Preparation of polyglycerol
EP0028234A1 (en) An improved process for the manufacture of levulinic acid and esters
JPS61140534A (en) Production of polyglycerol
EP0044510B1 (en) Process for the preparation of diaryl esters
JPS61145137A (en) Production of polyglycerol
JP3057876B2 (en) Preparation of biphenyltetracarboxylic dianhydride
JPH11130728A (en) Production of mono-tertiary-alkyl ester of malonic acid
US4475004A (en) Preparation of alkanediols
CN1270158A (en) Process for preparing antimony compound of binary alcohol
JP2001354618A (en) Method for producing di-tert-butyl 1, 3- adamantanedicarboxylate
JPS62263195A (en) Production of pentaacetylarubutin
JPS6118543B2 (en)
JPH06211744A (en) Production of high-purity dimethyl 4,4'-biphenyldicarboxylate
JPH0410465B2 (en)
JPH0454177A (en) Production of gamma-alkyl-gamma-lactone
KR930003892B1 (en) Poly vinyl chloride copolymer introduced thio alkanoic ester and process thereof
SU598567A3 (en) Method of preparing diethylphthalimidophosphate
SU571478A1 (en) Method of preparing bis-(b-oxyethyl)-terephtalate
JPS58144353A (en) Preparation of trans-4-carboxamidocyclohexane-1- carboxylic acid
SU595300A1 (en) Method of preparing cyanbenzoic acids
JPS61215621A (en) Production of polytetramethylene ether glycol
SU1177300A1 (en) Method of producing 2-methyl-3-acetyl-5-phenyl-4,5-dihydrofuran
JPS6366304B2 (en)