JPH0324071A - Purification of cyclic acetal - Google Patents

Purification of cyclic acetal

Info

Publication number
JPH0324071A
JPH0324071A JP15872889A JP15872889A JPH0324071A JP H0324071 A JPH0324071 A JP H0324071A JP 15872889 A JP15872889 A JP 15872889A JP 15872889 A JP15872889 A JP 15872889A JP H0324071 A JPH0324071 A JP H0324071A
Authority
JP
Japan
Prior art keywords
crude
acetal
solid
cyclic acetal
cyclic acetals
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.)
Pending
Application number
JP15872889A
Other languages
Japanese (ja)
Inventor
Kensho Nakagawa
中川 憲昭
Motoyuki Suzuki
基之 鈴木
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.)
Sanyo Chemical Industries Ltd
Original Assignee
Sanyo 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 Sanyo Chemical Industries Ltd filed Critical Sanyo Chemical Industries Ltd
Priority to JP15872889A priority Critical patent/JPH0324071A/en
Publication of JPH0324071A publication Critical patent/JPH0324071A/en
Pending legal-status Critical Current

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  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Abstract

PURPOSE:To purify a cyclic acetal in high purity by treating crude cyclic acetal with aqueous alkali and/or solid alkali hydroxide to remove the impurities which remain in the crude acetal and can be removed only with very difficulty through conventional processes simply in high efficiency. CONSTITUTION:Crude acetal is treated with an aqueous alkali of 50 to 70% concentration such as an aqueous solution of NaOH, KOH, Ca(OH)<2> and/or solid alkali hydroxide such as solid, granular or powdery NaOH, KOH, Ca(OH)2, preferably with an aqueous alkali followed by with solid alkali hydroxide to remove water, glycols, methanol, aldehydes or their polymers and other impurities in high efficiency to give cyclic acetal of high purity, which is used as an electrolyte solvent for electric cells.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は環状アセタール類の精製法に関するものである
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for purifying cyclic acetals.

[従来の技術] 従来、環状アセタール類の精製法としては、粗アセター
ル類にモレキュラーシーブ,無水ボウ硝等を加え脱水し
た後蒸留するという方法が知られている。
[Prior Art] Conventionally, as a method for purifying cyclic acetals, a method is known in which molecular sieves, anhydrous sulfur salt, etc. are added to crude acetals, the mixture is dehydrated, and then distilled.

[9.明が解決しようとする課題] しかしながら,従来の方法で組環状アセタール類を精製
するにはグリコール類,メタノール,アルデヒド類およ
びその重合物などの不純物の除去が困難で、高純度のも
のが得にくいという欠点を有するので、fIn車で効率
の良い精製法が望まれている。
[9. [Problems that Ming is trying to solve] However, when purifying assembled cyclic acetals using conventional methods, it is difficult to remove impurities such as glycols, methanol, aldehydes, and their polymers, making it difficult to obtain highly pure products. Therefore, an efficient refining method using fIn vehicles is desired.

[課題を解決するための手段] 本発明者らは上記問題点のない環状アセタール類の精製
法に関して鋭意検討した結果、本発明に到達した。
[Means for Solving the Problems] The present inventors have arrived at the present invention as a result of intensive studies on a method for purifying cyclic acetals that does not have the above-mentioned problems.

すなわち、本発明は粗環状アセタール類をアルカリ水溶
液および/または固型水酸化アルカリ化合物で処理する
ことを特徴とする環状アセタール類の右1製法である。
That is, the present invention is a method for producing cyclic acetals, which is characterized in that crude cyclic acetals are treated with an aqueous alkali solution and/or a solid alkali hydroxide compound.

本発明の環状アセタール類の鞘製法に用いられるアルカ
リ水溶液は例えば水酸化ナトリウム,水酸化カリウム,
水酸化カルシウムの水溶液等があげられる。水溶液の濃
度は好ましくは50〜70%である。
The alkaline aqueous solution used in the method for producing cyclic acetal sheaths of the present invention includes, for example, sodium hydroxide, potassium hydroxide,
Examples include aqueous solutions of calcium hydroxide. The concentration of the aqueous solution is preferably 50-70%.

固型水酸化アルカリ化合物は例えば水酸化ナトリウム,
水酸化カリウム,水酸化カルシウム等の固状,顆粒状,
粉末状物があげられる。
Solid alkali hydroxide compounds include, for example, sodium hydroxide,
Solid, granular, etc. potassium hydroxide, calcium hydroxide, etc.
Powdered products are available.

粗環状アセタール類をアルカリ水溶液で処理する方法は
粗環状アセタール類に50〜70%のアルカリ水溶液を
任意の割合で加え0.  1〜2時間攪拌後分液により
アルカリ水溶液を除去する。
The method of treating crude cyclic acetals with an aqueous alkaline solution is to add an aqueous alkali solution of 50 to 70% to the crude cyclic acetals in any proportion. After stirring for 1 to 2 hours, the alkaline aqueous solution is removed by liquid separation.

粗環状アセタール類とアルカリ水溶液の重量割合は好ま
しくは3: 1〜1: 3である。
The weight ratio of the crude cyclic acetals to the aqueous alkali solution is preferably 3:1 to 1:3.

粗環状アセタール類を固型水酸化アルカリ化合物で処理
する方法としては粗環状アセタール類をそのままか,ま
たはアルカリ水溶液で処理した後,固型水酸化アルカリ
化合物を任意の割合で加え0.l〜5時間撹拌後水酸化
アルカリを除去する方法がある。
A method for treating crude cyclic acetals with a solid alkali hydroxide compound is to treat the crude cyclic acetals as they are or with an aqueous alkali solution, and then add a solid alkali hydroxide compound in any proportion. There is a method of removing alkali hydroxide after stirring for 1 to 5 hours.

粗環状アセタール類はグリコール類とアルデヒド類を硫
酸等の触媒の存在下に,加熱撹拌し留出させて製造する
ことができる。
Crude cyclic acetals can be produced by heating, stirring, and distilling glycols and aldehydes in the presence of a catalyst such as sulfuric acid.

環状アセタール類の製造に使用されるグリコール類は例
えば脂肪族または脂環式グリコールなどが仙川される。
Glycols used in the production of cyclic acetals include, for example, aliphatic or alicyclic glycols.

脂肋放グリコールとしては例えばエチレングリコール,
プロピレングリコール,トリメチレングリコール, 1
●3−ブタンジオーノレ,1●2−ベンタンジオール,
1●2−ヘキサンジオール, 1●2−へブタンジオー
ル, 1●2−オクタンジオール,脂環式グリコールと
しては例えばシクロペンタン−1●2−ジオーノレ,シ
クロヘキサン−1●2−ジオーノレなどがあげられる。
Examples of fatty glycols include ethylene glycol,
Propylene glycol, trimethylene glycol, 1
●3-butanediol, 1●2-bentanediol,
Examples of the alicyclic glycols include 1●2-hexanediol, 1●2-hebutanediol, 1●2-octanediol, and alicyclic glycols such as cyclopentane-1●2-dionole and cyclohexane-1●2-dionole.

アルデヒド類としては例えば脂肪族,芳香族または複素
環式アルデヒドが使用される。脂肪族アルデヒドとして
は例えばホルムアルデヒド,パラホルムアルデヒド,ア
セトアルデヒド,プロピオンアルデヒド,プチルアルデ
ヒP,インブチルアルデヒド,芳香族アルデヒドとして
は例えばベンズアルデヒド,サリチルアルデヒドなどが
あげられる。複素環式アルデヒドとしては例えばフルフ
ラールなどがあげられる。
As aldehydes, for example aliphatic, aromatic or heterocyclic aldehydes are used. Examples of aliphatic aldehydes include formaldehyde, paraformaldehyde, acetaldehyde, propionaldehyde, butyraldehyde P, and inbutyraldehyde, and examples of aromatic aldehydes include benzaldehyde and salicylaldehyde. Examples of the heterocyclic aldehyde include furfural.

触媒としては例えば塩酸、硫酸、硝酸、りん酸、パラト
ルエンスルホン酸などの酸,イオン交換樹脂例えばアン
バーライト124(住友化学)々どがあげられる。
Examples of the catalyst include acids such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, and para-toluenesulfonic acid, and ion exchange resins such as Amberlite 124 (Sumitomo Chemical).

環状アセタール類の製造方法は,例えば,反応器にグリ
コール類とアルデヒド類をモル比で,好ましくは3: 
1〜1: 1の割合で仕込み,硫酸等の触媒をグリコー
ル類とアルデヒド類の合計重mの3〜10%加え,#j
l拌下に,環状アセタール類の沸点より高い温度に加熱
し留出させて製造することが出来る。
The method for producing cyclic acetals includes, for example, adding glycols and aldehydes to a reactor at a molar ratio of preferably 3:
Prepare at a ratio of 1 to 1: 1, add a catalyst such as sulfuric acid in an amount of 3 to 10% of the total weight m of glycols and aldehydes, and add #j
It can be produced by distilling the cyclic acetal by heating it to a temperature higher than the boiling point of the cyclic acetal while stirring.

[実施例コ 以下、実施例により本発明を更に説明するが、本発明は
これに限定されるものではない。以下において、部およ
び%はそれぞれ重ffi部および重m%を示す。
[Example] Hereinafter, the present invention will be further explained with reference to Examples, but the present invention is not limited thereto. In the following, parts and % indicate parts by weight and m% by weight, respectively.

製造例1 環状アセタール製造例として次のような1.3−ジオキ
ソランの製造法があげられる。
Production Example 1 An example of producing a cyclic acetal is the following method for producing 1,3-dioxolane.

撹拌機、温度計、窒素吹込み管、冷却取り出し管を装着
した2Lの4ツロコルベンにエヂレングリコール298
g(4.8モル),バラホルムアルデヒド120g(4
モル),硫酸(97%)11gを加え撹拌●昇温を開始
した。too”cに昇温したところで凝縮物取り出し管
から無色透明液状の粗1,3−ジオキソランの留出が開
始した。以後昇温を続け353gが出終わるまでに6時
間を要した。
Ethylene glycol 298 in a 2L 4-turocolben equipped with a stirrer, thermometer, nitrogen inlet tube, and cooling takeout tube.
g (4.8 mol), rose formaldehyde 120 g (4.8 mol),
mol) and 11 g of sulfuric acid (97%) were added, and stirring and heating were started. When the temperature was raised to too''c, distillation of crude 1,3-dioxolane in the form of a colorless transparent liquid started from the condensate extraction tube.The temperature continued to rise after that, and it took 6 hours until 353 g had finished coming out.

実施例1 製造例1のようにして製造したifl1.3−ジオキソ
ラン1.12gを,撹拌機を装着した3Lの4ツロコル
ベンに仕込み48%水酸化ナトリウム水溶t&0.5K
gを加え1時間撹拌し分液ろ斗中で20分静置後分液し
て0.94Kgの1,3一ジオキソランが得られた。
Example 1 1.12 g of ifl1.3-dioxolane produced as in Production Example 1 was charged into a 3 L 4-turokolbene equipped with a stirrer, and 48% sodium hydroxide aqueous solution t&0.5K was added.
g was added thereto, stirred for 1 hour, allowed to stand for 20 minutes in a separatory funnel, and then separated to obtain 0.94 kg of 1,3-dioxolane.

実施例2 実施例1の1,3−ジオキソランIKgを,撹拌機を装
着した3Lの4ツロコルベンに仕込み顆粒状水酸化ナト
リウム50gを加え3時間攪拌し濾過して0.98Kg
の1,3−ジオキソランが得られた。
Example 2 IKg of 1,3-dioxolane from Example 1 was charged into a 3L 4-turocolben equipped with a stirrer, 50g of granular sodium hydroxide was added, stirred for 3 hours, and filtered to give 0.98Kg.
1,3-dioxolane was obtained.

実施例3 実施例2の1,3−ジオキソランIKgを,撹拌機、温
度計と蒸留ヘッドを装着した3Lの4ツロコルペンに仕
込み撹拌しながらフルベン温度75〜80℃で蒸留し、
沸点76℃の1,3−ジオキソラン0.97Kgが得ら
れた。
Example 3 I kg of 1,3-dioxolane from Example 2 was charged into a 3 L 4-turokorpen equipped with a stirrer, a thermometer and a distillation head, and distilled with stirring at a fulvene temperature of 75 to 80°C.
0.97 kg of 1,3-dioxolane having a boiling point of 76°C was obtained.

比較例1 製造例1のようにして製造した粗1,3−ジオキソラン
の無水ボウ硝で脱水したちのIKgを,撹拌機、温度計
と蒸留ヘッドを装着した3Lの4ツロコルベンに仕込み
拌しながらコルベン温度75〜80℃で蒸留し、沸点7
6℃の1,3−ジオキソラン0.96kgが得られた。
Comparative Example 1 IKg of crude 1,3-dioxolane produced as in Production Example 1, dehydrated with anhydrous sulfur salt, was charged into a 3 L 4-turokolbene equipped with a stirrer, thermometer and distillation head, while stirring. Distilled at Kolben temperature 75-80℃, boiling point 7
0.96 kg of 1,3-dioxolane at 6°C was obtained.

実施例1〜3および比較例1の1,3−ジオキソランの
ガスクロマトグラフ分析による純度およびカールフィブ
シャー法での水分含有量は表1の通りである。
The purity of the 1,3-dioxolanes of Examples 1 to 3 and Comparative Example 1 by gas chromatographic analysis and the water content by Karl Fibscher method are shown in Table 1.

表  1 A: 水              B: メタノー
ルC:  (IIマリン).        D: エ
チレンク゜リコール不純物の単位:  XIO” PP
M [発明の効果] 本発明の精製法で得られる環状アセタール類は,粗環状
アセタール類をアルカリ水溶液や固型水酸化アルカリ化
合物で処理して,粗環状アセタール類中に残存する水分
,グリコール類,メタノール,アルデヒド類およびその
重合物々どの不純物が除去されているので高純度である
Table 1 A: Water B: Methanol C: (II Marine). D: Unit of ethylene glycol impurity: XIO” PP
M [Effects of the Invention] The cyclic acetals obtained by the purification method of the present invention can be obtained by treating the crude cyclic acetals with an aqueous alkali solution or a solid alkali hydroxide compound to remove moisture and glycols remaining in the crude cyclic acetals. It is highly pure because impurities such as , methanol, aldehydes, and their polymers have been removed.

上記効果を奏することから電池用電解溶媒として存用で
ある。
Since it exhibits the above effects, it is useful as an electrolytic solvent for batteries.

Claims (1)

【特許請求の範囲】 1、粗環状アセタール類をアルカリ水溶液および/また
は固型水酸化アルカリ化合物で処理することを特徴とす
る環状アセタール類の精製法。 2、粗環状アセタール類をアルカリ水溶液で処理し、ア
ルカリ水溶液を分離したのち固型水酸化アルカリ化合物
で処理することを特徴とする請求項1記載の精製法。
[Scope of Claims] 1. A method for purifying cyclic acetals, which comprises treating crude cyclic acetals with an aqueous alkali solution and/or a solid alkali hydroxide compound. 2. The purification method according to claim 1, characterized in that the crude cyclic acetals are treated with an aqueous alkali solution, the aqueous alkali solution is separated, and then the crude cyclic acetal is treated with a solid alkali hydroxide compound.
JP15872889A 1989-06-21 1989-06-21 Purification of cyclic acetal Pending JPH0324071A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15872889A JPH0324071A (en) 1989-06-21 1989-06-21 Purification of cyclic acetal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15872889A JPH0324071A (en) 1989-06-21 1989-06-21 Purification of cyclic acetal

Publications (1)

Publication Number Publication Date
JPH0324071A true JPH0324071A (en) 1991-02-01

Family

ID=15678038

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15872889A Pending JPH0324071A (en) 1989-06-21 1989-06-21 Purification of cyclic acetal

Country Status (1)

Country Link
JP (1) JPH0324071A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5164516A (en) * 1991-02-14 1992-11-17 Eastman Kodak Company Purification of cyclic ketene acetals
JPH10226682A (en) * 1997-02-18 1998-08-25 Mitsubishi Gas Chem Co Inc Method for producing cyclic formal

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5164516A (en) * 1991-02-14 1992-11-17 Eastman Kodak Company Purification of cyclic ketene acetals
JPH10226682A (en) * 1997-02-18 1998-08-25 Mitsubishi Gas Chem Co Inc Method for producing cyclic formal

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