JPH0324071A - Purification of cyclic acetal - Google Patents
Purification of cyclic acetalInfo
- 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
Links
- -1 cyclic acetal Chemical class 0.000 title claims abstract description 43
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 238000000746 purification Methods 0.000 title claims description 3
- 238000000034 method Methods 0.000 claims abstract description 13
- 239000007787 solid Substances 0.000 claims abstract description 12
- 239000003513 alkali Substances 0.000 claims abstract description 11
- 229910001854 alkali hydroxide Inorganic materials 0.000 claims abstract description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract description 18
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Substances [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 abstract description 10
- 150000002334 glycols Chemical class 0.000 abstract description 8
- 239000007864 aqueous solution Substances 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 5
- 150000008044 alkali metal hydroxides Chemical class 0.000 abstract description 4
- 125000002777 acetyl group Chemical class [H]C([H])([H])C(*)=O 0.000 abstract description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 abstract description 3
- 239000000920 calcium hydroxide Substances 0.000 abstract description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 abstract description 3
- 229920000642 polymer Polymers 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 239000002904 solvent Substances 0.000 abstract description 2
- 235000011116 calcium hydroxide Nutrition 0.000 abstract 1
- 239000003792 electrolyte Substances 0.000 abstract 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 abstract 1
- WNXJIVFYUVYPPR-UHFFFAOYSA-N 1,3-dioxolane Chemical compound C1COCO1 WNXJIVFYUVYPPR-UHFFFAOYSA-N 0.000 description 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000003756 stirring Methods 0.000 description 7
- 150000001299 aldehydes Chemical class 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N butyric aldehyde Natural products CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- NBBJYMSMWIIQGU-UHFFFAOYSA-N Propionic aldehyde Chemical compound CCC=O NBBJYMSMWIIQGU-UHFFFAOYSA-N 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- SMQUZDBALVYZAC-UHFFFAOYSA-N salicylaldehyde Chemical compound OC1=CC=CC=C1C=O SMQUZDBALVYZAC-UHFFFAOYSA-N 0.000 description 2
- 150000003463 sulfur Chemical class 0.000 description 2
- 125000006091 1,3-dioxolane group Chemical class 0.000 description 1
- XKTYXVDYIKIYJP-UHFFFAOYSA-N 3h-dioxole Chemical compound C1OOC=C1 XKTYXVDYIKIYJP-UHFFFAOYSA-N 0.000 description 1
- PGTKVMVZBBZCKQ-UHFFFAOYSA-N Fulvene Chemical compound C=C1C=CC=C1 PGTKVMVZBBZCKQ-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- AYVGBNGTBQLJBG-UHFFFAOYSA-N [3-(hydroxymethyl)cyclopentyl]methanol Chemical compound OCC1CCC(CO)C1 AYVGBNGTBQLJBG-UHFFFAOYSA-N 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000003934 aromatic aldehydes Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 229920001429 chelating resin Polymers 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 description 1
- 229920002866 paraformaldehyde Polymers 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N valeric aldehyde Natural products CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)
Abstract
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)
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.
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)
| 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 |
-
1989
- 1989-06-21 JP JP15872889A patent/JPH0324071A/en active Pending
Cited By (2)
| 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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