JPS6223739B2 - - Google Patents
Info
- Publication number
- JPS6223739B2 JPS6223739B2 JP53139481A JP13948178A JPS6223739B2 JP S6223739 B2 JPS6223739 B2 JP S6223739B2 JP 53139481 A JP53139481 A JP 53139481A JP 13948178 A JP13948178 A JP 13948178A JP S6223739 B2 JPS6223739 B2 JP S6223739B2
- Authority
- JP
- Japan
- Prior art keywords
- thionyl chloride
- butyrolactone
- hours
- alcohol
- producing
- 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
Links
- FYSNRJHAOHDILO-UHFFFAOYSA-N thionyl chloride Chemical compound ClS(Cl)=O FYSNRJHAOHDILO-UHFFFAOYSA-N 0.000 claims description 28
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical class O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 claims description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 229930188620 butyrolactone Natural products 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 150000002596 lactones Chemical class 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 239000000203 mixture Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 5
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 5
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- -1 chlorocarboxylic acid ester Chemical class 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- GAEKPEKOJKCEMS-UHFFFAOYSA-N gamma-valerolactone Chemical compound CC1CCC(=O)O1 GAEKPEKOJKCEMS-UHFFFAOYSA-N 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 150000004702 methyl esters Chemical class 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- JOOXCMJARBKPKM-UHFFFAOYSA-N 4-oxopentanoic acid Chemical compound CC(=O)CCC(O)=O JOOXCMJARBKPKM-UHFFFAOYSA-N 0.000 description 2
- OZJPLYNZGCXSJM-UHFFFAOYSA-N 5-valerolactone Chemical compound O=C1CCCCO1 OZJPLYNZGCXSJM-UHFFFAOYSA-N 0.000 description 2
- QGLBZNZGBLRJGS-UHFFFAOYSA-N Dihydro-3-methyl-2(3H)-furanone Chemical compound CC1CCOC1=O QGLBZNZGBLRJGS-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 125000004494 ethyl ester group Chemical group 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- ALZLTHLQMAFAPA-UHFFFAOYSA-N 3-Methylbutyrolactone Chemical compound CC1COC(=O)C1 ALZLTHLQMAFAPA-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 239000000370 acceptor Substances 0.000 description 1
- 244000309464 bull Species 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- YMGUBTXCNDTFJI-UHFFFAOYSA-N cyclopropanecarboxylic acid Chemical class OC(=O)C1CC1 YMGUBTXCNDTFJI-UHFFFAOYSA-N 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- KFZMSGVFBACQDK-UHFFFAOYSA-N ethyl 3-chloropentanoate Chemical compound CCOC(=O)CC(Cl)CC KFZMSGVFBACQDK-UHFFFAOYSA-N 0.000 description 1
- HSMWWODOXVRNOR-UHFFFAOYSA-N ethyl 4-chloro-2-methylbutanoate Chemical compound CCOC(=O)C(C)CCCl HSMWWODOXVRNOR-UHFFFAOYSA-N 0.000 description 1
- OJAYUEGXOWQYTB-UHFFFAOYSA-N ethyl 4-chloropentanoate Chemical compound CCOC(=O)CCC(C)Cl OJAYUEGXOWQYTB-UHFFFAOYSA-N 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 229940040102 levulinic acid Drugs 0.000 description 1
- BHQQXAOBIZQEGI-UHFFFAOYSA-N methyl 2-chlorobutanoate Chemical compound CCC(Cl)C(=O)OC BHQQXAOBIZQEGI-UHFFFAOYSA-N 0.000 description 1
- YCQMBQQPRXPRAA-UHFFFAOYSA-N methyl 4-chloro-3-methylbutanoate Chemical compound COC(=O)CC(C)CCl YCQMBQQPRXPRAA-UHFFFAOYSA-N 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/30—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
- C07C67/307—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by introduction of halogen; by substitution of halogen atoms by other halogen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
- C07C51/363—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by introduction of halogen; by substitution of halogen atoms by other halogen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/58—Preparation of carboxylic acid halides
- C07C51/60—Preparation of carboxylic acid halides by conversion of carboxylic acids or their anhydrides or esters, lactones, salts into halides with the same carboxylic acid part
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C53/00—Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen
- C07C53/15—Saturated compounds having only one carboxyl group bound to an acyclic carbon atom or hydrogen containing halogen
- C07C53/19—Acids containing three or more carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/62—Halogen-containing esters
- C07C69/63—Halogen-containing esters of saturated acids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明はブチロラクトン又は置換されたブチロ
ラクトン、アルコール及び塩化チオニルからγ―
クロルカルボン酸エステルを製造する方法に関す
る。γ―クロルカルボン酸エステルはなかんづ
く、殊にシクロプロパンカルボン酸及びそのエス
テル製造の有利な中間生成物である。DETAILED DESCRIPTION OF THE INVENTION The present invention provides γ-
The present invention relates to a method for producing chlorocarboxylic acid ester. γ-chlorocarboxylic acid esters are particularly preferred intermediates for the production of cyclopropanecarboxylic acids and their esters.
γ―クロル脂肪酸エステルを製造する方法は多
数公知である。すなわちブチロラクトンとアルコ
ールとから、塩化水素の存在下にω―クロル酪酸
メチル―、―エチル―、―プロピル―及びブチル
エステルが製造されるが、この場合ラクトン2〜
3モルから高位エステルも生成する。メチルエス
テルの場合、この高縮合エステルの量は50%以上
である。ZnCl2を添加することにより、高縮合エ
ステルの量は減少するが、この場合、例えばω―
クロル酪酸メチルエステルの収率は理論値の50.4
%にすぎない。エチルエステルの収率は57.6%で
ある(Reppe,Ann.第596巻第163〜224頁)
更に、γ―バレロラクトンと無水エタノール及
びHCl―ガスとの反応も公知である。この場合4
―クロル吉草酸エチルエステルは理論値の55%の
収率で得られる(Julia et al,Bull.Soc.Chirnie
フランス国1960年第306頁)。このような混合物
を数時間、HCl―ガスで飽和させた場合、収率は
理論値の79%に高まる。α―メチル―γ―クロル
酪酸エチルエステルを2工程法で合成することも
公知である。それによれば、α―メチルブチロラ
クトンをHClとSOCl2を用いて68%の収率でα―
メチル―γ―塩化ブチリルに変換し、次にこれを
無水アルコールと反応させることにより、84%の
収率で所望のα―メチルエステルを得る。全収率
は理論値の57.1%である(Cannon et al.Am.
Soc,第81巻、第1664頁以下)。 Many methods for producing γ-chloro fatty acid esters are known. That is, from butyrolactone and alcohol, in the presence of hydrogen chloride, omega-chlorobutyrate methyl-, -ethyl-, -propyl- and butyl esters are produced, but in this case, the lactones 2-
Higher esters are also produced from 3 moles. In the case of methyl esters, this amount of highly condensed esters is greater than 50%. By adding ZnCl2 , the amount of highly condensed esters is reduced, but in this case, for example ω-
The theoretical yield of chlorobutyric acid methyl ester is 50.4.
It is only %. The yield of ethyl ester is 57.6% (Reppe, Ann. 596, pp. 163-224). Furthermore, the reaction of γ-valerolactone with absolute ethanol and HCl gas is known. In this case 4
- Chlorovaleric acid ethyl ester is obtained in a yield of 55% of theory (Julia et al, Bull.Soc.Chirnie
France 1960, p. 306). If such a mixture is saturated with HCl-gas for several hours, the yield increases to 79% of theory. It is also known to synthesize α-methyl-γ-chlorobutyric acid ethyl ester in a two-step process. According to this study, α-methylbutyrolactone was prepared using HCl and SOCl 2 with a yield of 68%.
Conversion to methyl-γ-butyryl chloride, which is then reacted with anhydrous alcohol, yields the desired α-methyl ester in 84% yield. The overall yield is 57.1% of theory (Cannon et al. Am.
Soc, Vol. 81, pp. 1664 et seq.).
従つて公知の方法により達成される収率は極め
て不満足なものである。この欠点はγ―クロルカ
ルボン酸エステルを90%以上の収率で得ることに
成功した本発明により取り除かれる。 The yields achieved by the known methods are therefore very unsatisfactory. This drawback is eliminated by the present invention, which has succeeded in obtaining γ-chlorocarboxylic acid esters with a yield of over 90%.
本発明は一般式:
〔式中、R,R1,R2,R3,R4及びR5は同一も
しくは異なつていてよく、炭素原子数1〜4を有
する直鎖又は分枝鎖のアルキル基を表わし、かつ
R以外は水素原子を表わすこともできる〕で示さ
れるγ―クロルカルボン酸エステルを製造するに
当り、場合により置換されていてもよい相応する
ブチロラクトン、アルコール及び塩化チオニル
(SOCl2)から出発し、かつ場合により置換されて
いてもよいブチロラクトンを無水アルコール中に
溶解し、少なくとも当量の塩化チオニル
(SOCl2)と反応させ、引続き生成したSO2から公
知方法で単離することを特徴とするγ―クロルカ
ルボン酸エステルの製造法に関する。 The present invention has the general formula: [In the formula, R, R 1 , R 2 , R 3 , R 4 and R 5 may be the same or different and represent a straight or branched alkyl group having 1 to 4 carbon atoms, and In producing the γ-chlorocarboxylic acid ester represented by [Other than R can also represent a hydrogen atom], starting from the corresponding optionally substituted butyrolactone, alcohol and thionyl chloride (SOCl 2 ), and optionally substituted butyrolactone is dissolved in anhydrous alcohol, reacted with at least an equivalent amount of thionyl chloride (SOCl 2 ), and subsequently isolated from the SO 2 formed by known methods. This invention relates to a method for producing chlorocarboxylic acid ester.
反応は既に低い温度で始まるので、塩化チオニ
ル添加の間、冷却により温度を約20〜−60℃に保
持することが推奨される。塩化チオニルの添加終
了後に望ましくは更に数時間例えば1〜2時間、
例えば−20〜約5℃の低い温度で後撹拌する。次
に、更に後撹拌を1〜2時間、例えば室温で継続
実施することが好ましい。 Since the reaction starts already at a low temperature, it is recommended to keep the temperature between about 20 and -60° C. by cooling during the thionyl chloride addition. After the addition of thionyl chloride is completed, the addition is desirably continued for several hours, e.g. 1 to 2 hours.
Post-stirring is carried out at a low temperature, for example from -20°C to about 5°C. Next, it is preferable to carry out further post-stirring for 1 to 2 hours, for example at room temperature.
塩化チオニルは特にラクトン対塩化チオニルの
モル比が約1:1であるような量で使用する。し
かしながら、有利には塩化チオニルは例えば25%
以上の過剰量で使用される。通常、1:1〜1:
3の間、特に1:1.1〜1:1.25の間の上記の比
に調節される。 Thionyl chloride is particularly used in an amount such that the molar ratio of lactone to thionyl chloride is about 1:1. However, advantageously the thionyl chloride is e.g. 25%
Used in excess amount. Usually 1:1-1:
3, in particular between 1:1.1 and 1:1.25.
本発明方法で使用することのできるアルコール
には殊にメタノール及びエタノールが挙げられる
が、プロパノール及びブタノール、即ち炭素原子
数1〜4を有する全てのアルコールも使用でき
る。 Alcohols which can be used in the process of the invention include in particular methanol and ethanol, but also propanol and butanol, ie all alcohols having 1 to 4 carbon atoms.
反応終了後又は僅かに高めた温度での後撹拌中
に、生成したSO2を溶液から除去するが、これは
アルコールの除去と共に行なうことができる。例
えば真空にするかもしくは不活性ガス、例えば窒
素を導入することができる。しかし、SO2―受容
体、例えばアルカリ液又は炭酸塩で中和すること
もできる。しかし、反応混合物を水中に注入する
こともできる。この場合、クロルカルボン酸エス
テルは分離するが、SO2及び場合によつてはHCl
は水中に溶解残留する。 After the end of the reaction or during post-stirring at a slightly elevated temperature, the SO 2 formed is removed from the solution, which can take place together with the removal of the alcohol. For example, a vacuum can be applied or an inert gas, for example nitrogen, can be introduced. However, it is also possible to neutralize with SO 2 -acceptors, such as lye or carbonates. However, it is also possible to pour the reaction mixture into water. In this case, the chlorocarboxylic acid ester is separated, but with SO 2 and possibly HCl
remains dissolved in water.
次に精製のために生成物を、例えば真空中で蒸
留する。 The product is then distilled, for example in vacuo, for purification.
この方法により、γ―クロルカルボン酸エステ
ルを高収率でかつ著量の副生産物の発生なしに得
ることができる。 By this method, γ-chlorocarboxylic acid ester can be obtained in high yield and without generating significant amounts of by-products.
例 1
1の3頚フラスコ中でγ―ブチロラクトン
258g(=3モル)と無水メタノール500mlとを混
合する。混合物を0℃に冷却する。次に良好な撹
拌下に塩化チオニル380gを徐々に滴加し、この
場合温度を+5℃以下に保持する。混合物を0℃
で2時間、次に20℃で2時間保持し、引続き真空
にする。その際SO2及びCH3OHはポンプで吸出
される。残渣を真空中で蒸留する。沸点62℃/10
mmHgでω―クロル酪酸メチルエステルに移行す
る。量:374g、理論値の91.3%に相当。Example 1 γ-Butyrolactone in a 3-necked flask from 1.
Mix 258 g (=3 mol) with 500 ml of anhydrous methanol. Cool the mixture to 0°C. 380 g of thionyl chloride are then slowly added dropwise with good stirring, keeping the temperature below +5.degree. Mixture at 0℃
for 2 hours at 20°C, then 2 hours at 20°C, and then evacuated. SO 2 and CH 3 OH are then pumped out. The residue is distilled in vacuo. Boiling point 62℃/10
Converts to ω-chlorobutyric acid methyl ester at mmHg. Amount: 374g, equivalent to 91.3% of the theoretical value.
例 2
バレロラクトン(=γ―メチル―γ―ブチロラ
クトン、レブリン酸から水素添加により製造)
300gを無水エタノール500mlに添加する。混合物
に0℃で塩化チオニル380gを加え、2時間この
温度で撹拌し、引続き、10〜20℃でSO2を窒素で
放出する。残渣を真空中で蒸留する。沸点84〜85
℃/15mmHgで3―クロル吉草酸エチルエステル
が留出する。量:462.6g、理論値の93.7%に相
当。Example 2 Valerolactone (=γ-methyl-γ-butyrolactone, produced from levulinic acid by hydrogenation)
Add 300 g to 500 ml of absolute ethanol. 380 g of thionyl chloride are added to the mixture at 0.degree. C. and stirred for 2 hours at this temperature, followed by evacuation of SO.sub.2 with nitrogen at 10-20.degree. The residue is distilled in vacuo. Boiling point 84-85
3-chlorovaleric acid ethyl ester is distilled out at ℃/15 mmHg. Amount: 462.6g, equivalent to 93.7% of the theoretical value.
例 3
無水エタノール500ml中のα―メチル―γ―ブ
チロラクトン300gに0℃で塩化チオニル400gを
加え、引続き0℃で4時間かつ20℃で2時間撹拌
し、その際亜硫酸を窒素で放出する。粗生成物を
水に注入し、NaOHで中和し、次に塩化メチレン
で取り、乾燥し、真空下に蒸発させる。生成物を
真空下に精留器で精留する。沸点78℃/10mmHg
でα―メチル―ω―クロル酪酸エチルエステルが
留出する。量:443.5g=理論値の89.9%。Example 3 400 g of thionyl chloride are added to 300 g of α-methyl-γ-butyrolactone in 500 ml of absolute ethanol at 0° C. and subsequently stirred for 4 hours at 0° C. and 2 hours at 20° C., during which the sulfurous acid is liberated with nitrogen. The crude product is poured into water, neutralized with NaOH, then taken up with methylene chloride, dried and evaporated under vacuum. The product is rectified in a rectifier under vacuum. Boiling point 78℃/10mmHg
α-methyl-ω-chlorobutyric acid ethyl ester is distilled out. Amount: 443.5g = 89.9% of theoretical value.
例 4
β―メチルブチロラクトン500gを無水メタノ
ール1と混合し、−20℃に冷却し、次に撹拌下
に塩化チオニル750gを徐々に添加し、2時間−
20〜−10℃で撹拌し、次に室温にする。6時間
後、混合物を回転圧力釜中で40℃及び20トルで蒸
発させる。残渣を真空下に1mのVigreux―カラ
ムで蒸留する。短時間の経過後に、沸点67〜68
℃/10mmHgでβ―メチル―γ―クロル酪酸メチ
ルエステルが留出する。量:674.1g、理論値の
89.6%に相当。Example 4 500 g of β-methylbutyrolactone was mixed with 1 part of anhydrous methanol, cooled to -20°C, then 750 g of thionyl chloride was slowly added under stirring for 2 hours.
Stir at 20 to -10°C and then bring to room temperature. After 6 hours, the mixture is evaporated in a rotary pressure cooker at 40°C and 20 Torr. The residue is distilled on a 1 m Vigreux column under vacuum. After a short period of time, boiling point 67-68
β-Methyl-γ-chlorobutyric acid methyl ester is distilled out at ℃/10mmHg. Amount: 674.1g, theoretical value
Equivalent to 89.6%.
比較例
1の3頚フラスコ中でγ―ブチロラクトン
258gと無水メタノール500mlとを混合する。十分
な冷却下にHClガスを飽和するまで導入し、次に
20℃で4時間放置させる。γ-Butyrolactone in the three-necked flask of Comparative Example 1
Mix 258 g with 500 ml of absolute methanol. Introduce HCl gas until saturation under sufficient cooling, then
Leave it at 20℃ for 4 hours.
後処理は未反応ブチロラクトンの主要量と共に
ω―クロル酪酸メチルエステル45.8g(理論値の
11.2%に相当)が生じる。 The post-treatment consisted of 45.8 g of ω-chlorobutyric acid methyl ester (theoretical value) along with the main amount of unreacted butyrolactone.
11.2%).
Claims (1)
しくは異なつていてよく、炭素原子数1〜4を有
する直鎖又は分枝鎖のアルキル基を表わし、かつ
R以外は水素原子を表わすこともできる〕で示さ
れるγ―クロルカルボン酸エステルを置換されて
いてもよい相応するブチロラクトンからアルコー
ル及び塩化チオニルの使用下に製造する方法にお
いて、置換されていてもよいブチロラクトンを無
水アルコールに溶解し、少なくとも当量の塩化チ
オニルと反応させ、引続き、生成したSO2を自体
公知の方法で分離することを特徴とする、γ―ク
ロルカルボン酸エステルの製造法。 2 塩化チオニルを約20℃以下の温度で添加す
る、特許請求の範囲第1項記載の方法。 3 ラクトン対塩化チオニルのモル比を1:1〜
1:3の間に保持する、特許請求の範囲第1項又
は第2項記載の方法。 4 炭素原子数1〜4を有する無水アルコールを
使用する、特許請求の範囲第1項記載の方法。[Claims] 1. General formula: [In the formula, R, R 1 , R 2 , R 3 , R 4 and R 5 may be the same or different and represent a straight or branched alkyl group having 1 to 4 carbon atoms, and A method for producing a γ-chlorocarboxylic acid ester represented by [Other than R can also represent a hydrogen atom] from the corresponding optionally substituted butyrolactone using an alcohol and thionyl chloride, which may be substituted. 1. A process for producing γ-chlorocarboxylic acid ester, which comprises dissolving butyrolactone in anhydrous alcohol, reacting it with at least an equivalent amount of thionyl chloride, and subsequently separating the SO 2 formed by a method known per se. 2. The method of claim 1, wherein thionyl chloride is added at a temperature below about 20°C. 3. Molar ratio of lactone to thionyl chloride is 1:1~
The method according to claim 1 or 2, wherein the ratio is maintained between 1:3. 4. The method according to claim 1, wherein an anhydrous alcohol having 1 to 4 carbon atoms is used.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2751134A DE2751134C2 (en) | 1977-11-16 | 1977-11-16 | Process for the preparation of γ-chlorocarboxylic acid esters |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5479224A JPS5479224A (en) | 1979-06-25 |
JPS6223739B2 true JPS6223739B2 (en) | 1987-05-25 |
Family
ID=6023827
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13948178A Granted JPS5479224A (en) | 1977-11-16 | 1978-11-14 | Manufacture of gammaachlorcarboxylic acid ester |
Country Status (10)
Country | Link |
---|---|
JP (1) | JPS5479224A (en) |
BE (1) | BE872028A (en) |
CA (1) | CA1136643A (en) |
CH (1) | CH636593A5 (en) |
DE (1) | DE2751134C2 (en) |
FR (1) | FR2409254A1 (en) |
GB (1) | GB2008111B (en) |
IL (1) | IL55933A (en) |
IT (1) | IT1157707B (en) |
NL (1) | NL7808304A (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI86889C (en) * | 1984-03-29 | 1992-10-26 | Lonza Ag | Process for the preparation of L-carnitine in a microbiological manner |
DE3538133A1 (en) * | 1985-10-26 | 1987-04-30 | Huels Chemische Werke Ag | METHOD FOR PRODUCING PURE, CHLORINE-FREE CYCLOPROPANCARBONIC ACID ESTERS |
JPH0291049A (en) * | 1988-09-21 | 1990-03-30 | Lonza Ag | Production of gamma-butyrobetaine |
DE4412316A1 (en) * | 1994-04-11 | 1995-10-12 | Basf Ag | Process for the preparation of o-chloromethylbenzoic acid chlorides |
US6552217B2 (en) * | 2000-08-01 | 2003-04-22 | Eastman Chemical Company | Process for the preparation of alkyl 1-methylcyclopropanecarboxylate |
CN106631777B (en) * | 2016-11-30 | 2019-02-19 | 浙江大学 | Synthesize γ-chlorobutanoate method |
CN117510328B (en) * | 2023-12-29 | 2024-04-12 | 山东京新药业有限公司 | Preparation method of methyl 4-chlorobutyrate |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3927074A (en) * | 1974-06-19 | 1975-12-16 | Olin Corp | Preparation of halobutyrate esters |
-
1977
- 1977-11-16 DE DE2751134A patent/DE2751134C2/en not_active Expired
-
1978
- 1978-08-08 NL NL7808304A patent/NL7808304A/en not_active Application Discontinuation
- 1978-10-27 CA CA000314569A patent/CA1136643A/en not_active Expired
- 1978-11-08 GB GB7843737A patent/GB2008111B/en not_active Expired
- 1978-11-10 FR FR7831873A patent/FR2409254A1/en active Granted
- 1978-11-14 BE BE6046668A patent/BE872028A/en not_active IP Right Cessation
- 1978-11-14 IL IL55933A patent/IL55933A/en unknown
- 1978-11-14 JP JP13948178A patent/JPS5479224A/en active Granted
- 1978-11-15 IT IT51914/78A patent/IT1157707B/en active
- 1978-11-15 CH CH1175178A patent/CH636593A5/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
FR2409254A1 (en) | 1979-06-15 |
JPS5479224A (en) | 1979-06-25 |
DE2751134C2 (en) | 1986-04-17 |
CA1136643A (en) | 1982-11-30 |
IL55933A0 (en) | 1979-01-31 |
DE2751134A1 (en) | 1979-05-17 |
GB2008111A (en) | 1979-05-31 |
IL55933A (en) | 1982-02-28 |
IT7851914A0 (en) | 1978-11-15 |
GB2008111B (en) | 1982-04-15 |
CH636593A5 (en) | 1983-06-15 |
NL7808304A (en) | 1979-05-18 |
BE872028A (en) | 1979-05-14 |
IT1157707B (en) | 1987-02-18 |
FR2409254B1 (en) | 1984-10-05 |
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