JPS59141538A - Production of halogenated propionic acid ester - Google Patents
Production of halogenated propionic acid esterInfo
- Publication number
- JPS59141538A JPS59141538A JP58014816A JP1481683A JPS59141538A JP S59141538 A JPS59141538 A JP S59141538A JP 58014816 A JP58014816 A JP 58014816A JP 1481683 A JP1481683 A JP 1481683A JP S59141538 A JPS59141538 A JP S59141538A
- Authority
- JP
- Japan
- Prior art keywords
- halogenated
- propionic acid
- acid ester
- mixture
- halogenated alcohol
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は一般式
%式%
X、 7C−C−C−OH(式中ty) R,、R2は
水素原子1 1 1
HX4R2−’J*ハアyvキyv基、X+ 、 X2
、x3およびX4はハロゲン原子である)のハロゲン化
アルコールのプロピオン酸エステルの製法の改良方法で
、さらに詳しく言えば、ハロゲン化アルコールよりプロ
ピオン酸エステルを製造する際に不飽和ア)Vコールお
よび不飽和アルコールのプロピオン酸エステルの生成を
極力おさえて、目的のハロゲン化プロピオン酸エステル
の収率を向上させる方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention is based on the general formula: X+, X2
, x3 and X4 are halogen atoms. The present invention relates to a method for suppressing the production of propionate esters of saturated alcohols as much as possible to improve the yield of the target halogenated propionate esters.
本発明者は先に、ハロゲン化アルコールの酢酸エステル
を、塩素含有不飽和アルコールと無水酢酸の混合液中に
リン酸を滴下することによって、塩素含有アルコールの
酢酸エステルの製造方法を提案した。(日本特許第7g
3103号)しかし、この方法をプロピオン酸エステル
の製造に適要した場合に、前記のようにハロゲン化不飽
和アルコールおよびハロゲン化不飽和エステルを副生ず
る欠点がある。このため、本発明者は、副生ずるハロゲ
ン化不飽和アルコール
生成を極力おさえて、目的のプロピオン酸エステルの収
率を向上させる努力を行なった結果、本発明をなすに至
った。The present inventor previously proposed a method for producing an acetate ester of a chlorine-containing alcohol by dropping phosphoric acid into a mixed solution of a chlorine-containing unsaturated alcohol and acetic anhydride. (Japanese Patent No. 7g
(No. 3103) However, when this method is applied to the production of propionic acid esters, it has the disadvantage that halogenated unsaturated alcohols and halogenated unsaturated esters are produced as by-products as described above. Therefore, the present inventor has made efforts to improve the yield of the target propionic acid ester by suppressing the production of a by-product halogenated unsaturated alcohol as much as possible, and as a result has achieved the present invention.
本発明に従うと、一般式
%式%
(式中のR+ 、R2 、X4 、X2 、X3 ’i
;? j U X4 (d 前記ト同じ意味を持つ)で
表わされるハロゲン化アルコールを無水プロピオン酸と
リン酸の混合液中に滴下後加熱反応せしめることを特徴
とする。According to the invention, the general formula % formula % (in which R+ , R2 , X4 , X2 , X3 'i
;? The method is characterized in that a halogenated alcohol represented by j U
一般式
%式%
(1)
(式中のR+ 、R2 、X+ 、X2 、X3および
X4は前記Zと同じ意味を持つ)で示されるハロゲン化
プロピオン酸エステルの製法である。This is a method for producing a halogenated propionate ester represented by the general formula % (1) (R+, R2, X+, X2, X3 and X4 have the same meaning as Z above).
本発明方法において原料として用いられるハロゲン化ア
ルコールは直鎖状または枝分かれ状のいスレでもよいが
、ハロゲン化アルコールの炭素数は3〜10までが適当
である。The halogenated alcohol used as a raw material in the method of the present invention may be linear or branched, but it is appropriate that the halogenated alcohol has 3 to 10 carbon atoms.
ハロゲンとしてはフッ素原子、塩素原子、臭素原子など
が用いられる。無水プロピオン酸と混合するリン酸は乙
00Beを用い、場合によってはメタリン酸、ポリリン
酸を併用して用いることができる。As the halogen, a fluorine atom, a chlorine atom, a bromine atom, etc. are used. Otsu00Be is used as the phosphoric acid to be mixed with propionic anhydride, and metaphosphoric acid and polyphosphoric acid may be used in combination depending on the case.
しかし、リン酸の濃度が高い場合などは次式で示す反応
により不飽和結合を有する化合物(1)、(n)が生成
する。However, when the concentration of phosphoric acid is high, compounds (1) and (n) having unsaturated bonds are produced by the reaction shown by the following formula.
?H3 H3’PO4
CHCI2−CC上,−CHOH半(’CH.CH2C
oh O −一→H3
CC工2二CC上−〇HOHー1ーHC]−(1)
このため、無水プロピオン酸とリン酸を混合したのち、
ハロゲン化アルコール全滴下反応させることによって(
It)、(II)への反応が極力おさえられることがわ
かった。? H3 H3'PO4 CHCI2-CC, -CHOH half ('CH.CH2C
oh O -1→H3 CC engineering 22 CC top -〇HOH-1-HC]-(1) Therefore, after mixing propionic anhydride and phosphoric acid,
By reacting by dropping all of the halogenated alcohol (
It was found that the reactions to It) and (II) were suppressed as much as possible.
無水プロピオン酸はハロゲン化ア)V V. − )V
/に対して/〜10が適当で、l〜乙が最も好ましい
。Propionic anhydride is halogenated a) V V. -)V
/~10 is appropriate for /, and l~B is most preferable.
この割合が少ないと副生物の生成が増加する。リン酸は
乙0°CBeのものであれば充分で、原料ハロゲン化ア
ルコール、に対して30−りOモル%程度が適当である
。反応時間は7〜3時間で温度は90〜100°Cで充
分である。If this ratio is low, the formation of by-products will increase. It is sufficient that the phosphoric acid has a concentration of 0°CBe, and is suitably about 30% by mole based on the raw material halogenated alcohol. A reaction time of 7 to 3 hours and a temperature of 90 to 100°C are sufficient.
本発明のハロゲン化プロピオン酸エステルは、昆虫の誘
引物質としてまた臭素化して難燃処理剤製造などに用い
られる。!.た脱ハロゲン化を行なってアセチレン化合
物となし、光エネルギーを蓄えることのできる有機蓄熱
剤の合成原料として有用なものである。The halogenated propionic acid ester of the present invention can be used as an insect attractant, and can also be brominated and used in the production of flame retardant treatment agents. ! .. It undergoes dehalogenation to form an acetylene compound, which is useful as a raw material for the synthesis of organic heat storage agents that can store light energy.
次に本発明を実施例によって、さらに詳細に説明する。Next, the present invention will be explained in more detail with reference to Examples.
実施例/″
2、2,、3.3−テトラクロロプロパン〜/ーオー/
L’ / 2.乙?9COO3モtv)f無水7” a
ヒylーン酸3903ji’ ( 0.3.0モw)
とAooBel)ン酸λ.2乙F ( 0. 0 2モ
ル)の混合液中にθ〜ータ°Cで30分かかつて滴下す
る。滴下後反応液を70〜9!;′Cの温度に徐々に上
昇させたのち、その温度で3時間加熱反応させた。反応
復水水中に投入分解し、四塩化炭素で抽出する。抽出液
は酸性水素ナトリウム水溶液および塩化す) IJウム
の飽和水溶液で洗ったのち亡硝で乾燥した。抽出液より
四塩化炭素および未反応無水プロピオン酸を留去し、粗
油/9. g 09を得た。粗油を蒸留して沸慨り乙0
〜10.fO°C/10mmHgの留分/7乙3Zを得
た。これを分留して沸点9汐0 ’C/ 7 ynm
Hl ( d:’ i 41 、2/ 3、?L−,
i 41.! 、241 )の留分/2.10グ(収
率9夕3%)を得た。この留分の元素分析値は、H’.
309.C:、2g3g。Example/''2,2,,3.3-tetrachloropropane~/-o/
L'/2. Otsu? 9COO3mo tv) f anhydrous 7” a
Hylic acid 3903ji' (0.3.0 mow)
and AooBel) acid λ. It was added dropwise into a mixed solution of 2 F (0.02 mol) at θ to 30 °C for 30 minutes. After dropping the reaction solution is 70-9! ; After the temperature was gradually raised to 'C, the reaction was carried out by heating at that temperature for 3 hours. The reaction condensate is decomposed in water and extracted with carbon tetrachloride. The extract was washed with an aqueous acidic sodium hydrogen solution and a saturated aqueous solution of IJium chloride, and then dried over cold nitrogen. Carbon tetrachloride and unreacted propionic anhydride were distilled off from the extract to obtain a crude oil/9. g09 was obtained. Crude oil is distilled and boiling
~10. A fraction of fO°C/10 mmHg/7 Otsu 3Z was obtained. This is fractionated to a boiling point of 9 0'C/7 ynm
Hl (d:' i 41, 2/3, ?L-,
i41. ! , 241)/2.10 g (yield: 9, 3%) was obtained. The elemental analysis value of this fraction was H'.
309. C:, 2g3g.
C工:j左73で分子式C6 H8 02 C工4の元
素分析値H’.3.77、C”、2g37.C工:ss
g41tv値とよく一致する。また赤外線吸収スペクト
ルは、波数/753cm に強いエステルのカルボニル
のd=oの伸縮振動を示し、目的の/−プロピオールオ
キシ−,2,2,3,3−テトラクロロプロパンである
。C engineering: j 73 on the left, molecular formula C6 H8 02 Elemental analysis value H' of C engineering 4. 3.77, C”, 2g37.C engineering: ss
It agrees well with the g41tv value. In addition, the infrared absorption spectrum shows a strong stretching vibration of d=o of the carbonyl of the ester at a wave number of 753 cm, indicating that it is the desired /-propioloxy-,2,2,3,3-tetrachloropropane.
実施例2
3.3.グ、41−テトラクロロブタン−2−オー)v
13.39!(00!;−F=ル)を無水フロピオン酸
39.03!(030−e−/v)と乙00Beリン酸
λ1.2乙fZ(00,2モ/L/)の混合液中にθ〜
=夕°Cで30分かかつて滴下する。滴下後反応液ヲ9
0〜り5 ’Cの温度に徐々に上昇させたのち、その温
度で3時間反応させた。反応後、実施例/と同様に処理
して粗油241/乙gtヲ得た。粗油全蒸留して沸屯り
SO〜//2.0°C/10朋Hgの留分/70乙yを
得た。これをさらに分留して沸転1010°C/7糖H
gCd−t13gクタ、9tγ/りg2g、C132,
93%)の2−プロピオールオキシ−3,3,41,4
1−テトラクロロブタン//、77 P (収率g7g
%)を得た。Example 2 3.3. 41-tetrachlorobutan-2-o)v
13.39! (00!;-F=L) to fropionic anhydride 39.03! (030-e-/v) and θ~
Drop once for 30 minutes at = evening °C. After dropping reaction solution 9
The temperature was gradually raised to 0 to 5'C, and the reaction was continued at that temperature for 3 hours. After the reaction, the crude oil was treated in the same manner as in Example 2 to obtain 241 gt of crude oil. The crude oil was completely distilled to obtain a boiling SO~/2.0°C/10 Hg fraction/70 Oty. This is further fractionated and boiled at 1010°C/7 sugar H
gCd-t13gcta, 9tγ/g2g, C132,
93%) of 2-propioloxy-3,3,41,4
1-tetrachlorobutane //, 77 P (yield g7g
%) was obtained.
実施例3
y、q、s、s−テトラクロロベンクン−3−オー)L
”/41.0りy<oosモル)を無水フロピオン酸3
’?IO!9CO30モtv)と乙00Bel)ン酸、
2..2乙f! (0,02モy’v)(D混合液中に
o〜−t’cで30分かかつて滴下する。滴下後、反応
液は90〜93”Qの温度で3時間反応させた。反応後
、実施例/と同様に処理して粗油/79り2を得た。Example 3 y, q, s, s-tetrachlorobencune-3-o)L
”/41.0 y<oos mol) to 3 ml of fropionic anhydride
'? IO! 9CO30motv) and 00Bel) acid,
2. .. 2 o f! (0,02 moy'v) (Dropped into the D mixture at o~-t'c for 30 minutes. After the dropwise addition, the reaction mixture was reacted for 3 hours at a temperature of 90~93''Q. Reaction Thereafter, it was treated in the same manner as in Example to obtain crude oil/79ri 2.
粗油全分留して沸g、 / / 00 °C/ 7 a
m Hg (tl:/3クタざ、飛/グざグア、cエタ
ooり%)の3−プロピオニルオキシーク、り、5.!
;−テトラクロロベンクン//: 29 S’ (収率
g00%)を得た。Total distillation of crude oil to boiling g, / / 00 °C / 7 a
m Hg (tl:/3ktaza, fly/guzagua, cetaooori%), 3-propionyloxy, ri, 5. !
;-Tetrachlorobencune//: 29S' (yield: 00%) was obtained.
実施例り 。Examples.
2−メチルー3.3,41.47−チトラクロロブタン
ー2−オール/グo9ノ(0,03モル)を無水プロピ
オン酸39039 (030モル)と乙。。2-Methyl-3.3,41.47-titrachlorobutan-2-ol/guo9 (0.03 mol) and propionic anhydride 39039 (0.30 mol). .
Beリン酸2.2乙9COO2モ/l/ )の混合液中
に0〜−夕°Cで30分かがって滴下する。滴下後、反
応液を90〜93℃で3時間反応させた。反応後、実施
例/と同様に処理して粗油37乙97を得た。これを分
留して沸点/−?り〜/2乙0 ’C// OynmJ
(C130,/ 3%)の−一プロピオニルオキシー
2−メチ/I/−3,3,41,ゲーテ1−ラクロロブ
クン/グOタン(収率100%)を得た。The mixture was added dropwise to a mixture of 2.2% Be and 9COO2 mo/l/) at 0°C to -12°C over 30 minutes. After the dropwise addition, the reaction solution was reacted at 90 to 93°C for 3 hours. After the reaction, the crude oil 37 Otsu 97 was obtained by processing in the same manner as in Example. Fractionally distill this and boiling point /-? Ri~/2 Otsu0 'C// OynmJ
(C130,/3%) -1-propionyloxy-2-methy/I/-3,3,41, Goethe 1-lachlorobucne/gOtan (yield 100%) was obtained.
実施例S
タウ5.乙、乙−テトヲクロロヘキサンーグーオー/L
/ /グg09(003モル)を無水プロピオン酸39
03 y、(?)30モル)と乙。。Be l) ン酸
2.2乙F (0,0,2モル)の混合液にQ〜−s
’cで30分かかつて滴下する。滴下後、反応液′f!
:90〜?j°Cで3時間反応させた。反応後、実施例
/と同様に処理して粗油2/乙22を得た。これを分留
して沸慨/ 、2 o o°c/7mygHg (、t
l:/307/、入D/りg、2グ、Cニゲ7gg%)
のグープロピオニルオキシ−5,、ff、乙、乙−テト
ラクロロヘキサン/11.g09 (収率100%)を
得た。Example S Tau5. Otsu, Otsu-tetowochlorohexane-goo/L
/ /g09 (003 mol) to propionic anhydride 39
03 y, (?) 30 mole) and Otsu. . Be l) Add Q~-s to a mixture of 2.2 F (0,0,2 mol) of phosphoric acid.
Drip for 30 minutes at 'C. After dropping, the reaction solution 'f!
:90~? The reaction was carried out at 1°C for 3 hours. After the reaction, crude oil 2/Otsu 22 was obtained by processing in the same manner as in Example. This was fractionated and boiled / , 2 o o ° C / 7 mygHg (, t
l: /307/, entering D/rig, 2, C 7gg%)
Gopropionyloxy-5,, ff, Otsu, Otsu-tetrachlorohexane/11. g09 (yield 100%) was obtained.
Claims (1)
11 HX4R2またはアルキル基、Xl、X2X3およびX
4はハロゲン原子である)のハロゲン化アルコールを無
水プロピオン酸とリン酸の混合液中で反応させ 一般式 %式% x4は前記と同じ意味を持つ)で表わされるハロゲン化
プロピオン酸エステ/L/の製法。[Claims] General formula Xl-C-C-C-OH (in the formula, R1 and R2 are hydrogen atoms 11 HX4R2 or alkyl groups,
4 is a halogen atom) is reacted in a mixture of propionic anhydride and phosphoric acid to produce a halogenated propionic acid ester /L/ manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58014816A JPS59141538A (en) | 1983-02-01 | 1983-02-01 | Production of halogenated propionic acid ester |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58014816A JPS59141538A (en) | 1983-02-01 | 1983-02-01 | Production of halogenated propionic acid ester |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59141538A true JPS59141538A (en) | 1984-08-14 |
JPH0138776B2 JPH0138776B2 (en) | 1989-08-16 |
Family
ID=11871560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58014816A Granted JPS59141538A (en) | 1983-02-01 | 1983-02-01 | Production of halogenated propionic acid ester |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59141538A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61286351A (en) * | 1985-06-10 | 1986-12-16 | チバ−ガイギ− アクチエンゲゼルシヤフト | Manufacture of cyclopropylamine |
US4791223A (en) * | 1986-12-22 | 1988-12-13 | Societe Atochem | Process for the preparation of 1,1,2,2-tetrahydroperfluoroalkanols and their esters |
-
1983
- 1983-02-01 JP JP58014816A patent/JPS59141538A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61286351A (en) * | 1985-06-10 | 1986-12-16 | チバ−ガイギ− アクチエンゲゼルシヤフト | Manufacture of cyclopropylamine |
JPH0529214B2 (en) * | 1985-06-10 | 1993-04-28 | Ciba Geigy | |
US4791223A (en) * | 1986-12-22 | 1988-12-13 | Societe Atochem | Process for the preparation of 1,1,2,2-tetrahydroperfluoroalkanols and their esters |
Also Published As
Publication number | Publication date |
---|---|
JPH0138776B2 (en) | 1989-08-16 |
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