JPS593463B2 - Dimethyl carbonate recovery method - Google Patents

Dimethyl carbonate recovery method

Info

Publication number
JPS593463B2
JPS593463B2 JP51017175A JP1717576A JPS593463B2 JP S593463 B2 JPS593463 B2 JP S593463B2 JP 51017175 A JP51017175 A JP 51017175A JP 1717576 A JP1717576 A JP 1717576A JP S593463 B2 JPS593463 B2 JP S593463B2
Authority
JP
Japan
Prior art keywords
dimethyl carbonate
recovery method
azeotrope
carbonate recovery
methanol
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
Application number
JP51017175A
Other languages
Japanese (ja)
Other versions
JPS51108019A (en
Inventor
ウゴー・ロマーノ
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.)
Anic SpA
Original Assignee
Anic SpA
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 Anic SpA filed Critical Anic SpA
Publication of JPS51108019A publication Critical patent/JPS51108019A/ja
Publication of JPS593463B2 publication Critical patent/JPS593463B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C68/00Preparation of esters of carbonic or haloformic acids
    • C07C68/08Purification; Separation; Stabilisation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C68/00Preparation of esters of carbonic or haloformic acids
    • C07C68/06Preparation of esters of carbonic or haloformic acids from organic carbonates

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Nitrogen Condensed Heterocyclic Rings (AREA)

Description

【発明の詳細な説明】 本発明はメタノールとの共沸混合物から純粋なジメチル
カーボネートを回収する方法に係わる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for recovering pure dimethyl carbonate from an azeotrope with methanol.

ジメチルカーボネートは環状カーボネートおよびアルコ
ールを原料とするエステル交換反応により得られるが、
ジメチルカーボネートの場合には該化合物とメチルアル
コールとの共沸混合物として生成されることは公知であ
る。米国特許第3803201号明細書によれば、反応
生成物から蒸留により前記共沸混合物を取出5 したの
ち、低温における晶析工程および蒸留工程の2つの工程
でジメチルカーボネートが共沸混合物から分離されるっ
本発明者は、加圧下での蒸留工程のみを実施することに
より、上記の方法よりも経済的でかつ簡10単に、製造
工程中に生成された共沸混合物からジメチルカーボネー
トを単離できることを見出し、本発明に到達した。
Dimethyl carbonate is obtained by transesterification using cyclic carbonate and alcohol as raw materials.
In the case of dimethyl carbonate, it is known that it is produced as an azeotrope of this compound and methyl alcohol. According to US Pat. No. 3,803,201, after the azeotrope is extracted from the reaction product by distillation5, dimethyl carbonate is separated from the azeotrope in two steps: a crystallization step at low temperature and a distillation step. The present inventor has discovered that dimethyl carbonate can be isolated from the azeotrope produced during the production process more economically and more easily than the above method by performing only a distillation step under pressure. Heading, we arrived at the present invention.

実施例 O、32cm(1/ 8インチ)のセラミク製ラシヒ1
5 リングを充填した、直径3.8cm(1.5インチ
)、高さ101.6cm(40インチ)スチールカラム
を具備する容積11■の容器に、メタノール−ジメチル
カーボネート混合物を導入した。
Example O, 32 cm (1/8 inch) ceramic rashich 1
The methanol-dimethyl carbonate mixture was introduced into a 11 .mu. volume vessel equipped with a 1.5 inch diameter, 40 inch high steel column packed with 5 rings.

混合物の組成は70:30(重量)であり、これは1気
圧下で20共沸する組成に相当する。窒素圧力下、混合
物を10気圧で蒸留した。
The composition of the mixture was 70:30 (by weight), which corresponds to a composition with a 20 azeotrope under 1 atmosphere. The mixture was distilled at 10 atmospheres under nitrogen pressure.

塔底温度は150℃であり、塔頂温度は142℃であつ
た。この蒸留により、メタノール95%およびジメ25
チルカーボネート5%を含有する塔頂留分が得られ、
一方塔底留分は純粋なジメチルカーボネートであつた。
The tower bottom temperature was 150°C, and the tower top temperature was 142°C. This distillation produces 95% methanol and 25% dimethane.
An overhead fraction containing 5% chill carbonate is obtained,
On the other hand, the bottom fraction was pure dimethyl carbonate.

Claims (1)

【特許請求の範囲】[Claims] 1 メタノールとの共沸混合物からジメチルカーボネー
トを回収する方法において、前記共沸混合物を10気圧
、塔底温度150℃および塔頂温度142℃で蒸留する
ことを特徴とする、ジメチルカーボネートの回収法。
1. A method for recovering dimethyl carbonate from an azeotrope with methanol, the method comprising distilling the azeotrope at 10 atm, a bottom temperature of 150°C, and a top temperature of 142°C.
JP51017175A 1975-02-21 1976-02-20 Dimethyl carbonate recovery method Expired JPS593463B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT20505/75A IT1031933B (en) 1975-02-21 1975-02-21 PROCESS FOR THE RECOVERY OF DIMETHYL CARBONATE

Publications (2)

Publication Number Publication Date
JPS51108019A JPS51108019A (en) 1976-09-25
JPS593463B2 true JPS593463B2 (en) 1984-01-24

Family

ID=11167935

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51017175A Expired JPS593463B2 (en) 1975-02-21 1976-02-20 Dimethyl carbonate recovery method

Country Status (18)

Country Link
JP (1) JPS593463B2 (en)
AU (1) AU1108876A (en)
BE (1) BE838502A (en)
CH (1) CH620416A5 (en)
CS (1) CS188130B2 (en)
DD (1) DD123451A5 (en)
DE (1) DE2607003C3 (en)
DK (1) DK146413C (en)
FR (1) FR2301509A1 (en)
GB (1) GB1470160A (en)
IL (1) IL49005A0 (en)
IT (1) IT1031933B (en)
LU (1) LU74382A1 (en)
NL (1) NL7601777A (en)
NO (1) NO146772C (en)
SE (1) SE426060B (en)
YU (1) YU39121B (en)
ZA (1) ZA76678B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2740243A1 (en) 1977-09-07 1979-03-15 Bayer Ag PROCESS FOR THE PRODUCTION OF DIALKYLCARBONATES
JP2557099B2 (en) * 1989-02-13 1996-11-27 ダイセル化学工業株式会社 Method for separating dimethyl carbonate
DE4234525A1 (en) * 1992-10-13 1994-04-14 Bayer Ag Process for the separation of alkanols from oxygen-containing organic compounds with a higher carbon number
DE4319570A1 (en) * 1993-06-14 1994-12-15 Bayer Ag Process and separation of alkanols from other organic compounds with a higher carbon number
ES2103520T3 (en) * 1993-07-15 1997-09-16 Bayer Ag PROCEDURE FOR OBTAINING DIMETHYL CARBONATE.
DE4339977A1 (en) * 1993-11-24 1995-06-01 Bayer Ag Process for working up the liquid reaction products from the copper-catalyzed production of dimethyl carbonate
EP2121563B1 (en) 2007-02-16 2016-05-04 SABIC Global Technologies B.V. Process for manufacturing dimethyl carbonate
PL2121562T3 (en) 2007-02-16 2017-12-29 Sabic Global Technologies B.V. Process for manufacturing dimethyl carbonate

Also Published As

Publication number Publication date
CH620416A5 (en) 1980-11-28
DD123451A5 (en) 1976-12-20
DK146413B (en) 1983-10-03
DK66876A (en) 1976-08-22
AU1108876A (en) 1977-08-18
NO146772C (en) 1982-12-08
FR2301509A1 (en) 1976-09-17
GB1470160A (en) 1977-04-14
DE2607003B2 (en) 1979-08-16
CS188130B2 (en) 1979-02-28
IT1031933B (en) 1979-05-10
YU39121B (en) 1984-06-30
SE7601800L (en) 1976-08-23
YU32676A (en) 1982-05-31
DE2607003A1 (en) 1976-09-02
JPS51108019A (en) 1976-09-25
DK146413C (en) 1984-03-12
IL49005A0 (en) 1976-04-30
FR2301509B1 (en) 1979-02-02
DE2607003C3 (en) 1980-04-17
NO146772B (en) 1982-08-30
ZA76678B (en) 1977-04-27
NO760557L (en) 1976-08-24
LU74382A1 (en) 1976-08-13
NL7601777A (en) 1976-08-24
BE838502A (en) 1976-08-12
SE426060B (en) 1982-12-06

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