WO1999012876A1 - Procede de production d'alkyleneglycols - Google Patents
Procede de production d'alkyleneglycols Download PDFInfo
- Publication number
- WO1999012876A1 WO1999012876A1 PCT/RU1998/000087 RU9800087W WO9912876A1 WO 1999012876 A1 WO1999012876 A1 WO 1999012876A1 RU 9800087 W RU9800087 W RU 9800087W WO 9912876 A1 WO9912876 A1 WO 9912876A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- acid
- alkyleneglycols
- anion
- producing
- hydration
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/09—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
- C07C29/10—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes
- C07C29/103—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers
- C07C29/106—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers of oxiranes
Definitions
- diluted alkylene glycol products are used, which will consume more energetic waste of water.
- the method of producing alkylene glycol by the interaction of alkylene oxide with water in the presence of a catalytic system including a solid material is known. having electrical centers that are directly connected to anions other than metal or galogen anion.
- the solid material is an anion-exchanging resin with four-part ammonium groups, and the anion is a biocompositing agent and / or consuming drugs (95)
- the best solid materials in this way are materials containing lower t-alkylalkylamines and trimethylbenzylammonium groups.
- the process of the production of alkylene glycols by the catalytic hydration of oxides of alkylene at 20–250 ° ⁇ and pressure up to 3 ieriPa in the presence of anhydride in hydrogen is known.
- the catalytic converter used is anionite ⁇ 5 ⁇ -1, in the form of electri- cally favorable centers that consume nitrogen atoms of methylbenzylamino.
- a disadvantage of the method is the difficulty of isolating glycols from a mixture with carb-batteries due to the proximity of the temperature of the storage of diglycules and tanks.
- the closest analogue to the shortest means is the means of doing so.
- Suitable source materials for the production of the catalytic system for the invention are foreign exchangeable materials: , ⁇ -1 - ( ⁇ ig.16), ⁇ -1 -
- Electronic systems can also be obtained from other well-known foreign exchange materials of various kinds. For example, they have 25 investigative processes:
- acid uses sulfuric acid, carbonic acid, acid, boric acid, brown acid, acid, and carbon dioxide, containing 1–20 hydrocarbons.
- the facility in the facility was maintained in the range of 20-100 ° ⁇ . Pressure 1.0 ⁇ Pa. At the exit, the mixture was removed,% wt: ⁇ -2.14; ethylene glycol (EG) -34.1; diethylene
- the multiplicity of the formation of the monoglycol ( ⁇ ) is 98.1%.
- Example 2 The process was carried out in the process of displacing a volume of 50 ml, filled with a foreign exchange, which is electrically inactive.
- the pressure in the reactor is 40-100 ° ⁇ , the pressure is 1.9 ⁇ Pa.
- the mixture was removed, wt%: S-2,66; ⁇ yleneglycol (GH) - 44.9; di- ⁇ yleneglycol (DPG) - 1.18; ⁇ 2 -0,00 ⁇ , water - other. Degree of Conversion ⁇ P-
- the electrically powered centers are connected to the hydraulic anion ( ⁇ 0 ⁇ ) and the anion ( ⁇ " ).
- the exchange capacity is min / min.
- the receptor in the reactant is maintained in the range of 60-110 ° ⁇ .
- the mixture was fed,% wt: water-74.87; ⁇ -25.1; ⁇ 2 -0.03 at a speed of 112.5 g / h, the mixture that was discharged from the mixture 5 g / hour of ethylene oxide and directed to the entrance of the reacting cascade.
- the mixture On a regular basis, coming out of the second factory, added 34.5
- the process was carried out in a cas- cade of the processes described in Example 3 and completed by exchanges of two electrical components.
- the electrical centers are connected to the sulfide - anion (W0 3 ⁇ ) and the hydrogen - anion ((30 4 ⁇ ).
- the exchange volume for the sulphite is an anion of 1.4 mg-eq / ml, but the hydrosulfate is an anion of 0.4 mg-eq / ml.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Cette invention se rapporte au domaine des procédés catalytiques permettant de produire des alkylèneglycols. Cette invention concerne plus particulièrement un procédé de préparation d'alkylèneglycols consistant à hydrater des oxydes d'alkylène. Cette hydratation se déroule en présence d'un système catalytique à base de matériaux polymères à échange ionique et contenant de l'azote, lesquels matériaux contiennent en qualité de centres électriques positifs des atomes d'azote qui sont coordonnés à des anions. Au moins un des centres électriques positifs est coordonné à un anion d'acides di- et/ou tri- et/ou polybasiques dont au moins un atome d'hydrogène est substitué par un ion d'un atome de métal du groupe I de la classification périodique et/ou par un ion d'ammonium. L'hydratation des oxydes d'alkylène peut se faire à une température de 20 à 200° C et à une pression de 0,6 à 5,0 MPa. La température et la pression varient de préférence dans des plages allant de 80 à 130° C et de 1,0 à 2,0 MPa, respectivement.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU97114713 | 1997-09-09 | ||
RU97114713A RU2122995C1 (ru) | 1997-09-09 | 1997-09-09 | Способ получения алкиленгликолей |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1999012876A1 true WO1999012876A1 (fr) | 1999-03-18 |
Family
ID=20196822
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/RU1998/000087 WO1999012876A1 (fr) | 1997-09-09 | 1998-03-27 | Procede de production d'alkyleneglycols |
Country Status (2)
Country | Link |
---|---|
RU (1) | RU2122995C1 (fr) |
WO (1) | WO1999012876A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6448456B1 (en) | 2001-05-31 | 2002-09-10 | The Dow Chemical Company | Process for the preparation of alkylene glycols |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AR069726A1 (es) * | 2007-07-20 | 2010-02-17 | Shell Int Research | Proceso de preparacion de glicoles alquileno |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4393254A (en) * | 1981-01-12 | 1983-07-12 | Texaco Inc. | Process for the production of alkylene glycols |
EP0156447A2 (fr) * | 1984-03-28 | 1985-10-02 | Union Carbide Corporation | Production de monoalkylène glycol augmentée par le dioxyde de carbone |
EP0160330A1 (fr) * | 1984-03-28 | 1985-11-06 | Union Carbide Corporation | Procédé de production d'éthylèneglycols en présence de solides contenant des metalates |
RU2001901C1 (ru) * | 1992-05-19 | 1993-10-30 | Государственное научно-производственное предпри тие "Совинтех" | Способ получени алкиленгликолей |
RU2002726C1 (ru) * | 1992-05-19 | 1993-11-15 | Государственное научно-производственное предпри тие "Совинтех" | Способ получени алкиленгликолей |
-
1997
- 1997-09-09 RU RU97114713A patent/RU2122995C1/ru active
-
1998
- 1998-03-27 WO PCT/RU1998/000087 patent/WO1999012876A1/fr active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4393254A (en) * | 1981-01-12 | 1983-07-12 | Texaco Inc. | Process for the production of alkylene glycols |
EP0156447A2 (fr) * | 1984-03-28 | 1985-10-02 | Union Carbide Corporation | Production de monoalkylène glycol augmentée par le dioxyde de carbone |
EP0160330A1 (fr) * | 1984-03-28 | 1985-11-06 | Union Carbide Corporation | Procédé de production d'éthylèneglycols en présence de solides contenant des metalates |
RU2001901C1 (ru) * | 1992-05-19 | 1993-10-30 | Государственное научно-производственное предпри тие "Совинтех" | Способ получени алкиленгликолей |
RU2002726C1 (ru) * | 1992-05-19 | 1993-11-15 | Государственное научно-производственное предпри тие "Совинтех" | Способ получени алкиленгликолей |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6448456B1 (en) | 2001-05-31 | 2002-09-10 | The Dow Chemical Company | Process for the preparation of alkylene glycols |
US6479715B1 (en) | 2001-05-31 | 2002-11-12 | Dow Global Technologies Inc. | Process for the preparation of alkylene glycols |
Also Published As
Publication number | Publication date |
---|---|
RU2122995C1 (ru) | 1998-12-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU736421B2 (en) | Process for producing alkylene glycol | |
CN101184717B (zh) | 乙醇酸的制造方法 | |
KR950014164A (ko) | 이중 금속 시안화 복합(double metal cyanide complex)촉매, 그 제조방법, 그 촉매를 이용한 에폭시드 중합체 제조방법 및 그 촉매를 이용하여 제조된 에폭시드 중합체 | |
CN101928389B (zh) | 一种缩水甘油醚基封端烯丙醇聚氧乙烯醚的制备方法 | |
CA2771440A1 (fr) | Procede continu pour la fabrication de polycarbonate aliphatique a partir de dioxyde de carbone et de composes epoxydes | |
WO1994001362A1 (fr) | Procede de production de nitrate d'hydroxylammonium de grande purete | |
CN100532371C (zh) | 丙烯环氧化制备环氧丙烷的方法 | |
KR100447357B1 (ko) | 알킬렌글리콜의제조방법 | |
WO1999012876A1 (fr) | Procede de production d'alkyleneglycols | |
WO1997033850A1 (fr) | Procede de production d'alcyleneglycols | |
CN112939924B (zh) | 环状碳酸酯的制备方法 | |
CA1133522A (fr) | Procede assurant l'hydrolyse des oxydes d'alkylene en alkyleneglycols | |
CN111018727A (zh) | 甘氨酸的生产方法 | |
US9518035B2 (en) | Method for preparing glycidol using glycerol and glycidol obtained thereby | |
CN108728656A (zh) | 一种含稀土废料的分离回收方法 | |
CN111747908B (zh) | 一种合成环氧环己烷的方法 | |
CN1978427A (zh) | 超声波辐射下环己酮肟重排制备ε-己内酰胺的方法 | |
KR960015308B1 (ko) | 고선택적 흡수력을 지닌 붕소 수지 | |
EP0656876B1 (fr) | Procede de preparation de 2-n-butyl-2-ethyl-1-3-propane diol | |
CN1693302A (zh) | 低压溶剂化均相反应生产氨基甲酸甲酯的方法 | |
KR20080038284A (ko) | 에피클로로히드린의 제조방법 | |
CN118164832A (zh) | 一种1,6-己二醛的制备方法 | |
CN1126712C (zh) | 基于硝酸的二氧化氯生产方法 | |
CN115819261B (zh) | 一种季铵化对苯二甲酸双羟乙酯及其制备方法和应用 | |
CN1297878A (zh) | 用碱性阴离子交换树脂催化合成丁酮醇的工艺方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
122 | Ep: pct application non-entry in european phase | ||
NENP | Non-entry into the national phase |
Ref country code: CA |