IPC분류정보
국가/구분 |
United States(US) Patent
공개
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0935024
(2001-08-22)
|
공개번호 |
US-0066703
(2002-06-06)
|
우선권정보 |
DE-10041197.5 (2000-08-23) |
발명자
/ 주소 |
- Wagner, Paul
- Klausener, Alexander
|
대리인 / 주소 |
|
인용정보 |
피인용 횟수 :
0 인용 특허 :
0 |
초록
▼
The invention relates to a process for preparing trimethylolpropane with simultaneous formation of formate salts of the formula M(OOCH)n (I), where M represents the alkali metals lithium, sodium, potassium, rubidium, caesium and/or the alkaline earth metals beryllium, calcium, strontium,
The invention relates to a process for preparing trimethylolpropane with simultaneous formation of formate salts of the formula M(OOCH)n (I), where M represents the alkali metals lithium, sodium, potassium, rubidium, caesium and/or the alkaline earth metals beryllium, calcium, strontium, barium and n is 1 when M is an alkali metal and is 2 when M is an alkaline earth metal, where n-butyraldehyde, formaldehyde and a base are reacted by the inorganic Cannizzaro process and the reaction mixture formed is subjected to vapour pressure filtration as a suspension, if appropriate after partly removing distillable constituents, such as water.
대표청구항
▼
1. A process for preparing trimethylolpropane with simultaneous formation of formate salts of the formula (I): (I),wherein M is a metal selected from the group consisting of alkali metals, alkaline earth metals, and mixtures thereof, wherein n is 1 when M is an alkali metal and n is 2 wh
1. A process for preparing trimethylolpropane with simultaneous formation of formate salts of the formula (I): (I),wherein M is a metal selected from the group consisting of alkali metals, alkaline earth metals, and mixtures thereof, wherein n is 1 when M is an alkali metal and n is 2 when M is an alkaline earth metal, the process comprising reacting n-butyraldehyde and formaldehyde by an inorganic Cannizzaro process, forming a reaction mixture, and subjecting the reaction mixture formed to vapor pressure filtration. 2. The process according to claim 1, wherein M represents sodium or calcium. 3. The process according to claim 1, wherein formate salt is isolated and has a residual moisture content of <3.5% by weight. 4. The process according to claim 1, wherein the vapor pressure filtration is carried out continuously. 5. The process according to claim 1, wherein the differential pressure in the vapor pressure filtration is from 0 to 6 bar. 6. The process according to claim 1, wherein a filter cake is formed in the vapor pressure filtration and the filter cake is subjected to at least one washing step during the filtration procedure. 7. The process according to claim 6, wherein the washing of the cake is carried out using a fully saturated or partially saturated aqueous solution of the formate salt to be isolated. 8. The process according to claim 7, wherein distillable constituents are partly separated from the resulting reaction mixture prior to the formate salt being separated off. 9. The process according to claim 6, wherein cake formation, cake washing, vapor treatment of the cake and demoisterizataion of the cake are carried out during the vapor pressure filtration. 10. The process according to claim 9, wherein in the vapor treatment of the cake, the filter cake of formate salt to be separated off formed on the filter area is treated with a gaseous treatment fluid whose pressure and temperature are set so that the treatment fluid condenses in the filter cake, optionally initially in the uppermost layer of the filter cake farthest from the filter area, so that a condensation front is formed along this layer and that, in addition, the filter cake is heated to the temperature of the gaseous treatment fluid progressively from the uppermost layer in the direction of the filter area, so that the condensation front at the phase boundary between the gaseous treatment fluid and the liquid is shifted towards the filter area. 11. The process according to claim 9, wherein in the demoisturization of the cake, the filter cake of formate salt to be separated off formed on the filter area is treated with compressed inert gas and/or compressed air. 12. The process according to claim 1, wherein the reaction mixture after the vapor pressure filtration is subjected to at least one further purification and drying step which comprises a recrystallization from and redispersion in a solvent, or redispersion in a solvent. 13. The process according to claim 12, wherein the solvent is water or a water-containing mixture.
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