GB922650A - Improvements relating to processes for propagating chemical reactions - Google Patents
Improvements relating to processes for propagating chemical reactionsInfo
- Publication number
- GB922650A GB922650A GB3027659A GB3027659A GB922650A GB 922650 A GB922650 A GB 922650A GB 3027659 A GB3027659 A GB 3027659A GB 3027659 A GB3027659 A GB 3027659A GB 922650 A GB922650 A GB 922650A
- Authority
- GB
- United Kingdom
- Prior art keywords
- glycol
- acid
- liquid
- mass
- derived
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G85/00—General processes for preparing compounds provided for in this subclass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
- B01D1/222—In rotating vessels; vessels with movable parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/10—Vacuum distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
- B01J10/02—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor of the thin-film type
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
- C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
- C08G63/16—Dicarboxylic acids and dihydroxy compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
- C08G63/785—Preparation processes characterised by the apparatus used
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G67/00—Macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing oxygen or oxygen and carbon, not provided for in groups C08G2/00 - C08G65/00
- C08G67/04—Polyanhydrides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/04—Preparatory processes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Polyamides (AREA)
Abstract
A process for propogating a chemical reaction in a liquid reaction mass which is at chemical equilibrium and which contains incompletely reacted reactants and at least one relatively volatile product of the reaction that must be removed to enable the reaction to be driven to a desired degree of completion comprises removing the reaction product from the mass by a process which includes the steps of applying the mass to at least a part of a surface of revolution having an upright axis, the mass being applied thereto in such a way that it is caused to flow downwardly over the surface in a film under the influence of gravity and at a temperature and reduced pressure which are such that at least a portion of said reaction product will leave the film by evaporation, so shifting the equilibrium in a direction to permit incompletely reacted reactants to react further, wiping the surface so as to remove the liquid residue of said film therefrom, the wiping step being so performed as simultaneously to accelerate the downward movement of said residue, which latter includes the desired reaction product and to recover the removed residue. Preferably evaporation is effected in a thin film using the apparatus described in Specification 825,438 in which the liquid falls down under gravity, under vacuum, the evaporating surface being wiped with a plurality of axially overlapping wiping edges of separate wiping elements, the working faces of which have oblique slots which remove the liquid. The removed liquid may be reapplied to the surface located below the first portion. The process may be applied to the manufacture of (a) dioctyl phthalate or esters derived from carbonic, oxalic, succinic, glutaric, adipic, pimelic, sebacic, hexadecamethylene dicarboxylic or phthalic acids with ethylene glycol, polyethylene glycol, propylene glycol, trimethylene glycol, hexamethylene glycol or decamethylene glycol; and to polyesters derived from lactic acid, o -hydroxy decanoic acid and o -hydroxy-caproic acid (b) polyamides derived from pimelic, sebacic, phthalic and hexadecamethylene dicarboxylic acids, with pentamethylene diamine, benzidene, phenylene diamine and propylene diamine and from 5-amino caproic acid, 10-aminoundecanoic acid and caprolactam. (c) Polyethers derived from ethylene glycol, propylene glycol, trimethylene glycol, hexamethylene glycol, tripropylene glycol (d) polyanhydrides derived from adipic acid, pimelic acid, suberic acid, and hexadecamethylene dicarboxylic acid and (e) polyacetals derived from hydroxy aldehydes hydroxyketones or propionaldehydes, butyraldehyde benzaldehyde with glycols and (f) mixed polyesters-polyamides prepared by heating a mixture containing a dibasic acid , a glycol and a diamine. Specification 596,392 also is referred to.ALSO:A process for propagating a chemical reaction in a liquid reaction mass which is at chemical equilibrium and which contains incompletely reacted reactants and at least one relatively volatile product of the reaction that must be removed to enable the reaction to be driven to a desired degree of completion comprises removing the reaction product from the mass by a process which includes the steps of applying the mass to at least a part of a surface of revolution having an upright axis, the mass being applied thereto in such a way that it is caused to flow downwardly over the surface in a film under the influence of gravity and at a temperature and reduced pressure which are such that at least a portion of said reaction product will leave the film by evaporation, so shifting the equilibrium in a direction to permit incompletely reacted reactants to react further, wiping the surface so as to remove the liquid residue of said film therefrom, the wiping step being so performed as simultaneously to accelerate the downward movement of said residue, which latter includes the desired reaction product and to recover the removed residue. Preferably evaporation is effected in a thin film using the apparatus described in Specification 825,438 in which the liquid falls down under gravity, under vacuum, the evaporating surface being wiped with a plurality of axially overlapping wiping edges of separate wiping elements, the working faces of which have oblique slots which remove the liquid. The removed liquid may be reapplied to the surface located below the first portion. The process may be applied to the manufacture of (a) polyesters derived from carbonic, oxalic, succinic, glutaric, adipic, pimelic, sebacic, hexadecamethylene dicarboxylic or phthalic acids with ethylene glycol, polyethylene glycol, propylene glycol, trimethylene glycol, hexamethylene glycol or decamethylene glycol; and to polyesters derived from lactic acid, o -hydroxy decanoic acid and o -hydroxycaproic acid, (b) polyamides derived from pimelic, sebacic, phthalic and hexadecamethylene dicarboxylic acids, with pentamethylene diamine, benzidene, phenylene diamine and propylene diamine and from 5-amino caproic acid, 10-aminoundecanoic acid and caprolactam, (c) polyethers derived from ethylene glycol, propylene glycol, trimethylene glycol, hexamethylene glycol, tripropylene glycol, (d) polyanhydrides derived from adipic acid, pimelic acid, suberic acid, and hexadecamethylene dicarboxylic acid and (e) polyacetals derived from hydroxy aldehydes, hydroxy ketones or propionaldehydes, butyraldehyde benzaldehyde with glycols and (f) mixed polyesters-polyamides prepared by heating a mixture containing a dibasic acid, a glycol and a diamine. Specification 596,392 also is referred to.ALSO:A process for propagating an esterification reaction in a liquid reaction mass which is at chemical equilibrium and which contains incompletely reacted reactants comprises removing the water of esterification from the mass by a process which includes the steps of applying the mass to at least a part of a surface of revolution having an upright axis, the mass being applied thereto in such a way that it is caused to flow downwardly over the surface in a film under the influence of gravity and at a temperature and reduced pressure which are such that at least a portion of said water will leave the film by evaporation, so shifting the equilibrium in a direction to permit incompletely reacted reactants to react further, wiping the surface so as to remove the liquid residue of said film therefrom, the wiping step being so performed as simultaneously to accelerate the downward movement of said residue, which latter includes the desired ester and to recover the removed residue. Preferably evaporation is effected in a thin film using the apparatus described in Specification 825,438 in which the liquid falls down under gravity, under vacuum, the evaporating surface being wiped with a plurality of axially overlapping wiping edges of separate wiping elements, the working faces of which have oblique slots which remove the liquid. The removed liquid may be reapplied to the surface located below the first portion. The process may be applied to the manufacture of dioctyl phthalate by reacting phthalic anhydride with 2-ethylhexyl alcohol in the presence of carbon dioxide, which acts as a sweep gas and a mild catalyst. Zinc fluoride or zinc chloride may also be used as catalyst. The preparation of dioctyl and didecyl azelates, and of dioctyl sebacate, is referred to. Specification 596,392 also is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US75991958A | 1958-09-09 | 1958-09-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB922650A true GB922650A (en) | 1963-04-03 |
Family
ID=25057464
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3027659A Expired GB922650A (en) | 1958-09-09 | 1959-09-04 | Improvements relating to processes for propagating chemical reactions |
Country Status (3)
Country | Link |
---|---|
CH (1) | CH401049A (en) |
FR (1) | FR1240141A (en) |
GB (1) | GB922650A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104117333A (en) * | 2014-08-12 | 2014-10-29 | 无锡阿科力科技股份有限公司 | Device for producing polyetheramine by using continuous method |
CN113477087A (en) * | 2021-06-28 | 2021-10-08 | 浙江工业大学 | Polyester modified polysulfone ultrafiltration membrane and preparation method thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2447941A2 (en) * | 1979-02-01 | 1980-08-29 | Ato Chimie | Block poly(etheresteramide) co:polycondensates - prepd. in thin layer reactor between rotor and stator |
-
1959
- 1959-09-04 GB GB3027659A patent/GB922650A/en not_active Expired
- 1959-09-08 CH CH7798459A patent/CH401049A/en unknown
- 1959-09-09 FR FR804717A patent/FR1240141A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104117333A (en) * | 2014-08-12 | 2014-10-29 | 无锡阿科力科技股份有限公司 | Device for producing polyetheramine by using continuous method |
CN104117333B (en) * | 2014-08-12 | 2015-11-04 | 无锡阿科力科技股份有限公司 | The process units of continuity method polyetheramine |
CN113477087A (en) * | 2021-06-28 | 2021-10-08 | 浙江工业大学 | Polyester modified polysulfone ultrafiltration membrane and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
FR1240141A (en) | 1960-09-02 |
CH401049A (en) | 1965-10-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3681434A (en) | Batch distillation of phthalate esters with recycle and spraying | |
ES2305241T3 (en) | PROCESS TO PREPARE CARBOXILIC ACIDS AND DERIVATIVES OF THE SAME. | |
JPS5935372B2 (en) | Process for producing formic acid by hydrolysis of methyl formate | |
US3651125A (en) | Continuous method for formation of a liquid monomer for a condensation polymer | |
GB922650A (en) | Improvements relating to processes for propagating chemical reactions | |
US2644009A (en) | Continuous esterification process | |
US4112235A (en) | Transesterification of carboxylic acids | |
US3390135A (en) | Continuous polyester process | |
Ragaini et al. | Increasing the value of dilute acetic acid streams through esterification: Part I. Experimental analysis of the reaction zone | |
US3752861A (en) | Production of hydroxy compounds by hydrogenolysis of buffered carboxylate salts | |
EP0329337A2 (en) | The production of formic acid from a nitrogenous base, carbon dioxide and hydrogen | |
RU97120887A (en) | METHOD FOR PROCESSING REACTION MIXTURES FORMED BY CYCLOGEXANE OXIDATION | |
US3399035A (en) | Process for the recovery of boric acid from the oxidation mixtures of liquidphase oxidation of hydrocarbons | |
US3529002A (en) | Production of glycol monoesters of carboxylic acids | |
US3280183A (en) | Method of producing dicarboxylic acids | |
US2773094A (en) | Oxidation of fatty acids | |
GB952124A (en) | Preparation of polyesters | |
US1067665A (en) | Process for the manufacture of formaldehyde. | |
US2885436A (en) | Process for the purification of lactic acid | |
US1081959A (en) | Manufacture of acetic acid. | |
US3462500A (en) | Process for the purification of alcohols containing formic acid esters | |
ES473111A1 (en) | Process for working up distillation residues from the hydroformylation of propene | |
US4822518A (en) | Convenient synthesis of polyamide polyol/urethane diol blends | |
SU1704628A3 (en) | Method for preparation hydroformylation medium | |
US3119849A (en) | Esterification process |