US4085129A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the preparation of chloroformic acid aryl esters and cyclic carbonates
Assignee: Hoechst AG
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Filing: 1976-09-28
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Granted: 1978-04-18
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Expires: 1996-09-28
Abstract
Abstract A process for the preparation of chloroformic acid aryl-esters and cyclic carbonates of aryl compounds containing at least two phenolic hydroxy groups wherein aromatic compounds containing one or more hydroxy groups linked to an aromatic nucleus, are reacted with phosgene in the presence of catalytic amounts of N,N-disubstituted acid amide either under pressure or without pressure while removing the hydrogen chloride continuously from the reaction mixture. This improved process results in almost quantitative or very high yields of pure products and avoids problems such as disposal of waste water.
Inventors
- 👤 Gunther Semler
- 👤 Georg Schaeffer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 07:12
CPC Classifications
C; C07; C07C; C07C69/00; C07C69/96; C07C68/00; C07C68/02; C07D; C07D317/00; C07D317/08; C07D317/44; C07D317/70
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
172 words
A process for preparation of chloroformic acid aryl esters in high yields comprising the steps of: forming a liquid phase reaction mixture in a reaction zone, said reaction mixture comprising a phenol or naphthol and from 0.5 to about 20 mol percent of said phenol or naphthol of an N,N-dialkyl acid amide; introducing phosgene into said liquid phase reaction mixture in said reaction zone and reacting said phosgene and said phenol or naphthol at a temperature of 30° to 180° C and at a pressure of from atmospheric pressure to six atmospheres; continuously venting gases from said reaction zone during the course of said reaction, said vented gases including unreacted phosgene and by-product hydrogen chloride, and thereby maintaining a molar ratio of phosgene to phenol or naphthol, in said liquid phase reaction mixture, in the range of from 0.01 to 0.95, until 80% of said phenol or naphthol has been converted; and thereafter removing the liquid phase reaction mixture from the said reaction zone and recovering the chloroformic acid aryl esters therein.
Claim 2
Dependent Claim
172 words
A process for preparation of chloroformic acid aryl esters in high yields comprising the steps of: forming a liquid phase reaction mixture in a reaction zone, said reaction mixture comprising a phenol or naphthol and from 0.5 to about 20 mol percent of said phenol or naphthol of an N,N-dialkyl acid amide; introducing phosgene into said liquid phase reaction mixture in said reaction zone and reacting said phosgene and said phenol or naphthol at a temperature of 30° to 180° C and at a pressure of from atmospheric pressure to six atmospheres; continuously venting gases from said reaction zone during the course of said reaction, said vented gases including unreacted phosgene and by-product hydrogen chloride, and thereby maintaining a molar ratio of phosgene to phenol or naphthol, in said liquid phase reaction mixture, in the range of from 0.01 to 0.95, until 80% of said phenol or naphthol has been converted; and thereafter removing the liquid phase reaction mixture from the said reaction zone and recovering the chloroformic acid aryl esters therein.
Claim 3
Dependent Claim
61 words
A process as claimed in claim 1, wherein substituted phenols or substituted naphthols are reacted which contain as substituents halogen atoms, nitro groups, alkyl groups having from 1 to 18 carbon atoms, substituted phenyl radicals, alkoxy groups having from 1 to 5 carbon atoms, substituted phenoxy groups or substituted aralkyl radicals having alkylene groups of from 1 to 6 carbon atoms.
Claim 4
Dependent Claim
136 words
A process as claimed in claim 1, wherein the phenols and naphthols are of the formula ##STR5## wherein R 1 , R 2 , R 4 and R 5 each is identical or different and represents hydrogen atoms, alkyl groups having from 1 to 12 carbon atoms, alkoxy groups having from 1 to 4 carbon atoms or halogen atoms or R 1 and R 2 and/or R 4 and R 5 together represent a condensed benzene radical, R 3 and R 6 which may be identical or different, each represents hydrogen atoms or chlorine atoms or nitro groups, A is a direct linkage, an oxygen atom or a lower alkylene or cycloalkylene group having up to 6 carbon atoms, n is a whole number from 1 to 3 and m is zero or 1 or 2.
Claim 5
Dependent Claim
103 words
A process as claimed in claim 1, wherein the phenolic compounds are of the formula ##STR6## wherein R 1 , R 2 , R 4 and R 5 are identical or different and each represents a hydrogen, a chlorine or a bromine atom, alkyl groups having from 1 to 6 carbon atoms, alkoxy groups having from 1 to 4 carbon atoms or R 1 and R 2 together represent a condensed benzene radical, A is a direct linkage, an oxygen atom or an alkylene group having from 1 to 3 carbon atoms, n is 1 or 2 and m is zero or 1.
Claim 6
Dependent Claim
15 words
A process a claimed in claim 1, wherein the reaction is effected under atmospheric pressure.
Claim 7
Dependent Claim
78 words
A process as claimed in claim 1, wherein carboxylic acid amides disubstituted at the nitrogen atoms of the formula ##STR7## are used wherein R and R' each represents a lower alkyl radical or together an alkylene radical having from 4 to 6 carbon atoms and X represents a hydrogen atom, a lower alkyl radical or a low-molecular dialkyl-amino group and R and R' and X together may represent an alkylene group having from 3 to 5 carbon atoms.
Claim 8
Dependent Claim
14 words
A process as claimed in claim 1, wherein N,N-dimethyl-formamide or N,N,N',N'-tetramethyl urea is used.
Claim 9
Dependent Claim
39 words
A process as claimed in claim 1, wherein the reaction product of N,N-dialkylated carboxylic acid amide with phosgene or with chloroformic acid phenyl ester of the formula ##STR8## are used wherein R, R' and X are defined as above.
Claim 10
Dependent Claim
22 words
A process as claimed in claim 1, wherein the reaction is carried out at a temperature of from 40° to 180° C.
Claim 11
Dependent Claim
22 words
A process as claimed in claim 1, wherein the reaction is carried out at a temperature of from 40° to 130° C.
Claim 12
Dependent Claim
22 words
A process as claimed in claim 1, wherein the reaction is carried out at a temperature of from 70° to 130° C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-04-17 | 1981-10-17 | 1982-04-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-04-17 | 1985-10-17 | 1986-04-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-04-17 | 1989-10-17 | 1990-04-18 | $7700.00 | Window Closed / Lapsed |