US3265735A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Manufacture of para-chloroaniline and para-aminophenol
Assignee: Frontier Chemical Co
•
Filing: 1964-06-15
•
Granted: 1966-08-09
•
Expires: 1984-06-15
Abstract
No abstract record available.
Inventors
- 👤 Walter C Bradbury
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 10:28
CPC Classifications
C; C07; C07C; C07C213/00; C07C213/02
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
164 words
A PROCESS FOR THE MANUFACTURE OF P-CHLOROANILINE AS THE PRINCIPAL PRODUCT AND P-AMINOPHENOL AS A SECONDARY PRODUCT WHICH COMPRISES MAINTAINING AQUEOUS HYDROCHLORIC ACID CONTAINING ABOUT 5 TO 38% HCL, A SOLID ADSORBENT AND A PLATINUM METAL CATALYST IN INTIMATE CONTACT IN A REACTION ZONE AT A REACTION TEMPERATURE OF BETWEEN ABOUT 50* TO 135*C. AND AT A PRESSUURE SUFFICIENT TO MAINTAIN AN AQUEOUS LIQUID PHASE IN SAID REACTION ZONE BUT NOT GREATER THAN 50 P.S.I.G., ADDING NITROBENZENE TO SAID REACTION ZONE IN A PROPORTION SUCH AS TO GIVE AN HCI/NITROBENZENE RATIO BETWEEN 4/1 AND 8/1 AND SUCH THAT IT IS SUBSTANTIALLY COMPLETELY ADSORBED ON SAID ADSORBENT WITHOUT FORMING A SEPARATE ORGANIC PHASE IN SAID REACTION ZONE, THEREBY FORMING A REACTION MIXTURE WHICH COMPRISES AN AQUEOUS PHASE AND A NITROBENZENE-CONTAINING SOLID PHASE, CONTACTING MOLECULAR HYDROGEN WITH SAID REACTION MIXTURE AT SAID REACTION TEMPERATURE, MECHANICALLY SEPARATING THE SOLID ADSORBENT AND CATALYST FROM THE RESULTING AQUEOUS LIQUID PRODUUCT, AND RECOVERING PARA-CHLOROANILINE AND PARAAMINOPHENOL FROM SAID AQUEOUS PRODUCT.
Claim 2
Dependent Claim
164 words
A PROCESS FOR THE MANUFACTURE OF P-CHLOROANILINE AS THE PRINCIPAL PRODUCT AND P-AMINOPHENOL AS A SECONDARY PRODUCT WHICH COMPRISES MAINTAINING AQUEOUS HYDROCHLORIC ACID CONTAINING ABOUT 5 TO 38% HCL, A SOLID ADSORBENT AND A PLATINUM METAL CATALYST IN INTIMATE CONTACT IN A REACTION ZONE AT A REACTION TEMPERATURE OF BETWEEN ABOUT 50* TO 135*C. AND AT A PRESSUURE SUFFICIENT TO MAINTAIN AN AQUEOUS LIQUID PHASE IN SAID REACTION ZONE BUT NOT GREATER THAN 50 P.S.I.G., ADDING NITROBENZENE TO SAID REACTION ZONE IN A PROPORTION SUCH AS TO GIVE AN HCI/NITROBENZENE RATIO BETWEEN 4/1 AND 8/1 AND SUCH THAT IT IS SUBSTANTIALLY COMPLETELY ADSORBED ON SAID ADSORBENT WITHOUT FORMING A SEPARATE ORGANIC PHASE IN SAID REACTION ZONE, THEREBY FORMING A REACTION MIXTURE WHICH COMPRISES AN AQUEOUS PHASE AND A NITROBENZENE-CONTAINING SOLID PHASE, CONTACTING MOLECULAR HYDROGEN WITH SAID REACTION MIXTURE AT SAID REACTION TEMPERATURE, MECHANICALLY SEPARATING THE SOLID ADSORBENT AND CATALYST FROM THE RESULTING AQUEOUS LIQUID PRODUUCT, AND RECOVERING PARA-CHLOROANILINE AND PARAAMINOPHENOL FROM SAID AQUEOUS PRODUCT.
References Cited (Backward Citations)
US2198249A
Cited
US2765342A
Cited
US2772313A
Cited
US2884458A
Cited
US3073865A
Cited
US3093685A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1969-08-08 | 1970-02-07 | 1970-08-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1973-08-08 | 1974-02-07 | 1974-08-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1977-08-08 | 1978-02-07 | 1978-08-09 | $7700.00 | Window Closed / Lapsed |