US3133124A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Multi-stage nitration of cyclohexane
Assignee: Honeywell International Inc
•
Filing: 1961-02-16
•
Granted: 1964-05-12
•
Expires: 1981-02-16
Abstract
No abstract record available.
Inventors
- 👤 John H Bonfield
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 18:14
CPC Classifications
C; C07; C07C; C07C201/00; C07C201/06; C07C201/08; C07C2601/00; C07C2601/12; C07C2601/14
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
219 words
A MULTI-STAGE VAPOR PHASE PROCESS OF MONONITRATING AN ALKANE HAVING FROM 2 TO 7 CARBON ATOMS, COMPRISING: (A) MIXING VAPORS OF THE ALKANE AND VAPORS OF A NITRATING AGENT SELECTED FROM THE GROUP CONSISTING OF NITRIC ACID AND NITROGEN DIOXIDE IN THE ABSENCE OF LIQUID PHASE REACTANTS, IN THE PROPORTIONS OF AT LEAST 4 MOLS OF THE ALKANE PER MOL OF NITRIC ACID WHEN USING NITRIC ACID AS THE NITRATING AGENT, AND AT LEAST 1 MOL OF THE ALKANE PER MOL OF NITROGEN DIOXIDE CALCULATED AS NO2, WHEN USING NITROGEN DIOXIDE AS THE NITRATING AGENT AT A TEMPERATURE BELOW THAT AT WHICH SUBSTANTIAL NITRATION OCCURS; (B) PASSING THE RESULTANT VAPOR MIXTURE INTO THE FIRST OF A PLURALITY OF REACTION ZONES, IN EACH OF WHICH THE TEMPERATURE IS MAINTAINED WITHIN THE RANGE OF FROM 250* TO 375*C. AND THE RESIDENCE TIME FOR THE REACTANTS AND REACTION PRODUCTS IS AT LEAST 20 SECONDS; AND (C) ADMIXING THE REACTION PRODUCTS FROM EACH ZONE WITH ADDITIONAL VAPORS OF THE NITRATING AGENT PRIOR TO PASSAGE OF THE RESULTING MIXTURE TO A SUCCEEDING ZONE, THE OVERALL MOLAR RATIO OF THE ALKANE TO THE NITRATING AGENT SUPPLIED TO THE PROCESS BEING LOWER THAN 4 TO 1 WHEN USING NITRIC ACID AS THE NITRATING AGENT, AND 1 TO 1 WHEN USING NITROGEN DIOXIDE AS THE NITRATING AGENT.
Claim 2
Dependent Claim
219 words
A MULTI-STAGE VAPOR PHASE PROCESS OF MONONITRATING AN ALKANE HAVING FROM 2 TO 7 CARBON ATOMS, COMPRISING: (A) MIXING VAPORS OF THE ALKANE AND VAPORS OF A NITRATING AGENT SELECTED FROM THE GROUP CONSISTING OF NITRIC ACID AND NITROGEN DIOXIDE IN THE ABSENCE OF LIQUID PHASE REACTANTS, IN THE PROPORTIONS OF AT LEAST 4 MOLS OF THE ALKANE PER MOL OF NITRIC ACID WHEN USING NITRIC ACID AS THE NITRATING AGENT, AND AT LEAST 1 MOL OF THE ALKANE PER MOL OF NITROGEN DIOXIDE CALCULATED AS NO2, WHEN USING NITROGEN DIOXIDE AS THE NITRATING AGENT AT A TEMPERATURE BELOW THAT AT WHICH SUBSTANTIAL NITRATION OCCURS; (B) PASSING THE RESULTANT VAPOR MIXTURE INTO THE FIRST OF A PLURALITY OF REACTION ZONES, IN EACH OF WHICH THE TEMPERATURE IS MAINTAINED WITHIN THE RANGE OF FROM 250* TO 375*C. AND THE RESIDENCE TIME FOR THE REACTANTS AND REACTION PRODUCTS IS AT LEAST 20 SECONDS; AND (C) ADMIXING THE REACTION PRODUCTS FROM EACH ZONE WITH ADDITIONAL VAPORS OF THE NITRATING AGENT PRIOR TO PASSAGE OF THE RESULTING MIXTURE TO A SUCCEEDING ZONE, THE OVERALL MOLAR RATIO OF THE ALKANE TO THE NITRATING AGENT SUPPLIED TO THE PROCESS BEING LOWER THAN 4 TO 1 WHEN USING NITRIC ACID AS THE NITRATING AGENT, AND 1 TO 1 WHEN USING NITROGEN DIOXIDE AS THE NITRATING AGENT.
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) | 1967-05-12 | 1967-11-11 | 1968-05-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1971-05-12 | 1971-11-11 | 1972-05-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1975-05-12 | 1975-11-11 | 1976-05-12 | $7700.00 | Window Closed / Lapsed |