US3310592A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing high purity benzene
Assignee: Mitsubishi Chemical Corp
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Filing: 1965-04-19
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Granted: 1967-03-21
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Expires: 1985-04-19
Abstract
No abstract record available.
Inventors
- 👤 Fukuda Junichi
- 👤 Suzuki Yasuo
- 👤 Ikebe Munetaka
- 👤 Sagara Mitsuo
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:13
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/04; C10G65/06; C10G2400/00; C10G2400/30
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
197 words
A PROCESS FOR PRODUCING HIGH PURITY BENZENE WHICH COMPRISES: (A) AS FIRST PROCESS STEP, CONTACTING THE 60-200*C. FRACTION OF CRACKED OILS, WHICH ARE THE BY-PRODUCT IN THE PRODUCTION OF GASEOUS OLEFINS BY STEAM CRACKING PETROLEUM HYDROCARBONS, WITH HYDROGEN IN A MOLAR PROPORTION OF CRACKED OIL FRACTION:HYDROGEN OF 1:0.2 TO 2.00 AT A TEMPERATURE FROM AMBIENT TEMPERATURE TO 250*C. AND A PRESSURE OF AT LEAST 10 KG./CM.2 IN THE PRESENCE OF HYDROGENATION CATALYST, TO CONVERT THE DIOLEFINS CONTAINED IN SAID FRACTION TO MONO-OLEFINS AND/OR PARAFFIN HYDROCARBONS; (B) AS SECOND PROCESS STEP, CONTACTING THE OIL OBTAINED IN STEP (A) WITH HYDROGEN IN A MOLAR PROPORTION OF OIL:HYDROGEN OF 1:2 TO 10 AT A TEMPERATURE OF 500* TO 800*C. AND A PRESURE OF AT LEAST 10 KG./CM.2 IN THE ABSENCE OF SOLID DEALKYLATION CATALYST, TO HYDROCRACK MONO-OLEFINS AND/OR PARAFFIN HYDROCARBONS AS WELL AS TO DEALKYLATE ALKYL-SUBSTITUTED AROMATIC HYDROCARBONS CONTAINED IN SAID LAST-NAMED OIL, AND (C) AS THIRD PROCESS STEP, HEATING THE RESULTANT PRODUCT OF THE SECOND STEP OF 150* TO 200*C. IN THE PRESENCE OF HYDRODESULFURATION CATALYST TO DECOMPOSE AND REMOVE SULFUR COMPOUNDS CONTAINED IN SAID PRODUCT, AND (D) THEREAFTER SEPARATING BENZENE FROMTHE RESULTANT LIQUID PRODUCT OF THE THIRD STEP.
Claim 2
Dependent Claim
197 words
A PROCESS FOR PRODUCING HIGH PURITY BENZENE WHICH COMPRISES: (A) AS FIRST PROCESS STEP, CONTACTING THE 60-200*C. FRACTION OF CRACKED OILS, WHICH ARE THE BY-PRODUCT IN THE PRODUCTION OF GASEOUS OLEFINS BY STEAM CRACKING PETROLEUM HYDROCARBONS, WITH HYDROGEN IN A MOLAR PROPORTION OF CRACKED OIL FRACTION:HYDROGEN OF 1:0.2 TO 2.00 AT A TEMPERATURE FROM AMBIENT TEMPERATURE TO 250*C. AND A PRESSURE OF AT LEAST 10 KG./CM.2 IN THE PRESENCE OF HYDROGENATION CATALYST, TO CONVERT THE DIOLEFINS CONTAINED IN SAID FRACTION TO MONO-OLEFINS AND/OR PARAFFIN HYDROCARBONS; (B) AS SECOND PROCESS STEP, CONTACTING THE OIL OBTAINED IN STEP (A) WITH HYDROGEN IN A MOLAR PROPORTION OF OIL:HYDROGEN OF 1:2 TO 10 AT A TEMPERATURE OF 500* TO 800*C. AND A PRESURE OF AT LEAST 10 KG./CM.2 IN THE ABSENCE OF SOLID DEALKYLATION CATALYST, TO HYDROCRACK MONO-OLEFINS AND/OR PARAFFIN HYDROCARBONS AS WELL AS TO DEALKYLATE ALKYL-SUBSTITUTED AROMATIC HYDROCARBONS CONTAINED IN SAID LAST-NAMED OIL, AND (C) AS THIRD PROCESS STEP, HEATING THE RESULTANT PRODUCT OF THE SECOND STEP OF 150* TO 200*C. IN THE PRESENCE OF HYDRODESULFURATION CATALYST TO DECOMPOSE AND REMOVE SULFUR COMPOUNDS CONTAINED IN SAID PRODUCT, AND (D) THEREAFTER SEPARATING BENZENE FROMTHE RESULTANT LIQUID PRODUCT OF THE THIRD STEP.
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) | 1970-03-20 | 1970-09-19 | 1971-03-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1974-03-20 | 1974-09-19 | 1975-03-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1978-03-20 | 1978-09-19 | 1979-03-21 | $7700.00 | Window Closed / Lapsed |