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US3310592A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing high purity benzene

Assignee: Mitsubishi Chemical Corp
•
Filing: 1965-04-19
•
Granted: 1967-03-21
•
Expires: 1985-04-19
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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)

US2957925A Cited
US2876268A Cited
US3150196A Cited
US3213150A Cited
US3222410A Cited

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

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