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US3928170A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for manufacturing petroleum pitch having high aromaticity

Assignee: Kureha Corp
•
Filing: 1974-08-22
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Granted: 1975-12-23
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Expires: 1994-08-22
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Abstract

Abstract Method of producing a pitch suitable for a binder, said method comprising bringing petroleum base residual oil into direct contact with a non-oxidative gaseous heat transfer medium to subject said oil to cracking poly-condensation.

Inventors

  • 👤 Ryoichi Takahashi
  • 👤 Takuji Hosoi
  • 👤 Takaaki Aiba
  • 👤 Tsutomu Konno

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 20:50
CPC Classifications
C; C10; C10G; C10G51/00; C10G51/02; C10G51/023; C10C; C10C3/00; C10C3/002

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 204 words
A PROCESS FOR THE LIQUID PHASE CRACKING AND AROMATIZATION OF A REDUCED CRUDE OIL RESIDUUM CONSISTING ESSENTIALLY OF ALIPHATIC HYDROCARBONS TO PRODUCE PITCH HAVING A H/C RATIO OF 0.4 - 1.1 AND A NON-PITCH OIL CONTAINING A MAJOR PORTION OF ALIPHATIC HYDROCARBONS, SAID PROCESS COMPRISING: PROVIDING, IN A REACTION ZONE, A VAPOR PHASE AND A CONTINUOUS LIQUID PHASE, WHICH INCLUDES SAID RESIDUUM, AT A TOTAL PRESSURE LESS THAN 3.0 KG/CM2G WITH A LIQUID DWELL TIME OF 0.5 TO 20 HOURS; FEEDING A NON-OXIDATIVE HEAT TRANSFER MEDIUM AT A TEMPERATURE WITHIN THE RANGE OF 400*C TO 2000*C THROUGH AND IN DIRECT CONTACT WITH SAID LIQUID PHASE AT A TEMPERATURE OF ,TO MAINTAIN SAID LIQUID PHASE AT A TEMPERATURE OF 350*-450*C, TO INDUCE A POLYCONDENSATION REACTION IN SAID LIQUID PHASE, AND TO STRIP VOLATILE COMPONENTS FROM SAID LIQUID PHASE; CONTROLLING THE FEED RATE OF SAID HEAT TRANSFER MEDIUM TO MAINTAIN THE PARTIAL PRESSURE IN MMHG OF ORGANICS IN SAID VAPOR PHASE AT LESS THAN ABOUT; 1.03 X (10)11 X E- (1200/R+220) WHEREIN T IS THE TEMPERATURE (*C) OF THE LIQUID PHASE WITHIN THE REACTION ZONE; AND REMOVING A NON-PITCH OVERHEAD FROM SAID REACTION ZONE AND RECOVERING SAID PITCH AS THE BOTTOMS PRODUCT OF SAID REACTION ZONE.
Claim 2
Dependent Claim 204 words
A PROCESS FOR THE LIQUID PHASE CRACKING AND AROMATIZATION OF A REDUCED CRUDE OIL RESIDUUM CONSISTING ESSENTIALLY OF ALIPHATIC HYDROCARBONS TO PRODUCE PITCH HAVING A H/C RATIO OF 0.4 - 1.1 AND A NON-PITCH OIL CONTAINING A MAJOR PORTION OF ALIPHATIC HYDROCARBONS, SAID PROCESS COMPRISING: PROVIDING, IN A REACTION ZONE, A VAPOR PHASE AND A CONTINUOUS LIQUID PHASE, WHICH INCLUDES SAID RESIDUUM, AT A TOTAL PRESSURE LESS THAN 3.0 KG/CM2G WITH A LIQUID DWELL TIME OF 0.5 TO 20 HOURS; FEEDING A NON-OXIDATIVE HEAT TRANSFER MEDIUM AT A TEMPERATURE WITHIN THE RANGE OF 400*C TO 2000*C THROUGH AND IN DIRECT CONTACT WITH SAID LIQUID PHASE AT A TEMPERATURE OF ,TO MAINTAIN SAID LIQUID PHASE AT A TEMPERATURE OF 350*-450*C, TO INDUCE A POLYCONDENSATION REACTION IN SAID LIQUID PHASE, AND TO STRIP VOLATILE COMPONENTS FROM SAID LIQUID PHASE; CONTROLLING THE FEED RATE OF SAID HEAT TRANSFER MEDIUM TO MAINTAIN THE PARTIAL PRESSURE IN MMHG OF ORGANICS IN SAID VAPOR PHASE AT LESS THAN ABOUT; 1.03 X (10)11 X E- (1200/R+220) WHEREIN T IS THE TEMPERATURE (*C) OF THE LIQUID PHASE WITHIN THE REACTION ZONE; AND REMOVING A NON-PITCH OVERHEAD FROM SAID REACTION ZONE AND RECOVERING SAID PITCH AS THE BOTTOMS PRODUCT OF SAID REACTION ZONE.
Claim 3
Dependent Claim 73 words
The method of claim 1 wherein said petroleum base residual oil is preheated to a temperature of 450*C - 520*C by passing said residual oil through a tubular system where the outlet temperature is within the range of 450*C to 520*C and the outlet pressure within the range of 0 to 150 kg/cm2G, maintaining the dwell time of the residual oil in the tubular system within the range of 0.5 to 5.0 minutes.
Claim 4
Dependent Claim 26 words
The method of claim 1 wherein said non-oxidative gaseous heat transfer medium is selected from the group consisting of nitrogen, argon, steam, hydrogen and hydrocarbon gases.
Claim 5
Dependent Claim 30 words
The method of claim 1 wherein said liquid phase temperature and said partial pressure of organics are within the operating region designated ''''condition suitable for pitch formation'''' in FIG. 2.

References Cited (Backward Citations)

US3318801A Cited
US3617477A Cited
US3692663A Cited
US3835024A Cited
US3794579A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-12-22 1979-06-23 1979-12-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-12-22 1983-06-23 1983-12-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-12-22 1987-06-23 1987-12-23 $7700.00 Window Closed / Lapsed

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