GB731838A - Improvements in or relating to cracking of heavy hydrocarbon oils - Google Patents

Improvements in or relating to cracking of heavy hydrocarbon oils

Info

Publication number
GB731838A
GB731838A GB1985652A GB1985652A GB731838A GB 731838 A GB731838 A GB 731838A GB 1985652 A GB1985652 A GB 1985652A GB 1985652 A GB1985652 A GB 1985652A GB 731838 A GB731838 A GB 731838A
Authority
GB
United Kingdom
Prior art keywords
zone
per cent
bauxite
hydrogen
cracking
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB1985652A
Inventor
Percival Cleveland Keith
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hydrocarbon Research Inc
Original Assignee
Hydrocarbon Research Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hydrocarbon Research Inc filed Critical Hydrocarbon Research Inc
Priority to GB1985652A priority Critical patent/GB731838A/en
Publication of GB731838A publication Critical patent/GB731838A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00Regeneration or reactivation of catalysts, in general
    • B01J38/04Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12Treating with free oxygen-containing gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • B01J8/28Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/34Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with stationary packing material in the fluidised bed, e.g. bricks, wire rings, baffles

Abstract

<PICT:0731838/III/1> Heavy hydrocarbon oils are cracked to lighter hydrocarbons including gasoline by contacting the oil with hot solid particles circulating between the cracking zone and a regeneration zone, the pressure in the system being maintained between 150 and 800 p.s.i.g.; the contaminated particles are regenerated, at a temperature of 1600-2500 DEG F., with a mixture of steam and oxygen, in the molar ratio of about 1.5 : 1 to 5 : 1, which react with the carbonaceous deposit to give a gas containing substantial proportions of hydrogen and carbon monoxide, and this gas is passed into the cracking zone, which is maintained at a temperature of 850 DEG to 1100 DEG F., so as to maintain a hydrogen partial pressure of 35 to 200 p.s.i. therein. Suitable contact materials include quartz, alumina, magnesia, zircon, beryl and bauxite. The vessel 10 contains both a cracking zone 12 and a regeneration zone 11, the two zones being separated by perforated plate 13. For cracking asphaltenic petroleum oil (13 per cent carbon residue and 5 per cent sulphur), bauxite particles which will pass through a 20-mesh sieve (but not through a 200-mesh sieve) are used as catalyst. The oil is preheated to 750 DEG F. and fed through distributor 16 into zone 12 where it contacts the fluidized bauxite at 980 DEG F. Contaminated bauxite particles pass downwards through plate 13 into zone 11 where they are contacted with a mixture of steam and oxygen, in the volume ratio of 15 : 8, introduced through distributer 17. The carbonaceous matter on the bauxite is thereby converted, at 1750 DEG F., into gases rich in hydrogen and carbon monoxide. The regenerated particles are conveyed from zone 11 to zone 12 through tube 14 by injecting steam into the lower end of the tube. The regeneration product gases flow up through plate 13 and become mixed with the hydrocarbons being cracked in zone 12. The pressure maintained in vessel 10 is 460 p.s.i.g., and the hydrogen in the gases flowing up into zone 12 exerts a partial pressure therein of 75 p.s.i. The mixture of cracked vapours and regeneration product gases is withdrawn through outlet 18, and is subjected to cooling and separation into fractions including gasoline, light gas oil and heavy gas oil. The gasoline has an octane number of at least 85, and contains at least 40 per cent of olefines and at least 30 per cent of aromatic hydrocarbons. The uncondensed product gas contains 32 per cent by volume of hydrogen and 25 per cent by volume of carbon monoxide.
GB1985652A 1952-08-06 1952-08-06 Improvements in or relating to cracking of heavy hydrocarbon oils Expired GB731838A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1985652A GB731838A (en) 1952-08-06 1952-08-06 Improvements in or relating to cracking of heavy hydrocarbon oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1985652A GB731838A (en) 1952-08-06 1952-08-06 Improvements in or relating to cracking of heavy hydrocarbon oils

Publications (1)

Publication Number Publication Date
GB731838A true GB731838A (en) 1955-06-15

Family

ID=10136343

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1985652A Expired GB731838A (en) 1952-08-06 1952-08-06 Improvements in or relating to cracking of heavy hydrocarbon oils

Country Status (1)

Country Link
GB (1) GB731838A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0026645A1 (en) * 1979-09-29 1981-04-08 Research Association For Residual Oil Processing Process for cracking heavy hydrocarbons into light oils and for producing hydrogen, and so produced light oil and hydrogen

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0026645A1 (en) * 1979-09-29 1981-04-08 Research Association For Residual Oil Processing Process for cracking heavy hydrocarbons into light oils and for producing hydrogen, and so produced light oil and hydrogen

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