Abstract A process is disclosed for producing pitches of high quality in a high yield by subjecting selected crude oil to adiabatic thermal and steam cracking process at a temperature between 700 DEG C. and 1000 DEG C. to produce gases containing ethylene, propylene and the like and a tar pitch having an ethylene-to-acetylene ratio above 5; adjusting the pitch content of the tar pitch in the range between 20 and 80 wt % (if this content is outside this specified range); heat-treating at a temperature between about 450 DEG C. and about 550 DEG C. under a pressure between about 50 and about 150 kg/cm2(G) for about 1 to 15 minutes, and subsequently heat-soaking at a temperature between about 350 DEG and about 450 DEG C. under a pressure between about 0.5 and about 10 kg/cm2(G) for about 15 minutes to 10 hours.
A process for producing various pitches of high quality, which comprises the steps of: (a) adiabatically thermally cracking a starting oil in an ACR thermal cracking process at a temperature between 700° C. and 1000° C. to produce gases containing ethylene, propylene, and the like and a tar pitch having a pitch content controlled within the range of between 20 and 80 wt%; (b) heat-treating said controlled tar pitch in a heater at a temperature between about 450° C. and about 550° C. under a pressure between about 50 and 150 kg/cm 2 (G) for about 1 to 15 minutes; and (c) subsequently treating it in a soaker at a temperature between about 350° and about 450° C. under a pressure between about 0.5 and about 10 kg/cm 2 (G) for about 15 minutes to 10 hours.
Claim 2
Dependent Claim
137 words
A process for producing various pitches of high quality, which comprises the steps of: (a) adiabatically thermally cracking a starting oil in an ACR thermal cracking process at a temperature between 700° C. and 1000° C. to produce gases containing ethylene, propylene, and the like and a tar pitch having a pitch content controlled within the range of between 20 and 80 wt%; (b) heat-treating said controlled tar pitch in a heater at a temperature between about 450° C. and about 550° C. under a pressure between about 50 and 150 kg/cm 2 (G) for about 1 to 15 minutes; and (c) subsequently treating it in a soaker at a temperature between about 350° and about 450° C. under a pressure between about 0.5 and about 10 kg/cm 2 (G) for about 15 minutes to 10 hours.
Claim 3
Dependent Claim
20 words
The process according to claim 1, wherein said pitch content is controlled within the range between 25 and 60 wt%.
Claim 4
Dependent Claim
32 words
The process according to claim 1, wherein the temperature in the heater is about 470°-520° C., the pressure is about 80-120 kg/cm 2 (G), and the residence time is about 2-8 minutes.
Claim 5
Dependent Claim
32 words
The process according to claim 1, wherein the temperature in the soaker is about 380°-420° C., the pressure is about 0.5-5 kg/cm 2 (G) and the residence time is about 0.5-5 hours.
Claim 6
Dependent Claim
26 words
The process according to claims 1-4 wherein a part of the tar or tar pitch in the process is recycled to the inlet of the heater.