Abstract A process for the preparation of carbon fibers, including the steps of: subjecting a raw material oil to thermal cracking conditions at a temperature of between 400 DEG to 500 DEG C. while removing cracked, light hydrocarbon components to obtain a pitch product containing at least 5 weight % of mesophase and not more than 10 weight % of light hydrocarbon components with a boiling point at 60 mmHg (absolute) of 300 DEG C. or less and having a softening point of between 140 DEG and 220 DEG C., the raw material oil having a boiling point of at least 500 DEG C. and containing at least 30 weight % of a residual oil which has a boiling point of at least 500 DEG C. and a metal content of at least 200 weight ppm and which is derived from a napthene base and/or intermediate base petroleum crude; removing the mesophase having a particle size of more than 10 mu m from the pitch product to obtain a substantially mesophase-free carbonaceous pitch; spinning the substantially mesophase-free pitch into fibers; rendering the spun fibers infusible; and carbonizing the infusible fibers.
A process for the preparation of carbon fibers, comprising the steps of:
Claim 2
Dependent Claim
12 words
A process for the preparation of carbon fibers, comprising the steps of:
Claim 3
Dependent Claim
168 words
subjecting a raw material oil to thermal cracking conditions at a temperature of between 400° and 500° C. while removing cracked, light hydrocarbon components to obtain a pitch product containing 5-40 weight % of mesophase and not more than 10 weight % of light hydrocarbon components with a boiling point at 60 mmHg (absolute) of 300° C. or less and having a softening point of between 140° and 220° C., the raw material oil having a boiling point of at least 500° C. and containing at least 30 weight % of a residual oil which has a boiling point of at least 50° C. and a metal content of at least 200 weight ppm and which is obtained from fractionation of naphthene base and/or intermediate base petroleum crude; removing the mesophase having a particle size of more than 10 μm from the pitch product to obtain a substantially mesophase-free carbonaceous pitch; spinning the substantially mesophase-free pitch into fibers; rendering the spun fibers infusible; and carbonizing the infusible fibers.
Claim 4
Dependent Claim
168 words
subjecting a raw material oil to thermal cracking conditions at a temperature of between 400° and 500° C. while removing cracked, light hydrocarbon components to obtain a pitch product containing 5-40 weight % of mesophase and not more than 10 weight % of light hydrocarbon components with a boiling point at 60 mmHg (absolute) of 300° C. or less and having a softening point of between 140° and 220° C., the raw material oil having a boiling point of at least 500° C. and containing at least 30 weight % of a residual oil which has a boiling point of at least 50° C. and a metal content of at least 200 weight ppm and which is obtained from fractionation of naphthene base and/or intermediate base petroleum crude; removing the mesophase having a particle size of more than 10 μm from the pitch product to obtain a substantially mesophase-free carbonaceous pitch; spinning the substantially mesophase-free pitch into fibers; rendering the spun fibers infusible; and carbonizing the infusible fibers.
Claim 5
Dependent Claim
37 words
A process as claimed in claim 1, wherein said thermal cracking is performed in a reaction zone which is maintained under reduced pressure so that the cracked light hydrocarbon components are continuously removed from said reaction zone.
Claim 6
Dependent Claim
43 words
A process as claimed in claim 1, wherein said thermal cracking is performed in a reaction zone to which is continuously fed a gaseous heat transfer medium so that the cracked light hydrocarbon components are continuously removed by stripping from said reaction zone.
Claim 7
Dependent Claim
20 words
A process as claimed in claim 1, wherein said removing the mesophase is effected by filtration at an elevated temperature.