Process for the production of pitch-derived carbon fibers

Claim 2

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting point to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by incorporating 100 parts by volume of a heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene, with 10-200 parts by volume of aromatic hydrocarbons of 2-3 rings having their nuclei at least partly hydrogenated to form a mixed oil and then heat treating the thus formed mixed oil at a temperature of 380°-480° C. and a pressure of 2-50 Kg/cm 2 ·G.

Claim 3

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by incorporating 100 parts by volume of a heavy fraction oil (b) boiling at substantially 200°-450° C. obtained as a by-product at the time of fluidized catalytic cracking of petroleum comprising at least one member selected from kerosene, light oil and atmospheric pressure bottom oils, at a temperature of 450°-550° C. and a pressure of atmospheric to 20 Kg/cm 2 ·G in the presence of natural or synthetic silica.alumina catalyst or zeolite catalyst, with 10-200 parts by volume of aromatic hydrocarbons of 2-3 rings having their nuclei at least partly hydrogenated to form a mixture and then heat treating the thus formed mixture at a temperature of 380°-480° C. and a pressure of 2-50 Kg/cm 2 ·G.

Claim 4

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by incorporating 100 parts by volume of a heavy fraction oil (b) boiling at substantially 200°-450° C. obtained as a by-product at the time of fluidized catalytic cracking of petroleum comprising at least one member selected from kerosene, light oil and atmospheric pressure bottom oils, at a temperature of 450°-550° C. and a pressure of atmospheric to 20 Kg/cm 2 ·G in the presence of natural or synthetic silica.alumina catalyst or zeolite catalyst, with 10-200 parts by volume of aromatic hydrocarbons of 2-3 rings having their nuclei at least partly hydrogenated to form a mixture and then heat treating the thus formed mixture at a temperature of 380°-480° C. and a pressure of 2-50 Kg/cm 2 ·G.

Claim 5

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by heat treating a heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene at a temperature of 400°-500° C. under a hydrogen pressure of 20-350 Kg/cm 2 ·G.

Claim 6

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by heat treating a heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene at a temperature of 400°-500° C. under a hydrogen pressure of 20-350 Kg/cm 2 ·G.

Claim 7

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by heat treating at a temperature of 400°-500° C. under a hydrogen pressure of 20-350 Kg/cm 2 ·G, a heavy fraction oil boiling at substantially 200°-450° C. obtained as a by-product at the time of fluidized catalytic cracking of petroleum comprising at least one member selected from kerosene, light oil and atmospheric pressure bottom oils, at a temperature of 450°-550° C. and a pressure of atmospheric to 20 Kg/cm 2 ·G in the presence of natural or synthetic silica.alumina catalyst or zeolite catalyst.

Claim 8

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by heat treating at a temperature of 400°-500° C. under a hydrogen pressure of 20-350 Kg/cm 2 ·G, a heavy fraction oil boiling at substantially 200°-450° C. obtained as a by-product at the time of fluidized catalytic cracking of petroleum comprising at least one member selected from kerosene, light oil and atmospheric pressure bottom oils, at a temperature of 450°-550° C. and a pressure of atmospheric to 20 Kg/cm 2 ·G in the presence of natural or synthetic silica.alumina catalyst or zeolite catalyst.

Claim 9

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by (A) incorporating 100 parts by volume of a heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene, with 10-200 parts by volume of a hydrogenated oil (c) obtained by contacting with hydrogen in the presence of a hydrogenating catalyst a fraction (i) boiling at 160°-400° C. produced at the time of steam cracking of petroleum or a hydrogenated oil obtained by contacting with hydrogen in the presence of a hydrogenated catalyst, a fraction (ii) boiling between 160°-400° C. produced at the time of heat treating at 380°-480° C. a heavy fraction oil boiling at not lower than 200° C. obtained at the time of steam cracking of petroleum or a hydrogenated oil obtained by contacting with hydrogen a mixture of fraction (i) and fraction (ii), to hydrogenate 10-70% of aromatic nuclei of the aromatic hydrocarbons contained in aromatic nuclei of the aromatic hydrocarbons contained in the fractions (i) and (ii) thereby to obtain a mixture of the oils (a) and (c) and then (B) heat treating the thus obtained mixture at a temperature of 380°-480° C. under a pressure of 2-50 Kg/cm 2 ·G thereby obtaining a pitch.

Claim 10

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by (A) incorporating 100 parts by volume of a heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene, with 10-200 parts by volume of a hydrogenated oil (c) obtained by contacting with hydrogen in the presence of a hydrogenating catalyst a fraction (i) boiling at 160°-400° C. produced at the time of steam cracking of petroleum or a hydrogenated oil obtained by contacting with hydrogen in the presence of a hydrogenated catalyst, a fraction (ii) boiling between 160°-400° C. produced at the time of heat treating at 380°-480° C. a heavy fraction oil boiling at not lower than 200° C. obtained at the time of steam cracking of petroleum or a hydrogenated oil obtained by contacting with hydrogen a mixture of fraction (i) and fraction (ii), to hydrogenate 10-70% of aromatic nuclei of the aromatic hydrocarbons contained in aromatic nuclei of the aromatic hydrocarbons contained in the fractions (i) and (ii) thereby to obtain a mixture of the oils (a) and (c) and then (B) heat treating the thus obtained mixture at a temperature of 380°-480° C. under a pressure of 2-50 Kg/cm 2 ·G thereby obtaining a pitch.

Claim 11

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by mixing together the heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene, heavy fraction oil (b) boiling at substantially 200°-450° C. obtained as a by-product at the time of fluidized catalytic cracking of petroleum comprising at least one member selected from kerosene, light oil and atmospheric pressure bottom oils, at a temperature of 450°-550° C. and a pressure of atmospheric to 20 Kg/cm 2 ·G in the presence of natural or synthetic silica.alumina catalyst or zeolite catalyst and hydrogenated oil (c) obtained by contacting with hydrogen in the presence of a hydrogenating catalyst a fraction (i) boiling at 160°-400° C. produced at the time of steam cracking of petroleum or a hydrogenated oil obtained by contacting with hydrogen in the presence of a hydrogenation catalyst said fraction (i) together with a fraction (ii) boiling between 160°-400° C. produced at the time of heat treating at 380°-480° C. a heavy fraction oil boiling at not lower than 200° C. obtained at the time of steam cracking of petroleum or a mixture of said fraction (i) and said fraction (ii), to hydrogenate 10-70% of aromatic nuclei of the aromatic hydrocarbons containing in the fractions (i) and (ii), in such amounts that the ratio by weight of said heavy fraction oil (a) to said heavy fraction oil (b) is 1:0.1-9 and the ratio by weight of the total of said heavy fraction oils (a) and (b) to said hydrogenated oil (c) is 1:0.1-2, to obtain a mixture and then heat treating the thus obtained mixture at a temperature of 380°-480° C. under a pressure of 2-50 Kg/cm 2 ·G.

Claim 12

In a process for the production of carbon fibers comprising melt spinning a pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers, carbonizing or further graphitizing the thus infusibilized pitch fibers to obtain high performance carbon fibers, the improvement which consists of melting a starting pitch to obtain a liquid pitch, forming the thus formed liquid pitch to a thin film having a thickness not greater than 5 mm in thickness, treating said film at a temperature of 250°-350° C. under reduced pressure of 0.1-10 mm Hg for 1-30 minutes to obtain a specific optically isotropic pitch having a reflectivity of 9.0-11.0% as measured using monochromatic light having a wavelength of 547 nm, melt spinning said optically isotropic pitch to obtain pitch fibers, infusibilizing the thus obtained pitch fibers and then carbonizing or graphitizing the infusibilized pitch fibers to obtain carbon fibers, wherein the starting pitch is a pitch obtained by mixing together the heavy fraction oil (a) boiling at substantially 200°-450° C. obtained as a by-product at the time of steam cracking at 700°-1200° C. of petroleum comprising at least one member selected from naphtha, kerosene and light oil to produce olefins including ethylene and propylene, heavy fraction oil (b) boiling at substantially 200°-450° C. obtained as a by-product at the time of fluidized catalytic cracking of petroleum comprising at least one member selected from kerosene, light oil and atmospheric pressure bottom oils, at a temperature of 450°-550° C. and a pressure of atmospheric to 20 Kg/cm 2 ·G in the presence of natural or synthetic silica.alumina catalyst or zeolite catalyst and hydrogenated oil (c) obtained by contacting with hydrogen in the presence of a hydrogenating catalyst a fraction (i) boiling at 160°-400° C. produced at the time of steam cracking of petroleum or a hydrogenated oil obtained by contacting with hydrogen in the presence of a hydrogenation catalyst said fraction (i) together with a fraction (ii) boiling between 160°-400° C. produced at the time of heat treating at 380°-480° C. a heavy fraction oil boiling at not lower than 200° C. obtained at the time of steam cracking of petroleum or a mixture of said fraction (i) and said fraction (ii), to hydrogenate 10-70% of aromatic nuclei of the aromatic hydrocarbons containing in the fractions (i) and (ii), in such amounts that the ratio by weight of said heavy fraction oil (a) to said heavy fraction oil (b) is 1:0.1-9 and the ratio by weight of the total of said heavy fraction oils (a) and (b) to said hydrogenated oil (c) is 1:0.1-2, to obtain a mixture and then heat treating the thus obtained mixture at a temperature of 380°-480° C. under a pressure of 2-50 Kg/cm 2 ·G.