序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
141 JPH06504565A - JP50272892 1991-12-05 JPH06504565A 1994-05-26
142 JPH048475B2 - JP21149488 1988-08-25 JPH048475B2 1992-02-17
143 JPH046755B2 - JP12565786 1986-06-02 JPH046755B2 1992-02-06 TATE KAZUHITO; YOSHIDA HAJIME; SASAKI TERUHIKO
144 JPH0258311B2 - JP3813680 1980-03-25 JPH0258311B2 1990-12-07 KOONERIUSU JII FUITSUTSUJERARUDO; HAARII DABURYUU BAANAMU
145 Binder pitch and its preparation JP26886489 1989-10-16 JPH02258892A 1990-10-19 DEII ROURII BUREIKUBAAN ZA SEK; KIISU EMU RUUSERU; TAA UEI FU
PURPOSE: To obtain binder pitch having high density, high strength and low electric resistance by subjecting hydrogenated petroleum aromatic mineral oil to pyrolytic treatment and distilling the obtained product to obtain hot tar and combining this tar with fine baked petroleum coke particles. CONSTITUTION: Petroleum aromatic mineral oil pref. being supernatant oil is subjected to hydrogenation treatment and the obtained product is subjected to pyrolytic treatment to obtain hot tar which is, in turn, distilled to obtain topping hot tar. This hot tar is combined with about 1-18 wt.% of fine baked petroleum coke particles with an average particle size of about 1-40 μm (pref. about 5 μm or less) to obtain the objective binder pitch. COPYRIGHT: (C)1990,JPO
146 Production of pitch as starting material for carbon material JP2459289 1989-02-02 JPH02204314A 1990-08-14 SEO IKUO; ONO TORU; MURAKAMI YOSHINOBU
PURPOSE: To obtain a carbon molded product having a low ash content and superior quality by polymerizing naphthalene or a deriv. thereof at a specified temp. in the presence of an aluminum chloride catalyst, adding water, carrying out emulsification by stirring, and separating the water. CONSTITUTION: Naphthalene or a deriv. thereof is polymerized at 100-330°C in the presence of an aluminum chloride catalyst, water is added to the polymn. system and emulsification is carried out by stirring to prepare an emulsion. This emulsion is then broken and the residue of the catalyst is removed by separating and removing the water. A carbon material using the resultant pitch has a very low ash content and can give a carbon molded body having superior quality. COPYRIGHT: (C)1990,JPO&Japio
147 Pitch-based carbon fiber having excellent compression property and production thereof JP16068388 1988-06-30 JPH0214023A 1990-01-18 TAKASHIMA HIROAKI; KATO OSAMU; AZAMI KIYOSHI; NAKAJIMA HAJIME
PURPOSE: To obtain the subject pitch-based carbon fiber having novel structure by spinning pitch containing specific amount of optically anisotropic phase obtained by hydrolyzing carbonaceous pitch, heat treating and extracting with respectively specific two organic solvents, infusibilizing and carbonizing. CONSTITUTION: Carbonaceous pitch is hydrolyzed with hydrolyzing catalyst and ≥2mol hydrogen per a pitch molecule is added, then heattreated under normal pressure or reduced pressure, thus pitch containing 5-40vol% optically anisotropic phase. Said pitch is extracted with an organic solvent having 7.4-9.0 solubility parameter at 25°C and insoluble component is extracted with an organic solvent having 9.2-11.0 solubility parameter at 25°C, then soluble component is spun, infusibilized and carbonized to obtain the aimed pitch-based carbon fiber having ≥50vol% fine texture comprising of respectively ≤1000Å La and Lc values in X-ray diffraction and ≤1000Å fibril width, 1.95-2.12g/cm 3 density and a relation expressed by the formula of layer spacing d 002 in X-ray diffraction and density. COPYRIGHT: (C)1990,JPO&Japio
148 JPH0149316B2 - JP15865883 1983-08-29 JPH0149316B2 1989-10-24 MORI MAKIHIKO; FUJITA KATSUMI; NAKAGAWA YOSHITERU; AIDA YASUKI; MAEDA TOYOHIRO
149 Production of raw material pitch for carbon fiber JP23708786 1986-10-07 JPS62174294A 1987-07-31 ISHIKAWA SEIJI; HIRANO SHUICHI; MATSUMOTO YUKIO; KAIHARA TSUTOMU; MORISHIGE TAKUO; SUGIYAMA KENJI
PURPOSE: To obtain the title pitch capable of providing a carbon fiber which is excellent in mechanical properties such as strength and modulus of elasticity, by heat- treating a particular raw material such as a high-boiling oil derived from petroleum, removing insoluble matter therefrom, heating the treated material to remove low- boiling fractions and further heat-treating the material at a high temp. CONSTITUTION: Cracked petroleum is obtd. by fluidized catalystic cracking of petroleum at 480W560°C in the presence of a silica-alumina or zeolite cracking catalyst. At least one raw material selected from among a high-boiling oil contg. entrained catalyst powder obtd. from the cracked petroleum, a distillate or distillation residue of the cracked petroleum or pitch obtd. by heat treatment thereof is heat-treated in a hydrogen atmosphere at 350W550°C for 10min W3hr. Insoluble matter is separated and removed from the reaction mixture to obtain a first treatment mixture. The first treatment mixture is heated at 250W400°C in an inert gas atmosphere under a reduced pressure to remove a low-boiling fraction which distilled at the same temp., thereby obtaining a second treatment mixture. The second treatment mixture is treated in an inert gas atmosphere under a reduced pressure at 430W550°C for 10W60min to obtain the title pitch having a softening point of 260W340°C, a toluene insoluble content of 50W90% and a quinoline insoluble content of 10W40%. COPYRIGHT: (C)1987,JPO&Japio
150 Optically anisotropic pitch JP21807985 1985-10-02 JPS6279215A 1987-04-11 TATE KAZUHITO; YOSHIDA HAJIME; SASAKI TERUHIKO
PURPOSE: To obtain the titled pitch useful as a production raw material for high-tenacity and high-modulus carbon fiber and other carbon material, by using a specific polymer as a starting raw material and heat-treating the polymer. CONSTITUTION: An alkylbenzene (preferably 2W4-substituted 9W10C alkylbenzene) is made to react with a 2W4-cyclic aromatic compound and preferably formaldehyde in the presence of preferably a protonic acid catalyst and the resultant polymer wherein the alkylbenzene and the 2W4-cyclic aromatic compound are bonded together through methylene group is used as a raw material. The objective pitch is produced by heat-treating the raw material preferably at 350W460°C for 0.5W10hr under refluxing. COPYRIGHT: (C)1987,JPO&Japio
151 Membrane separation of non-converted carbon fiber precursor from flux solvent JP9310584 1984-05-11 JPS60235606A 1985-11-22 MAAMUUDO EMU HAFUEZU; ROORA II BURATSUKU
152 Method for treating coal tar or coal tar pitch JP15865883 1983-08-29 JPS6049085A 1985-03-18 MORI MAKIHIKO; FUJITA KATSUMI; NAKAGAWA YOSHITERU; AIDA YASUKI; MAEDA TOYOHIRO
PURPOSE: To obtain coal tar (pitch) containing only pure secondary substances insoluble in quinoline useful as a raw material for producing carbon fibers, etc., by centrifuging coal tar (pitch), and heat-treating the resultant clear liquid under specific conditions. CONSTITUTION: Coal tar (pitch) is centrifuged at 100W400°C temperature, preferably 200W350°C usually under about 500W4,000G centrifugal force to give a clear liquid, which is then heat-treated at 300W500°C under conditions of ordinary pressure W20kg/cm 2.G for 0.5W50hr and then preferably centrifuged at 150W450°C, preferably 200W400°C usually under about 500W5,000G centrifugal force. COPYRIGHT: (C)1985,JPO&Japio
153 Manufacture of carbon fiber JP8877583 1983-05-20 JPS59216921A 1984-12-07 GOMI SHINPEI; ARAI TOMIO; MOGI FUMIO; MIURA KUNIO; OOTANI SUGIROU
PURPOSE: To manufacture carbon fiber without the restriction of the raw materials, at a remarkably reduced cost, by thermally cracking a specific petroleum residue oil e.g. by contacting with a gaseous heat medium, separating and removing the meso-phase, and carrying out the melt-spinning, infusibilization and carbonization of the product. CONSTITUTION: A petroleum residue oil having a boiling point of ≥500°C and containing ≥30wt% of a residue oil having a boiling point of ≥500°C and a metal content of ≥200ppm and obtained from a napthenic crude oil or mixed- base crude oil, is made to contact with a gas or vapor of an inert heat medium or cracked at 400W500°C under reduced pressure in liquid phase while evporating and removing the cracked light oil, to obtain a pitch having a softening point of 140W220°C and containing ≥5wt% of meso-phase and ≤10wt% of the light fraction having a boiling point of ≤300°C under the pressure of 60mmHg. The meso-phase (and its agglomerate) is separated and removed from the pitch, and the obtained pitch free from the meso-phase (and its agglomerate) having a diameter of ≥10μ is subjected to melt-spinning. The produced fiber is made infusible and carbonized to obtain the objective carbon fiber. COPYRIGHT: (C)1984,JPO&Japio
154 Custom blend precursor for manufacturing carbon article and manufacture JP6048784 1984-03-28 JPS59189168A 1984-10-26 GAJII DEITSUKAKIAN
155 JPS5930192B2 - JP17681380 1980-12-15 JPS5930192B2 1984-07-25 OOTANI SUGIRO
156 JPS59501266A - JP50214383 1983-07-04 JPS59501266A 1984-07-19
157 JPS5910713B2 - JP6555879 1979-05-29 JPS5910713B2 1984-03-10 HAYASHI KYOSHIGE
158 JPS5854081B2 - JP23880 1980-01-04 JPS5854081B2 1983-12-02 NOGUCHI KOSAKU; TANAKA HONAMI; HISAMURA YUKIMASA; KITAJIMA EIJI; TSUCHA TOKUYUKI; SUNADA TOMONORI
159 Preparation of pitch carbon fiber JP17207681 1981-10-29 JPS5876523A 1983-05-09 KAMIMURA SEIICHI; YAMAMOTO SHIYUNICHI; HIROSE TAKAO; TAKASHIMA HIROAKI; KATOU OSAMU
PURPOSE: To obtain carbon fibers having a high elasticity and high strength from a uniform low-melting pitch in melt spinning, by using an optically isotropic pitch exhibiting a specific reflectance as a raw material. CONSTITUTION: An optically isotropic pitch, exhibiting 9.0W11.0% reflectance, and containing the mesophase is used as a raw material. For example, a petroleum, e.g. naphtha or kerosene, is steam cracked at 700W1,200°C to prepare an olefin. A heavy oil, produced in the process as a byproduct, and having 200W 450°C boiling point is molten in an inert gaseous atmosphere to form a liquid, which is then formed into a thin film of ≤5mm thickness. The resultant thin film is then treated at 280W345°C and 0.1W10mmHg reduced pressure for 5W20min to give the reflectance within the above-mentioned range. The resultant film is then melt spun to afford pitch fibers, which are made infusible, carbonized and graphitized to give the aimed carbon fibers. COPYRIGHT: (C)1983,JPO&Japio
160 Preparation of raw material pitch for carbon fiber JP14950181 1981-09-24 JPS5852386A 1983-03-28 MORIYA KUNIHIKO; TATE KAZUHITO; MUROGA GOROU; YANAGIDA KAZUHIRO
PURPOSE: To stably obtain raw material pitch with high modulus of elasticity for preparing carbon fiber, by extractiong a deasphalted oil obtd. by the vacuum distillation and solvent deasphalting of a heavy petroleum residue, or extracting a vacuum distillate of the heavy residue, with a solvent and thermally treating the extract. CONSTITUTION: A heavy petroleum residue such as an atmospheric distillation residue or hydrocracked residue of crude oil is subjected to vacuum distillation and a vacuum residue of b.p. ≥500°C under normal press is subjected to deasphalting with a solvent such as propane, to remove asphaltene contg. V, Ni, etc. in a large amt. The obtd. solvent-deasphalted oil or a fraction of b.p. 300W 500°C under normal press. obtd. by the vacuum distillation of the heavy oil without deasphalting, is extracted at about 45W145°C by using furfural as a solvent. Then the purpase pitch is obtd. by thermally treating a furfural-extract at about 390W460°C for about 1W30hr. COPYRIGHT: (C)1983,JPO&Japio
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