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    • 1. 发明专利
    • PREPARATION OF BINDER PITCH FOR USE IN CARBON MATERIALS
    • JPH03277690A
    • 1991-12-09
    • JP7559590
    • 1990-03-27
    • NIPPON STEEL CHEMICAL CO
    • KANBE MASAZUMIMIURA KUNIOMIWA SHIGERUSHIBUYA TADASHI
    • C10C3/02C10C3/08
    • PURPOSE:To simply and inexpensively obtain the title pitch which has a high fixed carbon content and a high beta-resin content and generates no mesophase pitch by extracting coal tar pitch with a specific hydrocarbon solvent in a supercritical state of the solvent and removing lightweight fractions. CONSTITUTION:Coal tar pitch (preferably pitch having a softening point of 70 deg.C or below and 0.5-7.0wt.% quinoline-insolubles, obtained by distillation of coal tar secondary produced in the carbonization of coal) and a paraffin or an aromatic hydrocarbon solvent are charged into an extraction zone which is maintained at a temp. from the critical temp. of the solvent to 370 deg.C and a pressure from the critical pressure of the solvent to 100kg/cm G and at a solvent/coal tar pitch weight ratio of 0.5-6.0. The lightweight fractions in coal tar pitch are removed by extraction so that the softening point of the pitch is adjusted to 80-200 deg.C. Thus, binder pitch for carbon material use which has a high fixed carbon content and a high beta-resin content and generates no mesophase pitch can be obtained by an extremely simple and inexpensive means without use of a complex process and a lot of secondary materials.
    • 10. 发明专利
    • METHOD FOR FRACTIONATING BETA RESIN
    • JPH0386789A
    • 1991-04-11
    • JP22319089
    • 1989-08-31
    • NIPPON STEEL CHEMICAL CO
    • MIURA KUNIOKANBE MASAZUMISUMIMOTO ISAO
    • C10C3/00C10C3/08
    • PURPOSE:To efficiently produce beta-resin useful as a raw material for a highly value-added carbon product using simple equipment by treating coal tar pitch with solvents under specific conditions. CONSTITUTION:Coal tar pitch 4 pref. having a softening point of 100 deg.C or lower and a mixed solvent 5 comprising the first arom. solvent (e.g. coker gas oil) and an aliph. solvent (e.g. kerosene) are introduced into the first fractionating zone 1, where they are mixed and kept standing to separate into two phases, a low-density liq. 7 and a high density liq. 8 mainly comprising quinoline-insols. (e.g. carbon, ash, and other inorg. matters), and both liqs. are separately taken out. After the solvent 9 of the low density liq. 7 is removed, the solvent-free low density liq. 10 and the second arom. solvent (e.g. toluene) are introduced in a wt. ratio of the second solvent to the coal tar pitch component of 0.5-5 into the second fractionating zone 2, where they are kept at a temp. in the range of from the critical temp. of the second arom. solvent to 370 deg.C under a pressure in the range of from the critical pressure of the second arom. solvent to 100kg/cm G to separate into two phases, a low density liq. 13 mainly comprising toluene-sols. and a high density liq. 14 mainly comprising beta-resin, and both liqs. 13 and 14 are separately taken out.