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    • 2. 发明专利
    • JPH05298919A
    • 1993-11-12
    • JP22128992
    • 1992-08-20
    • CHICHIBU CEMENT KK
    • EMU JII EMU YUU ISUMAIRUNAKAI ZENJIROARAI HIROSHI
    • H01B3/08H05K1/03
    • PURPOSE:To provide sufficient mechanical strength to a composite substrate, make its thermal expansion coefficient near that of silicon and its dielectric constant low, and fire at low temperature by making the composite circuit substrate using a cordierite-anorthite-boron-based composite and providing a fine structure to the composite circuit substrate wherein the anorthite is taken in the cordierite phase. CONSTITUTION:A composite circuit substrate is made of a cordierite-anorthite- boron-based composite material and has a fine structure wherein the anorthite is taken in the cordierite phase. The weight ratio of cordierite/anorthite is (50-95)/(5-50) and boron (calculated in terms of B2O3) to cordierite is 0.5-10wt.%. A cordierite-anorthite composite composition sol is prepared by mixing boehmite sol, silica sol, a water-soluble magnesium salt, and a water-soluble calcium salt, gelled, calcined, and sintered. As a result, the resulting composite circuit substrate has sufficient mechanical strength, thermal expansion coefficient near that of silicon, low dielectric constant, and can be sintered at low temperature.
    • 7. 发明专利
    • PRODUCTION OF NON-OXIDE CERAMIC POWDER
    • JPS62278109A
    • 1987-12-03
    • JP11840586
    • 1986-05-24
    • CHICHIBU CEMENT KK
    • YUZAWA YUKIONAKAI ZENJIRONEMOTO FUMIOTSUNATORI HIDEO
    • C01B21/068C01B21/072C01B31/36
    • PURPOSE:To produce the titled uniform and fine ceramic powder in high efficiency, by using granulated raw material composed of a carbonaceous material and a material composed mainly of SiO2 or Al2O3, charging the granule is a reaction chamber having a specific structure and calcining in a non-oxidizing atmosphere. CONSTITUTION:1pt.wt. of a raw material composed mainly of SiO2 or Al2O3 is mixed with 0.1-3pts.wt. of a carbonaceous raw material and the mixture is granulated. The granulated material is fed to the lower A-2 chamber of a reaction vessel divided by a gas-permeable partition wall 2 and composed of vertically divided semicylinders 20a, 20b having >=2 reaction chambers along longitudinal direction. The semicylinders 20a, 20b are restored to the original state by relatively sliding by the length of one chamber to vertically combine the chambers A, B and C with each other. The cylinders are rotated, the cylinder 20b is slid by the length of one chamber to combine the lower chamber A-2 with the upper chamber B-1, turned 180 deg. to transfer the raw material from the lower A-2 chamber to the upper B-2 chamber and the A-1 chamber is supplied with fresh raw material. The raw material is calcined at 1,200-2,200 deg.C in the reaction vessel having non-oxidizing atmosphere by repeating the above procedures.