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    • 2. 发明专利
    • METHOD FOR JOINING CALCIUM SILICATE MOLDING
    • JPH03109274A
    • 1991-05-09
    • JP24530989
    • 1989-09-22
    • UNIV TOHOKUONODA CEMENT CO LTDONODA ALC KK
    • TAKAHASHI HIDEAKITERAMURA TOSHIFUMIWADA CHIHARU
    • C04B37/00B28B3/00
    • PURPOSE:To produce the large and thick calcium silicate molding by superposing the surfaces to be joined of plural pieces of the calcium silicate moldings and joining and integrating the moldings under heating and pressurizing. CONSTITUTION:The calcium silicate moldings are joined by the following (a) or (b) method: (a) The surfaces to be joined of plural pieces of the calcium silicate moldings are superposed on each other and a pressure is applied on the surfaces to be joined to joint and integrate the moldings when the temp. of the superposed moldings attains 900 to 1350 deg.C. (b) Plural pieces of the calcium silicate moldings are heated and the surfaces to be joined are superposed on each other at the point of the time when the individual temps. attain 900 to 1350 deg.C, then the pressure is applied on the surfaces to be joined to join and integrate the surfaces. The powder of the calcium silicate or the mixture composed of the calcium silicate and org. binder may be interposed between the surfaces to be joined of plural pieces of the calcium silicate moldings in the above-mentioned method. The characteristics of the surfaces to be joined in this case may be relatively rough.
    • 6. 发明专利
    • PRODUCTION OF XONOTLITE FIBER
    • JPS62260713A
    • 1987-11-13
    • JP10448086
    • 1986-05-07
    • UNIV TOHOKUONODA ALC KK
    • TAKAHASHI HIDEAKISHOJI TETSUOTERAMURA TOSHIFUMI
    • C01B33/24D01F9/08
    • PURPOSE:To increase length and aspect ratio of a xonotlite fiber, by reacting calcium and silica used as raw materials in a continuous hydrothermal reactor under a stable condition to form xonotlite in one step. CONSTITUTION:A raw material releasing Ca in an aqueous solution and a raw material releasing silica in an aqueous solution or a raw material releasing both Ca and silica in an aqueous solution is used as the starting material. For example, former two raw materials are preliminarily mixed, charged in a tank 1, converted to an aqueous solution or slurry in the tank and transferred to an autoclave 4 with a high-pressure pump. The autoclave 3 is heated with a heater 4 attached to the outer circumference of the tank while passing a raw material mixture liquid through the autoclave. The rate of temperature rise of the raw material liquid can be arbitrarily varied by varying the flow rate of the raw material liquid or the performance of the heater 4. The raw materials are made to react with each other in the flow to form xonotlite from the raw material in one step. The liquid containing the reaction product is temporarily stored in a tank 5 and filtered (6).
    • 7. 发明专利
    • METHOD AND APPARATUS FOR PRODUCING CALCIUM SILICATE MOLDING
    • JPH04202048A
    • 1992-07-22
    • JP33634890
    • 1990-11-30
    • UNIV TOHOKUONODA CEMENT CO LTD
    • TAKAHASHI HIDEAKIWADA CHIHARU
    • C04B35/22
    • PURPOSE:To allow the successive and continuous execution of the heating treatment of the calcium silicate moldings by repeating a stage for carrying the calcium silicate moldings of raw materials into a furnace kept at a permissible upper limit temp. or below and a stage for holding the moldings in the above-mentioned furnace until the moldings attain a uniform temp., thereby maintaining the moldings at the prescribed uniform temp. CONSTITUTION:The stage for carrying the calcium silicate moldings of the raw materials into the furnace kept at the permissible upper limit temp. or below and the stage for holding the moldings in the above-mentioned furnace until the moldings attain the uniform temp. are repeated to maintain the moldings at the prescribed uniform temp. (raw materials: 1 to 4, products: W). The device provided with the plural furnaces (e.g.; 11 to 20 are heating furnaces, 21 to 30 are cooling furnaces) disposed in series, a temp. controller (50: for the heating stage, 56: for the cooling stage) which controls the temp. difference between the above-mentioned furnaces adjacent to each other to the permissible max. temp. difference or below, a transporting device 57 which is provided through the inside of the respective furnaces and a means for controlling the transporting device is used to execute the above-mentioned production process.