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    • 4. 发明专利
    • Treatment equipment and method for waste including nitrate
    • 包括硝酸盐在内的废物处理设备和方法
    • JP2005241531A
    • 2005-09-08
    • JP2004053935
    • 2004-02-27
    • Toshiba Corp株式会社東芝
    • OMURA TSUNEOAKAI YOSHIEHOSAKA KATSUMIHATAKEYAMA HIDEO
    • G21F9/06B01J3/00C02F1/32C02F1/72C02F1/78G21F9/10G21F9/12G21F9/30
    • Y02P20/544
    • PROBLEM TO BE SOLVED: To provide treatment equipment and a treatment method for waste including nitrate which treat nitrogen component in the waste including nitrate without exhausting nitrogen oxide, and improve safety of the equipment by preventing the generation of nitrogen gas after waste treatment. SOLUTION: The waste treatment equipment comprises a reaction vessel 1 for reacting the waste 5 including nitrate and a reducing agent 6, a waste supplier 2 for supplying the reaction vessel 1 with waste including nitrate, a reducing agent supplier 3 for supplying the reaction vessel 1 with the reducing agent 6, a supply line 7 for supplying the reaction vessel 1 with the waste including nitrate and the reducing agent 6 by connecting the waste supplier 2, the reducing agent supplier 3 and the reaction vessel 1, and a treated fluid exhaust line 10 for exhausting treated fluid 9 from the reaction vessel 1. The waste 5 including nitrate and the reducing agent 6 supplied to the reaction vessel 1 are reacted in a condition that water is supercritical fluid so as to reduce nitrogen in the nitrate to nitrogen gas by the reducing agent 6. COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供处理设备和废物处理方法,其包括硝酸盐,其处理包括硝酸盐在内的废物中的氮成分而不排出氮氧化物,并且通过在废物处理之后防止产生氮气来提高设备的安全性 。 解决方案:废物处理设备包括用于使包括硝酸盐的废物5和还原剂6反应的反应容器1,用于向反应容器1供应含有硝酸盐的废物的废物供应器2,用于向 具有还原剂6的反应容器1,用于通过连接废物供应商2,还原剂供应商3和反应容器1向反应容器1供应包括硝酸盐和还原剂6的废物的供应管线7和经处理的 用于排出来自反应容器1的处理过的流体9的流体排放管线10.包含硝酸盐和供给到反应容器1的还原剂6的废物5在水是超临界流体的条件下反应,以将硝酸盐中的氮还原为 还原剂为氮气。版权所有(C)2005,JPO&NCIPI
    • 5. 发明专利
    • FEED WATER CONTROLLER
    • JP2001116206A
    • 2001-04-27
    • JP29045099
    • 1999-10-13
    • TOSHIBA CORP
    • HATAKEYAMA HIDEOSANADA MASAHIKO
    • F01D17/24F22D5/32
    • PROBLEM TO BE SOLVED: To provide a feed water controller to suppress operation exceeding allowable shaft torque even when pump efficiency is eminently reduced and perform safe operation of a feed water pump, in a feed water control device to control a flow rate of a feed water pump by controlling a steam regulation valve. SOLUTION: This feed water controller comprises a regulation valve opening computing means 7 to determine a first steam regulation opening signal 51 from a number of revolutions command signal 1 and a number of revolutions detecting signal 2, a steam flow rate converting means 11 to convert the number of revolutions detecting signal 2 into an allowable steam flow rate signal 52, a steam regulation valve opening signal converting means 12 to covert the allowable steam flow rate signal 52 into a second steam regulation valve opening signal 53, and a low value selecting means 13 to compare the first and second steam regulation valve opening signals 51 and 53 with each other and output one, being lower, of the values whichever it may be.
    • 10. 发明专利
    • HEAT PIPE DEVICE FOR LOOP TYPE THIN PIPE
    • JPH09303978A
    • 1997-11-28
    • JP12181996
    • 1996-05-16
    • TOSHIBA CORP
    • TAKAHASHI MASAHIKOROOHANA CHIYANDORATEIRAKAHATAKEYAMA HIDEONAKAGOME HIDEKIKOBAYASHI TAKAYUKI
    • F28D15/02
    • PROBLEM TO BE SOLVED: To require no large precooling mechanism, prevent an entire body from being enlarged and a thermal efficiency from being lowered by providing a refrigerant forcedly flowing means for forcedly flowing a refrigerant in a loop type thin pipe through a plurality of refrigerant guide tubes communicating with a plurality of parts of the loop type thin pipe. SOLUTION: Refrigerant guide tubes 42 and 49 communicate with the two parts of a loop type thin pipe 36 so that a refrigerant is forcedly supplied in the loop type thin pipe 36 therethrough. While high pressure nitrogen gas passes through a heat exchanger 45 after it passes through a heat exchanger 46, the gas is completely cooled to a low temperature in a first cooling stage 33, and then, the nitrogen gas is completely cooled to a low temperature in a first stage 34 while it passes through a heat exchanger 43 after it passes through a heat exchanger 44. The cooled nitrogen gas flows into the loop type thin pipe 36 in a part A. The gas divided into two passages after the part A flows in the loop type thin pipe 36, absorbs heat from the loop type thin pipe 36 and a superconducting coil 31 and flows to the inlet port of a compressor 48 through the refrigerant guide pipe 49 from a part B.