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    • 3. 发明专利
    • DE2303586A1
    • 1974-09-05
    • DE2303586
    • 1973-01-25
    • SIEMENS AG
    • KOCH CHRISTIAN DIPL ING
    • F02C3/24F02C3/20F02C7/00
    • Disclosed herein is an improvement for a gas turbine which has been adapted to burn fuel processed by catalytic or non catalytic type gas converters. This adaptation has resulted in the reduction of the harmful polutants being emitted to the environment. The improvement, recognizing that a turbine operating with such processed fuel runs at considerably high combustion chamber temperatures, calls for the positioning of heat exchange mechanisms in the path of the exhaust gases emanating from the turbine's decompression unit. These mechanisms preheat the fuel and air needed in the conversion process. Additionally, heat exchange mechanisms are positioned about and between the reaction chambers in the gas converter. Part of the exhaust gases are routed through these facilitating the gas conversion process. Further, mixing means are provided wherein the preheated air cooperates with the exhaust gases to reduce the heat of the latter before they pass via the turbine's decompression unit into the environment. An alternate improvement calls for the placement of a water vaporizer in the path of the exhaust gases. Water supplied thereto is vaporized and then supplied to the gas converter for reaction with the fuel in a known way.
    • 4. 发明专利
    • DE2306008A1
    • 1974-08-08
    • DE2306008
    • 1973-02-07
    • SIEMENS AG
    • KOCH CHRISTIAN DIPL ING
    • B01D3/20B01D3/22B01D53/18
    • The invention concerns a column for bringing gases or vapors and liquids into contact which uses a plurality of plates made from a highly porous, open-pore, sintered material. According to the invention, the gas and the liquid are conducted in this column countercurrent-wise; the column plates are equipped with run-off tubes which have at the lower end a gas shut-off device such that upon starting, the path for the gas is blocked by the gas shut-off device because of the liquid column contained therein. This liquid column exerts on the gas a larger pressure than corresponds to the pressure difference between the gas in the space under the associated column plate and that above. The run-off tube is of such size that it is only partly filled by the liquid column so that it can continuously adjust itself during operation. The actual reaction between the gas and the liquid takes place partially within the column plates resulting in a greater exchange between the liquid and the gas and making the column relatively insensitive to motion effects and load variations.