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    • 86. 发明专利
    • METHOD AND APPARATUS FOR FEEDING CONDENSATE TO A HIGH PRESSURE VAPOR GENERATOR
    • CA1120798A
    • 1982-03-30
    • CA313271
    • 1978-10-12
    • CHEN THOMAS Y C
    • CHEN THOMAS Y C
    • F22B35/00F22D5/30F22D5/34F22D11/00F22D11/06F22D5/28
    • METHOD AND APPARATUS FOR FEEDING CONDENSATE TO A HIGH PRESSURE VAPOR GENERATOR A mechanical arrangement to reduce drastically the energy consumption for pumping condensate to feed high pressure vapor generators for power generation, industrial processing, and heating systems. Involved is a method to pump the condensate into one condensate receiver located at the suction side of the condensate feed pump, and to bleed high pressure vapor from the vapor generator into the condensate receiver for imposing a pressure head upon the condensate therein to be approximately the same as that in the generator, and thus the pressure difference between the suction side and the discharge side of the pump is drastically reduced while pumping the condensate into the generator, with the result that the energy consumption of the pump is also drastically reduced. The receiver is full of high pressure vapor while the condensate therein is drained by the pump, and the high pressure vapor means energy. Further new methods are involved to reduce the vapor pressure in the receiver by returning the vapor to the system or to utilize it, as disclosed in the application. Generally speaking, at least two closed receivers operated in series are required for the method of restoring the vapor in the receivers to the generator after the condensate is pumped into the generator. The invented receivers are also designed for condensate healing with almost no energy consumption.
    • 89. 发明专利
    • ES490893A0
    • 1981-02-16
    • ES490893
    • 1980-04-25
    • FRANCIA GIOVANNI
    • F22B35/10F24J2/40F22G5/04F22D5/28
    • A solar energy plant comprises a solar energy boiler having pre-heating, evaporation, and superheating stages, and a control system for maintaining constant the temperature and the volume of the superheated steam at the boiler outlet upon variations in the incident solary energy. The flow of water entering the boiler is divided into a main flow, passing through the preheating, evaporation and superheating stages, and a secondary water flow. A first part of the secondary water flow is injected directly into the evaporation stage and a second part of the secondary water flow is injected directly into the superheating stage. The control system includes valve means for varying the rate of flow of the main water flow, and the first and second parts of the secondary water flow such as to maintain constant the temperature of the output superheated steam.
    • 90. 发明专利
    • NL161276B
    • 1979-08-15
    • NL7300703
    • 1973-01-17
    • SULZER AG
    • G01K17/00F22B35/10G01K17/06G01N25/60G06G7/56G06G7/12F22D5/28
    • The enthalpy calculating device includes a function generator which receives two signals, one representative of either the temperature or pressure property of the steam and the other representative of the enthalpy of the steam for the particular state of the steam. The function generator then emits an output signal corresponding to the other of the temperature or pressure property of the steam. The device also has a controller means composed of a comparator and integrator or an integral action controller. This latter means receives the output of the function generator and compares it with the actual value of the "other" property of the monitored steam. If there is a difference, the output of the controller means is corrected accordingly. This output serves not only as one of the input signals to the function generator but also as the output signal of the device to control the flow of feed water.