Variable load control and optimization method for air separation liquefaction device
A technology of liquefaction device and optimization method, applied in design optimization/simulation, special data processing application, geometric CAD, etc., can solve the problems of waste of energy consumption, difficult control of variable load process, gas emission of pipeline network, etc.
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[0071] Taking medium-pressure nitrogen feed at 313K with a pressure of 24.44atm (the pressure fluctuates between 1.6MPa-2.5Mpa) as an example, the operating pressures at the compression end BC1 and BC2 of the high-temperature expander at steady state are 33atm and 14.2atm respectively; The operating pressures of ET1 and ET2 are 10atm and 1.35atm respectively; the temperature of multi-stream heat exchange outlet streams 1-4 is about 200K, and the temperature of 1-12 is about 139K. The total flow of nitrogen from the pipe network is 15000Nm3 / h, of which 2700Nm3 / h nitrogen directly enters the nitrogen channel of the main heat exchanger to exchange heat with the return gas, liquefies in the main heat exchanger, cools down to 81.1K, and throttles through the V6y valve After reaching about 3atm, it will be sent out as a product. Based on this working condition, the equivalent heat exchange network parameters of the multi-stream heat exchanger are estimated. The parameters of the eq...
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