Simulation system and method for wet desulphurization flow fields
A technology of wet desulfurization and simulation method, which is applied in simulators, separation methods, general control systems, etc., and can solve problems such as the accuracy of CFD numerical simulation results and design feasibility.
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Embodiment 1
[0165] This embodiment provides a simulation system of a wet desulfurization flow field, including a spray tower model, an air supply system, a water supply system, an online control system, a powder feeding device and a dust removal system.
[0166] see figure 1 , figure 1 A schematic flow chart of the simulation system for the wet desulfurization flow field simulation system of the coal-fired power plant provided by the present invention,
[0167] In this embodiment, the spray tower model includes an inlet flue, a slurry tank, a tray, a spray layer, a demister and an outlet flue; wherein, in the vertical direction, the slurry tank, the inlet flue, the tray, the spray The spray layer, mist eliminator and outlet flue are arranged in sequence from bottom to top.
[0168] The air supply system includes a shaft-driven centrifugal blower, a fan frequency conversion controller, an online test device for the air supply system, and an air supply pipeline.
[0169] The water supply...
Embodiment 2
[0174] The flue gas flow rate of a 660MW coal-fired power plant wet desulfurization prototype is 1779800m under 100% BMCR condition 3 / h, the flue gas temperature is 92°C, and the flue gas density is 0.9983kg / m 3 , limestone slurry flow rate is 42000m 3 / h, the slurry density is 1140kg / m 3 ; During the model test, air simulates flue gas and water simulates limestone slurry, the air temperature is 27°C, and the air density is 1.2kg / m 3 , the water temperature is 15°C, and the water density is 998.4kg / m 3 ;The model is scaled down according to the prototype size 1:12, then the structural parameters and test parameters of the model are determined as follows:
[0175] (1) Model structure parameters
[0176] The inlet flue, outlet flue, and tower diameter of the model are reduced in proportion to the prototype size 1:12; the opening ratio of the model tray is the same as the prototype, and the partition height is the same as the prototype; the nozzles and nozzle spacing of the ...
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