Column plate structure capable of eliminating gas-phase deflected flow and design method
A technology of structural design and trays, applied in the field of chemical vapor-liquid mass transfer separation equipment, can solve the problems of reduced tray efficiency, induced trays, and pouring at the entrance of trays, etc., to eliminate liquid level drop and gas phase distribution. Uniform, uniform gas phase flow effect
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Embodiment 1
[0111] The design gas phase mass flow rate is 15000kg / hr, and the gas phase density is 2.5kg / m 3 , the mass flow rate of the liquid phase is 40000kg / hr, and the density of the liquid phase is 880kg / m 3 , the surface tension is 10N / m, and the viscosity is 1mPa·s. The mass transfer tray type is selected as a sieve tray column. Through the preliminary design, the structural parameters of the tray type are shown in Table 1:
[0112] Table 1 Design parameters of mass transfer tray structure
[0113]
[0114] The parameters calculated by formulas (1) to (9) are shown in Table 2:
[0115] Table 2 Calculation results of parameters related to the liquid level gradient of the mass transfer tray
[0116]
[0117] Divide the gas phase distribution plate into five zones, the length of each zone is 200 mm, and the ratio coefficient of gas phase distribution plate opening ratio is 1.4 (the gas phase distribution plate opening rate is 17.85%), then the gas phase distribution plate calc...
Embodiment 2
[0124] The design gas phase mass flow rate is 60000kg / hr, and the gas phase density is 2.5kg / m 3 , the mass flow rate of the liquid phase is 70000kg / hr, and the density of the liquid phase is 880kg / m 3 , the surface tension is 10N / m, and the viscosity is 1mPa·s. The mass transfer tray type is selected as a sieve tray column. Through the preliminary design, the structural parameters of the tray type are shown in Table 5:
[0125] Table 5 Mass transfer tray structure design parameters
[0126]
[0127] The parameters calculated by formulas (1) to (9) are shown in Table 6:
[0128] Table 6 Calculation results of parameters related to the liquid level gradient of the mass transfer tray
[0129]
[0130] The gas phase distribution plate is divided into four zones, the length of each zone is 400 mm, and the ratio coefficient of the gas phase distribution plate opening ratio is 1.4 (the gas phase distribution plate opening rate is 20.31%), then the gas phase distribution cal...
Embodiment 3
[0137] The design gas phase mass flow rate is 60000kg / hr, and the gas phase density is 2.5kg / m 3 , the mass flow rate of the liquid phase is 70000kg / hr, and the density of the liquid phase is 880kg / m 3 , the surface tension is 10N / m, and the viscosity is 1mPa·s. The mass transfer tray type is selected as a sieve tray column. Through the preliminary design, the structural parameters of the tray type are shown in Table 9:
[0138] Table 9 Mass transfer tray structure design parameters
[0139]
[0140] The parameters calculated by formulas (1) to (9) are shown in Table 10:
[0141] Table 10 Calculation results of parameters related to the liquid level gradient of the mass transfer tray
[0142]
[0143] Divide the gas phase distribution plate into two zones, the length of each zone is 800 mm, and the ratio coefficient of the opening ratio of the gas phase distribution plate is 1.4 (the opening rate of the gas phase distribution plate is 20.31%), then the gas phase distr...
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