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Where is it more appropriate to send the liquid separated by the transformed torch separator?
Will NH3 and H2S present in the condensate have an impact on wastewater treatment?
It can also be sent to transformed stripping, but the amount should not be too large, otherwise it will disrupt the operating conditions of stripping.
The design of the Second Chemical Plant is to separate gas, water, and steam
What height of head does the condensate pump need? Additionally, is it appropriate to send the condensate to the gas-water separator?
No pump is needed; system pressure is used. The gas condensate designed by the Second Chemical Engineering Institute is sent to the gas-water separation unit
The liquid separated in the torch separator tank cannot have such high pressure!
First, determine the amount of condensate. Under normal conditions, there is almost no condensate in the flare liquid separation tank in the conversion unit. Moreover, the back pressure in the flare system is generally not very high. If it is necessary to remove moisture from the gas, the pressure may need to be increased significantly. Whether gas stripping is feasible depends on the back pressure of the flare system and the operating pressure of the gas stripping system; it is possible if the pressures are suitable and the amount of condensate is not excessive. Monitor the water quality and send it to the wastewater treatment facility
Yes, the back pressure on the torch gas side is at most a few dozen kPa