Seeking advice on issues with the coke gas condenser
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I’m currently designing a tar vapor condenser: the fluids involved are tar vapor and gas, with a temperature starting at 450 degrees and dropping to 80 degrees (the phase transition temperature of tar is 120 degrees). The tar that is condensed has a high viscosity, amounting to 12.5 mPaS. The cooling medium is deionized water, at a temperature of 25 degrees, with the outlet temperature being 80 degrees. Which type of heat exchanger is suitable? Should the coke gas flow through the shell side or the tube side?
Has the tar condenser been designed and put into use? We happen to have a project with a similar requirement! If the product is already in use or the technology is mature, please send relevant materials to 877165052@qq.com