Thread Content
22. During the production process of a certain silicone plant, two streams of exhaust gas containing HCl are generated. It is planned to use clean water at 20°C in an absorption tower to recover the HCl from these two streams; one of these streams has a flow rate of 146 kmol/h, with a HCl content of 10% (on a molar basis), and this stream is introduced into the tower from the bottom; Another flow rate of 108 kmol/h, with a 4% HCl content, is added separately at the optimal feeding point of the absorber. The absorber operates at atmospheric pressure, and the Henry’s coefficient under these operating conditions is 2.786×10^5 Pa. If a total HCl recovery rate of not less than 95% is required, the actual liquid-to-gas ratio in the upper section of the absorber should be 1.2 times the minimum liquid-to-gas ratio. What is the value (in kmol/h) of the absorption dose that needs to be applied to the absorber? A 254 B 698 C 754 D 838 This question was discussed before, and answer B was ultimately chosen. The process is calculated based on a feed material concentration of 4%. However, based on the absorption process as indicated in the question, the concentration in the gas phase should gradually decrease; therefore, the feed concentration should be taken as 10%. The result obtained through this calculation is 737, so the correct answer should be C.
First, it must be clear that the inlet location in the upper section is at the point where the concentration in the lower section reaches 4%. For this problem, calculation can only be done using the method described in the previous paragraph; if the method from the following paragraph is used, the gas volumes at the upper and lower ends will differ, and the baseline will also be different, which makes it easy to make mistakes in determining the value of Y. The exact answer is 701. If 0.04 is used, it will be 698.