Process device and process method for liquid phase reaction desulfurization of sulfur dioxide and hydrogen sulfide
A process method, sulfur dioxide technology, applied in chemical instruments and methods, separation methods, preparation/purification of sulfur, etc., can solve the problems that the purity of sulfur products cannot meet the market demand, increase the operating cost of the device, etc., shorten the reaction time, prevent Effect of depositing scale and increasing reaction rate
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Embodiment 1
[0056] Process devices for liquid-phase reaction desulfurization of sulfur dioxide and hydrogen sulfide, such as figure 1 As shown, it includes a reactor 10 and a separator 20. The reactor 10 is followed by a tail gas absorption area 100, a liquid holding tank area 200 and a reaction area 300 from top to bottom; the liquid holding tank area 200 includes a partition 201, Several gas lift cylinders 202 and downcomers 203, the partition plate 201 is fixed on the wall of the device to isolate the tail gas absorption zone 200 and the reaction zone 300, the gas lift cylinder 202 penetrates through the partition plate 201 and communicates with the tail gas absorption zone 100 and the reaction zone 300; one end of the downcomer 203 is fixed to the partition plate 201 and communicated with the exhaust gas absorption zone 100, and the other end extends downward to the bottom of the reaction zone 300; the lower part of the reaction zone 300 is provided with two nozzles 301, symmetrically ...
Embodiment 2
[0059] use figure 1 The process method for the reaction desulfurization of sulfur dioxide and hydrogen sulfide in the process unit shown is as follows:
[0060] First pure SO 2 The gas is introduced into the reaction zone 300 of the reactor 10 through the two nozzles 301. The reaction solution in the reaction zone 300 is an aqueous solution of an organic basic compound. When the pH online monitor 304 shows that it is 6.5, the gas starts to be passed into the reaction zone 300. pure H 2 S gas, the liquid in the reaction zone 300 quickly turns yellow, and it can be seen that the two react immediately to generate sulfur; the sulfur slurry flows upwards and enters the liquid collecting tank 302 under the impetus of the continuously introduced gas. When the liquid level is higher than the liquid phase, it is drawn out. When the outlet of the pipe 303, the slurry entrained with sulfur flows into the separator 20, and the sulfur and the reaction solution are separated, and the reac...
Embodiment 3
[0064] use figure 1 The process method for the reaction desulfurization of sulfur dioxide and hydrogen sulfide in the device shown:
[0065] Except that the organic alkaline compound aqueous solution is a 20% benzylamine solution, other conditions are the same as in Example 2.
[0066] Access H 2 The reaction response time of the two gases after S is 5s. According to the material balance calculation, H 2 The conversion rate of S was 93.7%.
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