Method and device for purifying and regenerating hot potash solution of Fischer-Tropsch synthesis tail gas and application
A purification and regeneration device and a Fischer-Tropsch synthesis technology are applied in the field of purification and regeneration of hot potash alkali solution of Fischer-Tropsch synthesis tail gas, and purification and regeneration of hot potash alkali solution after decarbonization of Fischer-Tropsch synthesis tail gas, which can solve safety accidents, complicated operations, The problems such as low utilization rate of material energy can achieve the effect of improving the use efficiency, solving the high loss and reducing the production and operation cost.
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Embodiment 1
[0050] This embodiment provides a method for purifying and regenerating hot potassium-alkali solution of Fischer-Tropsch synthesis tail gas, which includes: sending the decarburized hot potassium-alkali solution into an evaporation crystallization device, under an absolute pressure of 20kPa and a solution heating temperature of 100°C Crystallized by evaporation to obtain K 2 CO 3 、KHCO 3 and CH 3 COOK, C 2 h 5 Solid mixed potassium salt composed of organic acid potassium such as COOK. The steam condensate obtained after condensing the steam formed by evaporation and crystallization is recycled. The obtained solid mixed potassium salt enters the screw conveyor of the electrothermal roasting and cooling furnace. The screw conveyor pushes the material into the preheating section. After preheating, the material enters the roasting section. Moisture and volatile matter in high-temperature gasification materials at 650°C under pressure conditions. The time that the material s...
Embodiment 2
[0052] The hot potassium alkali solution (mainly potassium carbonate solution containing KHCO 3 and CH 3 COOK, C 2 h 5 COOK and other organic acid potassium solutions) are pumped into the spray drying device, and spray-dried with hot air at 180°C, so that the solution is dehydrated and dried until the water content is less than 1%, and K 2 CO 3 、KHCO 3 and CH 3 COOK, C 2 h 5 Solid mixed potassium salt composed of organic acid potassium such as COOK. The steam condensate obtained after the steam formed by spray drying is condensed is recycled. The obtained solid mixed potassium salt enters the screw conveyor of the electrothermal roasting and cooling furnace. The screw conveyor pushes the material into the preheating section. After preheating, the material enters the roasting section. Moisture and volatile matter in 600°C high-temperature gasification materials under pressure conditions. The time that the material stays in the roasting section is 60 minutes. The roas...
Embodiment 3
[0054] The difference from Example 2 is that the solid mixed potassium salt was calcined at 300°C, 400°C, 500°C, 650°C, 700°C, 750°C and 800°C for 60 minutes at each constant temperature. All the other operations are the same as in Example 2.
[0055] Performance Testing
[0056] 1. Sample weight loss test
[0057] Measure 50mL of decarburized sample solution (hot potassium alkali solution after decarburization) into a pre-dried and weighed crucible, spray dry with hot air at 180°C until there is no flowing liquid, and record the initial sample solution quality and after roasting After the total mass of the crucible and the sample liquid is put into the muffle furnace and roasted at 300°C, 400°C, 500°C, 600°C, 650°C, 700°C, 750°C and 800°C for 1 hour, observe the Change the situation and weigh its quality, and calculate the weight loss under different temperatures, as shown in Table 1.
[0058] Table 1 Sample weight loss under different temperatures
[0059]
[0060] No...
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