Technology and equipment for continuously preparing sulfur dioxide from low-concentration fuming sulfuric acid
A technology of fuming sulfuric acid and sulfur dioxide, applied in the direction of sulfur compounds, inorganic chemistry, chemical instruments and methods, etc., can solve the problems of unrecovered sulfur trioxide, long process route, hidden safety hazards, etc., and achieve the reduction of sulfur trioxide technology, process Simplicity and efficiency-enhancing effects
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Embodiment 1
[0034] 1) The gas phase of the 4th and 5th stage converters of the sulfuric acid preparation process is passed from the gas phase input pipeline 1 to the secondary absorption tower 2 for absorption, and the gas phase enters the external absorption system to continue absorption. The liquid phase obtained by absorption is oleum (concentration 101%), enter the circulation tank 3, and continuously drive into the first-stage reaction tower 6 through the mechanical pump A4. At the same time, the liquid sulfur is introduced through the liquid sulfur pipeline A8 to react at 100°C and 0.05MPa, and the liquid sulfur is always maintained The state of under-quantity; among them, the mass ratio of liquid sulfur to oleum is 1:30.
[0035] 2) The reaction liquid produced by the reaction in step 1) is continuously pumped back into the circulation tank 3 through the mechanical pump B5; the concentration of the fuming sulfuric acid in the reaction liquid is 100.5%.
[0036] 3) The mixed gas produced...
Embodiment 2
[0039] 1) The gas phase of the 4th and 5th stage converters of the sulfuric acid preparation process is passed from the gas phase input pipeline 1 to the secondary absorption tower 2 for absorption, and the gas phase enters the external absorption system to continue absorption. The liquid phase obtained by absorption is oleum (concentration 100.3%), enter the circulation tank 3, and continuously drive into the first-stage reaction tower 6 through the mechanical pump A4. At the same time, the liquid sulfur is introduced through the liquid sulfur pipeline A8 to react at 135°C and normal pressure, and the liquid sulfur is always maintained. The state of under-quantity; among them, the mass ratio of liquid sulfur to oleum is 1:50.
[0040] 2) The reaction liquid produced by the reaction in step 1) is continuously pumped back into the circulation tank 3 through the mechanical pump B5; the concentration of oleum in the reaction liquid is 100.1%.
[0041] 3) The mixed gas produced by the ...
Embodiment 3
[0044] 1) The gas phase of the 4th and 5th stage converters of the sulfuric acid preparation process is passed from the gas phase input pipeline 1 to the secondary absorption tower 2 for absorption, and the gas phase enters the external absorption system to continue absorption. The liquid phase obtained by absorption is oleum (concentration 102%), enter the circulation tank 3, continuously drive into the first-stage reaction tower 6 through the mechanical pump A4, and at the same time, pass the liquid sulfur through the liquid sulfur pipeline A8 to react at 70°C and 0.1MPa, and always maintain the liquid sulfur The state of under-quantity; among them, the mass ratio of liquid sulfur to oleum is 1:12.
[0045] 2) The reaction liquid produced by the reaction in step 1) is continuously pumped back into the circulation tank 3 through the mechanical pump B5; the concentration of oleum in the reaction liquid is 101%.
[0046] 3) The mixed gas generated by the reaction in step 1) enters t...
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