Adjustable apparatus for producing SO3 gas by using inertia catalyst to process high-density SO2 flue gas
A SO2, high-concentration technology, applied in the direction of climate sustainability, sustainable manufacturing/processing, inorganic chemistry, etc., can solve the problems of inefficient use of energy, high investment, etc., and achieve improved utilization of waste heat, high production intensity, and land occupation saving effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] Environmental protection desulfurization recovery of SO in a power plant 2 The gas is used to produce sulfuric acid, and the gas composition of the flue gas after drying is: SO 2 —30.69%, O 2 —18.47%, N 2 —49.36%, CO 2 —1.48%, the total gas volume is about 90000Nm 3 / hr. flue gas through SO 2 After the blower 1 is boosted, it is heated to 390°C by the heat exchanger 2 and then enters the first inert catalyst conversion layer 31, the conversion rate is about 35%, and the outlet gas temperature is 660°C and contains SO 2 The concentration is 21.43%; after heat exchange by the first waste heat utilization device 41 (production of medium pressure 2.5MPa saturated steam 17.7t / hr), the temperature is lowered to 390°C and then enters the second inert catalyst conversion layer 32, and the total conversion rate of the reaction is about 60%. The outlet temperature is 580°C and contains SO 2 The concentration is 13.75%; after heat exchange by the second waste heat utilizat...
Embodiment 2
[0030] A sulfur acid plant adopts oxygen-enriched combustion to generate SO 2 The gas is used to produce sulfuric acid, and its gas composition after combustion is: SO 2 —20.78%, O 2 —17.39%, N 2 —61.83%, the total gas volume is about 115930Nm 3 / hr. flue gas through SO 2 After the blower 1 is boosted, it is heated to 390°C by the heat exchanger 2 and then enters the first inert catalyst conversion layer 31, the conversion rate is about 35%, and the outlet gas temperature is 587°C and contains SO 2 The concentration is 14.28%; after heat exchange by the first waste heat utilization device 41 (production of medium pressure 2.5MPa saturated steam 15.56t / hr), the temperature is lowered to 420°C and then enters the second inert catalyst conversion layer 32. The total conversion rate of the reaction is about 65%. The outlet temperature is 585°C and contains SO 2 The concentration is 7.95%; after heat exchange by the second waste heat utilization device 42 (production of medi...
Embodiment 3
[0032] SO 2 The gas is used to produce sulfuric acid, and its gas composition after combustion is: SO 2 —15.26%, O 2 —13.04%, N 2 —69.64%, CO 2 —2.06%, the total gas volume is about 154800Nm 3 / hr. flue gas through SO 2 After the blower 1 is boosted, it is heated to 390°C by the heat exchanger 2 and then enters the first inert catalyst conversion layer 31, the conversion rate is about 47%, and the outlet temperature is 590°C and contains SO 2 The concentration is 8.55%; after the heat exchange of the first waste heat utilization device 41 (production of medium pressure 2.5MPa saturated steam 17.46t / hr), the temperature is lowered to 390°C, and then enters the first layer reaction of the traditional active catalyst layer 5, and the total conversion rate of the reaction is About 85%, the outlet temperature is 550°C and contains SO 2 The concentration is 2.5%, the exhaust gas is cooled to 420°C by the corresponding heat exchanger, and then enters the second layer of the tra...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
