Low sulfur emission sulfur recovery process for low concentration acid gas
A sulfur recovery and acid gas technology, applied in the preparation/purification of sulfur, energy input, etc., can solve the problems of ineffective utilization of waste sulfur, multi-safety and environmental pollution, affecting the safety of operators, etc., and achieve scrap treatment. Good conditions, good safe operating conditions, good effect on site environment
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Embodiment 1
[0043] A set of 10,000 tons / year sulfur recovery unit, including selective oxidation reactor and two adsorption desulfurization towers that can be connected in series and parallel, the selective oxidation reactor is filled with Fe 2 o 3 / SiO 2 selective oxidation of H 2 S Catalyst 60m 3 , the catalyst is packed in 6 layers, and a cooling coil is installed between the layers to generate steam; two adsorption desulfurization towers are filled with Na 2 CO 3 / Activated carbon catalytic oxidation adsorption desulfurizer 150m 3 ; The basic operating conditions of the device are:
[0044] 1) Acid gas 28000m 3 / hr,H 2 S volume content 3.6%, the rest is mainly CO 2 , COS≤20mg / m 3 , SO 2 ≤100mg / m 3 , the difficult-to-handle CS 2 , with air 2400m 3 / hr or so, preheated to 200°C and enters the selective oxidation reactor, H 2 S is selectively oxidized to elemental sulfur. The process gas from the selective oxidation reactor enters the medium temperature condenser and is co...
Embodiment 2
[0054] A set of 10,000 tons / year sulfur recovery unit, including selective oxidation reactor and two adsorption desulfurization towers that can be connected in series and parallel, the selective oxidation reactor is filled with Fe 2 o 3 / SiO 2 selective oxidation of H 2 S Catalyst 60m 3 , the catalyst is packed in 6 layers, and a cooling coil is installed between the layers to generate steam; the two adsorption desulfurization towers are filled with Fe 2 o 3 / Activated carbon catalytic oxidation adsorption desulfurizer 140m 3 ; The basic operating conditions of the device are:
[0055] 1) Acid gas 20000m 3 / hr,H 2 S volume content 5%, the rest is mainly CO 2 , SO 2 ≤100mg / m 3 , excluding COS, CS 2 , mercaptan, sulfide and other organic sulfur; with air 2400m 3 / hr or so, preheated to 200°C and enters the selective oxidation reactor, H 2 S is selectively oxidized to elemental sulfur. The process gas from the selective oxidation reactor enters the medium temperatur...
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