DCM & CCL4 Removal with Diesel II Fuel
Hydrocarbon Gas (Methane to Octane) was contaminated with Dichloromethane (DCM) and Carbon Tetra Chloride (CCL4). Proposal was sent to clean the gas using Diesel II Fuel. Simulation results shows that 5 Theoretical stages are required with HETP of 3 ft and total 15 ft packing height using 25 mm VSP® or Metal Saddles in Stainless Steel. Tower diameter of 18 inch was calculated based on the pressure drop requirement from customer. Tower Internals were design to handle minimum of 30 cfm and maximum of 100 cfm.
Hydrocarbon Gas (Methane to Octane) was contaminated with Dichloromethane (DCM) and Carbon Tetra Chloride (CCL4). Proposal was sent to clean the gas using Diesel II Fuel. Simulation results shows that 5 Theoretical stages are required with HETP of 3 ft and total 15 ft packing height using 25 mm VSP® or Metal Saddles in Stainless Steel. Tower diameter of 18 inch was calculated based on the pressure drop requirement from customer. Tower Internals were design to handle minimum of 30 cfm and maximum of 100 cfm.