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    Nitrogen+Syngas

    Problem No. 46: CO₂ cooler failure


    CO2 coolers in the inter stages of CO2 compressors typically cool down the CO2 stream by means of cooling water. It is preferable for the cooling water through the tubes to have a minimum velocity to avoid fouling and corrosion issues. This is not a problem after the first and second stage when CO2 pressures are still relatively low. However, after the third stage the CO2 pressure is about 10 bar, too high (meaning too expensive) to have the CO2 on the shell side. Vendors specify coolers with the cooling water on the shell side and the CO2 through the tubes. This however introduces several failure mechanisms: As cooling water velocities cannot be guaranteed to be above a minimum value in the complete shell, fouling can occur. Also, chlorides accumulate (even when chloride levels are relatively low) and cause chloride stress corrosion cracking in austenitic stainless-steel tubes. In this type of cooler choosing duplex as the material of construction for the tubes is the best choice for a reliable heat exchanger.

    Irfan Rashid, working in Operations at FFBL in Pakistan starts the discussion with the following question: Does anyone have experience of CO2 cooler failure where failure occurs after the third stage of the CO2 compressor?

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