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In addition, they could be regenerated by heat treatment to release the adsorbates.
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Furthermore, if fouled, they can be regenerated by heating in air or using an acid wash.
For pre-combustion, MnO will capture CO2 at a partial pressure of about 10 bar below 327 °C and then could be regenerated by heating above 377 °C to produce a stream of pure CO2.
The palladium catalyst wafers and desiccant wafers need to be regenerated by heating 160°C for two hours weekly, and can be reused for one year.
Afterwards, the solvent is regenerated by heating and/or flashing to a lower pressure.
In the stripper, the rich solvent is regenerated by heating it further to about 120 °C at a pressure of about 1.8 atm.
The Selexol in the sulfur removal unit is regenerated by heating which removes the dissolved sulfur and CO2.
After the adsorption of SO2, the exhausted sorbent/catalysts could be regenerated by direct heat treatment in inert gas at temperatures between 260 and 480 °C, while the neighboring surface oxygen complexes on the carbon surface were acting as the reducing agents to reduce CuSO4 to Cu.
Spent adsorbent can be regenerated by simple heating treatment in N2 at 500 °C, without obvious losing of thiophene adsorption capacity even after eight cycles.
Egyptian Salafis believe that society can be regenerated by a return to strict Islamic values.
Coked catalysts may often be regenerated by in situ oxidation.
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