Process for removal of carbon dioxide from industrial gases

Claim 2

In a process for removing carbon dioxide (CO 2 ) from industrial combustion gases containing the CO 2 and O 2 contacting the gas, in a gas-liquid contactor, with an aqueous solution which contains an alkanol amine absorbent-reactant; circulating the solution from the contactor to a regeneration step wherein the CO 2 is released from the absorbent, the CO 2 recovered and the essentially CO 2 free absorbent recycled to the contactor, the improvement which consists of employing as the essential additives to said solution, to reduce degradation of the absorbent under the conditions of use and corrosion of the metals in contact with said solution during use, at least above 50 ppm of copper +2 and at least from 50 parts per million parts of solution one or more of the following: dihydroxyethylglycine, an alkali metal carbonate, an alkali metal or ammonium permanganate and nickel and/or bismuth oxides.

Claim 3

In a process for removing carbon dioxide (CO 2 ) from industrial combustion gases containing the CO 2 and O 2 contacting the gas, in a gas-liquid contactor, with an aqueous solution which contains an alkanol amine absorbent-reactant; circulating the solution from the contactor to a regeneration step wherein the CO 2 is released from the absorbent, the CO 2 recovered and the essentially CO 2 free absorbent recycled to the contactor, the improvement which consists of employing as the essential additives to said solution, to reduce degradation of the absorbent under the conditions of use and corrosion of the metals in contact with said solution during use, from 50 to 2000 ppm of copper as copper carbonate and at least from about 50 to about 2000 parts per million parts of the total solution of one or more of the following: dihydroxyethylglycine, an alkali metal carbonate, an alkali metal or ammonium permanganate, and nickel and/or bismuth oxides.

Claim 4

In a process for removing carbon dioxide (CO 2 ) from industrial combustion gases containing the CO 2 and O 2 contacting the gas, in a gas-liquid contactor, with an aqueous solution which contains an alkanol amine absorbent-reactant; circulating the solution from the contactor to a regeneration step wherein the CO 2 is released from the absorbent, the CO 2 recovered and the essentially CO 2 free absorbent recycled to the contactor, the improvement which consists of employing as the essential additives to said solution, to reduce degradation of the absorbent under the conditions of use and corrosion of the metals in contact with said solution during use, from 50 to 2000 ppm of copper as copper carbonate and at least from about 50 to about 2000 parts per million parts of the total solution of one or more of the following: dihydroxyethylglycine, an alkali metal carbonate, an alkali metal or ammonium permanganate, and nickel and/or bismuth oxides.

Claim 5

In a process for removing carbon dioxide (CO 2 ) from industrial combustion gases containing the CO 2 and O 2 by contacting the gas, in a gas:liquid contactor, with an aqueous solution which contains an alkanol amine absorbent-reactant; circulating the solution from the contactor to a regeneration step wherein the CO 2 is released from the absorbent, the CO 2 recovered and the essentially CO 2 free absorbent recycled to the contactor, the improvement which consists of employing as the essential additives to said solution, to reduce degradation of the absorbent under the conditions of use and corrosion of the metals in contact with said solution during use, from at least about 50 ppm of dihydroxyethylglycine and at least about 50 parts per million parts of a thiocyanate salt and nickel and/or bismuth oxides.

Claim 6

In a process for removing carbon dioxide (CO 2 ) from industrial combustion gases containing the CO 2 and O 2 by contacting the gas, in a gas:liquid contactor, with an aqueous solution which contains an alkanol amine absorbent-reactant; circulating the solution from the contactor to a regeneration step wherein the CO 2 is released from the absorbent, the CO 2 recovered and the essentially CO 2 free absorbent recycled to the contactor, the improvement which consists of employing as the essential additives to said solution, to reduce degradation of the absorbent under the conditions of use and corrosion of the metals in contact with said solution during use, from at least about 50 ppm of dihydroxyethylglycine and at least about 50 parts per million parts of a thiocyanate salt and nickel and/or bismuth oxides.