heal.abstract |
Carbon dioxide (CO2) is the major contributor of global warming covering more than 60%
of greenhouse gases. Major CΟ2 production occurs by industries and power plants using
fossil fuel. Chemical absorption is an effective and widely used, by industries, method for
CO2 separation and capture due to low equipment cost, high removal efficiency, stable
operation conditions, and mature technology background. Main solvent in industry is the
alkanolamines with high absorption rates. Depending on the kind of amine (primary,
secondary, tertiary) higher rates have been noticed for Μonoethanolamine (MEA) following
by Pentaethylenehexamine (PEHA) and last Methyldiethanolamine (MDEA). As solvents or in
mixtures with alkanolamines, the ionic liquids (PEHA-prolinate) offer stability and lower
volatility to the system. The use of biocatalysts (enzymes) into the system has been proven
to increase the absorption rates useful. Carbonic anhydrase (CA) is a powerful zinc
metalloenzyme that accelerates the transformation of carbon dioxide to bicarbonate ion. A
mutant version of the carbonic anhydrase has an activity of the order of 4.5 units/μL enzyme
solution or 2.07 units/mg of lyophilized enzyme, which remains quite high when the enzyme
appears in high temperatures and basic pH.
In a tiny clave absorption process the maximum capacity in CO2 differs among the amines
with capacity for aqueous solution of MDEA (25% w/w) being 80.7mgCO2/g of solvent, 122.0
mgCO2/g of solvent for the PEHA (25% w/w), 109.5 mgCO2/g of solvent for the MEA (25%
w/w) and 82.7 mgCO2/g of solvent for the ionic liquid PEHA-prolinate (25% w/w). The
absorption rates for the alkanolamines and the ionic liquid were calculated 0.75 mgCO2/g
MDEA (25% w/w) /min, 2.79 mgCO2/g PEHA (25% w/w)/min, 3.12 mgCO2/g MEA (25%
w/w)/min and 1.64 mgCO2/g PEHA-prolinate (25% w/w)/min. By adding an enzyme solution
(1% w/w), an increase of 40%, 9.32%, 8.01% and 4.88% occurred in the absorption rates of
MDEA, PEHA, MEA, PEHA-prolinate respectively.
By scaling up the equipment, absorption and stripping rates of alkanolamines and the
mixes among them and with ionic liquids were calculated, offering significant results.
Specifically, the mix of MDEA-PEHA (1:1 ratio) had an absorption rate higher than the rate of
MDEA 25% and close to the rate of the PEHA 25%. The PEHA-prolinate - MDEA (1:1 ratio) did
showed a high rate, as well. Experiments were also carried out in a pilot plant for MDEA
solution. |
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