3 research outputs found
Comparison of the CO<sub>2</sub> Absorption Characteristics of Aqueous Solutions of Diamines: Absorption Capacity, Specific Heat Capacity, and Heat of Absorption
Aqueous
amine solutions have been widely used for the absorption of carbon
dioxide (CO<sub>2</sub>) from the gas mixtures. An understanding of
the physical and chemical properties of aqueous amine solutions is
important for the successful design and operation of CO<sub>2</sub> absorption processes. Particularly, the absorption capacity, absorption
rate, and heat of absorption of CO<sub>2</sub> are major factors that
affect the CO<sub>2</sub> absorption and stripping performance. A
comparison study of the aqueous piperazine (PZ), 2-methylpiperazine
(2-MPZ), homopiperazine (HomoPZ), and hexamethylenediamine (HMDA)
solutions was conducted in this study. Absorption capacities and heats
of absorption of these diamine solutions were measured using a semibatch-type
reactor and a differential reaction calorimeter (DRC). The species
distributions of the absorbents were investigated using a nuclear
magnetic resonance spectroscopy (NMR), and the CO<sub>2</sub> absorption
mechanism was also discussed. Aqueous PZ and PZ derivative solutions
(2-MPZ and HomoPZ) displayed excellent characteristics as CO<sub>2</sub> absorbents. Aqueous 10 wt % PZ and PZ derivative solutions had higher
absorption capacities and lower heats of absorption than that of aqueous
10 wt % monoethanolamine (MEA) at 313 K (−Δ<i>H</i><sub>abs</sub> of the CO<sub>2</sub>-saturated PZ, 2-MPZ, HomoPZ,
and MEA solutions: 62, 58, 68, and 80 kJ/mol CO<sub>2</sub>)
CO<sub>2</sub> Absorption and Sequestration as Various Polymorphs of CaCO<sub>3</sub> Using Sterically Hindered Amine
One aspect of the attempt to restrain
global warming is the reduction
of the levels of atmospheric CO<sub>2</sub> produced by fossil fuel
power systems. This study attempted to develop a method that reduces
CO<sub>2</sub> emissions by investigating the absorption of CO<sub>2</sub> into sterically hindered amine 2-amino-2-methyl-1-propanol
(AMP), the acceleration of the absorption rate by using the enzyme
carbonic anhydrase (CA), and the conversion of the absorption product
to stable carbonates. CO<sub>2</sub> absorbed by AMP is converted
via a zwitterion mechanism to bicarbonate species; the presence of
these anions was confirmed with <sup>1</sup>H and <sup>13</sup>C NMR
spectral analysis. The catalytic efficiency (<i>k</i><sub>cat</sub>/<i>K</i><sub>m</sub>), CO<sub>2</sub> absorption
capacities, and enthalpy changes (Δ<i>H</i><sub>abs</sub>) of aqueous AMP in the presence or absence of CA were found to be
2.61 × 10<sup>6</sup> or 1.35 × 10<sup>2</sup> M<sup>–1</sup> s<sup>–1</sup>, 0.97 or 0.96 mol/mol, and −69 or −67
kJ/mol, respectively. The carbonation of AMP-absorbed CO<sub>2</sub> was performed by using various Ca<sup>2+</sup> sources, viz., CaCl<sub>2</sub> (CAC), CaÂ(OOCCH<sub>3</sub>)<sub>2</sub> (CAA), and CaÂ(OOCCH<sub>2</sub>CH<sub>3</sub>)<sub>2</sub> (CAP), to obtain various polymorphs
of CaCO<sub>3</sub>. The yields of CaCO<sub>3</sub> from the Ca<sup>2+</sup> sources were found in the order CAP > CAA > CAC as
a result
of the effects of the corresponding anions. CAC produces pure rhombohedral
calcite, and CAA and CAP produce the unusual phase transformation
of calcite to spherical vaterite crystals. Thus, AMP in combination
with CAA and CAP can be used as a CO<sub>2</sub> absorbent and buffering
agent for the sequestration of CO<sub>2</sub> in porous CaCO<sub>3</sub>
Carbonic Anhydrase Promotes the Absorption Rate of CO<sub>2</sub> in Post-Combustion Processes
The rate of carbon dioxide (CO<sub>2</sub>) absorption by monoethanol
amine (MEA), diethanol amine (DEA), <i>N</i>-methyl-2,2′-iminodiethanol
(MDEA), and 2-amino-2-methyl 1-propanol (AMP) solutions was found
to be enhanced by the addition of bovine carbonic anhydrase (CA),
has been investigated using a vapor–liquid equilibrium (VLE)
device. The enthalpy (−Δ<i>H</i><sub>abs</sub>) of CO<sub>2</sub> absorption and the absorption capacities of aqueous
amines were measured in the presence and/or absence of CA enzyme via
differential reaction calorimeter (DRC). The reaction temperature
(Δ<i>T</i>) under adiabatic conditions was determined
based on the DRC analysis. Bicarbonate and carbamate species formation
mechanisms were elucidated by <sup>1</sup>H and <sup>13</sup>C NMR
spectral analysis. The overall CO<sub>2</sub> absorption rate (flux)
and rate constant (<i>k</i><sub>app</sub>) followed the
order MEA > DEA > AMP > MDEA in the absence or presence of
CA. Hydration
of CO<sub>2</sub> by MDEA in the presence of CA directly produced
bicarbonate, whereas AMP produced unstable carbamate intermediate,
then underwent hydrolytic reaction and converted to bicarbonate. The
MDEA > AMP > DEA > MEA reverse ordering of the enhanced CO<sub>2</sub> flux and <i>k</i><sub>app</sub> in the presence
of CA
was due to bicarbonate formation by the tertiary and sterically hindered
amines. Thus, CA increased the rate of CO<sub>2</sub> absorption by
MDEA by a factor of 3 relative to the rate of absorption by MDEA alone.
The thermal effects suggested that CA yielded a higher activity at
40 °C