9 research outputs found
Results from a pilot plant using un-promoted potassium carbonate for carbon capture
A pilot plant facility has been designed and built to trial potassium carbonate solvent technology for carbon capture under a range of conditions. The rig is capable of capturing 4 - 10 kg/hr of CO2 from 30 - 55 kg/hr of an air-CO2 mixture, with different packings. A series of trials have been completed with a range of solvent concentrations from 20 wt% to 30 wt% potassium carbonate. The experimental holdup, solvent loading and absorber temperatures have been matched with rate-based simulations in Aspen PlusĀ® software
Dissociation Constants (p<i>K</i><sub>a</sub>) of Tertiary and Cyclic Amines: Structural and Temperature Dependences
The dissociation constants of the
conjugate acids of 14 amines
(diethylethanolamine, monoethanolamine, <i>n</i>-butyldiethanolamine, <i>t</i>-butyldiethanolamine, <i>n</i>,<i>n</i>-dimethylpropanolamine, methyl-diethanolamine, ethyldiethanolamine,
monoethylethanolamine, <i>n</i>,<i>n</i>-dimethylisopropanolamine,
triethanolamine, 4-methylpiperazine-1-amine, 3-morpholino propylamine,
4,2-hydroxylethylmorpholine, and triethylamine) were measured over
a temperature range between 293.15 and 333.15 K using the potentiometric
titration method. The change in standard state thermodynamic properties
was derived from the vanāt Hoff equation. The influence of
the steric hindrance, number of āOH groups, and length of alkyl
chain on the dissociation constants was identified. Of the studied
amines, few sterically hindered derivatives of piperazine, a secondary
amine monoethylethanolamine, and a tertiary amine <i>n</i>,<i>n</i>-dimethylpropanolamine have high p<i>K</i><sub>a</sub> values but lower standard enthalpy than those of the
benchmark amine, monoethanolamine (MEA), and thus were deemed promising
for CO<sub>2</sub> capture technology. Monoethylethanolamine (MEEA)
was found to have the highest basicity (p<i>K</i><sub>a</sub>) with the lowest standard state enthalpy (Ī<i>H</i>Ā°/kJĀ·mol<sup>ā1</sup>)
Kinetics of the reaction of carbon dioxide (CO2 ) with cyclic amines using the stopped-flow technique
The Kinetic Effect of Adding Piperazine Activator to Aqueous Tertiary and Sterically-hindered Amines Using Stopped-flow Technique
CO<sub>2</sub> Capture Using Fluorinated Hydrophobic Solvents
Finding
more efficient gasāliquid scrubbing systems with
lower parasitic energy penalties is important for the future deployment
of carbon capture plants for large point source CO<sub>2</sub> emitters.
Minimization of the energy penalty using advanced solvents is one
way to reduce the energy penalty. Nonaqueous, hydrophobic solvents
are one type of solvent in which the physical properties of the solvent
combined with low heats of absorption and low loading at high temperature
even with high CO<sub>2</sub> pressure result in promising solvents
with low estimated reboiler heat duty. In this paper, a solvent composed
of a hydrophobic amine (2-fluorophenethylamine) combined with an acidic,
hydrophobic alcohol (octafluoropentanol) is studied mechanistically,
and the experimentally determined reaction products, heats of absorption,
and vapor liquid equilibria are reported. Approximating process models
are compared and indicate the potential to lower reboiler heat duty
in a commercial implementation
Challenges in Predicting Ī<sub>rxn</sub><i>G</i> in Solution: The Mechanism of Ether-Catalyzed Hydroboration of Alkenes
Ab
initio (coupled-cluster and density-functional) calculations
of Gibbs reaction energies in solution, with new entropy-of-solvation
damping terms, were performed for the ether-catalyzed hydroboration
of alkenes. The goal was to test the accuracy of continuum-solvation
models for reactions of neutral species in nonaqueous solvents, and
the hope was to achieve an accuracy sufficient to address the mechanism
in the āPasto caseā: B<sub>2</sub>H<sub>6</sub> + alkene
in THF solvent. Brownās S<sub>N</sub>2/S<sub>N</sub>1 ādissociativeā
mechanism, of S<sub>N</sub>2 formation of boraneāether adducts
followed by S<sub>N</sub>1 alkene attack, was at odds with Pastoās
original S<sub>N</sub>2/S<sub>N</sub>2 hypothesis, and while Brown
could prove his mechanism for a variety of cases, he could not perform
the experimental test with THF adducts in THF solvent, where the higher
THF concentrations might favor an S<sub>N</sub>2 second step. Two
diboranes were tested: B<sub>2</sub>H<sub>6</sub>, used by Pasto,
and (9BBN)<sub>2</sub> (9BBN = 9-borabicyclo[3.3.1]Ānonane, C<sub>8</sub>H<sub>15</sub>B), used by Brown. The new entropy terms resulted in
improved accuracy vs traditional techniques (ā¼2 kcal mol<sup>ā1</sup>), but this accuracy was not sufficient to resolve
the mechanism in the Pasto case