3 research outputs found
Tetraethylenepentamine-Modified Activated Semicoke for CO<sub>2</sub> Capture from Flue Gas
To separate CO<sub>2</sub> from coal-fired power plant emissions,
semicoke, which is cheap and easy to obtain, was further activated
to use as the carrier and tetraethylenepentamine (TEPA) was impregnated
in the activated semicoke to prepare solid amine sorbents. The effects
of activating agents, adsorption temperature, and the presence of
water on CO<sub>2</sub> sorption were investigated in a fixed-bed
reactor, and the regenerability and adsorption kinetics for prepared
sorbents were also studied. The equilibrium adsorption capacity for
N<sub>2</sub>-activated semicoke (SE-N<sub>2</sub>) was 2.70 and 2.14
mmol/g at 20 °C when water was absent and present, respectively,
and the equilibrium adsorption capacity for 10 wt % TEPA-modified
N<sub>2</sub>-activated semicoke (SE-N<sub>2</sub>-TEPA10%) was 3.24
and 3.58 mmol/g at 60 °C when water was absent and present, respectively.
After 10 cyclic regenerations, the adsorption capacity for SE-N<sub>2</sub>-TEPA10% reduced by 7.7% under dry conditions, and SE-N<sub>2</sub>-TEPA10% showed good regenerability
Development of Low-Cost Porous Carbons through Alkali Activation of Crop Waste for CO<sub>2</sub> Capture
To achieve the “double carbon” (carbon
peak and carbon
neutrality) target, low-cost CO2 capture at large CO2 emission points is of great importance, during which the
development of low-cost CO2 sorbents will play a key role.
Here, we chose peanut shells (P) from crop waste as the raw material
and KOH and K2CO3 as activators to prepare porous
carbons by a simple one-step activation method. Interestingly, the
porous carbon showed a good adsorption capacity of 2.41 mmol/g for
15% CO2 when the mass ratio of K2CO3 to P and the activation time were only 0.5 and 0.5 h, respectively,
and the adsorption capacity remained at 98.76% after 10 adsorption–desorption
cycle regenerations. The characterization results suggested that the
activated peanut shell-based porous carbons were mainly microporous
and partly mesoporous, and hydroxyl (O–H), ether (C–O),
and pyrrolic nitrogen (N-5) functional groups that promoted CO2 adsorption were formed during activation. In conclusion,
KOH- and K2CO3-activated P, especially K2CO3-activated P, showed good CO2 adsorption
and regeneration performance. In addition, not only the use of a small
amount of the activator but also the raw material of crop waste reduces
the sorbent preparation costs and CO2 capture costs
Enhanced CO<sub>2</sub> Adsorption Capacity and Hydrothermal Stability of HKUST‑1 via Introduction of Siliceous Mesocellular Foams (MCFs)
New
hierarchical composites containing micropores and mesopores
were synthesized by assembling HKUST-1 (Cu<sub>3</sub>(BTC)<sub>2</sub>) on siliceous mesocellular foams (MCFs). The structure, morphology,
and textural properties of as-prepared composites were characterized
by X-ray diffraction, scanning electron microscopy, thermogravimetric
analysis, and N<sub>2</sub> sorption isotherms, respectively. The
results suggest that the coexistence of mesoporous silicas promotes
the formation of nanosized MOFs, and the mesostructures of silicas
are not destroyed by MOFs. Moreover, the micropore/mesopore volume
ratio can be controlled by varying the amounts of MOFs. The CO<sub>2</sub> adsorption capacities were calculated by breakthrough curves,
which were tested in a fixed bed. The CO<sub>2</sub> adsorption capacity
of the composites reaches 1.40 mmol/g, which is higher than that of
bulk HKUST-1. The structure and CO<sub>2</sub> adsorption capacity
of the composites after the hydrothermal treatment also have been
evaluated. The results show that composite-2 has a larger CO<sub>2</sub> adsorption capacity of 1.68 mmol/g after steam conditioning and
that the structure of HKUST-1 in the composites remain stable