• Korean Chemical Engineering Research
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• v.55 no.3
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• pp.419-425
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• 2017

In this study, the performance characteristics of the K-based sorbents (KEP-CO2P2, KEPCO RI, Korea) has been studied in relation with the heat exchanger structure and shape in a mixing zone of the carbonator in the bench-scale dry $CO_2$ capture process. Two types of heat exchangers (different structure and shape) were used in the carbonator as CASE 1 and CASE 2, in which the experiment has been continuously performed under the same operating conditions. During the continuous operation, working temperature of carbonator was 75 to $80^{\circ}C$, that of regenerator was 190 to $200^{\circ}C$, and $CO_2$ inlet concentration of the feed gas was 12 to 14 vol%. Especially, to compare the dynamic sorption capacity of sorbents, the differential pressure of the mixing zone in the carbonator was maintained around 400 to 500 mm $H_2O$. Also, solid samples from the carbonator and the regenerator were collected and weight variation of those samples was evaluated by TGA. The $CO_2$ removal efficiency and the dynamic sorption capacity were 64.3% and 2.40 wt%, respectively for CASE 1 while they were 81.0% and 4.66 wt%, respectively for CASE 2. Also, the dynamic sorption capacity of the sorbent in CASE 1 and CASE 2 was 2.51 wt% and 4.89 wt%, respectively, based on the weight loss of the TGA measurement results. Therefore, It was concluded that there could be a difference in the performance characteristics of the same sorbents according to the structure and type of heat exchanger inserted in the carbonator under the same operating conditions.

• Journal of Hydrogen and New Energy
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• v.27 no.1
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• pp.83-94
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• 2016

Performance of absorbent for post-combustion $CO_2$ capture was measured and discussed. Fully saturated fresh absorbent (P2-15F) and absorbents sampled from absorption and regeneration reactor of continuous $CO_2$ capture process, P2-15A, P2-15R, respectively, were used as representative absorbents. Small scale fluidized bed reactor (0.05 m I.D., 0.8 m high) which can measure exhaust gas concentration and weight change simultaneously was used to analyze regeneration characteristics for those absorbents. Exhausted moles of $CO_2$ and $H_2O$ were measured with increasing temperature. $H_2O/CO$ ratio and working capacity were determined and discussed to confirm reason of reactivity decay after continuous operation. Moreover, possibility of side reaction was checked based on the $H_2O/CO_2$ mole ratio. Finally, suitable regeneration temperature range was confirmed based on the trend of working capacity with temperature.

• Polymer(Korea)
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• v.38 no.5
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• pp.676-681
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• 2014

Licorice, widely used as a herbal medicine, has flavonoids such as liquiritin and its aglycone, liquiritigenin that show anti-oxidant and anti-inflammatory properties. Licorice flavonoid-loaded cellulose hydrogels were prepared as carriers for skin drug delivery, and their properties were investigated. The porous cellulose hydrogel was made by reacting cellulose with epichlorohydrin as a cross-linking agent in NaOH/urea(1~10%) solutions. Through studies on the rheological properties and water uptake of the hydrogel, a NaOH/urea(6%) solution was established as being optimum for the synthesis of the cellulose hydrogel containing liquiritin and liquiritigenin. Scanning electron microscopy (SEM) observations of a cross-section of the prepared hydrogel indicated its porosity. In particular, in skin permeation experiments using a Franz diffusion cell, hydrogel containing the licorice flavonoids showed remarkable transdermal permeation compared to the control group. These results indicate that porous cellulose hydrogel is a potential drug delivery system to enhance the skin permeation of licorice flavonoids.