• Title/Summary/Keyword: carbon dioxide adsorption

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Adsorption Measurement of Thin Film Using a Quartz Crystal Resonator (수정진동자를 이용한 박막의 흡착 측정)

  • Kim, Byoung Chul;Park, Jung Woo;Kim, Young Han
    • Korean Chemical Engineering Research
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    • v.48 no.3
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    • pp.405-408
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    • 2010
  • A technique to measure the adsorption characteristic of surface area and pore size of a ceramic thin film is proposed, and its performance is examine. The thin film is fabricated directly on the resonator surface to measure the adsorption capacity of the film as it is, and using carbon dioxide makes the measurement easy. The results indicates that the measured surface area is satisfactory, while the pore size has some error. It is suggested that readily available carbon dioxide can be used to determine adsorption capacity of thin film at room temperature.

Enhanced Carbon Dioxide Adsorption on Post-Synthetically Modified Metal-Organic Frameworks

  • Ko, Na-Keun;Kim, Ja-Heon
    • Bulletin of the Korean Chemical Society
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    • v.32 no.8
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    • pp.2705-2710
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    • 2011
  • Four MOFs functionalized with 1-Me, 1-Pr, 1-Ph, and 1-$PhCF_3$ were prepared through post-synthetic modifications of a metal-organic framework (MOF), UMCM-1-$NH_2$ (1) with acetic, butyric, benzoic, and 4-(trifluoromethyl)benzoic anhydrides, respectively. Methane adsorption measurements between 253 and 298 K at pressures up to 1 bar indicated that both 1-Ph and 1-$PhCF_3$ adsorbed more $CH_4$ than the parent MOF, 1. All the functionalized MOFs adsorbed more $CO_2$ than 1 under conditions similar to the $CH_4$ test. The introduction of functional groups promoted adsorption of both $CH_4$ and $CO_2$ despite significantly reducing Brunauer-Emmet-Teller (BET) surface area: 4170 (1), 3550 (1-Me), 2900 (1-Pr), 3680 (1-Ph), and 3520 $m^2/g$ (1-$PhCF_3$). Electron-withdrawing aromatic groups (1-Ph, 1-$PhCF_3$) more effectively enhanced $CO_2$ adsorption than electron-donating alkyl groups (1-Me, 1-Pr). In particular, 1-Ph adsorbed 23% more $CO_2$ at 298 K and 50% more at 253 K than 1.

Preparation of Activated Carbon from Wastepaper and Adsorption of Endocrine Disrupting Chemicals

  • Okayama, Takayuki;Matsushita, Kiyofumi;Sasuzuki, Hiroma;Shimada, Masahiro
    • Proceedings of the Korea Technical Association of the Pulp and Paper Industry Conference
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    • 2006.06b
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    • pp.279-284
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    • 2006
  • Activated carbon is proposed as a new application of wastepaper recycling other than the paper-making. Waste kraft bag is considered to be a suitable raw material for activated carbon because of its low ash content. Small pellets of wastepaper squeezed out from the continuous kneader were carbonized in a nitrogen atmosphere and activated using carbon dioxide. The BET specific surface areas of activated carbon prepared from waste kraft bag was $1,285m^{2}/g$, which is higher than commercially available activated carbons. The activated carbon prepared from wastepaper has a well-developed porous structure, particularly in mesopore and macropore ranges. As a result, activated carbon with iodine adsorption capacity of 1,400 mg/g was obtained from waste kraft bag. In this paper, adsorption amount of Bisphenol A (BPA) was determined to investigate adsorbability of activated carbon from waste kraft bag. Adsorption measurements were on solutions ranging from $0.1{mu}g/L\;to\;100mg/L$. The activated carbon from waste kraft bag gave higher BPA adsorbabilities over a wide range, compared with commercially available activated carbons.

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Regeneration Characteristics of Adsorbent Loaded with VOCs using Supercritical Carbon Dioxide (휘발성 유기용제가 흡착된 흡착제의 초임계 이산화탄소를 이용한 재생특성)

  • Lee, Seung Bum;Seong, Dae Hyung;Hong, In Kwon
    • Applied Chemistry for Engineering
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    • v.8 no.5
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    • pp.737-741
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    • 1997
  • The typical removal method of volatile organic compounds is adsorption process. In this study, granular activated carbon and activated carbon fiber were used as adsorbents, and the adsorption behavior for the two types of adsorbent was compared. And they were regenerated by supercritical carbon dioxide extraction at a constant temperature, 318.15 K, and 2000, 2500, 3000 psi respectively. The desorption percentage of initial adsorbates and iodine values were increased with pressure of supercritical carbon dioxide. The regeneration time was 70 and 60 minutes in adsorbents loaded with methyl ethyl ketone(MEK) and benzene, respectively. The desorption percentages were 64.0% for granular activated carbon and 55.3% for activated carbon fiber loaded with MEK, and 59.1% for granular activated carbon and 45.2% for activated carbon fiber loaded with benzene. The exit concentration could be evaluated by Tan and Liou model. Therefore, the granular activated carbon and the activated carbon fiber could be regenerated by supercritical fluid extraction process.

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Sorption Analysis of Carbon Dioxide onto Cesium Carbonate (세슘카보네이트에서 이산화탄소의 수착반응)

  • Son, Young-Sik;Kim, Seong-Soo;park, Sang-Wook
    • Korean Chemical Engineering Research
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    • v.47 no.3
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    • pp.373-379
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    • 2009
  • Cesium carbonate was used as an adsorbent to capture carbon dioxide from gaseous stream of carbon dioxide, nitrogen, and moisture in a fixed-bed to obtain the breakthrough data of $CO_2$. The deactivation model in the non-catalytic heterogeneous reaction systems is used to analyze the sorption kinetics among carbon dioxide, carbonate, and moisture using the experimental breakthrough data. The experimental breakthrough data are fitted very well to the deactivation model than the adsorption isotherm models in the literature.

A Study on the Estimation of Carbon Dioxide Generation During High Purity Hydrogen Production According to Natural Gas Composition (천연가스 조성에 따른 수소 생산 시에 발생하는 이산화탄소 배출량 산출에 대한 연구)

  • CHO, JUNGHO;NOH, JAEHYUN;KIM, DONG SUN
    • Transactions of the Korean hydrogen and new energy society
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    • v.30 no.6
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    • pp.485-489
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    • 2019
  • Hydrogen is known to be a clean fuel which does not generate a green house gas during the combustion. However, about 8 kg of carbon dioxide is generated during the course of producing 1 kg of hydrogen through reforming, water gas shift reaction and pressure swing adsorption in order to obtain a high purity hydrogen over 99.999% by volume. In this work, carbon dioxide generation is estimated according to four kinds of natural gas compositions supplied by Korea Gas Corporation and regarding natural gas as pure methane. For the simulation of the modeling, PRO/II with PROVISION V10.2 at AVEVA was utilized and Peng-Robinson equation of state with Twu's alpha function was selected.

Morphological study of porous aromatic schiff bases as a highly effective carbon dioxide storages

  • Rehab Hammoda;Naser Shaalan;Mohammed H. Al-Mashhadani;Dina S. Ahmed;Rahimi M. Yusop;Ali H. Jawad;Emad Yousif
    • Analytical Science and Technology
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    • v.36 no.5
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    • pp.236-249
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    • 2023
  • Carbon dioxide (CO2) capture and storage is a critical issue for mitigating climate change. Porous aromatic Schiff base complexes have emerged as a promising class of materials for CO2 capture due to their high surface area, porosity, and stability. In this study, we investigate the potential of Schiff base complexes as an effective media for CO2 storage. We review the synthesis and characterization of porous aromatic Schiff bases materials complexes and examine their CO2 sorption properties. We find that Schiff base complexes exhibit high CO2 adsorption capacity and selectivity, making them a promising candidate for use in carbon capture applications. Moreover, we investigate the effect of various parameters such as temperature, and pressure on the CO2 adsorption properties of Schiff base complexes. The Schiff bases possessed tiny Brunauer-Emmett-Teller surface areas (4.7-19.4 m2/g), typical pore diameters of 12.8-29.43 nm, and pore volumes ranging from 0.02-0.073 cm3/g. Overall, our results suggest that synthesized complexes have great potential as an effective media for CO2 storage, which could significantly reduce greenhouse gas emissions and contribute to mitigating climate change. The study provides valuable insights into the design of novel materials for CO2 capture and storage, which is a critical area of research for achieving a sustainable future.

CaO Manufacture for $CO_2$ Adsorption at a High Temperature (고온에서의 이산화탄소 흡착을 위한 흡착제 CaO 제조)

  • Lee Tae-Jong;Kim Gil-Soo;Baek Il-Hyun;Kim Bu-Ung
    • Journal of the Korean Institute of Gas
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    • v.5 no.4 s.16
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    • pp.27-32
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    • 2001
  • It is desired that carbon dioxide causing a greenhouse effect be removed at a high temperature and high pressure in a steam reforming reaction. In this research, a pellet form of adsorbent CaO is employed to capture $CO_2$. The adsorbent was manufactured using a high pressure molding on powdered $CaCO_3$ followed by calcination. Then its properties were analyzed and the adsorption experiments were carried out in a batch adsorption chamber. The pore area was found to be dependent on a molding pressure and the pore distribution showed two peaks. It is examined that $CO_2$ binds to CaO by means of chemisorption and its maximum conversion is nearly $80\%$ at $700^{\circ}C$.

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Sequential adsorption - photocatalytic oxidation process for wastewater treatment using a composite material TiO2/activated carbon

  • Andriantsiferana, Caroline;Mohamed, Elham Farouk;Delmas, Henri
    • Environmental Engineering Research
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    • v.20 no.2
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    • pp.181-189
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    • 2015
  • A composite material was tested to eliminate phenol in aqueous solution combining adsorption on activated carbon and photocatalysis with $TiO_2$ in two different ways. A first implementation involved a sequential process with a loop reactor. The aim was to reuse this material as adsorbent several times with in situ photocatalytic regeneration. This process alternated a step of adsorption in the dark and a step of photocatalytic oxidation under UV irradiation with or without $H_2O_2$. Without $H_2O_2$, the composite material was poorly regenerated due to the accumulation of phenol and intermediates in the solution and on $TiO_2$ particles. In presence of $H_2O_2$, the regeneration of the composite material was clearly enhanced. After five consecutive adsorption runs, the amount of eliminated phenol was twice the maximum adsorption capacity. The phenol degradation could be described by a pseudo first-order kinetic model where constants were much higher with $H_2O_2$ (about tenfold) due to additional ${\bullet}OH$ radicals. The second implementation was in a continuous process as with a fixed bed reactor where adsorption and photocatalysis occurred simultaneously. The results were promising as a steady state was reached indicating stabilized behavior for both adsorption and photocatalysis.

Adsorption and Oxidation Reaction Rate of $SO_2$ in Slurries of Activated Carbon (활성탄 슬러리를 이용한 $SO_2$ 가스의 흡착 및 산화반응 속도)

  • 최용택;신창섭;이태희
    • Journal of Korean Society for Atmospheric Environment
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    • v.3 no.1
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    • pp.41-46
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    • 1987
  • Adsorption and reaction studies were made for the catalytic oxidation in aqueous slurries of activated carbon at room temperature and atmospheric pressure. In order to analyze the reaction rate, the mechanism was assumed by the steps of nonhomogeneous catalytic reaction. The experimental result show that oxidation rate was controlled by the reaction between adsorbed molecular oxygen and sulfur dioxide on the catalyst surface. Ar room temperature, the equat5ion of reaction rate was given as $ro_2 = 2.49 \times 10^{-7} P_O_2^{0.604}$.

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