• 제목/요약/키워드: Bio-char catalyst

검색결과 4건 처리시간 0.019초

Development of Carbon-Based Solid Acid Catalysts Using a Lipid-Extracted Alga, Dunaliella tertiolecta, for Esterification

  • Ryu, Young-Jin;Kim, Z-Hun;Lee, Seul Gi;Yang, Ji-Hyun;Shin, Hee-Yong;Lee, Choul-Gyun
    • Journal of Microbiology and Biotechnology
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    • 제28권5호
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    • pp.732-738
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    • 2018
  • Novel carbon-based solid acid catalysts were synthesized through a sustainable route from lipid-extracted microalgal residue of Dunaliella tertiolecta, for biodiesel production. Two carbon-based solid acid catalysts were prepared by surface modification of bio-char with sulfuric acid ($H_2SO_4$) and sulfuryl chloride ($SO_2Cl_2$), respectively. The treated catalysts were characterized and their catalytic activities were evaluated by esterification of oleic acid. The esterification catalytic activity of the $SO_2Cl_2$-treated bio-char was higher ($11.5mmol\;Prod.{\cdot}h^{-1}{\cdot}gCat.\;^{-1}$) than that of commercial catalyst silica-supported Nafion SAC-13 ($2.3mmol\;Prod.{\cdot}h^{-1}{\cdot}gCat.^{-1}$) and $H_2SO_4$-treated bio-char ($5.7mmol\;Prod.{\cdot}h^{-1}{\cdot}gCat.^{-1}$). Reusability of the catalysts was examined. The catalytic activity of the $SO_2Cl_2$-modified catalyst was sustained from the second run after the initial activity dropped after the first run and kept the same activity until the fifth run. It was higher than that of first-used Nafion. These experimental results demonstrate that catalysts from lipid-extracted algae have great potential for the economic and environment-friendly production of biodiesel.

제올라이트 촉매 열분해를 이용한 볏짚으로부터 바이오 오일 생산 (Bio-oil Production from Rice Straw by the Catalytic Pyrolysis over Zeolites)

  • 최종철;류지혜;강보성;김주식;전종기;박영권
    • Korean Chemical Engineering Research
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    • 제44권4호
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    • pp.382-386
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    • 2006
  • 볏짚은 국내에서 유용한 재생 가능한 바이오매스이다. 유동층과 char 분리 장치가 구비된 벤치 규모 급속 열분해 장치와 제올라이트 촉매를 이용하여 볏짚으로부터 바이오 오일의 생산에 대한 실험을 수행하였다. 본 연구는 제올라이트 촉매의 첨가에 따른 볏짚의 열분해 생성물의 분포와 바이오 오일의 화학적 구성을 알아보기 위한 것이다. 볏짚의 촉매 열분해 결과 무촉매 열분해에 비해 기체, char 성분은 증가하고 액체 성분은 감소하였다. 또한, 오일 중 수분이 탈산소의 영향으로 증대된 결과를 가져왔다. 촉매 열분해의 경우 오일 성분 중의 aromatics 성분이 증대되었고 발열량이 증가하였다.

Hydrodeoxygenation of Spent Coffee Bio-oil from Fast Pyrolysis using HZSM-5 and Dolomite Catalysts

  • Park, Jeong Woo;Ly, Hoang Vu;Linh, Le Manh;Tran, Quoc Khanh;Kim, Seung-Soo;Kim, Jinsoo
    • 청정기술
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    • 제25권2호
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    • pp.168-176
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    • 2019
  • Spent coffee is one of biomass sources to be converted into bio-oil. However, the bio-oil should be further upgraded to achieve a higher quality bio-oil because of its high oxygen content. Deoxygenation under hydrotreating using different catalysts (catalytic hydrodeoxygenation; HDO) is considered as one of the promising methods for upgrading bio-oil from pyrolysis by removal of O-containing groups. In this study, the HDO of spent coffee bio-oil, which was collected from fast pyrolysis of spent coffee ($460^{\circ}C$, $2.0{\times}U_{mf}$), was carried out in an autoclave. The product yields were 72.16 ~ 96.76 wt% of bio-oil, 0 ~ 18.59 wt% of char, and 3.24 ~ 9.25 wt% of gas obtained in 30 min at temperatures between $250^{\circ}C$ and $350^{\circ}C$ and pressure in the range of 3 to 9 bar. The highest yield of bio-oil of 97.13% was achieved at $250^{\circ}C$ and 3 bar, with high selectivity of D-Allose. The carbon number distribution of the bio-oil was analyzed based on the concept of simulated distillation. The $C_{12}{\sim}C_{14}$ fraction increased from 22.98 wt% to 27.30 wt%, whereas the $C_{19}{\sim}C_{26}$ fraction decreased from 24.74 wt% to 17.18 wt% with increasing reaction time. Bio-oil yields were slightly decreased when the HZSM-5 catalyst and dolomite were used. The selectivity of CO was increased at the HZSM-5 catalyst and decreased at the dolomite.

2단계 촉매 분해공정을 이용한 리그닌 유래 선택적 페놀화합물 생산 (Selective Production of Monomeric Phenols from Lignin via Two-step Catalytic Cracking Process)

  • 김재영;허수정;박신영;최인규;최준원
    • Journal of the Korean Wood Science and Technology
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    • 제45권3호
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    • pp.278-287
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    • 2017
  • 본 연구에서는 2단계 촉매 분해공정 시스템을 이용하여 효과적으로 리그닌을 분해하였으며 리그닌 분해산물로 액상의 리그닌 오일, 촤, 가스가 생성되었다. 1차 촉매 분해공정에서는 MgO, CaO, Pt/C 촉매를 사용하였으며 Pt/C 촉매를 사용했을 때 가장 높은 리그닌 오일 수율(76.2 wt%) 및 가장 낮은 촤 수율(4.1 wt%)을 얻을 수 있었다. 리그닌 오일의 GC-MS/FID 분석을 통해 guaiacol, 4-ethylphenol, 4-methylguaiacol, 4-ethylguaiacol, syringol 등 18종류의 페놀화합물을 검출하였으며 Pt/C 조건에서 생산된 페놀화합물 수율이 97.8 mg/g lignin로 가장 높았다. 한편 MgO와 CaO에서 생산된 페놀화합물은 촉매에 흡착되어 상대적으로 낮은 수율을 보였다. Pt/C 조건에서 생산된 리그닌 오일을 다공성 구조를 가지는 Pd/activated carbon aerogel 촉매 하에서 추가 분해하였다. 2차 촉매 분해공정을 통해 상대적으로 선택성이 높은 4가지 페놀화합물(4-ethylguaiacol, 4-propylguaiacol, 4-ethylsyringol, 4-propylsyringol)을 0.89 - 1.82 wt% 수준으로 생산하였다.