유준재 교수님 2팀 - 편집 역사

Uosche2528: /* 개발 과제 평가 */

2025-12-04T02:28:20Z

‎개발 과제 평가

Uosche2528: /* 참고문헌 */

2025-12-04T02:25:25Z

‎참고문헌

Uosche2528: /* 참고문헌 */

2025-12-04T02:23:39Z

‎참고문헌

Uosche2528: /* 개발 과제 관련 향후 전망 */

2025-12-04T02:23:20Z

‎개발 과제 관련 향후 전망

Uosche2528: /* 개발 과제 평가 */

2025-12-04T02:23:02Z

‎개발 과제 평가

Uosche2528: /* 개발 과제 평가 */

2025-12-04T02:21:29Z

‎개발 과제 평가

Uosche2528: /* 개발 과제 평가 */

2025-12-04T02:19:37Z

‎개발 과제 평가

Uosche2527: /* (1) Gasification Modeling */

2025-12-03T08:00:19Z

‎(1) Gasification Modeling

Uosche2527: /* 나. 논문조사 */

2025-12-03T07:59:55Z

‎나. 논문조사

Uosche2527: /* (1) Gasification Modeling */

2025-12-03T07:51:15Z

‎(1) Gasification Modeling

@@ 473번째 줄: / 473번째 줄: @@
 ==개발 과제 평가==
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 ==개발 과제 관련 향후 전망==

@@ 488번째 줄: / 488번째 줄: @@
 .	Fuchs, Constantin, Ulrich Arnold, and Jörg Sauer. "Synthesis of sustainable aviation fuels via (co–) oligomerization of light olefins." Fuel 382 (2025): 133680.
 .	Fuchs, Constantin, Ulrich Arnold, and Jörg Sauer. "(Co‐) Oligomerization of Olefins to Hydrocarbon Fuels: Influence of Feed Composition and Pressure." Chemie Ingenieur Technik 95.5 (2023): 651-657.
 .	Dubray, Florent J., Vladimir Paunovic, and Jeroen A. van Bokhoven. "Optimization of Sustainable Aviation Fuel Production through Experiment-Driven Modeling of Acid-Catalyzed Oligomerization." ACS Sustainable Chemistry & Engineering 12.48 (2024): 17590-17599.
 .	Xie, Ying, et al. "Pilot test and process modification of CO2 chemical absorption for top gas recycling-oxygen blast furnace." Separation and Purification Technology (2025): 133148.
 .	SPIETZ, Tomasz, et al. "Technological modifications in pilot research on CO.“
 .	Oh, Se-Young, Seokwon Yun, and Jin-Kuk Kim. "Process integration and design for maximizing energy efficiency of a coal-fired power plant integrated with amine-based CO2 capture process." Applied Energy 216 (2018): 311-322.
 .	Li, Tianci, et al. "Comparative desorption energy consumption of post-combustion CO2 capture integrated with mechanical vapor recompression technology." Separation and Purification Technology 294 (2022): 121202.
 .	Nyserda, “Process Development for Low-Moisture Content Wood Chips Final Report,” 2016.
 .	I. Energy Agency, “Towards hydrogen definitions based on their emissions intensity.” [Online]. Available: www.iea.org
 .	K. Sandeep and S. Dasappa, “Oxy-steam gasification of biomass for hydrogen rich syngas production using downdraft reactor configuration,” Int J Energy Res, vol. 38, no. 2, pp. 174–188, Feb. 2014, doi: 10.1002/er.3019.
 .	W. Doherty, A. Reynolds, D. Kennedy, W. Doherty, A. Reynolds, and D. Kennedy, “Aspen Plus Simulation of Biomass Gasification in a Steam Blown Aspen Plus Simulation of Biomass Gasification in a Steam Blown Dual Fluidised Bed Dual Fluidised Bed Recommended Citation Recommended Citation Aspen plus simulation of biomass gasification in a steam blown dual fluidised bed.” [Online]. Available: https://arrow.tudublin.ie/engmecbk
 .	M. Formica, S. Frigo, and R. Gabbrielli, “Development of a new steady state zero-dimensional simulation model for woody biomass gasification in a full scale plant,” Energy Convers Manag, vol. 120, pp. 358–369, Jul. 2016, doi: 10.1016/j.enconman.2016.05.009.
 .	World Bioenergy Association, “Gasification of Biomass,” Jun. 2015.
 .	“Analysis, Synthesis, and Design of Chemical Processes, Fifth Edition.”
 .	Prabir. Basu, Biomass gasification and pyrolysis : practical design and theory. Academic Press, 2010.
 .	S. Begum, M. G. Rasul, D. Akbar, and N. Ramzan, “Performance analysis of an integrated fixed bed gasifier model for different biomass feedstocks,” Energies (Basel), vol. 6, no. 12, pp. 6508–6524, Dec. 2013, doi: 10.3390/en6126508.
 .	N. Ranjan, N. Yadav, H. Singh, S. Kumar, and S. M. Mahajani, “Modelling and simulation of autothermal downdraft co-gasification of biomass and plastic wastes using Aspen Plus,” Energy Convers Manag, vol. 297, Dec. 2023, doi: 10.1016/j.enconman.2023.117714.
 .	M. Fernandez-Lopez, J. Pedroche, J. L. Valverde, and L. Sanchez-Silva, “Simulation of the gasification of animal wastes in a dual gasifier using Aspen Plus®,” Energy Convers Manag, vol. 140, pp. 211–217, 2017, doi: 10.1016/j.enconman.2017.03.008.
 .	R. M. Swanson, J. A. Satrio, R. C. Brown, A. Platon, and D. D. Hsu, “Techno-Economic Analysis of Biofuels Production Based on Gasification,” 2010. [Online]. Available: http://www.osti.gov/bridge
 .	P. Spath, A. Aden, T. Eggeman, M. Ringer, B. Wallace, and J. Jechura, “Biomass to Hydrogen Production Detailed Design and Economics Utilizing the Battelle Columbus Laboratory Indirectly-Heated Gasifier,” 2005. [Online]. Available: http://www.osti.gov/bridge
 .	K. R. Craig and M. K. Mann, “Cost and Performance Analysis of Biomass-Based Integrated Gasification Combined-Cycle (BIGCC) Power Systems.” [Online]. Available: http://www.doe.gov/bridge/home.html
 .	D. J. Stevens, “Hot Gas Conditioning: Recent Progress With Larger-Scale Biomass Gasification Systems; Update and Summary of Recent Progress,” 2001. [Online]. Available: http://www.doe.gov/bridge
 .	P. Mondal, G. S. Dang, and M. O. Garg, “Syngas production through gasification and cleanup for downstream applications - Recent developments,” 2011, Elsevier B.V. doi: 10.1016/j.fuproc.2011.03.021.
 .	P. Spath, A. Aden, T. Eggeman, M. Ringer, B. Wallace, and J. Jechura, “Biomass to Hydrogen Production Detailed Design and Economics Utilizing the Battelle Columbus Laboratory Indirectly-Heated Gasifier,” 2005. [Online]. Available: http://www.osti.gov/bridge
 .	U. Izquierdo et al., “Catalyst deactivation and regeneration processes in biogas tri-reforming process. The effect of hydrogen sulfide addition,” Catalysts, vol. 8, no. 1, Jan. 2018, doi: 10.3390/catal8010012.
 .	N. Inc and S. Francisco, “Equipment Design and Cost Estimation for Small Modular Biomass Systems, Synthesis Gas Cleanup, and Oxygen Separation Equipment; Task 2: Gas Cleanup Design and Cost Estimates -- Wood Feedstock,” 2006. [Online]. Available: http://www.osti.gov/bridge
 .	A. E. Martell, R. J. Motekaitis, D. Chen, R. D. Hancock, and D. Mcmanus, “Selection of new Fe(lll)/Fe(ll) chelating agents as catalysts for the oxidation of hydrogen sulfide to sulfur by air.”
 .		W. L. Luyben, “Capital cost of compressors for conceptual design,” Chemical Engineering and Processing - Process Intensification, vol. 126, pp. 206–209, Apr. 2018, doi: 10.1016/j.cep.2018.01.020.
 .	Xu, Jianguo, and Gilbert F. Froment. "Methane steam reforming, methanation and water‐gas shift: I. Intrinsic kinetics." AIChE journal 35.1 (1989): 88-96.
 .	D. F. Rodríguez Vallejo and A. De Klerk, “Improving the interface between Fischer-Tropsch synthesis and refining,” Energy and Fuels, vol. 27, no. 6, pp. 3137–3147, Jun. 2013, doi: 10.1021/ef400560z.
 .	Matzen, Michael, Mahdi Alhajji, and Yaşar Demirel. "Chemical storage of wind energy by renewable methanol production: Feasibility analysis using a multi-criteria decision matrix." Energy 93 (2015): 343-353.
 .	이웅, et al. "모노에탄올아민 (MEA)을 이용한 이산화탄소 포집공정: 배가스 분할 유입을 통한 흡수제 재생 에너지 절감 연구." 화학공학 49.6 (2011): 764-768.
 .	Hjelmaas, Silje, et al. "Results from MEA amine plant corrosion processes at the CO2 Technology Centre Mongstad." Energy Procedia 114 (2017): 1166-1178.
 .	Chemtech, Sulzer. "Structured packings for distillation, absorption and reactive distillation." Sulzer Chemtech Ltd, Winterthur (2010).
 .	Matzen, Michael, Mahdi Alhajji, and Yaşar Demirel. "Chemical storage of wind energy by renewable methanol production: Feasibility analysis using a multi-criteria decision matrix." Energy 93 (2015): 343-353.
 .	宋维端, et al. "KINETICS OF METHANOL SYNTHESIS IN THE PRESENCE OF C301 Cu-BASED CATALYST (Ⅰ) INTRINSIC AND GLOBAL KINETICS." 中国化学工程学报: 英文版 2 (1989): 248-257.
 .	Atsonios et al., Process analysis and comparative assessment of advanced thermochemical pathways for e-kerosene production, Energy, 2023.
 .	Dubray et al., Kinetic modeling of olefin oligomerization over solid acid catalysts, ACS Sustainable Chemistry & Engineering, 2024.
 .	P. P. Shah, G. C. Sturtevant, J. H. Gregor, M. Humbach, F. Padrta, and K. Steigleder, "Fischer-Tropsch Wax Characterization and Upgrading: Final Report," Jun. 1988.
 .	P. García-Bacaicoa, J. F. Mastral, J. Ceamanos, C. Berrueco, and S. Serrano, “Gasification of biomass/high density polyethylene mixtures in a downdraft gasifier,” Bioresour Technol, vol. 99, no. 13, pp. 5485–5491, Sep. 2008, doi: 10.1016/j.biortech.2007.11.003.
 .	“Levelised Cost of Hydrogen (LCOH) Calculator Manual,” 2024. [Online]. Available: https://observatory.clean-
 .	A. Aden et al., “• • • • • • Lignocellulosic Biomass to Ethanol Process Design and Economics Utilizing Co-Current Dilute Acid Prehydrolysis and Enzymatic Hydrolysis for Corn Stover,” 2002. [Online]. Available: http://www.osti.gov/bridge
 .	U.S. Bureau of Labor Statistics, “Occupational Employment and Wages, May 2022: 51-8091 Chemical Plant and System Operators,” U.S. Department of Labor.
 .	J. Lee et al., “Catholyte-free electroreduction of CO2for sustainable production of CO: concept, process development, techno-economic analysis, and CO2reduction assessment,” Green Chemistry, vol. 23, no. 6, pp. 2397–2410, Mar. 2021, doi: 10.1039/d0gc02969f.

← 이전 판		2025년 12월 4일 (목) 02:23 판
486번째 줄:		486번째 줄:

	==참고문헌==		==참고문헌==
		+
		+	1. Fuchs, Constantin, Ulrich Arnold, and Jörg Sauer. "Synthesis of sustainable aviation fuels via (co–) oligomerization of light olefins." Fuel 382 (2025): 133680.
		+	2. Fuchs, Constantin, Ulrich Arnold, and Jörg Sauer. "(Co‐) Oligomerization of Olefins to Hydrocarbon Fuels: Influence of Feed Composition and Pressure." Chemie Ingenieur Technik 95.5 (2023): 651-657.
		+	3. Dubray, Florent J., Vladimir Paunovic, and Jeroen A. van Bokhoven. "Optimization of Sustainable Aviation Fuel Production through Experiment-Driven Modeling of Acid-Catalyzed Oligomerization." ACS Sustainable Chemistry & Engineering 12.48 (2024): 17590-17599.
		+	4. Xie, Ying, et al. "Pilot test and process modification of CO2 chemical absorption for top gas recycling-oxygen blast furnace." Separation and Purification Technology (2025): 133148.
		+	5. SPIETZ, Tomasz, et al. "Technological modifications in pilot research on CO.“
		+	6. Oh, Se-Young, Seokwon Yun, and Jin-Kuk Kim. "Process integration and design for maximizing energy efficiency of a coal-fired power plant integrated with amine-based CO2 capture process." Applied Energy 216 (2018): 311-322.
		+	7. Li, Tianci, et al. "Comparative desorption energy consumption of post-combustion CO2 capture integrated with mechanical vapor recompression technology." Separation and Purification Technology 294 (2022): 121202.
		+	8. Nyserda, “Process Development for Low-Moisture Content Wood Chips Final Report,” 2016.
		+	9. I. Energy Agency, “Towards hydrogen definitions based on their emissions intensity.” [Online]. Available: www.iea.org
		+	10. K. Sandeep and S. Dasappa, “Oxy-steam gasification of biomass for hydrogen rich syngas production using downdraft reactor configuration,” Int J Energy Res, vol. 38, no. 2, pp. 174–188, Feb. 2014, doi: 10.1002/er.3019.
		+	11. W. Doherty, A. Reynolds, D. Kennedy, W. Doherty, A. Reynolds, and D. Kennedy, “Aspen Plus Simulation of Biomass Gasification in a Steam Blown Aspen Plus Simulation of Biomass Gasification in a Steam Blown Dual Fluidised Bed Dual Fluidised Bed Recommended Citation Recommended Citation Aspen plus simulation of biomass gasification in a steam blown dual fluidised bed.” [Online]. Available: https://arrow.tudublin.ie/engmecbk
		+	12. M. Formica, S. Frigo, and R. Gabbrielli, “Development of a new steady state zero-dimensional simulation model for woody biomass gasification in a full scale plant,” Energy Convers Manag, vol. 120, pp. 358–369, Jul. 2016, doi: 10.1016/j.enconman.2016.05.009.
		+	13. World Bioenergy Association, “Gasification of Biomass,” Jun. 2015.
		+	14. “Analysis, Synthesis, and Design of Chemical Processes, Fifth Edition.”
		+	15. Prabir. Basu, Biomass gasification and pyrolysis : practical design and theory. Academic Press, 2010.
		+	16. S. Begum, M. G. Rasul, D. Akbar, and N. Ramzan, “Performance analysis of an integrated fixed bed gasifier model for different biomass feedstocks,” Energies (Basel), vol. 6, no. 12, pp. 6508–6524, Dec. 2013, doi: 10.3390/en6126508.
		+	17. N. Ranjan, N. Yadav, H. Singh, S. Kumar, and S. M. Mahajani, “Modelling and simulation of autothermal downdraft co-gasification of biomass and plastic wastes using Aspen Plus,” Energy Convers Manag, vol. 297, Dec. 2023, doi: 10.1016/j.enconman.2023.117714.
		+	18. M. Fernandez-Lopez, J. Pedroche, J. L. Valverde, and L. Sanchez-Silva, “Simulation of the gasification of animal wastes in a dual gasifier using Aspen Plus®,” Energy Convers Manag, vol. 140, pp. 211–217, 2017, doi: 10.1016/j.enconman.2017.03.008.
		+	19. R. M. Swanson, J. A. Satrio, R. C. Brown, A. Platon, and D. D. Hsu, “Techno-Economic Analysis of Biofuels Production Based on Gasification,” 2010. [Online]. Available: http://www.osti.gov/bridge
		+	20. P. Spath, A. Aden, T. Eggeman, M. Ringer, B. Wallace, and J. Jechura, “Biomass to Hydrogen Production Detailed Design and Economics Utilizing the Battelle Columbus Laboratory Indirectly-Heated Gasifier,” 2005. [Online]. Available: http://www.osti.gov/bridge
		+	21. K. R. Craig and M. K. Mann, “Cost and Performance Analysis of Biomass-Based Integrated Gasification Combined-Cycle (BIGCC) Power Systems.” [Online]. Available: http://www.doe.gov/bridge/home.html
		+	22. D. J. Stevens, “Hot Gas Conditioning: Recent Progress With Larger-Scale Biomass Gasification Systems; Update and Summary of Recent Progress,” 2001. [Online]. Available: http://www.doe.gov/bridge
		+	23. P. Mondal, G. S. Dang, and M. O. Garg, “Syngas production through gasification and cleanup for downstream applications - Recent developments,” 2011, Elsevier B.V. doi: 10.1016/j.fuproc.2011.03.021.
		+	24. P. Spath, A. Aden, T. Eggeman, M. Ringer, B. Wallace, and J. Jechura, “Biomass to Hydrogen Production Detailed Design and Economics Utilizing the Battelle Columbus Laboratory Indirectly-Heated Gasifier,” 2005. [Online]. Available: http://www.osti.gov/bridge
		+	25. U. Izquierdo et al., “Catalyst deactivation and regeneration processes in biogas tri-reforming process. The effect of hydrogen sulfide addition,” Catalysts, vol. 8, no. 1, Jan. 2018, doi: 10.3390/catal8010012.
		+	26. N. Inc and S. Francisco, “Equipment Design and Cost Estimation for Small Modular Biomass Systems, Synthesis Gas Cleanup, and Oxygen Separation Equipment; Task 2: Gas Cleanup Design and Cost Estimates -- Wood Feedstock,” 2006. [Online]. Available: http://www.osti.gov/bridge
		+	27. A. E. Martell, R. J. Motekaitis, D. Chen, R. D. Hancock, and D. Mcmanus, “Selection of new Fe(lll)/Fe(ll) chelating agents as catalysts for the oxidation of hydrogen sulfide to sulfur by air.”
		+	28. W. L. Luyben, “Capital cost of compressors for conceptual design,” Chemical Engineering and Processing - Process Intensification, vol. 126, pp. 206–209, Apr. 2018, doi: 10.1016/j.cep.2018.01.020.
		+	29. Xu, Jianguo, and Gilbert F. Froment. "Methane steam reforming, methanation and water‐gas shift: I. Intrinsic kinetics." AIChE journal 35.1 (1989): 88-96.
		+	30. D. F. Rodríguez Vallejo and A. De Klerk, “Improving the interface between Fischer-Tropsch synthesis and refining,” Energy and Fuels, vol. 27, no. 6, pp. 3137–3147, Jun. 2013, doi: 10.1021/ef400560z.
		+	31. Matzen, Michael, Mahdi Alhajji, and Yaşar Demirel. "Chemical storage of wind energy by renewable methanol production: Feasibility analysis using a multi-criteria decision matrix." Energy 93 (2015): 343-353.
		+	32. 이웅, et al. "모노에탄올아민 (MEA)을 이용한 이산화탄소 포집공정: 배가스 분할 유입을 통한 흡수제 재생 에너지 절감 연구." 화학공학 49.6 (2011): 764-768.
		+	33. Hjelmaas, Silje, et al. "Results from MEA amine plant corrosion processes at the CO2 Technology Centre Mongstad." Energy Procedia 114 (2017): 1166-1178.
		+	34. Chemtech, Sulzer. "Structured packings for distillation, absorption and reactive distillation." Sulzer Chemtech Ltd, Winterthur (2010).
		+	35. Matzen, Michael, Mahdi Alhajji, and Yaşar Demirel. "Chemical storage of wind energy by renewable methanol production: Feasibility analysis using a multi-criteria decision matrix." Energy 93 (2015): 343-353.
		+	36. 宋维端, et al. "KINETICS OF METHANOL SYNTHESIS IN THE PRESENCE OF C301 Cu-BASED CATALYST (Ⅰ) INTRINSIC AND GLOBAL KINETICS." 中国化学工程学报: 英文版 2 (1989): 248-257.
		+	37. Atsonios et al., Process analysis and comparative assessment of advanced thermochemical pathways for e-kerosene production, Energy, 2023.
		+	38. Dubray et al., Kinetic modeling of olefin oligomerization over solid acid catalysts, ACS Sustainable Chemistry & Engineering, 2024.
		+	39. P. P. Shah, G. C. Sturtevant, J. H. Gregor, M. Humbach, F. Padrta, and K. Steigleder, "Fischer-Tropsch Wax Characterization and Upgrading: Final Report," Jun. 1988.
		+	40. P. García-Bacaicoa, J. F. Mastral, J. Ceamanos, C. Berrueco, and S. Serrano, “Gasification of biomass/high density polyethylene mixtures in a downdraft gasifier,” Bioresour Technol, vol. 99, no. 13, pp. 5485–5491, Sep. 2008, doi: 10.1016/j.biortech.2007.11.003.
		+	41. “Levelised Cost of Hydrogen (LCOH) Calculator Manual,” 2024. [Online]. Available: https://observatory.clean-
		+	42. A. Aden et al., “• • • • • • Lignocellulosic Biomass to Ethanol Process Design and Economics Utilizing Co-Current Dilute Acid Prehydrolysis and Enzymatic Hydrolysis for Corn Stover,” 2002. [Online]. Available: http://www.osti.gov/bridge
		+	43. U.S. Bureau of Labor Statistics, “Occupational Employment and Wages, May 2022: 51-8091 Chemical Plant and System Operators,” U.S. Department of Labor.
		+	44. J. Lee et al., “Catholyte-free electroreduction of CO2for sustainable production of CO: concept, process development, techno-economic analysis, and CO2reduction assessment,” Green Chemistry, vol. 23, no. 6, pp. 2397–2410, Mar. 2021, doi: 10.1039/d0gc02969f.

@@ 476번째 줄: / 476번째 줄: @@
 ==개발 과제 관련 향후 전망==
-내용
 ==참고문헌==

@@ 473번째 줄: / 473번째 줄: @@
 ==개발 과제 평가==
-[[파일:Last2.png]]
+[[파일:Last3.png]]
 ==개발 과제 관련 향후 전망==

← 이전 판		2025년 12월 3일 (수) 08:00 판
227번째 줄:		227번째 줄:
	Fixed-bed gasifier에서는 균일한 충전층을 유지하기 위해 feedstock이 덩어리 형태 또는 chip 형태여야 하며, 대형 입자는 기체 흐름의 불균일이나 막힘을 방지하기 위해 피해야 한다 [13]. wood는 chip 형태로 공급되어 추가 전처리가 필요 없으나 [8], waste-HDPE는 병 형태로 공급되기 때문에 fixed-bed gasifier의 feedstock 요건을 충족하기 위해 전처리 과정을 거쳐야 한다 [9]. 따라서 waste-HDPE는 해머 밀을 사용해 작은 조각으로 파쇄한 후 pelletizer (입자화 장치)를 통해 균일한 크기의 입자로 가공하여 fixed-bed gasifier 내에서 안정적인 기체 흐름을 확보한다 [14].		Fixed-bed gasifier에서는 균일한 충전층을 유지하기 위해 feedstock이 덩어리 형태 또는 chip 형태여야 하며, 대형 입자는 기체 흐름의 불균일이나 막힘을 방지하기 위해 피해야 한다 [13]. wood는 chip 형태로 공급되어 추가 전처리가 필요 없으나 [8], waste-HDPE는 병 형태로 공급되기 때문에 fixed-bed gasifier의 feedstock 요건을 충족하기 위해 전처리 과정을 거쳐야 한다 [9]. 따라서 waste-HDPE는 해머 밀을 사용해 작은 조각으로 파쇄한 후 pelletizer (입자화 장치)를 통해 균일한 크기의 입자로 가공하여 fixed-bed gasifier 내에서 안정적인 기체 흐름을 확보한다 [14].

−	[[파일:5-3.png\|frame\|가운데\|Fig 12. Schematic diagram of a downdraft gasifier [15].]]	+	[[파일:A-2.png\|frame\|가운데\|Fig 12. Schematic diagram of a downdraft gasifier [15].]]

@@ 126번째 줄: / 126번째 줄: @@
 ◇ Mechanical Vapor Recompression (MVR): Comparative desorption energy consumption of post-combustion CO2 capture integrated with mechanical vapor recompression technology.[7]
-[[파일:2-8.png|frame|가운데|Figure 8. Flowsheet of Lean Vapor Recompression]]
+[[파일:A-1.png|frame|가운데|Figure 8. Flowsheet of Lean Vapor Recompression]]
 Mechanical Vapor Recompression이란 stripper로부터 들어오는 혹은 나오는 고온의 solvent를 flash 후 compress해서 새로운 열원으로 쓰는 개념이다. 이는 기존 reboiler에서 사용되는 steam의 양을 줄일 수 있고, reboiler energy 또한 줄어들게 된다. Figure 8은 lean solvent를 flash 한 후, flashed vapor를 compress해서 stripper에 주입해 새로운 열원으로 쓰이는 공정을 나타낸다.

@@ 211번째 줄: / 211번째 줄: @@
 ====(1)	 Gasification Modeling====
-[[파일:0-1.png|frame|가운데|Figure 11 Process flow diagram of Gasification Process]]
+[[파일:0-1.png|frame|가운데|Figure 11. Process flow diagram of Gasification Process]]
 Gasification의 원료는 wood chip과 waste-HDPE를 사용한다. Wood chip은 40 × 40 × 50 mm 크기로 공급되며, waste-HDPE는 병 형태로 제공되어 가스화기에 투입하기 전 전처리가 필요하다 [8], [9]. Aspen Plus에서는 이들 원료를 proximate analysis과 ultimate analysis을 사용하여 다음과 같이 non-conventional 타입으로 모델링 한다.