Review

Critical factors affecting the integration of biomass gasification and syngas fermentation technology

  • Received: 05 April 2016 Accepted: 15 May 2016 Published: 17 May 2016
  • Gasification-fermentation is a thermochemical-biological platform for the production of fuels and chemicals. Biomass is gasified at high temperatures to make syngas, a gas composed of CO, CO2, H2, N2 and other minor components. Syngas is then fed to anaerobic microorganisms that convert CO, CO2 and H2 to alcohols by fermentation. This platform offers numerous advantages such as flexibility of feedstock and syngas composition and lower operating temperature and pressure compared to other catalytic syngas conversion processes. In comparison to hydrolysis-fermentation, gasification-fermentation has a major advantage of utilizing all organic components of biomass, including lignin, to yield higher fuel production. Furthermore, syngas fermentation microorganisms do not require strict CO:H2:CO2 ratios, hence gas reforming is not required. However, several issues must be addressed for successful deployment of gasification-fermentation, particularly those that involve the integration of gasification and fermentation. Most previous reviews have focused only on either biomass gasification or syngas fermentation. In this review, the critical factors that affect the integration of biomass gasification with syngas fermentation, such as carbon conversion efficiency, effect of trace gaseous species, H2 to CO ratio requirements, and microbial preference of carbon substrate, are thoroughly discussed.

    Citation: Karthikeyan D. Ramachandriya, Dimple K. Kundiyana, Ashokkumar M. Sharma, Ajay Kumar, Hasan K. Atiyeh, Raymond L. Huhnke, Mark R. Wilkins. Critical factors affecting the integration of biomass gasification and syngas fermentation technology[J]. AIMS Bioengineering, 2016, 3(2): 188-210. doi: 10.3934/bioeng.2016.2.188

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  • Gasification-fermentation is a thermochemical-biological platform for the production of fuels and chemicals. Biomass is gasified at high temperatures to make syngas, a gas composed of CO, CO2, H2, N2 and other minor components. Syngas is then fed to anaerobic microorganisms that convert CO, CO2 and H2 to alcohols by fermentation. This platform offers numerous advantages such as flexibility of feedstock and syngas composition and lower operating temperature and pressure compared to other catalytic syngas conversion processes. In comparison to hydrolysis-fermentation, gasification-fermentation has a major advantage of utilizing all organic components of biomass, including lignin, to yield higher fuel production. Furthermore, syngas fermentation microorganisms do not require strict CO:H2:CO2 ratios, hence gas reforming is not required. However, several issues must be addressed for successful deployment of gasification-fermentation, particularly those that involve the integration of gasification and fermentation. Most previous reviews have focused only on either biomass gasification or syngas fermentation. In this review, the critical factors that affect the integration of biomass gasification with syngas fermentation, such as carbon conversion efficiency, effect of trace gaseous species, H2 to CO ratio requirements, and microbial preference of carbon substrate, are thoroughly discussed.


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    [1] El-Rub ZA, Bramer EA, Brem G (2004) Review of catalysts for tar elimination in biomass gasification processes. Ind Eng Chem Res 43: 6911–6919.
    [2] Huber GW, Iborra S, Corma A (2006) Synthesis of transportation fuels from biomass: Chemistry, catalysts, and engineering. Chem Rev 106: 4044–4098. doi: 10.1021/cr068360d
    [3] Kumar A, Jones DD, Hanna MA (2009) Thermochemical biomass gasification: A review of the current status of the technology. Energies 2: 556–581. doi: 10.3390/en20300556
    [4] Spath PL, Dayton DC (2003) Preliminary screening - Technical and economic assessment of synthesis gas to fuels and chemicals with emphasis on the potential for biomass-derived syngas. Golden: National Renewable Energy Laboratory pp. 142.
    [5] Berzin V, Kiriukhin M, Tyurin M (2012) Selective production of acetone during continuous synthesis gas fermentation by engineered biocatalyst Clostridium sp. MAceT113. Lett Appl Microbiol 55: 149–154. doi: 10.1111/j.1472-765X.2012.03272.x
    [6] Köpke M, Mihalcea C, Liew F, et al. (2011) 2,3-butanediol production by acetogenic bacteria, an alternative route to chemical synthesis, using industrial waste gas. Appl Environ Microbiol 77: 5467–5475. doi: 10.1128/AEM.00355-11
    [7] Liu K, Atiyeh HK, Tanner RS, et al. (2012) Fermentative production of ethanol from syngas using novel moderately alkaliphilic strains of Alkalibaculum bacchi. Bioresource Technol 102: 336–341.
    [8] Maddipati P, Atiyeh HK, Bellmer DD, et al. (2011) Ethanol production from syngas by Clostridium strain P11 using corn steep liquor as a nutrient replacement to yeast extract. Bioresource Technol 102: 6494–6501. doi: 10.1016/j.biortech.2011.03.047
    [9] Ramachandriya KD, Wilkins MR, Delorme MJM, et al. (2011) Reduction of acetone to isopropanol using producer gas fermenting microbes. Biotechnol Bioeng 108: 2330–2338. doi: 10.1002/bit.23203
    [10] Liu K, Atiyeh HK, Stevenson BS, et al. (2014) Mixed culture syngas fermentation and conversion of carboxylic acids into alcohols. Bioresource Technol 152: 337–346. doi: 10.1016/j.biortech.2013.11.015
    [11] Liu K, Atiyeh HK, Stevenson BS, et al. (2014) Continuous syngas fermentation for the production of ethanol, n-propanol and n-butanol. Bioresource Technol 151: 69–77. doi: 10.1016/j.biortech.2013.10.059
    [12] Heiskanen H, Virkajärvi I, Viikari L (2007) The effect of syngas composition on the growth and product formation of Butyribacterium methylotrophicum. Enzyme MicrobTech 41: 362–367. doi: 10.1016/j.enzmictec.2007.03.004
    [13] Bertsch J, Muller V (2015) Bioenergetic constraints for conversion of syngas to biofuels in acetogenic bacteria. Biotechnol Biofuels 8.
    [14] Phillips JR, Atiyeh HK, Tanner RS, et al. (2015) Butanol and hexanol production in Clostridium carboxidivorans syngas fermentation: Medium development and culture techniques. Bioresource Technol 190: 114–121. doi: 10.1016/j.biortech.2015.04.043
    [15] Wiselogel A, Tyson S, Johnson D (1996) Biomass feedstock resources and composition. In: Wyman CE, editor. Handbook on Bioethanol: Production and Utilization. Washington, DC: Taylor & Francis. 105–118.
    [16] Worden RM, Grethlein AJ, Jain MK, et al. (1991) Production of butanol and ethanol from synthesis gas via fermentation. Fuel 70: 615–619. doi: 10.1016/0016-2361(91)90175-A
    [17] Abubackar HN, Veiga MC, Kennes C (2011) Biological conversion of carbon monoxide: Rich syngas or waste gases to bioethanol. Biofuels, Bioprod Bior 5: 93–114. doi: 10.1002/bbb.256
    [18] Wilkins MR, Atiyeh HK (2011) Microbial production of ethanol from carbon monoxide. Curr Opin Biotech 22: 326–330. doi: 10.1016/j.copbio.2011.03.005
    [19] Drzyzga O, Revelles O, Durante-Rodríguez G, et al. (2015) New challenges for syngas fermentation: towards production of biopolymers. J Cheml Technol Biot 90: 1735–1751. doi: 10.1002/jctb.4721
    [20] Latif H, Zeidan AA, Nielsen AT, et al. (2014) Trash to treasure: production of biofuels and commodity chemicals via syngas fermenting microorganisms. Curr Opin Biotech 27: 79–87. doi: 10.1016/j.copbio.2013.12.001
    [21] Yasin M, Jeong Y, Park S, et al. (2015) Microbial synthesis gas utilization and ways to resolve kinetic and mass-transfer limitations. Bioresource Technol 177: 361–374. doi: 10.1016/j.biortech.2014.11.022
    [22] Daniell J, Köpke M, Simpson S (2012) Commercial biomass syngas fermentation. Energies 5: 5372–5417. doi: 10.3390/en5125372
    [23] Aghbashlo M, Tabatabaei M, Dadak A, et al. (2016) Exergy-based performance analysis of a continuous stirred bioreactor for ethanol and acetate fermentation from syngas via Wood–Ljungdahl pathway. Chem Eng Sci 143: 36–46. doi: 10.1016/j.ces.2015.12.013
    [24] Islam MA, Zengler K, Edwards EA, et al. (2015) Investigating Moorella thermoacetica metabolism with a genome-scale constraint-based metabolic model. Integr Biol. [In press].
    [25] Brown RC (2011) Thermochemical Processing of Biomass: Conversion into Fuels, Chemicals and Power. Hoboken, NJ, USA: John Wiley & Sons, Ltd.
    [26] Higman C, van der Burgt M (2003) Gasification. Burlington, MA, USA: Gulf Professional Publishing. pp. 412.
    [27] Sharma A, Kumar A, Patil K, et al. (2011) Performance evaluation of a lab-scale fluidized bed gasifier using switchgrass as feedstock. T ASABE 54: 2259–2266. doi: 10.13031/2013.40639
    [28] Li XT, Grace JR, Lim CJ, et al. (2004) Biomass gasification in a circulating fluidized bed. Biomass Bioenerg 26: 171–193. doi: 10.1016/S0961-9534(03)00084-9
    [29] Ciferno JP, Marano JJ (2002) Benchmarking biomass gasification technologies for fuels, chemicals and hydrogen production. US Department of Energy National Energy Technology Laboratory, Pittsburgh, PA, USA.
    [30] Ahmed A, Cateni B, Huhnke R, et al. (2006) Effects of biomass-generated producer gas constituents on cell growth, product distribution and hydrogenase activity of Clostridium carboxidivorans P7T. Biomass Bioenerg 30: 665–672. doi: 10.1016/j.biombioe.2006.01.007
    [31] Boerrigter H, Rauch R (2005) Syngas production and utilization. In: Knoef HAM, editor. Handbook of Biomass Gasification. Enschede, The Netherlands: Biomass Technology Group. pp. 211–230.
    [32] Dogru M, Midilli A, Howarth CR (2002) Gasification of sewage sludge using a throated downdraft gasifier and uncertainty analysis. Fuel Process Technol 75: 55–82. doi: 10.1016/S0378-3820(01)00234-X
    [33] Erlich C, Fransson TH (2011) Downdraft gasification of pellets made of wood, palm-oil residues respective bagasse: experimental study. Appl Energ 88: 899–908. doi: 10.1016/j.apenergy.2010.08.028
    [34] Kumabe K, Hanaoka T, Fujimoto S, et al. (2007) Co-gasification of woody biomass and coal with air and steam. Fuel 86: 684–689. doi: 10.1016/j.fuel.2006.08.026
    [35] Kumar A, Eskridge K, Jones DD, et al. (2009) Steam–air fluidized bed gasification of distillers grains: Effects of steam to biomass ratio, equivalence ratio and gasification temperature. Bioresource Technol 100: 2062–2068. doi: 10.1016/j.biortech.2008.10.011
    [36] Lv PM, Xiong ZH, Chang J, et al. (2004) An experimental study on biomass air–steam gasification in a fluidized bed. Bioresource Technol 95: 95–101. doi: 10.1016/j.biortech.2004.02.003
    [37] Ahmed A, Lewis RS (2007) Fermentation of biomass-generated synthesis gas: Effects of nitric oxide. Biotechnol Bioeng 97: 1080–1086. doi: 10.1002/bit.21305
    [38] Xu D, Tree DR, Lewis RS (2011) The effects of syngas impurities on syngas fermentation to liquid fuels. Biomass Bioenerg 35: 2690–2696. doi: 10.1016/j.biombioe.2011.03.005
    [39] Barik S, Prieto S, Harrison SB, et al. (1988) Biological production of alcohols from coal through indirect liquefaction. Appl Biochem Biotech 18: 363–378. doi: 10.1007/BF02930840
    [40] Datar RP, Shenkman RM, Cateni BG, et al. (2004) Fermentation of biomass-generated producer gas to ethanol. Biotechnol Bioeng 86: 587–594. doi: 10.1002/bit.20071
    [41] Ramachandriya K, Wilkins M, Patil K (2013) Influence of switchgrass generated producer gas pre-adaptation on growth and product distribution of Clostridium ragsdalei. Biotechnol Bioproce 18: 1201–1209. doi: 10.1007/s12257-013-0384-3
    [42] Vega J, Klasson K, Kimmel D, et al. (1990) Sulfur gas tolerance and toxicity of CO-utilizing and methanogenic bacteria. Appl Biochem Biotech 24: 329–340.
    [43] Xu D, Lewis RS (2012) Syngas fermentation to biofuels: effects of ammonia impurity in raw syngas on hydrogenase activity. Biomass Bioenerg 45: 303–310. doi: 10.1016/j.biombioe.2012.06.022
    [44] Ramachandriya KD (2009) Effect of biomass generated producer gas, methane and physical parameters on producer gas fermentations by Clostridium strain p11: Oklahoma State University. pp. 20.
    [45] Ensign SA, Hyman MR, Ludden PW (1989) Nickel-specific, slow-binding inhibition of carbon monoxide dehydrogenase from Rhodospirillum rubrum by cyanide. Biochemistry 28: 4973–4979. doi: 10.1021/bi00438a011
    [46] Grethlein AJ, Soni BK, Worden RM, et al. Influence of hydrogen sulfide on the growth and metabolism of butyribacterium methylotrophicum andclostridium acetobutylicum. Appl Biochem Biotech 34: 233–246.
    [47] Hyman MR, Ensign SA, Arp DJ, et al. (1989) Carbonyl sulfide inhibition of CO dehydrogenase from Rhodospirillum rubrum. Biochemistry 28: 6821–6826. doi: 10.1021/bi00443a007
    [48] Kundiyana DK, Huhnke RL, Wilkins MR (2010) Syngas fermentation in a 100-L pilot scale fermentor: Design and process considerations. J Biosci Bioeng 109: 492–498. doi: 10.1016/j.jbiosc.2009.10.022
    [49] Kusel K, Karnholz A, Trinkwalter T, et al. (2001) Physiological ecology of Clostridium glycolicum RD-1, an aerotolerant acetogen isolated from sea grass roots. Appl Environ Microbiol 67: 4734–4741. doi: 10.1128/AEM.67.10.4734-4741.2001
    [50] Pinto F, Franco C, Andre RN, et al. (2003) Effect of experimental conditions on co-gasification of coal, biomass and plastics wastes with air/steam mixtures in a fluidized bed system. Fuel 82: 1967–1976. doi: 10.1016/S0016-2361(03)00160-1
    [51] Shima S, Warkentin E, Thauer RK, et al. (2002) Structure and function of enzymes involved in the methanogenic pathway utilizing carbon dioxide and molecular hydrogen. J Biosci Bioeng 93: 519–530. doi: 10.1016/S1389-1723(02)80232-8
    [52] Sun JH, Hyman MR, Arp DJ (1992) Acetylene inhibition of Azotobacter vinelandii hydrogenase: Acetylene binds tightly to the large subunit. Biochemistry 31: 3158–3165. doi: 10.1021/bi00127a016
    [53] Kusel K, Pinkart HC, Drake HL, et al. (1999) Acetogenic and sulfate-reducing bacteria inhabiting the rhizoplane and deep cortex cells of the sea grass Halodule wrightii. Appl Environ Microbiol 65: 5117.
    [54] Sprott G, Jarrell K, Shaw K, et al. (1982) Acetylene as an inhibitor of methanogenic bacteria. J Gen Microbiol 128: 2453.
    [55] Schink B (1985) Fermentation of acetylene by an obligate anaerobe, Pelobacter acetylenicus sp. nov. Arch Microbiol 142: 295–301. doi: 10.1007/BF00693407
    [56] Schink B (1985) Inhibition of methanogenesis by ethylene and other unsaturated hydrocarbons. FEMS Microbiol Letters 31: 63–68. doi: 10.1111/j.1574-6968.1985.tb01132.x
    [57] Oremland RS, Taylor BF (1975) Inhibition of methanogenesis in marine sediments by acetylene and ethylene: Validity of the acetylene reduction assay for anaerobic microcosms. Appl Environ Microbiol 30: 707–709.
    [58] Rabou LPLM, Zwart RWR, Vreugdenhil BJ, et al. (2009) Tar in biomass producer gas, the Energy Research Centre of The Netherlands (ECN) experience: an enduring challenge. Energ Fuel 23: 6189–6198. doi: 10.1021/ef9007032
    [59] Cateni BG (2007) Effects of feed composition and gasification parameters on product gas from a pilot scale fluidized bed gasifier. Stillwater, Oklahoma: Oklahoma State University. pp. 384.
    [60] Caballero MA, Corella J, Aznar MP, et al. (2000) Biomass gasification with air in fluidized bed. Hot gas cleanup with selected commercial and full-size nickel-based catalysts. Ind Eng Chem Res 39: 1143–1154.
    [61] Abu El-Rub Z, Bramer EA, Brem G (2004) Review of catalysts for tar elimination in Biomass gasification processes. Ind Eng Chem Res 43: 6911–6919. doi: 10.1021/ie0498403
    [62] Bhandari PN, Kumar A, Bellmer DD, et al. (2014) Synthesis and evaluation of biochar-derived catalysts for removal of toluene (model tar) from biomass-generated producer gas. Renew Energ 66: 346–353. doi: 10.1016/j.renene.2013.12.017
    [63] Qian KZ, Kumar A (2015) Reforming of lignin-derived tars over char-based catalyst using Py-GC/MS. Fuel 162: 47–54. doi: 10.1016/j.fuel.2015.08.064
    [64] James AM, Yuan WQ, Boyette MD, et al. (2014) In-chamber thermocatalytic tar cracking and syngas reforming using char-supported NiO catalyst in an updraft biomass gasifier. Int J Agric Biol Eng 7: 91–97.
    [65] Paterson N, Zhuo Y, Dugwell DR, et al. (2001) Investigation of ammonia formation during gasification in an air-blown spouted bed:  Reactor design and initial tests. Energ Fuel 16: 127–135.
    [66] Burch R, Breen J, Meunier F (2002) A review of the selective reduction of NOx with hydrocarbons under lean-burn conditions with non-zeolitic oxide and platinum group metal catalysts. Appl Catal B-Environ 39: 283–303. doi: 10.1016/S0926-3373(02)00118-2
    [67] Jiang H, Wang H, Liang F, et al. (2009) Direct decomposition of nitrous oxide to nitrogen by in situ oxygen removal with a perovskite membrane. Angew Chem Int Edit 48: 2983–2986. doi: 10.1002/anie.200804582
    [68] Shelef M (1995) Selective catalytic reduction of NOx with N-free reductants. Chem Rev 95: 209–225. doi: 10.1021/cr00033a008
    [69] Qin X, Mohan T, El-Halwagi M, et al. (2006) Switchgrass as an alternate feedstock for power generation: an integrated environmental, energy and economic life-cycle assessment. Clean Technol Envir 8: 233–249. doi: 10.1007/s10098-006-0065-4
    [70] Simbeck DR, Dickenson RL, Oliver ED (1983) Coal-gasification systems: a guide to status, applications, and economics. Final report. EPRI-AP-3109 EPRI-AP-3109. Medium: X; Size: Pages: 408 p.
    [71] Smith K, Klasson K, Clausen A, et al. (1991) COS degradation by selected CO-utilizing bacteria. Appl Biochem Biotech 28: 787–796.
    [72] Hu P, Jacobsen LT, Horton JG, et al. (2010) Sulfide assessment in bioreactors with gas replacement. Biochem Eng J 49: 429–434. doi: 10.1016/j.bej.2010.02.006
    [73] Seefeldt LC, Arp DJ (1989) Oxygen Effects on the Nickel-Containing and Iron-Containing Hydrogenase from Azotobacter-Vinelandii. Biochemistry 28: 1588–1596. doi: 10.1021/bi00430a025
    [74] Drake H, Küsel K, Matthies C (2006) Acetogenic prokaryotes. In: Dworkin M, Falkow S, Rosenberg E et al., editors. The Prokaryotes. New York: Springer. pp. 354–420.
    [75] Karnholz A, Kusel K, Gossner A, et al. (2002) Tolerance and metabolic response of acetogenic bacteria toward oxygen. Appl Environ Microbiol 68: 1005–1009. doi: 10.1128/AEM.68.2.1005-1009.2002
    [76] Zhitnev YN, Tveritinova EA, Lunin VV (2008) Catalytic properties of a copper-carbon system formed by explosive decomposition of copper acetylide. Russ J Phys Chem A 82: 140–143. doi: 10.1134/S003602440801024X
    [77] Yan Q, Wan C, Street J, et al. (2013) Catalytic removal of oxygen from biomass-derived syngas. Bioresource Technol 147: 117–123. doi: 10.1016/j.biortech.2013.08.036
    [78] Phillips S, Aden A, Jechura J, et al. (2007) Thermochemical ethanol via indirect gasification and mixed alcohol synthesis of lignocellulosic biomass. Golden: National Renewable Energy Laboratory, Golden, CO, USA. pp.125.
    [79] Rajagopalan S, Datar RP, Lewis RS (2002) Formation of ethanol from carbon monoxide via a new microbial catalyst. Biomass Bioenerg 23: 487–493. doi: 10.1016/S0961-9534(02)00071-5
    [80] Phillips JR, Clausen EC, Gaddy JL (1994) Synthesis gas as substrate for the biological production of fuels and chemicals. Appl Micrbiol Biot 45/46: 145–157.
    [81] Gaddy J, Arora D, Ko C-W, et al. (2007) Methods for increasing the production of ethanol from microbial fermentation. US Patent No 7,285,402.
    [82] Speight JG (2005) Handbook of Coal Analysis. Hoboken, NJ, USA: Wiley.
    [83] Ragsdale SW, Wood HG (1991) Enzymology of the Acetyl-CoA Pathway of CO2 Fixation. Crit Rev Biochem Mol 26: 261–300. doi: 10.3109/10409239109114070
    [84] Thauer RK, Jungermann K, Decker K (1977) Energy conservation in chemotrophic anaerobic bacteria. Bacteriol Rev 41: 100–180.
    [85] Hurst KM, Lewis RS (2010) Carbon monoxide partial pressure effects on the metabolic process of syngas fermentation. Biochem Eng J 48: 159–165. doi: 10.1016/j.bej.2009.09.004
    [86] Orgill JJ, Atiyeh HK, Devarapalli M, et al. (2013) A comparison of mass transfer coefficients between trickle-bed, hollow fiber membrane and stirred tank reactors. Bioresource Technol 133: 340–346. doi: 10.1016/j.biortech.2013.01.124
    [87] Munasinghe PC, Khanal SK (2010) Syngas fermentation to biofuel: Evaluation of carbon monoxide mass transfer coefficient (kLa) in different reactor configurations. Biotechnol Progr 26: 1616–1621. doi: 10.1002/btpr.473
    [88] Munasinghe PC, Khanal SK (2012) Syngas fermentation to biofuel: Evaluation of carbon monoxide mass transfer and analytical modeling using a composite hollow fiber (CHF) membrane bioreactor. Bioresource Technol 122: 130–136. doi: 10.1016/j.biortech.2012.03.053
    [89] Shen Y, Brown R, Wen Z (2014) Syngas fermentation of Clostridium carboxidivorans P7 in a hollow fiber membrane biofilm reactor: Evaluating the mass transfer coefficient and ethanol production performance. Biochem Eng J 85: 21–29. doi: 10.1016/j.bej.2014.01.010
    [90] Devarapalli M, Atiyeh HK, Phillips JR, et al. (2016) Ethanol production during semi-continuous syngas fermentation in a trickle bed reactor using Clostridium ragsdalei. Bioresource Technol 209: 56–65. doi: 10.1016/j.biortech.2016.02.086
    [91] Datta R, Zeikus JG (1985) Modulation of acetone-butanol-ethanol fermentation by carbon monoxide and organic acids. Appl Environ Microb 49: 522–529.
    [92] Gaddy JL (2000) Biological production of products from waste gases with Clostridium ljundahlii. US Patent No 6,136,577.
    [93] Hu P, Bowen S, Lewis R (2011) A thermodynamic analysis of electron production during syngas fermentation. Bioresource Technol 102: 8071–7076. doi: 10.1016/j.biortech.2011.05.080
    [94] Vega JL, Holmberg VL, Clausen EC, et al. (1988) Fermentation parameters of Peptostreptococcus productus on gaseous substrates (CO, H2/CO2). Arch Microbiol 151: 65–70. doi: 10.1007/BF00444671
    [95] Ramachandriya KD, Kundiyana DK, Wilkins MR, et al. (2013) Carbon dioxide conversion to fuels and chemicals using a hybrid green process. Appl Energ 112: 289–299. doi: 10.1016/j.apenergy.2013.06.017
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