Chemistry and Industry of Forest Products ›› 2022, Vol. 42 ›› Issue (4): 119-130.doi: 10.3969/j.issn.0253-2417.2022.04.017
Fang WANG1, Hongdan ZHANG2,*()
Received:
2021-09-07
Online:
2022-08-28
Published:
2022-09-01
Contact:
Hongdan ZHANG
E-mail:hdzhang@scau.edu.cn
CLC Number:
Fang WANG, Hongdan ZHANG. Application of Aspen Plus in Lignocellulosic Biomass Pretreatment for Ethanol Production: A Review[J]. Chemistry and Industry of Forest Products, 2022, 42(4): 119-130.
Table 1
The Comparison of different pretreatment methods"
预处理方法 pretreatment method | 活化物质 active agent | 作用机制 mode of action |
稀酸 dilute acid | H2SO4、H3PO4和其他强酸 H2SO4, H3PO4 and other strong acids | 水解半纤维素 hydrolysis of hemicelluloses |
碱 alkali | NaOH、Ca(OH)2、Na2CO3等碱性物质 NaOH, Ca(OH)2, Na2CO3 and similar alkaline compounds | 提取木质素 extraction of lignin |
蒸汽爆破 steam explosion | 高温蒸汽(加入少量催化剂) high-temperature steam, catalyst may be added | 水解半纤维素并分离纤维 hydrolysis of hemicelluloses, fibre separation |
高温热水 liquid hot water | 水解离出的H+ H+ from H2O | 水解半纤维素 hydrolysis of hemicelluloses |
微波 microwave | 催化剂 catalysts | 水解半纤维素 hydrolysis of hemicelluloses |
亚临界CO2 subcritical CO2 | 碳酸 carbonic acid | 水解半纤维素并分离纤维 hydrolysis of hemicelluloses, fibre separation |
离子液体 ionic liquids | 有机阳离子和无机阴离子 organic cation and inorganic anion | 组分分离 fractionation of polymers |
低共熔溶剂 deep-eutectic solvents | 路易斯和布朗斯特酸和碱的混合物 mixtures of Lewis and Bronsted acids and bases | 组分分离 fractionation of polymers |
有机溶剂 organosolv | 乙醇、丁醇等有机溶剂 organic solvents, e.g. ethanol, butanol | 提取木质素 extraction of lignin |
研磨/粉碎 milling/grinding | 缩小尺寸 particle size reduction | 增加比表面积、提高可及度 surface increase and improved access |
生物 biological | 降解原料 degradation of the material | 褐腐菌降解半纤维素和纤维素、白腐菌降解木质素、软腐菌降解纤维素 brown-rot degrades hemicelluloses and cellulose, white-rot degrades lignin, soft-rot degrades cellulose |
Table 2
Key economic results for investigated furfural and ethanol biorefineries from lignocellulose at 2018 cost year of analysis[59]"
方案 scenario | 设备总投资/百万美元 total cost of investment /million US$ | 总生产成本/(百万美元/年) total cost of production /(million US$/a) | 糠醛得率/% furfural yield | 乙醇得率/% ethanol yield | 内部收益率/% internal rate of return(IRR) |
1 | 272 | 13.70 | 59.50 | — | 12.92 |
2 | 294 | 18.12 | — | 95.69 | 10.18 |
3 | 327 | 18.37 | 13.68 | 63.79 | 3.64 |
4 | 306 | 18.17 | 31.14 | 74.71 | 7.19 |
5 | 305 | 18.57 | 68.73 | 53.51 | 12.78 |
6 | 305 | 18.17 | 29.00 | 77.30 | 8.64 |
7 | 322 | 18.89 | 50.47 | 17.02 | 10.54 |
Table 3
Techno-economic assessment of different pretreatment methods[60]"
预处理方式 pretreatment | 设备投资/亿元 equipment investment/ ×108 yuan | 总投资费用/亿元 total capital investment/ ×108 yuan | 总运营成本/(亿元/年) total variable operating costs/(×108 yuan/a) | 乙醇生产成本/ (元/升) the costs of ethanol/(yuan/L) | 最低乙醇出厂价格/(元/升) minimum ethanol selling price(MESP)/(yuan/L) |
稀酸dilute acid | 15.74 | 28.47 | 5.43 | 2.59 | 4.32 |
氨纤维爆破 ammonia fiber expansion | 15.82 | 28.56 | 5.26 | 2.74 | 4.62 |
液态热水 liquid hot water | 16.07 | 29.02 | 5.00 | 2.64 | 4.59 |
Table 4
Summary of the scenarios evaluated, process features, mass and energy balances[64]"
参数 parameter | 方案1 case 1 | 方案2 case 2 | 方案3 case 3 | 方案4 case 4 | 方案5 case 5 | 方案6 case 6 |
操作单元顺序 unit operation sequence | D-N-E | D-N-E | D-N-E | N-E-D | N-E-D | N-E-D |
溶剂补充源 solvent make-up source | 回收柱侧流 side stream from recycling column | 发酵醪蒸馏塔产物 beer column product | 精馏塔产物 rectifying column product | 回收柱侧流 side stream from recycling column | 发酵醪蒸馏塔产物 beer column product | 精馏塔产物 rectifying column product |
乙醇产量/(kg·h-1) ethanol production | 23 822 | 24 047 | 24 063 | 24 412 | 24 559 | 24 685 |
溶剂回收率/% solvent recovery | 98.26 | 98.30 | 98.31 | 98.71 | 98.74 | 98.62 |
发酵后乙醇质量分数/% ethanol mass fraction after ferm. | 11.47 | 11.29 | 11.25 | 11.13 | 11.25 | 10.65 |
水消耗量/(kg·h-1) water consumption | 182 021 | 180 253 | 184 663 | 191 652 | 195 053 | 206 465 |
总能量消耗/kW total power consumption | 521.4 | 521.5 | 521.4 | 524.4 | 528.3 | 525.6 |
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