{"title":"以生物质为原料的两种乙酰丙酸生产工艺的生命周期温室气体排放和经济可行性:日本和加拿大案例研究","authors":"","doi":"10.1016/j.cesys.2024.100222","DOIUrl":null,"url":null,"abstract":"<div><p>We evaluated CO<sub>2</sub> equivalent (CO<sub>2</sub>eq) greenhouse gas (GHG) emissions and minimum selling price of levulinic acid (LA) produced in two biomass-waste-based processes: the AlCl<sub>3</sub>/choline chloride (ChCl) process, and the formic acid (FA) process, with catalysts recycling. Six scenarios were synthesized to compare the performances of the two processes in Japan and Canada. In the AlCl<sub>3</sub>/ChCl process, the total GHG emission was 11.35–11.56 kg-CO<sub>2</sub>eq/kg-LA and those from the energy input to the pretreatment and ChCl production were 5.22 and 3.90 kg-CO<sub>2</sub>eq/kg-LA, respectively. In the FA process, the total GHG emission was 9.46–9.68 and 22.29–22.51 kg-CO<sub>2</sub>eq/kg-LA for 60 wt% and 80 wt% FA, respectively. The operational emissions for makeup FA input were 7.65 and 20.80 kg-CO<sub>2</sub>eq/kg-LA (60 wt% and 80 wt%, respectively), which accounted for more than 80% in all scenarios. The optimization of the product purge volume, FA concentration in the pretreatment, and FA production using biomass and/or renewable energy are critical parameters to reduce overall environmental impacts of the processes. The liquid content of the solid residue (moisture, water soluble organic matters, and catalyst) had insignificant influences on the GHG emission and minimum selling price. In the FA process, combustion of solid residue can compensate the GHG emissions from the reaction and separation units.</p></div>","PeriodicalId":34616,"journal":{"name":"Cleaner Environmental Systems","volume":null,"pages":null},"PeriodicalIF":6.1000,"publicationDate":"2024-09-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S2666789424000606/pdfft?md5=479e258e72ca322ea8144f5c2d307e3a&pid=1-s2.0-S2666789424000606-main.pdf","citationCount":"0","resultStr":"{\"title\":\"Life cycle GHG emissions and economic viability of two levulinic acid production processes from biomass: A case study of Japan and Canada\",\"authors\":\"\",\"doi\":\"10.1016/j.cesys.2024.100222\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>We evaluated CO<sub>2</sub> equivalent (CO<sub>2</sub>eq) greenhouse gas (GHG) emissions and minimum selling price of levulinic acid (LA) produced in two biomass-waste-based processes: the AlCl<sub>3</sub>/choline chloride (ChCl) process, and the formic acid (FA) process, with catalysts recycling. Six scenarios were synthesized to compare the performances of the two processes in Japan and Canada. In the AlCl<sub>3</sub>/ChCl process, the total GHG emission was 11.35–11.56 kg-CO<sub>2</sub>eq/kg-LA and those from the energy input to the pretreatment and ChCl production were 5.22 and 3.90 kg-CO<sub>2</sub>eq/kg-LA, respectively. In the FA process, the total GHG emission was 9.46–9.68 and 22.29–22.51 kg-CO<sub>2</sub>eq/kg-LA for 60 wt% and 80 wt% FA, respectively. The operational emissions for makeup FA input were 7.65 and 20.80 kg-CO<sub>2</sub>eq/kg-LA (60 wt% and 80 wt%, respectively), which accounted for more than 80% in all scenarios. The optimization of the product purge volume, FA concentration in the pretreatment, and FA production using biomass and/or renewable energy are critical parameters to reduce overall environmental impacts of the processes. The liquid content of the solid residue (moisture, water soluble organic matters, and catalyst) had insignificant influences on the GHG emission and minimum selling price. In the FA process, combustion of solid residue can compensate the GHG emissions from the reaction and separation units.</p></div>\",\"PeriodicalId\":34616,\"journal\":{\"name\":\"Cleaner Environmental Systems\",\"volume\":null,\"pages\":null},\"PeriodicalIF\":6.1000,\"publicationDate\":\"2024-09-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://www.sciencedirect.com/science/article/pii/S2666789424000606/pdfft?md5=479e258e72ca322ea8144f5c2d307e3a&pid=1-s2.0-S2666789424000606-main.pdf\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Cleaner Environmental Systems\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2666789424000606\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, ENVIRONMENTAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Cleaner Environmental Systems","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2666789424000606","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, ENVIRONMENTAL","Score":null,"Total":0}
引用次数: 0
摘要
我们评估了两种基于生物质废弃物的工艺:氯化铝/氯化胆碱(ChCl)工艺和甲酸(FA)工艺生产的乙酰丙酸(LA)的二氧化碳当量(CO2eq)温室气体(GHG)排放量和最低销售价格,其中甲酸(FA)工艺的催化剂可回收利用。为了比较这两种工艺在日本和加拿大的性能,我们合成了六种方案。在 AlCl3/ChCl 工艺中,温室气体总排放量为 11.35-11.56 kg-CO2eq/kg-LA,预处理和 ChCl 生产的能源输入排放量分别为 5.22 和 3.90 kg-CO2eq/kg-LA。在 FA 过程中,60 wt% 和 80 wt% FA 的温室气体排放总量分别为 9.46-9.68 和 22.29-22.51 kg-CO2eq/kg-LA。合成 FA 输入的运行排放量分别为 7.65 和 20.80 kg-CO2eq/kg-LA(60 wt% 和 80 wt%),在所有方案中均占 80% 以上。优化产品净化量、预处理中的 FA 浓度以及使用生物质和/或可再生能源生产 FA 是减少工艺对环境总体影响的关键参数。固体残留物的液体含量(水分、水溶性有机物和催化剂)对温室气体排放和最低销售价格的影响不大。在 FA 工艺中,固体残渣的燃烧可以补偿反应和分离单元的温室气体排放。
Life cycle GHG emissions and economic viability of two levulinic acid production processes from biomass: A case study of Japan and Canada
We evaluated CO2 equivalent (CO2eq) greenhouse gas (GHG) emissions and minimum selling price of levulinic acid (LA) produced in two biomass-waste-based processes: the AlCl3/choline chloride (ChCl) process, and the formic acid (FA) process, with catalysts recycling. Six scenarios were synthesized to compare the performances of the two processes in Japan and Canada. In the AlCl3/ChCl process, the total GHG emission was 11.35–11.56 kg-CO2eq/kg-LA and those from the energy input to the pretreatment and ChCl production were 5.22 and 3.90 kg-CO2eq/kg-LA, respectively. In the FA process, the total GHG emission was 9.46–9.68 and 22.29–22.51 kg-CO2eq/kg-LA for 60 wt% and 80 wt% FA, respectively. The operational emissions for makeup FA input were 7.65 and 20.80 kg-CO2eq/kg-LA (60 wt% and 80 wt%, respectively), which accounted for more than 80% in all scenarios. The optimization of the product purge volume, FA concentration in the pretreatment, and FA production using biomass and/or renewable energy are critical parameters to reduce overall environmental impacts of the processes. The liquid content of the solid residue (moisture, water soluble organic matters, and catalyst) had insignificant influences on the GHG emission and minimum selling price. In the FA process, combustion of solid residue can compensate the GHG emissions from the reaction and separation units.