Swapan K Ray, Riyadh H Bhuiyan, Tanvir Muslim and M Q Ehsan*,
{"title":"Development of a Material-Driven Phase III Lignocellulosic Feedstock Biorefinery System","authors":"Swapan K Ray, Riyadh H Bhuiyan, Tanvir Muslim and M Q Ehsan*, ","doi":"10.1021/acssusresmgt.4c0016810.1021/acssusresmgt.4c00168","DOIUrl":null,"url":null,"abstract":"<p >The present status of operational biorefineries confronts an array of technological and economic hurdles, encompassing challenges related to product diversification, environmental impacts, and efficient waste management. In this study, a highly streamlined and techno-economically viable material-driven phase III lignocellulosic feedstock biorefinery system is delineated, aiming to sequentially extract non-structural and structural components from diverse lignocellulosic biomass and pretreatment chemicals such as nitrogen-, potassium-, and phosphorus- (NPK) containing materials. To construct the biorefinery system, a thermo-pressurized sequential phosphoric acid-potassium hydroxide pretreatment method was employed on extractives-free lignocellulosic biomass, effectively fractionating numerous non-wood and hardwood samples into their structural components. Applying the pretreatment process, the primary structural components, i.e., hemicellulose (77 to 98%), cellulose/pulp (77 to 93%), and lignin (75 to 85%), were separated. The pretreatment chemicals were also recovered (around 100%) as valuable NPK fertilizers in crystalline and liquid forms from the spent liquors by using ammonium hydroxide. A techno-economic analysis was performed on the biorefinery system (small-scale plant; lignocellulosic biomass used: 7300 t/y; production capacity: 19,568 t/y; estimated capital cost: 31.00 million USD; operating cost: 23.48 million USD) by developing a deterministic model that showed a payback period of 6.69 years. Local sensitivity and uncertainty analyses were also performed using the deterministic model, and changes in the return on investment were evaluated. Additionally, a superstructure was developed for the biorefinery, showing potential downstream operations. Overall studies, including cradle-to-gate lifecycle assessment, demonstrated that the biorefinery is a green and sustainable technology for the conversion of lignocellulosic biomass with greater than 95% atom economy.</p>","PeriodicalId":100015,"journal":{"name":"ACS Sustainable Resource Management","volume":"1 9","pages":"1994–2013 1994–2013"},"PeriodicalIF":0.0000,"publicationDate":"2024-09-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"ACS Sustainable Resource Management","FirstCategoryId":"1085","ListUrlMain":"https://pubs.acs.org/doi/10.1021/acssusresmgt.4c00168","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
The present status of operational biorefineries confronts an array of technological and economic hurdles, encompassing challenges related to product diversification, environmental impacts, and efficient waste management. In this study, a highly streamlined and techno-economically viable material-driven phase III lignocellulosic feedstock biorefinery system is delineated, aiming to sequentially extract non-structural and structural components from diverse lignocellulosic biomass and pretreatment chemicals such as nitrogen-, potassium-, and phosphorus- (NPK) containing materials. To construct the biorefinery system, a thermo-pressurized sequential phosphoric acid-potassium hydroxide pretreatment method was employed on extractives-free lignocellulosic biomass, effectively fractionating numerous non-wood and hardwood samples into their structural components. Applying the pretreatment process, the primary structural components, i.e., hemicellulose (77 to 98%), cellulose/pulp (77 to 93%), and lignin (75 to 85%), were separated. The pretreatment chemicals were also recovered (around 100%) as valuable NPK fertilizers in crystalline and liquid forms from the spent liquors by using ammonium hydroxide. A techno-economic analysis was performed on the biorefinery system (small-scale plant; lignocellulosic biomass used: 7300 t/y; production capacity: 19,568 t/y; estimated capital cost: 31.00 million USD; operating cost: 23.48 million USD) by developing a deterministic model that showed a payback period of 6.69 years. Local sensitivity and uncertainty analyses were also performed using the deterministic model, and changes in the return on investment were evaluated. Additionally, a superstructure was developed for the biorefinery, showing potential downstream operations. Overall studies, including cradle-to-gate lifecycle assessment, demonstrated that the biorefinery is a green and sustainable technology for the conversion of lignocellulosic biomass with greater than 95% atom economy.