Youxiao Xu , Guangfei Qu , Zhoupeng Yan , Huanhuan Wu , Ping Ning
{"title":"金属氧化物-熔盐催化热解:提高小麦秸秆的能量转化效率","authors":"Youxiao Xu , Guangfei Qu , Zhoupeng Yan , Huanhuan Wu , Ping Ning","doi":"10.1016/j.psep.2024.10.118","DOIUrl":null,"url":null,"abstract":"<div><div>This study systematically investigates the pyrolysis process of wheat straw in a ternary carbonate molten salt system (Li₂CO₃-Na₂CO₃-K₂CO₃) with the addition of different metal oxides (CaO, Al₂O₃, Fe₂O₃, TiO₂). The effects of the ratio of molten salt, type of metal oxide, and pyrolysis temperature on the pyrolysis products were examined. As the temperature increased, in the MS15 (wheat straw: molten salt = 1:15) system, the yield of gas-phase products rose from 21.21 wt% to 82.57 wt%, while the yields of solid products and bio-oil rapidly decreased to 23.76 wt% and 37.60 wt%, respectively. Additionally, the system exhibited the highest lower heating value (LHV) within the temperature range of 450–750 ℃. Therefore, the optimal ratio of wheat straw to carbonate molten salt is 1:15. Furthermore, when adding four metal oxides (Al₂O₃, CaO, Fe₂O₃, TiO₂) to the MS15 system, it was found that the addition of CaO (CaO-MS15) resulted in the highest LHV across all pyrolysis temperatures. Notably, at 550 ℃, the maximum LHV was 21.89 MJ/Nm³, an increase of 5 MJ/Nm³ compared to MS15. Analysis of the solid phase using XRD, XPS, and SEM indicated that the active sites on the surface of CaO facilitated the cleavage and deoxygenation of bio-oil on the biochar during the pyrolysis process, breaking it down into small molecular gases.</div></div>","PeriodicalId":20743,"journal":{"name":"Process Safety and Environmental Protection","volume":"192 ","pages":"Pages 1051-1061"},"PeriodicalIF":6.9000,"publicationDate":"2024-10-31","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Metal oxide-molten salt catalyzed pyrolysis: Improving the energy conversion efficiency of wheat straw\",\"authors\":\"Youxiao Xu , Guangfei Qu , Zhoupeng Yan , Huanhuan Wu , Ping Ning\",\"doi\":\"10.1016/j.psep.2024.10.118\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>This study systematically investigates the pyrolysis process of wheat straw in a ternary carbonate molten salt system (Li₂CO₃-Na₂CO₃-K₂CO₃) with the addition of different metal oxides (CaO, Al₂O₃, Fe₂O₃, TiO₂). The effects of the ratio of molten salt, type of metal oxide, and pyrolysis temperature on the pyrolysis products were examined. As the temperature increased, in the MS15 (wheat straw: molten salt = 1:15) system, the yield of gas-phase products rose from 21.21 wt% to 82.57 wt%, while the yields of solid products and bio-oil rapidly decreased to 23.76 wt% and 37.60 wt%, respectively. Additionally, the system exhibited the highest lower heating value (LHV) within the temperature range of 450–750 ℃. Therefore, the optimal ratio of wheat straw to carbonate molten salt is 1:15. Furthermore, when adding four metal oxides (Al₂O₃, CaO, Fe₂O₃, TiO₂) to the MS15 system, it was found that the addition of CaO (CaO-MS15) resulted in the highest LHV across all pyrolysis temperatures. Notably, at 550 ℃, the maximum LHV was 21.89 MJ/Nm³, an increase of 5 MJ/Nm³ compared to MS15. Analysis of the solid phase using XRD, XPS, and SEM indicated that the active sites on the surface of CaO facilitated the cleavage and deoxygenation of bio-oil on the biochar during the pyrolysis process, breaking it down into small molecular gases.</div></div>\",\"PeriodicalId\":20743,\"journal\":{\"name\":\"Process Safety and Environmental Protection\",\"volume\":\"192 \",\"pages\":\"Pages 1051-1061\"},\"PeriodicalIF\":6.9000,\"publicationDate\":\"2024-10-31\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Process Safety and Environmental Protection\",\"FirstCategoryId\":\"93\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S095758202401406X\",\"RegionNum\":2,\"RegionCategory\":\"环境科学与生态学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Process Safety and Environmental Protection","FirstCategoryId":"93","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S095758202401406X","RegionNum":2,"RegionCategory":"环境科学与生态学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Metal oxide-molten salt catalyzed pyrolysis: Improving the energy conversion efficiency of wheat straw
This study systematically investigates the pyrolysis process of wheat straw in a ternary carbonate molten salt system (Li₂CO₃-Na₂CO₃-K₂CO₃) with the addition of different metal oxides (CaO, Al₂O₃, Fe₂O₃, TiO₂). The effects of the ratio of molten salt, type of metal oxide, and pyrolysis temperature on the pyrolysis products were examined. As the temperature increased, in the MS15 (wheat straw: molten salt = 1:15) system, the yield of gas-phase products rose from 21.21 wt% to 82.57 wt%, while the yields of solid products and bio-oil rapidly decreased to 23.76 wt% and 37.60 wt%, respectively. Additionally, the system exhibited the highest lower heating value (LHV) within the temperature range of 450–750 ℃. Therefore, the optimal ratio of wheat straw to carbonate molten salt is 1:15. Furthermore, when adding four metal oxides (Al₂O₃, CaO, Fe₂O₃, TiO₂) to the MS15 system, it was found that the addition of CaO (CaO-MS15) resulted in the highest LHV across all pyrolysis temperatures. Notably, at 550 ℃, the maximum LHV was 21.89 MJ/Nm³, an increase of 5 MJ/Nm³ compared to MS15. Analysis of the solid phase using XRD, XPS, and SEM indicated that the active sites on the surface of CaO facilitated the cleavage and deoxygenation of bio-oil on the biochar during the pyrolysis process, breaking it down into small molecular gases.
期刊介绍:
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