{"title":"热自养甲烷菌在固定床反应器中由H2和CO2连续生成CH4的研究","authors":"Hae Sung Jee, Naomichi Nishio, Shiro Nagai","doi":"10.1016/0385-6380(88)90054-4","DOIUrl":null,"url":null,"abstract":"<div><p>Methanation of H<sub>2</sub> and CO<sub>2</sub> by <em>Methanobacterium thermoautotrophicum</em> ΔH was carried out in a fixed-bed reactor (31 mm<em>φ</em> × 180 mm H) packed with granular diatomaceous earth clay (2–3 mmφ) as a support material. The maximum methane production rate obtained was <span><math><mtext>5.2 </mtext><mtext>l</mtext><mtext>l</mtext></math></span> bed volume/h, while a conversion rate reaching up to some 80% of the theoretical value was achieved by controlling the feed rate of the substrate gas throughout the culture period. After cultivation methanogen cells were fixed almost homogeneously on the whole of the support material, giving 30 mg dry cell/cm<sup>3</sup> packed support.</p></div>","PeriodicalId":15702,"journal":{"name":"Journal of Fermentation Technology","volume":"66 2","pages":"Pages 235-238"},"PeriodicalIF":0.0000,"publicationDate":"1988-01-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0385-6380(88)90054-4","citationCount":"47","resultStr":"{\"title\":\"Continuous CH4 Production from H2 and CO2 by Methanobacterium thermoautotrophicum in a fixed-bed reactor\",\"authors\":\"Hae Sung Jee, Naomichi Nishio, Shiro Nagai\",\"doi\":\"10.1016/0385-6380(88)90054-4\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Methanation of H<sub>2</sub> and CO<sub>2</sub> by <em>Methanobacterium thermoautotrophicum</em> ΔH was carried out in a fixed-bed reactor (31 mm<em>φ</em> × 180 mm H) packed with granular diatomaceous earth clay (2–3 mmφ) as a support material. The maximum methane production rate obtained was <span><math><mtext>5.2 </mtext><mtext>l</mtext><mtext>l</mtext></math></span> bed volume/h, while a conversion rate reaching up to some 80% of the theoretical value was achieved by controlling the feed rate of the substrate gas throughout the culture period. After cultivation methanogen cells were fixed almost homogeneously on the whole of the support material, giving 30 mg dry cell/cm<sup>3</sup> packed support.</p></div>\",\"PeriodicalId\":15702,\"journal\":{\"name\":\"Journal of Fermentation Technology\",\"volume\":\"66 2\",\"pages\":\"Pages 235-238\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1988-01-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/0385-6380(88)90054-4\",\"citationCount\":\"47\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of Fermentation Technology\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/0385638088900544\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of Fermentation Technology","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/0385638088900544","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 47
摘要
热自养甲烷杆菌ΔH在固定床反应器(31 mmφ × 180 mm H)中进行了H2和CO2的甲烷化反应,反应器填充颗粒状硅藻土粘土(2-3 mmφ)作为支撑材料。最大产甲烷率为5.2 l床体积/h,而在整个培养过程中控制底物气体的进给量,转化率可达到理论值的80%左右。培养后,甲烷菌细胞几乎均匀地固定在整个支撑材料上,给予30 mg干细胞/cm3填充支撑。
Continuous CH4 Production from H2 and CO2 by Methanobacterium thermoautotrophicum in a fixed-bed reactor
Methanation of H2 and CO2 by Methanobacterium thermoautotrophicum ΔH was carried out in a fixed-bed reactor (31 mmφ × 180 mm H) packed with granular diatomaceous earth clay (2–3 mmφ) as a support material. The maximum methane production rate obtained was bed volume/h, while a conversion rate reaching up to some 80% of the theoretical value was achieved by controlling the feed rate of the substrate gas throughout the culture period. After cultivation methanogen cells were fixed almost homogeneously on the whole of the support material, giving 30 mg dry cell/cm3 packed support.