Recovery of butyl acetate in wastewater of penicillin plant by solvent sublation II. Theoretical modeling
文献类型:期刊论文
作者 | Sun, XH; Chang, ZD; Liu, HZ; Gao, RL |
刊名 | SEPARATION SCIENCE AND TECHNOLOGY
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出版日期 | 2005 |
卷号 | 40期号:4页码:941-957 |
关键词 | solvent sublation mathematical model butyl acetate penicillin wastewater |
ISSN号 | 0149-6395 |
其他题名 | Sep. Sci. Technol. |
中文摘要 | In recent years, pilot-scale solvent sublation has been explored in the treatment of industrial wastewater containing dilute organics. In the present work, a mathematical model is proposed to describe the experimental results of semibatch sublation for recovering butyl acetate (BA) in the wastewater from solvent extraction of penicillin. Different from other models in recent literatures, our model took account of the variation of the volume of solvent, v(o) in the sublation. The model parameters of the sublation of BA in the wastewater are calculated. Calculation results show the volume of solvent could increase by more than 30% in 180min under optimal conditions. Calculation results with different operation parameters show that increasing the gas flow rate, Q(a) could improve the sublation efficiency, E-ss, which would be more than 70% under optimal conditions. Decreasing the bubble size, a, would increase the rate of the sublation. The initial solvent volume, v(oi), may affect the sublation weakly when initial ratio of water to solvent used is in the range from 50 to 70. Calculation results also show that the loss of butyl acetate to the atmosphere, E-ls, is minimal, though with high gas flow rate. The simulated results are in good agreement with experimental results. |
英文摘要 | In recent years, pilot-scale solvent sublation has been explored in the treatment of industrial wastewater containing dilute organics. In the present work, a mathematical model is proposed to describe the experimental results of semibatch sublation for recovering butyl acetate (BA) in the wastewater from solvent extraction of penicillin. Different from other models in recent literatures, our model took account of the variation of the volume of solvent, v(o) in the sublation. The model parameters of the sublation of BA in the wastewater are calculated. Calculation results show the volume of solvent could increase by more than 30% in 180min under optimal conditions. Calculation results with different operation parameters show that increasing the gas flow rate, Q(a) could improve the sublation efficiency, E-ss, which would be more than 70% under optimal conditions. Decreasing the bubble size, a, would increase the rate of the sublation. The initial solvent volume, v(oi), may affect the sublation weakly when initial ratio of water to solvent used is in the range from 50 to 70. Calculation results also show that the loss of butyl acetate to the atmosphere, E-ls, is minimal, though with high gas flow rate. The simulated results are in good agreement with experimental results. |
WOS标题词 | Science & Technology ; Physical Sciences ; Technology |
类目[WOS] | Chemistry, Multidisciplinary ; Engineering, Chemical |
研究领域[WOS] | Chemistry ; Engineering |
关键词[WOS] | VOLATILE ORGANIC-COMPOUNDS ; REFRACTORY ORGANICS ; REMOVAL ; AERATION ; ATMOSPHERE ; MECHANISM ; EMISSION |
收录类别 | SCI |
原文出处 | |
语种 | 英语 |
WOS记录号 | WOS:000227877800012 |
公开日期 | 2013-10-25 |
版本 | 出版稿 |
源URL | [http://ir.ipe.ac.cn/handle/122111/4242] ![]() |
专题 | 过程工程研究所_研究所(批量导入) |
作者单位 | 1.Chinese Acad Sci, Lab Separat Sci & Engn, State Key Lab Biochem Engn, Inst Proc Engn,Grad Sch, Beijing, Peoples R China 2.N China Pharmaceut Corp Ltd, Shijiazhuang, Peoples R China |
推荐引用方式 GB/T 7714 | Sun, XH,Chang, ZD,Liu, HZ,et al. Recovery of butyl acetate in wastewater of penicillin plant by solvent sublation II. Theoretical modeling[J]. SEPARATION SCIENCE AND TECHNOLOGY,2005,40(4):941-957. |
APA | Sun, XH,Chang, ZD,Liu, HZ,&Gao, RL.(2005).Recovery of butyl acetate in wastewater of penicillin plant by solvent sublation II. Theoretical modeling.SEPARATION SCIENCE AND TECHNOLOGY,40(4),941-957. |
MLA | Sun, XH,et al."Recovery of butyl acetate in wastewater of penicillin plant by solvent sublation II. Theoretical modeling".SEPARATION SCIENCE AND TECHNOLOGY 40.4(2005):941-957. |
入库方式: OAI收割
来源:过程工程研究所
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