中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
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
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://WOS:000227877800012
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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