Sub and supercritical water oxidation of pharmaceutical wastewater

被引:60
作者
Mylapilli, S. V. Prasad [1 ]
Reddy, Sivamohan N. [1 ]
机构
[1] Indian Inst Technol Roorkee, Dept Chem Engn, Roorkee 247667, Uttarakhand, India
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2019年 / 7卷 / 03期
关键词
Pharmaceutics; Sub and supercritical oxidation; Oxidation coefficient; Total organic carbon; Toxicity; PHOTOCATALYTIC DEGRADATION; HYDROTHERMAL TREATMENT; PERSULFATE PROCESS; AQUEOUS-SOLUTION; BY-PRODUCTS; REMOVAL; REACTOR; GASIFICATION; TEMPERATURE; IBUPROFEN;
D O I
10.1016/j.jece.2019.103165
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Sub and supercritical water oxidation (Sub- CWO & SCWO) technology has gained attention over the past few years due to near complete conversions at shorter residences times. A pharmaceutical sample containing variety of analgesics, antibiotics, antipyretics, antifungal, beta-blockers and drug intermediates contributing to overall total organic carbon (TOC) of 2017 +/- 49 mg/L was collected from a nearby pharmaceutical industry for this research. The sample was subjected to sub and supercritical water oxidation both in batch and continuous processes. A maximum removal efficiency of 80.1% was achieved with excess oxidant (oxidation coefficient (OC 3)) at 400 degrees C for 60 min residence time in batch reactor. The pharmaceutical sample was also processed in continuous supercritical water reactor by varying both temperature (400-550 degrees C) and oxidant coefficient (0-2) at 23 MPa for 60 s residence time. With the operating temperature of 550 degrees C and OC 2 resulted in maximum removal of the pharmaceutics with efficiency of 97.8%.
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页数:9
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