Optimization of the process parameters for fine coal-oil agglomeration process using waste mustard oil

被引:19
作者
Shukla, Darpan [1 ]
Venugopal, R. [1 ]
机构
[1] Indian Sch Mines Dhanbad, Indian Inst Technol, Dept Fuel & Mineral Engn, Police Line, Dhanbad 826004, Jharkhand, India
关键词
Oil agglomeration; Waste vegetable oil; Coal fines; Response surface methodology; Optimization; RESPONSE-SURFACE METHODOLOGY; BOX-BEHNKEN DESIGN; CLEANING WASTES; VEGETABLE-OILS; BITUMINOUS COAL; RECOVERY; FLOCCULATION; PERFORMANCE; WVO;
D O I
10.1016/j.powtec.2019.02.001
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Numerous fine coal processing technologies like froth flotation, enhanced gravity separation exist today, but their insularity have led to the adoption of oil agglomeration as a retrieval technique. In the present study, coal fines were recovered by the oil agglomerating process with the agglomerating oil as a waste vegetable oil - waste mustard oil. The effect of pulp density, oil dosage and agglomeration time were analysed on the responses - organic matter recovery (% OMR) and ash rejection (% AR). The responses were optimized using three-level Box Behnken experimental design in conjunction with the Response Surface Methodology. The resulting conditions were 99.69% for % OMR and 62.56% for % AR, showcasing that waste mustard oil has good agglomerating properties, despite of the heat treatment undergone by it during frying. Optimization studies were also performed by minimizing the oil dosage to countervail the poor economics of the oil agglomeration process. The observed conditions were investigated as 79.21% for % OMR and 65.41% for % AR obtained at an oil dosage of 8.39%. The comparative examination of these results with the contemporary studies of different oil types proved that waste mustard oil is a much better bridging liquid than the currently available oils. (C) 2019 Elsevier B.V. All rights reserved.
引用
收藏
页码:316 / 325
页数:10
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