Statistical modelling and optimization of hydrolysis of urea to generate ammonia for flue gas conditioning

被引:62
作者
Mahalik, K. [2 ,3 ]
Sahu, J. N. [1 ,2 ]
Patwardhan, Anand V. [4 ]
Meikap, B. C. [2 ,5 ]
机构
[1] Univ Malaya, Fac Engn, Dept Chem Engn, Kuala Lumpur 50603, Malaysia
[2] Indian Inst Technol, Dept Chem Engn, Kharagpur 721302, W Bengal, India
[3] Gandhi Inst Engn & Technol, Dept Chem Engn, Gunupur, Orissa, India
[4] Inst Chem Technol, Dept Chem Engn, Mumbai 400019, Maharashtra, India
[5] Univ KwaZulu Natal, Sch Chem Engn, ZA-4041 Durban, South Africa
关键词
Urea; Ammonia; Hydrolysis; Factorial design; Suspended particulate matter; Flue gas; SELECTIVE CATALYTIC-REDUCTION; SUSPENDED PARTICULATE MATTER; THERMAL POWER-PLANTS; FLY-ASH; ELECTROSTATIC PRECIPITATORS; STATIONARY APPLICATIONS; SEMIBATCH REACTOR; NITROGEN-OXIDES; BATCH REACTOR; NOX;
D O I
10.1016/j.jhazmat.2010.06.075
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The present study is concerned with the technique of producing a relatively small quantity of ammonia which can be used safely in a coal-fired thermal power plant to improve the efficiency of electrostatic precipitator by removing the suspended particulate material mostly fly ash, from the flue gas. In this work hydrolysis of urea has been conducted in a batch reactor at atmospheric pressure to study the different reaction variables such as reaction temperature, initial concentration and stirring speed on the conversion by using design expert software. A 2(3) full factorial central composite design (CCD) has been employed and a quadratic model equation has been developed. The study reveals that conversion increases exponentially with an increase in temperature, stirring speed and feed concentration. However the stirring speed has the greatest effect on the conversion with concentration and temperature exerting least and moderate effect respectively. The values of equilibrium conversion obtained through the developed models are found to agree well with their corresponding experimental counterparts with a satisfactory correlation coefficient of 93%. The developed quadratic model was optimized using quadratic programming to maximize conversion of urea within experimental range studied. The optimum production condition has been found to be at the temperature of 130 degrees C, feed concentration of 4.16 mol/l and stirring speed of 400 rpm and the corresponding conversion, 63.242%. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:603 / 610
页数:8
相关论文
共 57 条