Reaction mechanism of a single calcium hydroxide particle with humidified HCl

被引:9
作者
Koch, M
Zhang, XH
Deng, J
Kavouras, A
Krammer, G
Xu, JC
Ge, LM
机构
[1] Norwegian Univ Sci & Technol, Dept Energy & Proc Engn, N-7491 Trondheim, Norway
[2] Univ Sci & Technol, Energy Engn Inst, Xian, Peoples R China
[3] Xi An Jiao Tong Univ, Energy & Power Sch, Xian 710049, Peoples R China
[4] Graz Univ Technol, Inst Chem Apparatus Design Particle Technol & Com, A-8010 Graz, Austria
基金
奥地利科学基金会;
关键词
reaction engineering; absorption; dechlorination; kinetics; multiphase reactions; flue gas cleaning;
D O I
10.1016/j.ces.2005.05.035
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The reaction of HCl,with Ca(OH)(2) is investigated at industrially relevant conditions of 10% relative humidity, 250ppm or less HCl in nitrogen and a temperature of 100 degrees C. A particle model is used where an interface step and diffusion in pores as well as in solid state are taken into account. The textural parameters of the model are based on data of commercially available Ca(OH)(2). Most importantly Ca(OH)2 single crystals are exposed to HCl containing gas to independently determine the product layer diffusion coefficient. A comparison between model simulations and single-particle (SP) experiments that are performed by means of an ultrasonic levitator (i.e., a particle is held against gravity without neighbouring surfaces) reveals that the overall reaction is solely governed by pore diffusion since the interface step is reaching equilibrium almost instantly and solid-state diffusion in conjunction with mean pore wall thickness is fast at 1.78 x 10(-14) m(2) s(-1). Elementary analyses of Cl across the cross-sections of the SP show significant local textural and chemical variability that cannot be fully explained yet. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:5819 / 5829
页数:11
相关论文
共 18 条
[1]   Reaction mechanism of calcium hydroxide with gaseous hydrogen chloride [J].
Allal, KM ;
Dolignier, JC ;
Martin, G .
REVUE DE L INSTITUT FRANCAIS DU PETROLE, 1998, 53 (06) :871-880
[2]  
[Anonymous], HDB ANORGANISCHE B 3
[3]   Reaction of Ca(OH)2 with HCl in the presence of water vapour at low temperatures [J].
Bausach, M ;
Krammer, G ;
Cunill, F .
THERMOCHIMICA ACTA, 2004, 421 (1-2) :217-223
[4]   Dry absorption of HCL and SO2 with hydrated lime from humidified flue gas [J].
Chisholm, PN ;
Rochelle, GT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (10) :4068-4080
[5]   ONE-STEP AND EXTRAPOLATION METHODS FOR DIFFERENTIAL-ALGEBRAIC SYSTEMS [J].
DEUFLHARD, P ;
HAIRER, E ;
ZUGCK, J .
NUMERISCHE MATHEMATIK, 1987, 51 (05) :501-516
[6]   ALTERATION WITH REACTION PROGRESS OF THE RATE-LIMITING STEP FOR SOLID-GAS REACTIONS OF CA-COMPOUNDS WITH HCL [J].
DUO, W ;
KIRKBY, NF ;
SEVILLE, JPK ;
CLIFT, R .
CHEMICAL ENGINEERING SCIENCE, 1995, 50 (13) :2017-2027
[7]   Possible applications for municipal solid waste fly ash [J].
Ferreira, C ;
Ribeiro, A ;
Ottosen, L .
JOURNAL OF HAZARDOUS MATERIALS, 2003, 96 (2-3) :201-216
[8]   Kinetic modeling of the reaction of HCl and solid lime at low temperatures [J].
Fonseca, AM ;
Orfao, JJ ;
Salcedo, RL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (12) :4570-4576
[9]   A new approach to the kinetic modeling of the reaction of gaseous HCl with solid lime at low temperatures [J].
Fonseca, AM ;
Orfao, JJ ;
Salcedo, RL .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (15) :3499-3506
[10]   REACTION-MECHANISMS OF DRY CA-BASED SORBENTS WITH GASEOUS HCL [J].
JOZEWICZ, W ;
GULLETT, BK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (02) :607-612