水煤浆与煤粉燃烧脱硫比较

6(2000)JOURNAL OF COMBUSTION SCIENCE AND TECHNOLOGYVol.6(2000)No.1f‰§“,”….310027)-c‰。0-…f‰x“f丰(W℃a/S-)Ef‰56B-,f%‰":TK227.1一正别:1006-8740(2000)01-0047-04Comparison Between Desulfurization During Pulverized-Coal Combustionand Desulfurization During Coal-Water Slurry CombustionFAN Hao-jie, ZHANG Ming-chuan, HU Guo-xinYAO Qiang, CAO Xin-yu, CEN Ke-fa(1. Dept. of Energy Engineering Shanghai Jiao Tong University Shanghai 200240 China2. Dept. of Power Engineering, Shanghai Jiao Tong University, Shanghai 200030, China;3. Dept. of Energy Engineering Zhejiang University Hangzhou 310027 China)Abstract: It is a trend to replace oil-fuel by coal in the field of energy industry. CwS(coal-water slurry ) is a newsubstitute for oil-fuel which has been widely used In this paper the sulfur release parameters of desulfurization(temperature, Ca/S ratio), particulate emission and so on were studied during CwS combustion. Compared with thedesulfurization during PC(pulverized coal)combustion the desulfurization during CWS combustion has a high SOzremoval efficiency. The results prove that the desulfurization during CWS combustion is a good method of desulfurzationKeywords: pulverized coal; coal-water slurry i combustion desulfurizatic士一御f‰,f‰.,,,5一。a%°￠,,,0”‰是二~元一之2,罪O七‰丰‰5.·f^一%申20W正。,f%≤1.1科乙3<-0--。%暑「手d￥‰丰、‰E”>f‰<中…士十老十1998-10-06;1999-08-02§6f二>科§1-‰2-2千-(f1350C。己N”-….「….,暑SO2-「”一.十51,423.852.550.864.63(口%‰丰、9中丰1[4812121637097171203216242“科“一空气预处理装置科-傘-C00AOS02FeO96.900.780.0392.040.082库仑积分仪电解题乐B燃烧炉。°。°。搅拌器库仑温控仪‰f,%」丰,丰‰阝-.3(T=1200C)。-‰<82%丰"丰,十O,丰(o,O4)2>8.+(ab,AB)‰「:→0,丰1.20.25MWz/f0.25MW^/f%丰f只.‰是,,-“丰口“2/~>￠丰-育計f,%,阝.2煤粉%oFs fl十究一煤桨,,0MSI20005((SEM),十15020025>-κTAM军乙十老>-列一之￠丰3丰,丰科f-.2压缩空气烟气分析油枪插口而暑》5;…小一冷水飞灰取样风温度测点烟气分个除尘器十丰只,。…,十千一2,,%<=:(1400C)°燃尽室风尽室、度测十老220%)W2丰喷水点灰取样“∴∵”「科,…t灰取样下温度测点丰,二Q‰。,‰十22/f%…”Q口2000-匪%:f%<2-..-%-本:‰"°4~12dfI阝。煤浆煤粉1150125013501450T/Cv煤粉T=1200煤浆T=1170丰只W0.51.01.52.02.53.03.52.2.T,.71000C)》…,‰,…,∈aO‰A2.4-f‰<「丰一二》…-%。5》%8酊.2f%2-2士m~0.3pm3,900C,‰6。乙足-g”<3-”十s正≤-千一元中丰乙i「-B-:T,,fs-f正。3--F‰Ⅶ-÷"年,而一f‰s.,辶十》,,‰∈÷”T)f5%~7%30%,E,f%,一§”十中->f”÷,f‰<5”2f‰Tfi-sz->3士<?十∴FAM￡‰軒,a/S=1.5“,「-1200C°二.fl2f‰·>%十%0B‰…(48%);Ca/S=3“WT172C,%>-%‰8E58.94m,2‰-》-‰G￡“4.200C‰一十>,“m,W2.25.09m。E>,“-x“f钙”>∑,>fx‰之—∑十利”,≥、%‰己∑干》”≤≥▲煤浆Ca/S=1.5∑」>刮∑一%￡「石●煤浆Ca/S=3△煤粉Ca/=2》2-。「”,,f‰←》-E‰∑-…%‰之∑T/℃軒,-2CaCO3￡‰‰。,,鲁f可‰2.3Ca/S-,「…-E“,-2,O2”,士s∈a/S丰,Ca/S,压SO2eaO‰-￥一￡乐7-.10),十ee用Em丰:,f%‰》辶一‰f‰§6f‰》-00010f2-》.000-Wf‰3‰阝+乙。(1)3sf十,辶十L十0。+‰T→0.+,平[1 Falkenberry, SO, Removal by Limestone Injection [J]. Chem Eng0。%丰s2Prog,1969,12:61~70.(2)「f‰i Ca/ [2] Lachapelle G. EPA'S LIMB Technology Development ProgramLJI Chem Eng Prog. 1985.5: 56-63,S‰,≤Ca/S…"°厍-∷鄱:%六.[4]fT‰,十一af‰Ca/s%∴TT..1200J].^”辶昏叫96,21(4):438~441f‰[5]‰.2/,f‰E)].”…,%>§6]-‰m,f%§‰》-s‰。∷1992.1[7]-一而曰].f‰c,1994,(3):13~202->‰,%