水煤浆与煤粉燃烧脱硫比较

6(2000)1JOURNAL OF COMBUSTION SCIENCE AND TECHNOLOGYVol.6(2000)No.1f%,9e,f·十刮一红sfIf310027)￠;二-0,f‰(W、Ca/S-)丰≤”-,f‰f‰"":TK227.1q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 China:2. Dept. of Power Engineering, Shanghai Jiao Tong University, Shanghai 200030, China3. 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 soremoval efficiency. The results prove that the desulfurization during CWS combustion is a good method of desulfurzationKeywords: pulverized coal; coal-water slurry combustion; desulfurization可f‰f‰￠,,,0-‰二~元-之2,罪O七%f‰丰T‰s.·f^%申20「正。f‰≤1.1oflt中国煤化工d“f￥0e--。%CNMHG、‰乙f‰<二丰。十之十:1999-08-02%方数据969-)Cs Goff§6。f七y.,f》科1-%22千-(f5(%)350C。f,,%量Nf…,O2「.十|51.423.852.550.864.632.8633.829中…丰1[ma8126.370.971.1730.326.2“科“世(%空气预处理装置96.900.02.04库仑积分仪电解乐B一可燃烧搅拌器库仑沮控仪。gf,%丰,丰‰B3T=1200C),。-%<2丰“,丰,丰(o,O4)》0,丰(ab,AB)%T丰;十s≤20.25MW2/f‰<."Ef‰丰0.25MW一2/f‰….°丰fi%0十■一>-￠丰⑧只.%,,一丰2/‰“:f扦“f,%,B.2.。-煤粉%oFsfI煤桨丰“‰O)2求坛,0MS2000↓.(;0-(SEM),十→-不FAM…軍之十老》-。-‰丰,丰科f-.2压缩空气‰i烟气分析油枪插口次风却灰取样烟气分十‰T.4/^‰水冷除尘器温度测点水冷十干5(1400C)燃尽室风尽室M度测点中℃.20%),W、唢喷水点灰取样而””「科,…三士灰取样干温度测点中国煤化工,二Q%CNMHG、‰‰十—0…-‰。,,°%ng,>一忌2000~「%。:f%1000C)>,‰,∈aO‰A2.4f%<-丰‰6。>5为68乙酊.2f‰2m~0.3gm8),C,-%∴-邪十s正≤-千CaSO4-‰阝:「,,>fs-f正「年f‰s十>,》7%∈”…”)“55元…%,f‰<‰6%1,Fe_fi2十f%≤丰THIfi T"o士?十∴FAM∑‰軒,a/S=1.5,1200C“°二.f2f‰·》‰十%BT172C‰》‰B∑酊“8.9454%),fi%02>>34.80‰一》-%G￡“4.76T"200C,%十-十》,“{m,「225.09m。乙>“f‰x‰之一∑fi %cA。十。”,≥、们%‰己∑干之》”≤≥煤浆CaS=1.5∑·」>刮--‰。￡「石°煤浆Ca/S=3煤粉1CS=2∑”,f‰》E「115012501350%-…‰L∑T/℃,-2CaCO3￡5 Ill安二一2.3Ca/S-%乙中国煤化工士s长a/S一SBCNMHG辶丰,Ca/SSO2eaO‰-￥辶丰:f%>元∑f‰CacO3一§B..十》,「B十;x‰,Ca/S--厍,A§610f→》-k1000-丌f‰3‰E十,丰辶十L十0+:一→0丰,W[1] Falkenberry, SO Removal by Limestone Injection [J]. Chem EngProg,1969,12:61~70(2)TfS>Ca[23 Lachapelle G. EPA'S LIMB Technology Development Program[JI. Chem Eng Prog.1985.5:56-63fi‰M]‰,≤Ca/S压-‰∴….和T….1200.^§叫996,21(4):438~441f‰6]-2,f‰丰一而暑,而曰].f‰%0s>-￡[8]中国煤化工s]CNMHG