几种烟气脱硫工艺及技术经济分析_李成益

整理文档很辛苦,赏杯茶钱您下走!

免费阅读已结束,点击下载阅读编辑剩下 ...

阅读已结束,您可以下载文档离线阅读编辑

资源描述

22··(,l20(8):、BFFGD、M、5,,5,。:,50:,《》(GB132232X()3)2〕41,,200350:,:,。,,:、,,,、。,2《X)4,20GW,30GW。5,2X()GW。10,300GW。,,。,。1,10,。、、、。,;、,,。、CLFGD、Mgo、、。:126x10Nm,/h,5022Ioomm3,Zoomm,,138CC。1.1、。,,,50:,(),。(l)①,,80%,;②,,;;③,50:,。(2)2X(0923。:,,1965,,。6(2《X)6).①,;②,;③、;④94%。1.2CLFBFGD、、。,。,,。。、。、、,,PLC。(l)①,;②,,,;③,,;④,,,。(2)①,80%;②,,;③,。(3)、:1t50:,0.9tLZt。:1tSO:,Zt。1.3M:、50:、、、、。(l)①,。,。,。②,。,95%98%。③,/,。(2)①。M0,M04,。Cao,“”。。②,。③:,。:(Mg503)。④。450/t(:,75%so%),200,550/t,so/t,,363。,,,90%、325,1600/t(:1250,2700/t:25X(),46X()/t)。Mgo,90%,250,7X()ojt。⑤。M。1.450:NH3,50:,。,。(l)①、;②;③,90%95%;④;⑤,1250aP22;。(2)①(2X()mm,),350m,It。②。1t50:0.5t。,(,,)。③。④,。1.5CANSOVL,50:,99%。,50:,50:,S,。(l)①,50m;②、。(2)①;②,;③、。22.1:,;:,;:(75%),(),;:,,;:,,(、、),、。.221。1598()47495355026835180700800850400()1824082263l884OnJQù,ùùsol8OUù(、)97788752930493502.3:(l)72X()h。(2)14,3%5%。(3):0.50/kw·;h1/t;250/t;(75%,)630/t;260/t;1770/t;59300)t;100/t;。(4):24;、、12,3。(5):40/t;/,5/t;,5/t;6!/t;50:2X()。2。2,5,。。6(2).2/(14)///kt.。:/·t’t.h,/kw·ht·h1/t/.h,/·t’/t/.h,t·。’//·a’/·’9304664.57279.1224.6763093507.86280.512.63177092X()657.1452145632607。.28256262778:43422509698293304《)40256()353(XX】60107018.14723512X()20727.0440202.752380171363245.373042.621.78423515.232116235.22473.142488371.639.01532.442380171363203.773236.211.895.132218.142380171364364.402]46271.252.5932oo5l8.6()259318669.64225.923707321.9933.15,,、,。50:,CO:,。,CaS03,,。,90%,50:,。,Mg-50;,MgS03,M,Mgo90%,M04300t,1.%/kg50:,。,,GB535199550x106,,、、。,(GB294589)、(BG35592001),(GB24402001)、,。。,(bP)0.001%。3.25,GGH(),,0.76/kg5020.50/kg502,,(),。(),。3.380%,—。225,2.0x105kw·h(500Mt,1.0%),,30Mt。15Mt,,,15Mt。,20Mt,。,(,),,、,,。3.4、,、,:,(),,。3.52005519《》,:“1%(1%)2X()MW(200MW),”;“,,”。《》:,,,:、,。《》,“,。、、、,,,,,”。。《》,2(X)6“”,“`”,,,。、,,,、。3.6,、。:CO:,,,,“”,。4(l),(、、、)。(2),,,,()。(3),(、),。(4),()(、),。,、(NO)、。(5),6(2X().,,410“hCFB60Mw,(、。)、(),CFB,3(D),200()。(、,()CFB、,,)。,,,1.0%0.5%50CFB。,,。SeveriaFlueGasDesulforizationProcessesandTechno.EconocAnalysisofhtemUChengyi(。nnignDament,SECaYn1etPocrhemicaloC.,d.NainjgnZI《x8)ABSTRACThTisperbireflyinotrdueed5fluegasdesulfuirzationporeesses,ineludinglimestoneplasterwetPoreess,LCFBFGDeicruliatngfluidbedprocess,MgOwetPoreess,ammoniafertilizerporeessanderpordue-ibleamineporeess,andeomPaerdtheadvantagesanddisadvanta5ofeachmethod.Basedonteehnoeeo-nomieeompiarsonofhteifvevocresses,itporposedforenteirsestodevelopflue5desuifuirzationaeeodringtotheirowneonditions.Keywords:fluegasdesuifuirzation,ammoniaporeessofdesulfuirzation,sulfurdioxideBASF、DowSolvHPPOBsAF、oDwsohayBASFDowAnt-we/(HPPO),10。230kaH202Solv50%,BASF25%Dow25%。H20:,300ka200ktH20:。BASFDowHPPO,BASFDow50:50。2008,(PO)200kaBASF。。BASFeGismar2X()9,Dow。BASFAnwte,,25%,70%80%,35%,。。DowBASF,。DowBASF/,。20103%4%。(CW,Oot.4,2006)

1 / 6
下载文档,编辑使用

©2015-2020 m.777doc.com 三七文档.

备案号:鲁ICP备2024069028号-1 客服联系 QQ:2149211541

×
保存成功