|
摘要:汽包爐的給水控製是相對獨立的,而超臨界機組鍋爐給水控製則是和燃燒、qiwendengxitongxianghuouhezaiyiqide,yincizhiliuludegeishuikongzhixiangduiyuqibaolueryanyaofuzaxie。tongshigeishuikongzhixitongyoushichaolinjiejizurekongxitongzhongdezhongdian,duitigaojizudekongzhizidonghuachengdu、減少啟停誤操作、縮短機組啟動時間、提高機組啟停的可靠性具有重要作用,也是實現機組級自啟停(APS)控製的一個技術關鍵。本文以某超超臨界600MW機組為例,介紹鍋爐給水調節係統的控製。
關鍵詞:600MW,超臨界,給水,焓,煤水比,自動調節
一、超臨界機組給水係統的控製特性
汽包爐通過改變燃料量、減溫水量和給水流量控製蒸汽壓力(簡稱汽壓)、蒸汽溫度(簡稱汽溫)和汽包水位,汽壓、汽溫、給水流量控製相對獨立。而直流爐作為一個多輸入、多輸出的被控對象,其主要輸出量為汽溫、汽壓和蒸汽流量(負荷),其主要的輸入量是給水量、燃燒率和汽機調門開度,youyushiqiangzhixunhuanqieshourequduanzhijianwugudingjiexian,yizhongshuruliangraodongjiangduigeshuchuliangchanshengzuoyong,rudandugaibiangeishuilianghuoranliaoliang,bujinyingxiangzhuqiyayuzhengqiliuliang,guoreqichukouqiwenyehuichanshengxianzhudebianhua,suoyibizhikongzhi(如給水量/蒸汽量、燃料量/給水量及噴水量/給水量等)和變定值、變參數調節是直流鍋爐的控製特點。
實踐證明要保證直流鍋爐汽溫的調節性能,維持特定的煤水比來控製汽水行程中某一點焓(分離器入口焓)達到規定要求,是一個切實有效的調溫手段。當給水量或燃料量擾動時,汽水行程中各點工質焓值的動態特性相似;在鍋爐的煤水比保持不變時(工況穩定),汽水行程中某點工質的焓值保持不變,所以采用微過熱蒸汽焓替代該點溫度作為煤水比校正是可行的,其優點在於:
1) 分離器入口焓(中間點焓)值對煤水比失配的反應快,係統校正迅速; 2) 焓值代表了過熱蒸汽的作功能力,隨工況改變焓給定值不但有利於負荷控製,而且也能實現過熱汽溫(粗)調正。
3) 焓值物理概念明確,它不僅受溫度變化影響,還受壓力變化影響,在低負荷壓力升高時(分離器入口溫度有可能進入飽和區),焓值的明顯變化有助於判斷,進而能及時采取相應措施。
因此,靜態和動態煤水比值及隨負荷變化的焓值校正是超臨界直流鍋爐給水係統的主要控製特征。
二、超臨界機組給水係統工藝介紹
某電廠2×600MW超超臨界燃煤鍋爐(HG-1792/26.15-YM1),由哈爾濱鍋爐廠引進三菱技術製造,其形式為超超臨界、П型布置、單爐膛、牆式切園燃燒方式,爐膛采用內螺紋管垂直上升膜式水冷壁、帶再循環泵的啟動係統、一次中間再熱。鍋爐采用平衡通風、半露天布置、固態排渣、全鋼構架、全懸吊結構,燃用煙煤。主要參數見表一:
| 表一:主要參數 |
| 項目 |
BMCR |
項目 |
BMCR |
|
過熱蒸汽流量 |
1792t/h |
再熱器出口蒸汽壓力 |
4.58Mpa |
|
過熱蒸汽出口壓力 |
26.15Mpa |
再熱器出口蒸汽溫度 |
603℃ |
|
過熱蒸汽出口溫度 |
605℃ |
省煤器進口給水溫度 |
292℃ |
|
再熱蒸汽流量 |
1462t/h |
鍋爐純直流運行負荷 |
25%MBCR |
啟動係統配有2隻(zhi)內(nei)置(zhi)式(shi)分(fen)離(li)器(qi),在(zai)鍋(guo)爐(lu)啟(qi)動(dong)和(he)低(di)負(fu)荷(he)運(yun)行(xing)時(shi),分(fen)離(li)器(qi)處(chu)於(yu)濕(shi)態(tai)運(yun)行(xing),同(tong)汽(qi)包(bao)一(yi)樣(yang)起(qi)著(zhe)汽(qi)水(shui)分(fen)離(li)的(de)作(zuo)用(yong),此(ci)時(shi)適(shi)當(dang)控(kong)製(zhi)分(fen)離(li)器(qi)水(shui)位(wei),通(tong)過(guo)循(xun)環(huan)回(hui)收(shou)合(he)格(ge)工(gong)質(zhi);當鍋爐進入直流運行階段,分離器處於幹態運行,成為(過熱)蒸汽通道。鍋爐給水係統的工藝流程如圖1所示,機組配備有二台50%BMCR汽動給水泵和一台25%BMCR的(de)電(dian)動(dong)給(gei)水(shui)泵(beng),電(dian)泵(beng)轉(zhuan)速(su)由(you)液(ye)耦(ou)調(tiao)節(jie),用(yong)於(yu)啟(qi)動(dong)時(shi)調(tiao)節(jie)給(gei)水(shui)壓(ya)力(li)。啟(qi)動(dong)過(guo)程(cheng)中(zhong),蒸(zheng)汽(qi)加(jia)熱(re)除(chu)氧(yang)器(qi)給(gei)水(shui),主(zhu)給(gei)水(shui)泵(beng)的(de)出(chu)水(shui)經(jing)高(gao)壓(ya)加(jia)熱(re)器(qi)後(hou)進(jin)入(ru)省(sheng)煤(mei)器(qi),考(kao)慮(lv)到(dao)低(di)負(fu)荷(he)下(xia)直(zhi)流(liu)鍋(guo)爐(lu)對(dui)重(zhong)量(liang)流(liu)速(su)的(de)要(yao)求(qiu),在(zai)啟(qi)動(dong)和(he)低(di)負(fu)荷(he)階(jie)段(duan)最(zui)小(xiao)給(gei)水(shui)流(liu)量(liang)設(she)置(zhi)為(wei)25%BMCR,流(liu)過(guo)水(shui)冷(leng)壁(bi)管(guan)的(de)汽(qi)水(shui)混(hun)合(he)物(wu)進(jin)入(ru)分(fen)離(li)器(qi),分(fen)離(li)器(qi)貯(zhu)水(shui)箱(xiang)出(chu)來(lai)疏(shu)水(shui)分(fen)兩(liang)路(lu),一(yi)路(lu)進(jin)入(ru)省(sheng)煤(mei)器(qi),另(ling)一(yi)路(lu)經(jing)擴(kuo)容(rong)器(qi)擴(kuo)容(rong)後(hou)進(jin)入(ru)疏(shu)擴(kuo)箱(xiang),由(you)擴(kuo)疏(shu)泵(beng)輸(shu)送(song)至(zhi)凝(ning)汽(qi)器(qi)或(huo)直(zhi)接(jie)向(xiang)外(wai)排(pai)放(fang)。隨(sui)著(zhe)循(xun)環(huan)加(jia)熱(re)的(de)進(jin)行(xing),當(dang)給(gei)水(shui)達(da)到(dao)一(yi)定(ding)溫(wen)度(du)後(hou),鍋(guo)爐(lu)允(yun)許(xu)火(huo)。鍋(guo)爐(lu)汽(qi)水(shui)係(xi)統(tong)如(ru)圖(tu)一(yi)所(suo)示(shi):

三、超臨界機組給水係統控製方案
第一階段:啟動和低負荷階段;當啟動初期在濕態時(30%負荷以下),給水控製係統使省煤器入口流量維持在30%BMCR流量(本生流量)左zuo右you,省sheng煤mei器qi入ru口kou流liu量liang為wei循xun環huan泵beng出chu口kou流liu量liang和he高gao加jia出chu口kou流liu量liang之zhi和he,此ci時shi省sheng煤mei器qi流liu量liang控kong製zhi主zhu要yao依yi靠kao循xun環huan泵beng出chu口kou調tiao閥fa控kong製zhi,電dian泵beng液ye耦ou手shou動dong控kong製zhi給gei水shui母mu管guan壓ya力li,通tong過guoBR閥控製省煤器入口流量穩定。汽水分離器起到汽水分離的作用,蒸汽進入過熱器,水進入貯水箱,此時貯水箱中的水位主要依靠WDC閥1和WDC閥2控製,此次控製貯水箱水位控製如同汽包爐的汽包水位,應注意虛假水位的控製。為防止循環泵(BCP)入口汽化,從高加出口引入一路噴射水,一般維持在1%~3%左右的噴射水量以達到控製BCP入口的過冷度的目的。
第二階段:轉直流運行階段;在負荷大於25%~35%BMCR 以上時鍋爐即轉入直流運行方式。
1、概述:鍋(guo)爐(lu)進(jin)入(ru)直(zhi)流(liu)狀(zhuang)態(tai),給(gei)水(shui)控(kong)製(zhi)與(yu)汽(qi)溫(wen)調(tiao)節(jie)和(he)前(qian)一(yi)階(jie)段(duan)控(kong)製(zhi)方(fang)式(shi)有(you)較(jiao)大(da)的(de)不(bu)同(tong),給(gei)水(shui)不(bu)再(zai)控(kong)製(zhi)分(fen)離(li)器(qi)水(shui)位(wei)而(er)是(shi)和(he)燃(ran)料(liao)一(yi)起(qi)控(kong)製(zhi)汽(qi)溫(wen)即(ji)控(kong)製(zhi)煤(mei)水(shui)比(bi)WFR。負荷大於20%後(hou),第(di)一(yi)台(tai)汽(qi)泵(beng)啟(qi)動(dong),達(da)到(dao)衝(chong)轉(zhuan)轉(zhuan)速(su),泵(beng)出(chu)口(kou)壓(ya)力(li)達(da)到(dao)預(yu)定(ding)壓(ya)力(li)後(hou),汽(qi)泵(beng)可(ke)以(yi)投(tou)入(ru)自(zi)動(dong),並(bing)入(ru)第(di)一(yi)台(tai)汽(qi)泵(beng),並(bing)逐(zhu)步(bu)降(jiang)電(dian)泵(beng)負(fu)荷(he)轉(zhuan)移(yi)到(dao)汽(qi)泵(beng)上(shang)來(lai),到(dao)40%負fu荷he左zuo右you可ke以yi將jiang電dian泵beng退tui出chu運yun行xing。電dian泵beng退tui出chu運yun行xing後hou,啟qi動dong第di二er台tai汽qi泵beng,衝chong轉zhuan到dao預yu定ding轉zhuan速su,泵beng出chu口kou壓ya力li達da到dao預yu定ding壓ya力li後hou,投tou入ru自zi動dong,並bing入ru第di二er台tai汽qi泵beng,將jiang第di一yi台tai汽qi泵beng的de部bu分fen負fu荷he轉zhuan移yi到dao第di二er台tai汽qi泵beng上shang來lai。轉zhuan直zhi流liu後hou,汽qi水shui分fen離li器qi中zhong已yi沒mei有you水shui存cun在zai,僅jin作zuo為wei一yi個ge蒸zheng汽qi通tong道dao,循xun環huan泵beng退tui出chu運yun行xing。在zai本ben生sheng負fu荷he以yi上shang時shi,汽qi水shui分fen離li器qi入ru口kou汽qi溫wen是shi微wei過guo熱re蒸zheng汽qi,這zhe個ge區qu域yu的de汽qi溫wen變bian化hua,可ke以yi直zhi接jie反fan映ying出chu燃ran料liao量liang和he給gei水shui蒸zheng發fa量liang的de匹pi配pei程cheng度du以yi及ji過guo熱re汽qi溫wen的de變bian化hua趨qu勢shi。所suo以yi在zai直zhi流liu鍋guo爐lu的de汽qi溫wen調tiao節jie中zhong,通tong常chang選xuan取qu汽qi水shui分fen離li器qi出chu口kou汽qi溫wen做zuo為wei主zhu汽qi溫wen調tiao節jie回hui路lu的de前qian饋kui信xin號hao,此ci點dian的de溫wen度du稱cheng為wei中zhong間jian點dian溫wen度du。依yi據ju該gai點dian溫wen度du的de變bian化hua對dui燃ran料liao量liang和he給gei水shui量liang進jin行xing微wei調tiao。直zhi流liu鍋guo爐lu一yi定ding要yao嚴yan格ge控kong製zhi好hao水shui煤mei比bi和he中zhong間jian點dian過guo熱re度du。
2.給水流量需求指令形成生成;鍋(guo)爐(lu)給(gei)水(shui)流(liu)量(liang)給(gei)水(shui)控(kong)製(zhi)係(xi)統(tong)負(fu)責(ze)向(xiang)鍋(guo)爐(lu)給(gei)水(shui)泵(beng)發(fa)出(chu)流(liu)量(liang)需(xu)求(qiu)信(xin)號(hao),使(shi)進(jin)入(ru)鍋(guo)爐(lu)的(de)給(gei)水(shui)量(liang)與(yu)離(li)開(kai)鍋(guo)爐(lu)的(de)蒸(zheng)汽(qi)量(liang)相(xiang)匹(pi)配(pei)。當(dang)與(yu)鍋(guo)爐(lu)啟(qi)動(dong)係(xi)統(tong)配(pei)合(he)時(shi),給(gei)水(shui)流(liu)量(liang)控(kong)製(zhi)係(xi)統(tong)還(hai)需(xu)負(fu)責(ze)維(wei)持(chi)爐(lu)膛(tang)水(shui)冷(leng)壁(bi)管(guan)中(zhong)的(de)流(liu)量(liang)不(bu)低(di)於(yu)最(zui)小(xiao)流(liu)量(liang)值(zhi);給水指令形成回路見圖二所示:

zheshiyigecaiyongzhongjiandianhanzhikongzhizhiliuguolugeishuidefangan,guoluranshaoxuqiuzhilingbingxingdesongzhiranshaozhukonghegeishuiliuliangxuqiuhuilu,zaigegefuhexiaranliaohegeishuipipei,jiarumeishuibixiuzheng。
回路一是一個焓值控製校正回路。焓值控製的任務是保證分離器出口蒸汽焓始終在其微過熱蒸汽焓(汽水分離器入口)。weiguorezhengqihanyuguoreqichukouzhengqihanbijiao,tamenyouxiangsidedongtaitexingquxian,danweiguorezhengqihanguanxingxiao,xiangyingkuai,nengkuaisudifanyingguolumeishuibixinhaodebianhua,daibiaoxingqiang,qugaidianxiuzhengmeishuibikeyihuoqujiaohaodekongzhizhiliang。youfuhezhilingjingF(X)1shengchengyigebutongfuhexiadeweiguorezhengqideedinghanzhi,jingguoyigeduojieguanxinghuanjie,yinweifuhezhilingfanyingdaozhongjiandianwenduyouyigeguoludeguanxinghuanjie。yunxingguochengyinweimeizhibianhuahuiyinqilutangrefuhebianhua,yehuifanyingdaowendubianhua,suoyizengjiayigecaozuorenyuanshoudongxiuzhenghanzhishedingdejiekou。guoreqijianwenshuixiaozhengzhiliuguoludegeishuiliuliangkongzhiyujianwenshuizongliangdekongzhizhijianyouzhebirandelianxi,genjushejizaibutongdefuhexia,geishuiliulianghejianwenshuiliuliangyouxiangduiyingbizhi,ruguoshijijianwenshuiliuliangfashengpianchashi,hansheshedingzhifashengqijiuhuizidongxiaozhenghanyaoqiuzhi,gaibianmeishuibi,zuizhonggeishuiliuliangzhilingshijianwenshuiliangzhubuxiaochupiancha。fuhebianhuashihanzhishedingdedongtaibuchang,bianfuheshi,zhongjiandianhanzhihuiyouyigedongtaidebianhua,fuhewendinghouhuizidongxiaochu,jiashangzhegebuchang,zehuizaibianfuheshiweichihanzhishedingzhiyougedongtaidebianhua,yishiyingbianfuheshihanzhidebianhua。zhongjiandianhanzhiyouzhongjiandianyalihezhongjiandianwendujingguohanzhishengchengqishengcheng。
回路二是給水指令形成回路。燃料量(鍋爐指令)經F (X)2的函數變換後,作為給水流量的指令信號,它代表不同負荷(燃料量)下(xia)對(dui)給(gei)水(shui)流(liu)量(liang)的(de)要(yao)求(qiu)。由(you)於(yu)汽(qi)溫(wen)對(dui)給(gei)水(shui)量(liang)的(de)動(dong)態(tai)響(xiang)應(ying)要(yao)比(bi)燃(ran)燒(shao)率(lv)快(kuai),設(she)置(zhi)一(yi)個(ge)多(duo)階(jie)慣(guan)性(xing)環(huan)節(jie),使(shi)給(gei)水(shui)遲(chi)於(yu)燃(ran)燒(shao)率(lv)變(bian)化(hua),減(jian)小(xiao)汽(qi)溫(wen)的(de)動(dong)態(tai)變(bian)化(hua)。給(gei)水(shui)量(liang)用(yong)分(fen)離(li)器(qi)出(chu)口(kou)溫(wen)度(du)來(lai)微(wei)調(tiao),保(bao)證(zheng)汽(qi)溫(wen)。給(gei)水(shui)量(liang)需(xu)求(qiu)中(zhong)增(zeng)加(jia)FQ是為了快速響應電網需求而加的。另外給水調節係統中設有煤、水交叉限製回路,用於保證煤水比在安全的範圍內。為了防止省煤器出口汽化,增加了省煤器保護功能;在蒸汽流量小於最小爐膛給水流量時,爐膛最小給水流量限製程序強製給水流量給定值為爐膛最小給水流量。
3.給水控製回路;geishuixuqiuzhilingheshijigeishuiliuliangjingeishuikongzhiqi,chanshengguolugeishuibengzhuansuzhiling,jingguoyigepinghenghuilu,fenpeigeiliangtaigeishuibeng,dangliangtaigeishuibengdoutouzidongshi,keyirengonggeiliangtaibengshedingpianzhi。yinweidianbengwei25%的啟動泵,而且電泵和汽泵的出口壓力不一樣,不推薦電泵和汽泵並列運行,因此電泵的轉速控製有單獨回路。給水控製回路如圖三:

四、結論
超(超)臨界機組的給水控製和亞臨界汽包爐的給水控製有著很大的區別,超(超)臨lin界jie鍋guo爐lu給gei水shui控kong製zhi係xi統tong的de控kong製zhi任ren務wu是shi在zai低di負fu荷he時shi保bao持chi給gei水shui流liu量liang不bu低di於yu最zui小xiao爐lu膛tang給gei水shui流liu量liang,在zai鍋guo爐lu進jin入ru直zhi流liu運yun行xing時shi,保bao持chi適shi當dang的de煤mei水shui比bi,這zhe也ye是shi超chao(超)臨界機組控製過熱汽溫的最基本的手段。
(敬請持續關注:科遠股份002380,NT6000分散控製係統DCS、SY係列智能一體化電動執行機構、SyncPlant管控一體化信息係統等,詳情請登錄www.sciyon.com,或致電:4008818758谘詢,歡迎關注新浪微博@科遠股份002380)
|