1、烘幹理論
hongganguochengshirefengjiangrenengyiduiliudefangshizhijiechuangeiyuqijiechudeshiwuliao,shishiwuliaozhongshuifenqihua,bingjiangshuizhengqidaizoudeguocheng。dangrefenglusuotigongdegaowenqiliuyuzaolijixialaideshiwuliaojiechushi,qiguliangxiangjiansuofashengdere、質(zhi)同(tong)時(shi)傳(chuan)遞(di)。造(zao)粒(li)機(ji)的(de)物(wu)料(liao)到(dao)達(da)烘(hong)幹(gan)機(ji)頭(tou)部(bu)時(shi),粒(li)子(zi)的(de)表(biao)麵(mian)溫(wen)度(du)低(di)於(yu)熱(re)風(feng)的(de)溫(wen)度(du),熱(re)風(feng)將(jiang)熱(re)量(liang)傳(chuan)遞(di)給(gei)粒(li)子(zi)。同(tong)時(shi)熱(re)風(feng)中(zhong)的(de)水(shui)氣(qi)分(fen)壓(ya)低(di)於(yu)粒(li)子(zi)表(biao)麵(mian)的(de)水(shui)氣(qi)分(fen)壓(ya),粒(li)子(zi)中(zhong)的(de)水(shui)被(bei)氣(qi)化(hua)並(bing)進(jin)入(ru)氣(qi)相(xiang),粒(li)子(zi)內(nei)部(bu)的(de)水(shui)分(fen)以(yi)液(ye)態(tai)或(huo)水(shui)氣(qi)的(de)形(xing)式(shi)擴(kuo)散(san)至(zhi)表(biao)麵(mian)。因(yin)此(ci),對(dui)流(liu)烘(hong)幹(gan)是(shi)一(yi)熱(re)、質反向傳遞的過程。
造粒機來的物料所帶水分有結合水和非結合水2種,整個烘幹過程可分為恒速烘幹與降速烘幹2個階段,每個階段的傳熱、chuanzhigeyoutedian。wuliaozhongdefeijieheshuiwulunqishuliangduoshao,suobiaoxiandexingzhijunyuyetaichunshuixiangtong,cishideqiyigujiechutongdaliangkongqiyudaliangshuijiechuyiyang,jingjiaoduandejiechushijianhou,wuliaobiaomianjidadaokongqideshiqiuwendu,zhiyaowuliaobiaomianquanbubeifeijieheshuisuofugai,honggansulvweidingzhi,wuliaobiaomianwenduyeweichizaidingzhi。yinci,zaicijieduanjishishizaigaowenxiayiyubianzhi、pohuaidewuliaorengranyunxuzaihengsujieduancaiyongjiaogaodehongganqiliuwendu,yitigaohonggansuduhereliyonglv。erzaijiangsujieduan,wuliaowenduzhujianshenggao,guzaihongganhouqibixuzhuyibushiwuliaodewenduguogao,yingduijiangsujieduandehonggantiaojianyangejiayikongzhi,fangzhiwuliaoyinghua、幹裂、起皺等不良現象的發生。
2、提高烘幹機熱利用率,降低磷銨成品水分的措施
2.1提高烘幹機的熱效率
烘hong幹gan機ji的de熱re效xiao率lv是shi用yong來lai衡heng量liang烘hong幹gan過guo程cheng熱re量liang利li用yong,率lv的de指zhi標biao,其qi值zhi是shi烘hong幹gan機ji內nei水shui分fen汽qi化hua所suo需xu熱re量liang加jia上shang物wu料liao升sheng溫wen耗hao熱re與yu空kong氣qi在zai預yu熱re器qi中zhong所suo獲huo得de的de熱re量liang的de比bi值zhi,如ru果guo烘hong幹gan機ji內nei未wei補bu充chong加jia熱re,烘hong幹gan機ji熱re損sun失shi也ye可ke忽hu略lve的de情qing況kuang下xia可ke用yong下xia麵mian的de公gong式shi計ji算suan熱re效xiao率lv:
很顯然,要想提高熱效率就需提高烘幹機進出口氣體溫度差,也就是從提高預熱溫度t,及(ji)降(jiang)低(di)廢(fei)氣(qi)出(chu)口(kou)溫(wen)度(du)。人(ren)手(shou),而(er)降(jiang)低(di)廢(fei)氣(qi)出(chu)口(kou)溫(wen)度(du)就(jiu)應(ying)延(yan)長(chang)烘(hong)幹(gan)時(shi)間(jian)或(huo)增(zeng)加(jia)烘(hong)幹(gan)機(ji)的(de)填(tian)充(chong)率(lv)。若(ruo)延(yan)長(chang)烘(hong)幹(gan)時(shi)間(jian)則(ze)須(xu)增(zeng)加(jia)設(she)備(bei)容(rong)積(ji),這(zhe)樣(yang)做(zuo)投(tou)資(zi)大(da),原(yuan)則(ze)上(shang)是(shi)不(bu)可(ke)取(qu)的(de),因(yin)此(ci),隻(zhi)有(you)增(zeng)加(jia)烘(hong)幹(gan)機(ji)的(de)填(tian)充(chong)率(lv),使(shi)物(wu)料(liao)在(zai)烘(hong)幹(gan)機(ji)內(nei)形(xing)成(cheng)完(wan)整(zheng)的(de)料(liao)幕(mu),能(neng)與(yu)熱(re)空(kong)氣(qi)最(zui)大(da)限(xian)度(du)地(di)接(jie)觸(chu),提(ti)高(gao)熱(re)利(li)用(yong)率(lv)。烘(hong)幹(gan)機(ji)內(nei)物(wu)料(liao)料(liao)幕(mu)形(xing)成(cheng)的(de)好(hao)壞(huai)主(zhu)要(yao)由(you)烘(hong)幹(gan)機(ji)內(nei)物(wu)料(liao)量(liang)、烘幹機抄板數、烘幹機抄板結構、烘(hong)幹(gan)機(ji)轉(zhuan)速(su)決(jue)定(ding),而(er)烘(hong)幹(gan)機(ji)物(wu)料(liao)的(de)多(duo)少(shao)及(ji)烘(hong)幹(gan)機(ji)轉(zhuan)速(su)受(shou)設(she)備(bei)容(rong)積(ji)及(ji)電(dian)機(ji)的(de)影(ying)響(xiang)。因(yin)此(ci),我(wo)廠(chang)對(dui)烘(hong)幹(gan)機(ji)抄(chao)板(ban)的(de)數(shu)量(liang)及(ji)結(jie)構(gou)做(zuo)了(le)改(gai)進(jin),首(shou)先(xian)增(zeng)加(jia)部(bu)分(fen)抄(chao)板(ban),其(qi)次(ci)對(dui)抄(chao)板(ban)的(de)結(jie)構(gou)做(zuo)如(ru)下(xia)改(gai)動(dong),中(zhong)間(jian)間(jian)隔(ge)1塊2折抄板,2邊的將2折抄板改為3折,使得烘幹機內的物料可以在左右2麵都產生料幕。目前在返料量、電(dian)機(ji)轉(zhuan)速(su)不(bu)變(bian)的(de)情(qing)況(kuang)下(xia),烘(hong)幹(gan)機(ji)內(nei)形(xing)成(cheng)的(de)料(liao)幕(mu)相(xiang)當(dang)好(hao)。同(tong)時(shi)過(guo)程(cheng)中(zhong)也(ye)必(bi)須(xu)注(zhu)意(yi)尾(wei)氣(qi)溫(wen)度(du)不(bu)能(neng)過(guo)低(di),以(yi)防(fang)達(da)到(dao)尾(wei)氣(qi)的(de)露(lu)點(dian),堵(du)塞(sai)管(guan)道(dao),因(yin)此(ci),應(ying)控(kong)製(zhi)尾(wei)氣(qi)溫(wen)度(du)比(bi)烘(hong)幹(gan)機(ji)進(jin)口(kou)氣(qi)體(ti)的(de)濕(shi)球(qiu)溫(wen)度(du)高(gao)20—50℃。
同樣,提高烘幹機進口氣體溫度也可以提高熱效率,但溫度過高會使物料逸出過多的氨,將增大烘幹洗滌器中的n(N)/n(P),給洗滌係統的運行帶來困難。設計時烘幹機的進口氣體溫度在200℃以下,如果用預中和工藝生產DAP,在維持負荷不變的情況下,如此低的進口氣體溫度要使成品水分降到2%是不可能的。目前此套裝置所用工藝為單管式反應器工藝,進口氣體溫度控製在180~250℃之間就能使成品水分達到國標。但有時因酸質發生變化,導致烘幹機進口氣體溫度可能超過250℃,由(you)於(yu)溫(wen)度(du)高(gao)可(ke)能(neng)導(dao)致(zhi)熱(re)風(feng)風(feng)管(guan)結(jie)料(liao),也(ye)可(ke)能(neng)使(shi)烘(hong)幹(gan)機(ji)頭(tou)物(wu)料(liao)局(ju)部(bu)過(guo)熱(re)而(er)生(sheng)成(cheng)焦(jiao)磷(lin)銨(an),影(ying)響(xiang)產(chan)品(pin)質(zhi)量(liang),並(bing)使(shi)烘(hong)幹(gan)機(ji)頭(tou)部(bu)抄(chao)板(ban)結(jie)料(liao)。因(yin)此(ci),將(jiang)烘(hong)幹(gan)機(ji)頭(tou)部(bu)抄(chao)板(ban)數(shu)從(cong)12塊減為6塊kuai,適shi當dang降jiang低di烘hong幹gan機ji進jin口kou處chu物wu料liao的de料liao幕mu,同tong時shi通tong過guo對dui烘hong幹gan風feng管guan先xian擴kuo大da後hou縮suo小xiao的de改gai造zao,熱re風feng風feng速su增zeng大da後hou,烘hong幹gan係xi統tong的de運yun轉zhuan率lv得de到dao了le較jiao大da幅fu度du的de提ti高gao。
2.2減少濕線帶入造粒機的水分
選用預中和工藝時,帶人造粒係統的水分可能達到30%左右,此時將水分降到2%很困難,烘幹耗煤量相當大,負荷也受影響。而單管式反應器工藝帶人造粒係統的水分可降到2%~4%,這樣將成品水分烘幹到2%以下就容易得多,煤耗也大幅減少。
在生產中有時會出現一種情況,即烘幹機進口氣體溫度很高,噴射風機、烘幹風機風門開度最大,而烘幹機尾氣溫度卻很低。造成此種情況可能有以下幾種原因:
(1)烘幹洗滌器液位過高 cishisuiransuoyoufengmendouyikaidaozuida,danyouyukongjianbeixidiyezhanju,daozhifengliangbugou,yanzhongshihuiduifengjizaochengwufamibudesunshi。youqidanghongganxidiqiyeweijixianshipiandishigengrongyichuxiancizhongqingkuang。bimiancileixianxiang,shouxianxutigaocaozuogongdezerenxin,kongzhihaohongganxidiqideyewei,dangyeweijishilingshi,jishijianghongganxidiqizhongbufenxidiyepairendicao,guanchawendujifengguanfuyayouwubianhua,ruguohongganweiqiwendushenggaojifuyashangshengjiubiaomingpanduanzhengque,yingjixujiangxidiyepairudicaozhidaohuifuzhengchang。cizhongqingkuangyekeyitongguobengjinkouyalibiaoxianshilaipanduan。
(2)返料過大 太(tai)多(duo)的(de)返(fan)料(liao)會(hui)造(zao)成(cheng)烘(hong)幹(gan)機(ji)內(nei)風(feng)速(su)受(shou)阻(zu),這(zhe)可(ke)以(yi)直(zhi)觀(guan)地(di)通(tong)過(guo)烘(hong)幹(gan)機(ji)電(dian)流(liu)顯(xian)示(shi)來(lai)判(pan)斷(duan),如(ru)果(guo)烘(hong)幹(gan)機(ji)電(dian)流(liu)太(tai)高(gao)就(jiu)很(hen)可(ke)能(neng)是(shi)此(ci)種(zhong)情(qing)況(kuang)。這(zhe)時(shi)隻(zhi)有(you)設(she)法(fa)減(jian)少(shao)係(xi)統(tong)的(de)返(fan)料(liao)量(liang),將(jiang)合(he)格(ge)粒(li)子(zi)盡(jin)可(ke)能(neng)送(song)去(qu)包(bao)裝(zhuang),同(tong)時(shi)降(jiang)低(di)負(fu)荷(he)生(sheng)產(chan),直(zhi)到(dao)指(zhi)標(biao)恢(hui)複(fu)正(zheng)常(chang)。
(3)熱風風管堵塞 如(ru)果(guo)不(bu)是(shi)以(yi)上(shang)兩(liang)種(zhong)情(qing)況(kuang)就(jiu)有(you)可(ke)能(neng)是(shi)進(jin)烘(hong)幹(gan)機(ji)的(de)熱(re)風(feng)風(feng)管(guan)發(fa)生(sheng)堵(du)塞(sai),應(ying)立(li)即(ji)停(ting)車(che)清(qing)理(li)。另(ling)外(wai)一(yi)種(zhong)可(ke)能(neng)是(shi)風(feng)機(ji)葉(ye)輪(lun)等(deng)其(qi)它(ta)設(she)備(bei)存(cun)在(zai)隱(yin)患(huan),但(dan)以(yi)上(shang)幾(ji)種(zhong)情(qing)況(kuang)是(shi)生(sheng)產(chan)中(zhong)經(jing)常(chang)可(ke)能(neng)出(chu)現(xian)的(de)。
3、小結
為了提高烘幹機熱利用率,降低產品水分,生產過程控製中應注意以下方麵:
(1)在(zai)不(bu)影(ying)響(xiang)造(zao)粒(li)機(ji)物(wu)料(liao)成(cheng)粒(li)的(de)情(qing)況(kuang)下(xia),適(shi)當(dang)提(ti)高(gao)造(zao)洗(xi)液(ye)的(de)密(mi)度(du)對(dui)降(jiang)低(di)烘(hong)幹(gan)能(neng)耗(hao)所(suo)起(qi)到(dao)的(de)作(zuo)用(yong)不(bu)可(ke)低(di)估(gu),即(ji)生(sheng)產(chan)過(guo)程(cheng)中(zhong)應(ying)盡(jin)可(ke)能(neng)減(jian)少(shao)帶(dai)人(ren)造(zao)粒(li)係(xi)統(tong)的(de)水(shui)分(fen)。
(2)weilechongfenliyongdanguanfanyingqishengchanshizaolijineiwendugaodetedianlaijinkenengchuqugengduodeshuifen,yingshidangyanchangwuliaozaizaolijineidetingliushijianjixingchenggengchongfendeliaomu,rangzaolijijianyouhongganjidezuoyong。xianzaizaolijidangquangaoduwei380 mm左右,適當提高造粒機擋圈高度到420mm左右(應計算造粒機電機的負荷能否適用),keyizengdazaolijineiwuliaodetianchonglv,jiadazaolijineiliaomudemianji,shideguanshifanyingqicaokoupenchulaideliaojiangzuidaxiandudiyuliaomujiechu,bimianzhijiepenzaizaolijineijiaobanshangchanshengdaliao,bingnengtigaozaolijineiwuliaodeguanghuadu。ciwai,zaizaolijigudingjiaopidegangbanshanganzhuang2~3塊抄板,也可以使管式反應器槽口噴出來的料漿與造粒機內物料料幕接觸更加充分。
(3)我廠此套裝置烘幹機的抄板均是T型抄板,其中有2折的也有3折的,每2塊3折的中間有1塊2折(zhe)的(de)抄(chao)板(ban),雖(sui)然(ran)烘(hong)幹(gan)機(ji)內(nei)物(wu)料(liao)料(liao)幕(mu)已(yi)經(jing)足(zu)夠(gou)大(da),但(dan)仍(reng)有(you)部(bu)分(fen)物(wu)料(liao)在(zai)烘(hong)幹(gan)過(guo)程(cheng)中(zhong)不(bu)能(neng)形(xing)成(cheng)料(liao)幕(mu)而(er)是(shi)沿(yan)著(zhe)烘(hong)幹(gan)機(ji)內(nei)壁(bi)直(zhi)接(jie)出(chu)去(qu),對(dui)烘(hong)幹(gan)效(xiao)果(guo)有(you)一(yi)定(ding)的(de)影(ying)響(xiang)。根(gen)據(ju)烘(hong)幹(gan)原(yuan)理(li),在(zai)恒(heng)速(su)烘(hong)幹(gan)階(jie)段(duan)應(ying)該(gai)使(shi)物(wu)料(liao)充(chong)分(fen)形(xing)成(cheng)料(liao)幕(mu)才(cai)有(you)利(li)於(yu)烘(hong)幹(gan),因(yin)此(ci),建(jian)議(yi)改(gai)進(jin)烘(hong)幹(gan)機(ji)頭(tou)部(bu)第(di)2、3圈部分抄板,將1/4的T型抄板兩頭口封起來成為盒式抄板(盒式抄板主要是盡量減少物料順著烘幹機內壁走,將2折抄板兩端封起來所得),如圖2所示(順著烘幹機內壁的兩頭)使大部分物料最大可能地形成料幕,增加烘幹效果。目前大部分物料在烘幹機內形成了較好的料幕,烘幹效果較好。
(4)當空氣濕度大時,適當將噴射風機風門關小,以減少熱風係統進入烘幹機的水分;反之當空氣濕度小時,可以加大噴射風機的風門,采用低溫大風量進行物料烘幹。
筆者對怎樣提高烘幹機的烘幹效率、降低煤耗談了一點自己的看法,希望對其他企業磷銨生產過程中烘幹效率的提高能有所幫助。
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