1. Inkqubo yokomisa ifilimu encinci ihamba
Inkqubo ye-sludge medium: i-sludge emanzi efumana umgqomo + impompo yokuhanjiswa kodaka + isomisi bhanyabhanya esibhityileyo + isixhobo sokukhupha udaka esinesiqingatha esomileyo + isisomisi esinemigca + epholileyo yemveliso.
Inkqubo yokukhupha igesi ephakathi: umphunga ophuma ngumphunga (umphunga oxutyiweyo)+ ibhokisi yerhasi yenkunkuma + icondenser + inkungu yokuphelisa inkungu + eyenzelwe idrafti yefeni + isixhobo sokuvumba.
I-sludge kwi-sludge yokufumana umgqomo ithunyelwa ngokuthe ngqo kwi-dryer yefilimu ebhityileyo ngepompo ye-sludge screw yokomisa unyango. I-sludge inlet yesomisi esincinci sefilimu sixhotyiswe nge-valve yesango ye-knife ye-pneumatic, edibeneyo kunye nemilinganiselo yokulawula ingqiqo yempompo yokutya, i-screw yokutya, ukhuseleko lokukhusela ifilimu ebhityileyo kunye nezinye izixhobo kunye nezixhobo zokubona.
Imodeli yomzimba yomshini wokomisa ifilimu, ubunzima bomshini omnye yi-33 000 kg, ubungakanani bomnatha besixhobo yi-Φ1 800 × 15 180, ukuhlelwa okuthe tye kunye nofakelo, i-sludge engena kwi-dryer yefilimu encinci isasazwa ngokulinganayo kudonga olushushu lwesomisi nge-rotor ngexesha lokujikeleza kwi-rotor kwi-rotor ejikelezayo kwi-rotor ejikelezayo umphezulu wodonga olushushu, Kwaye phambili kwi-outlet ye-sludge, amanzi e-sludge ayaphuphuma kwinkqubo. Amasuntswana e-semi-dry sludge emva kokumiswa ukusuka kumaleko abhityileyo athunyelwa kwi-linear dryer nge-sludge conveyor (eyenziwe ngokwemfuno yokufuma kwemveliso ye-sludge), emva koko ungene kwi-sludge cooler. Imveliso ye-sludge ipholiswa ngumoya ohamba kwindawo epholileyo kunye namanzi okupholisa ahamba kwiqokobhe kunye ne-shaft ejikelezayo. Isiqulatho sokufuma sicuthiwe ukusuka kwi-80% ukuya kwi-35% (ubumanzi bodaka oluyi-35% yinkqubo yokulawula umda ophezulu wesixhobo esinye sesomisi sefilim esibhityileyo).
Irhasi ehambisa igesi ekhutshwe kwi-dryer yefilimu encinci iqulethe umphunga wamanzi amaninzi, uthuli kunye nomlinganiselo othile wegesi eguquguqukayo (ikakhulukazi i-H2S kunye ne-NH3). Ukuba ikhutshwe ngokuthe ngqo, iya kubangela iqondo elithile lokungcoliseka kwendalo. Ngoko ke, le projekthi iqwalasela inkqubo yokuqokelela igesi yokuthwala kunye ne-condenser kunye ne-mist remover ukususa uthuli kunye nomphunga wamanzi kwi-exhaust gas, echasene nolwalathiso lwentshukumo ye-sludge kwi-cylinder ejikelezayo. Umbhobho wegesi ophumayo ngaphezu kodaka ungena kwi-condenser, kwaye amanzi apholiswa phantsi kwi-evaporation yokukhupha igesi. Ngokutshintshana kobushushu obungathanga ngqo, amanzi okutshizwa asuswa ngokutshintsha ubushushu bepleyiti kunye nenqaba yokupholisa, ukuze kugcinwe amanzi kunye nokunciphisa ukukhutshwa kwelindle. Igesi engabonakaliyo (ixabiso elincinci lomphunga, i-N2, i-air and sludge volatiles) idlula kwi-demister. Ekugqibeleni, i-fan yedrafti ebangelwa yi-exhaust ikhutshwe kwisistim yokomisa ukuya kwisixhobo sokukhupha ivumba.
Imfuno yomthombo wobushushu imiselwe ukuba ibe ngumphunga, othatyathwe kuthungelwano lombhobho we-thermal coverage owakhiwe kufutshane nendawo yokuphunyezwa kweprojekthi. Iimeko zonikezelo lomphunga luxinzelelo lomphunga lwe-1.0MPa, ubushushu bomphunga we-180 ℃ kunye nonikezelo lomphunga lwe-2.5t / h.
2. Iiparamitha zezobugcisa zezixhobo eziphambili zenkqubo yokomisa ifilimu encinci
Ngokwemfuno yale projekthi, umthamo wonyango lwe-sludge yesethi enye yenkqubo yokomisa i-sludge izimisele ukuba yi-2.5t / h (ngokomxholo wokufuma we-80%), kunye nomthamo wokufuma kwe-sludge yi-35%. Umthamo wokunyanga udaka lwemihla ngemihla yesomisi sefilimu esicekethekileyo yi-60 t/d (ngokomxholo wokufuma we-80%), umthamo olinganisiweyo wokuba ngumphunga wesomiso sefilimu esicekethekileyo yi-1.731 t/h, indawo yokutshintshiselana ngobushushu yesomisi sefilimu esibhityileyo yi-50 m2, kunye nesiqulatho sokufuma se-sludge inlet kunye ne-3% yesiqulatho sokufuma yi-80% yokufuma. Umthombo wobushushu wesomisi sefilimu esibhityileyo ngumphunga ogcweleyo, kwaye umgangatho wonikezelo lomphunga ungeniswa kwamanye amazwe: ubushushu bomphunga yi-180 ℃, uxinzelelo lomphunga yi-1.0 MPa, ukusetyenziswa komphunga wesomisi sefilimu esibhityileyo yi-2.33t / h, kunye nenani lesomisi sefilimu esincinci si-2, enye yokusetyenziswa enye.
Umphunga ogcweleyo we-180 ℃ uthuthwa usiwe kwisixhobo sokomisa umgama ngombhobho woxinzelelo, kwaye usetyenziswa njengomthombo wobushushu ukufudumeza ngokungathanga ngqo udaka oluphantse lube manzi. Amanzi akwi-semi-dry sludge aphinda abe ngumphunga kwi-linear dryer. Ngokwemfuno yangempela yemveliso ye-sludge (ukuqala kunye nokuyeka), i-sludge yokugqibela inokufikelela kwi-10% yomswakama womswakama kwaye uye kwi-cooler yemveliso.
Umthamo wokucutshungulwa kwesomisi somgca ngu-0.769t / h (umswakama we-35%), ubushushu obulinganisiweyo ngu-0.214t / h, indawo yokutshintshiselana ngobushushu yi-50 m2, umxholo wokufuma we-sludge inlet ye-dryer linear yi-35%, umxholo wokufuma we-sludge outlet yi-10%, umgangatho we-steam we-steam 0 kwiqondo lobushushu le-steam 0. ℃, uxinzelelo lwe-steam yi-1.0 MPa, ukusetyenziswa kwe-steam ye-dryer eyodwa yomgca ngu-0.253 t / h, kwaye ubuninzi buxhotyiswe ngesethi enye.
Uhlobo lwesixhobo se-condenser yegesi yokuthwala yi-condenser ye-injection edibeneyo, kunye ne-air intake eyi-3 500 Nm3 / h, i-inlet gas ye-inlet ye-95 ~ 110 ℃, i-outlet yegesi ye-90 ~ 180 Nm3 / h, kunye ne-outlet yegesi ye-55 ℃.
Uhlobo lwezixhobo zomthwali wegesi owenziwe yidrafti fan yi-fan yoxinzelelo oluphezulu lwe-centrifugal, umthamo omkhulu wokufunxa umoya yi-400 Nm3 / h, uxinzelelo lomoya ngu-4.8 kPa, iiparamitha ezibonakalayo zomthuthi wegesi ephakathi: ubushushu ngu-45 ℃, ukufuma yi-80% ~ 100% yenkqubo emanzi iseti isethi yomoya omile kunye ne-1 equipped igesi eyomileyo.
Umthamo wokucubungula we-cooler yemveliso ngu-1.8t / h, ukushisa kwe-sludge inlet yi-110 ° C, ukushisa kwe-sludge ku-≤45 ° C, indawo yokutshintsha ubushushu yi-20 m2, kwaye ubuninzi buyiyunithi ye-1.
3. Uhlalutyo lokusetyenziswa kwamandla ezoqoqosho ngexesha lokugunyaziswa kwesomisi esincinci sefilimu
Emva kwesiqingatha senyanga sokugunyaziswa okukodwa kunye nokuhanjiswa kodaka lwenkqubo yokumisa ifilimu ebhityileyo, iziphumo zezi zilandelayo.
Umthamo woqwalaselo loyilo lwesisomisi sefilimu esibhityileyo esinye kule projekthi yi-60 t/d. Okwangoku, i-avareji yonyango lwe-sludge emanzi ngexesha lokugunyaziswa yi-50 t / d (umxholo wokufuma ngu-79%), ofikelele kwi-83% ye-sludge eyilelwe isikali sonyango lwesiseko esimanzi kunye ne-87.5% ye-sludge eyilwe isikali sonyango esomileyo.
Umyinge wokunyakama kodaka lwe semi-dry sludge oluveliswe sisomisi sefilimu esibhityileyo yi-36%, kwaye isiqulatho sokufuma sodaka oluphantse lube manzi athunyelwa kumazwe angaphandle sisisomisi somgca ngama-36%, nto leyo ihambelana nexabiso ekujoliswe kulo kwimveliso yoyilo (35%).
Ilinganiswe ngemitha yangaphandle egcwele umphunga kwindawo yokusebenzela yokumisa i-sludge, ukusetyenziswa komphunga ogcweleyo yi-25 t/d, kunye nethiyori iyonke yokusetyenziswa kobushushu bemihla ngemihla yobushushu obufihlakeleyo bomphunga womphunga yi-25 t×1 000×2 014.8 kJ/kg÷4.184 kJ =07 × 1.29 kJ = 1.184 kJ = 7. I-avareji yonke imihla engumphunga amanzi inkqubo yokomisa yi (50 t × 0.79)-[50 t × (1-0.79)]÷ (1-0.36)×1 000=23 875 kg/d, Emva koko ukusetyenziswa kobushushu kweyunithi yenkqubo yokomisa i-sludge yi-1.203 871kg 5/5 × 1 × 1.203 871 kg = 5 × 3 × 1 × 1. amanzi abe ngumphunga; Ngenxa yokuba inkqubo yokomisa i-sludge ixhomekeke kutshintsho lwesiqulatho sokunyakama kodaka olumanzi, umgangatho womphunga wangaphandle, kunye neempawu zesixhobo sothutho semveliso ye-semi-dry sludge kwiimfuno ze-granularity kunye nezinye izinto, kuyafuneka ukuba kunyuswe ixabiso leenguqu ezahlukeneyo kwixesha elizayo lomsebenzi wovavanyo lwexesha elide, ukuze ushwankathele ezona meko zibalaseleyo zokusebenza kunye nesalathiso soqoqosho lwenkqubo yokusetyenziswa kwamandla.