1、第1頁共8頁垃垃圾圾焚焚燒燒計計算算序號項 目符號計算公式或依據(jù)數(shù)據(jù)數(shù)據(jù)數(shù)據(jù)數(shù)據(jù)單位一一垃垃圾圾元元素素分分析析值值設(shè)計值校核高值(風(fēng)機選型）校核低值設(shè)計值1應(yīng)用基碳Car垃圾元素分析16.80018.70016.80017.0002應(yīng)用基氫Har垃圾元素分析1.8002.4001.0002.2003應(yīng)用基氧Oar垃圾元素分析12.78012.78012.78012.7804應(yīng)用基氮Nar垃圾元素分析0.4000.4000.4000.4005應(yīng)用基硫Sar垃圾元素分析0.1400.1400.1400.1406應(yīng)用基氯Clar垃圾元素分析0.3480.3480.3480.3487應(yīng)用基水份Mar

2、垃圾元素分析45.00045.00045.50045.0008應(yīng)用基灰份Aar垃圾元素分析22.73220.23223.03222.132合計100.000100.000100.000100.00010收到基低位發(fā)熱量Qnet,arQnet,ar=339Car+1030Har-109(Oar-Sar)-Mar5046.446308.544209.945526.24kj/kg1205.551507.061005.721320.17kcal/kg二二垃垃圾圾量量計計算算（一一） 天天垃垃圾圾焚焚燒燒量量Wd工程設(shè)計值1000.001000.001000.001000.00t/d1設(shè)計每小時垃圾焚燒

3、量Bj單臺焚燒爐工程設(shè)計值 Wd/24/220.8320.8320.8320.83t/h2設(shè)計每小時最大垃圾焚燒量Bjz1.1*Bj22.9222.9222.9222.92t/h三三燃燃燒燒計計算算1NOXNOX轉(zhuǎn)轉(zhuǎn)化化率率0.0500.0500.0500.0502SOXSOX的的轉(zhuǎn)轉(zhuǎn)化化率率0.6000.6000.6000.6003理論干空氣量V00.0889(Car+0.375Sar)+0.265Har+0.008*N轉(zhuǎn)化率Nar-0.0333Oar1.5501.8781.3381.674Nm3/kg4理論濕空氣量Vw01.016V01.5751.9081.3591.700Nm3/kg5爐

4、膛出口過量空氣系數(shù)傳統(tǒng)焚燒爐排取值范圍1.61.8（新型燃燒技術(shù)為1.31.4）氧含量7-9%1.7001.7001.7001.7006實際干空氣量V0a*V02.6353.1922.2742.845Nm3/kg7實際濕空氣量Va.w01.016*V02.6773.2432.3112.891Nm3/kg1.7001.7001.7001.700含氧量8.6478.6478.6478.647第2頁共8頁0.0000.0000.0000.000（二） 燃燃燒燒產(chǎn)產(chǎn)物物理理論論體體積積1氮容積V0N20.79*V0+0.008*(1-N轉(zhuǎn)化率)*Nar1.22741.48641.05991.3251N

5、m3/kg2三原子氣體容積V0RO21.866(Car+0.375*S轉(zhuǎn)*Sar)/1000.31410.34950.31410.3178Nm3/kg其中SO2V0SO21.866*0.375*S轉(zhuǎn)*Sar/1000.00060.00060.00060.0006Nm3/kg其中CO2V0CO21.866*Car/1000.31350.34890.31350.3172Nm3/kg3NOV0NO0.016*Nar0.00030.00030.00030.0003Nm3/kg4水蒸氣V0H2O0.111Har-0.00315Clar+0.0124Mar+0.0161*V00.78350.85590.6

6、9660.8302Nm3/kg5燃燒產(chǎn)物理論干煙氣體積（干煙氣）V0dgV0N2+V0RO2+V0NO+V0HCL1.54401.83851.37651.6455Nm3/kg6燃燒產(chǎn)物理論濕煙氣體積(濕煙氣)V0wyV0N2+V0RO2+V0H2O+V0NO+V0HCL2.32742.69442.07312.4757Nm3/kg7實際燃燒產(chǎn)體積(干煙氣)VdgV0dg+(-1)*V02.62883.15282.31292.8170Nm3/kg8實際水蒸汽容積VH2OV0H2O+0.016*(-1)*V00.80080.87700.71160.8490Nm3/kg9實際燃燒產(chǎn)體積(濕煙氣)Va.

7、wgVdg+VH2O3.42964.02983.02453.6659Nm3/kg10HCL含量估算V0HCL0.631*Clar/1000.00220.00220.00220.0022Nm3/kg（三） 燃燃燒燒產(chǎn)產(chǎn)物物實實際際體體積積1當(dāng)?shù)卮髿鈮篜d0.100.100.100.10MPa2氣壓修正系數(shù)Mp0.101325/Pd1.001.001.001.00MPa一焚焚燒燒爐爐出出口口煙煙氣氣量量1爐排漏風(fēng)系數(shù)py1不計入爐膛出口過剩空氣計算0.020.020.020.022爐膛漏風(fēng)系數(shù)py2不計入爐膛出口過剩空氣計算0.020.020.020.023爐膛出口煙氣溫度TGT850.00850

8、.00850.00850.004爐膛出口燃燒產(chǎn)物的體積(標(biāo)態(tài)、濕煙氣)VpydwVa.wg3.434.033.023.67Nm3/kg5爐膛出口煙氣量（標(biāo)態(tài)、濕煙氣）Qpy1000*Bjz*Vpydw78595.1592349.5469312.3584011.35Nm3/h6爐膛出口煙氣量（實際、濕煙氣）Vpy1Mp*Qpy*(273+TGT)/273324281.44381031.70285980.86346628.54m3/h7爐膛出口燃燒產(chǎn)物的實際體積(干煙氣)VpydgVdg2.633.152.312.82Nm3/kg8爐膛出口煙氣量（標(biāo)態(tài)、干煙氣）Qpg1000*Bjz*Vpydg6

9、0243.1972252.4453004.2764555.29Nm3/h9爐膛出口煙氣量（實際、干煙氣）Vpy2Mp*Qpg*(273+TGT)/273248561.77298111.60218694.19266353.36m3/h二余余熱熱爐爐出出口口煙煙氣氣量量1余熱鍋爐漏風(fēng)系數(shù)py30.030.030.030.03第3頁共8頁2余熱鍋爐出口煙氣溫度TYT220.00220.00220.00220.003余熱鍋爐出口燃燒產(chǎn)物的體積(標(biāo)態(tài)、濕煙氣) VrydwVpydw+1.016*py3*V03.484.093.073.72Nm3/kg4余熱鍋爐出口煙氣量（標(biāo)態(tài)、濕煙氣）Vry11000*

10、Bjz*Vrydw79677.6693661.1170246.7885180.33Nm3/h5余熱鍋爐出口煙氣量（實際、濕煙氣）QrydwMp*Vry1*(273+TYT)/273144321.19169649.58127238.92154288.24m3/h6余熱鍋爐出口燃燒產(chǎn)物的實際體積(干煙氣)VrydgVpydg*py3*V02.683.212.352.87Nm3/kg7余熱鍋爐出口煙氣量（標(biāo)態(tài)、干煙氣）Vry21000*Bjz*Vrydg61308.6673543.3553923.9965705.86Nm3/h8余熱鍋爐出口煙氣量（實際、干煙氣）Qrydg1000*Bjz*Mp*Vr

11、y2*(273+TYT)/273111049.18133210.0297673.23119013.87m3/h除除塵塵器器出出口口煙煙氣氣量量1除塵器漏風(fēng)系數(shù)py40.200.200.200.202除塵器出口煙氣溫度TYT150.00150.00150.00150.003除塵器出口燃燒產(chǎn)物的體積(標(biāo)態(tài)、濕煙氣)VrydwVpydw+1.016*py4*V03.794.473.344.06Nm3/kg4除塵器出口煙氣量（標(biāo)態(tài)、濕煙氣）Vry11000*Bjz*Vrydw86894.44102404.8576476.3592973.51Nm3/h5除塵器出口煙氣量（實際、濕煙氣）QrydwMp*V

12、ry1*(273+TYT)/273135045.14159150.31118854.08144492.79m3/h6除塵器出口燃燒產(chǎn)物的實際體積(干煙氣)VrydgVpydg+py4*V02.943.532.583.15Nm3/kg7除塵器出口煙氣量（標(biāo)態(tài)、干煙氣）Vry21000*Bjz*Vrydg67346.3280858.4959135.7472225.74Nm3/h8除塵器出口煙氣量（實際、干煙氣）Qrydg1000*Bjz*Mp*Vry2*(273+TYT)/273104664.84125664.4991904.54112248.09m3/h三組組分分分分析析一一（實實際際氧氧，濕濕

13、態(tài)態(tài)，標(biāo)標(biāo)態(tài)態(tài)）體體積積濃濃度度1氮含量（實際氧，濕態(tài)，標(biāo)態(tài)） N2(V0N2+0.79*(+py3-1)*V0)/Vrydw61.006962.864059.745161.6172%2二氧化硫（實際氧，濕態(tài)，標(biāo)態(tài)）SO2V0SO2/Vrydw0.01690.01440.01920.0158%3二氧化碳（實際氧，濕態(tài)，標(biāo)態(tài)）CO2V0C02/Vrydw9.01658.537810.22698.5344%4一氧化氮（實際氧，濕態(tài)，標(biāo)態(tài)）NOV0N0/Vrydw(未脫硝)0.00920.00780.01040.0086%5水汽容積（實際氧，濕態(tài)，標(biāo)態(tài)）H2O(V0H2O+0.0161*(+py3-

14、1)*V0)/Vrydw23.057421.482723.239522.8659%6氧含量（實際氧，濕態(tài)，標(biāo)態(tài)） O2(0.21*(+py3-1)*V0)/Vrydw6.83327.04306.69046.9023%7氯化氫（實際氧，濕態(tài)，標(biāo)態(tài)） HCLV0HCL/Vrydw0.06320.05370.07160.0591%四組分分析二（實際氧，濕態(tài)，標(biāo)態(tài)）質(zhì)量濃度1二氧化硫（實際氧，濕態(tài)，標(biāo)態(tài)）SO2E78/22.4*64*10000483.0243410.9096547.8721451.8209mg/Nm32氯化氫（實際氧，濕態(tài)，標(biāo)態(tài)） HCLE83/22.4*36*100001015.0

15、278863.48591151.2989949.4568mg/Nm3第4頁共8頁3氮氧化物（實際氧，濕態(tài)，標(biāo)態(tài)）以NO2計 E80/22.4*46*10000189.0056160.7874214.3803176.7958mg/Nm3五組分分析三（實際氧，干態(tài)，標(biāo)態(tài)）質(zhì)量濃度1二氧化硫（實際氧，干態(tài)，標(biāo)態(tài)）SO2(E33/E62*100)/22.4*64*10000627.7457523.3138713.7129585.7355mg/Nm32氯化氫（實際氧，干態(tài)，標(biāo)態(tài)） HCL(E42/E62*100)/22.4*36*100001319.14551099.69221499.79701230.

16、8651mg/Nm33氮氧化物（實際氧，干態(tài)，標(biāo)態(tài)）以NO2計 (E35/E62*100)/22.4*46*10000245.6345204.7707279.2732229.1961mg/Nm3六（11%O2，干態(tài)，標(biāo)態(tài)）質(zhì)量濃度及達(dá)標(biāo)計算（一） 初始排放濃度1二氧化硫（11%O2，干態(tài)，標(biāo)態(tài)）SO2(E33/(E37+(1-0.0161)*(2.1-1)*E22)*100)/22.4*64*10000521.3493433.8803594.6187485.8334mg/Nm32氯化氫（11%O2，干態(tài)，標(biāo)態(tài)） HCL(E42/(E37+(1-0.0161)*(2.1-1)*E22)*100)

17、/22.4*36*100001095.5640911.75641249.53231020.9307mg/Nm33氮氧化物（11%O2，干態(tài)，標(biāo)態(tài)）以NO2計 (E35/(E37+(1-0.0161)*(2.1-1)*E22)*100)/22.4*46*10000204.0020169.7757232.6720190.1048mg/Nm34煙塵（11%O2，干態(tài)，標(biāo)態(tài)）(1*0.04*1000)/(E37+(1-0.0161)*(2.1-1)*E22)12.417510.334214.162611.5716g/Nm3（二） 國家最新排放標(biāo)準(zhǔn)1二氧化硫（11%O2，干態(tài)，標(biāo)態(tài)）SO2新國家標(biāo)準(zhǔn)GB

18、 184852011(征求意見稿)80.0080.0080.0080.00mg/Nm32氯化氫（11%O2，干態(tài)，標(biāo)態(tài)） HCL新國家標(biāo)準(zhǔn)GB 184852011(征求意見稿)50.0050.0050.0050.00mg/Nm33氮氧化物（11%O2，干態(tài)，標(biāo)態(tài)）以NO2計 新國家標(biāo)準(zhǔn)GB 184852011(征求意見稿)200.00200.00200.00200.00mg/Nm34煙塵（11%O2，干態(tài)，標(biāo)態(tài)）新國家標(biāo)準(zhǔn)GB 184852011(征求意見稿)20.0020.0020.0020.00mg/Nm35二氧化硫計算脫除效率(E94-E99)/E9484.66%81.56%86.55%

19、83.53%6氯化氫計算脫除效率(E95-E100)/E9595.44%94.52%96.00%95.10%7脫硝計算脫除效率(E96-E101)/E961.96%-17.80%14.04%-5.21%8除塵計算脫除效率(E97*1000-E102)/(E97*1000)99.84%99.81%99.86%99.83%七鍋鍋爐爐蒸蒸發(fā)發(fā)量量t/h2過熱蒸汽壓力Pne鍋爐廠家提供4.004.004.004.00MPa（g）3過熱蒸汽溫度Tne鍋爐廠家提供400.00400.00400.00400.004給水溫度Tnl鍋爐廠家提供130.00130.00130.00130.005汽包壓力Pk鍋爐廠

20、家提供4.394.394.394.39MPa（a）6過熱蒸汽焓igr#NAME?#NAME?#NAME?#NAME?kj/kg7飽和爐水焓i#NAME?#NAME?#NAME?#NAME?kj/kg8給水焓igs7.85MPa,130#NAME?#NAME?#NAME?#NAME?kj/kg第5頁共8頁9給水量Dg#NAME?#NAME?#NAME?#NAME?9機械未燃損失q機械本項目爐渣熱灼減率要求不大于3%3.003.003.003.00%10排煙溫度Tpy鍋爐廠家提供200.00200.00200.00200.0011鍋爐效率（低位發(fā)熱量）g鍋爐廠家提供0.790.790.790.79

21、14燃燒室出口過剩空氣系數(shù)l鍋爐廠家提供1.701.701.701.7015鍋爐排污率ps鍋爐廠家提供0.020.020.020.0216冷空氣溫度Tlk20.0020.0020.0020.0017一次風(fēng)溫度Trk鍋爐廠家提供220.00220.00220.00220.00一次風(fēng)量Q一次風(fēng)49721.8960242.3442920.2353693.17Nm3/h一次風(fēng)預(yù)熱器熱負(fù)荷12713887.7315403965.7310974701.5613729342.74二次熱風(fēng)溫度Tek鍋爐廠家提供166.00166.00166.00166.00二次風(fēng)量Q二次風(fēng)21309.3825818.1418

22、394.3823011.36二次風(fēng)預(yù)熱器熱負(fù)荷3927319.144758284.073390084.644240993.1318冷空氣比熱Clk1.011.011.011.01kj/kg.19每公斤蒸汽吸熱量ig(igr-igs)+ps(i-igs)#NAME?#NAME?#NAME?#NAME?kj/kg20鍋爐蒸發(fā)量Do(g*Bj*Qnet,ar)/ig 加一、二次風(fēng)熱量#NAME?#NAME?#NAME?#NAME?t/h21飛灰量爐排為垃圾量的2%5%，流化床為8%12%0.920.920.920.92t/h八八汽汽輪輪發(fā)發(fā)電電機機組組功功率率計計算算1汽水損失率1取值0.030.0

23、30.030.032汽輪機進汽量D12Dg（1-1）#NAME?#NAME?#NAME?#NAME?t/h3汽機進中壓蒸汽壓力(a)p13.803.803.803.80Mpa4汽機進中壓蒸汽溫度t1395.00395.00395.00395.005汽機進中壓蒸汽焓h1查表#NAME?#NAME?#NAME?#NAME?kJ/kg6凝結(jié)水焓0.539MPa，31.8#NAME?#NAME?#NAME?#NAME?7一級抽汽壓力（空預(yù)器）1.2091.2091.2091.209MPa8一級抽汽溫度（空預(yù)器）293.97293.97293.97293.979一級抽汽焓（空預(yù)器）#NAME?#NAME

24、?#NAME?#NAME?kJ/kg10空氣預(yù)熱器疏水焓值0.12MPa，80#NAME?#NAME?#NAME?#NAME?kJ/kg11一級抽汽流量（空預(yù)器）#NAME?#NAME?#NAME?#NAME?t/h12二級抽汽參數(shù)焓值(除氧器）0.582MPa，224.1#NAME?#NAME?#NAME?#NAME?kJ/kg第6頁共8頁13二級抽汽量(除氧器）#NAME?#NAME?#NAME?#NAME?t/h14低加出水參數(shù)焓值0.538MPa，80.1#NAME?#NAME?#NAME?#NAME?kJ/kg15低加疏水參數(shù)焓值0.0537MPa，83.1#NAME?#NAME?#

25、NAME?#NAME?kJ/kg16低加抽汽參數(shù)焓值0.058MPa，85.2#NAME?#NAME?#NAME?#NAME?kJ/kg17低加抽汽量#NAME?#NAME?#NAME?#NAME?t/h18汽機排汽壓力pp0.004750.004750.004750.0047519汽機排汽溫度tp32.0032.0032.0032.0020汽機排蒸汽焓查表2270.002270.002270.002270.00kJ/kg21汽機排飽和水焓查表#NAME?#NAME?#NAME?#NAME?kJ/kg22排汽干度0.950.950.950.9523汽機排汽焓hp查表#NAME?#NAME?#N

26、AME?#NAME?kJ/kg24汽輪發(fā)電機組機電效率jd取值0.920.920.920.9225汽輪機組發(fā)電功率P Pjd*(D1-D2)(h1-hp)+D2(h1-h2)/3.6#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?kW26機組利用小時數(shù)H3已知8000.008000.008000.008000.0027廠用電率0.200.180.200.2028年發(fā)電量P(a)PH3#NAME?#NAME?#NAME?#NAME?kWh29年供電量P(g)P(a)(1-)#NAME?#NAME?#NAME?#NAME?kWh30每噸垃圾發(fā)電量#N

27、AME?#NAME?#NAME?#NAME?Kw/t31每噸垃圾上網(wǎng)電量#NAME?#NAME?#NAME?#NAME?Kw/t32處理每噸垃圾耗電量#NAME?#NAME?#NAME?#NAME?t/kwh#NAME?#NAME?#NAME?#NAME?九九鍋鍋爐爐空空氣氣流流量量計計算算(一) 標(biāo)態(tài)風(fēng)量1過剩空氣系數(shù)F鍋爐廠資料2.002.002.002.001.1送風(fēng)量（實際）QFBj103V0(273+tlk)/273 (P0/P)76465.2092644.1566005.2082572.46m3/h1.2送風(fēng)量（標(biāo)態(tài)）FBj103V071031.2786060.4861314.61

28、76704.52m3/h2一次風(fēng)量VS1燃燒空氣計算70%Q49721.8960242.3442920.2353693.17Nm3/h2.1一次風(fēng)量(熱風(fēng))VS1r燃燒空氣計算70%Q51142.5261963.5544146.5255227.26Nm3/h2二次風(fēng)量（冷風(fēng)）VS2燃燒空氣計算30%Q21309.3825818.1418394.3823011.36Nm3/h第7頁共8頁2.1二次風(fēng)量（熱風(fēng)）VS2r燃燒空氣計算30%Q19888.7624096.9417168.0921477.27Nm3/h3爐排密封風(fēng)燃燒空氣計算10%Q7103.138606.056131.467670.45Nm3/h(二） 實際風(fēng)量1一次風(fēng)總量(冷風(fēng))VS1Mp*VS1*(273+t1k)/27353525.6464850.9046203.6457800.72m3/h1.1一次風(fēng)量(熱風(fēng))VS1rMp*VS1r*(273+trk)/27392635.11112235.3879963.16100033.85m3/h2二次風(fēng)量(冷風(fēng))VS2Mp*VS2*(273+t1k)/27322939.5627793.2419801.5624771.74m3/h2.1二次風(fēng)量(熱風(fēng))VS2rMp*VS2r*(273+trk)/27322939.5627793.2419801.5624771.74m3/h十