垃圾發(fā)電計(jì)算表格

1、第1頁共9頁垃垃圾圾焚焚燒燒計(jì)計(jì)算算序號(hào)項(xiàng) 目符號(hào)計(jì)算公式或依據(jù)單位數(shù)據(jù)數(shù)據(jù)數(shù)據(jù)數(shù)據(jù)一一垃垃圾圾元元素素分分析析值值設(shè)計(jì)值校核高值(風(fēng)機(jī)選型）校核低值設(shè)計(jì)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(jì)100.000100.000100.000100.00010收到基低位發(fā)熱量Qnet,arQnet,ar=339Car+1030Har-109(Oar-Sar)-MarkJ/kg5046.446308.544209.945526.24kcal/kg1205.551507.061005.721320.171000二二垃垃圾圾量量計(jì)計(jì)算算1100（一一） 天天垃垃圾圾焚焚燒燒量量Wd工程設(shè)計(jì)值t/d1000.001000.001000.001000.0012

3、001垃圾焚燒爐臺(tái)數(shù) z工程設(shè)計(jì)值臺(tái)2.002.002.002.002設(shè)計(jì)每小時(shí)垃圾焚燒量 t/hBj單臺(tái)焚燒爐工程設(shè)計(jì)值 Wd/24/zt/h20.8320.8320.8320.833設(shè)計(jì)每小時(shí)最大垃圾焚燒量Bjz1.1*Bjt/h22.9222.9222.9222.92三三燃燃燒燒計(jì)計(jì)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-0.0333OarNm3/kg1.5501.8781.3381.

4、6744理論濕空氣量Vw01.016V0Nm3/kg1.5751.9081.3591.7005爐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(shí)際干空氣量V0a*V0Nm3/kg2.6353.1922.2742.8457實(shí)際濕空氣量Va.w01.016*V0Nm3/kg2.6773.2432.3112.891含氧量8.6478.6478.6478.647第2頁共9頁（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)*NarNm3/kg1.22741.486

5、41.05991.32512三原子氣體容積V0RO21.866(Car+0.375*S轉(zhuǎn)*Sar)/100Nm3/kg0.31410.34950.31410.3178其中SO2V0SO21.866*0.375*S轉(zhuǎn)*Sar/100Nm3/kg0.00060.00060.00060.0006其中CO2V0CO21.866*Car/100Nm3/kg0.31350.34890.31350.31723NOV0NO0.016*NarNm3/kg0.00030.00030.00030.00034水蒸氣V0H2O0.111Har-0.00315Clar+0.0124Mar+0.0161*V0Nm3/kg0

6、.78350.85590.69660.83025燃燒產(chǎn)物理論干煙氣體積（干煙氣）V0dgV0N2+V0RO2+V0NO+V0HCLNm3/kg1.54401.83851.37651.64556燃燒產(chǎn)物理論濕煙氣體積(濕煙氣)V0wyV0N2+V0RO2+V0H2O+V0NO+V0HCLNm3/kg2.32742.69442.07312.47577實(shí)際燃燒產(chǎn)體積(干煙氣)VdgV0dg+(-1)*V0Nm3/kg2.62883.15282.31292.81708實(shí)際水蒸汽容積VH2OV0H2O+0.016*(-1)*V0Nm3/kg0.80080.87700.71160.84909實(shí)際燃燒產(chǎn)體積

7、(濕煙氣)Va.wgVdg+VH2ONm3/kg3.42964.02983.02453.665910HCL含量估算V0HCL0.631*Clar/100Nm3/kg0.00220.00220.00220.0022（三） 燃燃燒燒產(chǎn)產(chǎn)物物實(shí)實(shí)際際體體積積1當(dāng)?shù)卮髿鈮篜dMPa0.100.100.100.102氣壓修正系數(shù)Mp0.101325/PdMPa1.001.001.001.00一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(jì)入爐膛出口過?？諝庥?jì)算0.020.020.020.022爐膛漏風(fēng)系數(shù)py2不計(jì)入爐膛出口過剩空氣計(jì)算0.020.020.020.023爐膛出口煙氣溫度TGT8

8、50.00850.00850.00850.004爐膛出口燃燒產(chǎn)物的體積(標(biāo)態(tài)、濕煙氣)VpydwVa.wgNm3/kg3.434.033.023.675爐膛出口煙氣量（標(biāo)態(tài)、濕煙氣）Qpy1000*Bjz*VpydwNm3/h78595.1592349.5469312.3584011.356爐膛出口煙氣量（實(shí)際、濕煙氣）Vpy1Mp*Qpy*(273+TGT)/273m3/h324281.44381031.70285980.86346628.547爐膛出口燃燒產(chǎn)物的實(shí)際體積(干煙氣)VpydgVdgNm3/kg2.633.152.312.828爐膛出口煙氣量（標(biāo)態(tài)、干煙氣）Qpg1000*Bj

9、z*VpydgNm3/h60243.1972252.4453004.2764555.299爐膛出口煙氣量（實(shí)際、干煙氣）Vpy2Mp*Qpg*(273+TGT)/273m3/h248561.77298111.60218694.19266353.36二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)py30.030.030.030.032余熱鍋爐出口煙氣溫度TYT220.00220.00220.00220.00第3頁共9頁3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*V0Nm3/kg3.484.093.073.724余熱鍋爐出口煙氣量（標(biāo)態(tài)、濕煙氣）V

10、ry11000*Bjz*VrydwNm3/h79677.6693661.1170246.7885180.335余熱鍋爐出口煙氣量（實(shí)際、濕煙氣）QrydwMp*Vry1*(273+TYT)/273m3/h144321.19169649.58127238.92154288.246余熱鍋爐出口燃燒產(chǎn)物的實(shí)際體積(干煙氣)VrydgVpydg*py3*V0Nm3/kg2.683.212.352.877余熱鍋爐出口煙氣量（標(biāo)態(tài)、干煙氣）Vry21000*Bjz*VrydgNm3/h61308.6673543.3553923.9965705.868余熱鍋爐出口煙氣量（實(shí)際、干煙氣）Qrydg1000*B

11、jz*Mp*Vry2*(273+TYT)/273m3/h111049.18133210.0297673.23119013.87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*V0Nm3/kg3.794.473.344.064除塵器出口煙氣量（標(biāo)態(tài)、濕煙氣）Vry11000*Bjz*VrydwNm3/h86894.44102404.8576476.3592973.515除塵器出口煙氣量（實(shí)際、濕煙氣）Q

12、rydwMp*Vry1*(273+TYT)/273m3/h135045.14159150.31118854.08144492.796除塵器出口燃燒產(chǎn)物的實(shí)際體積(干煙氣)VrydgVpydg+py4*V0Nm3/kg2.943.532.583.157除塵器出口煙氣量（標(biāo)態(tài)、干煙氣）Vry21000*Bjz*VrydgNm3/h67346.3280858.4959135.7472225.748除塵器出口煙氣量（實(shí)際、干煙氣）Qrydg1000*Bjz*Mp*Vry2*(273+TYT)/273m3/h104664.84125664.4991904.54112248.09三組組分分分分析析一一（實(shí)

13、實(shí)際際氧氧，濕濕態(tài)態(tài)，標(biāo)標(biāo)態(tài)態(tài)）體體積積濃濃度度1氮含量（實(shí)際氧，濕態(tài)，標(biāo)態(tài)） N2(V0N2+0.79*(+py3-1)*V0)/Vrydw%61.006962.864059.745161.61722二氧化硫（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）SO2V0SO2/Vrydw%0.01690.01440.01920.01583二氧化碳（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）CO2V0C02/Vrydw%9.01658.537810.22698.53444一氧化氮（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）NOV0N0/Vrydw(未脫硝)%0.00920.00780.01040.00865水汽容積（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）H2O(V0H2O+0.016

14、1*(+py3-1)*V0)/Vrydw%23.057421.482723.239522.86596氧含量（實(shí)際氧，濕態(tài)，標(biāo)態(tài)） O2(0.21*(+py3-1)*V0)/Vrydw%6.83327.04306.69046.90237氯化氫（實(shí)際氧，濕態(tài)，標(biāo)態(tài)） HCLV0HCL/Vrydw%0.06320.05370.07160.0591四組分分析二（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）質(zhì)量濃度1二氧化硫（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）SO2E78/22.4*64*10000mg/Nm3483.0243410.9096547.8721451.82092氯化氫（實(shí)際氧，濕態(tài)，標(biāo)態(tài)） HCLE83/22.4*36*100

15、00mg/Nm31015.0278863.48591151.2989949.45683氮氧化物（實(shí)際氧，濕態(tài)，標(biāo)態(tài)）以NO2計(jì) E80/22.4*46*10000mg/Nm3189.0056160.7874214.3803176.7958第4頁共9頁五組分分析三（實(shí)際氧，干態(tài)，標(biāo)態(tài)）質(zhì)量濃度1二氧化硫（實(shí)際氧，干態(tài)，標(biāo)態(tài)）SO2(E33/E62*100)/22.4*64*10000mg/Nm3627.7457523.3138713.7129585.73552氯化氫（實(shí)際氧，干態(tài)，標(biāo)態(tài)） HCL(E42/E62*100)/22.4*36*10000mg/Nm31319.14551099.6922

16、1499.79701230.86513氮氧化物（實(shí)際氧，干態(tài)，標(biāo)態(tài)）以NO2計(jì) (E35/E62*100)/22.4*46*10000mg/Nm3245.6345204.7707279.2732229.1961六（11%O2，干態(tài)，標(biāo)態(tài)）質(zhì)量濃度及達(dá)標(biāo)計(jì)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*10000mg/Nm3521.3493433.8803594.6187485.83342氯化氫（11%O2，干態(tài)，標(biāo)態(tài)） HCL(E42/(E37+(1-0.0161)*(2.1-1)*E

17、22)*100)/22.4*36*10000mg/Nm31095.5640911.75641249.53231020.93073氮氧化物（11%O2，干態(tài)，標(biāo)態(tài)）以NO2計(jì) (E35/(E37+(1-0.0161)*(2.1-1)*E22)*100)/22.4*46*10000mg/Nm3204.0020169.7757232.6720190.10484煙塵（11%O2，干態(tài)，標(biāo)態(tài)）(1*0.04*1000)/(E37+(1-0.0161)*(2.1-1)*E22)g/Nm312.417510.334214.162611.5716（二） 國(guó)家最新排放標(biāo)準(zhǔn)1二氧化硫（11%O2，干態(tài)，標(biāo)態(tài)）SO

18、2新國(guó)家標(biāo)準(zhǔn)GB 184852011(征求意見稿)mg/Nm380.0080.0080.0080.002氯化氫（11%O2，干態(tài)，標(biāo)態(tài)） HCL新國(guó)家標(biāo)準(zhǔn)GB 184852011(征求意見稿)mg/Nm350.0050.0050.0050.003氮氧化物（11%O2，干態(tài)，標(biāo)態(tài)）以NO2計(jì) 新國(guó)家標(biāo)準(zhǔn)GB 184852011(征求意見稿)mg/Nm3200.00200.00200.00200.004煙塵（11%O2，干態(tài)，標(biāo)態(tài)）新國(guó)家標(biāo)準(zhǔn)GB 184852011(征求意見稿)mg/Nm320.0020.0020.0020.005二氧化硫計(jì)算脫除效率(E94-E99)/E94%84.66%81.

19、56%86.55%83.53%6氯化氫計(jì)算脫除效率(E95-E100)/E95%95.44%94.52%96.00%95.10%7脫硝計(jì)算脫除效率(E96-E101)/E96%1.96%-17.80%14.04%-5.21%8除塵計(jì)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MPa（g）4.004.004.004.003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.

20、005汽包壓力Pk鍋爐廠家提供 =(F108-0.1)*1.1+0.1)MPa（a）4.394.394.394.396過熱蒸汽焓igrkj/kg3214.373214.373214.373214.377飽和爐水焓ikj/kg1114.721114.721114.721114.728給水焓igs5.5MPa,130kj/kg549.94549.94549.94549.949給水量Dg35.0043.6329.3038.28第5頁共9頁9機(jī)械未燃損失q機(jī)械本項(xiàng)目爐渣熱灼減率要求不大于3%3.003.003.003.0010排煙溫度Tpy鍋爐廠家提供200.00200.00200.00200.001

21、1鍋爐效率（低位發(fā)熱量）g鍋爐廠家提供0.790.790.790.7914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)Nm3/h49721.8960242.3442920.2353693.17220空氣焓值 25空氣焓值一次風(fēng)預(yù)熱器熱負(fù)荷kJ/h12713887.7315403965.7310974701.5613729342.74288.232.5二次熱

22、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)21309.3825818.1418394.3823011.36166空氣焓值 25空氣焓值二次風(fēng)預(yù)熱器熱負(fù)荷kJ/h3927319.144758284.073390084.644240993.13216.832.518冷空氣比熱Clkkj/kg.1.011.011.011.0119每公斤蒸汽吸熱量ig(igr-igs)+ps(i-igs)kj/kg2675.732675.732675.732675.7320鍋爐蒸發(fā)量Do(g*Bj*Qnet,ar)/ig 加一、二次風(fēng)熱量t/h34.3242.7728.7

23、237.5321飛灰量爐排為垃圾量的2%5%，流化床為8%12%t/h0.920.920.920.92八八汽汽輪輪發(fā)發(fā)電電機(jī)機(jī)組組功功率率計(jì)計(jì)算算1汽水損失率1取值0.030.030.030.032汽輪機(jī)進(jìn)汽量D1zDg（1-1）t/h66.5782.9855.7272.813汽機(jī)進(jìn)中壓蒸汽壓力(a)p1Mpa3.803.803.803.804汽機(jī)進(jìn)中壓蒸汽溫度t1395.00395.00395.00395.005汽機(jī)進(jìn)中壓蒸汽焓h1查表kJ/kg3206.113206.113206.113206.116凝結(jié)水焓0.539MPa，31.8133.75133.75133.75133.757一級(jí)抽

24、汽壓力（空預(yù)器）MPa1.2091.2091.2091.2098一級(jí)抽汽溫度（空預(yù)器）293.97293.97293.97293.979一級(jí)抽汽焓（空預(yù)器）kJ/kg3033.023033.023033.023033.0210空氣預(yù)熱器疏水焓值0.12MPa，80kJ/kg335.01335.01335.01335.0111一級(jí)抽汽流量（空預(yù)器）t/h7.989.676.898.6112二級(jí)抽汽參數(shù)焓值(除氧器）0.582MPa，224.1kJ/kg2903.562903.562903.562903.5613二級(jí)抽汽量(除氧器）t/h6.027.505.046.58第6頁共9頁14低加出水參數(shù)

25、焓值0.538MPa，80.1kJ/kg335.76335.76335.76335.7615低加疏水參數(shù)焓值0.0537MPa，83.1kJ/kg347.96347.96347.96347.9616低加抽汽參數(shù)焓值0.058MPa，85.2kJ/kg2651.712651.712651.712651.7117低加抽汽量t/h4.755.953.965.2118汽機(jī)排汽壓力pp0.004750.004750.004750.0047519汽機(jī)排汽溫度tp31.9731.9731.9731.9720汽機(jī)排蒸汽焓查表kJ/kg2559.132559.132559.132559.1321汽機(jī)排飽和水焓查

26、表kJ/kg133.96133.96133.96133.9622排汽干度0.950.950.950.9523汽機(jī)排汽焓hp查表kJ/kg2437.872437.872437.872437.8724汽輪發(fā)電機(jī)組機(jī)電效率jd取值0.920.920.920.9225汽輪機(jī)組發(fā)電功率P Pjd*(D1-D2)(h1-hp)+D2(h1-h2)/3.6kW11010.4211010.4213763.7513763.759185.589185.5812057.1212057.1226機(jī)組利用小時(shí)數(shù)H3已知8000.008000.008000.008000.0027廠用電率0.200.180.200.202

27、8年發(fā)電量P(a)PH3kWh88083337.81110109999.0373484657.3096456954.3429年供電量P(g)P(a)(1-)kWh70466670.2590290199.2158787725.8477165563.4730每噸垃圾發(fā)電量Kw/t264.25330.33220.45289.3731每噸垃圾上網(wǎng)電量Kw/t211.40270.87176.36231.5032處理每噸垃圾耗電量t/kwh52.8559.4644.0957.8733汽耗率kg/kwh6.056.036.076.04九九鍋鍋爐爐空空氣氣流流量量計(jì)計(jì)算算(一) 標(biāo)態(tài)風(fēng)量1過?？諝庀禂?shù)F鍋爐廠

28、資料2.002.002.002.001.1送風(fēng)量（實(shí)際）QFBj103V0(273+tlk)/273 (P0/P)m3/h76465.2092644.1566005.2082572.461.2送風(fēng)量（標(biāo)態(tài)）FBj103V0m3/h71031.2786060.4861314.6176704.522一次風(fēng)量VS1燃燒空氣計(jì)算70%QNm3/h49721.8960242.3442920.2353693.172.1一次風(fēng)量(熱風(fēng))VS1r燃燒空氣計(jì)算70%QNm3/h51142.5261963.5544146.5255227.262二次風(fēng)量（冷風(fēng)）VS2燃燒空氣計(jì)算30%QNm3/h21309.382

29、5818.1418394.3823011.362.1二次風(fēng)量（熱風(fēng)）VS2r燃燒空氣計(jì)算30%QNm3/h19888.7624096.9417168.0921477.27第7頁共9頁3爐排密封風(fēng)燃燒空氣計(jì)算10%QNm3/h7103.138606.056131.467670.45(二） 實(shí)際風(fēng)量1一次風(fēng)總量(冷風(fēng))VS1Mp*VS1*(273+t1k)/273m3/h53525.6464850.9046203.6457800.721.1一次風(fēng)量(熱風(fēng))VS1rMp*VS1r*(273+trk)/273m3/h92635.11112235.3879963.16100033.852二次風(fēng)量(冷風(fēng))VS2Mp*VS2*(273+t1k)/273m3/h22939.5627793.2419801.5624771.742.1二次風(fēng)量(熱風(fēng))VS2rMp*VS2r*(273+trk)/273m3/h22939.5627793.2419801.5624771.74十十風(fēng)風(fēng)機(jī)機(jī)選選