托克托-DG-600MW 烟气焓温表计算-2010

托克托-DG-600MW 烟气焓温表计算-2010
托克托-DG-600MW 烟气焓温表计算-2010

5 空气、烟气、灰渣焓温表

V RO20.821V 0N2

3.461V 0H2O

0.549I RO2

I 0N2

I 0H2O

θc RO2θ,V RO2c RO2θc N2θ,V 0N2c N2θc H2O θ,V 0H2O c H2O θI y 0℃kJ/m 3kJ/kg kJ/m 3kJ/kg kJ/m 3kJ/kg kJ/kg 100170139129.6449150.583671200357293259.6899303.91671359300558458391.31354461.92542066400771633525.81820625.334327965009958176632295793.4435354760012211003802.62778965.6530431070014591198944.732701145.3629509680017011397109137761333.47325905900194816001241.542971521.583567321000219918061391.94818722.239670201100245420151542.453391922.8105584091200271322281692.958602127.6116892551300297224411847.663952340.81285101211400323526572006.4694525541402110041500349928742161.174802775.51523118771600376230902319.980302997.11645127651700403033102478.785793222.81769136581800429735292637.691293452.71895145541900456537492800.696933682.62021154642000483639722959.4102433920.82152163672100510841953122.5108084154.92280172832200

5380

4419

3285.5

11372

4393.2

2411

18202

V 0k

4.372G fh 0.27炉膛

I 0k

I fh

αpj

c k θ,θV 0k c k θc fh θ

G fh c fh θθ 1.205kJ/m 3℃kJ/kg kJ/kg kJ/kg ℃kJ/kg 132100577t lk 8021.6100810265.92001163℃16845.42001642402.1300175820.026070.23002497540.94002365理论冷空气焓35796.440033776835002986I 0lk 461124.55004284828.56003623kJ/kg 554149.66005203978.17004277115.4665179.670061531128.68004935770207.980071251279.19005593t rk 812219.290080981433.710006269350

1005271.4100085761592.611006963理论热空气焓1128304.61100101411751.4120076582061.6

1261340.51200111661910.3130083531426385.01300122182073.3140090651583427.41400132892236.3150097781777479.81500143612399.31600104911957528.41600154442562.31700112032206595.61700165502725.41800119162412651.21800176482892.61900126482625708.81900187653059.82000133792847768.720001987932272100141103078831.12100210073394.2

2200

14841

3319

896.1

2200

22140

飞灰焓计入烟气焓的判据

屏过高过后水吊高再后水引后后水转向室低再αpj

αpj αpj αpj 1.3 1.245 1.265 1.275kJ/kg kJ/kg kJ/kg kJ/kg 865834845851θ"l 17531689171217247422664256726022620I"l 36023472351935436561

4568440344634493554753485420545665596324高再进口焓640964527594

Q l

7322

742174708629186458322高再θ'843384899172理论燃烧温度8827

-745.98952901510803θa 10420

105591062911893℃11472高再θ"116251170213012188912552644.012719128031415113652高再I"138331392415290147525763.4

14948150461644015863160731617817614169981722217334187801812418363184821996719271195241965121150204142068120815223472157121854219952355022734

23031

23179

炉膛出口烟气焓

<1

低过主省旁省空预

αpjαpjαpjαpj

1.285 1.2925 1.2975 1.31

kJ/kg kJ/kg kJ/kg kJ/kg I'857861864871 1735174417501764θ'2637265126592681 66.43567358435963626高过4523I"45454560I"4598θ"5492552055385583 742.06495θ"65276548θ"6602 I"75205275577581527643 6879.78545858786158685 9078912591569235

10698107511078510872

11778118361187411970

12886129491299113095

14015140831412814241

15144152171526615388

16283163611641416545

17446175301758617726

18601186901875018899

19777198721993520093

20949210492111621283

22136222422231222489

23327234392351323698

空预空预

APH APH

θαpjαpjαpj

℃111θ100692692I'692 1252001404I'14041404

I py30021362136θ"2136 1094.44002893θ'2893 2.82893

50036721736723672

600446044604460 I700527652765276 1094800611361136113

900695169516951 101831000729172917291

1100871487148714

1200959695969596

1300105061050610506

1400114311143111431

1500123571235712357

1600132931329313293

1700142531425314253

1800152051520515205

1900161731617316173

2000171361713617136

2100181151811518115

2200190981909819098

θ

100 APH200θ"300

400 I"500 -20600

700

800

900

1000

1100θ"1200

1300 I"1400 -201500

1600

1700

1800

1900

2000

2100

2200

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