XX有限公司3th锅炉脱硫工程可行性研究报告.doc

1. 11.1.1 xxx3xxx3xxx3t/h1.1.2 xxx3xxx31.1.3 xxx3xxx31.1.4 xxx120200700XX1.2 1.2.1123GB13223-20034GB8978-19961.2.2.1xxxxxx2007102xxxxxx, xxx2007443xxxxxx, xxx2007621.2.3123xxx3t/h41.2.4 xxx3t/hxxx3xxx3xxx3t/h100%1.3 1.3.1 1.3.2 xxx3t/h12345 1.41xxx3xxx3xxx3t/hSO2234FGD567FGD1. 5xxx3xxx3xxxxxxxxx3t/hxxxxxx200710xxxxxx xxx200744xxxxxx xxx2007622008xxx3xxx3xxx3t/h1. 6xxxxxxxxx3xxx3xxx3t/hxxx1. 7589.831.7.181.7.2xxx3t/h 1.81.8.12xxx3xxx3SO2589.83SO22770t/a,141.3 t/a589.8333.839.291.8.21. 9 1. 589.832. 589.83 0.003. 176.37 4 141.125 33.836 1.427 8.468 25.37 1. % 5.74%2. % 5.98%3. % 10.67% 4. % 8.78% 5. 8.41 6. 9.29 7. 93.71 8. 26.66 9. BET % 53.43% 10. 1270%20051999185720001995200120022003215820052549.32168.438130%111pH4.026.7910392.8%80%22.5%pH5.68173.10%199012191992199581998112 1998217(19985)(1996124)20102000;pH4.5200020051()4611. 2xxx3xxx3xxxxxxxxx3t/hS02GB30951996 1998217(19985)(1996124)20102000;pH4.5200020051()4612. 2xxx3xxx3xxxxxxxxx3t/hS02GB30951996 TSP2.57l00%.GB38382001VSO2NH3N2H2CH4xxxxxx xxx200744xxxxxx xxx2007622008xxx3xxx3xxx3t/h 13. 113.1. 1xxxxxxxxx11343091140931334259335913xxxxxx251203929801.74 3.1.21xxx14.4727.543.410.4-20.6227267180726mm1238.5mm375.9mm6970%21215t/m20.25m160kPaxxx360m3/h1015m3.1.3pH 6.7 300mgL(CaCO3) 0.58gL 34.2mg/L(CaO) 140mgL(CaO) Cl- 60.1mgLS042- 88.6mg,/LNO3- 180mgLHC03- 80.3mgLNa+ 120mgLK+ l.2mg/LCa2+ 31.3mg/LMg2+ 36mg/LFe3+/Fe2+ 0.3mg/LSIO2 27.2mg/L(SIO2) 1320uS/cm14. 23.2.1 xxx3t/h10m3/h3.2.2 25KVA 380Vx429KVA.3.2.3 3.2xxx3t/h 4.1 4.1.1xxx3xxx31970xxxxxx1200300xxx 12153412MW20052.62.72343.98xxxxxx3xxx3122121xxx320341500t/h8500t/h96%xxx4.1.2xxx5Km700-800m 4.2 4.2.126MW1xUG-35/39-M62xYG-35/3.82-M33xYG-35/3.82-M64xTG-35/3.82-M12x4x1xN6-35-42xC6-3.43/1.2741x199012x199682x4x4-1 4-1 2x 4x t/h 35 35 MPa 3.82 3.82 450 450 150 150 150 150 % 75 87AGX35-1A15DAGX35-1A15D m3/h 30911 30911 Pa 14007 14007 kW 185 185AYX35-1A13DAYX50-5A18.5D m3/h 94217 115950 Pa 4411 5225 kW 185 250 4.2.24-2x2x44-34-2 Car(%)Har(%)Nar(%)Oar(%)Sar(%)Wad(%)Aar(%)Vdaf(%)Wt(%)Qnet,v,ar(MJ/kg)31.102.87 0.816.6 3.070.8247.8031.707.81 126694-3 x2x4 x2x4 x2x4 t/h 12.94 12.94 16.17 16.17 t/d 310.6 310.6 388.1 388.1 104t/a 9.71 9.71 12.13 12.132475001%4.2.34-44-4 140 m/s 25.2 27.4 mg/m32100 2100(1.4) mg/m3 1595 1939SO2 kg/h 231.5 mg/m3 500(1.4)mg/m3 251 395() kg/h 13.2 5.1 5.1.1