表4-5 屏的结序号1234567101112131415161718名称管子外径屏的片数每片屏的管子排数屏的深度一片屏的平面面积屏的平均高度屏的横向节距比值屏的纵向节距比值屏的角系数屏的计算受热面积屏区顶棚面积屏区两侧水冷壁面积符号dZnLAphS1单位mmmm2mmm1S2mm2xpApjAdpm2m2m2Asl屏区附加受热面面积烟气进屏流通面积烟气出屏流通面积烟气平均流通面积ApfjApm2m2m2m2ApAy19蒸汽流通面积Altm2202122烟气有效辐射层厚度屏区进口烟窗面积屏区出口烟窗面积smAchAchm2m2 表4-6 屏的热力计算序号名称符号单位1234567烟气进屏温度烟气进屏焓烟气出屏温度烟气出屏焓烟气平均温度屏区附加受热面对流吸热量屏的对流吸热量炉膛与屏相互换热系数炉膛出口烟窗的沿高度热负荷分配系数炉膛出口烟窗射入屏区的炉膛辐射热量屏间烟气有效辐射层厚度屏间烟气压力水蒸气容积份额三原子气体辐射减弱系数三原子气体和水蒸气容积总份额灰粒的辐射减弱系数烟气质量飞灰浓度烟气的辐射减弱系数屏区烟气黑度屏进口对出口的角系数燃料种类修正系数屏出口烟窗面积'p。C'hyp\"pkJ/kg。Ch\"ypkJ/kgpjdQpfjdQpCkJ/kgkJ/kg。yc'fQp10111213141516171819202122kJ/kgmMpasprH2Okq1/(mMPa)rkhy1/(mMPa)kg/m3k1/(mMPa)xr\"p23炉膛及屏间烟气向屏后受热面的辐射热量屏区吸收的炉膛辐射热屏区附加受热面吸收的辐射热量屏区水冷壁吸收的辐射热量屏区顶棚吸收的辐射热量屏吸收的辐射热量屏吸收的总热量第一级减温水喷水量第二级减温水喷水量屏中蒸汽流量蒸汽进屏温度蒸汽进屏焓蒸汽出屏焓蒸汽出屏温度屏内蒸汽平均温度平均传热温差屏内蒸汽平均比体积屏内蒸汽流速管壁对蒸汽的放热系数fQ\"pkJ/kg2425fQpqkJ/kgkJ/kgkJ/kgkJ/kgkJ/kgQfpfj26fQpsl27282930313233343536373839fQpldQfpQpDjw1Djw2Dpt'p'hpkJ/kgkg/hkg/hkg/h。CkJ/kgh\"pkJ/kg。t\"pCtpj。C。t1Cm3/kg4041qm/sW/(m2.C)22424344474849505152535556575859606162烟气流速烟气侧对流放热系数灰污系数管壁灰污层温度辐射放热系数利用系数烟气侧放热系数对流传热系数屏的对流传热量计算误差屏区水冷壁的温度平均传热温差屏区水冷壁对流吸热量屏区顶棚进口蒸汽温度屏区顶棚进口蒸汽焓屏区顶棚蒸汽焓增屏区顶棚出口蒸汽焓屏区顶棚出口蒸汽温度屏区顶棚平均汽温平均传热温差屏区顶棚对流吸热量ym/sW/(m2.C)dthb(m2.C)/W。CfW/(m2.C)1kdQpW/(m2.C)W/(mC)kJ/kg%2.ts。。Ct2dQpslCCkJ/kgkJ/kg。t'pld'hpldhpld''hpldkJ/kgkJ/kg。t''pldtpldpjC。Ct3dQpld。CkJ/kg636566676869屏区顶棚总吸热量屏区顶棚蒸汽流量屏区顶棚焓增计算误差检查屏区附加受热面对流吸热量计算误差屏区受热面总对流吸热量dQpldQpldkJ/kgkg/hkJ/kg%DpldhplddQpfjkJ/kg%dQpqkJ/kg 表4-7 凝渣管结构及计算序号名称符号单位12345671011121314151617管子尺寸管子排列方式及根数管子节距受热面积烟道流通截面积烟道容积烟道表面积烟气辐射层厚度烟气进凝渣管温度烟气进凝渣管焓烟气出凝渣管温度烟气出凝渣管焓凝渣管对流吸热量凝渣管角系数来自炉膛及屏的辐射热凝渣管吸收的辐射热凝渣管总吸收热量θθdnS1HnzAyVAs′nzmm根mmm²m²m³m²m℃kJ/kg℃kJ/kgkJ/kgh´ynz″nzh\"ynzQdnzxnzQ´fnzQfnzQnzkJ/kgkJ/kgkJ/kg18通过凝渣管的辐射热Q\"fnzkJ/kg屏的结构数据计算表公式结果42512备注410402.07613.57.4屏的间距S1/d59114.146S2/d查《标准》线算图1(即附录A-1),曲线51.090.9831715.630.145.758.8502ApxpZ宽深角系数高深角系数2AdpAsl(6.4241.760)120.042(6.4241.760)(6.4240.550)120.042(6.4240.550)2ApApApAp2d1210n4dn0.04220.005(其中 ,单位为m)1.8111S1 (注: 单位为m)hLS10.0970.77965.6149.34A2见表3-2中7.686.424表4-6 屏的热力计算公式结果备注查表3-9炉膛校核热力计算即炉膛出口烟气温度1105.944查表3-9炉膛校核热力计算即炉膛出口烟气焓14338.211先估后校1005查焓温表125.7005('p''p)/2先估后校'''0d(hyp-hyphlk)Qpfj1055.47212061228.705290.98查附录A-15查《标准》线算图11(即附录A-6)0.82(xh/H0H1/H019846/23938)''yc(Q1hyp)Ach/Alz997.791210.7790.10.08450559查表4-5屏的结构数据表查表2-9烟气特性表10.2(0.781.6rH2O10.2rps0.1)(10.37Tpj100010.36038740.23957759)查表2-9烟气特性表5590023(注:dμm2dhpj273)h单位为83.6657960.01098733.401378150.232745查表2-9烟气特性表kqrkhy1ekpsL2(s)1—1Ls1注:s1单位为m取用查表4-5屏的结构数据计算0.139568330.550'f4Qp(1)x0\"TchpjrBj/3600注:0=5.67X10-11W/(m2K4)237.472527760.318683'f''fQpQpQfQpqfpqApfjApjApfj95.7997347AslApjApfj63.0978559fQpqAdpApjApfj32.70187886.514813.2242465004500215500378.23063.3277.519462.91420.555634.9171010.02814693.555
ffQpqQpfjdQpQpf估计DjwDjw1DDjw2先估后校查附录B-6、B-7,按计算负荷下进屏p=10.49 Mpa'hpBjQp/Dp查附录B-6、B-7,按计算负荷下出屏p=10.20 Mpa(t'pt''p)/2pj-tpj查附录B-6、B-7,按计算负荷下屏进出口压力平均值p= 10.20 Mpa(查表1-6)及tpjDpv3600Alt2Cd017.365352446查《标准》线算图15(附录A-10)BjVy3600Ay(1pj273)(其中Vy见表2-9)5.08397715.9440.007719.88195269.940.8684.9805787d=0CzCsC查《标准》线算图12(附录A-7)查附录A-14曲线2(吹灰)tpj(12)f0BjQp3.6Apj查《标准》线算图19(附录A-11)查附录A-14曲线2(吹灰)(dd2s2xf)11(1fQpq3.6pjBjQdp)(12)1t1k42.08615211252.1667-1.8736652317.91737.562101138.118213ddd[Qp(估)-Qp]/Qp查计算负荷下汽包p= 10.98 Mpa的饱和温度pjts3.6kt2slBj查表3-10炉膛顶棚辐射受热面吸热量及工质焓增的计算表323.61查表3-10炉膛顶棚辐射受热面吸热量及工质焓增的计算表2755.56798先估后校'hpldhpld132768.56798321.3322.455733.01710171.1417查附录B中水和水蒸气性质表按计算负荷下汽包压力p=10.98 Mpa (查表1-6)(t'pldt''pld)/2pjtpldpj3.6kt3dpBjdQpldQpfld103.84363320900012.1001135等于表3-10中的DldQpldBj/Dpld[hpld(估)-hpld]/hpld(允许误差10%)ddQpslQplddddQpfj(估)-Qpfj)/Qpfj7.43700868209.259967-1.55785521437.96526ddQpfjQp表4-7 凝渣管结构及计算公式结果φ133*10备注横列-排7680/(10+1)πdlpjn=3.14*0.133*6.424*106.424(7.68-10*0.133)7.68*6.424*0.552(7.68*6.424+6.424*0.55+7.68*0.55)3.6*V/A等于屏出口烟气温度等于屏出口烟气焓´nz-5查焓温表(h´ynz-h\"ynz)查《标准》线算图1(即附录A-1)(a)曲线51070026.848.427.2114.10.8651005125.7005100012824.295771.01849960.27查表4-6屏的热力计算第23项,即等于Q\"fp237.472527Q´fnzxnzQdnz+Qfnz.1175824135.136082Q´fnz(1-xnz)173.3945