SE-1- 2002-TER I
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Prueba N°1 ITEM N°1 cambio Datos fluido n/(mol) expansión a) gas ideal 1 5 200 1 adiabática 6 reversible solución g W/(KJ) u/(m/s) W/(KJ) 1.49476831 5.06625137 6014.19513 17651.7776 2.54336333 105.897589 0 ITEM N°2 Datos fluido agua 2.27 1.51 0.76 1 56.3 conversión sistema 80.1643012 53.3251519 26.8391493 14.6959793 827.383636 cambio: calent solución 0.01672 26.78 3189.30334 1.00220871 0.00031414 ra las condicio 180.12 1077.6 180.401936 0.02512747 0.02512747 827.383636 812.53 0.0209 0.5596 508.8 1114.9 0.0079263 848.28 0.021 0.5342 514.8 1114.2 -35.75 -0.0001 0.0254 -6 0.7 0.02094155 0.54904665 511.292918 1114.60916 Q(kJ) 1070899.59 1129842.33 ITEM N°3 Datos fluido agua vapor saturado seco 37.8 0.35 204 504 136 conversión 100.04 4.97802369 399.2 1998.72315 299.82832 solución Hp 1105.1 1241.3 -38837.894 -11.382109 -8.4876501 ITEM N°4 Datos fluido freón - 12 28.3 26.7 1.05 80 7.03 37.8 1 80 15 100 100 solución 88.694 89.383 3.1281 80.7382364 0.80 0.20 0.012277 0.48591516 65.1237931 0.00740615 26.365 85.282 26.801348 0.01523259 65.2902153 80 98.87 26.5226504 -4076.5023 Prueba N°2 ITEM N°1 cambio Datos fluido n/(mol) expansión a) gas ideal 1 5 200 3 adiabática 4 reversible solución g W/(KJ) u/(m/s) W/(KJ) 1.98609732 5.06625137 6014.19513 19172.4456 2.10488164 55.6205248 0 ITEM N°2 Pi/(atm) Ti/(°F) mpistón/(lbm) Cp/(Btu/lbmol°F) Pi/(bar) Vi/(cm 3 /mol) Vf/(cm 3 /mol) V(m 3 ) Vi L (m 3 ) Vi V (m 3 ) Pi/(atm) Pf/(kgf/cm 2 ) V(ft 3 ) Vi L (ft 3 ) Vi V (ft 3 ) Pi/(lbf/in 2 ) Pf/(lbf/in 2 ) Vi L (ft 3 /lbm) Vi V (ft 3 /lbm) mi L (lbm) mi V (lbm) xi Ui L /(Btu/lbm) Ui V /(Btu/lbm) Ui(Btu/lbm) Vi(ft 3 /lbm) Vf(ft 3 /lbm) Pf/(lbf/in 2 ) Pf/(lbf/in 2 ) Vf L (ft 3 /lbm) Vf V (ft 3 /lbm) Uf L /(Btu/lbm) Uf V /(Btu/lbm) xf Q(Btu) Te(°C) Ps/(kgf/cm 2 ) Ts(°C) Te(°F) Ps/(lbf/in 2 ) Ts(°F) He/(Btu/lbm) Hs/(Btu/lbm) Vtamque(lt) Ti(°C) Pi/(kgf/cm 2 ) V L (%) Pe/(kgf/cm 2 ) Te(°C) Vtamque(ft 3 ) Ti(°F) Pi/(lbf/in 2 ) Pe/(lbf/in 2 ) Te(°F) He/(Btu/lbm) Hi/(Btu/lbm) Vi/(ft 3 /lbm) Ui/(Btu/lbm) Vi L /(ft 3 ) Vi V /(ft 3 ) V L /(ft 3 /lbm) mi V (lbm) mi L (lbm) xf H L /(Btu/lbm) H V /(Btu/lbm) Hf/(Btu/lbm) Vf/(ft 3 /lbm) me(lbm) Tf(°F) Pf/(lbf/in 2 ) Uf/(Btu/lbm) Q/(Btu) Pi/(atm) Ti/(°F) mpistón/(lbm) Cp/(Btu/lbmol°F) Pi/(bar) Vi/(cm 3 /mol) Vf/(cm 3 /mol) ˙ Q(kcal / h) ˙ m( kg m / h ) ˙ Q (Btu / h ) ˙ m( lb m / h ) ˙ W ( Btu / h ) ˙ W ( kW )
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Transcript of SE-1- 2002-TER I
Hoja1Prueba N1ITEM N1cambioDatosfluidon/(mol)Pi/(atm)Ti/(F)mpistn/(lbm)expansinCp/(Btu/lbmolF)R/(Btu/lbmolR)Pf/(atm)Pf/(bar)a)gas ideal152001adiabtica61.98611.0132502738reversiblesolucingPi/(bar)Vi/(cm3/mol)Vf/(cm3/mol)W/(KJ)u/(m/s)W/(KJ)1.49476831095.06625136926014.195134265317651.77763420912.5433633348105.89758897290no hay presin de oposicinITEM N2Datosfluido aguaV(m3)ViL(m3)ViV(m3)Pi/(atm)Pf/(kgf/cm2)2.271.510.76156.3conversinV(ft3)ViL(ft3)ViV(ft3)Pi/(lbf/in2)Pf/(lbf/in2)sistema: agua en la caldera80.164301153653.325151868726.839149284914.6959793216827.3836358054cambio: calentamiento a volumen constantesolucinViL(ft3/lbm)ViV(ft3/lbm)miL(lbm)miV(lbm)xi0.0167226.783189.30334142721.00220871120.0003141419UiL/(Btu/lbm)UiV/(Btu/lbm)Ui(Btu/lbm)Vi(ft3/lbm)Vf(ft3/lbm)para las condiciones finales el sistema es L+V180.121077.6180.40193609040.02512746820.0251274682Pf/(lbf/in2)Pf/(lbf/in2)VfL(ft3/lbm)VfV(ft3/lbm)UfL/(Btu/lbm)UfV/(Btu/lbm)xfUf(Btu/lbm)Q(Btu/lbm)827.3836358054812.530.02090.5596508.81114.90.0079263002516.0749835261335.6730474357848.280.0210.5342514.81114.2-35.75-0.00010.0254-60.70.02094154860.5490466476511.29291789741114.6091595786Q(Btu)Q(kJ)1070899.586265871129842.33082255ITEM N3Datosfluido aguavapor saturadoTe(C)Ps/(kgf/cm2)Ts(C)seco37.80.35204504136conversinTe(F)Ps/(lbf/in2)Ts(F)100.044.9780236872399.21998.7231450256299.82832solucinHe/(Btu/lbm)Hs/(Btu/lbm)Hp1105.11241.3-38837.8940389744-11.3821085002-8.4876500725ITEM N4DatosfluidoVtamque(lt)Ti(C)Pi/(kgf/cm2)VL(%)Pe/(kgf/cm2)Te(C)fren - 1228.326.71.05807.0337.8Vtamque(ft3)Ti(F)Pi/(lbf/in2)Pe/(lbf/in2)Te(F)18015100100solucinHe/(Btu/lbm)Hi/(Btu/lbm)Vi/(ft3/lbm)Ui/(Btu/lbm)ViL/(ft3)ViV/(ft3)VL/(ft3/lbm)VV/(ft3/lbm)88.69489.3833.128180.73823642080.800.200.0122770.41135miV(lbm)miL(lbm)xfHL/(Btu/lbm)HV/(Btu/lbm)Hf/(Btu/lbm)Vf/(ft3/lbm)mf(lbm)mi(lbm)0.485915162365.12379310910.007406147326.36585.28226.80134797910.015232593465.60970827130.3194929862me(lbm)Tf(F)Pf/(lbf/in2)Uf/(Btu/lbm)Q/(Btu)65.29021528528098.8726.5226503644-4076.5023017641Prueba N2ITEM N1cambioDatosfluidon/(mol)Pi/(atm)Ti/(F)mpistn/(lbm)expansinCp/(Btu/lbmolF)R/(Btu/lbmolR)Pf/(atm)Pf/(bar)a)gas ideal152003adiabtica41.9860.50.5066251369reversiblesolucingPi/(bar)Vi/(cm3/mol)Vf/(cm3/mol)W/(KJ)u/(m/s)W/(KJ)1.98609731885.06625136926014.195134265319172.4456340422.104881642455.62052478760no hay presin de oposicinITEM N2Datosfluido aguaV(m3)ViL(m3)ViV(m3)Pi/(atm)Pf/(kgf/cm2)3.271.811.46160.3conversinV(ft3)ViL(ft3)ViV(ft3)Pi/(lbf/in2)Pf/(lbf/in2)sistema: agua en la caldera115.478971265263.919552902251.559418363114.6959793216886.1675530918cambio: calentamiento a volumen constantesolucinViL(ft3/lbm)ViV(ft3/lbm)miL(lbm)miV(lbm)xi0.0167226.783822.93976687631.9252956820.000503363UiL/(Btu/lbm)UiV/(Btu/lbm)Ui(Btu/lbm)Vi(ft3/lbm)Vf(ft3/lbm)para las condiciones finales el sistema es L+V180.121077.6180.57175825560.03019164580.0301916458Pf/(kgf/cm2)Pf/(kgf/cm2)VfL(ft3/lbm)VfV(ft3/lbm)UfL/(Btu/lbm)UfV/(Btu/lbm)xfUf(Btu/lbm)Q(Btu/lbm)886.1675530918848.280.0210.5342514.81114.20.0181062098528.0938721805347.5221139249885.230.02120.51520.81113.3-36.95-0.00020.0242-60.90.02108309730.5241452311517.29291789741113.8260623154Q(Btu)Q(kJ)1329225.192017771402386.28196141ITEM N3Datosfluido aguavapor saturadoTe(C)Ps/(kgf/cm2)Ts(C)seco41.80.45204604146conversinTe(F)Ps/(lbf/in2)Ts(F)107.246.4003161692399.22395.2951976101321.87452Te(F)Te(F)He/(Btu/lbm)He/(Btu/lbm)Ps/(lbf/in2)Ps/(lbf/in2)Hs/(Btu/lbm)Hs/(Btu/lbm)107.241061107.61120.32722222226.400316169251241.31241.1039557363-36479.6579294049-10690.98711132121081108.5101240.61120.3272222222-50.71241.1039557363ITEM N4DatosfluidoVtamque(lt)Ti(C)Pi/(kgf/cm2)VL(%)Pe/(kgf/cm2)Te(C)fren - 1230.328.71.05827.0337.8Vtamque(ft3)Ti(F)Pi/(lbf/in2)Pe/(lbf/in2)Te(F)18415100100solucinHe/(Btu/lbm)Ti(F)Ti(F)Vi/(ft3/lbm)Hi/(Btu/lbm)Vi/(ft3/lbm)Hi/(Btu/lbm)Ui/(Btu/lbm)ViL/(ft3)ViV/(ft3)88.69484803.128189.3233.1589.8881.17074719820.880.191003.252192.357-20-0.124-3.0343.1589.88VL/(ft3/lbm)VV/(ft3/lbm)miV(lbm)miL(lbm)xfTf(F)Tf(F)HL/(Btu/lbm)HV/(Btu/lbm)0.0122770.411350.468229910871.46933584750.0065088373848026.36585.2829028.71386.174-10-2.348-0.89227.22436885.608472HL/(Btu/lbm)HV/(Btu/lbm)Hf/(Btu/lbm)Vf/(ft3/lbm)mf(lbm)mi(lbm)me(lbm)Pf/(lbf/in2)Uf/(Btu/lbm)Q/(Btu)27.22436885.60847227.60438063340.014874501271.93756575830.339608393771.597957364698.8727.3322347224-4411.6610649038Prueba N3ITEM N1cambioDatosfluidon/(mol)Pi/(atm)Ti/(F)mpistn/(lbm)expansinCp/(Btu/lbmolF)R/(Btu/lbmolR)Pf/(atm)Pf/(bar)a)gas ideal152004adiabtica51.9861.51.5198754107reversiblesolucingPi/(bar)Vi/(cm3/mol)Vf/(cm3/mol)W/(KJ)u/(m/s)W/(KJ)1.65892501665.06625136926014.195134265312427.07223006491.757684490944.01719199550no hay presin de oposicinITEM N2Datosfluido aguaV(m3)ViL(m3)ViV(m3)Pi/(atm)Pf/(kgf/cm2)4.272.811.46165.3conversinV(ft3)ViL(ft3)ViV(ft3)Pi/(lbf/in2)Pf/(lbf/in2)sistema: agua en la caldera150.793641376999.234223013951.559418363114.6959793216959.6474496997cambio: calentamiento a volumen constantesolucinViL(ft3/lbm)ViV(ft3/lbm)miL(lbm)miV(lbm)xi0.0167226.785935.06118503991.9252956820.0003242884UiL/(Btu/lbm)UiV/(Btu/lbm)Ui(Btu/lbm)Vi(ft3/lbm)Vf(ft3/lbm)para las condiciones finales el sistema es L+V180.121077.6180.41104232830.02539902050.0253990205Pf/(kgf/cm2)Pf/(kgf/cm2)VfL(ft3/lbm)VfV(ft3/lbm)UfL/(Btu/lbm)UfV/(Btu/lbm)xfUf(Btu/lbm)Q(Btu/lbm)959.6474496997923.390.02130.487526.91112.40.0087968611534.5178952266354.1068528982962.790.02150.4651532.91111.4-39.4-0.00020.0219-610.02138309730.4779008497529.39291789741111.9845136838Q(Btu)Q(kJ)2102327.598387712218040.55616213ITEM N3Datosfluido aguavapor saturadoTe(C)Ps/(kgf/cm2)Ts(C)seco44.80.5215610156conversinTe(F)Ps/(lbf/in2)Ts(F)112.647.11146241024192419.0895207652343.92072Te(F)Te(F)He/(Btu/lbm)He/(Btu/lbm)Ps/(lbf/in2)Ps/(lbf/in2)Hs/(Btu/lbm)Hs/(Btu/lbm)112.641121110.21116.43719298257.111462410251241.31264.71141111101240.61264.11116.4371929825-50.70.61241.00439526261264.4466245108Ts(F)Ts(F)Hs/(Btu/lbm)Hs/(Btu/lbm)4194001241.00439526261249.9124423769-43485.8143531462-12744.26097071624501264.4466245108-50-23.44222924821249.9124423769ITEM N4DatosfluidoVtamque(lt)Ti(C)Pi/(kgf/cm2)VL(%)Pe/(kgf/cm2)Te(C)fren - 1230.328.71.05847.0337.8Vtamque(ft3)Ti(F)Pi/(lbf/in2)Pe/(lbf/in2)Te(F)18415100100solucinHe/(Btu/lbm)Ti(F)Ti(F)Vi/(ft3/lbm)Hi/(Btu/lbm)Vi/(ft3/lbm)Hi/(Btu/lbm)Ui/(Btu/lbm)ViL/(ft3)ViV/(ft3)88.69484803.128189.3233.1589.8881.17074719820.900.171003.252192.357-20-0.124-3.0343.1589.88VL/(ft3/lbm)VV/(ft3/lbm)miV(lbm)miL(lbm)xfTf(F)Tf(F)HL/(Btu/lbm)HV/(Btu/lbm)0.0122770.411350.416204365173.21249038040.0056527468848026.36585.2829028.71386.174-10-2.348-0.89227.22436885.608472HL/(Btu/lbm)HV/(Btu/lbm)Hf/(Btu/lbm)Vf/(ft3/lbm)mf(lbm)mi(lbm)me(lbm)Pf/(lbf/in2)Uf/(Btu/lbm)Q/(Btu)27.22436885.60847227.55439855430.014532858673.62869474550.339608393773.289086351898.8727.2885033834-4518.6516062804Prueba N4ITEM N1cambioDatosfluidon/(mol)Pi/(atm)Ti/(F)mpistn/(lbm)expansinCp/(Btu/lbmolF)R/(Btu/lbmolR)Pf/(atm)Pf/(bar)a)gas ideal162004adiabtica61.9861.51.5198754107reversiblesolucingPi/(bar)Vi/(cm3/mol)Vf/(cm3/mol)W/(KJ)u/(m/s)W/(KJ)1.49476831096.0795016435011.829278554412669.93547401852.266252850749.98112823760no hay presin de oposicinITEM N2Datosfluido aguaV(m3)ViL(m3)ViV(m3)Pi/(atm)Pf/(kgf/cm2)4.572.911.66168.3conversinV(ft3)ViL(ft3)ViV(ft3)Pi/(lbf/in2)Pf/(lbf/in2)sistema: agua en la caldera161.3880424105102.76569002558.622352385414.69597932161003.7353876645cambio: calentamiento a volumen constantesolucinViL(ft3/lbm)ViV(ft3/lbm)miL(lbm)miV(lbm)xi0.0167226.786146.27332685632.18903481650.0003560296UiL/(Btu/lbm)UiV/(Btu/lbm)Ui(Btu/lbm)Vi(ft3/lbm)Vf(ft3/lbm)para las condiciones finales el sistema es L+V180.121077.6180.43952947770.02624852080.0262485208Pf/(kgf/cm2)Pf/(kgf/cm2)VfL(ft3/lbm)VfV(ft3/lbm)UfL/(Btu/lbm)UfV/(Btu/lbm)xfUf(Btu/lbm)Q(Btu/lbm)1003.73538766451003.50.02160.4442539.11110.30.0110209719547.9373092636367.49777978591045.40.02180.4243545.31109.1-41.9-0.00020.0199-6.21.20.02168309730.4359318223541.67601516071109.8014164205Q(Btu)Q(kJ)2259546.26701182383912.6036306ITEM N3Datosfluido aguavapor saturadoTe(C)Ps/(kgf/cm2)Ts(C)seco46.80.5215615160conversinTe(F)Ps/(lbf/in2)Ts(F)116.247.11146241024192438.9181233944352.7392Te(F)Te(F)He/(Btu/lbm)He/(Btu/lbm)Ps/(lbf/in2)Ps/(lbf/in2)Hs/(Btu/lbm)Hs/(Btu/lbm)116.241161111.91114.16311864417.111462410251241.31264.71181112.7101240.61264.11114.1631186441-50.70.61241.00439526261264.4466245108Ts(F)Ts(F)Hs/(Btu/lbm)Hs/(Btu/lbm)4194001241.00439526261249.9124423769-45445.1897306604-13318.48940640454501264.4466245108-50-23.44222924821249.9124423769ITEM N4DatosfluidoVtamque(lt)Ti(C)Pi/(kgf/cm2)VL(%)Pe/(kgf/cm2)Te(C)fren - 1235.328.71.05867.0337.8Vtamque(ft3)Ti(F)Pi/(lbf/in2)Pe/(lbf/in2)Te(F)18415100100solucinHe/(Btu/lbm)Ti(F)Ti(F)Vi/(ft3/lbm)Hi/(Btu/lbm)Vi/(ft3/lbm)Hi/(Btu/lbm)Ui/(Btu/lbm)ViL/(ft3)ViV/(ft3)88.69484803.128189.3233.1589.8881.17074719821.070.171003.252192.357-20-0.124-3.0343.1589.88VL/(ft3/lbm)VV/(ft3/lbm)miV(lbm)miL(lbm)xfTf(F)Tf(F)HL/(Btu/lbm)HV/(Btu/lbm)0.0122770.411350.424274334387.32456321580.0048350992848026.36585.2829028.71386.174-10-2.348-0.89227.22436885.608472HL/(Btu/lbm)HV/(Btu/lbm)Hf/(Btu/lbm)Vf/(ft3/lbm)mf(lbm)mi(lbm)me(lbm)Pf/(lbf/in2)Uf/(Btu/lbm)Q/(Btu)27.22436885.60847227.50666093460.014206557587.748837550.395649382887.353188167398.8727.2467358126-5388.949432749Prueba N5ITEM N1cambioDatosfluidon/(mol)Pi/(atm)Ti/(F)mpistn/(lbm)expansinCp/(Btu/lbmolF)R/(Btu/lbmolR)Pf/(atm)Pf/(bar)a)gas ideal183506adiabtica71.9861.51.5198754107reversiblesolucingPi/(bar)Vi/(cm3/mol)Vf/(cm3/mol)W/(KJ)u/(m/s)W/(KJ)1.39609094548.10600219064613.588398707515303.03774550283.569646580851.2175563810no hay presin de oposicinITEM N2Datosfluido aguaV(m3)ViL(m3)ViV(m3)Pi/(atm)Pf/(kgf/cm2)5.573.911.66170.3conversinV(ft3)ViL(ft3)ViV(ft3)Pi/(lbf/in2)Pf/(lbf/in2)sistema: agua en la caldera196.7027125222138.080360136758.622352385414.69597932161033.1273463077cambio: calentamiento a volumen constantesolucinViL(ft3/lbm)ViV(ft3/lbm)miL(lbm)miV(lbm)xi0.0167226.788258.394745022.18903481650.0002649976UiL/(Btu/lbm)UiV/(Btu/lbm)Ui(Btu/lbm)Vi(ft3/lbm)Vf(ft3/lbm)para las condiciones finales el sistema es L+V180.121077.6180.35783003960.02381220480.0238122048Pf/(kgf/cm2)Pf/(kgf/cm2)VfL(ft3/lbm)VfV(ft3/lbm)UfL/(Btu/lbm)UfV/(Btu/lbm)xfUf(Btu/lbm)Q(Btu/lbm)1033.12734630771003.50.02160.4442539.11110.30.0051396839544.5960001504364.23817011081045.40.02180.4243545.31109.1-41.9-0.00020.0199-6.21.20.02168309730.4359318223541.67601516071109.8014164205Q(Btu)Q(kJ)3008819.920014863174426.58028157ITEM N3Datosfluido aguavapor saturadoTe(C)Ps/(kgf/cm2)Ts(C)seco46.80.45215620170conversinTe(F)Ps/(lbf/in2)Ts(F)116.246.40031616924192458.7467260236374.7854Te(F)Te(F)He/(Btu/lbm)He/(Btu/lbm)Ps/(lbf/in2)Ps/(lbf/in2)Hs/(Btu/lbm)Hs/(Btu/lbm)116.241161111.91114.16311864416.400316169251241.31264.71181112.7101240.61264.11114.1631186441-50.70.61241.00439526261264.4466245108Ts(F)Ts(F)Hs/(Btu/lbm)Hs/(Btu/lbm)4194001241.00439526261249.9124423769-48418.1178689096-14189.75679795774501264.4466245108-50-23.44222924821249.9124423769ITEM N4DatosfluidoVtamque(lt)Ti(C)Pi/(kgf/cm2)VL(%)Pe/(kgf/cm2)Te(C)fren - 1245.328.71.05837.0337.8Vtamque(ft3)Ti(F)Pi/(lbf/in2)Pe/(lbf/in2)Te(F)28415100100solucinHe/(Btu/lbm)Ti(F)Ti(F)Vi/(ft3/lbm)Hi/(Btu/lbm)Vi/(ft3/lbm)Hi/(Btu/lbm)Ui/(Btu/lbm)ViL/(ft3)ViV/(ft3)88.69484803.128189.3233.1589.8881.17074719821.330.271003.252192.357-20-0.124-3.0343.1589.88VL/(ft3/lbm)VV/(ft3/lbm)miV(lbm)miL(lbm)xfTf(F)Tf(F)HL/(Btu/lbm)HV/(Btu/lbm)0.0122770.411350.6611365132108.15324633870.0060758192848026.36585.2829028.71386.174-10-2.348-0.89227.22436885.608472HL/(Btu/lbm)HV/(Btu/lbm)Hf/(Btu/lbm)Vf/(ft3/lbm)mf(lbm)mi(lbm)me(lbm)Pf/(lbf/in2)Uf/(Btu/lbm)Q/(Btu)27.22436885.60847227.57909925820.0147016954108.81438285190.5077313609108.30665149198.8727.3101150265-6675.6297690536
Hoja2
Hoja3
MBD00050D23.unknown
MBD0005EE74.unknown
MBD0005EE78.unknown
MBD000ED130.unknown
MBD000EDE41.unknown
MBD000F8A01.unknown
MBD000EDCC5.unknown
MBD0005EE7A.unknown
MBD0005EE7B.unknown
MBD000E67C3.unknown
MBD0005EE79.unknown
MBD0005EE76.unknown
MBD0005EE77.unknown
MBD0005EE75.unknown
MBD00050D27.unknown
MBD0005EE72.unknown
MBD0005EE73.unknown
MBD00050D28.unknown
MBD00050D25.unknown
MBD00050D26.unknown
MBD00050D24.unknown
MBD0003FC31.unknown
MBD00050D1E.unknown
MBD00050D21.unknown
MBD00050D22.unknown
MBD00050D20.unknown
MBD000403DC.unknown
MBD000403DD.unknown
MBD0003FEE2.unknown
MBD00003C0D.unknown
MBD0003FC2D.unknown
MBD0003FC2F.unknown
MBD0003FC30.unknown
MBD0003FC2E.unknown
MBD00003C0F.unknown
MBD0003FC2B.unknown
MBD00004810.unknown
MBD00003C0E.unknown
MBD000039D7.unknown
MBD000039D9.unknown
MBD00003C0C.unknown
MBD000039D8.unknown
MBD000039D5.unknown
MBD000039D6.unknown
MBD000039D4.unknown
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