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Esercizi impianti idraulici testi soluzioni

Study material for Gestione degli Impianti Industriali B, shared by the Studwiz community and reviewed by moderators.

Gestione degli Impianti Industriali BBy topic

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RECAP1 - hg- L'271571472075+12+6+15=89nnli peravere ⊥ ⊥ laPORTATAinkgls2coc,Asp 2loc ,Maud µ z Aperture=0,0375. F.2.G? 0,03µs0, 0182.89ms. -3600G)= . _ = 0,0617g? f.Ds noookglnn'. 0,159ms UNITÀDiMISURADi G: •DAmille•m'15DIVIDOPER3600 • Damille→ VlglsMoltiplicoPer /3600 lrcircuroeAperture= 0,0617- G? = g.zq.io?g2 f.g1000. 9.81 Le> lrgtlrcircuirot#%12T6,29- là!ci ha le { he-oiztg.za-eo-b.gr 12 di lui=80- 0,as- giB G Le=Li=312T6,29- leòcog?= 80- 0,75- G? 㱺 0,75g?+6,29- leòbg?= 80-12 0.75g?= 68 G= È, = 9.52m'1h 㱺 In=Le=lei= 12t6,29-lòb. 9,52?= 12M 1bar-10hm 1bar= 105Pa㱺no,2MNostra 10,2:105=12:x 㱺 ×= %È= 1,172- costa 9,52mi/h Potenza= G-Pressione= È.li = 443W | 0,7(BisognaaverelaPORTATAinMB/s µPSHD= [=soloQuelladi Aspirazione㱺15+2+14=31M 2 DP= 0,03msf-l- G=0.0375 G)" = 0,00214g? f.Ds nooo- 0,155 lrasp= AP= 0.00214%2,19.milÈ= 2,19- io!2,6452=0,15.io f-gnooo-9,81 la kgls NPSHD= ¥- lrasptlgi, t =10,33- 0,12. - 2,19-ÙÈsto.lu e. 2,645kgIs= 14,35M VISTO CHEnpshpsnps.HR=3nonèpresentela cavitazione Recato2 he hi f.Fa Re= l'[D=loookglni.com/F.2oomm/.uo-3m/1nnn/= 0,00098p/m. §= 1020408,16372000㱺 MoroTURBANO Rugositàrelativa= 0,04㱺 dall'ABACOdi Moody㱺 f-0,065 ④DISTRIBUITA= f.l. GZ f.D8 Vedendoil graficoe usandounametodologiaper punti, si puòcompletareaseguentetabella DORATAPerditecaricocaratteristicacaratteristica nonsipuòfare Amano, serve excel

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