1 TB
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 8 9 DN W Pr/L Pr Ksi Pr mm m/s mbar/m mbar mbar 40 2.36 0.02520 0.31248 5.6 0.12382 40 1.9 0.01680 0.05040 0 0.00000 40 1.4 0.00950 0.02850 0 0.00000 32 1 0.00570 0.01710 0.9 0.00357 25 1.7 0.02340 0.03978 1.4 0.01606 25 1.7 0.02340 0.03978 2.7 0.03098
2 3 V L m³/h m 1 11.8 12.4 2 9.5 3 3 7 3 4 3.5 3 5 3.5 1.7 6 3.5 1.7 KRİTİK HAT KOLON 1+6 0.4031 < 1 UYGUNDUR
10 h 2.80 3.00 3.00 3.00 -0.20 -0.20
RE 11 12 Pa ΣPt mbar mbar -0.1120 0.32430 -0.1200 -0.06960 -0.1200 -0.09150 -0.1200 -0.09933 0.0080 0.06384 0.0080 0.07876
10 9 8 7 5 4 3 2 1
24.5 22.5 20.5 18.5 14 11.8 9.5 7 3.5
EKLEME PARÇALARI REDÜKSİYON DİRSEK 90º T PARÇA DÜZ GEÇİŞ KURUVA TE TE PARÇASI DİRSEK 45º KÜRESEL VANA DİŞLİ DİRSEK TE PARÇASI ZIT AKIŞLI KSİ TOPLAMI
KSİ DEĞERİ TESPİT FORMU 1 2 3 4 5 6 0.5 1 1 1 0.4 14 1 1 1 0 1.5 1.3 1 0.3 0.5 1 1 0.5 1.5 5.6 0.0 0.0 0.9 1.4 2.7
ζ
1 TB 1 2 3 4 5 6 7 8 9 KRİTİK HAT 1+2+3+7
2 V m³/h 16.5 14 11.8 9.5 7 3.5 3.5 3.5 3.5 #REF!
3 L m 12.8 2.5 5.1 3 3 3 1.2 1.2 0.2
DAĞITIM HATTI BORUSU TS 301 'E GÖRE 4 5 6 7 DN W Pr/L Pr mm m/s mbar/m mbar 40 3.3 0.0475 0.6080 40 2.8 0.0348 0.0870 40 2.36 0.0252 0.1285 40 1.9 0.02 0.0504 32 1.9 0.02 0.0618 32 1 0.01 0.0171 25 1.7 0.02 0.0281 25 1.7 0.02 0.0281 25 1.7 0.02 0.0047
8 Ksi 5.6 0 0 0.9 1.4 2.7 #REF! #REF! #REF!
9 Pr mbar 0.2421 0.0000 0.0000 0.0129 0.0201 0.0107 #REF! #REF! #REF!
10 h m 2.9 0 3.5 3 3 3 -0.2 -0.2 -0.2
11 Pa mbar -0.1160 0.0000 -0.1400 -0.1200 -0.1200 -0.1200 0.0080 0.0080 0.0080
12 ΣPt mbar 0.7341 0.0870 -0.0115 -0.0567 -0.0381 -0.0922 #REF! #REF! #REF!