1 TB 1 2 3 4 5 6 7 8 9
2 3 V L m³/h m 11.8 13.9 9.5 2.5 7 0.1 7 3 3.5 3 3.5 0.5 3.5 0.5 3.5 0.4 3.5 0.2
KRİTİK HAT KOLON
DAĞITIM HATTI BORUSU 4 5 6 7 DN W Pr/L Pr mm m/s mbar/m mbar 40 2.36 0.02520 0.35028 40 1.9 0.01680 0.04200 40 1.4 0.00950 0.00095 32 1.9 0.02060 0.06180 32 1 0.00570 0.01710 25 1.7 0.02340 0.01170 25 1.7 0.02340 0.01170 25 1.7 0.02340 0.00936 25 1.7 0.02340 0.00468
1+2+8
TS 301 'E GÖRE 8 9 10 11 Ksi Pr h Pa mbar mbar 3.6 0.07960 4.60 -0.1840 0.8 0.01147 0.30 -0.0120 0.4 0.00311 0.00 0.0000 0.5 0.00717 3.00 -0.1200 0.4 0.00159 3.00 -0.1200 1.4 0.01606 -0.20 0.0080 2.7 0.03098 -0.20 0.0080 3.1 0.03557 -0.30 0.0120 2.3 0.02639 -0.20 0.0080
0.34427 < 0,8 UYGUNDUR
12 ΣPt mbar 0.24588 0.04147 0.00406 ### ### 0.03576 0.05068 0.05693 0.03907
10 9 8 7 5 4 3 2
24.5 22.5 20.5 18.5 14 11.8 9.5 7
EKLEME PARÇALARI
ζ
REDÜKSİYON DİRSEK 90º T PARÇA DÜZ GEÇİŞ KURUVA TE TE PARÇASI DİRSEK 45º KÜRESEL VANA DİŞLİ DİRSEK TE PARÇASI ZIT AKIŞLI KSİ TOPLAMI
0.5 0.4 0 1.5 1.3 0.3 0.5 0.5 1.5
1
2
9
2
KSİ DEĞERİ TESPİT FORMU 3 4 5 6 7 1 1 1 1 1 1 1
8 1 2
9 1
1
1
1
1
1
1
1
3.6 0.8 0.4 0.5 0.4 1.4 2.7 3.1 2.3
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 3.6 0.8 0.4 0.5 0.4 #REF! #REF! #REF! #REF!
9 Pr mbar 0.1556 0.0249 0.0088 0.0072 0.0057 #REF! #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 0.6476 0.1119 -0.0026 -0.0624 -0.0525 #REF! #REF! #REF! #REF!