DAĞITIM HATTI BORUSU TS 301 'E GÖRE 1 2 3 4 5 6 TB V L DN W Pr/L m³/h m mm m/s mbar/m 1 3.5 7.6 25 1.7 0.02340 2 1.6 3.9 20 1.18 0.01234 3 1.6 1.2 15 2.24 0.08368 4 2.5 5.3 20 1.9 0.04050 5 3.5 3.6 25 1.7 0.02340 6 3.5 4.5 20 2.7 0.07620 7 1.6 2.7 20 1.18 0.01234 8 1.6 1.3 15 2.24 0.08368 9 2.5 1 20 1.9 0.04050 KRİTİK HAT DAİRE 2 1+4 0.4670 < 1 UYGUNDUR DAİRE 11 5+6+7+8 0.6843 < 0,8 UYGUNDUR
7 Pr mbar 0.17784 0.04813 0.10042 0.21465 0.08424 0.34290 0.03332 0.10878 0.04050
8 Ksi 1.2 2.6 1 3.4 0.8 1.3 0.8 1.8 1.8
9 Pr mbar 0.01377 0.01437 0.01992 0.04873 0.00918 0.03762 0.00442 0.03586 0.02580
10 h 0.50 0.00 -1.20 -0.80 0.30 0.20 0.00 -1.20 -1.00
11 Pa mbar -0.0200 0.0000 0.0480 0.0320 -0.0120 -0.0080 0.0000 0.0480 0.0400
12 ΣPt mbar 0.17161 0.06250 0.16834 0.29538 0.08142 0.37252 0.03774 0.19264 0.10630
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
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 3
2 1 2
KSİ DEĞERİ TESPİT FORMU 3 4 5 6 7 1 1 1 6 2 2 2
8 1 2
1
9
1 1
1
1
1
1.2 2.6 1.0 3.4 0.8 1.3 0.8 1.8 1.8
1 TB
2 V m³/h 16.5 14 11.8 9.5 7 3.5 3.5 3.5 3.5
1 2 3 4 5 6 7 8 9 KRİTİK HAT 1+2+3+7 0.7677
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 1.2 2.6 1 3.4 0.8 1.3 0.8 1.8 1.8
9 Pr mbar 0.0519 0.0809 0.0221 0.0487 0.0115 0.0052 0.0092 0.0207 0.0207
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 0.5439 0.1679 0.0106 -0.0209 -0.0467 -0.0977 0.0453 0.0567 0.0333