Gunes Yapi 4-9-12
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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 15.4 25 1.7 0.02340 2 2.5 1.9 20 1.9 0.08368 3 1.6 1 15 2.24 0.04050 4 3.5 15.7 25 1.7 0.02340 5 2.5 2.2 20 1.9 0.08368 6 1.6 1 15 2.24 0.04050 7 3.5 3.6 25 1.7 0.02340 8 3.5 5.6 20 2.7 0.07620 9 2.5 1 20 1.9 0.08368 10 1.6 3 20 1.18 0.01234 11 1.6 0.9 15 2.24 0.04050 KRİTİK HAT DAİRE 4 1+2 0.6735 < 0,8 UYGUNDUR DAİRE 12 4+5 0.6245 < 0,8 UYGUNDUR DAİRE 9 7+8+10+11 0.6876 < 0,8 UYGUNDUR
7 Pr mbar 0.36036 0.15899 0.04050 0.36738 0.18410 0.04050 0.08424 0.42672 0.08368 0.03702 0.03645
8 Ksi 6.4 3.4 1 2.8 0.9 2.3 1.2 0.9 1.8 2.8 1
9 Pr mbar 0.07343 0.04873 0.01992 0.03213 0.01290 0.04582 0.01377 0.02605 0.02580 0.01548 0.01992
10 h 0.10 -0.90 -1.00 0.30 -1.00 -1.00 0.30 0.00 -1.00 -0.10 -0.90
11 Pa mbar -0.0040 0.0360 0.0400 -0.0120 0.0400 0.0400 -0.0120 0.0000 0.0400 0.0040 0.0360
12 ΣPt mbar 0.42979 0.24372 0.10042 0.38751 0.23699 0.12632 0.08601 0.45277 0.14948 0.05650 0.09237
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
KSİ DEĞERİ TESPİT FORMU 3 4 5 6 7 1 1 7 1 3
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
1 2 8 9 10 11 0.5 1 1 0.4 16 4 1 7 0 1.5 1.3 1 1 1 0.3 0.5 1 1 1 1 1 1 0.5 1.5 6.4 3.4 1.0 2.8 0.9 2.3 1.2 0.9 1.8 2.8 1.0
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 1.0220
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 6.4 3.4 1 2.8 0.9 2.3 1.2 0.9 1.8
9 Pr mbar 0.2767 0.1058 0.0221 0.0401 0.0129 0.0091 0.0138 0.0103 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 0.7687 0.1928 0.0106 -0.0295 -0.0453 -0.0938 0.0498 0.0464 0.0333
7 Pr mbar 0.36036 0.15899 0.04050 0.36738 0.18410 0.04050 0.08424 0.42672 0.08368 0.03702 0.03645
8 Ksi 6.4 3.4 1 2.8 0.9 2.3 1.2 0.9 1.8 2.8 1
9 Pr mbar 0.07343 0.04873 0.01992 0.03213 0.01290 0.04582 0.01377 0.02605 0.02580 0.01548 0.01992
10 h 0.10 -0.90 -1.00 0.30 -1.00 -1.00 0.30 0.00 -1.00 -0.10 -0.90
11 Pa mbar -0.0040 0.0360 0.0400 -0.0120 0.0400 0.0400 -0.0120 0.0000 0.0400 0.0040 0.0360
12 ΣPt mbar 0.42979 0.24372 0.10042 0.38751 0.23699 0.12632 0.08601 0.45277 0.14948 0.05650 0.09237
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
KSİ DEĞERİ TESPİT FORMU 3 4 5 6 7 1 1 7 1 3
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
1 2 8 9 10 11 0.5 1 1 0.4 16 4 1 7 0 1.5 1.3 1 1 1 0.3 0.5 1 1 1 1 1 1 0.5 1.5 6.4 3.4 1.0 2.8 0.9 2.3 1.2 0.9 1.8 2.8 1.0
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 1.0220
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 6.4 3.4 1 2.8 0.9 2.3 1.2 0.9 1.8
9 Pr mbar 0.2767 0.1058 0.0221 0.0401 0.0129 0.0091 0.0138 0.0103 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 0.7687 0.1928 0.0106 -0.0295 -0.0453 -0.0938 0.0498 0.0464 0.0333
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