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列管式散热器、冷却器

反应釜


反应釜

直径管程数管子数量换热面积 公称值/计算值管程通道截面积 管程通道流速为0.5m/sec时的流量m/hr公称压力
管子长度(m)φ25×2.5
15002000300040006000φ25×2
1591141.5/1.622/2.173/3.27

0.0044/7.92/0.25
0.00498.82
2191263/3.004/4.026/6.068/8.1
0.0082/14.76/0.6
0.00916.2
2263/3.004/4.026/6.068/8.81
0.0041/7.38/1
0.00458.01
2731445/5.087/5.1810/10.2614/13.7221/20.630.0138/24.84/1.6
0.015227.36

2405/4.626/6.199/9.3312/12.4719/18.760.0063/11.24/2.5
0.006912.42
3251607/6.939/9.2814/14.0019/18.7128/28.130.0188/33.84/0.6
0.020837.44

2566/6.479/8.6613/13.0517/17.4636/26.260.0088/15.84/1
0.009717.46
400111914/13.4718/18.4128/27.7637/37.1055/55.80.0374/67.32/1.6
0.041274.16

211013/12.7017/17.0226/25.6634/34.2050/51.580.0173/31.14/2.5
0.01934.2
5001185

45/4.1555/57.6885/86.740.0581/104.58/
0.0641115.38

2180

40/41.9955/57.6885/86.740.0283/50.94/
0.031256.16
6001269

60/62.785/83.88125/126.130.0845/152.10/
0.0932167.76

2266

60/32.0580/82.94125/14.720.0418/75.24/
0.046183.98
7001379

90/88.41120/118.17175/177.710.0091/214.38/
0.1313236.34

2358

85/83.51110/111.62165/167.850.0562/101.16/
0.062111.6
8001511

120/119.20160/159.16240/239.600.1605/288.90/
0.177318.6

2488

115/113.83150/152.16230/228.810.0767/138.06/
0.0845152.1
9001649

150/151.39200/202.36305/304.30.2039/367.02/
0.2248404.46