Tubular heat exchanger

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Tubular heat exchanger

1.The standard design pressure is only considered from a pressure perspective. When using steam, the maximum design temperature of the equipment shall not be exceeded.

2.Saturated steam at 160°C (320°F) corresponds to 6 bar.

3.Tube side design pressure: 1500 kPa, shell side design pressure: 1000 kPa.

Heat Exchanger Tube AISI 316 (L)
Shell AISI 304 (L)
Design Temperature 160°C
Specification & Model Shell Side Flange Flange Pressure Standard
RT-CIP 0 51×1.5 DIN DN65/ANSI 3" PN 16
RT-CIP 1 63.5×2 DIN DN65/ANSI 3" PN 16
RT-CIP 2 76×2 DIN DN100/ANSI 4" PN 16
RT-CIP 3 101×2 DIN DN100/ANSI 4" PN 16
RT-CIP 4 101×2 DIN DN100/ANSI 4" PN 16
Selection Table
Flow rate(m³/h) 50-70°C 60-80°C 70-90°C
15 RT-CIP 0 RT-CIP 0 RT-CIP 0
20 RT-CIP 0 RT-CIP 0 RT-CIP 1
25 RT-CIP 0 RT-CIP 1 RT-CIP 1
30 RT-CIP 1 RT-CIP 1 RT-CIP 2
35 RT-CIP 1 RT-CIP 2 RT-CIP 2
40 RT-CIP 2 RT-CIP 2 RT-CIP 3
45 RT-CIP 2 RT-CIP 2 RT-CIP 3
50 RT-CIP 2 RT-CIP 3 RT-CIP 4
55 RT-CIP 3 RT-CIP 3 RT-CIP 4
60 RT-CIP 3 RT-CIP 3 RT-CIP 4
Note: The calculation in this table is based on the working condition of steam at 3 bar (134°C) at the medium inlet.