Publicité
Fig2.-FF example scheme of heat exchanger (only demonstration example)
CHAMBERS
Maximum gauge pressure
Minimum gauge pressure (full vacuum a 20°C)
Maximum temperature
2
(tubes)
Minimum temperature
Volume
Fluid
Maximum gauge pressure
Minimum gauge pressure (full vacuum a 20°C)
1
Maximum temperature
(shell)
Minimum temperature
Volume
Fluid
NB: For AXL take into account only chamber 2
WARNING:
THE EQUIPMENT IS SUPPLIED WITH CONNECTIONS FOR THE INSTALLATION OF SAFETY DEVICES WHICH IN ANY
CASE MUST BE SELECTED AND INSTALLED BY THE END USER EITHER ON THE SUPPLY LINES OR ON ANY OTHER
PRESSURE EQUIPMENT DIRECTLY CONNECTED TO IT (THERE MUST NOT BE ANY INTERCEPT POINTS BETWEEN THE
EQUIPMENT AND THE SAFETY DEVICES). AS HIGHLIGHTED IN THE RESIDUAL RISK ANALYSIS, IMPULSIVE STRESS
FORCES DUE TO EARTHQUAKES HAVE NOT BEEN TAKEN INTO ACCOUNT, AS IT IS NOT POSSIBLE TO FORESEE THE
TYPE AND DURATION OF THE APPLICABLE FORCES IN THIS ANALYSIS. IF THE EQUIPMENT IS INSTALLED IN A SEISMIC
ZONE, IT IS THE TASK OF THE END USER TO CHECK THE STABILITY OF THE EQUIPMENT FOR LOADS CAUSED BY
EARTHQUAKES
WARNING:
VALUE REPORTED ON NAME PLATE FOR DIFFERENT FUNCTION CONDITION CONTACT THE
DO NOT EXCEED
MANUFACTURER.
PROJECTS DATA
Tab:-1 Example Design data FF & AXL-FF series Heat Exchanger
GB
- 23
FUNCTION LIMITS
10 barg/11 bar abs
-------
90°C
-10°C
By drawing dm3
GROUP 2/1 FLUID BY PED RULES
10 barg/11 bar abs
-------
90°C
-10°C
By drawing dm3
GROUP 2/1 FLUID BY PED RULES
Publicité
