file:///C:/DOCUME~1/ADMINI~1/LOCALS~1/Temp/msohtml1/01/clip_image002.gif | | Runtime Messages | | | Page 4 |
| | | Released to the following HTRI Member Company: | | | | |
| | | langsen | | | | |
| | | tfd | | | | |
| Xist E Ver. 5.00 2014-6-17 13:18 SN: Friendsl | | | | | SI Units |
| | | | | | | |
| GCP2014-006-001 | | | | | | |
| Rating - Horizontal Multipass Flow TEMA BEM Shell With Single-Segmental Baffles | | | | | | |
| Unit ID 100 - WARNING MESSAGES (CALCULATIONS CONTINUE) | | | |
| | | | | | | |
| The vapor specific heat of the hot fluid is calculated in the area of the critical temperature. The | | | | | | |
| linear interpolation of the vapor specific heat and the sensible heat duty may be inaccurate in this | | | | | | |
| region. Specify the vapor specific heat and/or the heat release curve for this case. | | | | | | |
| | | | | | | |
| The physical properties of the hot fluid have been extrapolated beyond the valid temperature range. | | | | | | |
| Check calculated values. | | | | | | |
| | | | | | | |
| WARNING-Crossflow velocity exceeds critical velocity, indicating probability of fluidelastic instability | | | | | | |
| and flow-induced vibration damage. If present, fluidelastic instability can lead to large amplitude | | | | | | |
| vibration and tube damage. | | | | | | |
| | | | | | | |
| WARNING-Crossflow velocity at baffle tip exceeds critical velocity, indicating a probability of | | | | | | |
| fluidelastic instability and flow-induced vibration damage. If present, fluidelastic instability can lead | | | | | | |
| to large amplitude vibration and tube damage. | | | | | | |
| | | | | | | |
| NOTE-Tube vibration from vortex shedding is possible. Check the crossflow-induced vibration | | | | | | |
| amplitude on Line 27 of the Vibration Analysis report for an asterisk. If no asterisk prints, probability | | | | | | |
| of tube damage is low. | | | | | | |
| | | | | | | |
| NOTE-Tube vibration from turbulent buffeting is possible. | | | | | | |
| | | | | | | |
| Bundle entrance velocity exceeds 80% of critical velocity, indicating that fluidelastic instability and | | | | | | |
| flow-induced vibration damage are possible. Fluidelastic instability can lead to large amplitude | | | | | | |
| vibration and tube damage. | | | | | | |
| | | | | | | |
| WARNING-Shell entrance velocity exceeds critical velocity, indicating a probability of fluidelastic | | | | | | |
| instability and flow-induced vibration damage. If present, fluidelastic instability can lead to large | | | | | | |
| amplitude vibration and tube damage. | | | | | | |
| | | | | | | |
| Bundle exit velocity exceeds 80% of critical velocity, indicating that fluidelastic instability and | | | | | | |
| flow-induced vibration damage are possible. Fluidelastic instability can lead to large amplitude | | | | | | |
| vibration and tube damage. | | | | | | |
| | | | | | | |
| WARNING-Shell exit velocity exceeds critical velocity, indicating a probability of fluidelastic instability | | | | | | |
| and flow-induced vibration damage. If present, fluidelastic instability can lead to large amplitude | | | | | | |
| vibration and tube damage. | | | | | | |
| | | | | | | |
| WARNING-Shell entrance rho-v-squared exceeds TEMA maximum recommended value of 5950 | | | | | | |
| kg/m s2 (4000 lb/ft sec2). | | | | | | |
| | | | | | | |
| WARNING-Shell exit rho-v-squared exceeds TEMA maximum recommended value of 5950 kg/m s2 | | | | | | |
| (4000 lb/ft sec2). | | | | | | |
| | | | | | | |
| Xvib can be used for a more detailed analysis of individual tubes in the bundle. | | | | | | |
| | | | | | | |
| The inlet unsupported span length (inlet baffle spacing + central baffle spacing) exceeds the TEMA | | | | | | |
| maximum unsupported span length. | | | | | | |
| | | | | | | |
| The central unsupported span length (twice the central baffle spacing) exceeds the TEMA maximum | | | | | | |