Application data (cont)
Vent and drain connections
Provide high points of the chiller piping system with vents and the low points with drains. If shutoff valves are provid- ed in the main liquid pipes near the unit, a minimal amount of system liquid is lost when the heat exchangers are drained. This reduces the time required for drainage and saves on the cost of
It is recommended that pressure gages be provided at points of entering and leaving liquid to measure pressure drop through the heat exchanger. Gages may be installed as shown in Pressure Gage Location table. Pressure gages installed at the vent and drain connections do not include nozzle pressure losses.
Use a reliable differential pressure gage to measure pres- sure differential when determining liquid flow. Regular gag- es of the required pressure range do not have the accuracy to provide accurate measurement of flow conditions.
PRESSURE GAGE LOCATION
NUMBER | GAGE LOCATION | |
OF | ||
(Cooler or Condenser) | ||
PASSES | ||
| ||
1 or 3 | One gage in each waterbox | |
2 | Two gages in waterbox with nozzles |
Each heat exchanger and economizer (if equipped) is ASME ‘U’ stamped on the refrigerant side of each vessel.
Relief valve discharge pipe sizing
See page 21 for number of relief valves.
Relief valve discharge piping size should be calculated per the current version of the ASHRAE 15, latest edition, code using the tabulated C factors for each vessel shown in the table below.
23XRV RELIEF VALVE DISCHARGE PIPE SIZING
|
| VESSEL | RELIEF |
| |
|
| VALVE | FIELD | ||
HEAT | FRAME | REQUIRED | |||
RATED | CONNECTION | ||||
EXCHANGER | SIZE | C FACTOR | |||
C FACTOR | SIZE (FPT) | ||||
|
| (lb air/Min) | (lb air/Min) |
| |
| 30 to 32 | 43.4 | 70.8 | 11/4″ | |
| 35 to 37 | 49.5 | 70.8 | 11/4″ | |
COOLER | 40 to 42 | 50.4 | 70.8 | 11/4″ | |
45 to 47 | 57.4 | 70.8 | 11/4″ | ||
| |||||
| 50 to 52 | 53.7 | 70.8 | 11/4″ | |
| 55 to 57 | 61.1 | 70.8 | 11/4″ | |
| 30 to 32 | 41.4 | 70.8 | 11/4″ | |
| 35 to 37 | 47.1 | 70.8 | 11/4″ | |
CONDENSER | 40 to 42 | 47.1 | 70.8 | 11/4″ | |
45 to 47 | 53.7 | 70.8 | 11/4″ | ||
| 50 to 52 | 51.2 | 70.8 | 11/4″ | |
| 55 to 57 | 58.3 | 70.8 | 11/4″ |
ASME stamping
All 23XRV heat exchangers are constructed in accordance with ASHRAE (American Society of Heating, Refrigerat- ing, and Air Conditioning Engineers) 15 Safety Code for Mechanical Refrigeration (latest edition). This code, in turn, requires conformance with ASME (American Society of Mechanical Engineers) Code for Unfired Pressure Ves- sels wherever applicable.
Carrier further recommends that an oxygen sensor be installed to protect personnel. Sensor should be able to sense the depletion or displacement of oxygen in the ma- chine room below 19.5% volume oxygen per ASHRAE 15, latest edition.
Design pressures
Design and test pressures for heat exchangers are listed below.
DESIGN AND TEST PRESSURES (23XRV)
| SHELL SIDE | STANDARD TUBE SIDE | OPTIONAL TUBE SIDE | |||||
PRESSURES | (Refrigerant) |
| (Liquid) |
| (Liquid) | |||
| psig | kPa | psig |
| kPa | psig |
| kPa |
Leak Test at Design Pressure* | 185 | 1276 | 150 |
| 1034 | 300 |
| 2068 |
Hydrostatic | — | — | 195 |
| 1344 | 390 |
| 2689 |
Proof Test* | 204 | 1407 | — |
| — | — |
| — |
*Nitrogen/Helium.
HEAT EXCHANGER MATERIAL SPECIFICATIONS
ITEM |
| MATERIAL | SPECIFICATION |
Shell |
| HR Steel | ASME SA516 GR 70 |
Tube Sheet |
| HR Steel | ASME SA516 GR 70 |
Condenser/Cooler Waterbox Cover |
| HR Steel | ASME SA516 GR 70, |
Condenser/Cooler Waterbox Shell |
| HR Steel | ASME SA675 GR 60, |
| |||
|
|
| |
Tubes |
| Finned Copper | ASME SB359 |
Discharge/Suction |
|
|
|
Pipe |
| Steel | ASME SA106 GRB |
Flanges |
| Steel | ASME SA105 |
LEGEND |
|
| |
ASME — American Society of Mechanical Engineers |
|
| |
HR — Hot Rolled |
|
|
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