Heatcraft Refrigeration Products When Are Expansion Loops Required? Understanding Expansion Loops and Their Tables

Page 9

Parallel Compressor Systems

Expansion Loops

Suction, liquid and remote condenser lines are subject to expansion and contraction and proper piping techniques must be employed (especially on hot gas lines) to prevent line breakage. This is critical on long straight runs of generally 70’or more where expansion loops must be provided and hangers should allow for longitudinal movement of the piping.

On a refrigeration system with gas defrost, the refrigerant lines expand and contract with temperature changes. The suction line normally has the greatest movement since it has the largest temperature change during defrost. If the expansion and contraction is not planned for during the installation of refrigeration lines, kinking and breaking of the lines could occur.

In order to compensate for the expansion of the tubing, it is necessary to estimate the amount of expansion and then provide offsets or loops in the refrigerant piping. Normally the area to be most concerned with is the straight line distance from the fixture to the parallel compressor unit.

A simple form of expansion loop can be made of soft tempered copper tube by bending it to the correct size and shape. A neater type is made by assembling hard tube with solder elbows as in Figure 9. The correct proportions of such expansion loops to meet various conditions are shown in Table 1.

In compensating for expansion and contraction, two items are very important:

Liquid and suction lines can not be joined together and should not touch at any point

Figure 9. Offsets

Table 1. Expansion Chart

Table of Values for “L”

Pipe hangers must be located and installed in such a manner as not to restrict the expansion and contraction of the tubing. All tubing clamps should have an insulating material (i.e. Hydra Sorb bushing) to prevent metal to metal contact

Ref. Line

 

 

 

Amount of Expansion (in.)

 

 

 

OD (in.)

1/2

1

1-1/2

2

2-1/2

3

4

5

6

7/8

10

15

19

22

25

27

30

34

38

 

 

 

 

 

 

 

 

 

 

1-1/8

11

16

20

24

27

29

33

38

42

1-3/8

11

17

21

26

29

32

36

42

47

 

 

 

 

 

 

 

 

 

 

1-5/8

12

18

23

28

31

35

39

46

51

 

 

 

 

 

 

 

 

 

 

2-1/8

14

20

25

31

34

38

44

51

57

2-5/8

16

22

27

32

37

42

47

56

62

 

 

 

 

 

 

 

 

 

 

NOTES: Calculations for expansion and contraction should be based on the average coefficient of expansion of copper which is .0000094 per degree Fahrenheit between 77°F and 212°F. Example, the expansion for each 100 feet of length of any size of tube heated from room temperature of 70°F to 170°F, a rise of 100°F, is:

100°F (rise °F) X 100 (linear feet) X 12 (inches) X.0000094 (coefficient) = 1.128 inches

(Reprinted from Copper & Brass Research Association)

Parallel Compressor Systems Installation & Operations Manual, October 2004

9

Image 9
Contents Parallel Compressor Systems Table of Contents Inspection IntroductionUnit Designation Model DefinitionRigging System WarrantyLocation Of Equipment Indoor Clearances Floor & Foundation RequirementsGround Mounting Location of Equipment OutdoorRoof Mounting Unit Vibration IsolationVertical Clearance Unit AccessDecorative Fences Units in PitsElectrical Ventilation Requirements Indoor UnitsRefrigerant Piping Suction P-TrapsRefrigerant Line Support Refrigerant Line InsulationExpansion Loops Table of Values for LRef. Line Amount of Expansion Equivalent Feet of Pipe Pressure Loss of Liquid RefrigerantsLiquid Line Rise in Feet Refrigerant 10’ 20’ 25’ 30’ 40’ 50’ 75’ 100’Weight of Refrigerants in Copper Lines During Operation Suction Line at Suction TemperatureLine 40F 20F Recommended Line Sizes for R-404A/R-507 Expansion Valve Liquid Line SizeLengths 100’ 150’ 200’ 25’Recommended Line Sizes for R-22 Suction Line SizeCapacity 40˚F 20˚F 10˚F 10˚F Liquid Line Size Suction TemperatureNet Recommended Remote Condenser Line Sizes12 & R-134A 502 507 & R-404A TotalLeak Checking, Evacuation and Start-up EvacuationStart-up Off-Cycle Refrigerant DistributionElectric Defrost Priority I Hot Gas DefrostSystem Balancing Electronic Control SystemSystem Superheat Evaporator SuperheatCopeland Compressors 4D/6D Solid State Modules CompressorsTypical Voltage Ranges Unloader FactorsOil Charges Oil Safety SwitchApproved Copeland Lubricants Carlyle CompressorsPhase Voltage Monitor Part Load Performance MultipliersRequired Differential Pressure for Unloader Operation Sight Glass Safety Relief Devices Sight Glass & Moisture IndicatorDischarge Piping Table Henry Relief Valve Capacity RatingManual Reset Models Auto Reset ModelsLiquid Level Switch Level Switch TableModule Replacement Oil ControlOil Separators Temprite Valve Adjustment Temprite ModelsOil Level Regulators AC&R Model Regulators Troubleshooting Oil SystemLiquid Filter-Driers & Suction Filters Sporlan Valve CoSuction Filter CompressorMotorBurnoutCleanupProcedureSporlan Valve Company Replaceable Suction FilterType AFD for cleanup Type DF for cleanupSuperior Valve Company Type F FilterField Adjustment Recommended Valve SettingsHot Gas Bypass Regulator Adjustment Liquid Drain Control MethodControl Settings for R-404A/R-507 Control SettingsControl Settings for R-22 Low Pressure Switch Setting for RmccWeekly General Maintenance ScheduleMonthly QuarterlyTemperature Symptom Cause Remedy CompressorDoes Not Run Unit ShortSwitch Open Symptom Cause Remedy LowHigh Suction Low SuctionSystem Reference Data Service Record