cavitation damage to polypropylene piping in high - … · – saturation, source water •...

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CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH- RISE DHWR APPLICATIONS JAMES R. PASCHAL, P.E.

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Page 1: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH-

RISE DHWR APPLICATIONS

JAMES R. PASCHAL, P.E.

Page 2: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Topics• Temperature

– Air/oxygen, Total Dissolved Gas (TDG) content– Boiler conditions– Saturation, source water

• Pressure– Air/oxygen, Total Dissolved Gas (TDG) content– Strength vs. temperature relationship– Water hammer, pressure surge and low pressure, transient– Cavitation

• Flow– Hydraulic balancing– Flow restriction– Velocity changes, water hammer

• Water Chemistry– Oxidation, pH, ORP– Sources of oxidizing chemicals– Accelerating effects of temperature, catalysts

• Cavitation damage examples– Domestic hot water recirculating systems– Mechanical damage, crack initiation– Stabilizer depletion, crack propagation

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Page 3: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Temperature

• As temperature increases, dissolved air comes out of solution• For plumbing systems, incoming cold water is normally close to saturation

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0

0.02

0.04

0.06

0.08

0.1

0.12

0.14

0.16

0.18

40 60 80 100 120 140 160 180 200

Solu

bilit

y, V

air /

Vw

ater

Temperature, °F

Air solubility in water at 80 psig

Page 4: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Temperature• Gaseous cavitation• Pressure falls below saturation pressure

of fluid• As temperature increases, saturation

pressure decreases• Release of gas, less dissolved gas in

fluid, higher gas concentration out of solution

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Page 5: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Temperature

• As temperature increases, vapor pressure increases• Increases likelihood of vapor bubbles forming in low pressure region

5

0

2

4

6

8

10

12

14

0 50 100 150 200 250

Pres

sure

, psia

Temperature, °F

Saturation pressure vs. Temperature

Page 6: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Temperature

• Vaporous cavitation• Pressure falls below vapor pressure of fluid• As temperature increases, vapor pressure increases• Locally low static pressure will promote the production

of vapor bubble

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Page 7: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Pressure• Pressure surge, water hammer• If air in pipelines can substantially magnify the pressure

surge effects, why do water hammer arresters work?

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4% air pocket

40% air pocket

No air pocket

Experimental and Analytical Investigation of entrapped air in a horizontal pipe3rd ASME/JSME Joint Fluids Engineering Conference, N. Lee, S. Martin

Page 8: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Pressure• Conversely, transient pressure surges, water hammer will

also cause low pressure events• Cavitation (low pressure)

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Pump VFD fail, sudden start/stop

Page 9: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Flow• Balanced flow is critical for:

– Maintaining proper temperatures, – System operation at best efficiency point

(energy savings), and – Reducing or eliminating damage to piping.

• Common in hydronic heating/cooling systems, information and data readily available

• Much less common in plumbing hot water circulating systems

• Balancing valves– Flow restrictors (flow balancing)– Temperature maintenance (thermal

balancing, flow modulation)

• Oversized circulating pumps, or flow imbalance

– High velocity in some legs, low or no flow in others

– High velocity areas can erode/corrode piping, introduce copper into water

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Page 10: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

• Copper erosion/corrosion, pinhole leaks– Often initiated by cavitation, then susceptible to

erosion/corrosion

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Page 11: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Identification• Mechanical stress under

elevated temperature, over-tightened clamp

• Cracks, degradation at clamp location

• Thermal oxidation, excessive temperature,

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Page 12: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Identification• Cavitation-initiated cracks, degradation• Cavitation “divot” at crack origin• Localized excessive stress, stabilizer

depletion susceptible to crack propagation and oxidative degradation

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Page 13: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Identification

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Divot with localized oxidative degradation

Cross-section, crack arrest lines

Page 14: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Identification

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Sample Wall depth OIT, minutes

At divot location

ID (1 mm) 0.3

Mid-wall 21.6

OD (1 mm) 34.8

Undamaged area

ID (1 mm) 16.0

Mid-wall 19.1

OD (1 mm) 40.7

Page 15: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Testing• Standard cavitation test stand, valving to reduce

pressure on suction side of pump• Aluminum pipe for comparison

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Page 16: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Testing• Aluminum pipe cavitation damage• No apparent damage to PP-R pipe

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Page 17: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

Testing• Next Steps

– No apparent damage to PP-R pipe– Damaged pipe in field– Differences in flow restriction vs.

surge for cause of low pressure– Heat aging, oxidation, evaluation of

surface embrittlement• Operation and Maintenance

– Air release– Pump operation, water hammer– Temperature monitoring– Copper corrosion, levels in water

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Page 18: CAVITATION DAMAGE TO POLYPROPYLENE PIPING IN HIGH - … · – Saturation, source water • Pressure – Air/oxygen, Total Dissolved Gas (TDG) content – Strength vs. temperature

QUESTIONS?

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