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Combined Cycle Plant Applications

FrothFlush™     Condensate and Feedwater

                                                  Results:

                                                  •Targets
SigmaClean™          HRSG Watersides              •Steam Chemistry

                                                  •Water Cycle Chemistry

                                                  •Stabile Operation
              Superheaters/Reheaters/MS piping,
SigmaBlow™               Condenser
•
•
•
•
•




•
•
•

•




•
•

•
•
Why       FrothFlush TM?


• Very high Reynolds numbers and complete turbulence using
  small quantities of water return the fastest, highest quality
  and most consistent flushing of pipe circuits
• Cleaning to this level prevents contaminates from entering
  the steam generation equipment.
• Improves water chemistry in the HRSG which in turn
  improves the ability to achieve steam purity.
• Current cleaning requirements result in minimal feedwater
  and condensate suction strainer fouling.
Froth Former Setup
FrothFlush™



                 6 inch pipe, 1,000 feet in length
                 40 feet per second
                 “Froth” (compressible) Air / Water “slug”

 The FrothFlush™ process utilizes short two phase (air/water) frothed slugs
 displaced at velocities of 15 20 meters/sec generating Reynolds numbers of
 4 5 million to remove both particulate and non particulate contamination
 from the metal surfaces.
FrothFlush™
              Full Turbulence




Effectiveness of FrothFlush™ is due to generation of full turbulence that
scrubs particles and salts from pipe & tube surfaces
Improved
                           Cleanliness
•   The FrothFlush™ effectiveness in removal of particulate contamination is
    monitored by means of Millipore filters. Samples of the flush effluent water
    are taken and filters using fine Millipore filters.
•   Millipore filters are so fine that the water sample will not flow through the filter
    without the aid of a vacuum to draw the sample water through the filter.
•




•   The effectiveness of the FrothFlush™ process in removal of salts from the
    metal surfaces is monitored by measurement of the conductivity of the
    effluent flush water.
•   VGB Guideline for acceptable solids in flush water is < 5 mg/l.
    FrothFlush™ will typically achieve cleanliness of < 0.05 mg/l.
•   The VGB Guideline for acceptable flush water conductivity is < 1,000 S/cm.
    The FrothFlush™ process typically achieves flush water effluent < 50 S/cm.

VGB(ISO-3166-1, British Virgin Islands)
Typical
                     FrothFlush™
                        Results




First FrothFlush™          11th Froth FrothFlush™         Final Effluent on
                                                          20th FrothFlush™


          The above sequence of photographs show the typical
              results of a FrothFlush™ of a piping system
Millipore®
                        0.45 Micron Patch Test




                         First FrothFlush™ (500ML)   11th FrothFlush™ (500ml)   Final Acceptable at 20th Pass
                                  600 S/cm                   60 S/cm                FrothFlush™ (500ml)
                                                                                         15 S/cm


                           System cleanliness far exceeds criteria specified in VGB
BES&T Millipore™ Test
     Apparatus             Guideline and all other water flush methods.
FrothFlush™
                     Preheat & Economizer
                         Coil Flushing

• Contamination is proportional to system metal surface area.
• Contamination is proportional to amount fabrication to build a HRSG coils.
  Cutting, grinding, welding and PWHT generates more contamination.
• Piping typically contributes less contamination than HRSG coils to the
  steam cycle as piping has less metal surface and less fabrication.
• The FrothFlush™ process effectively flushes contamination from HRSG
  preheat and economizer coil sections at high velocity and high turbulence.
• Effective removal of particulate and non-particulate contamination prior to
  gas turbine first fire minimizes fouling of BFW pump and attemperator
  strainers and sensitive control valve trim.
• Removal of imbedded salts from metal surfaces of the pre-boiler piping and
  coils reduces the tine required to achieve steam cycle purity.
Froth flush process
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Froth flush process

  • 1. Combined Cycle Plant Applications FrothFlush™ Condensate and Feedwater Results: •Targets SigmaClean™ HRSG Watersides •Steam Chemistry •Water Cycle Chemistry •Stabile Operation Superheaters/Reheaters/MS piping, SigmaBlow™ Condenser
  • 3. Why FrothFlush TM? • Very high Reynolds numbers and complete turbulence using small quantities of water return the fastest, highest quality and most consistent flushing of pipe circuits • Cleaning to this level prevents contaminates from entering the steam generation equipment. • Improves water chemistry in the HRSG which in turn improves the ability to achieve steam purity. • Current cleaning requirements result in minimal feedwater and condensate suction strainer fouling.
  • 5. FrothFlush™ 6 inch pipe, 1,000 feet in length 40 feet per second “Froth” (compressible) Air / Water “slug” The FrothFlush™ process utilizes short two phase (air/water) frothed slugs displaced at velocities of 15 20 meters/sec generating Reynolds numbers of 4 5 million to remove both particulate and non particulate contamination from the metal surfaces.
  • 6. FrothFlush™ Full Turbulence Effectiveness of FrothFlush™ is due to generation of full turbulence that scrubs particles and salts from pipe & tube surfaces
  • 7. Improved Cleanliness • The FrothFlush™ effectiveness in removal of particulate contamination is monitored by means of Millipore filters. Samples of the flush effluent water are taken and filters using fine Millipore filters. • Millipore filters are so fine that the water sample will not flow through the filter without the aid of a vacuum to draw the sample water through the filter. • • The effectiveness of the FrothFlush™ process in removal of salts from the metal surfaces is monitored by measurement of the conductivity of the effluent flush water. • VGB Guideline for acceptable solids in flush water is < 5 mg/l. FrothFlush™ will typically achieve cleanliness of < 0.05 mg/l. • The VGB Guideline for acceptable flush water conductivity is < 1,000 S/cm. The FrothFlush™ process typically achieves flush water effluent < 50 S/cm. VGB(ISO-3166-1, British Virgin Islands)
  • 8. Typical FrothFlush™ Results First FrothFlush™ 11th Froth FrothFlush™ Final Effluent on 20th FrothFlush™ The above sequence of photographs show the typical results of a FrothFlush™ of a piping system
  • 9. Millipore® 0.45 Micron Patch Test First FrothFlush™ (500ML) 11th FrothFlush™ (500ml) Final Acceptable at 20th Pass 600 S/cm 60 S/cm FrothFlush™ (500ml) 15 S/cm System cleanliness far exceeds criteria specified in VGB BES&T Millipore™ Test Apparatus Guideline and all other water flush methods.
  • 10. FrothFlush™ Preheat & Economizer Coil Flushing • Contamination is proportional to system metal surface area. • Contamination is proportional to amount fabrication to build a HRSG coils. Cutting, grinding, welding and PWHT generates more contamination. • Piping typically contributes less contamination than HRSG coils to the steam cycle as piping has less metal surface and less fabrication. • The FrothFlush™ process effectively flushes contamination from HRSG preheat and economizer coil sections at high velocity and high turbulence. • Effective removal of particulate and non-particulate contamination prior to gas turbine first fire minimizes fouling of BFW pump and attemperator strainers and sensitive control valve trim. • Removal of imbedded salts from metal surfaces of the pre-boiler piping and coils reduces the tine required to achieve steam cycle purity.