Repair is an Opportunity to Improve Pump Performance

Written by: Bob Bluse, Hydro East Inc.
Publisher: Pumps & Systems / February, 2012

 

Often all that is needed to improve a pump’s reliability and performance is to provide a high quality inspection and repair. Over time a pump may have been repaired by more than one service provider with varying levels of engineering and technical experience. Tolerances may have been opened up, fits and concentricities may have been lost and materials may have been changed, all of which contribute to reduced performance, loss of reliability and more frequent repairs.

This article highlights the opportunity seized by a coal-fired power station to upgrade a Westinghouse Vertical Pump during the repair process.

 

Background:

The Power Plant’s Unit #4 “Alpha” Circulating Water Pump was scheduled for repair and in the process of removal, the sister pump #4 “Bravo”, exhibited severe vibration and failed in a manner which was believed to have been a result of a broken shaft. The Alpha pump was put back into service and the Bravo pump removed and sent to the repair facility for inspection and emergency repair.

 

Observed Pump Condition:

The general condition of the Bravo pump when received at the repair facility was much worse than anticipated with the top column flange broken about half way around. The entire pump had been hanging from this broken joint leaving a gap of ¼” to ½” at the opening. The keyed coupling (internal to the pump) used to join its two shafts was broken in several pieces, the shaft journals were severely worn to one side and the impeller vanes & suction bell liner surface were also severely worn as expected, considering the significant pump damage.

 

 

After disassembly of the pump, it was also observed that the shaft enclosing tubes had spun in their fits due to not being fitted with any anti-rotation mechanism. This rotation caused damage to the ‘O’-ring fit areas at both ends of the enclosing tube assembly resulting in loss of proper flush water supply to the pump bearings below the packing box. Another issue observed during inspection was that part-to-part alignment of major pump components utilized dowel pins, which are very difficult, if not impossible, to verify.

 

Continue reading

Hydro Scotford Appointed Certified Service Vendor for ITT Goulds Pumps

Hydro Scotford’s pump service facility in Fort Saskatchewan, Alberta, Canada, has been appointed as a certified services vendor for ITT Goulds Pumps. Hydro Scotford provides aftermarket service for high-energy pumping equipment in the oil & gas and power industry markets and will support Goulds’ population of equipment in the Oil Sands region. As an established pump service provider and certified vendor, the Hydro Scotford service facility will operate in accordance with ITT technical, quality and safety guidelines. Repairs and upgrades will be made with the supervision of ITT field service personnel. This new service support will allow ITT to provide reduced cost and improved reliability to their customers in the Alberta area. For more information about Hydro’s comprehensive pump services for Goulds pumping equipment, please call Dennis Plaizier at 780-992-0100.

Calpine Renews National Service Agreement with Hydro

On May 11th, 2010, Hydro was selected as Calpine’s National Pump Repair Supplier. Hydro is proud to announce that the agreement to support Calpine’s operating locations throughout the United States was renewed on January 25th, 2012.

Founded in 1984, Calpine Corporation is the largest publicly traded, independent wholesale power company in the U.S. that can deliver approximately 28,000 megawatts of clean, reliable electricity to customers and communities in 20 U.S. states and Canada, with 91 operating power plants and two under construction. For more information, visit www.calpine.com.

“Combined Cycle 101” Presented by Evans Hydro

Alex Manchenkov, senior engineer and operations manager at Evans Hydro, has agreed to take part in the ASME Combined Cycle Committee Pre-conference workshop entitled “Combined Cycle 101”, which will take place at the 20th International Conference on Nuclear Engineering and is collocated with the ASME Power Conference in Anaheim, California. The 8-hour course offered to end users occurs July 30th through August 3rd and the topic presented by Alex will emphasize the critical pumps found in combined cycle plants, including boiler feed, vertical circulator, condensate, and raw-water pumps. For more information, please contact Angie Vruno at 562-618-7719 or send an email through the Evans Hydro contact form.

Air Void Testing for Safety-Related Feed Pumps in Nuclear Power Plants

Written by: Dr. T. Ravisundar, Ravi Somepalli, and Bill Nagle of HydroAire Inc.
Publisher: Pumps & Systems / December, 2011

 

An Interesting Challenge and Cause for Collaboration

A major nuclear power company approached an independent Pump Performance Test Lab in Chicago to discuss a series of tests for their Pacific 4” BFIDS in safety-related service. These auxiliary feed water (AFW) pumps were utilized in two pressurized water reactor plants to supply backup cooling water to the steam generators in the event the main feed water source was interrupted. The plants had been designed to utilize an air void between two motor operated valves to keep separate two different suction sources to the pump. The Nuclear Regulatory Commission (NRC) guidelines dictated that no more than a 2% air void could be passed through the pump to reliably assure its safety-related function. The nuclear power plant engineers believed the pump could ingest a greater margin of air without damage or impairment to pump performance. The NRC gave the nuclear power company an opportunity to demonstrate the capability of this pump by allowing them to conduct and monitor a series of transient air-void tests at the independent Pump Performance Test Lab.

 

The independent pump performance test lab in Chicago, IL.

Engineers Working Together to Define Test Scope

The nuclear power plant engineers worked closely with the engineers at the Test Lab and a third party engineering consultant to develop the scoping document which defined the tests needed to demonstrate the pump’s capability under a range of scenarios. To design these tests, the team first reviewed the system configuration at the plants.

For added safety, each unit at each plant had one motor driven and one diesel engine driven AFW pump. Each AFW pump had been installed and aligned through valves and piping to take suction from either the non-safety related condensate storage tank (CST) or the nuclear safety related essential service water system (SX). The SX system is the nuclear safety related system that is connected to the plants ultimate heat sink (UHS), which is raw river water. As can be imagined, there is considerable difference in the purity of the water between the CST water and the SX water. Therefore, both plants intentionally built in the air void as a provision for separating these two systems to reduce the chance of SX water contaminating the clean condensate side of the system.

After thorough review, the team issued specifications for ten different sets of test cases which encompassed several operating conditions and well over 35 test scenarios. The tests would cover injection of different void volumes into the pump operating with several variables, some of which included different flow rates, suction pressures, and pump statuses (i.e. operating pump, idle pump with a pump start while suction is being transferred, etc.).

 

Configuring the Test Lab

Once the scope had been clearly defined and agreed upon, the Test Lab engineers set out to configure the Test Lab in a way that would duplicate almost identically the plant’s AFW suction piping set-up. Within 10 days, the Test Lab was configured with a booster pump installed with a variable frequency drive to simulate the SX system as closely as possible so that the safety-related AFW pump could be operated within the same environment as it would function in the plant. The SX water source came from the Test Lab’s 38,000 gallon suppression tank which was fed through the booster pump. The CST, which was simulated by the Test Lab’s suppression tank, was not sent through the booster pump.

 

Continue reading