Engineered Replacement Parts
A refinery’s vertical pump passes the test, verifying its performance before installation.
The rotating equipment engineers at BP’s Whiting Refinery in Indiana approached the support team at a pump service center in Chicago to discuss testing its rebuilt vertical turbine pump in the center’s new 5,000-horsepower test lab. Their pump, a Johnston 40 GMC pump, is one of four pumps used for the refinery’s rainwater drainage and process sewer system. This pump is the first pump in line and has a diffuser built onto the suction bell to direct flow into the pump.
Two other pumps are in line behind this pump and a fourth pump is to the side. All are mounted in a large concrete channel system. BP had implemented a specially designed suction strainer on this pump to minimize potential sump vortexes from entering the pump through the suction side of the impeller.
Hydro’s 5000 HP Test Lab in Chicago, IL
This vertical pump had been rebuilt and modified by trimming the impeller and opening the inlet diameter (ID) of the suction bell to improve the flow path characteristics into the impeller eye opening. The refinery wanted verification that the modifications made to the pump resulted in the calculated decreases in horsepower and NPSH required. The goal of the tests, as defined by the refinery, was to determine the operating characteristics, including head (total discharge head—TDH), flow and horsepower, as well as the minimum submergence level of the pump so it could adjust its operating set points and submergence level alarms to avoid cavitation damage.
As the pump service center maintains an “open door” policy, several individuals from the refinery visited the test lab over a two-day period to observe the testing process, which proved to be an educational experience.
Johnston 40 GMC vertical pump on the test stand
The Performance Test
The service center engineers conducted the performance test and used a validation program to calculate the efficiency using data inputs such as flow, horsepower, barometric pressure, suction level, discharge pressure, temperature and specific gravity of the water, diameters of the piping system and the location of discharge collection points.
The pump’s best efficiency point (BEP) was proved at just under 18,000 gallons per minute, at about 130 feet of head, using about 750 horsepower. Proving the BEP of its pump will enable BP to determine how it should operate the pump most efficiently in the field.
The Minimum Submergence Level
Ironically, the test pool turned out to be a close replication of the refinery’s sump. This enabled the service center engineers to confirm BP’s suction strainer had been effectively designed. The witnesses to the test could visually see how the suction strainer sheared vortexes that had developed in the sump at low submergence levels.
Photo above shows vertical pump operating at lowest possible
sump level just before cavitation could occur
Jeff Johnson has 36 years experience in the pump service industry covering numerous markets. Johnson joined Hydro in 2009 and was appointed vice president of Hydro’s Petroleum and Pipeline Division. He was instrumental in the design and construction of Hydro’s new 5,000-Horsepower Test Lab.
With a BS in Mechanical Engineering, Bill Rademacher has been a member of BP’s Rotating Equipment Group at the Whiting Refinery for more than 20 years.