Using supplemental specifications and upgrading during pump repair provides reliability.

Purchasing the least expensive pump is rarely the wisest choice for users wishing to achieve long run times and low or moderate maintenance outlays. Although a new company may be able to design and manufacture a better pump, newcomers do not always suddenly produce a superior product. Many users choose from the most respected existing manufacturers.

The first step in purchasing should involve selecting and inviting only those bidders who pass certain tests. The following criteria must be met to determine acceptable vendors for situations demanding high reliability:

  • Acceptable vendors must have experience with the specified size, pressure, temperature, flow and service conditions.
  • Vendors must have proven capability in manufacturing with the chosen metallurgy, surface conversion treatment and fabrication method, such as sand casting or weld overlay.
  • Vendors' "shop loading" must be able to accommodate the order within the required timeframe.
  • Vendors must have implemented satisfactory quality control and must be able to demonstrate a solid on-time delivery history over the past several (usually two) years.

Use Supplemental Specifications

Reliability in a process pump is critical. Without an adequate specification, many pump suppliers default their offers and supplies to least expensive initial cost and relatively uncertain delivery times. Neither of these default situations will be in the user's best interest. So, the next steps users should follow when purchasing are:

  • Specify for low maintenance. Selective upgrading of certain components will result in rapid payback. Components that are upgrade candidates have been described in the references at the end of this article.
  • Be sure you specify upgraded components whenever these are available. For example, review failure statistics for principal failure causes. If bearings are prone to fail, realize that the failure cause may be incorrect lube application or lube contamination.

    Address these failure causes in your specification and insist on the best available components, such as the seemingly insignificant bearing protector seals (see Figure 1).

  • Evaluate vendor response. Allow exceptions to the specification if the exceptions are well-explained and valid. The potential reliability impact of waivers should be quantified.
  • Clearly document pump design. The plant will certainly need pump cross-section views and other documents for future repair and troubleshooting work. Do not allow the vendor to claim these documents are proprietary and that you, the purchaser, are not entitled to see them. Place the vendor under contractual obligation to supply all agreed-upon documents in a predetermined time frame. Include in the agreement that you will withhold 10 or 15 percent of the total purchase price until all contractual data transmittal requirements have been met.
  • On critical orders, contractually arrange for access to a factory contact. Alternatively, insist on the nomination of a management sponsor. The salesperson cannot fill this role. A management sponsor is a vice president or director of manufacturing (or a person holding a similar job function) working at the manufacturer's factory or head offices. Communicate with this person for help on issues that could impair pump quality or could seriously delay delivery.
Figure 1. This graph depicts bearing protector seals, also called bearing isolators. The large O-ring in the top left model can be cut by sharp groove corners. The chevron-shaped rotor cross section of the model at top right is likely to create high frictional resistance. The large O-ring in the bottom model moves axially, and two smaller O-rings clamp the rotor to the shaft. This would be the preferred model. (Courtesy of the author)Figure 1. This graph depicts bearing protector seals, also called bearing isolators. The large O-ring in the top left model can be cut by sharp groove corners. The chevron-shaped rotor cross section of the model at top right is likely to create high frictional resistance. The large O-ring in the bottom model moves axially, and two smaller O-rings clamp the rotor to the shaft. This would be the preferred model. (Courtesy of the author)

Following these guidelines will give best assurance of meeting the expectations of reliability-focused owner/purchasers.

Upgrade During Repair

As pump manufacturers go through cycles of consolidation and employee attrition, they often lose valuable employees to early retirement or to pump rebuilders. The rebuilder's focus is competence and customer satisfaction, although valuing the customer's needs should be a priority for both OEMs and non-OEM pump upgrade providers.

Users should look for competent pump repair shops (CPRS). A CPRS will understand the unquestionable merits of having oil rings manufactured with stress-relief annealing as an appropriate intermediate procedural step. A CPRS knows and can readily explain component upgrades worth an incremental cost over inexpensive, risk-prone or traditional products.

One particular CPRS headquartered in the U.S. has branches in the Middle East and other regions. This CPRS uses 3-D mapping of existing pump parts and can catalog these for future use (see Image 1). The facility and its worldwide associates can rapidly produce 3-D casting patterns and molds for needed parts.

Image 1. Mapping, recording, pattern production, casting and machining are efficiently done by a designated CPRS. Knowing component upgrade feasibility and providing cost justification represent additional benefits. (Courtesy of Hydro Middle East)Image 1. Mapping, recording, pattern production, casting and machining are efficiently done by a designated CPRS. Knowing component upgrade feasibility and providing cost justification represent additional benefits. (Courtesy of Hydro Middle East)

If your plant has units with two process pumps per service, the CPRS can rapidly produce the replacement parts for the pump that is out of service while your process unit stays online. Even more exciting is the prospect of your process plant entrusting the CPRS with manufacturing these replacement parts with whatever predefined contours and dimensions will yield higher throughput, greater efficiency or extended safe operating time (see Image 2). Again, it is a possibility that can be explored during the spare parts definition activity for new facilities or during a spare parts audit at an existing plant.

Image 2. Automated impeller welding at a well-equipped CPRS (Courtesy of Hydro Middle East)Image 2. Automated impeller welding at a well-equipped CPRS (Courtesy of Hydro Middle East)

If you were to visit the in-house pump shop of a repair-focused facility, you would probably see the mechanics and machinists working on repeat repairs. The facility's average pump operating life would probably not exceed two or three years, although the stated design life of many components is more likely five to 10 actual operating years. Ten operating years would mean 20 years of field installation for redundant (spared, or parallel-but-standby) pumps—an average seldom reached by even the best refineries. To their credit, the best will not get locked into a cycle of frequent failure and repair. Best-in-class facilities are not excessive consumers of spare parts. Instead, they work closely with a CPRS on predefining upgraded future spares.

Because the best refineries and petrochemical plants are reliability focused, they view every repair event as an opportunity to upgrade. Reliability professionals report to a manager who insists on fully understanding the exact component selection methods, installation procedures and work processes that the facility is pursuing.

This manager then commissions comparisons against best-in-class practices and asks for systematic upgrading at the facility. This is how facilities realize that seemingly minor issues exist and seemingly minor upgrades can be immensely helpful in reaching the stipulated higher reliability and desired maintenance cost-avoidance goals.

Some repair-focused refineries and process plants have already fallen by the wayside. Others are sure to close down unless they become reliability-focused. Learn to focus on understanding the root causes of pump failures. Take advantage of the problems that are easy to fix first. And realize that even the most glitzy maintenance cost-reduction program will fail unless you step in to do a professional's job.

These steps require that you, or your designated professional do the following:

  • Understand that equipment vendors base judgments on operation of machinery under near-perfect conditions, and field conditions are far from ideal.
  • Accept the fact that cost-effective upgrades are possible and that your plant must become familiar with these.
  • Implement the basics that appear in this article.
  • Insist on root-cause failure identification.
  • Refuse to tolerate repeat failures.

Most important, enable and empower someone at your plant to answer two critical questions:

  1. Is an upgrade possible, and what is the benefit-to-cost ratio of such upgrading?
  2. Which CPRS should be pre-qualified and pre-selected as the pump spare parts and upgrading provider?

Correctly answering these two questions will prove profitable.

References

  1. Bradshaw, Simon; Bradshaw et al., Proceedings of the 17th TAMU International Pump User's Symposium, (2000)
  2. Bloch, H.P., "Pump Wisdom: Problem Solving for Operators and Specialists," (2011) John Wiley & Sons, Hoboken, NJ
  3. Bloch, Heinz P., (1998) "Machinery Reliability Improvement," 3rd Edition, Gulf Publishing Company, Houston, TX
  4. Bloch, Heinz P., and Allan Budris; (2013) "Pump User's Handbook: Life Extension," 4th Edition, Fairmont Publishing Company, Lilburn, GA
  5. Bloch, Heinz P.; Updating your Sealing Knowledge," Hydrocarbon Processing, March 2008