Pumping high-temperature process liquids around the clock places extraordinary demands on most system components ," particularly the chemical pumps. In many applications, catastrophic pump failure is seldom an option because it can lead to production downtime, wasted effort, added maintenance costs, ruined final product and personnel hazards.
Because pump performance and reliability are critical issues whenever ," and wherever ," high-temperature liquids are being transferred, the American Petroleum Institute (API) many years ago set forth rigid standards for the design, construction and performance of process pumps used for these applications. The original API standards were issued some 40 years ago for refinery services.
According to the text of API Standard 610, "API standards are published as an aid to procurement of standardized equipment and materials. These standards are not intended to inhibit purchasers or producers from purchasing or producing products made to other standards."
The intent was to minimize failure possibilities from known causes with appropriate pump design and construction materials. Most of these requirements are stated in API Standard 610.
Over the years, however, a number of revisions have been made to that standard as more experience was gained through high-temperature process pump use. The changes also reflect the significant improvements made in pump design and construction materials.
Some manufacturers offer lower-cost pumps with many API-standard design and construction features by eliminating unnecessary documentation and testing.
Rising costs spark alternatives
Some manufacturers of high-temperature heavy-duty process pumps have refined their products often to meet subsequent revisions to the original standard. With each revision, the cost of API-type pumps continued to rise above that of other heavy-duty process pumps not meeting the API standard. Chemical pump users had little choice when selecting heavy-duty process pumps for many applications.
The American National Standards Institute (ANSI) eventually issued its own standards for chemical pumps. Those standards are not nearly as restrictive, nor as comprehensive, as API's, particularly in the areas of testing, documentation and traceability requirements. Consequently, ANSI-type pumps cost substantially less than API-type pumps.
API vs. ANSI
ANSI-type pumps do not incorporate many of the design and construction features specifically mandated for the extreme service typically encountered by API service pumps (see the table). For example, centerline support structures in API-type pumps are not required in ANSI-type pumps. Without centerline support, however, shaft alignment could lose concentricity under continuous high-temperature use. Premature bearing, coupling and/or seal failure could result. Other design/construction differences include heavy-duty baseplates and steel bearing housings, all of which are required in API-type pumps but not in ANSI standard pumps.
To bridge the gap between high-end API-type pumps and lower-cost ANSI-type pumps, some manufacturers offer pumps that incorporate many of the design and construction features required by the API standard at a substantially lower cost. They can do so by eliminating the extensive documentation and testing requirements that might be deemed unnecessary for many applications.
Revision eliminates restrictions
According to API sources involved in the standard's development, API Standard 610, Ninth Edition was approved in January of this year. This newest revision specifically allows users to employ non-API-style pumps in services defined by parameters addressed in "Section 1 ," Scope" of the standard. (Prior to this revision, users could employ a non-API pump in hazardous flammable operations, but the pump was not "approved" by API.) Although the API standard's Eighth Edition (Paragraph 1.1.4) includes these same service limits, it also specifies that the allowable services be "nonflammable and nonhazardous."
The Ninth Edition eliminates this restriction, permitting the use of non-API pumps in process and utility services, provided the stated criteria on performance and construction are met. As a result, many new and existing users of API-610 pumps now can take advantage of the lower costs offered by intermediate pumps for flammable and hazardous service without affecting performance, safety or reliability.
Like previous editions, the API-610 Ninth Edition also lists specific limits for process and utility services that allow the use of "pumps designed in compliance with other standards such as ISO 5199 or ANSI/American Society of Mechanical Engineers [ASME] B73.1M." In particular, the stated parameters mentioned are maximum discharge pressure (275 pounds per square inch gauge [psig]), maximum suction pressure (75 psig), maximum pumping temperature (300F), maximum rotating speed (3,600 rotations per minute [rpm]), maximum rated total head (400 feet [ft]) and maximum impeller diameter (13 inches [in.]).
Non-API pumps in service
Although the decision to use non-API pumps in flammable and hazardous service must be determined on an individual basis, many organizations have been using alternative pumps for these applications on a routine basis.
"Basically, users who require the ultimate' pump for high-temperature hot oil requirements ," the safest, heaviest possible pump ," with cost as no object would specify an API-610 pump," emphasizes Will McKnight, a vice president with Process Equipment Co. in Fort Mills, S.C. He has been involved with applications engineering for high-temperature pumps in the chemical and petrochemical industries for many years. "On the other hand, if a user requires a pump for virtually the same service at a substantially less[er] cost, a non-API pump such as described here is quite suitable. In our experience, some engineers just have a mindset' on the use of API pumps," McKnight maintains.