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The Split Flow Option | Split Flow Application

Pump Innovations Reduce Motor Size and Capital Cost
Andrew W. Sloley, Director, The Distillation Group, Inc. - asloley@distillationgroup.com
William E. Murray, Split flow, Inc. - billmurray@split-flow.com


Introduction
Making money in distillation or extraction includes looking at more than just towers and their internals. Engineers must also consider the auxiliary equipment. Often, projects proceed without seeking savings for the auxiliary equipment. Higher operating costs and higher capital costs are incurred. Instead, we should examine processes in their entirety to identify opportunities for capital and operating savings.

One opportinuty is the use of Split Flow technology in pumping services associated with towers. Use of the Split Flow feature reduces the number of pumps required. This simplifies piping and electrical, saves space, reduces the number of pump seals, and may simplify control systems. The Split Flow feature can be applied to pumps used for overhead systems, pumparounds, pumpdowns and pumped reboiler systems. One of its features is the ability to produce streams at two different pressures from one pump. Usually, the high-flow, low-head stream returns to the distillation column. The higher-head lower-flow product goes downstream.

This paper discusses options using Split Flow technology to reduce capital and operating costs and describes how API Standard centrifugal pump designs are modified to incorporate the Split Flow option.

Background
The API Standard 610 Forewords, since the January 1981 6th Edition note: Energy conservation is of concern and has become increasingly important in all aspects of equipment design, application, and operation. Thus, innovative energy-conserving approaches should be aggressively pursued by the manufacturer and the user during these steps. Alternative approaches that may result in improved energy utilization should be thoroughly investigated and brought forth. This is especially true of new equipment proposals, since the evaluation of purchase options will be based increasingly on total life costs as opposed to acquisition costs alone. Equipment manufacturers, in particular, are encouraged to suggest alternatives to those specified when such approaches achieve improved energy effectiveness and reduced total life costs without sacrifice of safety or reliability.

Conclusions:
New developments frequently occur in areas important to process plant design. Engineers in every discipline need to be alert for opportunities to save capital and reduce operating costs. We must prevent our habits from blinding us to new ways of improving our plants. The Split Flow option is a new way of reducing operating and capital costs for auxiliary systems.

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