Branch-Line Pumping and Other Options

Last of Two Parts

Written by:
Joe Evans

Pumps & Systems, March 2013

Last month, this column reviewed several examples of open flow, branch-line pumping applications. We used the Branch Line Pumping Calculator (available at www.PumpEd101.com) to compare a branch-line system with two different discharge elevations to a multi-line system that used two individual pumps. Based on the input data, the multi-line system was more efficient, and its breakeven point was barely more than 2 years.

 

Alternative Systems

In addition to multi-line, multi-pump systems, a system designer has several other alternatives to open-ended, branch-line systems with multiple elevations. One of the most common is the tank-based system. In this type application, a storage tank is installed at or above the upper most elevation. A lower flow pump is used to keep the tank filled, and gravity supplies water, under pressure, to the lower elevation discharge points.


One of the more common examples is a municipal water supply system. Elevated tanks or those located on hillsides use gravity to supply pressure to the surrounding areas. Another example is high-rise buildings. Many older buildings use roof-mounted tanks to supply pressurized water to the upper floors. One more option is to use a single-service line with two or more pumps operating in series. Figure 1 compares this design to an open-branch system.

 

Figure 1. Comparison of a single service line with two or more pumps operating in series to an open-branch system

 

System Comparison

The upper pipeline shown in Figure 1 is the same open-flow, branch-line design illustrated in Part 1. The pump at Point A produces 600 gallons per minute (gpm) at a total dynamic head (TDH) of 200 feet and supplies outflows of 400 gpm and 200 gpm at branch Points B and C. The power required to meet the two branch flows is 43.2 horsepower. The high horsepower is required because the total head seen by the pump is directly proportional to the elevation at Point C.


The pumping system in the lower portion of Figure 1 is different. The pump at Point A still provides 600 gpm, but since it is pumping to Point B only, its discharge head is reduced to 100 feet. A second pump, located at Point B and operating in series, moves the remaining water to Point C. This design reduces the total power required by 33 percent. This results in a smaller pump at Point A that requires 21.6 horsepower and an even smaller one at Point B requiring just 7.2 horsepower. Figure 2 is the calculator portion and compares the variables involved in these two alternatives.

 

Figure 2. The Branch Line Pumping Calculator computations of the systems


As in the configurations in Part 1, the required data are entered into the yellow cells, and the column to the left is the open-flow, branch-line system. The two columns in the middle represent the series system from Points A to B and B to C. The initial cost of the branch-line system is $44,000.


When converting to a series system the cost is reduced by $8,000 because of the smaller pump required at Point A. The additional pump and controls required at Point B adds an additional $11,000 to the cost of the series system. Therefore, the total additional cost for the series system is $3,000. Based on an annual electrical savings of about $3,300, the payback is less than one year.


For this example, the series system is more efficient than the single pump system. It also trumps the two pipeline design shown in Part 1 of this series. The horsepower required for the series system and the two pipeline design are exactly the same, but the lower piping cost of the series system makes it a more cost-effective system.


As I stated in Part 1, my branch-line pumping calculator is not a design tool. Instead, it is an evaluation tool that allows you to compare traditional branch-line systems with several alternatives. Once a choice is made, any number of software systems can assist with the design phase. The Branch Line Pumping Calculator can be downloaded from the “Pump Evaluation, Selection & Testing Tools” page at www.PumpEd101.com.

Note:  Part 1 (February 2013) of this series contained an error.  When describing Figure 2, I said that Point A was at an elevation of 100 feet and Point B is 100 feet higher.  Point A should have been Point B and Point B should have been Point C.


See also:

Upstream Pumping Solutions

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