*By Matthew Wirth*

Among people whose job it is to engineer systems and size equipment, there is a phrase commonly used by all: “You can’t do that!” Playing with numbers and ignoring the laws of physics and mathematics will land one in a world of trouble—costing time, money and resources. There is a place for sound science and engineering and it is found in the numbers. While math was not a favorite subject for many students, it was an effective form of sedation. For those who slept through math class, it is not too late to learn—water math is crucial to effective water treatment. The good thing is the math whiz folks within the industry simplified many of the equations and developed handy charts and graphs to help the mathematically challenged avoid trouble. In this article, take a math refresher course and possibly discover a few new ways of viewing complex equations and difficult hydraulic theory.

**Square footage (sq. ft./ ft2)**

One of the most important and most used values in water math is square feet (ft2) (see Figure 1). It determines filter loading rates (capacities), media backwash rates, pressure drop through a media bed and the starting calculation in establishing media volumes and bed depths (see Figure 2).

**Figure 1**

**Figure 2**

The equation for calculating the square feet within a circle is πr2 (π = 3.14), where r is the radius or half the diameter (D). The industry sizes tanks and pipes in inches. Media and flowrate specifications come in square feet. Here is an easy shortcut to simplify a diameter expressed in inches and have the equation’s result come out in square feet. The equation is:

D2/183 or (D x D) ÷ 183. For further discussion, note that A ÷ B is mathematically represented as A over B or A ÷ B.

This equation replaces πr2 ÷ 144, where r is inches and there are 144 square inches in a square foot. D2 ÷ 183 (D2/183) is accurate, quick and easy because manufacturers give their tank sizes in diameter inches.

Here is an example of the calculations for a 10-inch-diameter tank using both equations:

Pi = π = 3.14. Pi is not a mysterious number. It is simply the number of times a circle’s diameter goes around that circle’s circumference.

D = 5; D2 = 5 x 5 = 25

πr2 ÷ 144 = 3.14 (25) /144; 78.5/144 = 0.54 ft2

within a 10-inch circle or

D2 ÷ 183 = (10 x10) ÷ 183 = 100/183 = 0.54 ft2

Again, it is a quick and easy equation to use and remember (D2 ÷ 183 = D2/183). Try it. A 30-inch tank is 900/183 = 4.9 ft2. It works every time.

A rectangle or square is simply sides A x B. If A = 2 ft. and B = 3 ft.; then the squared value is 2 x 3 = 2 (3) = 6. For further discussion, note that A x B is mathematically represented as A next to B or A(B) (see Figure 3).

**Figure 3**

*Volume (cubic feet) (cu. ft./ ft3)*

**Figure 4**

Volumes are three dimensional, requiring three measurements. If the square footage is known, simply multiply by the height and the result is cubic feet (see Figure 4). The geometric equation for calculating the cubic feet within a cylinder (tank) is: πr2 h. Knowing the square footage of the cylinder, simply multiply ft2 times the height. Looking at the 10-inch tank with 0.54 ft2, then each foot of depth is 0.54 ft3 (cubic feet). A three-foot bed depth in a 10-inch-diameter tanks is:

D2/183 x 3 = 100/183 x 3 = 0.54 x 3 = 1.62 ft3

Another example is a 24-inch-diameter tank with a three-foot bed depth: D2/183 x 3 = D2/183 (3) = (24 x 24/183) (3) = 3.14 (3) = 9.42 ft3

A rectangle is W x L x H. Use measurements in feet to get cubic feet.

**Loading per square foot**

Manufacturers provide hydraulic loading rates in their specifications under operating conditions (see Figure 5). Using a common loading rate of five gallons per minute per square foot (5 gpm/ft2), here is the math to determine the size of a media filter vessel to filter 20 gpm:

20 gpm ÷ 5 gpm/ft2 = 20/5 = 4 ft2

**Figure 5**

Knowing that particulate ( i.e., iron, turbidity, etc.) loads at a rate of five gpm/ft2 and the flow is 20 gpm, then the application requires 4 ft2 of filter surface area. Using the available tank sizes (see Chart A), one can easily choose the tank required to handle the filtration of 20 gpm @ 5 gpm/ft2. From the chart, it takes a 30-inch-diameter tank to handle 20 gpm at a hydraulic loading rate of 5 gpm/ft2.

D2/183 = (12 x 12) ÷ 183 = 144/184 = 0.79 ft2; 5 gpm/ft2 x 0.79 ft2 = 3.95 gpm

**Backwash rate per square foot (gpm/ft2)**

Having the square foot calculation for a tank, one can easily calculate the backwash flowrate required for that tank. Assuming a backwash flowrate of 12 gpm/ft2 and a 12-inch-diameter tank with 0.79 ft2 (from Chart A), then the required flow to drain during backwash is: 12 x 0.79 = 12 (0.079) = 9.48 gpm.

Because there is no such thing as a 9.48-gpm drain line flow control (DLFC), it makes sense to round out to a DLFC of 10 gpm. Just double-check the bed expansion curve to ensure that there is adequate freeboard to handle the bed expansion during backwash.

**Figure 6.** Backwash bed expansion

Having the square foot calculation for a tank, one can easily

calculate the backwash flowrate required for that tank. Assuming a backwash flowrate of 12 gpm/ft2 and a 12-inch-diameter tank with 0.79 ft2 (from Chart A), then the required flow to drain during backwash is:

12 x 0.79 = 12 (0.079) = 9.48 gpm

**Bed expansion**

Bed expansion (Figure 6) is a function of bed depth and the lift or expansion of the bed at a given flowrate to the drain during the backwash cycle. Filter beds require expansion during backwash to lift the captured material loaded on and in the top surface of the bed (see Figure 7).

**Figure 7**

Allowing for a 30-percent specified bed expansion and 50°F water, looking at Figure 6, it specifies a 15 gpm/ft2 flowrate. Note: Best practices look for 30 psi feed pressure at the given backwash flow for optimum results in residential applications. For large commercial and industrial systems, it typically requires 40 psi for adequate lift during backwash. Assuming a 30-inch bed depth, the bed will expand: 30 (30 percent) = 30 (0.3) = 9 inches

Knowing this, a 30-inch bed will expand to 39 inches during backwash. To ensure that the bed material remains in the tank during backwash make sure that the freeboard (open space between the top of the media bed and the top of the tank) is greater than nine inches. It is common practice to leave 50-percent freeboard in media tanks. Note: Only use the side shell height (Figure 1) in calculating available freeboard and bed depth. If the media reaches the curvature of the tank during backwash, it is lost to the drain (see Figure 8).

**Figure 8**

**Empty bed contact time (EBCT)**

Empty bed contact time is a calculation used in adsorption, ion exchange and retention time. It is a calculation of how long water is in contact with media or chemicals. If an arsenic adsorptive media requires two minutes of EBCT, water must take two minutes to pass through the media. To calculate EBCT in measurements learned earlier in this lesson, use 7.48 gallons/ft3. To calculate a 10-gpm flow with an EBCT of two minutes in cubic feet (ft3), use these equations:

2-min. EBCT expressed in cubic feet is: (7.48 gal/ft3)/2 minutes = 7.48/2 = 3.74 gpm/ft3

10 gpm with 2-minute EBCT is: 10 gpm/(3.74 gpm/ft3) = 2.7 ft3

*Bed volumes (BV)*

Bed volumes are a measurement of how much water can pass through a media bed before it reaches exhaustion— commonly called throughput. Staying with arsenic adsorption, a bed-life estimate for arsenic adsorptive media with 50 ppm As(V), ortho-phosphate 0.15 ppm, silica 20 ppm and a pH of 7.2 is 55,000 BV. One can calculate how many gallons will pass through the media before arsenic breaks through above the maximum contaminant level. Knowing that there are 7.48 gallons per cubic feet, one cubic foot of arsenic adsorptive media with a throughput of 55,000 BV will treat 7.48 gals/ft3 (55,000 BV) = 441,400 gallons.

*Playing with the numbers*

Whenever an operating specification calls out a BV, maximum flowrate, EBCT, etc., it is providing the best-case scenario. An automobile engine is not designed to run at 8,000 rpm just because it can. The same engine runs optimally around 2,000 rpm. In the Olympics, the 100-meter dash is classified as a sprint. The 5,000-meter race is classified as long distance. This is because human beings cannot sprint for 5,000 meters. They will exhaust and fail.

Try to be conservative when looking at operating specifications and look for the optimum numbers, not the maximums. Manufacturers of POE and POU systems, media and related products provide conditions of operations. Refer to these specifications and use good old common sense when applying water technologies.

**Sound science and engineering**

Designing and troubleshooting equipment requires that one knows the math. Learning and using water math requires practice. Do the homework. Once the equations become part of everyday use, the numbers and calculations become instinctive—and make everyone smarter and better professionals.

**About the author**

*Matthew Wirth, Layne Christensen Commercial Sales, Water Technologies POE/POU Division, is responsible for the region west of the Mississippi River. He is a 32-year professional in the water industry and an active trainer for several national organizations. Wirth has extensive experience in light C&I, POE and POU problem-water applications. A graduate of Concordia University in St. Paul, MN with a BA Degree in organizational management and communications, he received engineering training at the South Dakota School of Mines and Technology in Rapid City, SD. He can be reached at [email protected] or cell phone, (319) 333-4174.*

*About the company*

*Layne Water Technologies (www.laynewater.com) owns the LayneRT adsorptive technology and offers it in multiple residential and commercial configurations through a network of approved professionals. They can be contacted at (800) 216-5505.*