When it comes to how grease interceptor's work, there are
many theories espoused that are supposed to be based on principles of fluid
dynamics, however, when tested under controlled conditions many of these
theories are debunked.

For example, I have heard the argument that Bernoulli's principle is behind hydromechanical grease interceptor performance. On its face the argument sounds plausible. I would, however, like to test the theory with historical research and current experience from thousands of tests conducted at our plant utilizing our own ASME A112.14.3 (PDI G-101) test apparatus.

For example, I have heard the argument that Bernoulli's principle is behind hydromechanical grease interceptor performance. On its face the argument sounds plausible. I would, however, like to test the theory with historical research and current experience from thousands of tests conducted at our plant utilizing our own ASME A112.14.3 (PDI G-101) test apparatus.

In fluid dynamics, Bernoulli's principle states that for an
inviscid flow, an increase in the speed of the fluid occurs simultaneously with
a decrease in pressure.

Bernoulli's principle is commonly used as a rudimentary explanation of how airplanes fly and the way 'lift' works on a wing.

It also explains how curve balls, sliders, and sinkers work in baseball.

Some argue that baffles inside a grease interceptor, which increase velocity, serve to create regions of higher pressure underneath regions of lower pressure aiding in separation efficiency as grease in the higher pressure region is forced to rise towards the region of lower pressure based on Bernoulli's principle.

What the research saysWhat the research says

In the early 1940s, research began at the Iowa Institute of Hydraulic Research to formalize a grease interceptor testing and rating system, initially for the construction branch of the US Army Engineers. The Plumbing and Drainage Manufacturer's Association took that research and in 1949 launched the first commercial standard for grease interceptors, PDI G-101.

In 1944 a symposium of four papers was presented at the Sixteen Annual Meeting of the New York State Sewage Works Association, one of which was titled,

*Symposium on Grease Removal, Design and Operation of Grease Interceptors*, by Francis Murray Dawson and Anton Adam Kalinske.

As a result of the research conducted by the IIHR, any kind
of interceptor, before it could be installed in an Army camp kitchen, had to
have a rating certificate from the Institute (Iowa Institute of Hydraulic
Research, Bulletin 30, 1946).

Dawson et al, established gravity differential separation as "the basic principle of grease interception." He defined this as, "the liquid greases and fats separate from the waste water in the interceptor, when the velocity of flow is reduced, owing to the difference in specific gravity."

"Since grease separation is due to gravity differential, a quantitative analysis of what occurs as waste water flows through an interceptor may lead to the establishment of some basic design data. For simplicity let us assume that pure grease and water enter near the bottom of a rectangular-shaped interceptor L feet long, B feet wide, and with a water depth of D feet. The interceptor will do a good job of separation if, as the flow goes through the interceptor, the mean velocity of the flow is such as to permit a grease globule to rise a vertical distance D in a length of L feet. If we neglect, for the moment, the presence of turbulence we see that the controlling item in the sizing of the interceptor for any particular rate of flow is the rate of rise of the grease globules," Dawson said.

Dawson then went on to explain the application of Stokes law, providing the formula and the basic calculations which led to the determination that 150 microns was the minimum size grease globule an interceptor could reasonably be sized to capture because, "the rate of rise of globules much less than this size is so small that gravitational separation is impracticable, and globules much larger than this size will be easily separated."

Bernoulli's principle was developed by Daniel Bernoulli and published in his book Hydrodynamica in 1738. It is a well known principle in fluid dynamics, yet Dawson et al. never made mention of it applying to grease interceptors. In fact, while Dawson et al. argued there was a benefit to some kind of baffle near the inlet with louvers to distribute the flow (throughout the cross-sectional area of the interceptor) and give it a gentle upward motion, he criticized the use of baffles in the interceptor body as, "undesirable since they induce turbulence."

Any positive effect that could be argued for baffles in the application of Bernoulli's principle is necessarily offset by the negative effect of the resultant turbulence created by the baffles.

ASPEs

Distributing the incoming flow throughout the cross-sectional area of a grease interceptor is the key to reducing forward velocity. While flow-rate measures volume, velocity measures speed and reducing the speed of the flow is critical to good interceptor design as was indicated by Dawson et al. in their research and confirmed more recently by ASPE.

Schier has literally run thousands of tests on interceptors, because it’s one thing to sit at a desk calculating the effects of all of the various principles of fluid dynamics on a grease interceptor, but where the leather meets the road is when you take your engineered design to the test bench.

In all of our thousands of tests, we have never found a benefit to adding internal baffles to somehow take advantage of Bernoulli's principle. Instead we experienced far worse consequences in the resulting turbulence.

Dawson et al, established gravity differential separation as "the basic principle of grease interception." He defined this as, "the liquid greases and fats separate from the waste water in the interceptor, when the velocity of flow is reduced, owing to the difference in specific gravity."

"Since grease separation is due to gravity differential, a quantitative analysis of what occurs as waste water flows through an interceptor may lead to the establishment of some basic design data. For simplicity let us assume that pure grease and water enter near the bottom of a rectangular-shaped interceptor L feet long, B feet wide, and with a water depth of D feet. The interceptor will do a good job of separation if, as the flow goes through the interceptor, the mean velocity of the flow is such as to permit a grease globule to rise a vertical distance D in a length of L feet. If we neglect, for the moment, the presence of turbulence we see that the controlling item in the sizing of the interceptor for any particular rate of flow is the rate of rise of the grease globules," Dawson said.

Dawson then went on to explain the application of Stokes law, providing the formula and the basic calculations which led to the determination that 150 microns was the minimum size grease globule an interceptor could reasonably be sized to capture because, "the rate of rise of globules much less than this size is so small that gravitational separation is impracticable, and globules much larger than this size will be easily separated."

Bernoulli's principle was developed by Daniel Bernoulli and published in his book Hydrodynamica in 1738. It is a well known principle in fluid dynamics, yet Dawson et al. never made mention of it applying to grease interceptors. In fact, while Dawson et al. argued there was a benefit to some kind of baffle near the inlet with louvers to distribute the flow (throughout the cross-sectional area of the interceptor) and give it a gentle upward motion, he criticized the use of baffles in the interceptor body as, "undesirable since they induce turbulence."

Any positive effect that could be argued for baffles in the application of Bernoulli's principle is necessarily offset by the negative effect of the resultant turbulence created by the baffles.

ASPEs

*Plumbing Engineering Design Handbook 4, Plumbing Components and Equipment, Chapter 8, Grease Interceptors*, states, "The ideal separation basin is one that has no turbulence, short-circuiting or eddies. The flow through the basin is laminar and distributed uniformly throughout the basin's cross-sectional area."Distributing the incoming flow throughout the cross-sectional area of a grease interceptor is the key to reducing forward velocity. While flow-rate measures volume, velocity measures speed and reducing the speed of the flow is critical to good interceptor design as was indicated by Dawson et al. in their research and confirmed more recently by ASPE.

Practical experiencePractical experience

Schier has literally run thousands of tests on interceptors, because it’s one thing to sit at a desk calculating the effects of all of the various principles of fluid dynamics on a grease interceptor, but where the leather meets the road is when you take your engineered design to the test bench.

In all of our thousands of tests, we have never found a benefit to adding internal baffles to somehow take advantage of Bernoulli's principle. Instead we experienced far worse consequences in the resulting turbulence.

By far, our greatest successes in design effectively control and distribute the entering flow throughout the interceptors cross-sectional area, while simultaneously creating a laminar flow pattern in a wide open vessel (no baffles).

The argument that Bernoulli’s principle is somehow necessary to hydromechanical grease interceptor performance is a theory that cannot be proven and has no support in any research that has ever been done going back as far as the original testing and rating protocols developed in the early 1940s.

Nothing has ever been written by PDI, ASPE or any other research body that supports the idea that Bernoulli’s principle is behind hydromechanical grease interceptor performance.

Bernoulli's principle does explain how curve balls, sliders and sinkers work though, in case you're interested!

## No comments:

## Post a Comment