Time for a Quiz
Last fall, I did a hydraulics quiz and readers seemed to enjoy it. So, hereās another one. See how you do and feel free to share. Answers are at the end, but donāt peek.
Last fall, I did a hydraulics quiz and readers seemed to enjoy it. So, hereās another one. See how you do and feel free to share. Answers are at the end, but donāt peek.
In my work in water and wastewater hydraulics, the two that show up most of the time are the Reynolds number and Froude number. A small Reynolds number indicates that viscous forces dominate, while a large value says that inertial forces dominate. A large Froude number indicates rapid flow, while a small number points to tranquil flow.
There are several reasons. First, the pressure is so high and constant in water systems in most developed countries that the effects of pressure on flow is negligible.
The most common question in pump selection these days is whether to use variable or constant-speed pumps.
One of the most fundamental decisions made in wastewater collection system design is choosing between a gravity or pressure sewer system. (Yes, there are other options such as septic tanks, vacuum systems, and onsite treatment, but once you decide on a central system of any significant size, gravity and pressure are usually the primary options.)
We all know that as two flows meet, according to the Law of Conservation of Mass, the resulting flow will be the sum of the two flows.
The fixture unit method (in some places called fixture value method) was developed by Roy B. Hunter from the US Bureau of Standards, based on research conducted by Hunter in the 1920s and 30s (Hunter, 1940). Every fixture in a building was assigned a fixture unit value. For example, a flush tank toilet uses 6, and a shower was 2.5, and a kitchen sink 1.5 (AWWA, 2014). For nearly the last 100 years, determining the peak flow in a pipe has been determined by the fixture unit method.
In a pipe network, all elements are connected such that changing anything at any location impacts the entire network. Adding a pipe in the far northwest part of the system affects flow in the far southeast part (minimally in many cases). The right way to model any pipe network is to include all elements that affect the behavior of the network.
They are nonlinear, partial differential equations which are about the worst kinds of equations to solve. About the only things that can make them worse are changes in state (e.g. steam condensing) or non-Newtonian fluids (e.g. mudflows). Numerous researchers have shown that it is impossible to arrive at a closed-form, analytical solution in the form v(r, Ļ, z) =⦠When people work with these equations these days, they almost always use numerical solutions. I heard a story once that Albert Einstein started his research in solving the Navier-Stokes equations but gave up because it was too difficult. He moved on to easy topics like quantum physics and relativity. I havenāt been able to verify this, but it makes for a good story.
The problem was that the people who developed the data underlying the GIS/CAD (Iāll call it GIS in this blog) used to build the model were not careful in how they laid out intersections. They would run the same pipe down several blocks without consideration of whether crossing pipes were interconnected. While we have tools in our model to clean up these issues (View > Network Navigator), it is best to avoid them from the start. Read Tom Walski’s blog and learn how to fix a model where the piping at intersections was poorly represented.