Lecture 27 Protective Structures I. Introduction • • • • • • • • • Protective structures include energy dissipation and erosion control structures, structures to divert excess water to prevent over-topping of canals, and others In this context, protective structures are for the canals and other infrastructure, and not for the protection of animals and people For example, there should be a wasteway weir or other structure in a canal, upstream of an in-line pumping plant -- the pump(s) could shut off unexpectedly, possibly causing over-topping of the canal upstream An inverted siphon could become clogged, or a landslide could block the flow in the canal, also causing the canal to overflow on the upstream side Of course, canal over-topping can also occur due to design deficiencies, construction problems, and operational error This means that spillway structures are generally designed to carry the full flow of the canal Side spillways sometimes have radial or vertical slide gates to facilitate dewatering of the channel in emergencies, for sediment removal, and other reasons Some in-line gate structures in canals have fixed-crest side weirs to allow for water to pass downstream in the event of an operational error The flow from spillway structures is generally directed into a natural channel which can safely carry the maximum spill rate away from the canal II. Wasteway Weirs • A wasteway weir is a sharp- or blunt-crested weir located along one bank of the canal BIE 5300/6300 Lectures 293 Gary P. Merkley • • • • The weir may be designed to accept “stop logs” to allow for changes in the operating level of the canal The crest of the weir is equal to the maximum operating level of the canal, taking into consideration that a higher water surface elevation will result in the canal for the full design discharge The wider the weir is, the less difference in water surface elevation between impending spill and full-flow spill through the structure Wasteway weirs are located at places where the canal would be most likely to overtop in the event of an operational error or the clogging of a flow control structure (e.g. cross regulator): 1. Upstream of an inverted siphon entrance 2. Upstream of a gate or weir structure 3. Upstream of a pumping station III. Siphon Spillways • • • • • • • • • • As opposed to inverted siphons, siphon spillways operate under negative pressures (below atmospheric) Once a siphon spillway is primed, water will continue to flow through the structure as long as the downstream water elevation is lower than that in the canal, or until suction is broken by other means Siphon spillways are generally more expensive to build than side spillway weirs, but for the same discharge they require a much smaller width Siphon spillways can discharge more water than a weir for a small increase in upstream water surface elevation As the water level in the canal increases, the siphon spillway acts like a weir As the water level continues to increase, the siphon will become “primed” and operate under full pipe flow conditions The USBR design calls for a crest elevation of about 0.2 ft above the normal water surface (or full supply level) in the canal Note that the inlet to the siphon can serve as a sediment trap, requiring periodic manual cleaning Also note that it is impractical to change the FSL of the canal once the siphon spillway is installed – with side spill weirs, you can always raise the level, if needed See Section 4-14 of the USBR Small Canal Structures book Gary P. Merkley 294 BIE 5300/6300 Lectures BIE 5300/6300 Lectures 295 Gary P. Merkley Air Vent for Breaking Suction • • • • • flo w • An air vent is located just downstream of the top of the siphon spillway to break suction when the upstream water level in the canal drops below a certain level This location is about 15° (from vertical) downstream of the top of the siphon pipe, as shown in Figure 4-17 of the USBR Small Canal Structures book The upstream end of the vent is open at the normal water surface level (or FSL) of the canal A potential operating problem with this type of structure is that when the suction is broken, the discharge will suddenly cease, and this can cause surges in the canal A pan can be attached to the upstream end of the vent to help prevent the vent from acting as a siphon itself, possibly causing the water level in the canal to drop below full supply level The pan helps reduce the amount of water level fluctuation in the canal Gary P. Merkley 296 FSL BIE 5300/6300 Lectures 2.00 ft 6.16 ft FSL 00 4. ft 1.25:1 ft 297 Barrel 3.85 ft 30o 2 0. 2.00 ft 2.00 ft 15o 60o 3.0 ft f tof u c ll wa 5.00 ft road 12.00 ft 6.36 ft 10.00 ft 1:1 sill 1.5:1 8.30 ft BIE 5300/6300 Lectures t 0f 4.0 Gary P. Merkley all w f tof cu high water Deflector at the Downstream Side of the Siphon • • • • A small angled deflector can be installed in the downstream end of the siphon to help direct water up to the top of the barrel under non-full-flow conditions This helps to mix air and water and cause the siphon to prime to full flow quicker The roof of the siphon structure at the outlet should be above the expected downstream water surface elevation This helps to evacuate air from the siphon IV. Design of a Siphon Spillway This design example is adapted from an example given by the USBR (1978) Given: Suppose there is a canal with a design discharge of 120 cfs in which an in-line pump station is used to lift the water up to a downstream reach. The canal is trapezoidal in cross-section, with a base width of 8.0 ft, side slope of 1½:1 (H:V). The canal is at an elevation of about 6000 ft above msl. The available head across the siphon spillway, H, is 6.0 ft. Solution: (a) Preliminary Calculations According to USBR recommendations, use a ratio RCL/D of 2.0. Assume an initial value of D = 2.0 ft. Then, the radius of the centerline of the siphon is RCL = 4.0 ft, and the radius of the siphon invert is RC = 4.0 ft - ½(2.0) = 3.0 ft. The radius of the top of the siphon is RS = 4.0 ft + ½(2.0) = 5.0 ft. (b) Full Pipe Discharge Estimate the full pipe discharge by assuming: (1) orifice flow; and (2) a discharge coefficient of 0.65. This will give a flow rate per “unit width” of the barrel: q = CdD 2gH = (0.65)(2.0) 2(32.2)(6.0) = 25.6 cfs / ft (1) Note that this is an estimate, using an assumed Cd value, and D instead of area. (c) Maximum Possible Discharge Now, estimate the discharge per unit width according to the “vortex” equation, which takes into account the atmospheric pressure available to “push” the water up over the invert of the siphon crest. The socalled vortex equation looks like this: ⎛R ⎞ qmax = RC 2g(0.7h) ln ⎜ S ⎟ ⎝ RC ⎠ (2) where h is the available atmospheric pressure head, based on the density of water; and qmax is the flow rate per foot of barrel width (cfs/ft). Gary P. Merkley 298 BIE 5300/6300 Lectures The change in average atmospheric pressure with elevation can be approximated by the following linear relationship: Patm ≈ (33.9 − 0.00105Elev) / 2.31 (3) where Patm is in psi and Elev is the elevation above mean sea level, in ft. For 6000-ft of elevation, the atmospheric pressure is about 11.9 psi, or h = 27.6 ft of head (water). Then, qmax is equal to: ⎛ 5.0 ⎞ qmax = (3.0) 2g(0.7)(27.6) ln ⎜ ⎟ = 54.1 cfs / ft 3.0 ⎝ ⎠ (4) This means that the previously-calculated unit discharge of 25.6 cfs/ft (from the orifice equation) is acceptable. If q were greater than qmax, it would have been necessary to decrease H or change RCL. (d) Barrel Width The width of the barrel is determined as: b= Q 120 cfs = = 4.7 ft q 25.6 cfs / ft (5) This value could be rounded up to provide a margin of safety, but we will leave it at 4.7 ft (at least for now). (e) Vent Diameter The diameter of the siphon breaker pipe, Dp, should be such that the cross-sectional area is at least 1/24th of the cross-sectional area of the barrel (according to USBR guidelines). This gives an area of (2.0)(4.7)/24 = 0.39 ft2. The corresponding ID is 0.70 ft, or 8.5 inches. Thus, use whatever pipe size would be closest to this diameter (perhaps 9-inch nominal size), noting that steel pipe is usually used (for strength). (f) Outlet Sill Height The height of the deflector sill at the outlet of the siphon is given as 1.5D, or 3.0 ft in our case. (g) Outlet Ceiling Height The ceiling of the outlet is defined as h2. Referring to Figure 4-17, this is given by: h2 = 1.5D + Ecritical + 1.0 ft (6) where Ecritical is the specific energy for critical flow conditions, in feet. This is how the dimensions are defined in the USBR design procedures. BIE 5300/6300 Lectures 299 Gary P. Merkley The width of the downstream pool will be the same as the barrel width, or 4.7 ft, and the section will be rectangular. Critical depth for the design discharge is: yc = 3 Q2 gb 2 =3 (120)2 2 (32.2)(4.7) = 2.7 ft (7) The velocity is Q/A = 120/(2.7*4.7) = 9.5 fps, so the velocity head is: V2 (9.5)2 = = 1.4 ft 2g 2(32.2) (8) Then, Ecritical is 2.7 + 1.4 = 4.1 ft. And, h2 = 1.5(2.0) + 4.1 + 1.0 = 8.1 ft. (h) Other Design Details The inlet structure from the canal can be designed with a height along the side slope of 2D (minimum). The inlet structure should provide a minimum submergence of 1.5hv + 0.5 ft, where hv is the velocity at the inlet, and the inlet area is at least 2Db. Gary P. Merkley 300 BIE 5300/6300 Lectures