CPD Test Prep
Flow in Drainage Systems
(Summary)
 
    
    
  
Get "100 days to CPD Certification"
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Drainage System Design for Self-Cleansing: - A well-designed drainage system maintains a flow velocity of about 2 feet per second. This speed is crucial to keep solids in suspension, avoiding sedimentation and blockages.
- Designers must consider the diameter and slope of pipes, which should be proportional to the anticipated flow rate.
 
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Minimum Slope Requirements: - Different pipe diameters require different minimum slopes to ensure adequate flow. For instance, a 4-inch pipe might need a slope of 1/8 inch per foot, whereas a 3-inch pipe might need 1/4 inch per foot.
- Insufficient slope can lead to slow water movement and potential blockages.
 
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Pipe Material and Size Selection: - The choice of material for pipes depends on factors like the type of waste (chemical composition, temperature), flow rate, and environmental considerations.
- Sizing of pipes is guided by estimating the peak discharge and ensuring the diameter can handle this flow without excessive velocity or pressure build-up.
 
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Venting Requirements: - Vents prevent the loss of trap seals due to pressure variations within the drainage system. These seals are crucial for blocking sewer gases from entering buildings.
- Proper venting involves strategic placement and sizing of vent pipes to balance the air pressure within the drainage system.
 
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Impact of Fittings on Flow: - Fittings like elbows and tees can create turbulence, reducing flow efficiency. Reducers can change flow velocity.
- The design should minimize sharp bends and use fittings that maintain a smooth flow path.
 
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Handling of Special Wastes: - Special wastes like chemicals or high-temperature effluents might require pipes made from specific materials (like CPVC for chemical resistance or temperature tolerance).
- The system might also need additional components like neutralization tanks or dilution pits.
 
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Maintenance and Accessibility: - Drainage systems should be designed for easy access for cleaning and maintenance. This involves strategic placement of cleanouts and access points.
- Regular maintenance is key to prevent blockages and ensure system longevity.
 
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Compliance with Codes and Standards: - Adherence to local building codes and plumbing standards is mandatory. These regulations specify requirements for materials, design, installation, and maintenance.
 
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Use of Cleanouts: - Cleanouts allow for easy access to the drainage system for removal of blockages and routine cleaning.
- They are typically installed at intervals specified by code, at changes in direction, and at the base of stacks.
 
Key Equations:
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Manning Formula for velocity of flow (V): V = 1.486 * R^(2/3) * S^(1/2) / n - V: velocity of flow (ft/s)
- R: hydraulic radius (ft)
- S: hydraulic slope (ft/ft)
- n: Manning's roughness coefficient
 
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Quantity rate of flow (Q): Q = A * V - Q: quantity rate of flow (cfs or gpm)
- A: cross-sectional area of flow (ft²)
 
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Hydraulic radius (R): R = A / P - P: wetted perimeter (ft)
 
Steps for Calculations:
- Identify the given values: pipe size, slope, roughness coefficient, and flow condition (full or half-full).
- Calculate hydraulic radius (R):
- For full flow: R = D/4 (D = pipe diameter)
- For half-full flow: R = πD²/8
 
- Find R^(2/3) from Tables 1-1 or 1-2. (shown below)
- Calculate velocity of flow (V) using Manning's formula.
- Find cross-sectional area of flow (A) from Tables 1-1 or 1-2.
- Calculate quantity rate of flow (Q) using Q = A * V.
Practical Examples:
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Calculate the velocity of flow in a 6-inch diameter pipe with a slope of 0.01 and a roughness coefficient of 0.013, flowing full. - R = D/4 = 0.125 ft
- R^(2/3) = 0.25 ft (from Table 1-1)
- V = 1.486 * 0.25 * 0.01^(1/2) / 0.013 ≈ 4.54 ft/s
 
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Determine the flow rate in gallons per minute for the same pipe in example 1. - A = 0.1964 ft² (from Table 1-1)
- Q = 0.1964 * 4.54 = 0.89 cfs
- Q = 0.89 * 450 ≈ 400 gpm
 
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Calculate the velocity and flow rate for the same pipe flowing half-full. - R = πD²/8 = 0.0982 ft
- R^(2/3) = 0.25 ft (still the same)
- V ≈ 4.54 ft/s (velocity remains the same for half-full flow)
- A = 0.0982 ft² (from Table 1-2)
- Q ≈ 0.44 cfs ≈ 200 gpm (flow rate is reduced for half-full flow)
 
Remember:
- Use consistent units throughout the calculations.
- Tables 1-1 and 1-2 provide values for R, R^(2/3), and A, saving calculation steps. These tables will be provided in the mep guy study/crib sheet as we get closer to the test.
- Consider the flow condition (full or half-full) when determining hydraulic radius and cross-sectional area.
Table 1-1: Values of R, R^(2/3), and A for Full Flow
| Pipe Size (in) | R = D/4 (ft) | R^(2/3) (ft) | A (ft²) | 
|---|---|---|---|
| 1½ | 0.0335 | 0.1040 | 0.01412 | 
| 2 | 0.0417 | 0.1200 | 0.02180 | 
| 2½ | 0.0521 | 0.1396 | 0.03408 | 
| 3 | 0.0625 | 0.1570 | 0.04910 | 
| 4 | 0.0833 | 0.1910 | 0.08730 | 
| 5 | 0.1040 | 0.2210 | 0.13640 | 
| 6 | 0.1250 | 0.2500 | 0.19640 | 
| 8 | 0.1670 | 0.3030 | 0.34920 | 
| 10 | 0.2080 | 0.3510 | 0.54540 | 
| 12 | 0.2500 | 0.3970 | 0.78540 | 
| 15 | 0.3125 | 0.4610 | 1.22700 | 
Table 1-2: Values of R, R^(2/3), and A for Half-Full Flow
| Pipe Size (in) | R = D/4 (ft) | R^(2/3) (ft) | A (ft²) | 
|---|---|---|---|
| 1½ | 0.0335 | 0.1040 | 0.00706 | 
| 2 | 0.0417 | 0.1200 | 0.01090 | 
| 2½ | 0.0521 | 0.1396 | 0.01704 | 
| 3 | 0.0625 | 0.1570 | 0.02455 | 
| 4 | 0.0833 | 0.1910 | 0.04365 | 
| 5 | 0.1040 | 0.2210 | 0.06820 | 
| 6 | 0.1250 | 0.2500 | 0.09820 | 
| 8 | 0.1670 | 0.3030 | 0.17460 | 
| 10 | 0.2080 | 0.3510 | 0.27270 | 
| 12 | 0.2500 | 0.3970 | 0.39270 | 
| 15 | 0.3125 | 0.4610 | 0.61350 | 
 
    
  
