Exam Cheat Sheet · Quick Reference
California C-36 Plumbing Contractor Exam
California · PSI Services Contractor
California State Portion 115 questions
Key Distinctions
Pipe serving flushometer valves is assigned flushometer fixture units based on the number and category of valves served (Table 610.10), while branches and mains serving flushometer tanks are sized consistent with flush tank water closet procedures.
2025 California Plumbing Code, Section 610.10A sectional water test requires at least a 10 foot head held not less than 15 minutes (including the upper 10 feet of the preceding section), while the air test requires a uniform gauge pressure of 5 psi (or a 10 inch mercury column) held 15 minutes without adding air — and plastic pipe shall not be tested with air.
2025 California Plumbing Code, Section 712.2An air test of the hot and cold water supply system must be a minimum of 50 psi, whereas a water test must be at least equal to the system working pressure.
2025 California Plumbing Code, Section 609.4With AHJ approval, building drain piping 4 inches and larger may slope not less than 1/8 inch per foot, while building sewers 4 through 6 inches may slope not less than 1/8 inch per foot and 8 inches and larger not less than 1/16 inch per foot.
2025 California Plumbing Code, Section 708.1Continuous drainage flow from a pump, sump ejector or air conditioning equipment is converted at 2 drainage fixture units per gpm, while a continuous-flow water supply connection has its required gpm determined and added separately to the system gpm demand.
2025 California Plumbing Code, Section 702.3Velocity shall not exceed 8 ft/s in cold water and 5 ft/s in hot water in copper and copper alloy tube and fitting systems.
2025 California Plumbing Code, Section 610.12.1CPC 608.2 normally requires an expansion tank downstream of the regulator, but a system designed by a licensed plumbing contractor or registered design professional may use approved pressure relief valves with a maximum pressure relief setting of 100 psi or less (the general maximum relief setting under 608.4 is 150 psi).
2025 California Plumbing Code, Section 608.2For a Category I appliance (excluding engineered systems), the maximum horizontal connector length is 100 percent of the chimney/vent height for Type B double-wall and 75 percent of the vent height for single-wall.
2025 California Mechanical Code, Section 802.10.8.2Brazing filler metals melt between 1,100°F and 1,500°F (and for gas tubing joints the brazing material must melt above 1000°F with not more than 0.05 percent phosphorus), while soldering requires only about 350°F to 550°F.
Plumbing Basics for Contractors (4th ed.), Chapter 6 (Copper Tube and Fittings), Section 2.4.1For occupancies other than single dwelling units the pump must pass a 2 inch solid ball and the discharge piping shall be not less than 3 inches with a backwater valve and gate valve; the 2 inch discharge minimum applies only to single dwelling units.
2025 California Plumbing Code, Section 710.3The velocity method may be used only for house-sized buildings three stories or fewer, with no designed continuously running outlets and at least 40 psi available pressure; below 40 psi another method such as the friction/pressure-loss method must be used.
Plumbing Technology: Design and Installation (4th ed.), Chapter 19, Velocity Method AssumptionsA commercial grid strainer connects with a 1 1/2-inch threaded tailpiece, whereas a residential pop-up uses a 1 1/4-inch threaded tailpiece.
Plumbing Technology: Design and Installation (4th ed.), Chapter 7 — Faucets and Drain AssembliesStopping leaks and clearing stoppages (including removing and reinstalling water closets) are exempt, but where a trap, drainpipe, soil, waste or vent pipe is defective and must be removed and replaced with new material, it is new work requiring a permit and inspection.
2025 California Plumbing Code, Section 104.2Option (1) of §1541.1(b)(1)(A) allows sloping no steeper than 1 1/2 horizontal to 1 vertical (34 degrees, the Type C slope) with no soil classification, appendices or engineer; steeper slopes require one of the other design options.
Cal/OSHA Title 8 Construction Safety Orders, §1541.1(b)(1)(A)Key Terms
Formulas to Know
Static pressure (psi) = vertical height of water above the point (ft) × 0.433 psi/ft; e.g., 60 ft × 0.433 = 26 psi; in the tank figure 46 ft × 0.433 ≈ 20 psiHeight (ft) = pressure (psi) ÷ 0.433 psi/ft; e.g., 20 ÷ 0.433 = 46.2 ft; 30 ÷ 0.433 = 69.3 ftStatic loss = height (ft) × 0.43; Pressure available for friction = supply pressure − (required residual + static loss); Friction loss per 100 ft = available ÷ developed length × 100. Worked example: 30 × 0.43 = 12.9; 60 − (15 + 12.9) = 32.1; 32.1 ÷ 150 × 100 = 21.4 psi/100 ftDFU = gpm of continuous flow × 2; example: 12 gpm × 2 = 24 fixture unitsEquivalent roof area = gpm × 24 sq ft per gpm (based on 4 in/h rainfall); example: 10 gpm × 24 = 240 sq ft added to projected roof areaAllowable horizontal fixture units at 1/8 in/ft slope = listed value (based on 1/4 in/ft) × 0.8Total fall = grade (in/ft) × run (ft); examples: 1/8 in/ft × 32 ft = 4 in; 1/4 in/ft × 48 ft = 12 in = 1.00 ftDownstream invert = upstream invert − total fall; example: 100.00' − (48 ft × 1/4 in/ft = 1.00 ft) = 99.00'Percent slope = (rise per foot in inches ÷ 12) × 100; example: 1/4 in/ft → (0.25 ÷ 12) × 100 = 2.08%Travel = set × 1.414 and run = set × 1.000; examples: 16 × 1.414 = 22.62 ≈ 22-5/8"; 20 × 1.414 = 28.28 ≈ 28-1/4"; run = 20 × 1.000 = 20". For 22½° fittings, travel = set × 2.613 (20 × 2.613 ≈ 52-1/4")Parallel angle = one-half the fitting angle (22-1/2° for 45° offsets); length difference = spread × 0.414; example: 0.414 × 10 in. = 4.14 in. ≈ 4-1/8 in.Cut length = center-to-center − (takeoff × 2 elbows) + (thread engagement × 2 ends); example: 36 − (2 × 2) + (2 × 1/2) = 33.00 in (total elbow deduction 2 in × 2 = 4 in)V = π × r² × h (r = half the diameter); gallons = cubic feet × 7.48. Examples: π × 1.5² × 5 = 35.34 cu ft → 264 gal; π × 2² × 6 = 75.4 cu ft → 565 gal; half-full (h = 3 ft) = 37.7 cu ft → 282 galBTU = gallons × 8.33 lb/gal × temperature rise (°F); example: 30 gal × 8.33 × (140 − 45) = 23,740 BTUUsable output = input BTU/hr × efficiency; time (hr) = BTU required ÷ usable output, × 60 for minutes; example: 50 × 8.33 × 80 = 33,320 BTU; 38,000 × 0.76 = 28,880 BTU/hr; 33,320 ÷ 28,880 = 1.1538 hr = 69 minutes. Another example: 40,000 × 0.75 = 30,000 BTU/hr ÷ (8.33 × 70 = 583.1) = 51.4 GPHOutput BTU/hr = watts × 3.413 BTU/hr per watt; time = BTU needed ÷ output. Example: 25 gal × 8.33 × 70 = 14,577.5 BTU; 5,500 W × 3.413 = 18,771.5 BTU/hr; 14,577.5 ÷ 18,771.5 = 0.7765 hr × 60 = 46.6 minutes (nearest listed answer 46.3 minutes)1 kW = 1,000 watts = 3,412 BTU; example: 5 kW × 3,412 = 17,060 BTUUseful output = input × efficiency; BTU per gallon = 8.33 × temperature rise; GPH = output ÷ BTU per gallon; GPM = GPH ÷ 60. Example: 199,000 × 0.84 = 167,160; 8.33 × 70 = 583.1; 167,160 ÷ 583.1 = 286.7 GPH ÷ 60 = 4.78 GPMTotal available = tank storage + recovery during the hour; remaining = total available − amount drawn; example: 40 + 43 = 83 gal; 83 − 55 = 28 gallonsLavatories credited = usable rim space (in) ÷ 20 in; examples: 100 ÷ 20 = 5; 80 ÷ 20 = 4Deduct one water closet per urinal added in excess of the minimum, but not below two-thirds of the minimum required; examples: 2/3 of 9 = 6 water closets; 2/3 of 6 = 4 water closetsVent diameter = not less than 1-1/4 in nor less than one-half the diameter of the drain served; example: half of a 3 in drain = 1-1/2 in, which governsOD = nominal size + 1/8 inch; example: 1/2 in NPS copper has a 5/8 in OD (3/4 in NPS = 7/8 in OD)Type B double-wall: 100% of vent height (24 ft vent → 24 ft); single-wall: 75% of vent height (24 ft vent → 18 ft); excludes engineered systems