Gas Distribution

District Regulator Sizing

Size district regulators that reduce pressure from high-pressure (HP) to low-pressure (LP) distribution mains. Covers diversity factors, load estimation, Cv sizing, lockup and droop analysis, and overpressure protection for underground vault and above-grade installations.

Typical service

HP → LP distribution

60 psig to 0.25 psig (7 in WC) serving residential neighborhoods.

Diversity factor

0.30 - 0.80

Fraction of connected load at peak; varies by customer count and climate.

Droop tolerance

< 10% of set point

LP systems require tight pressure control for burner performance.

Use this guide when you need to:

  • Estimate peak demand for a district.
  • Size regulators for HP-to-LP service.
  • Evaluate lockup and droop performance.
  • Design overpressure protection for LP mains.

1. District Regulator Overview

District regulators are the workhorse of gas distribution networks. They reduce pressure from the high-pressure (HP) distribution system (typically 30-100 psig) to the low-pressure (LP) distribution system (typically 0.25-2.0 psig or 7-56 inches water column). A single district regulator station may serve anywhere from 50 to 5,000 residential customers through the LP main network.

Unlike town border stations that operate at high pressures with sophisticated pilot-operated regulators and metering, district regulators are often simple, self-operated (spring-loaded) devices installed in underground vaults or small above-grade enclosures. Their design priority is reliability and stable outlet pressure, because LP distribution systems have very narrow pressure tolerances. Burner appliances require stable supply pressure for safe, efficient operation.

District Regulator vs. Service Regulator

It is important to distinguish between district regulators and service regulators (customer meter-set regulators):

  • District regulators: Reduce HP main pressure to LP main pressure. Serve multiple customers through downstream LP mains. Located in vaults at street intersections or distribution node points. Sized for aggregate peak demand of the served district.
  • Service regulators: Located at each customer meter set. Reduce service line pressure (HP or LP) to appliance delivery pressure (typically 7 inches WC or 0.25 psig). Sized for individual customer peak demand. Include integral relief or vent provisions.

Installation Types

Underground vault

Most common

Concrete or fiberglass vault below grade. Provides noise reduction and weather protection. Must have ventilation per 49 CFR 192. Requires confined space entry for maintenance.

Above-grade cabinet

Easy maintenance

Metal cabinet on concrete pad. Allows tool-free access for inspection. Higher noise impact on neighbors. Must be fenced or locked per security requirements.

Curb box

Small stations

Small underground box with removable cover. Limited to small regulators (1-inch or less). Used for very small districts or individual large commercial customers.

Building interior

Special applications

Inside a building utility room. Requires gas detection and ventilation. Used when outdoor installation is impractical (dense urban areas).

LP system pressure control: Low-pressure distribution systems operate with very small pressure margins. The minimum delivery pressure at any customer meter must be at least 6 inches WC (0.22 psig), while the maximum must not exceed the LP main MAOP (typically 14 inches WC or 0.50 psig per 49 CFR 192). This narrow band of approximately 8 inches WC total pressure budget must accommodate the district regulator droop, main pressure drop, and service line losses. This is why droop performance is so critical for district regulators.

2. Diversity Factors & Load Estimation

The diversity factor is the ratio of actual peak demand to the total connected appliance load. Not all customers use gas at the same time or at maximum rate, so the actual system peak is significantly less than the sum of all connected loads. Accurate diversity factor selection is essential for proper regulator sizing: too low leads to oversizing (hunting, poor control), too high leads to undersizing (inadequate pressure at peak demand).

Diversity Factor by Customer Count

Number of CustomersHeating ClimateModerate ClimateCooling-Dominated
1-100.800.700.50
11-250.700.600.45
26-500.650.550.40
51-1000.600.500.35
101-2500.550.450.30
251-5000.500.400.30
501+0.450.350.25

Connected Load Estimation

Residential Load per Customer (typical): Space heating: 80,000-120,000 BTU/hr (furnace) Water heating: 30,000-50,000 BTU/hr (tank heater) Cooking range: 65,000 BTU/hr (all burners + oven) Clothes dryer: 22,000 BTU/hr Fireplace: 30,000-60,000 BTU/hr (log set) Typical total connected load per residence: Northern climate: 180,000-250,000 BTU/hr Southern climate: 100,000-150,000 BTU/hr Peak demand per customer: Northern: 180,000 × 0.60 = 108,000 BTU/hr ≈ 106 SCFH Southern: 100,000 × 0.45 = 45,000 BTU/hr ≈ 44 SCFH For 200 customers (northern): Connected = 200 × 200,000 = 40,000,000 BTU/hr Diversity = 0.55 Peak = 40,000,000 × 0.55 = 22,000,000 BTU/hr = 21,569 SCFH
Growth factor: When sizing district regulators, apply a 20-30% growth factor to the calculated peak demand to accommodate future customer additions and load growth within the district. This is particularly important because replacing an undersized regulator in an underground vault is expensive and disruptive. Most utilities design for 10-20 year projected growth.

3. Cv Sizing & Selection

District regulator Cv calculation follows the same ISA 75.01 methodology as other gas regulators, but with particular attention to the large pressure ratio typical of HP-to-LP service. The pressure drop ratio for a 60 psig to 0.25 psig application is approximately 0.98, which is well above the critical pressure ratio and results in choked flow conditions.

Sizing for Choked Flow

District Regulator Cv (HP to LP, choked flow typical): For x ≥ xT (choked): Cv = Q / (N8 × P1 × (2/3) × sqrt(xT / (SG × T × Z))) Example: Q = 20,000 SCFH, P1 = 60 psig (74.7 psia), P2 = 0.25 psig (14.9 psia) x = (74.7 - 14.9) / 74.7 = 0.800 xT = 0.70 for self-operated regulator x > xT → CHOKED Cv = 20,000 / (1360 × 74.7 × 0.667 × sqrt(0.70/(0.60×519.67×1.0))) Cv = 20,000 / (1360 × 74.7 × 0.667 × 0.0454) Cv = 20,000 / 3,077 = 6.5 Select 1-1/4" self-operated (Cv = 20) or 1" pilot-operated (Cv = 18) Safety factor: 6.5 × 1.3 = 8.5 — 1" regulator at Cv = 12 is borderline Recommend 1-1/4" self-operated for adequate margin

Regulator Selection Criteria

  • Type selection: Self-operated (spring-loaded) regulators are preferred for district service up to about 2-inch size due to lower cost and simpler maintenance. Above 2-inch, pilot-operated regulators provide better lockup and droop performance.
  • Oversizing limit: Do not exceed 4:1 ratio of selected Cv to required Cv. Oversized regulators oscillate (hunt) at low flow conditions, which causes premature diaphragm failure and unstable outlet pressure.
  • Outlet pressure class: For LP service (under 2 psig), select regulators specifically rated for low-pressure service with spring ranges appropriate for the set point. Standard industrial regulators may not have fine enough adjustment for LP set points.

4. Lockup & Droop Analysis

Lockup and droop are the two most important performance characteristics for district regulators serving LP systems. Together, they determine the operating pressure envelope of the downstream distribution system.

Lockup

Lockup Pressure: Lockup = outlet pressure at zero flow (all customers off) P_lockup = P_set × (1 + lockup%) Typical lockup values: - Pilot-operated: 1-2% above set point - Self-operated: 3-5% above set point - Weight-loaded: 0.5-1% above set point Example: Set point = 7.0 in WC (0.253 psig) Self-operated lockup at 5%: P_lockup = 7.0 × 1.05 = 7.35 in WC (0.266 psig) LP main MAOP = 14 in WC (0.506 psig) Lockup margin = 14 - 7.35 = 6.65 in WC (acceptable) If lockup were 10%: 7.0 × 1.10 = 7.7 in WC Still acceptable (6.3 in WC margin to MAOP)

Droop

Droop (Proportional Band): Droop = decrease in outlet pressure from zero flow to maximum flow P_at_max_flow = P_set × (1 - droop%) Typical droop values: - Pilot-operated: 2-5% - Self-operated: 5-10% Example: Set point = 7.0 in WC, Self-operated droop = 8% P_at_max_flow = 7.0 × (1 - 0.08) = 6.44 in WC Minimum customer delivery pressure = 6.0 in WC Available main pressure drop budget = 6.44 - 6.0 = 0.44 in WC This is very tight! Main sizing must be checked carefully. If droop is too high, consider: 1. Upgrade to pilot-operated regulator (3-5% droop) 2. Increase regulator size (reduces droop by reducing load fraction) 3. Raise set point (if MAOP permits)

Pressure Budget Analysis

ComponentPressure (in WC)Cumulative
Regulator set point7.07.0
Less: Regulator droop (8%)-0.566.44
Less: Main pressure drop-0.306.14
Less: Service line drop-0.106.04
Customer meter delivery6.04
Minimum required6.00
Margin0.04 in WC
Low-pressure system design: The pressure budget analysis above illustrates why LP system design is so challenging. With only 0.04 in WC margin, any increase in demand, any degradation in regulator droop performance, or any increase in main friction losses could result in inadequate delivery pressure. This is why modern distribution design increasingly uses medium-pressure (2-60 psig) mains with individual service regulators at each customer, eliminating the LP main and district regulator entirely.

5. Design Examples

Example 1: Residential District

Given: Inlet: 60 psig HP distribution main Outlet: 7 in WC (0.253 psig) LP distribution Customers: 150 residential (northern climate) Average connected load: 200,000 BTU/hr per customer Step 1: Total connected load Total = 150 × 200,000 = 30,000,000 BTU/hr Step 2: Diversity factor (150 customers, heating climate) DF = 0.58 (interpolated from table) Step 3: Peak demand Peak = 30,000,000 × 0.58 = 17,400,000 BTU/hr Q = 17,400,000 / 1020 = 17,059 SCFH Step 4: Apply 25% growth factor Q_design = 17,059 × 1.25 = 21,324 SCFH Step 5: Cv calculation (choked flow, x = 0.98) P1 = 74.7 psia, Y = 2/3, xT = 0.70 Cv = 21,324 / (1360 × 74.7 × 0.667 × 0.0454) Cv = 21,324 / 3,077 = 6.93 Step 6: Select regulator Required Cv × 1.3 = 9.0 Select 1-1/4" self-operated (Cv = 20) Load fraction = 6.93 / 20 = 35% (good operating point) Step 7: Droop check Droop = 8% × 0.35 = 2.8% Outlet at peak = 7.0 × (1 - 0.028) = 6.80 in WC (acceptable)

Example 2: Commercial District

Given: Inlet: 60 psig HP distribution Outlet: 2 psig (medium-pressure LP) Loads: Shopping center + 50 small commercial Total connected: 15,000,000 BTU/hr Diversity factor: 0.75 (commercial loads are more coincident) Step 1: Peak demand Peak = 15,000,000 × 0.75 = 11,250,000 BTU/hr Q = 11,250,000 / 1020 = 11,029 SCFH Step 2: With 20% growth Q_design = 11,029 × 1.20 = 13,235 SCFH Step 3: Cv calculation P1 = 74.7 psia, P2 = 16.7 psia x = (74.7 - 16.7) / 74.7 = 0.776 xT = 0.70, choked Cv = 13,235 / (1360 × 74.7 × 0.667 × 0.0454) Cv = 13,235 / 3,077 = 4.30 Step 4: Select regulator Required Cv × 1.3 = 5.6 Select 1" self-operated (Cv = 12) Or 1" pilot-operated (Cv = 18) for better droop control With pilot-operated: Load fraction = 4.30 / 18 = 24% Droop = 3% × 0.24 = 0.7% (excellent)
Maintenance schedule: District regulators should be inspected annually per utility maintenance procedures and 49 CFR 192 Subpart M requirements. Inspection includes checking set pressure, lockup, vent operation, and physical condition of diaphragm and seat. In corrosive soil conditions, underground vaults should be inspected for water accumulation, structural integrity, and cathodic protection continuity. Many utilities are transitioning to smart monitoring with pressure transducers and cellular telemetry to detect regulator degradation between scheduled inspections.