Compression Equipment

Compressor Driver Fuel Gas Consumption

Calculate fuel gas requirements for compressor drivers including gas engines, gas turbines, and electric motors. Covers heat rate, derating, and RICE MACT emissions compliance.

Gas Engine

7,000-9,500 BTU/BHP-hr

Lean-burn 4-stroke; most common in gathering

Gas Turbine

8,500-11,000 BTU/BHP-hr

Simple cycle; preferred for large pipeline

Altitude Derating

3% per 1,000 ft

Above 1,000 ft elevation for gas engines

1. Overview

Compressor drivers consume significant quantities of fuel gas, representing the largest operating cost for pipeline and gas processing facilities. Accurate fuel consumption estimates are essential for gas balance, operating cost projections, emissions permitting, and driver selection.

Fuel Gas Volume

1-5% of Throughput

Typical fuel usage as percent of pipeline flow

Heat Rate

BTU/BHP-hr

Energy input per unit of shaft power output

Thermal Efficiency

2,545 / Heat Rate

Fraction of fuel energy converted to work

Fuel HHV

950-1,150 BTU/SCF

Heating value varies with gas composition

Gas balance impact: A 10,000 HP compressor station burning fuel at 8,500 BTU/BHP-hr consumes approximately 2.0 MMSCFD of gas. On a 100 MMSCFD pipeline, this is 2% of throughput -- a significant revenue impact that must be accounted for in pipeline design and tariff calculations.

2. Driver Types

Three primary driver types are used for gas compression in midstream operations. Selection depends on power range, fuel availability, emissions requirements, and site-specific factors.

Driver Comparison

ParameterGas EngineGas TurbineElectric Motor
Power range100-15,000 HP1,000-100,000+ HP100-50,000 HP
Heat rate7,000-9,500 BTU/BHP-hr8,500-11,000 BTU/BHP-hrN/A (electricity)
Thermal efficiency27-36%23-30%92-97% (motor only)
Speed range700-1,800 RPM3,600-16,000 RPM1,200-3,600 RPM
Startup time2-5 minutes10-30 minutesSeconds
Maintenance interval2,000-8,000 hrs20,000-40,000 hrs40,000-80,000 hrs
Typical applicationGathering, boostPipeline, LNGProcessing, urban

Gas Engine Types

Engine TypeHeat RateNOx EmissionsNotes
2-stroke lean burn (2SLB)8,000-9,5002-6 g/BHP-hrLegacy units; high emissions; RICE MACT affected
4-stroke lean burn (4SLB)7,000-8,5001-2 g/BHP-hrMost common new installation; low emissions
4-stroke rich burn (4SRB)7,500-9,0008-15 g/BHP-hr (uncontrolled)Requires 3-way catalyst (NSCR) for RICE MACT
4SRB + NSCR7,500-9,000< 1 g/BHP-hrLowest NOx with catalyst; common for gathering

Gas Turbine Types

ConfigurationHeat RateEfficiencyApplication
Simple cycle8,500-11,00023-30%Pipeline compression
Recuperated7,000-8,50030-36%Base load, high fuel cost
Combined cycle5,500-7,00036-46%Large power plants only
Aeroderivative8,000-9,50027-32%Mid-range pipeline
Industrial frame9,000-11,00023-28%Large pipeline, LNG
Driver selection rule of thumb: Gas engines dominate below 5,000 HP (gathering and boost). Gas turbines are preferred above 10,000 HP (pipeline mainline). The 5,000-10,000 HP range is competitive between the two. Electric motors are chosen when grid power is available and emissions are restricted.

3. Heat Rate & Fuel Consumption

Heat rate is the amount of fuel energy (in BTU) required to produce one brake horsepower-hour of shaft output. Lower heat rate means higher efficiency and less fuel consumption.

Fuel Gas Consumption: Q_fuel = (BHP x HR) / HHV Where: Q_fuel = Fuel gas consumption (SCF/hr) BHP = Brake horsepower (HP) HR = Heat rate (BTU/BHP-hr) HHV = Higher heating value of fuel gas (BTU/SCF) Convert to daily volume: Q_fuel_daily = Q_fuel x 24 / 1,000,000 (MMSCFD) Thermal Efficiency: eta_thermal = 2,545 / HR Where 2,545 BTU/HP-hr is the mechanical equivalent of one horsepower. Example: HR = 8,000 BTU/BHP-hr eta = 2,545 / 8,000 = 31.8% (68.2% of fuel energy becomes waste heat)

Fuel Gas Heating Values

Gas TypeHHV (BTU/SCF)LHV (BTU/SCF)Specific Gravity
Methane1,0129110.554
Pipeline gas (lean)1,000-1,050900-9500.58-0.62
Pipeline gas (rich)1,050-1,200950-1,0800.62-0.75
Ethane1,7701,6191.038
Propane2,5162,3141.522
Field gas (with CO2/N2)800-950720-8600.65-0.80

Part-Load Heat Rate

Part-Load Performance: Gas engines and turbines become less efficient at part load. Typical heat rate multipliers: Gas Engine: 100% load: 1.00 x rated HR 75% load: 1.05-1.10 x rated HR 50% load: 1.15-1.25 x rated HR 25% load: 1.40-1.60 x rated HR Gas Turbine: 100% load: 1.00 x rated HR 75% load: 1.10-1.15 x rated HR 50% load: 1.25-1.35 x rated HR Below 50%: typically not operated (poor efficiency) Part-load fuel consumption: Q_fuel_part = BHP_actual x HR_rated x HR_multiplier / HHV For gas turbines, part-load is usually controlled by: Variable speed (preferred): reduces fuel flow and air flow Variable IGV: adjusts inlet air to maintain efficiency Bleed air: least efficient method
HHV vs. LHV: Engine manufacturers typically quote heat rate on LHV basis (excludes latent heat of water vapor in exhaust). Gas utilities measure gas on HHV basis. To convert: HR_HHV = HR_LHV x (HHV/LHV). For natural gas, HHV/LHV is approximately 1.11. Always confirm which basis is used.

4. Derating Factors

Site conditions reduce the rated power output of gas engines and turbines below their ISO or NEMA nameplate ratings. The derated power determines the maximum shaft horsepower available at site conditions.

Gas Engine Derating

Gas Engine Site Power: BHP_site = BHP_rated x f_altitude x f_temperature x f_fuel x f_accessories Altitude Derating (f_altitude): f_altitude = 1.0 - 0.03 x (Elevation - 1,000) / 1,000 (for elevation > 1,000 ft) Example: 5,000 ft -> f = 1.0 - 0.03 x 4 = 0.88 Temperature Derating (f_temperature): f_temperature = 1.0 - 0.02 x (T_ambient - 77) / 10 (for T_ambient > 77 deg F; base = 77 deg F / 25 deg C) Example: 100 deg F -> f = 1.0 - 0.02 x 2.3 = 0.954 Fuel Quality Derating (f_fuel): f_fuel = HHV_actual / HHV_reference Reference is typically 950-1,000 BTU/SCF Low-BTU gas (< 900 BTU/SCF) may require engine modifications Accessory Loads (f_accessories): Cooling fans, lube oil pump, fuel gas booster: 3-5% f_accessories = 0.95-0.97 Combined Example (5,000 ft, 100 deg F, 980 BTU gas): f_total = 0.88 x 0.954 x (980/1000) x 0.96 = 0.79 BHP_site = 1,000 x 0.79 = 790 HP available

Gas Turbine Derating

Gas Turbine Site Power: BHP_site = BHP_ISO x (rho_site / rho_ISO) x f_inlet_loss x f_exhaust_loss Ambient Temperature Effect (most significant): Turbines are highly sensitive to inlet air temperature. Power decreases approximately 0.5-0.7% per deg F above ISO (59 deg F). At 100 deg F: Power reduction = 0.6% x 41 = 24.6% (typical) Altitude/Pressure Effect: Power proportional to air density. At 5,000 ft: P_atm = 12.23 psia vs 14.696 psia (sea level) Density ratio = 12.23/14.696 = 0.832 Power reduction: ~17% Inlet/Exhaust Pressure Losses: Inlet filter: 2-4 inches H2O Exhaust duct: 4-8 inches H2O Each 1" H2O inlet loss: ~0.5% power loss Each 1" H2O exhaust loss: ~0.3% power loss Humidity Effect: Minor for gas turbines: ~1% power loss per 0.01 specific humidity increase More significant in tropical/coastal environments
Derating FactorGas Engine ImpactGas Turbine Impact
Altitude (5,000 ft)-12%-17%
Ambient temp (100 deg F)-5%-25%
Low-BTU fuel (900 BTU)-5 to -10%-2 to -5%
Inlet loss (4" H2O)Negligible-2%
Combined worst case-20 to -25%-35 to -45%
Summer design case: Always size drivers for the hottest expected ambient temperature (summer design day). In Texas and the Gulf Coast, this is typically 105-110 deg F. A turbine rated at 10,000 HP ISO may only deliver 6,500-7,000 HP at summer conditions. Failing to account for derating is the most common driver sizing error.

5. RICE MACT Compliance

The Reciprocating Internal Combustion Engine (RICE) Maximum Achievable Control Technology (MACT) rule (40 CFR Part 63, Subparts ZZZZ and JJJJJJ) regulates hazardous air pollutant (HAP) emissions from stationary engines. Compliance requirements depend on engine type, size, and installation date.

RICE MACT Applicability

Engine CategorySubpartKey Requirements
Existing 2SLB > 500 HPZZZZEmissions limits or management practices; catalyst may be required
Existing 4SLB > 500 HPZZZZMaintenance and operational requirements
Existing 4SRB > 500 HPZZZZNSCR (3-way catalyst) required; formaldehyde limits
New/Reconstructed > 500 HPZZZZStrictest limits; emission standards at stack
Existing < 500 HP (area source)JJJJJJMaintenance practices; change oil, inspect plugs

Emission Limits (Major Source, Existing)

Pollutant2SLB4SLB4SRB + NSCRUnits
Formaldehyde (HCHO)2.02.72.7ppmvd @ 15% O2
CO (alternative)234776ppmvd @ 15% O2
NOx (for reference)Not HAP but often co-regulatedState/NSR permits

Compliance Strategies

NSCR (Non-Selective Catalytic Reduction) for 4SRB: Three-way catalyst converts CO, VOC, and NOx simultaneously Requires rich burn (lambda = 0.98-1.02) Formaldehyde reduction: 90-95% CO reduction: 90-95% NOx reduction: 90-98% Catalyst replacement: every 3-5 years ($15K-$40K) Oxidation Catalyst for 4SLB/2SLB: Reduces CO and formaldehyde only Does NOT control NOx Formaldehyde reduction: 85-95% CO reduction: 70-90% Lower backpressure penalty than NSCR Fuel Gas Impact on Catalyst Performance: H2S > 50 ppm: catalyst poisoning risk; treat fuel gas Siloxanes: permanent catalyst deactivation Lead compounds: rapid catalyst failure Ensure fuel gas treatment upstream of catalyst-equipped engines Alternative Compliance: Replace 2SLB with new 4SLB engine (lower emissions; meets limits without catalyst) Electrify: replace engine with electric motor (eliminates all combustion emissions) Install gas turbine: different emissions profile; may be exempt from RICE MACT
Testing requirements: RICE MACT requires initial performance testing within 180 days of startup (new engines) and periodic testing every 3 years or 8,760 operating hours, whichever comes first. Many operators use portable analyzers for interim monitoring between formal stack tests.

6. Economic Comparison

Driver selection involves balancing capital cost, fuel cost, maintenance cost, and emissions compliance cost over the project life. Fuel cost is typically the dominant operating expense.

Fuel Cost Comparison

Annual Fuel Cost: Annual_Fuel_Cost = Q_fuel_daily x 365 x Availability x Fuel_Price Where: Q_fuel_daily = Daily fuel consumption (MMSCFD) Availability = Operating factor (typically 0.90-0.97) Fuel_Price = Gas price ($/MMBTU or $/MCF) Example: 5,000 HP station, gas at $3.00/MMBTU: Gas Engine (HR = 8,000 BTU/BHP-hr): Q_fuel = (5,000 x 8,000) / 1,020,000 = 39.2 MCF/hr = 0.94 MMSCFD Annual = 0.94 x 365 x 0.95 x $3.00 x 1,000 = $978,000/yr Gas Turbine (HR = 10,000 BTU/BHP-hr): Q_fuel = (5,000 x 10,000) / 1,020,000 = 49.0 MCF/hr = 1.18 MMSCFD Annual = 1.18 x 365 x 0.95 x $3.00 x 1,000 = $1,228,000/yr Difference: $250,000/yr favoring gas engine at this size. Over 20 years: $5,000,000 cumulative fuel savings.

Total Cost of Ownership

Cost CategoryGas Engine (5,000 HP)Gas Turbine (5,000 HP)Electric Motor (5,000 HP)
Capital (installed)$2.5-4.0 million$4.0-7.0 million$3.0-5.0 million + power line
Annual fuel/power$800K-$1.2M$1.0-$1.5M$400K-$800K
Annual maintenance$150K-$300K$100K-$200K$30K-$80K
Emissions compliance$30K-$80K/yr$10K-$30K/yrNone (at site)
Major overhaul$200K-$500K every 3-5 yr$500K-$2M every 5-8 yrMinimal
Availability92-96%95-98%98-99%
Electric motor economics: Electric motors have the lowest operating cost but require grid power infrastructure. The breakeven distance for power line construction is typically 5-15 miles at $50K-$200K per mile. Electrification is increasingly favored for ESG reporting and in areas with strict air quality requirements.

7. Worked Examples

Example 1: Gas Engine Fuel Consumption

Given: BHP = 3,000 HP (at site conditions) Engine type: 4SLB Heat rate (LHV): 7,200 BTU/BHP-hr Fuel gas HHV = 1,020 BTU/SCF Fuel gas LHV = 920 BTU/SCF Operating hours: 8,500 hr/yr Step 1: Convert heat rate to HHV basis HR_HHV = HR_LHV x (HHV/LHV) = 7,200 x (1,020/920) = 7,983 BTU/BHP-hr Step 2: Hourly fuel consumption Q_fuel = BHP x HR_HHV / HHV Q_fuel = 3,000 x 7,983 / 1,020 = 23,479 SCF/hr = 23.5 MCF/hr Step 3: Daily consumption Q_daily = 23.5 x 24 = 0.564 MMSCFD Step 4: Annual consumption Q_annual = 23.5 x 8,500 / 1,000 = 199.7 MMSCF/yr Step 5: Annual fuel cost (at $3.50/MMBTU) Cost = 199,700 MCF x 1.020 MMBTU/MCF x $3.50/MMBTU = $713,000/yr

Example 2: Gas Turbine with Derating

Given: Turbine ISO rating: 12,000 HP Site elevation: 4,500 ft Summer ambient: 105 deg F Inlet filter loss: 3" H2O Exhaust duct loss: 6" H2O HR_ISO (LHV): 8,800 BTU/BHP-hr Step 1: Temperature derating dT = 105 - 59 = 46 deg F f_temp = 1.0 - 0.006 x 46 = 0.724 (27.6% loss) Step 2: Altitude derating P_atm at 4,500 ft = 12.47 psia f_alt = 12.47 / 14.696 = 0.849 (15.1% loss) Step 3: Inlet/exhaust losses f_inlet = 1.0 - 0.005 x 3 = 0.985 f_exhaust = 1.0 - 0.003 x 6 = 0.982 Step 4: Site power BHP_site = 12,000 x 0.724 x 0.849 x 0.985 x 0.982 BHP_site = 12,000 x 0.582 = 6,984 HP Step 5: Site heat rate (HR increases at derated conditions) HR_site = HR_ISO / f_temp (approximately) HR_site = 8,800 / 0.724 = 12,155 BTU/BHP-hr (LHV) Result: The 12,000 HP ISO turbine delivers only 6,984 HP at summer conditions -- a 42% reduction from nameplate. This is why turbine installations often include inlet chilling.

Example 3: Electric Motor vs. Gas Engine

Given: Required shaft power: 2,000 HP Operating hours: 8,400 hr/yr Gas price: $3.00/MMBTU Electricity: $0.08/kWh Gas engine HR: 8,000 BTU/BHP-hr (HHV) Motor efficiency: 95% Fuel HHV: 1,020 BTU/SCF Power line cost: $1.5M (one-time) Gas Engine Annual Fuel Cost: Q_fuel = 2,000 x 8,000 / 1,020 = 15,686 SCF/hr Annual fuel = 15,686 x 8,400 / 1,000,000 = 131.8 MMSCF Cost = 131.8 x 1.020 x $3.00 x 1,000 = $403,000/yr Electric Motor Annual Power Cost: kW = 2,000 x 0.746 / 0.95 = 1,570 kW Annual kWh = 1,570 x 8,400 = 13,188,000 kWh Cost = 13,188,000 x $0.08 = $1,055,000/yr Wait -- electric is MORE expensive in this case. At $0.08/kWh with $3/MMBTU gas, the gas engine wins on fuel alone. Breakeven electricity price: $403,000 / 13,188,000 = $0.031/kWh Electric motors become competitive when: Electricity < $0.035/kWh, OR Gas price > $6/MMBTU, OR Emissions compliance adds > $200K/yr to gas engine costs