Reciprocating gas compressor
A leaking valve shows up as heat before it shows up as a trip.
Each compressor stage has a discharge temperature that follows from its pressure ratio. A leaking valve or worn rings push gas back through the cylinder and the temperature climbs above that line. The twin reads it per throw, together with rod load, and names the valve before it breaks.
1,340 hp gas engine, 4 throws, 2 stages, 1,200 rpm, 10.4 MMscfd, 150 to 1,100 psig
Built and run to API 618, API 11P
- Capacity
- 10.4 MMscfd
- Brake power
- 1,225 hp
- Interstage
- 439 psig
- Peak rod load
- 45% of rating
Anatomy and nameplate
- 1Suction and discharge pressure per stage. Sets the pressure ratio each cylinder works against.
- 2Discharge temperature per cylinder. Compared with the model for that ratio. Heat above the line is gas going round again.
- 3Valve cap temperatures. Where fitted, these point to the one valve that leaks.
- 4Frame and crosshead vibration. Loose crosshead, worn pin bushing or liquid in a cylinder.
- 5Rod drop or rod position. Where fitted, tracks rider band wear and the piston settling in the bore.
- 6Engine speed and load. Speed sets the strokes. Load shows how close the engine is to its rating.
- 7Lube oil pressure and temperature. Frame oil and cylinder lubricator health.
- 8Scrubber levels. Liquid that gets past a scrubber ends up in a cylinder.
| Duty | |
|---|---|
| Service | Natural gas gathering, field to sales line |
| Gas | Specific gravity 0.65, k = 1.27 |
| Suction | 150 psig at 35 °C |
| Interstage | 439 psig, cooled to 45 °C |
| Discharge | 1,100 psig |
| Overall pressure ratio | 6.77 (stage 1 2.75, stage 2 2.46) |
| Capacity | 10.4 MMscfd |
| Brake power | 1,225 hp, 91% of the engine rating |
| Specific power | 117 hp per MMscfd |
| Discharge temperature | Stage 1 109 °C, stage 2 112 °C |
| Volumetric efficiency | Stage 1 75%, stage 2 75% |
| Machine | |
| Driver | 1,340 hp natural gas engine, 1,200 rpm, direct coupled |
| Frame | Separable, 4 throws, 2 stages, double-acting cylinders |
| Stroke and rod | 5.5 in stroke, 2.0 in rod, 1,100 ft/min piston speed |
| Stage 1 cylinders | 2 × 8.75 in bore, 17% clearance, 447 cfm displacement each |
| Stage 2 cylinders | 2 × 5.375 in bore, 20% clearance, 161 cfm displacement each |
| Rod load rating | 40,000 lb combined, tension and compression |
| Cooling | Engine-driven aerial cooler: jacket water, intercooler and aftercooler |
| Scrubbers | Suction and interstage, with level switches and dump valves |
| Rod load at design | |
| Stage 1 throws | 17,867 lb compression, 17,717 lb tension, 45% of rating |
| Stage 2 throws | 15,323 lb compression, 12,374 lb tension, 38% of rating |
| Reversal, stage 2 | 157° in tension, 203° in compression each turn |
From the well to market
Wells lift the fluid. The separator splits it. Oil goes to the tank battery and gas to the compressor station, and both leave by pipeline for processing.
- Well fluid
- Crude oil
- Gas
- Has its own twin page
The physics
The equations behind every curve on this page.
Discharge temperature
T₂ = T₁·r^((k − 1)/k)
Above this line means gas is going round again. Stage 2 runs at 112 °C healthy.
Volumetric efficiency
VE = 1 − Cl·(r^(1/k) − 1) − losses
Gas left in the clearance re-expands before new gas can come in.
Rod load
F = P_d·A_head − P_s·(A_head − A_rod)
Must stay inside the frame rating and change direction every stroke.
Isentropic power
P = k/(k−1)·p₁·Q₁·(r^((k−1)/k) − 1) / η
1,225 hp at the coupling for 10.4 MMscfd.
Heat and capacity
A leaking valve heats the cylinder and takes gas away from the line. Both show up against the model before the valve breaks.
Discharge temperature against pressure ratio, stage 2
Gas in at 45 °C after the intercooler, k = 1.27
- Model, healthy valves
- Leaking discharge valve, 10% backflow
- Stage 2 ratio, healthy
- 2.46
- Stage 2 ratio, leaking
- 2.37
- Throw 3 above the model
- 8.8 °C
Gas that leaks back through the valve gets compressed again, so the cylinder runs hot for its pressure ratio. The ratio itself falls, because the leak pushes interstage pressure up. That is why we compare against the model at the ratio the machine is actually running.
T₂ = T₁·r^((k−1)/k) leaking: T₂ = T₁·r_t·(1 − f) / (1 − r_t·f)
Capacity and power against suction pressure
1100 psig discharge, 1200 rpm, no unloaders
- Flow, healthy
- Flow, one leaking valve
- Brake power, healthy (right axis)
- Capacity lost to one valve
- 0.14 MMscfd
- Load at design
- 91% of engine rating
Higher suction pressure packs more gas into every stroke, so flow and power both climb until the engine runs out of horsepower. A leaking valve shifts the whole flow line down.
Q = VE·(2·A_head − A_rod)·S·N VE = 1 − Cl·(r^(1/k) − 1) − losses
Rod load
Gas pressure on both sides of the piston and the weight of the moving parts add up to the load on the rod, every degree of the turn.
Rod load across one turn, both stages
150 → 439 → 1,100 psig, 1,200 rpm. Compression positive.
- Stage 1 throw, combined
- Stage 2 throw, combined
- Stage 1 gas load only
- Peak, share of rating
- Stage 1 45%, stage 2 38%
- Reversal, stage 2
- 157° tension, 203° compression
The load must stay inside the frame rating and change direction every turn, so the crosshead pin bushing gets oil on both sides. A high interstage pressure or a stuck unloader can take either one away.
F = P_HE·A_head − P_CE·(A_head − A_rod) − m·r·ω²·(cos θ + λ·cos 2θ)
Failure modes
What breaks, what it looks like, what the twin does about it.
| Failure mode | The physics | Signals that show it | How the twin catches it |
|---|---|---|---|
| Valve failure | A broken plate or spring lets gas flow back through the valve, so the same gas is compressed again. | Discharge temperature above the model on one cylinder. Valve cap temperature up. Capacity down. Interstage pressure moves. | Compares each cylinder with the temperature its ratio predicts, and points to the end and the valve. |
| Piston ring wear | Gas leaks past the rings from one end of the cylinder to the other. | Both ends of one cylinder run hot. Capacity falls slowly. | Tells ring wear from a valve by the pattern across head end and crank end. |
| Packing leak | Worn packing rings let gas escape along the rod to the vent. | Packing vent flow or temperature up. Small capacity loss. | Trends packing temperature and vent flow against rod load and speed. |
| Rod load over rating or no reversal | High interstage pressure or an unloader out of place raises the gas load, or holds it in one direction. | Interstage pressure off the model. Crosshead vibration. Crosshead pin temperature. | Works out combined rod load and reversal every degree from the pressures it reads. |
| Liquid carryover | Liquid from a full scrubber reaches a cylinder and cannot be compressed. | Scrubber level high. Sharp crosshead vibration. Valve damage that follows. | Watches scrubber levels and dump cycles against gas temperature and flow. |
What the twin does not do
- The compressor panel and the station ESD stay in charge of every trip. TwinEdge is never in the safety loop.
- We do not change speed, unloaders or recycle valves. Your operators and your SCADA do.
- We read the panel. We have no write path into it.
How we catch it early
A physics twin and a PINN, working on one reciprocating gas compressor.
The twin is a set of equations for this machine, tuned to its nameplate. Give it the flow, speed and conditions and it returns what every reading should be. It always gives the same answer for the same inputs.
A physics-informed neural network, or PINN, sits on top. It is trained on the plant’s own data and it is penalized whenever it breaks a physics rule. So it can only learn what the equations leave out: wear, fouling, friction. It cannot invent an answer that the machine could never produce.
Step 1
Measure
Flow, pressure, current, temperature, vibration. Whatever the asset already has.
Step 2
Physics twin
The equations of this machine, set to its nameplate. It says what the readings should be right now.
Step 3
Residual
Measured minus expected. Demand, weather and speed are already taken out.
Step 4
PINN
A small neural network that learns the cause of the gap, under the physics rules.
Step 5
Finding
A named cause, a date, and the kWh or hours at stake. An engineer reviews it.
loss = (measured − predicted)² + λ · (physics residual)²
The second term is the rulebook. It is zero when the network obeys the equations.
Why this beats black-box AI
A black-box model learns patterns from history. It needs examples of each failure, and it goes quiet when the pump runs at a point it has not seen. The twin starts from physics, so it works on day one. The PINN adds what physics cannot know about this particular machine.
That is also what makes the savings countable. The baseline is a calculation, not a guess, so the gap between baseline and meter is a number a customer can check.
What the twin checks on this asset
- Discharge temperature against the model, per cylinder
- Capacity against volumetric efficiency: 10.4 MMscfd at design
- Combined rod load and reversal, every degree of the turn
- Frame and crosshead vibration trend
| Fixed alarm | Black-box AI | Twin + PINN | |
|---|---|---|---|
| Needs failure history to learn | No | Yes, lots | No |
| Says what is wrong | No | Rarely | Yes, by name |
| Works at a flow it has never seen | No | Often fails | Yes, the equations still hold |
| Puts a number on the saving | No | No | Yes, in kWh and dollars |
| Lead time on slow wear | Late | Varies | Weeks to months |
| Every number can be traced | Yes | No | Yes, to an equation |
What the twin puts a number on
Energy and cost, from the equations.
One leaking discharge valve
35 hp
Spent on gas that goes round again. $6,969 a year in engine fuel.
Capacity lost
0.14 MMscfd
1.4% of the line, $427 a day at $3.00 per Mscf
Throw 3 above the model
8.8 °C
At the stage 2 pressure ratio the machine is running
Unplanned shutdown day
$31,322
10.4 MMscfd not moved at $3.00 per Mscf
What we do for you
We watch it. We catch it. We prove it.
Our reliability engineers run the twin on your reciprocating gas compressor, review every finding, and help your crew fix it. After the repair we compare the meter to the baseline and write the result in the ledger.
More assets
More from oil & gas, then the lead asset of each other industry.
- Oil & gasBeam pumping unitOpen
- Oil & gasElectric submersible pumpOpen
- Oil & gasShell-and-tube heat exchangerOpen
- Oil & gasCrude storage tankOpen
- Water & wastewaterCentrifugal pumpOpen
- ManufacturingRotary screw air compressorOpen
- Buildings & data centersWater-cooled centrifugal chillerOpen
- Energy & utilitiesPower transformerOpen
- Telecom towersDiesel generator setOpen
- PharmaceuticalWFI distribution loopOpen