Why Synthetic Fuel Loses So Much Energy

A drop-in hydrocarbon can be assembled from water, electricity, and captured carbon. The chemistry is known. The hard part is paying for every conversion while keeping the whole factory busy.

Last updated September 2026
Figure 2 · Follow one unit through the stack

A fuel plant is a chain of conversions

Select a layer. The retained-energy ranges are an engineering frame, not a promise for a particular plant.

Layer 1 of 7

Clean electricity

Energy state
100 units in
Product
Electricity
Operating measure
$/MWh · carbon intensity · hourly match
Where energy goes
Curtailment, transmission, and an under-used connection

Binding constraint: The fuel plant needs low-carbon power at the same hours it needs utilization.

The ranges summarize the architecture of power-to-liquids. A defensible project model must replace them with measured unit operations, an hourly power profile, recycle streams, and product yields.

What the record shows

  • A litre of jet-range fuel stores roughly 9.5 kWh, while representative power-to-liquid designs require far more electrical input after hydrogen, syngas, synthesis, and upgrading losses.
  • Stoichiometry alone requires about 0.38 kg of hydrogen and 2.7 kg of CO₂ for one kilogram of idealized –CH₂– hydrocarbon; real plants need recycle and make off-products.
  • Cheap intermittent power can raise rather than lower fuel cost when electrolysers and synthesis trains recover capital across too few operating hours.
  • The EU requires synthetic aviation fuels to reach 1.2% of fuel supplied at covered airports in 2030 and 35% in 2050, creating demand before a mature cost curve exists.

Mass balances below are derived. Mandates are policy. Announced plants and nameplate tonnes are not counted as operating output.

Part I: Reverse combustion

Build the molecule that an engine takes apart

Combustion combines a hydrocarbon with oxygen and releases heat, CO₂, and water. Power-to-liquids pays energy to reverse that direction: split water, recover carbon, create carbon monoxide, form longer chains, and refine them into a specification.

Clean electricity + H₂OH₂ + captured CO₂Drop-in hydrocarbon + O₂

The product's advantage is compatibility. Dense liquid fuel can use aircraft, engines, tanks, pipelines, and logistics built around hydrocarbons. Its disadvantage is the same fact viewed thermodynamically: electricity is converted into a molecule and later converted again into motion, losing useful energy at both stages.

Compatibility is what the losses buy

44 MJ/kgRegulatory energy-content value for Fischer–Tropsch jet fuel.
1.2%EU synthetic-aviation-fuel minimum share from 2030.
35%EU synthetic share required in 2050 under ReFuelEU Aviation.

Those percentages are demand obligations, not evidence that production has reached scale. EASA's 2026 market report said no large synthetic-fuel facility had yet reached final investment decision in its assessed EU pipeline.

Part II: The material floor

The atoms set a lower bound

An idealized hydrocarbon repeat unit, CH₂, has one carbon atom and two hydrogen atoms. Molar mass makes the minimum feed transparent before conversion losses enter.

3.14 kgStoichiometric CO₂ per kilogram of idealized CH₂ hydrocarbon.
0.143 kgStoichiometric H₂ per kilogram before process losses and upgrading.
~2.5–4 kg/LPractical modeling range for CO₂ input once density, selectivity, and yield enter.

Not all captured carbon reaches saleable jet fuel. Fischer–Tropsch synthesis produces a distribution of chain lengths. Gas and light fractions may be recycled or used for heat; heavy waxes are hydrocracked; oxygenates and water are separated. A plant should report carbon efficiency to each product, not only conversion inside one reactor.

Part III: Compounded conversion

Every individually reasonable step takes a cut

Electrolysis, compression, reverse water-gas shift, synthesis, separation, and upgrading multiply rather than add their efficiencies.

A 70%-efficient electrolyser followed by an 80%-efficient synthesis and upgrading chain retains only 56% before balance-of-plant loads. Real system comparison must include capture energy, compression, recycle, heat integration, auxiliaries, and the fuel fraction that meets the target specification.

LayerMain measureFailure mode
ElectricityHourly $/MWh and carbon intensityCheap hours leave capital idle
HydrogenkWh/kg, stack life, utilizationReplacement and compression erase gains
CarbonOrigin, purity, $/t, capture energyCheap fossil CO₂ does not close the loop
SynthesisCarbon efficiency and target yieldOff-products dilute saleable output
UpgradingCertified litres per feed tonneFuel misses freezing, density, or blending rules
Figure 3 · Interactive production-floor model

Cheap electricity is not the same as cheap fuel

Change power price and plant utilization together. The model exposes electricity, carbon feedstock, and capital recovery for a nominal 100,000-litre-per-day plant; it is not a delivered-fuel quote.

Firm clean power$3.22/L

Exposed production burden

Electricity
$0.77/L
CO₂ feedstock
$0.32/L
Capital + fixed
$2.13/L
Electricity input
21.9 kWh/L
Implied power-to-liquid
43%

A litre of jet-range hydrocarbon contains roughly 9.5 kWh of lower-heating-value energy. The model's implied efficiency divides that by electrolyser plus selected process electricity; it therefore excludes upstream generation and downstream engine losses.

Calculation and boundaries

Electricity cost = (hydrogen input × electrolyser kWh/kg + other process kWh) × $/kWh. Carbon cost = kg CO₂/L × $/kg. Capital + fixed cost = installed capital × annual charge rate ÷ (100,000 L/day × 365 × utilization).

Excluded: water, catalysts, replacement stacks, oxygen or heat credits, carbon-capture energy if not included in CO₂ price, product yield outside the selected inputs, storage, blending, transport, taxes, margin, and financing beyond the annual charge. Installed capital is deliberately user-set; no single public number describes projects with different boundaries.

In the intermittent scenario, a lower power tariff is overwhelmed by capital spread across fewer litres. This is the central e-fuel trade: the cheapest hour can be an expensive factory schedule.
Part IV: The factory clock

The cheapest electron can make expensive fuel

A synthesis plant sized for occasional surplus power earns revenue occasionally but carries capital continuously.

Hydrogen storage can decouple a flexible electrolyser from a steadier synthesis loop, but it adds compression, tanks or caverns, inventory, and another utilization problem. Firm clean electricity costs more per MWh but can lower capital cost per litre. The optimum depends on the joint hourly system, not an annual average power price.

Electrolysers can flex

Stacks can follow power more readily than a hot, pressurized chemical loop, though cycling can affect efficiency and life.

Synthesis prefers continuity

Catalysts, recycle ratios, separation columns, and heat integration work best near a designed operating state.

Storage buys coupling

Hydrogen or intermediate storage protects synthesis utilization while exposing capital, safety, and geography.

Contracts shape operation

Hourly clean-power rules, grid access, and product offtake determine whether an optimized plant is legally low-carbon and financially useful.

Part V: Carbon is a feedstock and a claim

The cheapest source may defeat the purpose

Concentrated industrial CO₂ is easier to purify than atmospheric CO₂, but carbon origin changes the lifecycle story.

Biogenic CO₂ and direct air capture can create a circular atmospheric carbon flow when powered cleanly. Fossil point-source CO₂ can reduce emissions relative to extracting fresh oil but still introduces geological carbon after combustion. A credible fuel certificate traces carbon origin, hydrogen electricity, process energy, transport, and co-product allocation.

Part VI: The hard-use test

Aviation pays for density and compatibility

Cars can use batteries directly. Long-haul aircraft carry their energy source, making mass, volume, freezing behavior, and global refuelling compatibility unusually valuable.

This makes aviation the strongest case for synthetic hydrocarbons—and a stringent test. Fuel must meet ASTM pathways and blend rules, contain appropriate aromatics or be paired with them, work at low temperature, and arrive at airports through certified custody. Policy can create initial demand; only operating plants reveal the eventual premium.

An optimistic view, with conditions

Use synthetic fuel where the molecule earns its losses

The stack can improve through cheaper power, durable electrolysers, heat integration, higher selectivity, modular construction, and shared carbon infrastructure. It should compete first where direct electrification cannot deliver the same service.

Now

Prove full balances

Publish hourly electricity, net carbon intensity, utilization, carbon efficiency, target yield, and delivered litres.

First markets

Concentrate demand

Aviation mandates and durable offtake can support initial plants without pretending they match fossil price.

Scale test

Standardize trains

Repeatable electrolysis, synthesis, upgrading, and certification packages must turn projects into products.

Sources, method, and boundaries

Stoichiometric figures are derived from molar mass; the calculator exposes assumptions rather than predicting market price. Policy shares are legal requirements. Announced capacity and targets are not operating production.