PTE — Prestige Thermal Energy
Condensation and liquid recovery equipment in a dark industrial hall

Waste to liquid fuels

Recover the molecule.

Condensable hydrocarbons released during flash pyrolysis can be recovered as liquid and progressively refined into hydrocarbon streams with real commercial value.

The pathway

Feedstock to hydrocarbon streams

  1. 01Carbonaceous feedstockCharacterised and prepared
  2. 02Flash pyrolysisRapid oxygen-limited conversion
  3. 03Hydrocarbon vapoursCondensable product stream
  4. 04CondensationVapour recovered as liquid
  5. 05Pyrolysis liquidRaw intermediate
  6. 06Cleaning / upgradingContaminants · water · stability
  7. 07FractionationSeparation by boiling range
  8. 08Valuable hydrocarbon streamsProducts and intermediates

Potential product pathways

What the liquid can become

Actual product distribution and quality depend strongly on the feedstock and on the downstream processing selected for the project. No single yield or specification applies across waste streams.

Outputs depend on feedstock, plant configuration and downstream upgrading. Products are described as potential pathways, not guaranteed specification-grade fuels.

01

Naphtha-range fractions

Lighter cuts of potential interest to petrochemical and chemical recycling routes.

02

Distillate / diesel-range fractions

Mid-boiling material that may serve as a fuel intermediate after upgrading.

03

Heavier hydrocarbon fractions

Higher boiling material for fuel-oil-type use, further processing or recycle.

04

Chemical recycling feedstocks

Hydrocarbon streams directed to chemical rather than combustion routes.

05

Circular fuel intermediates

Blend or refinery intermediates, subject to acceptance criteria.

Separation

Fractions separate by boiling range

Scroll to follow the separation. The graphic is illustrative: it shows the principle of cut separation, not PTE operating conditions.

FEED

Separation by boiling range

  • Light fraction

    Lightest boiling range

    Light ends and gases, typically returned for energy use within the plant.

  • Naphtha-range

    Low boiling range

    Potential petrochemical or chemical recycling feedstock, subject to specification.

  • Middle distillate

    Mid boiling range

    Diesel-range material that may be suitable as an intermediate after upgrading.

  • Heavy fraction

    Highest boiling range

    Heavier hydrocarbons for fuel-oil-type use, further processing or recycle.

Illustrative only · no PTE operating conditions shown

Upgrading

Pyrolysis is the beginning.

Raw pyrolysis liquid is an intermediate. Product value is increased through a treatment sequence selected for the specific feedstock and the intended offtake route.

01

Contaminant removal

Targeted removal of species that limit product acceptance.

02

Dechlorination where required

Applied where chlorine-bearing feedstocks make it necessary.

03

Filtration

Removal of fines and particulate carry-over.

04

Dehydration

Reduction of water content to improve stability and handling.

05

Distillation

Separation into defined boiling-range cuts.

06

Guard-bed treatment

Protection of downstream catalysts and equipment.

07

Hydrotreating where appropriate

Applied when the product route and economics justify it.

08

Product blending

Combining cuts to meet a defined intermediate specification.

09

Further refining

Additional processing through appropriate third-party or partner facilities.

From waste stream
to hydrocarbon value stream.

Share feedstock composition, volume and intended offtake and PTE will outline the recovery and upgrading configuration worth evaluating.