substance

Glycerol

Formula
C3H8O3
CAS
56-81-5
InChIKey
PEDCQBHIVMGVHV-UHFFFAOYSA-N
ChEBI
CHEBI:17754

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Made by

Used by

No process in the Atlas uses this yet.

When a process with this chemical is added to the library, it appears here.

Routes compared

One route in the Atlas makes Glycerol: nothing to compare yet. A comparison appears when a second route is added.

Per 1 kg of Glycerol: inventory from each route's LCI dataset, unallocated; footprints per the functional unit of their own LCA.

RouteTier, design maturity, review statusGeography, yearEnergyFeedstocksKey emissionsFootprintComparability
Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept)Crude glycerol refining: HCl acidulation, fatty-layer decanting, NaOH neutralisation, atmospheric methanol column, vacuum dewatering, vacuum still with live steam and salt centrifuge, activated carbon bleaching; 10 000 t/a glycerol 99.7 wt%flowsheet or hand-writtenDesign maturity: Concept (research)Not independently reviewedDataset review: unreviewedGLO, 2026
  • MP steam 1000 kPa(a) to the methanol column reboiler (condensate returned): 0.43 kWh
  • LP steam 450 kPa(a) to the dewatering evaporator (condensate returned): 0.0286 kWh
  • HP steam 3000 kPa(a) to the still reboiler (condensate returned): 0.298 kWh
  • Electric power: 0.0499 kWh
  • Crude glycerol from the biodiesel plant: 1.76 kg
  • Hydrochloric acid 32 wt%: 0.116 kg
  • Caustic soda 50 wt%: 0.00743 kg
  • Activated carbon (fresh): 0.00201 kg
  • LP steam 450 kPa(a), live stripping steam to the still: 0.105 kg
  • MP steam 1000 kPa(a), motive steam of the still vacuum ejectors: 0.178 kg
noneno footprint–

ISO 14044 requires a critical review (by a panel of interested parties, ISO/TS 14071) of a comparative assertion intended to be disclosed to the public. These routes are listed side by side for screening; a statement that one is better than another needs that review. None of these routes has had such a review.