Hydrogen peroxide 50 wt% to storage

Activity Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%), GLO: the inventory of 1 kilogram of its reference product, attributional, cut-off.

Calculation maturity: not assessed Design maturity: Concept (research)Not independently reviewedhydrogen-peroxide-1:hydrogen-peroxide-anthraquinone-autoxidation-process-50-kt-a-h2o2-50-wt:product:PRODPreliminaryReport a problem with this dataset
Research outputAn inventory from a research design at the design maturity its process states, not verified plant data: check its calculation maturity and review status before use. Background activities are referenced by name only; no background data is included. All caveats

What it is

Unallocated foreground LCI of Hydrogen peroxide, anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%), case design, derived from the flowsheet by cheme assess lca.

Reference product
1 kilogram of Hydrogen peroxide 50 wt% to storage (3 bar(a), 30 degC, 50 % H2O2 (mass))
Chemical
hydrogen-peroxide
CAS
7722-84-1
Code
hydrogen-peroxide-1:hydrogen-peroxide-anthraquinone-autoxidation-process-50-kt-a-h2o2-50-wt:product:PROD
Dataset
hydrogen-peroxide-anthraquinone-autoxidation-process-50-kt-a-h2o2-50-wt version 0.1.0 · UUID 78732531-3b28-5c2d-aa45-0d3a5c6a4e58
Activity UUID
not available (the library assigns none; use the code)
Database
cheme-as-code-atlas-preview-c3ab348 (version preview-c3ab348)
Process
Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%)
Geography
GLO · background inputs with a site rule link at the user's site location (default DE)
Time period
2026 · valid until 2031
Technology
anthraquinone autoxidation (AO) process, fixed-bed Pd hydrogenation, air oxidation, water extraction, vacuum concentration to 50 wt%; 50 kt/a H2O2 (100 %) · level current
Boundary
gate-to-gate foreground of the plant
Production volume
100,000,000 kg/a (product:PROD per hour x operation.hours_per_year (8000 h/a))
Classification
ISIC Rev.4 2011 (taxonomy/families.yaml (ISIC Rev.4) of the process's families)
System model
attributional, cut-off (docs/system-model.md, methodology 1.1.0)
Allocation
mass, 100 % of the dataset to this product (rule single-output, from default)
one product: nothing to allocate
Rights
CC-BY-4.0: the ChemE-as-Code process library's own concept design (LICENSE-DATA)

Exchanges per 1 kilogram of Hydrogen peroxide 50 wt% to storage

As exported: allocated and scaled to the reference product. Provenance: 23 assumed. Pedigree scores (1 best, 5 worst): reliability, completeness, temporal correlation, geographical correlation, further technological correlation.

Preliminary15 exchanges are not yet linked to a background dataset. They count no burden, so the inventory is incomplete: do not read a result from it as complete.
InputAmountUnitProvenancePedigreeLinked to
Hydrogen (boundary feed; e.g. from hydrogen-1)
feed:H2
stream S01, 63.5 kg/t H2O2 (D-003, D-005)
From stream S01
0.03176kilogramassumed4 4 1 3 3market for hydrogen, gaseous, low pressure (hydrogen, gaseous, low pressure, RER) in your background (default ecoinvent-3.11-cutoff)
2-Ethylanthraquinone make-up
feed:MKQ
stream S02, 1.0 kg/t H2O2, BREF Table 12.4 (D-011)
From stream S02
5e-4kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Working-solution solvent make-up
feed:MKS
stream S03, 2.5 kg/t H2O2, BREF Table 12.4 (D-011)
From stream S03
0.00125kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Demineralised water
feed:DEMIN
stream S29, 1.19 t/t H2O2 (D-008)
From stream S29
0.5956kilogramassumed4 4 1 3 3market for water, deionised (water, deionised, RoW) in your background (default ecoinvent-3.11-cutoff)
Activated alumina (reversion agent)
feed:ALU
stream S34, 6 kg/t H2O2, BREF Table 12.4 (D-011)
From stream S34
0.003kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
LP steam, direct use (adsorber regeneration, ejector)
feed:STEAMD
streams S17 and S31: adsorber regeneration and WS dryer ejector (D-009, D-010)
From streams S17, S31
0.1167kilogramassumed4 4 1 3 3Atlas: steam, saturated, 11 bar(a), per kg, as heat from steam (Atlas unit proxy) (steam, saturated, 11 bar(a), GLO)
Electric power
feed:POWER
streams Q01-Q04: air compressor, WS pumps, auxiliary pumps, vacuum pump, 355 kWh/t H2O2 (D-007, D-010)
electricity
From streams Q01, Q02, Q03, Q04
0.1773kilowatt hourassumed4 4 1 3 3market for electricity, medium voltage (electricity, medium voltage, DE, site location) in your background (default ecoinvent-3.11-cutoff)
LP steam 350 kPa(a), indirect
feed:LPS
stream Q05, concentrator reboiler (D-010)
steam, LP, 137.85 degC, 3.5 bar(a)
From stream Q05
0.2371kilowatt hourassumed4 4 1 3 3Atlas: heat from steam, per kWh (Atlas unit proxy) (heat from steam, by energy, GLO)
Aqueous effluent to biological waste water treatment
product:WW
streams S19 and S32: adsorber condensate and WS dryer water with ejector condensate, 0.41 t/t H2O2, 0.15 kg TOC/t (D-011)
From streams S19, S32
0.2049kilogramassumed4 4 1 3 3Atlas (plant): wastewater to treatment, per kg (Atlas unit proxy) (wastewater, by mass, GLO)
compatible: grade the input names wastewater only; wastewater (Wastewater treated) is taken; unit kilogram; system model cutoff (one database); allocation mass (single-output); boundary plant gate of a site utility: no utility market yet (docs/markets.md)
Spent reversion agent (alumina with organics)
product:SPENT
stream S35, 9 kg/t H2O2 (D-011)
From stream S35
0.0045kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Cooling water return
product:CW
streams Q06-Q11: reactor heats, air aftercooler, off-gas condenser, concentrator condenser, product cooler (D-010)
cold, 25 degC
From streams Q06, Q07, Q08, Q09, Q10, Q11
1.233kilowatt hourassumed4 4 1 3 3Atlas (plant): cooling water service, per kWh heat rejected (Atlas screening proxy) (heat rejected to cooling water, GLO)
compatible: grade the input names cooling-water only; cooling-water (Heat rejected to cooling water, 25/35 degC) is taken; unit kilowatt hour; carrier cold, 25 degC from cold, 25 degC; system model cutoff (one database); allocation mass (single-output); boundary plant gate of a site utility: no utility market yet (docs/markets.md)
Nitric acid (100 % basis; pH adjustment and passivation)
consumable:nitric-acid
ASSUMED 4.0 kg/t H2O2, inside the BREF 2.5-7 kg/t (Table 12.4)
0.002kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (chemical 'nitric-acid'); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Disposal: Nitric acid (100 % basis; pH adjustment and passivation) (neutralised nitrate to biological waste water treatment)
disposal:consumable.nitric-acid
ASSUMED: all nitric acid leaves as nitrate in the effluent
0.002kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Sodium hydroxide (100 % basis)
consumable:sodium-hydroxide
ASSUMED 2.0 kg/t H2O2, inside the BREF 1.5-4 kg/t (Table 12.4)
0.001kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (chemical 'sodium-hydroxide'); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Disposal: Sodium hydroxide (100 % basis) (neutralised sodium salts to biological waste water treatment)
disposal:consumable.sodium-hydroxide
ASSUMED: all NaOH leaves as sodium salts in the effluent
0.001kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Activated carbon (off-gas adsorbers A-201)
consumable:activated-carbon
ASSUMED 0.10 kg/t H2O2 as spent adsorbent, inside the BREF 0.01-0.34 kg/t (Table 12.6)
5e-5kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Disposal: Activated carbon (off-gas adsorbers A-201) (incineration or reactivation of spent activated carbon)
disposal:consumable.activated-carbon
ASSUMED: replaced carbon leaves as spent adsorbent
5e-5kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Ion-exchange resin (crude purification)
consumable:ion-exchange-resin
ASSUMED 0.015 kg/t H2O2, inside the BREF 0.005-0.027 kg/t (Table 12.6)
7.5e-6kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Disposal: Ion-exchange resin (crude purification) (incineration of spent ion-exchange resin)
disposal:consumable.ion-exchange-resin
ASSUMED
7.5e-6kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges
Palladium lost from the hydrogenation catalyst (as Pd)
consumable:palladium-catalyst-loss
ASSUMED 0.2 g Pd/t H2O2, inside the BREF 0.1-0.3 g/t for fixed beds (12.3.3 b)
1e-7kilogramassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (no chemical slug or factor id); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges

Elementary flows

FlowDirectionCompartmentAmountUnitProvenancePedigree
DIBC to the environment
emission:DIBC
unlinked
unlinked, no biosphere mapping: emission of DIBC (fossil) has no biosphere3 flow identity and is not in lci/mappings.yaml biosphere
From streams S06, S18
emissionnot linked0kilogramassumed4 4 1 3 3
Hydrogen
no biosphere3 UUID: linked by name and compartment
From streams S06, S18
emissionair3.175e-4kilogramassumed4 4 1 3 3
TMB to the environment
emission:TMB
unlinked
unlinked, no biosphere mapping: emission of TMB (fossil) has no biosphere3 flow identity and is not in lci/mappings.yaml biosphere
From streams S06, S18
emissionnot linked4.893e-5kilogramassumed4 4 1 3 3

The streams are the plant's own flows: an amount here is allocated and per 1 kilogram of Hydrogen peroxide 50 wt% to storage, so it differs from the stream's flow, and it can sum several streams.

Where these numbers come from: each exchange names its source above; the dataset is processes/hydrogen-peroxide-1/lca/dataset.yaml in library version c3ab348.

Used by

How good it is

Review
Not reviewed: no LCI review record yet
Data quality
DQR 2.33 · PEF-style DQR 2.75
TeR 3 · GeR 3 · TiR 1 · P 4 · C 4 · weakest TeR · primary data 0 %
Mass and carbon closure
Assessed (lca/manifest.json balance, tolerance 5 %: design maturity concept (sourced screening))
  • lci-carbon-origin: not-assessable
  • lci-element-balance: not-assessable
  • lci-mass-balance: closed
  • element balance not assessable: no composition for consumable:nitric-acid (no composition), disposal:consumable.nitric-acid (no composition), consumable:sodium-hydroxide (no composition), disposal:consumable.sodium-hydroxide (no composition), consumable:activated-carbon (no composition), disposal:consumable.activated-carbon (no composition), consumable:ion-exchange-resin (no composition), disposal:consumable.ion-exchange-resin (no composition), consumable:palladium-catalyst-loss (no composition)
  • carbon balance not assessable: no composition for consumable:nitric-acid (no composition), disposal:consumable.nitric-acid (no composition), consumable:sodium-hydroxide (no composition), disposal:consumable.sodium-hydroxide (no composition), consumable:activated-carbon (no composition), disposal:consumable.activated-carbon (no composition), consumable:ion-exchange-resin (no composition), disposal:consumable.ion-exchange-resin (no composition), consumable:palladium-catalyst-loss (no composition)
Change report
Not available: this build has no change report against an earlier release.

KPI benchmark positions

Not available: no benchmarked KPI for this dataset.

How to use it

Downloads

A file with this activity alone is not available: each file above is the whole database, and the line under it says how to find this activity there.

import bw2data as bd
from cheme_as_code_lci import install

bd.projects.set_current("my-project")   # holds your licensed background + biosphere3
install("cheme-as-code-atlas-preview-c3ab348.xlsx", background="ecoinvent-3.11-cutoff", location="DE")
activity = bd.get_activity(("cheme-as-code-atlas-preview-c3ab348", "hydrogen-peroxide-1:hydrogen-peroxide-anthraquinone-autoxidation-process-50-kt-a-h2o2-50-wt:product:PROD"))

While any exchange of the database has no mapping, install() writes nothing and only lists the unlinked exchanges. So the last line finds no activity until the gaps are mapped: the download section gives the ways to use the database now.

How to cite

Hydrogen peroxide 50 wt% to storage, from Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%) (dataset hydrogen-peroxide-anthraquinone-autoxidation-process-50-kt-a-h2o2-50-wt 0.1.0), ChemE-as-Code Process Atlas LCI database preview-c3ab348, activity hydrogen-peroxide-1:hydrogen-peroxide-anthraquinone-autoxidation-process-50-kt-a-h2o2-50-wt:product:PROD. Cite the Process Atlas paper (in preparation, 2026), by Artur M. Schweidtmann and Jana M. Weber, and the ChemE-as-Code Process Atlas LCI database version preview-c3ab348.

DOI: none yet (the Process Atlas paper is in preparation)

For the data, cite the Process Atlas paper; for the platform that builds and checks it, the ChemE-as-Code paper.

Schweidtmann, A. M. & Weber, J. M. (2026, in preparation). Process Atlas: an open, git-native, reproducible library and life cycle inventory of chemical processes (working title).

BibTeX
@unpublished{schweidtmann_process_atlas,
  author = {Schweidtmann, Artur M. and Weber, Jana M.},
  title = {{Process Atlas: an open, git-native, reproducible library and life cycle inventory of chemical processes (working title)}},
  year = {2026},
  url = {https://atlas.cheme-as-code.org},
  note = {in preparation}
}

Schweidtmann, A. M. (2026, in preparation). ChemE-as-Code: An Open-Source Platform for AI-Accelerated Chemical Process Engineering (working title).

BibTeX
@unpublished{schweidtmann_cheme_as_code,
  author = {Schweidtmann, Artur M.},
  title = {{ChemE-as-Code: An Open-Source Platform for AI-Accelerated Chemical Process Engineering (working title)}},
  year = {2026},
  url = {https://cheme-as-code.org},
  note = {in preparation}
}