Acetic anhydride 99.5 wt% to storage

Activity Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept), GLO: the inventory of 1 kilogram of its reference product, attributional, cut-off.

Calculation maturity: not assessed Design maturity: Concept (research)Not independently reviewedacetic-anhydride-1:acetic-anhydride-by-acetic-acid-cracking-to-ketene-50-kt-a-concept:product:AC2OPreliminaryReport 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 Acetic anhydride by acetic acid cracking to ketene (50 kt/a, concept), case design, derived from the flowsheet by cheme assess lca.

Reference product
1 kilogram of Acetic anhydride 99.5 wt% to storage (3 bar(a), 40 degC, 99.153 % AC2O (mole))
Chemical
acetic-anhydride
CAS
108-24-7
Code
acetic-anhydride-1:acetic-anhydride-by-acetic-acid-cracking-to-ketene-50-kt-a-concept:product:AC2O
Dataset
acetic-anhydride-by-acetic-acid-cracking-to-ketene-50-kt-a-concept version 0.1.0 · UUID 89a06626-c94a-560a-8599-58b3a206c3c7
Activity UUID
not available (the library assigns none; use the code)
Database
cheme-as-code-atlas-preview-c3ab348 (version preview-c3ab348)
Process
Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept)
Geography
GLO · background inputs with a site rule link at the user's site location (default DE)
Time period
2026 · valid until 2031
Technology
acetic acid cracking to ketene at 700 C / 36 kPa(a) with triethyl phosphate, ammonia quench, condensation to -5 C, reactive absorption of ketene in acetic acid, two-column distillation, dilute acid recovery; furnace fired with natural gas and the vent gas; 50 kt/a, concept design · level current
Boundary
gate-to-gate foreground of the plant
Production volume
50,000,000 kg/a (product:AC2O 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 Acetic anhydride 99.5 wt% to storage

As exported: allocated and scaled to the reference product. Provenance: 11 assumed, 5 calculated. Pedigree scores (1 best, 5 worst): reliability, completeness, temporal correlation, geographical correlation, further technological correlation.

Preliminary4 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
Glacial acetic acid (boundary feed; e.g. methanol carbonylation, D-003)
feed:AA
fresh acid S1 (D-003)
From stream S1
1.246kilogramassumed4 4 1 3 3Atlas (pinned): Acetic acid by low-water iridium methanol carbonylation (60 t/h glacial acid, concept) (Glacial acetic acid to storage, GLO)
compatible: grade the input names no chemical only; acetic-acid (Glacial acetic acid to storage) is taken; unit kilogram; system model cutoff (one database); allocation none (single-output); boundary plant gate (pinned): no distribution or losses; the consumer's dataset counts its delivery
Triethyl phosphate (cracking catalyst)
feed:TEP
catalyst S4 (D-005)
From stream S4
0.001555kilogramassumed4 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
Ammonia (catalyst neutraliser; ammonia-1 makes it)
feed:NH3
neutraliser S8 (D-005)
From stream S8
2.912e-4kilogramassumed4 4 1 3 3market for ammonia, anhydrous, liquid (ammonia, anhydrous, liquid, RER) in your background (default ecoinvent-3.11-cutoff)
Natural gas to the furnace burners
feed:NG
furnace fuel S30 (D-010)
From stream S30
0.04006kilogramassumed4 4 1 3 3Atlas: natural gas, per kg, as methane (Atlas unit proxy) (natural gas, by mass, GLO)
Electric power
feed:POWER
K-301 vent vacuum pump and P-301 absorber circulation pumps (Q6, Q7; D-011)
electricity
From streams Q6, Q7
0.01045kilowatt 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 450 kPa(a)
feed:LPS
E-101 vaporiser and C-401 acid recovery (Q1, Q12; D-011)
steam, LP, 147.65 degC, 4.5 bar(a)
From streams Q1, Q12
0.2736kilowatt hourassumed4 4 1 3 3Atlas: heat from steam, per kWh (Atlas unit proxy) (heat from steam, by energy, GLO)
MP steam 1500 kPa(a)
feed:MPS
C-201 and C-202 reboilers (Q8, Q10; D-011)
steam, MP, 198.25 degC, 15 bar(a)
From streams Q8, Q10
0.329kilowatt hourassumed4 4 1 3 3Atlas: heat from steam, per kWh (Atlas unit proxy) (heat from steam, by energy, GLO)
Distillation residue (heavy ends, liquid) to incineration
product:RESIDUE
stream S20 (D-008)
From stream S20
0.008312kilogramassumed4 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
Wastewater from dilute acid recovery
product:WW
stream S22 (D-009)
From stream S22
0.1908kilogramassumed4 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)
Cooling water return
product:CW
Q3, Q5, Q9, Q11, Q13 (D-011)
cold, 25 degC
From streams Q3, Q5, Q9, Q11, Q13
1.093kilowatt 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)
Brine -10 C (refrigeration) return
product:BRINE
E-102 brine condensers Q4 (D-011)
cold, brine -10 C, -10 degC
From stream Q4
0.04939kilowatt hourassumed4 4 1 3 3unlinked
unlinked, no technosphere mapping: no mapping (chemical 'chilled-water'); add it to lci/mappings.yaml technosphere or to the process's lca/mappings.yaml exchanges

Elementary flows

FlowDirectionCompartmentAmountUnitProvenancePedigree
Ethylene
90f722bf-cb9b-571a-88fc-34286632bdc4
From stream S32
emissionair0kilogramcalculated3 4 1 3 3
Methane, fossil
70ef743b-3ed5-4a6d-b192-fb6d62378555
From stream S32
emissionair / non-urban air or from high stacks0kilogramcalculated3 4 1 3 3
Carbon monoxide, fossil
099b36ab-4c03-4587-87f4-2f81e337afb8
From stream S32
emissionair / non-urban air or from high stacks0kilogramcalculated3 4 1 3 3
Carbon dioxide, fossil
aa7cac3a-3625-41d4-bc54-33e2cf11ec46
From stream S32
emissionair / non-urban air or from high stacks0.1951kilogramcalculated3 4 1 3 3
KET to the environment
emission:KET
unlinked
unlinked, no biosphere mapping: emission of KET (fossil) has no biosphere3 flow identity and is not in lci/mappings.yaml biosphere
From stream S32
emissionnot linked0kilogramcalculated3 4 1 3 3

The streams are the plant's own flows: an amount here is allocated and per 1 kilogram of Acetic anhydride 99.5 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/acetic-anhydride-1/lca/dataset.yaml in library version c3ab348.

Used by

No other activity of this database links to it.

How good it is

Review
Not reviewed: no LCI review record yet
Data quality
DQR 2.33 · PEF-style DQR 2.5
TeR 3 · GeR 3 · TiR 1 · P 3 · 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: closed
  • lci-element-balance: closed
  • lci-mass-balance: closed
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", "acetic-anhydride-1:acetic-anhydride-by-acetic-acid-cracking-to-ketene-50-kt-a-concept:product:AC2O"))

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

Acetic anhydride 99.5 wt% to storage, from Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept) (dataset acetic-anhydride-by-acetic-acid-cracking-to-ketene-50-kt-a-concept 0.1.0), ChemE-as-Code Process Atlas LCI database preview-c3ab348, activity acetic-anhydride-1:acetic-anhydride-by-acetic-acid-cracking-to-ketene-50-kt-a-concept:product:AC2O. 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}
}