Liquid phosgene to the captive consumer
Activity Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive), GLO: the inventory of 1 kilogram of its reference product, attributional, cut-off.
What it is
Unallocated foreground LCI of Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive), case design, derived from the flowsheet by cheme assess lca.
- Reference product
- 1 kilogram of Liquid phosgene to the captive consumer (liquid, 3.4 bar(a), -20 degC, 99.9951 % COCL2 (mole))
- Chemical
- phosgene
- CAS
- 75-44-5
- Code
- phosgene-1:phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive:product:PHOSGENE
- Dataset
- phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive version 0.1.0 · UUID c8420ee2-1ec9-58d9-8f2c-9ca59275eb65
- Activity UUID
- not available (the library assigns none; use the code)
- Database
- cheme-as-code-atlas-preview-c3ab348 (version preview-c3ab348)
- Process
- Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive)
- Geography
- GLO · background inputs with a site rule link at the user's site location (default DE)
- Time period
- 2026 · valid until 2031
- Technology
- CO + Cl2 over activated carbon in a boiling-water-cooled multitubular reactor, two-stage condensation, caustic vent scrubber, thermal oxidiser; 17.3 t/h liquid phosgene, captive · level current
- Boundary
- gate-to-gate foreground of the plant
- Production volume
- 138,768,432 kg/a (product:PHOSGENE 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 Liquid phosgene to the captive consumer
As exported: allocated and scaled to the reference product. Provenance: 8 assumed, 5 calculated. Pedigree scores (1 best, 5 worst): reliability, completeness, temporal correlation, geographical correlation, further technological correlation.
| Input | Amount | Unit | Provenance | Pedigree | Linked to |
|---|---|---|---|---|---|
| Carbon monoxide (from a syngas cold box outside the boundary) feed:CO flowsheet stream S1 (scripts/balance.py, D-003, D-004) From stream S1 | 0.2995 | kilogram | assumed | 4 4 1 3 3 | unlinked 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 |
| Phosgene-grade chlorine (chlor-alkali-1) feed:CL2 flowsheet stream S2 (D-002, D-003) From stream S2 | 0.721 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Dry chlorine gas to the consumer (400 kPa(a)), GLO) compatible: grade the input names no chemical only; chlorine (Dry chlorine gas to the consumer (400 kPa(a))) is taken; unit kilogram; system model cutoff (one database); allocation shares (deviation); boundary plant gate (pinned): no distribution or losses; the consumer's dataset counts its delivery |
| Caustic soda 50 wt% (chlor-alkali-1) feed:NAOH flowsheet stream S20 (D-008) From stream S20 | 0.02561 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen) (Sodium hydroxide, Caustic soda 50 wt-% to storage, GLO) compatible: grade the input names no chemical only; sodium-hydroxide (Sodium hydroxide, Caustic soda 50 wt-% to storage) is taken; unit kilogram; system model cutoff (one database); allocation shares (deviation); boundary plant gate (pinned): no distribution or losses; the consumer's dataset counts its delivery |
| Process water (dilution) feed:PW flowsheet stream S21 (D-008) From stream S21 | 0.04553 | kilogram | assumed | 4 4 1 3 3 | market for water, deionised (water, deionised, RoW) in your background (default ecoinvent-3.11-cutoff) |
| Electric power feed:POWER flowsheet energy streams Q4 (reactor coolant vacuum pump), Q5 (scrubber pump), Q6 (air fan), D-010 electricity | 0.001107 | kilowatt hour | assumed | 4 4 1 3 3 | market for electricity, medium voltage (electricity, medium voltage, DE, site location) in your background (default ecoinvent-3.11-cutoff) |
| Spent scrubber liquor to wastewater treatment product:EFF flowsheet stream S24 (D-008) From stream S24 | 0.07607 | kilogram | assumed | 4 4 1 3 3 | Atlas (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 flowsheet energy streams Q1 (reactor, via the boiling-water circuit) and Q2 (condenser E-102), D-005, D-007 cold, 25 degC | 0.3608 | kilowatt hour | assumed | 4 4 1 3 3 | Atlas (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) |
| Refrigerated brine return (243 K) product:BRINE flowsheet energy stream Q3 (after-condenser E-103), D-007 cold, -30 degC From stream Q3 | 0.02779 | kilowatt hour | assumed | 4 4 1 3 3 | unlinked 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
| Flow | Direction | Compartment | Amount | Unit | Provenance | Pedigree |
|---|---|---|---|---|---|---|
| Chlorine 39d1390a-ded6-41cb-a536-d47510bf2fbc From stream S32 | emission | air | 1.072e-10 | kilogram | calculated | 3 4 1 3 3 |
| Carbon monoxide, fossil 099b36ab-4c03-4587-87f4-2f81e337afb8 From stream S32 | emission | air / non-urban air or from high stacks | 1.425e-5 | kilogram | calculated | 3 4 1 3 3 |
| Carbon dioxide, fossil aa7cac3a-3625-41d4-bc54-33e2cf11ec46 From stream S32 | emission | air / non-urban air or from high stacks | 0.02236 | kilogram | calculated | 3 4 1 3 3 |
| Phosgene 53b9f77b-7336-5c15-9e01-62a25d3e3d75 From stream S32 | emission | air | 5.278e-9 | kilogram | calculated | 3 4 1 3 3 |
| Hydrochloric acid c9a8073a-8a19-5b9b-a120-7d549563b67b From stream S32 | emission | air | 3.852e-7 | kilogram | calculated | 3 4 1 3 3 |
The streams are the plant's own flows: an amount here is allocated and per 1 kilogram of Liquid phosgene to the captive consumer, 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/phosgene-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 2.5TeR 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
- cheme-as-code-atlas-preview-c3ab348.xlsx · bw2io ExcelImporter workbook (bw2io 0.9 Excel layout) · the whole databasecode phosgene-1:phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive:product:PHOSGENE
- cheme-as-code-atlas-preview-c3ab348-olca-jsonld.zip · openLCA JSON-LD (olca-schema) (2) · the whole databaseprocess c8420ee2-1ec9-58d9-8f2c-9ca59275eb65 (processes/c8420ee2-1ec9-58d9-8f2c-9ca59275eb65.json)
- cheme-as-code-atlas-preview-c3ab348-multifunctional.json · Brightway 2.5 multifunctional database (JSON, for the multifunctional package) (cheme-as-code/lci-multifunctional/v1) · the whole databasecode phosgene-1:phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive:product:PHOSGENE
- cheme_as_code_lci-0.1.0-py3-none-any.whl · the installer
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", "phosgene-1:phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive:product:PHOSGENE"))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
Liquid phosgene to the captive consumer, from Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive) (dataset phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive 0.1.0), ChemE-as-Code Process Atlas LCI database preview-c3ab348, activity phosgene-1:phosgene-from-co-and-chlorine-over-activated-carbon-17.3-t-h-liquid-phosgene-captive:product:PHOSGENE. 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}
}