Dried sodium azide to packing
Activity Sodium azide by the hydrazine / methyl nitrite route, batch, with precipitation from the reaction liquor (670 t/a), GLO: the inventory of 1 kilogram of its reference product, attributional, cut-off.
What it is
Unallocated foreground LCI of Sodium azide by the hydrazine / methyl nitrite route, batch, with precipitation from the reaction liquor, case design, derived from the flowsheet by cheme assess lca.
- Reference product
- 1 kilogram of Dried sodium azide to packing (1.01325 bar(a), 60 degC, 99.2094 % NAN3S (mole))
- Chemical
- sodium-azide
- CAS
- 26628-22-8
- Code
- sodium-azide-1:sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor:product:NAN3P
- Dataset
- sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor version 0.1.0 · UUID a1551f0b-c590-54e0-b1d5-9011b57e249f
- Activity UUID
- not available (the library assigns none; use the code)
- Database
- cheme-as-code-atlas-preview-a3c52e4 (version preview-a3c52e4)
- Process
- Sodium azide by the hydrazine / methyl nitrite route, batch, with precipitation from the reaction liquor (670 t/a)
- Geography
- GLO · background inputs with a site rule link at the user's site location (default DE)
- Time period
- 2026 · valid until 2031
- Technology
- Batch plant on a dedicated train: methyl nitrite generated from sodium nitrite, methanol and 98.5 % sulfuric acid at 298 K (R-101) and absorbed over 10 h into hydrazine hydrate and caustic soda with the recycled mother liquor at 313 K (R-102, semi-batch); methanol stripped and the liquor concentrated at 10 kPa(a) (C-101), NaN3 precipitated at 303 K, filtered, washed with methanol and vacuum-dried at 333 K (filter-dryer F-101); 1027.6 kg per batch, 652.6 batches a year · level current
- Boundary
- gate-to-gate foreground of the plant
- Production volume
- 670,643 kg/a (product:NAN3P per hour x operation.hours_per_year (7920 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 Dried sodium azide to packing
As exported: allocated and scaled to the reference product. Provenance: 12 assumed, 4 calculated. Pedigree scores (1 best, 5 worst): reliability, completeness, temporal correlation, geographical correlation, further technological correlation.
| Input | Amount | Unit | Provenance | Pedigree | Linked to |
|---|---|---|---|---|---|
| Sodium nitrite (sodium-nitrite-1) feed:NANO2 flowsheet stream S1 (D-004) From stream S1 | 1.222 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (Sodium nitrite, dried, 99.0 wt-% (to bagging and storage), GLO) compatible: grade the input names sodium-nitrite only; sodium-nitrite (Sodium nitrite, dried, 99.0 wt-% (to bagging and 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 (nitrite generator) feed:PW1 flowsheet stream S2 (D-004) From stream S2 | 3.051 | kilogram | assumed | 4 4 1 3 3 | market for water, deionised (water, deionised, RoW) in your background (default ecoinvent-3.11-cutoff) |
| Sulfuric acid 98.5 wt% (sulfuric-acid-1) feed:ACID flowsheet stream S5 (D-004) From stream S5 | 0.8834 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Sulfuric acid from sulfur burning, double contact / double absorption (1000 t/d, 98.5 wt%) (Sulfuric acid 98.5 wt% to storage, GLO) compatible: grade the input names sulfuric-acid only; sulfuric-acid (Sulfuric acid 98.5 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 |
| Hydrazine hydrate 64 wt% N2H4 (hydrazine-1) feed:HH flowsheet stream S8 (D-004) From stream S8 | 0.8315 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a) (Hydrazine hydrate (64 wt% N2H4), GLO) compatible: grade the input names hydrazine only; hydrazine (Hydrazine hydrate (64 wt% N2H4)) is taken; unit kilogram; system model cutoff (one database); allocation mass (single-output); 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 S9 (D-004) From stream S9 | 1.287 | 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 sodium-hydroxide 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 (azide reactor) feed:PW2 flowsheet stream S10 (D-004) From stream S10 | 1.377 | kilogram | assumed | 4 4 1 3 3 | market for water, deionised (water, deionised, RoW) in your background (default ecoinvent-3.11-cutoff) |
| Methanol make-up (methanol-1) feed:MEOH flowsheet stream S22, the make-up of the methanol loop (D-009) From stream S22 | 0.07396 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Methanol synthesis loop and purification (2500 t/d Grade AA, natural-gas syngas) (Methanol Grade AA to storage, GLO) compatible: grade the input names methanol only; methanol (Methanol Grade AA to storage) is taken; unit kilogram; system model cutoff (one database); allocation exergy (deviation); boundary plant gate (pinned): no distribution or losses; the consumer's dataset counts its delivery |
| Electric power feed:POWER flowsheet energy streams P1-P4 (agitators, gas dispersion, vacuum pumps), D-012 electricity From streams P1, P2, P3, P4 | 0.1535 | 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) |
| LP steam 350 kPa(a) (still and filter-dryer) feed:LPS flowsheet energy streams Q3 (still boil-up) and Q7 (filter-dryer), D-012 steam, LP, 138.85 degC, 3.5 bar(a) From streams Q3, Q7 | 2.297 | kilowatt hour | assumed | 4 4 1 3 3 | Atlas: heat from steam, per kWh (Atlas unit proxy) (heat from steam, by energy, GLO) |
| Sodium sulfate liquor to wastewater treatment product:SULF flowsheet stream S6 (D-014) From stream S6 | 4.72 | kilogram | calculated | 3 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) |
| Evaporator condensate to wastewater treatment product:COND flowsheet stream S16 (D-007) From stream S16 | 2.781 | kilogram | calculated | 3 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) |
| Mother-liquor purge to azide destruction and wastewater treatment product:PURGE flowsheet stream S29 (D-016) From stream S29 | 0.08622 | kilogram | calculated | 3 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 |
| Azide reactor off-gas to the thermal oxidiser product:OFFGAS flowsheet stream S14 (D-005, D-013) From stream S14 | 0.1381 | kilogram | calculated | 3 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 |
| Chilled water return (R-101, R-102 and the methanol condensers) product:CHW flowsheet energy streams Q1 (R-101), Q2 (R-102), Q4 (methanol condenser) and Q8 (dryer condenser), D-012 cold, chilled water, 5 degC From streams Q1, Q2, Q4, Q8 | 2.081 | kilowatt hour | assumed | 4 4 1 3 3 | unlinked 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 |
| Cooling water return (still's water condenser and crystallizer) product:CW flowsheet energy streams Q5 (water-cut condenser) and Q6 (crystallizer), D-012 cold, 25 degC From streams Q5, Q6 | 1.984 | 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) |
| Nitrogen for inerting R-101 and R-102, breaking C-101's vacuum and the pressure filtrations of F-101 consumable:nitrogen 40 Nm3 per batch (vapour-space purges of R-101 and R-102 before the methyl nitrite, the vacuum of C-101 and F-101 broken, two filtrations at 200 kPa in F-101) x 1.2506 kg/Nm3, ASSUMED (D-013); 50 kg per batch x 652.6 batches in 7920 h (process/recipe.yaml, case design, bottleneck AZIDE) | 0.04865 | kilogram | assumed | 4 4 1 3 3 | Atlas (pinned): Cryogenic air separation unit (500 t/d GOX) (Nitrogen, gaseous, <= 10 ppm O2, 8 barg, GLO) compatible: grade the input names nitrogen only; nitrogen/gan-8barg-10ppm (Nitrogen, gaseous, <= 10 ppm O2, 8 barg) is taken; unit kilogram; system model cutoff (one database); allocation exergy (physical-exergy); boundary plant gate (pinned): no distribution or losses; the consumer's dataset counts its delivery |
Elementary flows
No elementary flows are exported for this activity (pass-through emissions and free inputs are left out, see the caveats).
The streams are the plant's own flows: an amount here is allocated and per 1 kilogram of Dried sodium azide to packing, 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/sodium-azide-1/lca/dataset.yaml in library version a3c52e4.
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 2.69TeR 3 · GeR 3 · TiR 1 · P 3.75 · 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:nitrogen (no composition)
- carbon balance not assessable: no composition for consumable:nitrogen (no composition)
- Change report
- Not available: this build has no change report against an earlier release.
KPI benchmark positions
| KPI | Value | Reference range | Position |
|---|---|---|---|
| Hydrazine hydrate (64 wt% N2H4) per kg of sodium azide | – kg/kg | 0.807 to 0.852 kg/kg | not evaluated |
| Azide reactor off-gas to treatment per kg of sodium azide No open source with the off-gas (unabsorbed methyl nitrite, N2O, NH3) of a sodium azide plant found (searched 2026-11-05: Google Patents US 5 208 002 A and US 5 098 597 A read, which name the nitrogen of side reactions but give no off-gas amounts; J. Studley, Scientific Update 2023, a secondary summary without figures). The dataset's off-gas follows from the methyl nitrite not absorbed in the patent's Example 1 balance and its ASSUMED side reaction (DESIGN.md D-004, D-005). | – kg/kg | not available | not evaluated |
How to use it
Downloads
- cheme-as-code-atlas-preview-a3c52e4.xlsx · bw2io ExcelImporter workbook (bw2io 0.9 Excel layout) · the whole databasecode sodium-azide-1:sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor:product:NAN3P
- cheme-as-code-atlas-preview-a3c52e4-olca-jsonld.zip · openLCA JSON-LD (olca-schema) (2) · the whole databaseprocess a1551f0b-c590-54e0-b1d5-9011b57e249f (processes/a1551f0b-c590-54e0-b1d5-9011b57e249f.json)
- cheme-as-code-atlas-preview-a3c52e4-multifunctional.json · Brightway 2.5 multifunctional database (JSON, for the multifunctional package) (cheme-as-code/lci-multifunctional/v1) · the whole databasecode sodium-azide-1:sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor:product:NAN3P
- 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-a3c52e4.xlsx", background="ecoinvent-3.11-cutoff", location="DE")
activity = bd.get_activity(("cheme-as-code-atlas-preview-a3c52e4", "sodium-azide-1:sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor:product:NAN3P"))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
Dried sodium azide to packing, from Sodium azide by the hydrazine / methyl nitrite route, batch, with precipitation from the reaction liquor (670 t/a) (dataset sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor 0.1.0), ChemE-as-Code Process Atlas LCI database preview-a3c52e4, activity sodium-azide-1:sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor:product:NAN3P. 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-a3c52e4.
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). ChemE-as-Code: An Open-Source Platform for Agentic AI in Chemical Engineering. arXiv:2611.07947. https://doi.org/10.48550/arXiv.2611.07947
BibTeX
@misc{schweidtmann_cheme_as_code,
author = {Schweidtmann, Artur M.},
title = {{ChemE-as-Code: An Open-Source Platform for Agentic AI in Chemical Engineering}},
year = {2026},
eprint = {2611.07947},
archivePrefix = {arXiv},
doi = {10.48550/arXiv.2611.07947},
url = {https://arxiv.org/abs/2611.07947}
}