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.

Calculation maturity: not assessed Design maturity: Concept (research)Not independently reviewedsodium-azide-1:sodium-azide-by-the-hydrazine-methyl-nitrite-route-batch-with-precipitation-from-the-reaction-liquor:product:NAN3PPreliminaryReport 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 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.

Preliminary3 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
Sodium nitrite (sodium-nitrite-1)
feed:NANO2
flowsheet stream S1 (D-004)
From stream S1
1.222kilogramassumed4 4 1 3 3Atlas (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
3.051kilogramassumed4 4 1 3 3market 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
0.8834kilogramassumed4 4 1 3 3Atlas (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
0.8315kilogramassumed4 4 1 3 3Atlas (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
1.287kilogramassumed4 4 1 3 3Atlas (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
1.377kilogramassumed4 4 1 3 3market 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
0.07396kilogramassumed4 4 1 3 3Atlas (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
0.1535kilowatt 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) (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
2.297kilowatt hourassumed4 4 1 3 3Atlas: 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
4.72kilogramcalculated3 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)
Evaporator condensate to wastewater treatment
product:COND
flowsheet stream S16 (D-007)
From stream S16
2.781kilogramcalculated3 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)
Mother-liquor purge to azide destruction and wastewater treatment
product:PURGE
flowsheet stream S29 (D-016)
From stream S29
0.08622kilogramcalculated3 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
Azide reactor off-gas to the thermal oxidiser
product:OFFGAS
flowsheet stream S14 (D-005, D-013)
From stream S14
0.1381kilogramcalculated3 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
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
2.081kilowatt 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
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
1.984kilowatt 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)
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)
0.04865kilogramassumed4 4 1 3 3Atlas (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 2.69
TeR 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

KPIValueReference rangePosition
Hydrazine hydrate (64 wt% N2H4) per kg of sodium azide– kg/kg0.807 to 0.852 kg/kgnot 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/kgnot availablenot evaluated

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-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}
}