Sodium nitrite, dried, 99.0 wt-% (to bagging and storage)

Activity Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion), GLO: the inventory of 1 kilogram of its reference product, attributional, cut-off.

Calculation maturity: not assessed Design maturity: Concept (research)Not independently reviewedsodium-nitrite-1:sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product:product:NANO2PreliminaryReport 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 nitrite from ammonia oxidation and soda absorption (2.5 t/h NaNO2, NaNO3 co-product), case design, derived from the flowsheet by cheme assess lca.

Reference product
1 kilogram of Sodium nitrite, dried, 99.0 wt-% (to bagging and storage) (1.013 bar(a), 50 degC, 99.0184 % NaNO2 (mass))
Chemical
sodium-nitrite
CAS
7632-00-0
Code
sodium-nitrite-1:sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product:product:NANO2
Dataset
sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product version 0.1.0 · UUID 7f7b99d9-16ba-5d5f-9e5b-4e5533be418a
Activity UUID
not available (the library assigns none; use the code)
Database
cheme-as-code-atlas-preview-c3ab348 (version preview-c3ab348)
Process
Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion)
Geography
GLO · background inputs with a site rule link at the user's site location (default DE)
Time period
2026 · valid until 2031
Technology
Ammonia oxidation over Pt/Rh gauze near atmospheric pressure with waste heat boiler, NOx absorption in 20 wt-% soda solution, double-effect evaporation, NaNO2 vacuum crystallisation, centrifuging and drying, inversion of the mother-liquor purge with 60 wt-% nitric acid to sodium nitrate; 20 kt/a NaNO2 · level current
Boundary
gate-to-gate foreground of the plant
Production volume
20,000,000 kg/a (product:NANO2 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
shares, 86.2 % of the dataset to this product (rule deviation, from study)
Economic allocation would follow the library hierarchy for two material co-products of unequal value, but no open price basis for either salt was found in this run; mass is used until prices are sourced (open input, DESIGN.md D-013).
Rights
CC-BY-4.0: the ChemE-as-Code process library's own concept design (LICENSE-DATA)

Exchanges per 1 kilogram of Sodium nitrite, dried, 99.0 wt-% (to bagging and storage)

As exported: allocated and scaled to the reference product. Provenance: 12 assumed. Pedigree scores (1 best, 5 worst): reliability, completeness, temporal correlation, geographical correlation, further technological correlation.

Preliminary1 exchange is not yet linked to a background dataset. It counts no burden, so the inventory is incomplete: do not read a result from it as complete.
InputAmountUnitProvenancePedigreeLinked to
Liquid ammonia from ammonia-1 (battery limit, 1600 kPa(a))
feed:NH3
S1, D-004
From stream S1
0.2346kilogramassumed4 4 1 3 3Atlas (pinned): Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop) (Liquid ammonia product (refrigerated, to the battery limit), NL)
compatible: grade the input names no chemical only; ammonia (Liquid ammonia product (refrigerated, to the battery limit)) 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
Soda ash, dense, from soda-ash-1
feed:SODA
S6, D-004
From stream S6
0.7465kilogramassumed4 4 1 3 3market for soda ash, dense (soda ash, dense, GLO) in your background (default ecoinvent-3.11-cutoff)
Nitric acid 60 wt-% from nitric-acid-1
feed:HNO3
S20, D-004, D-009
From stream S20
0.0826kilogramassumed4 4 1 3 3Atlas (pinned): Weak nitric acid by dual-pressure ammonia oxidation (1000 t/d HNO3 as 60 wt% acid) (Weak nitric acid 60 wt% to storage, GLO)
compatible: grade the input names no chemical only; nitric-acid (Weak nitric acid 60 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
Electric power (AC, grid)
feed:POWER
Q3, Q5, Q8, Q10, Q12, Q13, Q16, Q18; D-011
electricity
From streams Q3, Q5, Q8, Q10, Q12, Q13, Q16, Q18
0.06488kilowatt hourassumed4 4 1 3 3market for electricity, medium voltage (electricity, medium voltage, DE, site location) in your background (default ecoinvent-3.11-cutoff)
Low-pressure steam 450 kPa(a) from the site header
feed:LPS
Q2, Q6, Q11, Q14, Q17; D-010
steam, LP, 147.65 degC, 4.5 bar(a)
From streams Q2, Q6, Q11, Q14, Q17
0.6877kilowatt hourassumed4 4 1 3 3Atlas: heat from steam, per kWh (Atlas unit proxy) (heat from steam, by energy, GLO)
Surplus process condensate to the site water system
product:COND
S14, S24; D-008
From streams S14, S24
0.2667kilogramassumed4 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
Q4, Q7, Q9, Q15; D-010
cold, 25 degC
From streams Q4, Q7, Q9, Q15
1.919kilowatt 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)

Elementary flows

FlowDirectionCompartmentAmountUnitProvenancePedigree
Carbon dioxide, fossil
349b29d1-3e58-4c66-98b9-9d1a076efd2e
From stream S10
emissionair0.3098kilogramassumed4 4 1 3 3
Dinitrogen monoxide
20185046-64bb-4c09-a8e7-e8a9e144ca98
From stream S10
emissionair0.004244kilogramassumed4 4 1 3 3
Ammonia
87883a4e-1e3e-4c9d-90c0-f1bea36f8014
From stream S10
emissionair0kilogramassumed4 4 1 3 3
Nitric oxide
17f7e776-7934-54af-8c3c-ed0247cb697b
From stream S10
emissionair0.002115kilogramassumed4 4 1 3 3
Nitrogen oxides
c1b91234-6f24-417b-8309-46111d09c457
From stream S10
emissionair0kilogramassumed4 4 1 3 3

The streams are the plant's own flows: an amount here is allocated and per 1 kilogram of Sodium nitrite, dried, 99.0 wt-% (to bagging and 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/sodium-nitrite-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 2.75
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: 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 database
    code sodium-nitrite-1:sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product:product:NANO2
  • cheme-as-code-atlas-preview-c3ab348-olca-jsonld.zip · openLCA JSON-LD (olca-schema) (2) · the whole database
    process 7f7b99d9-16ba-5d5f-9e5b-4e5533be418a (processes/7f7b99d9-16ba-5d5f-9e5b-4e5533be418a.json) · the dataset's unallocated multi-output process; this product's allocation factor is in it
  • 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 database
    code sodium-nitrite-1:sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product · the dataset unallocated, with all its products; this product is its desired_code
  • 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", "sodium-nitrite-1:sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product:product:NANO2"))

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

Sodium nitrite, dried, 99.0 wt-% (to bagging and storage), from Sodium nitrite from ammonia oxidation and soda absorption (with sodium nitrate by inversion) (dataset sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product 0.1.0), ChemE-as-Code Process Atlas LCI database preview-c3ab348, activity sodium-nitrite-1:sodium-nitrite-from-ammonia-oxidation-and-soda-absorption-2.5-t-h-nano2-nano3-co-product:product:NANO2. 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}
}