utility
Wastewater
Wastewater sent to treatment (kg; 1 m3 = 1000 kg); the treatment service of processes/utility-wwtp.
Made by
- Wastewater treatment, activated sludgeMain productConcept · not reviewed
Used by
- Wastewater treatment, activated sludgeFeedstockConcept · not reviewed
Emitted by
- Acetaldehyde by the one-stage Wacker oxidation of ethylene (100 kt/a)WasteConcept · not reviewed
- Acetic anhydride by the ketene route (acetic acid cracking, 50 kt/a, concept)WasteConcept · not reviewed
- Acetone and phenol from cumene (cumene hydroperoxide route, 200 kt/a phenol)WasteConcept · not reviewed
- Acetylene by partial oxidation of natural gas with NMP recovery (6.25 t/h, synthesis-gas co-product)WasteConcept · not reviewed
- Ammonia from natural gas (1500 t/d, steam reforming with air-fed secondary reformer, Haber-Bosch loop)WasteConcept · not reviewed
- Aniline by adiabatic gas-phase hydrogenation of nitrobenzene (25 t/h)WasteConcept · not reviewed
- Bromine from bromide brine by chlorine oxidation and steaming-out (Smackover-type brine)WasteConcept · not reviewed
- Chlor-alkali by membrane-cell electrolysis (100 kt/a Cl2, 50 wt-% caustic soda, hydrogen)WasteConcept · not reviewed
- Ethanol by direct hydration of ethylene (100 000 t/a anhydrous, phosphoric acid catalyst)WasteConcept · not reviewed
- Ethylbenzene by liquid-phase zeolite alkylation of benzene with ethyleneWasteConcept · not reviewed
- Ethylene and propylene by ethane steam cracking (1000 kt/a ethylene, concept)WasteConcept · not reviewed
- Ethylene glycol by ethylene oxide hydration (glycols-only EO/EG plant, 1200 t/d MEG)WasteConcept · not reviewed
- Refined glycerol (USP) from biodiesel crude glycerol (10 000 t/a, concept)WasteConcept · not reviewed
- Hydrazine hydrate by the peroxide process (PCUK, methyl ethyl ketazine route, 16 kt/a)WasteConcept · not reviewed
- Hydrogen peroxide by the anthraquinone autoxidation process (50 kt/a H2O2, 50 wt%)WasteConcept · not reviewed
- Iodine from natural iodide brine by chlorine oxidation, air blowing-out and SO2 absorption (1000 t/a)WasteConcept · not reviewed
- Isobutene by MTBE cracking (50 kt/a, gas-phase cleavage)WasteConcept · not reviewed
- Bleached softwood kraft pulp with chemical recovery (1000 ADt/d market pulp, concept)WasteConcept · not reviewed
- Methylamines (MMA, DMA, TMA) from methanol and ammoniaWasteConcept · level Balanced · not reviewedEvidence outdated
- N-Bromosuccinimide by semi-batch bromination of succinimide in aqueous NaOH (500 t/a)WasteConcept · not reviewed
- Phosgene from CO and chlorine over activated carbon (17.3 t/h liquid phosgene, captive)WasteConcept · not reviewed
- Phosphorus oxychloride from white phosphorus, chlorine and oxygen via PCl3 (4.0 t/h)WasteConcept · not reviewed
- Potassium permanganate from MnO2 ore by KOH roasting and electrolysis (1250 kg/h, concept)WasteConcept · not reviewed
- Soda ash by the Solvay ammonia-soda process (1000 t/d light ash, concept)WasteConcept · not reviewed
- Solid sodium cyanide from Andrussow HCN (6.25 t/h, 50 kt/a)WasteConcept · not reviewed
- Styrene by adiabatic catalytic dehydrogenation of ethylbenzeneWasteConcept · not reviewed
- Tetrahydrofuran from 1,4-butanediol (50 kt/a, cyclodehydration and pressure-swing distillation)WasteConcept · not reviewed
- Thionyl chloride from sulfur, chlorine and SO2 over activated carbon (3.75 t/h)WasteConcept · not reviewed
- Cooling water, evaporative cooling tower, 25/35 degCWasteConcept · not reviewed
- Instrument air, dried, 8 bar(a)WasteConcept · not reviewed
- Steam generation, natural-gas boiler, saturated 11 bar(a)WasteConcept · not reviewed
Routes compared
One route in the Atlas makes Wastewater: nothing to compare yet. A comparison appears when a second route is added.
Per 1 kg of Wastewater: inventory from each route's LCI dataset, unallocated; footprints per the functional unit of their own LCA.
| Route | Tier, design maturity, review status | Geography, year | Energy | Feedstocks | Key emissions | Footprint | Comparability |
|---|---|---|---|---|---|---|---|
| Wastewater treatment, activated sludgeactivated sludge, fine-bubble aeration | Tier 1 (sourced conceptual)Design maturity: Concept (research)Not independently reviewedDataset review: unreviewed | GLO, 2026 |
|
|
| no footprint | – |
ISO 14044 requires a critical review (by a panel of interested parties, ISO/TS 14071) of a comparative assertion intended to be disclosed to the public. These routes are listed side by side for screening; a statement that one is better than another needs that review. None of these routes has had such a review.