Authorized and anonymized project references where each entry documents the feed characterization (TDS, COD, dominant salts), nameplate evaporation duty, configured process route (energy reuse × evaporator type × crystallizer type), and the specific process challenge that drove selection — not a gallery of nameplates. Where client confidentiality prevents full disclosure, only the process envelope and configuration family are published.
170+
Reference projects with documented feed, duty and process route
10
Industries served — chemical, battery, food, pharma and more
6+
Process route families: MVR, TVR, multi-effect, forced circulation, DTB, Oslo
Recover sellable sodium sulfate from chemical, pharma and fermentation wastewater: MVR forced-circulation crystallization at 28500 kg/h, or vacuum/freezing routes for hydrate control and waste
Falling-film MVR evaporation stations concentrate viscous beet juice into high-brix syrup with no live steam after start-up, and handle molasses alcohol wastewater and purified
MVR evaporation plus OSLO cooling crystallization for potassium nitrate: handling 10-15C boiling point elevation, chloride-grade materials, 20-40 mesh 99.9% crystals, and NaCl salt-out in
Sodium phosphate crystallization by hydrate: trisodium dodecahydrate cooling routes, the 73C phase boundary, evaporative routes for monosodium, and phosphorus recovery from wastewater.
Integrated BPA wastewater treatment with low-temperature MVR evaporation and crystallization: phenol recovery first, salt recovery second, reusable condensate and compliant solids for epoxy resin
Lecithin concentration and drying solutions from degumming to thin-film vacuum drying – capacities 3-150 t/d, four product grades, food-grade specs and the viscosity challenges
Crystallizing vitamin C (ascorbic acid) from concentrated fermentation-purification liquor is a crystal-size and stability problem: the product oxidizes in the presence of heat, air
Convert by-product hydrochloric acid from soda ash, chlor-alkali and polysilicon plants into saleable calcium chloride: neutralization, forced circulation evaporation, dihydrate flake or anhydrous granule
Tryptophan fermentation finishing: chromatographic purification, deamination with ammonia water recovery, and dilute-feed (2.8-3 g/100mL) evaporation crystallization to a 58-60% slurry, centrifugation and drying.
Hybrid CaCl2 concentration: MVR below ~35%, multi-effect forced circulation to 55-60%, single-effect falling film finisher to 68%+ for flake and granule production. Proven on
Evidence constraint. Only authorized or anonymized project information is displayed on this page. Process parameters cited (TDS, COD, throughput, particle size distribution, steam economy) are bounded by documented operating conditions and should not be extrapolated to other feed compositions, capacities or utility profiles without project-specific re-validation.
Send your feed characterization (TDS, COD, main salts, viscosity), throughput and product targets — we respond with a preliminary process route within two business days.
