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
Evaporation systems for starch sweetener plants: five-effect and MVR falling film trains from 10% to 77% solids, the chromatographic 60% DS interface, ion exchange
Plant protein and biological feed processing solutions: MVR falling film concentration of fermentation broths and protein liquors at 60-80C, viscosity and foaming control, and
Integrated vanillin concentration, crystallization and closed-loop nitrogen drying systems for solvent-wet, heat-sensitive aroma chemicals – with 5,000 TPA reference practice.
Engineering guide to continuous cooling crystallization of tartaric acid: solubility-driven staging, DTB/Oslo vessel selection, mother-liquor purge strategy, and the failure modes that decide product
Complete threonine broth downstream train: ceramic membrane clarification, multi-effect or MVR evaporation crystallization to 58-60% solids, two-stage centrifugation, and fluidized bed drying. Reference plants
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
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
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.
Evaporation and crystallization engineering for the three big fermentation products: lysine dual-route finishing, MSG vacuum pan crystallization, citric acid hydrate/anhydrous control, and MVR economics
Dry fractionation of coconut oil explained: feed conditioning at 60-70C, programmed cooling crystallization from 40C to 15-25C, membrane filter press separation of stearin and
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.
