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
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
Bayer-route and precipitation-route aluminum hydroxide: particle engineering controls product value, washing governs sodium residuals, and spin-flash drying converts wet filter cake to powder –
Evaporation and concentration of lithium precipitation mother liquor recovers residual lithium, crystallizes sodium sulfate by-product, and returns clean condensate — the MVR-based route to
Battery-grade lithium carbonate plants built on MVR evaporation, hot precipitation crystallization, sodium sulfate by-product recovery and rotary drying – 30,000 TPA reference practice.
Ammonium sulfate recovery by MVR evaporation crystallization and neutralization: by-product sources, 1.6-2 mm large-particle crystallization, route selection, drying, and ZLD economics.
Sodium acetate crystallizes by cooling, not evaporation: supersaturation controlled through temperature, concentration, cooling rate and agitation, with continuous operation delivering pharma and food-grade consistency.
Evaporation and crystallization plants that turn copper sulfate liquors, etch solutions and smelter waste streams into pentahydrate crystal product, reusable water and recovered copper
MVR forced-circulation evaporation plus cooling crystallization recovers ammonium chloride from soda-ash coupling and rare-earth wastewater; steam rotary drying cuts cost by $15.57/t with 14.4
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.
