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
Calcium chloride concentration and anhydrous granulation from soda ash distiller waste – high boiling-point-rise evaporation, spray granulation, 600,000 TPA reference practice.
Continuous cooling crystallization purifies hydroquinone: isomer separation from catechol, oxidation color control, four critical process control points, and photographic-grade polishing routes.
KCl purification by MVR forced-circulation evaporation and DTB crystallization: 34% hot dissolution, BaCl2/EDTA purification, 1.5-2.0% supersaturation control, 0.2-1.5 mm Class I premium potash product.
Two-stage fractional crystallization separates NaCl from KCl in mixed chloride brines: evaporation recovers 96-98% pure sodium chloride, flash cooling recovers potassium chloride, and an
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
MVR/TVR evaporation and controlled crystallization systems for allulose (D-psicose) plants: concentrating chromatography eluate, protecting heat-sensitive rare sugar quality, and delivering uniform crystals at 50-100
Integrated thin stillage evaporation, DDGS drying and condensate-to-biogas solutions for ethanol plants – process chain, MVR vs multi-effect selection and the numbers that decide
Denim mills close their water loops with a biological-plus-membrane architecture whose published benchmarks come from two sites of one group: a Shunde, China mill
For coal chemical brines where sodium chloride and calcium chloride coexist, scaling control in the falling-film evaporator is not a cleaning-schedule question – it
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.
