الطرد المركزي للدليل

Cake-Washing Pusher Centrifuge for Copper Sulfate Dewatering Description Cake-Washing Pusher Centrifuge for Copper Sulfate Crystal Dewatering is designed for continuous dewatering, mother liquor separation, and cake washing of copper sulfate crystals in chemical crystallization and copper salt production lines. Copper sulfate crystals, especially copper sulfate pentahydrate, are usually produced through crystallization, evaporation concentration, cooling crystallization, or

Moisture-Control Pusher Centrifuge for Calcium Chloride Dewatering Description Moisture-Control Pusher Centrifuge for Calcium Chloride Crystal Dewatering is designed for continuous dewatering and brine separation of calcium chloride crystals in inorganic chemical and salt processing lines. Calcium chloride is highly hygroscopic. After crystallization or brine concentration, calcium chloride crystals may carry concentrated mother liquor, residual brine, and surface moisture.

Salt-Recovery Pusher Centrifuge for Glyphosate Desalination Description Salt-Recovery Pusher Centrifuge for Glyphosate Desalination is designed for continuous dewatering and separation of crystallized inorganic salts from glyphosate mother liquor desalination systems. In glyphosate production or post-treatment processes, process liquor may contain high concentrations of dissolved salts, residual organics, mother liquor, and crystallized salt slurry after evaporation or

Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering Description Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering is designed for continuous dewatering and mother liquor separation of soda ash crystals, sodium carbonate crystals, and soda ash-related crystalline slurry in chemical production lines. In soda ash production or sodium carbonate crystallization processes, the crystal slurry usually contains soda ash solids, alkaline mother liquor, dissolved salts

Safety-Control Pusher Centrifuge for Nitrate Crystal Dewatering Description Pusher Centrifuge for Nitrate Crystal Dewatering is designed for continuous solid-liquid separation, mother liquor removal, and optional cake washing of nitrate crystals in inorganic chemical and crystallization production lines. Nitrate crystal slurry may come from evaporation crystallization, cooling crystallization, reaction crystallization, or salt recovery systems. The slurry usually contains

Heavy-Duty Pusher Centrifuge for Mineral Salt Dewatering Description Heavy-Duty Pusher Centrifuge for Mineral Salt Dewatering is designed for continuous solid-liquidseparation of mineral salt crystals, salt lake crystallization products, brine-derived salts, andinorganic salt mixtures. In mineral salt recovery, salt lake brine processing, mining brine treatment, and evaporationcrystallization systems, the discharged slurry may contain mineral salt crystals, mother liquor,

Safety-Interlocked Pusher Centrifuge for Wet Nitrocotton Dehydration Description Safety-Interlocked Pusher Centrifuge for Wet Nitrocotton Dehydration is designed for controlled liquid removal from wet nitrocotton / wet nitrocellulose cake under strictly evaluated process conditions. In nitrocotton production and post-treatment processes, the wet material may contain nitrocellulose fibers, water, wetting liquid, residual process liquor, and fine fibrous solids. The centrifuge

Wear-Resistant Pusher Centrifuge for Potassium Chloride Dewatering Description Wear-Resistant Pusher Centrifuge for Potassium Chloride Crystal Dewatering is designed for continuous dewatering and mother liquor separation of potassium chloride crystals in potash, fertilizer, mineral salt, and chemical production lines. Potassium chloride crystal slurry may come from crystallization, flotation, washing, brine concentration, or potash processing systems. The slurry usually

Horizontal Perforated Basket Centrifuge / Continuous Pusher Centrifuge Intruduction Pusher centrifuge is a type of horizontal, spiral discharging filtrating equipment with continuous operation. With the drum and the helix rotating in the same direction at high speed difference, the material is continuously led, via the feeding pipe, into the inner cylinder of the spiral feeder and, after acceleration, enters the drum. Under the action of the centrifugal force field, the