ファスナー・冷間圧造
Phosphate coating residue, iron fines and sludge in cold heading oil.
Cold heading oil filtration →Start with your industry, fluid and solids problem. Compare published application guides, then confirm flow, temperature, sump volume and discharge method before choosing a centrifuge.
Each guide starts with the contamination generated by the process, explains the operating consequences, and identifies the information needed for model selection. Choose the nearest application even if your exact machine type is not listed.
Phosphate coating residue, iron fines and sludge in cold heading oil.
Cold heading oil filtration →Metal fines and lubricant condition in aluminium, copper and steel wire drawing circuits.
Wire drawing filtration →Mill scale, metallic solids and recirculating oil in rolling and tube-processing systems.
Rolling mill oil filtration →Sapphire lapping slurry, diamond abrasive and process stability in precision finishing.
Sapphire slurry recovery →Fine metallic contamination in CNC, grinding and shared coolant circuits.
Grinding coolant filtration →Industry names alone do not determine separation performance. Particle density and size distribution, fluid viscosity, temperature, solids generation and the required result all affect whether centrifugal separation is appropriate.
Review the general guide when small chips or metallic fines block nozzles, settle slowly, or recirculate through the machine.
Fines removal from coolant →Start with the fastener application when phosphate coating residue and iron fines build sludge in neat oil.
Review cold heading conditions →Use the grinding guide for fine metallic contamination, surface-quality concerns and sump turnover questions.
Review grinding coolant →Use the sapphire guide when recovery decisions must balance abrasive value, slurry consistency and product quality.
Review slurry recovery →A coolant centrifuge is not a universal substitute for every filter. Some processes use centrifugal separation as a primary solids-removal step; others require a polishing filter, oil skimmer, magnetic separator or fluid-condition control alongside it.
The application determines not only the centrifuge size but also how collected solids should leave the system. Base the decision on continuity, solids per shift, safe access and available operator time.
Use the automatic series as the starting point when the line should continue operating while the centrifuge manages repeated solids discharge cycles.
View automatic discharge series →Use the VC-30 series when a compact circuit has a manageable solids load and the separator can be stopped, isolated and cleaned at a planned interval.
View manual discharge series →These models are useful reference points, not automatic recommendations. Final selection still depends on fluid properties, contamination, required turnover, solids capacity and installation conditions.
A starting point for a single machine or compact circuit where high centrifugal force is the main selection direction.
固体の容量A starting point for multiple machines or a central sump where circulation flow and greater solids capacity are the priority.
複数台の機械 / 中央サンプNominal flow is a model rating, not a guaranteed commissioned flow for every liquid. Confirm viscosity, temperature, pipe loss and the separation target before ordering.
Identify neat oil, water-miscible coolant, slurry or another process fluid, including concentration where relevant.
Describe the contaminant and estimate solids generated per shift or current cleaning interval.
Provide current pump flow, number of machines, sump volume and desired turnover.
Temperature changes viscosity and may determine the required machine configuration.
Confirm whether manual cleaning can fit production or automatic discharge is required.
Confirm footprint, service access, electrical supply and how separated fluid returns to the sump.
Send your fluid, contaminant, flow, sump volume, temperature and operating schedule. We will identify the closest published application and the next sizing step.