Portfolio Demo This is a sample website, not an equipment supplier.

Compare the process routes

Industrial Drying Equipment

Choose a starting point from the feed form, operating mode and process limits—not from an equipment name alone. This portfolio demo compares three common drying routes and shows the project data a real supplier would need before making a recommendation.

01 / Side-by-side review

Start With the Material You Have

The examples below define a discussion path. They are not commercial models or a final process selection.

Scroll the table to compare every column. Testing and supplier review are required.

Three candidate dryer types · Portfolio Demo comparison
Decision pointCentrifugal Spray DryerFluid Bed DryerDouble Cone Vacuum Dryer
Feed formPumpable liquid or slurryWet particles that can fluidizeSolids that can tumble in a batch
Operating mode in this demoContinuousContinuous; batch arrangements also exist and need separate reviewBatch
Capacity basisFeed, evaporation and powder output in kg/hWet feed and dried output in kg/hWorking volume in L and wet load in kg/batch; no kg/h without a cycle time
Core inputsSolids, viscosity and powder targetParticle distribution, bulk density and moistureBatch load, bulk density and liquid to remove
Trial questionsAtomization, heat response and powder recoveryFluidization, stickiness and particle breakageHeat response, tumbling, discharge and solvent handling
Review pageExplore spray drying →Explore fluid bed drying →Explore vacuum drying →

Selection boundary These three types do not cover every drying duty. A paste, sticky sludge, large wet lump or feed with an unresolved hazard may need another process.

02 / Feed form

The First Question Is Physical Form

Can the feed be pumped and atomized?

A spray dryer can be a useful starting point for a stable liquid or slurry. Record solids content and viscosity at a stated temperature. Settling, abrasion or rapid thickening can change pumping and atomization. The required powder moisture, particle size and recovery also belong in the first review.

Review the centrifugal spray dryer →

Can wet particles form a moving bed?

A fluid bed depends on air moving through the particles. Share the full particle-size range, not only an average. Bulk density, moisture, stickiness and fragility affect fluidization and retention time. Very fine, cohesive or easily damaged particles may require trials or a different arrangement.

Review the fluid bed dryer →

Can solids tumble as a batch?

A double cone vacuum dryer is a batch starting point for solids that can move as the vessel rotates. Define wet load, bulk density, working volume and the liquid to remove. Discharge behaviour, product heat limits, solvent properties and cleaning requirements must be reviewed together.

Review the double cone vacuum dryer →

03 / Operating mode

Separate Continuous Rate From Batch Load

Continuous duties

Spray and continuous fluid bed examples use kg/h, but the basis must be named. Feed rate is not the same as dry product output. Moisture removal, solids retention and expected losses change the result. State operating hours, turndown and upstream feed variation.

Batch duties

Vacuum examples use litres of working volume and kilograms per batch. A batch size does not become kg/h until filling, heating, drying, cooling, sampling and discharge time are known. State the expected cycle and identify which steps are included.

04 / Process limits

“Heat-Sensitive” Is a Starting Point, Not a Selection

Provide a measurable product limit and the method used to assess damage. Short exposure in a spray dryer may suit one material, while reduced pressure in a vacuum dryer may help another. Neither statement guarantees a result. Fluid beds can provide controlled particle drying, but product temperature, residence time and air conditions still need agreement.

Also identify solvents, dust behaviour, oxygen sensitivity, corrosion, contamination limits and cleaning needs. Those inputs affect process safety, materials of construction, exhaust treatment and the test plan. This demo does not claim explosion protection, hygienic construction, containment or certification.

05 / Prepare a useful review

Bring Comparable Project Data

Material and liquid
Composition, water or solvent, feed form, safety data and any known corrosion concerns.
Capacity and moisture
kg/h or kg/batch with units, initial and target moisture, moisture basis and expected operating hours.
Product limits
Maximum product temperature, particle target, acceptable breakage, recovery needs and quality checks.
Site and scope
Utilities, layout limits, cleaning, emissions, documentation and responsibility boundaries.

Use measured values when possible and mark assumptions clearly. Write “Unknown” for missing information instead of inventing a number. A real supplier can then identify the gaps, propose a representative test and state what can—or cannot—be confirmed.

06 / Detailed page demos

Continue With a Candidate Process

Liquid or slurry

Centrifugal Spray Dryer

Review sample mass balances, atomization inputs, powder recovery questions and a process-specific RFQ checklist.

Open the spray dryer page

Wet particles

Fluid Bed Dryer

Review fluidization, particle distribution, air conditions, abrasion risks and continuous moisture-balance examples.

Open the fluid bed page

Batch solids

Double Cone Vacuum Dryer

Review volume and load, absolute pressure, heat and solvent questions, tumbling behaviour and batch acceptance.

Open the vacuum dryer page

Not sure which dryer fits?

Prepare the Unknowns for Review

Try the local RFQ workflow with sample details. It does not send an enquiry.

Not sure which dryer fits?
Request a Quote