Fines, solids and chemistry
Changed PSD, clay, concentration, temperature or reagents can reduce cake permeability.
BOYUN Industrial Filtration Solutions – Ceramic Vacuum Disc Filter
Troubleshoot high filter cake moisture by checking feed concentration, particle size, vacuum, disc speed, cake thickness, cloth condition and drying time.

A higher result can come from a real filtration change, a different sample, inconsistent laboratory method or a changed feed. Verify the measurement before adjusting the machine.
Changed PSD, clay, concentration, temperature or reagents can reduce cake permeability.
Low or unstable vacuum, flooding or leakage can shorten effective drying.
Disc speed, slurry level and valve zones determine the time available.
Stop the equipment and isolate all hazardous energy that can cause rotation, vacuum, pressure, stored mechanical movement, electrical energization or chemical exposure. Follow the site lockout and permit procedure; inspection and maintenance must be performed only by authorized personnel.
Change one controlled variable at a time and retain the before-and-after operating evidence.
Repeat sampling and laboratory method.
Review solids, PSD, chemistry and temperature.
Trend vacuum, filtrate and leakage indicators.
Assess blinding, damage, fit and cake release.
Change one approved setting and compare capacity too.
Use the same instruments, sampling points and laboratory method so changes can be compared.
More drying time can reduce throughput; thinner cake can affect release; higher vacuum demand can expose leakage or auxiliary limits.
| Finding | Review | Possible controlled response |
|---|---|---|
| Feed became finer or lower-solids | Upstream operation, sample data and test history. | Restore feed control or retest the changed duty. |
| Vacuum is below stable baseline | Leaks, valve, piping, receiver, pump and filtrate removal. | Repair the confirmed constraint before raising setpoints. |
| Media permeability declined | Deposit, wash coverage, damage and cloth age. | Apply approved cleaning or replace with verified media. |
| Drying time is too short | Disc speed, immersion and valve-zone relationship. | Trial an approved cycle change while tracking dry throughput. |
| Cake is too thick or uneven | Feed level, solids, agitation, formation and sector condition. | Stabilize feed and formation before optimizing moisture. |
Use related technical and service pages to resolve the underlying cause.
These answers support project preparation; the final recommendation depends on the actual duty.
Share the feed, throughput, operating target and site constraints. BOYUN will identify missing information and recommend testing, sizing or the appropriate equipment scope.