01
Temperature and viscosity
Record both throughout the run; cooling can dominate pressure rise and gel risk.
Application guide
A technical approach to gelatin filter-media selection, staged clarification, temperature control, throughput and yield using cellulose depth pads and compatible cartridges.

Process requirements
Gelatin manufacture creates a demanding clarification duty because the process liquid can be warm, viscous and sensitive to yield loss. Suspended tissue, mineral residues, fines and process aids must be reduced without imposing excessive pressure drop or holding valuable gelatin within the media.
Successful gelatin filtration balances four objectives: visible clarity or turbidity, contaminant removal, acceptable throughput and product recovery. Temperature control is important because viscosity rises as gelatin solution cools, sharply increasing pressure drop and the tendency to gel within equipment.
Cellulose depth pads provide a tortuous, porous network that can retain a broad distribution of fine suspended matter and build a clarifying cake. They can be cut for sparkler presses or incorporated in lenticular modules. Their useful dirt capacity makes them practical after bulk solids removal and before finer polishing cartridges.
Process design
Screening, settling or a suitably open filter stage protects clarification media from coarse particles and fibres.
Pulp or cellulose pads capture suspended fines through sheet thickness. Sparkler filter pads suit installed horizontal plate equipment; lenticular modules provide an enclosed sheet format.
A compatible PP pleated cartridge may reduce the remaining particle burden and protect downstream processing. A nominal or absolute label must be supported by the required efficiency data.
Trend temperature, pressure, flow, turbidity or agreed clarity, cycle volume and recovered yield. Trial at representative concentration because water testing does not reproduce gelatin viscosity or solids behaviour.
Selection variables
01
Record both throughout the run; cooling can dominate pressure rise and gel risk.
02
Coarse fibres, fines and soft particles load depth media differently.
03
Define turbidity, visual standard or analytical particle criterion.
04
Measure hold-up, flush recovery and gelatin retained in spent media.
05
Request fibre furnish, alpha-cellulose and extractables information for the actual grade.
06
Define cleaning, contact and traceability requirements before approval.
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Technical questions
There is no universal value. Feed solids, viscosity, temperature, stage objective and rating method must be defined. A staged trial is more reliable than choosing from a nominal number.
Cooling and concentration can raise viscosity or start gel formation; a loaded cake or too-fine medium can compound the pressure rise.
Purity can be relevant to extractables and media consistency, but it does not independently define clarity. Request grade-specific alpha-cellulose data and test method.
Usually heavy solids should be reduced upstream. Sending unclarified gelatin directly to a fine pleated cartridge can produce short cycles and high cost.
Minimise unnecessary hold-up, size the system appropriately, optimise pre-wet/flush recovery and stop before gel blocks drainage—within the validated process.
Application support
Share feed quality, temperature, viscosity, solids, batch volume, existing equipment, desired result and required quality documents so an appropriate trial sequence can be proposed.