High-shear mixing / Lab-to-production transfer
A laboratory result stays attached to its formulation, preparation, mixer geometry, workhead, vessel or loop, working quantity, feed sequence, thermal history, air state, exposure history, sampling and method. Pilot and production equipment can change several of those conditions at once, so one matched number cannot establish equivalent processing.
Separate three transfer questions
Equal RPM, rotor tip speed or reported power per volume can describe one selected comparison field. None proves equivalent shear distribution, turnover, heat transfer, air incorporation, residence history or product result across different machines and scales.
Retain the controlled formulation, raw-material and preparation history, lab equipment and geometry, complete batch or loop path, operating timeline, sample identity, method, raw result, repeatability, deviations and bounded disposition. A result detached from those records is not a scale-up basis.
Compare rotor/stator or dispersing-element geometry, clearances, vessel and working level, bulk agitator, baffles, inline loop and pump, feed location, speed and power measurement points, cooling surface, control sequence, cleaning and site interfaces. Do not convert one similar field into equipment or process equivalence.
Predefine a representative trial, sampling and endpoint plan, hold and adjustment rules, retained-property checks, uncertainty, deviations, material disposition and change triggers. Assign buyer, formulation, laboratory, safety and candidate-supplier review owners before a commercial release decision.
Scale-up evidence register
The register allocates evidence; it does not calculate a scale-up ratio, select equipment or prescribe operating values. Each row stays tied to one formulation revision and one identified configuration at each scale.
Swipe or scroll horizontally to review every evidence column.
| Evidence item | Laboratory record | Pilot / changed-scale record | Production release record | Owner / disposition |
|---|---|---|---|---|
| Material and formulation identity | Formula revision, phase and raw-material lots, concentrations or solids basis, substitutions, preparation and hold history. | Every difference from the lab material, including lot, water quality, pre-phase preparation, hold and rework state. | Approved representative production material and traceable batch identity; no silent substitution. | Formulation owner, buyer quality owner and disposition of every difference. |
| Process objective and endpoint method | Required dispersion, emulsion or other bounded result; method, instrument, sample preparation, units, repeats and retained properties. | Same method basis or a documented method bridge with limitations and approval. | Raw production results, sample map, repeats, acceptance decision and separately owned downstream checks. | Method owner, acceptance owner and unresolved-method disposition. |
| Mixer, workhead and geometry identity | Named lab device, mixer type, rotor/stator or dispersing element, diameter, clearances, openings, mounting and revision. | Candidate geometry and every non-geometric similarity assumption recorded without claiming equivalence. | As-tested and as-proposed production equipment identity, drawings, revisions and deviations. | Candidate supplier, mechanical reviewer and configuration approver. |
| Vessel, loop and material-path topology | Vessel geometry, levels, baffles, bulk agitation, in-tank or inline path, pump, lines, return, bypass and heel. | Pilot inventory, turnover or pass route, source and return state, holds and boundary changes. | Production topology drawing with material balance, sampling points, controls and complete scope split. | Process, mechanical, controls and supplier interface owners. |
| Feed and addition sequence | Phase order, feed location, material state, timing record, addition-rate context and observed wetting or phase change. | Changed dosing equipment, feed point, line, sequence, duration or operator action and its trial disposition. | Approved production batch instruction inputs and evidence that the tested sequence matches the proposed route. | Formulation, operations, safety and supplier review owners. |
| Speed, tip-speed, power and torque basis | Actual speed record, relevant diameter, calculation basis, electrical or shaft measurement point, torque and included loads. | Each candidate quantity recalculated from its own geometry and measurement boundary; no equal-value equivalence claim. | Production measured values, instrument records, limits and variance tied to the accepted configuration and material state. | Drive, instrumentation, process and equipment-supplier reviewers. |
| Exposure, pass, turnover and time history | Clock events, mixer-on history, pass or turnover definition, sampling timeline, interruptions and holds. | Changed inventory, flow, circulation, residence distribution and control sequence stated without a universal conversion. | Raw production timeline and endpoint evidence; no fixed process time or exposure guarantee inferred. | Process owner, data owner and adjustment or stop authority. |
| Rheology, temperature, pressure and air state | Property method and sample history, temperature locations, pressure or vacuum state, foam and air observations. | Changed heat-transfer area, coolant, surface exposure, pumping, pressure, gas and phase behavior. | Production thermal and material-state history with alarms, deviations and separately evaluated product risks. | Formulation, thermal, mechanical, safety and quality owners. |
| Sampling, raw results and repeatability | Sample locations and times, preparation, instrument files, repeats, retained samples, uncertainty and rejected data. | Pilot sample map and method comparability, including missing locations and limits on interpretation. | Production raw records, repeatability, acceptance, retained samples and bounded claim wording. | Laboratory or measurement owner, quality reviewer and commercial claim owner. |
| Cleaning, safeguards, scope and change control | Wetted path, materials, seals, recovery, cleaning, guarding, controls, utilities, exclusions and trial safety record. | Changed wetted components, cleanability, controls, site interfaces and open hazards or evidence gaps. | Approved production scope, safeguards, cleaning release, deviations, handover and revalidation triggers. | Buyer and supplier process, mechanical, electrical, safety, quality and commercial owners. |
Scale-up decision route
These steps do not prescribe RPM, tip speed, power per volume, exponent, ratio, mixer time, geometry or an operating procedure. The responsible parties must define safe trial and production conditions for the actual material and equipment.
Lock the formulation and material preparation, complete equipment and vessel or loop identity, operating timeline, raw samples, methods, results, repeatability and limitations.
Compare lab, pilot and production geometry, topology, inventory, feeding, speed and power basis, circulation, heat path, air state, cleaning, controls and scope field by field.
Define material quantity and disposition, exact candidate configuration, safe operating envelope owners, sample map, methods, stop or adjustment rules, deviations and evidence handover before the run.
Approve the bounded result and commercial wording against raw evidence; reopen the review when formulation, geometry, route, control, site or acceptance conditions change.
High-shear mixer scale-up RFQ checklist
Unknowns stay open and assigned. Do not replace supplier evidence with a Silverson, EKATO or AIChE example, and do not infer a JINPIONEER mixer, laboratory, CFD, test, scale-up service or result.
Open the process briefControlled identity, phase regime, intended application, formula revision, formulation owner, quality owner and commercial decision owner.
Required bounded result, method, instrument, sample preparation, units, repeats, tolerance owner and properties that must remain separate.
Actual lab material quantity, density basis, vessel dimensions, level, headspace, heel and start/end inventory.
Proposed pilot inventory and geometry, minimum and maximum levels, reason for the intermediate scale and material disposition.
Production inventory or stream basis, campaign pattern, start-up, normal, transition, shutdown, hold and rework state.
Phase and lot identities, concentrations or solids basis, substitutions, premixes, conditioning, storage and hold history.
Order, physical form, feed point, dosing equipment, timing record, operator actions and observed wetting or phase change.
Property and method, instrument geometry or spindle, shear condition, sample temperature, conditioning, density and time dependence.
Named device and revision, mixer mechanism, rotor/stator or dispersing element, relevant dimensions, clearances, openings and mounting.
Named candidate, workhead, vessel or loop, auxiliaries, controls, wetted construction, evidence required, included scope and exclusions.
As-proposed machine and revision, complete geometry and material path, drawings, auxiliaries, controls, safeguards, scope and open evidence.
Dimensions, working levels, headspace, baffles, heating or cooling surfaces, bulk agitator and circulation responsibilities at each scale.
If applicable, source and return points, pump and drive, lines, valves, bypass, pressure state, instruments, holds and ownership.
Actual shaft or rotor speed, relevant diameter, units, calculation revision and reviewer for each scale; no inferred equivalence.
Motor input, drive output or shaft point, included loads, losses, measurement or calculation method, instrument and operating state.
If reported, exact numerator, denominator, working-volume basis, measurement boundary, averaging interval and limitation; no universal transfer rule.
Supplier-defined quantity, material path, clock events, flow or circulation basis, sampling timeline, holds, interruptions and uncertainty.
Temperature window and locations, heat-sensitive stages, coolant and surface boundary, pressure or vacuum, air, foam, gas and safeguards.
Locations and times, sample identity and preparation, instrument files, raw results, retained samples and rejected or missing data.
Repeat plan, method uncertainty, batch-to-batch variation, deviations, investigation, retest rule and limitation on conclusions.
Complete exposure path, material and elastomer evidence, seals, product recovery, drainability, cleaning method, inspection and changeover release.
Utilities, layout, access, guarding, interlocks, instruments, calibration, environmental and hazardous inputs, installation and responsible approvals.
Exact material and configuration, approved conditions, sample map, stop or adjustment authority, material disposition and evidence package.
Every scale-up assumption, buyer and supplier reviewer, open gap, bounded acceptance wording, handover owner and revalidation trigger.
Draft source record / Pending technical review
Reviewed on 2 August 2026. Silverson and EKATO describe their own equipment and service context; the AIChE proceeding describes one named emulsion study. Their methods, values, equipment and findings do not transfer to another supplier or project.
Buyer decision FAQ
No universal equivalence follows from equal RPM. Rotor or blade diameter, geometry, workhead, vessel or loop, material inventory, feed, bulk circulation, power and thermal conditions can all differ. Record the actual configuration and verify the proposed scale with representative material.
No. Tip speed is one calculated field. It does not by itself prove equal local or distributed shear, turnover, residence history, heat path, air incorporation, droplet or particle result, rheology, stability or production performance.
No. The numerator, denominator, measurement point, included loads, material state, averaging interval, geometry and flow path must be explicit. A matched reported value is not equipment, process or result equivalence.
The buyer and responsible technical parties should decide from the material risk, scale and configuration changes, available production evidence, material quantity, safety, uncertainty and consequence of failure. This page sets no universal pilot threshold.
No. Those sources describe named manufacturers' own context or one named study. Their equipment, services, setup, values, methods and findings do not transfer to JINPIONEER or another project.
No. It is an RFQ and evidence-allocation framework only. Equipment, engineering, laboratory, CFD, testing, scale-up, operating values, results, services, compliance and certification remain unconfirmed until project-specific supplier and buyer evidence is reviewed and approved.