What process condition is fixed?
Name the product or approved substitute, density, rheology, solids or settling behavior, foaming, temperature, batch quantity, normal end level, agitator and internals state, and discharge start and end events.
Mixing tank / Bottom geometry and discharge
Bottom shape is only one part of a discharge route. The same material, batch, normal end level, outlet, valve, venting, downstream piping and test method must stay visible before recovered quantity, elapsed time or residual heel can be compared.
Separate four decisions
This route owns normal-discharge comparison under a fixed product and configuration. Working-volume definition, post-recovery cleaning, complete tank scope, agitator entry, FAT/SAT allocation and surface finish stay with their dedicated decision pages.
Name the product or approved substitute, density, rheology, solids or settling behavior, foaming, temperature, batch quantity, normal end level, agitator and internals state, and discharge start and end events.
Freeze the approved GA and sections, bottom form and datum, any slope or angle as a project field, outlet location and connection, valve orientation, venting, hose or piping elevation and length, and downstream backpressure.
Record elapsed time, recovered quantity and residual heel by named location, method and instrument. Preserve raw observations, repeatability, witness, substitutions and uncertainty rather than reducing the decision to the bottom label.
Assign buyer and supplier owners for drawings, process basis, test execution, deviation, retest and release. State which geometry, material and discharge route the conclusion covers and which changes reopen review.
Candidate comparison map
The rows organize questions and records. They do not rank the geometries or prescribe a slope, angle, outlet, valve, drain time or residual-heel target.
Swipe or scroll horizontally to review every evidence column.
| Candidate or interface | Fixed comparison context | Candidate-specific record | Approval boundary |
|---|---|---|---|
| Flat-bottom candidate | Same material, batch, temperature, end level, agitator state, outlet path and discharge start/end definition used for every candidate. | Controlled bottom section, datum, local low points, outlet relationship and as-built differences without assuming complete drainage. | Recovered quantity, residual-heel map, elapsed time, repeat runs, deviations and named release for this exact configuration only. |
| Sloped-bottom candidate | The common test basis remains fixed; slope direction and value are project fields rather than universal recommendations. | Controlled slope, high and low datums, outlet relationship, fabrication tolerance and installed orientation. | Candidate-specific raw observations and disposition; no result transfers from another slope, outlet or downstream arrangement. |
| Cone-bottom candidate | The common material and discharge boundary remains fixed; cone angle is recorded, not prescribed. | Controlled cone geometry, transition, outlet position, supports, clearances and as-built record. | Evidence is bounded to the tested cone, batch and line; no default recovery or drain-time advantage is assumed. |
| Dished-bottom candidate | The same batch, outlet, valve, vent and downstream conditions are retained wherever the comparison permits. | Controlled head profile, tangent and low-point datums, outlet relationship, fabrication state and installed orientation. | Observed recovery and heel record with explicit differences from the other candidates and named technical acceptance. |
| Outlet and valve interface | Outlet size, location, connection, valve type and orientation stay explicit rather than being hidden inside a bottom label. | Approved nozzle schedule, valve data, low-point relationship, internal projection, dead space and temporary test items. | As-designed, as-built and as-tested identities reconciled before any discharge result is compared. |
| Venting and downstream path | Venting state, hose or piping elevation and length, downstream equipment and backpressure are fixed or declared as differences. | Piping route, elevations, restrictions, open or closed boundaries, temporary connections and site interface record. | Result applicability stops at the named downstream boundary; changed line or pressure conditions reopen review. |
| Normal-discharge state | Start and end events, valve sequence, agitator and internals state, temperature and operator boundary are defined consistently. | Approved test or observation protocol with safe operating ownership and no improvised instruction from this guide. | Elapsed time is accepted only for the declared sequence and endpoint, not as a universal drain-time promise. |
| Recovered quantity and residual heel | One quantity basis, collection boundary, heel definition, location map, method and uncertainty are used across candidates. | Raw mass or volume observations, instrument identity, uncollected locations, repeatability and material-balance reconciliation. | Project acceptance or open gap is recorded without inventing a universal recovery percentage or residual-heel limit. |
Controlled project evidence
Named OEM material supports RFQ-field and geometry vocabulary only. The project-specific records below control any actual candidate comparison or acceptance.
Swipe or scroll horizontally to review every evidence column.
| Evidence item | Controlled source | Boundary to preserve | Result or discrepancy record | Owner and release |
|---|---|---|---|---|
| Approved GA, sections and nozzle schedule | Controlled vessel drawings showing bottom form, datums, slope or angle if applicable, outlet, nozzles, internals and revision. | As-quoted, as-designed, as-built and as-tested geometry kept distinct; orientation and temporary items identified. | Drawing match, redlines, dimensional differences and approved as-built correction. | Supplier drawing owner, buyer mechanical reviewer and document-control release. |
| Fixed material, batch and discharge brief | Approved product or substitute record, properties, temperature, batch quantity, normal end level and start/end events. | Density, rheology, solids, settling, foaming, agitator state and substitutions remain visible. | Actual batch observations, departures from the approved basis and applicability limits. | Buyer process owner, supplier reviewer, test lead and release authority. |
| Bottom, outlet and valve configuration record | Approved geometry, outlet size and connection, valve identity and orientation, low-point relationship and fabrication record. | Candidate-specific dimensions, internal projections, dead spaces, tolerances and installed state. | Inspection observations, configuration mismatch, correction and retest trigger. | Supplier mechanical and quality owners plus buyer reviewer. |
| Venting and downstream-interface record | Vent state and downstream hose, piping, elevation, length, restriction, receiving equipment and backpressure record. | Temporary factory route and installed site route separated; open, closed and pressurized boundaries named. | As-tested path, interface differences, pressure observations where approved and unresolved applicability gaps. | Buyer and supplier process, piping and site-interface owners. |
| Approved normal-discharge protocol | Contract or project protocol defining safe prerequisites, start/end events, sequence, instruments, collection and witness. | Exact vessel, material, batch, temperature, agitator state, valve sequence and downstream path. | Execution log, timing events, interruptions, substitutions and protocol deviations. | Test performer, safety owner, buyer witness and protocol approver. |
| Recovered-quantity and residual-heel record | Calibrated or verified mass or volume method, collection boundary, heel map, instrument identity and raw observations. | Quantity basis, uncollected locations, temperature, uncertainty, repeat runs and product versus water evidence separated. | Recovered quantity, mapped heel, elapsed time, material balance, variability and bounded result statement. | Test lead, metrology or quality owner, buyer reviewer and result approver. |
| Deviation, retest and change-control release | Numbered deviation, root review, corrective record, retest protocol, disposition and controlled change notice. | Changes to material, batch, geometry, outlet, valve, vent, downstream path, method or acceptance limit identified. | Accepted, rejected or open status with evidence reference and explicit applicability boundary. | Named technical, quality, commercial and buyer release authorities. |
Comparison route
This sequence allocates evidence; it is not an operating instruction. Approved supplier and site procedures, safeguards and responsible personnel govern any inspection or test.
Approve the material or substitute, properties, batch, temperature, normal end level, agitator state and discharge start and end events before comparing candidates.
Issue controlled sections and a nozzle schedule for the bottom, outlet, valve, vent and downstream route, keeping as-designed and as-built changes visible.
Define recovered quantity, residual heel, location map, elapsed-time events, instruments, collection boundary, uncertainty, repeats and witnesses.
Use only the approved safe protocol; retain actual material, configuration, timing, quantities, heel locations, interruptions, photographs if approved and deviations.
Reconcile candidate differences without transferring water behavior to product recovery, cleaning, mixing, hygiene or safety and without ranking geometry by name alone.
Record the accepted candidate or open gap, owners, evidence, exclusions and the material, geometry, valve, vent, line or method changes that trigger renewed review.
Tank-bottom discharge RFQ checklist
Unknown values remain open and assigned. Do not copy a competitor geometry, invent a JINPIONEER capability or treat a substitute-medium observation as proof of real-product recovery or cleanability.
Open the process briefExact material, substitute rationale, batch or lot identity and the owner who approves representativeness.
Measurement method, temperature, shear or time basis where relevant, solids distribution, settling and uncertainty.
Observed behavior and actual discharge temperature without extrapolating from water or a dissimilar liquid.
Mass or volume basis, declared level datum, normal end condition and link to the working-volume record.
Drawing numbers, revisions, orientation, datums, dimensions, bottom form, nozzles, internals and approval status.
Flat, sloped, cone or dished definition plus project-specific geometry fields and fabrication tolerances; no universal value assumed.
Centreline or invert, low-point relationship, internal projection, nominal and actual dimensions, connection and drawing reference.
Valve type, bore or restriction record, orientation, actuation, open state and any temporary factory substitution.
Open or closed state, vent path, restrictions, safeguards and responsible process or safety owner.
Elevation, length, diameter or restriction, fittings, receiving equipment, hold-up and as-tested versus installed differences.
Approved measurement point and observed condition where applicable, without turning the record into a pressure-design claim.
Stopped or operating status, approved sequence, baffles, coils, dip pipes, probes and other items affecting the path.
Named valve, pump or transfer event, timestamp rule, prerequisites and safe-procedure reference.
Defined collection, flow, level or other observable endpoint with no universal drain-time assumption.
Raw timestamps, interruptions, operator actions and sequence differences; use only inside the approved test boundary.
Mass or volume basis, collection boundary, instrument identity, calibration or verification, temperature and uncertainty.
Included locations, map, access method, measurement method, raw result and unmeasured or inaccessible areas.
Repeat-run plan, witness points, photographs if approved, raw observations, data custodian and variance review.
Numbered departures, corrective action, retest trigger, acceptance or rejection owner and remaining open items.
Buyer and supplier process, mechanical, quality, safety and commercial owners; bounded conclusion; separate cleaning, mixing, hygiene and safety decisions; changes that reopen review.
Draft source record / Pending technical review
Use these sources to identify fields worth controlling. The project drawings, process brief and raw discharge records remain the primary evidence for an actual decision.
Buyer decision FAQ
There is no default winner. Compare candidates with the same material, batch, temperature, end level, outlet, valve, venting, downstream path, discharge definition and measurement method, then approve the result within that exact boundary.
This guide publishes no universal slope or cone angle and does not promise complete drainage. Geometry, fabrication, orientation, material behavior, outlet and valve arrangement, venting and the downstream path all belong in the project-specific review.
No universal outlet location or size guarantees a result. The valve, restrictions, venting, material condition, downstream elevation and backpressure, start and end events and measurement method must be reviewed with the complete configuration.
No. A water observation is bounded to the as-tested geometry, medium, temperature, valve, vent, line, method and endpoints. It does not prove actual-product recovery, residual heel, cleanability, mixing, hygienic design or safety.
Keep them separate. Residual heel here is measured at the end of the defined normal product-recovery route. Cleaning starts after that boundary and needs its own chemistry, access, residue locations, method and release evidence.
No. It is an RFQ and evidence-allocation framework only. Geometry, slope or angle, outlet, valve, drawings, materials, pressure design, fabrication, testing, recovery, residual heel, drain time, cleaning, performance, suitability and services remain unconfirmed until project-specific supplier and buyer evidence is reviewed and approved.