How to Evaluate Screw Pump Vendor Quotations - TBE Guide

Complete technical bid evaluation guide for screw pumps including scoring methodology, critical parameters, common deviations, and red flags for Equipment Engineers.

API 676

TBE Evaluation Categories

Weighted Scoring Matrix

CategoryWeightKey Evaluation Points
Technical Compliance40-50%Flow, pressure, viscosity range
Performance Verification15-20%Curves, efficiency, slip
Materials of Construction15%Chemical compatibility
Vendor Experience10%References, track record
Delivery Schedule10%Project alignment
Documentation Quality5-10%Completeness, clarity

Technical Compliance Evaluation

Flow and Pressure

ParameterWhat to VerifyAcceptance
Rated flowMeets specification±3% tolerance
Differential pressureAt rated flow≥ specified
Maximum pressureRelief valve setting≤ 110% operating
Flow tolerancePer ISO/DIN±3% typical

Viscosity Verification

ConditionCheckWhy Critical
Operating viscosityPump efficient at thisNormal operation
Maximum viscosityCan start/runCold start
Minimum viscositySlip acceptableHot operation
Temperature rangeFull range coveredAll conditions

Critical Check:

Cold Start Verification:
- Viscosity at minimum ambient temperature: ___ cSt
- Motor torque adequate for cold start? □ Yes □ No
- Soft start or VFD required? □ Yes □ No

Slip and Efficiency

ParameterTargetRed Flag
Slip at rated< 5-10%> 15%
Volumetric efficiency> 85%< 80%
Overall efficiency> 70%< 60%

Performance Curve Review

Required Curves

CurvePurposeMust Show
Flow vs SpeedCapacity verificationLinear relationship
Flow at multiple viscositiesRange verificationFull viscosity range
Power vs FlowMotor sizingAt worst case
NPSHr vs SpeedSuction verificationIf applicable

Curve Analysis Checklist

□ Curves provided at specified viscosity
□ Rated point clearly marked
□ Operating range within capability
□ Power curve shows motor margin
□ Slip characteristic provided
□ Efficiency stated at rated point

Warning Signs in Curves

IssueRiskAction
Curves at different viscosityPerformance uncertaintyRequest correct viscosity
Non-linear flow vs speedDesign problemInvestigate
Power exceeds motor ratingMotor failureReselect motor
No NPSHr dataCavitation riskRequest data

Materials Evaluation

Wetted Parts Verification

ComponentRequiredOfferedCompatible?
Casing______□ Yes □ No
Rotors/Screws______□ Yes □ No
Shaft______□ Yes □ No
Bearings______□ Yes □ No
Seals______□ Yes □ No
O-rings______□ Yes □ No

Material Deviation Analysis

Deviation TypeRiskEvaluation
Alternative equivalentLow-MediumAccept with data
Downgrade materialHighUsually reject
Upgrade materialLowAccept
Different coatingMediumVerify performance

Scoring Methodology

Scoring Scale

ScoreDefinition
5Exceeds requirements, no deviations
4Fully compliant
3Minor deviations, acceptable
2Significant deviations, needs clarification
1Major gaps, marginally acceptable
0Does not comply

Sample Evaluation Matrix

CriteriaWeightVendor AVendor BVendor C
Flow/Pressure compliance20%453
Viscosity range15%544
Slip/Efficiency10%443
Materials15%454
Bearing life (L10)10%543
References10%534
Documentation5%443
Delivery10%454
Commercial5%345
Weighted Score100%4.204.303.60

Common Deviations

Performance Deviations

DeviationRiskGuidance
Slightly lower efficiencyLowAccept if within 5%
Higher slipMediumVerify flow still meets spec
Different speedLowAccept if flow met
Lower NPSHr marginMediumVerify system NPSHa

Design Deviations

DeviationRiskGuidance
No relief valveCriticalReject or require
Different seal typeMediumVerify API 682 compliance
Alternative bearingMediumVerify L10 life
Longer deliveryCommercialNegotiate

Documentation Deviations

Missing ItemRiskAction
Performance curvesHighRequest before evaluation
Material certificatesMediumAccept as clarification
Reference listMediumRequest minimum 3
Deviation listHighCannot properly evaluate

Red Flags

Critical Red Flags (Potential Rejection)

Red FlagWhy Serious
No performance curves at specified viscosityCannot verify performance
Relief valve not includedSafety requirement missing
Cold start not addressedMay not start
Slip not specifiedEfficiency unknown
L10 life < 15,000 hoursBelow API 676 requirement
No referencesUnproven design

Warning Signs (Require Clarification)

WarningQuestions to Ask
Significantly lower priceWhat’s excluded?
Very short deliveryProven design?
Incomplete datasheetRequest completion
Vague deviationsRequest specifics

Vendor Experience Evaluation

Reference Requirements

CriterionMinimumPreferred
Number of references35+
Similar viscosityWithin 50%Same range
Similar pressureWithin 20%Same or higher
Operating duration1 year3+ years

Questions for References

  1. Operating viscosity range vs design?
  2. Any cold start issues?
  3. Actual slip vs quoted?
  4. Bearing/seal replacement frequency?
  5. Vendor support quality?
  6. Would you purchase again?

Lifecycle Cost Considerations

Cost Components

ComponentTypical %Notes
Initial purchase10-15%Higher than centrifugal
Energy35-40%Efficiency dependent
Maintenance30-35%Seals, bearings
Downtime10-15%Reliability dependent
Spare parts5-10%Long-term availability

Comparison Factors

FactorLower CostHigher Cost
EfficiencyHigher efficiency pumpLower efficiency
Seal typeSingle sealDouble seal
MaterialsStandardUpgraded
L10 lifeLonger lifeShorter life

TBE Summary Report Format

TECHNICAL BID EVALUATION SUMMARY

Project: _______________
Tag Number: _______________
Date: _______________

VENDOR RANKING:
1. Vendor ___: Score ___/5.0
2. Vendor ___: Score ___/5.0
3. Vendor ___: Score ___/5.0

KEY FINDINGS:
- Technical leader: Vendor ___ (reason)
- Commercial leader: Vendor ___ (reason)
- Best value: Vendor ___ (reason)

CRITICAL DEVIATIONS:
1. Vendor ___: [deviation] - [resolution]
2. Vendor ___: [deviation] - [resolution]

CLARIFICATIONS REQUIRED:
□ Vendor ___: [item needed]
□ Vendor ___: [item needed]

RECOMMENDATION:
□ Award to Vendor ___
□ Award with conditions (list)
□ Re-bid required
□ Further clarification needed

Prepared by: _______________
Reviewed by: _______________
Approved by: _______________

Frequently Asked Questions

What is the most critical item when evaluating screw pump quotations?
Viscosity compatibility is most critical. Verify the pump is designed for the full viscosity range including cold start conditions. A pump sized for operating viscosity may not start with cold, high-viscosity fluid.
How should I weight the evaluation criteria?
Typical weighting: Technical Compliance 40-50%, Viscosity/Performance 20%, Materials 15%, Vendor Experience 10%, Delivery 10%, Cost 5-10%. Adjust based on specific application criticality.
What are red flags in screw pump quotations?
Major red flags: no performance curves at specified viscosity, relief valve not included, inadequate cold-start consideration, slip not specified, L10 bearing life below 15,000 hours, and significantly lower price without clear explanation.

📚References & Sources

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