Bakrol, Ahmedabad, India+91 97277 86892

Engineering tools

Make the numbers work for you.

Preliminary calculations with visible formulas, SI units and your own design inputs. Build a starting point for a conversation with our engineers.

RO Mass Balance & Recovery

Enter recovery as a percentage. Feasible recovery depends on feed chemistry and membrane design.

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RO Preliminary Membrane Area

Flux and element area must come from approved design/manufacturer data.

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Two-Pass RO Mass Balance

Do not combine recoveries by simple addition.

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UF Membrane Area & Module Count

Backwash/CEB/CIP and availability reduce net production; treat them explicitly.

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NF Mass Balance

Do not promise hardness/TDS rejection without membrane projection.

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Softener Resin & Regeneration Load

Operating capacity and salt dose are resin/process inputs.

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DM / Ion Exchange Load

Use ionic analysis rather than TDS alone for final design.

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EDI Feed Check & Capacity Summary

Final module selection and current/voltage settings are manufacturer-specific.

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Pressure Filter Diameter

Check selected vessel standard diameter, freeboard and backwash expansion.

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Filter Media Quantity

Bulk density is media-specific input.

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Filter Backwash Flow

Confirm expansion, temperature and available drain capacity.

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Rectangular Tank Volume & Plate Area

No structural adequacy implied.

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Cylindrical Tank Volume & Plate Area

Head geometry must be selected explicitly.

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Preliminary Tank Plate Mass

Stiffener/support/nozzle weight must be separately entered or engineered.

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Pressure Vessel Preliminary Thickness

Not for fabrication; code calculations and reinforcement checks mandatory.

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Pipe Diameter by Velocity

Select nearest commercial pipe size and re-check actual velocity.

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Darcy-Weisbach Headloss

Fluid viscosity and roughness must match service.

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Pump Hydraulic Power

Final motor selection includes service factor and vendor curve.

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Blower Airflow / Oxygen Screening

Vendor/diffuser verification required.

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Chemical Dosing Rate

Dose must be lab/process approved.

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STP Population & Sewage Flow

Generation rate is project input, not a universal website default.

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STP Tank Volume by HRT

HRT is process design input and technology-specific.

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MBBR Media Volume Screening

Media data and loading criteria must be vendor/process approved.

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MBR Membrane Area

Flux and cleaning regime must be approved for feed and membrane.

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SBR Cycle Capacity

Detailed cycle phases and biological sizing require process design.

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ETP Equalization & Load Summary

Treatability and chemistry determine downstream process.

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Clarifier / Lamella Surface Area

Solids characteristics and manufacturer plate data matter.

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Sludge Dry Solids & Cake Quantity

Capture efficiency and polymer conditioning are separate inputs.

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ZLD Water Balance

Salt chemistry controls feasible recovery and scaling limits.

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MEE/MVR/ATFD Mass Balance

Energy/heat-transfer design is vendor-specific and not derived from mass balance alone.

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