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Evaporator Steam Economy One Effect Term Tool

One-effect mass and latent-energy ratios; sensible heating and external losses are not independently modeled.

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Description

Return steam economy and a latent-heat ratio.

Heat-flow and specific-enthalpy terms depend on a sign convention, a reference state and compatible mass/time bases. A temperature shift, heat-duty residual or latent-energy ratio evaluates a supplied model without determining heat-transfer feasibility, actual properties or equipment performance.

Return steam economy and a latent-heat ratio.

When to use this tool

Use Evaporator Steam Economy One Effect Term when checking the stated thermal, reference-state or energy-balance convention.

How to use the tool and how it works

  1. Enter evaporatedMass, steamMass, steamLatentHeat, vaporLatentHeat. Use the units and conventions below.
  2. Run the tool. Correct any format, range, or cross-field input error before interpreting the output.
  3. Read steamEconomy, latentEfficiency. Use the output convention below.

Return steam economy and a latent-heat ratio. Require evaporatedMass >= 0, steamMass/steamLatentHeat > 0 and vaporLatentHeat >= 0; economy = evaporated/steam, latentEfficiency = evaporated*vapor latent/(steam*steam latent).1

Input fieldMeaning and unitsAccepted input
evaporatedMassEvaporated MassRequired. Finite number; minimum 0.
steamMassSteam MassRequired. Finite number; strictly above 0.
steamLatentHeatSteam Latent HeatRequired. Finite number; strictly above 0.
vaporLatentHeatVapor Latent HeatRequired. Finite number; minimum 0.
Output fieldInterpretationReturned shape
steamEconomySteam EconomyRequired. Finite number.
latentEfficiencyEvaporated-mass latent energy divided by supplied-steam latent energy; can exceed one.Required. Finite number.
json
{
  "input": {
    "evaporatedMass": 80,
    "steamMass": 100,
    "steamLatentHeat": 2200,
    "vaporLatentHeat": 2000
  },
  "output": {
    "steamEconomy": 0.8,
    "latentEfficiency": 0.7272727272727273
  }
}

Limitations and assumptions

  • The named efficiency can exceed one; sensible loads, heat losses and actual evaporator performance are not established.
  • Inputs must satisfy both the field types and the cross-field conditions above. Invalid input causes an error; a successful false flag or documented placeholder is a different result.
  • Numeric calculations use binary floating point unless exact decimal-integer arithmetic is explicitly stated. No hidden measurement tolerance or decimal rounding is added; nonfinite or out-of-contract results are rejected. Numeric signed-zero results are exported as zero.

Alternative or Complementary methods

Use verified state-dependent properties and the complete heat/work balance; evaluate heat transfer and equipment constraints separately for engineering decisions.

References

  1. Calculation and input contract: chemical-engineering/evaporator-steam-economy-one-effect-term — tool.io

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