zhaoyuanjuns/moonbit_extractor/thermo

README
U
ActivityModel
U
AuditReport
U
BalanceAudit
U
BenchmarkCase
U
BenchmarkResult
U
BinodalCurve
U
BoundaryIntersection
U
BoundaryProjection
U
CartesianPoint
U
Concentration
U
ContactPattern
U
CountercurrentResult
U
CountercurrentStage
U
CrossValidation
U
CrosscurrentLeachingResult
U
CrosscurrentResult
U
CrosscurrentStage
U
CsvOptions
U
DesignPoint
U
Duration
U
EfficiencyCalibration
U
EfficiencyStageResult
U
EfficiencyStep
U
EquilibriumCurve
U
EquilibriumPoint
U
EquilibriumTable
U
ExtractionError
U
ExtractionStep
U
Extrapolation
U
Finding
U
LeachingStage
U
LeachingStageResult
U
LedgerEntry
U
LeverResult
U
LinearTable
U
Mass
U
MassFlow
U
MassUnit
U
NumericSummary
U
Observation
U
OperatingWindow
U
PhaseSplit
U
Point
U
Range
U
RecoveryEnvelope
U
RegressionModel
U
SafetyFactor
U
ScenarioResult
U
ScenarioSummary
U
SearchResult
U
SensitivityPoint
U
Severity
U
SingleStageResult
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SingleStageScenario
U
SolventDesign
U
StageCountResult
U
Statistics
U
SvgCanvas
U
TernaryComposition
U
TieLine
U
TieLineTable
U
TimeUnit
U
Violation
V
activity_factor
V
analysis_balance_report
V
apply_safety_factor
V
approximately_equal
V
audit_balances
V
average_recovery
V
balance_report
V
bounded_minimize
V
calibrate_efficiency
V
cartesian_grid
V
casebook
V
centroid
V
compare_contact_patterns
V
concentration_from_fraction
V
contains
V
countercurrent_constant_k
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crosscurrent_constant_k
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crosscurrent_equal_solvent
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crosscurrent_equal_wash
V
crosscurrent_leach
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distribution_coefficient
V
extraction_factor
V
fit_linear
V
fit_polynomial
V
from_cartesian
V
grid_minimize
V
is_finite
V
latin_hypercube
V
leave_one_out
V
ledger_entry
V
ledger_passes
V
lever_rule
V
linspace
V
map_unit_triangle
V
maximum_residual
V
mccabe_thiele_stages
V
minimum_countercurrent_stages
V
mix_point
V
operating_line
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pareto_front
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parse_equilibrium_csv
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parse_tie_lines_csv
V
polygon_area
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quantile
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recommended_safety_factor
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recovery_fraction
V
run_casebook
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run_single_stage_scenario
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run_single_stage_scenarios
V
sample_curve
V
selectivity
V
shortcut_actual_stages
V
single_stage_constant_k
V
single_stage_leach
V
single_stage_recovery_envelope
V
single_stage_sensitivity
V
single_stage_table
V
solvent_for_countercurrent
V
solvent_for_crosscurrent
V
solvent_for_single_stage
V
split_on_tie_line
V
stages_with_efficiency_profile
V
stages_with_uniform_efficiency
V
summarize
V
summarize_scenarios
V
sweep_distribution
V
sweep_solvent_flow
V
ternary_triangle
V
to_cartesian
V
validate_curve
V
wash_for_target

zhaoyuanjuns/moonbit_extractor/thermo does not have a README file

ActivityModel

pub(all) enum ActivityModel {
  ConstantK(k~ : Double)
  Margules(two_sided~ : Double, three_sided~ : Double)
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Lightweight activity-coefficient relations for screening non-ideal data.

ActivityModel::equilibrium

source

fn ActivityModel::equilibrium(self : ActivityModel, x : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

ActivityPair

source

pub(all) struct ActivityPair {
  first_fraction : Double
  second_fraction : Double
  first_coefficient : Double
  second_coefficient : Double
  first_ln_coefficient : Double
  second_ln_coefficient : Double
  excess_gibbs_over_rt : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Activity coefficients and excess Gibbs-energy diagnostics for a binary pair.

AntoineCorrelation

source

pub(all) struct AntoineCorrelation {
  component : String
  a : Double
  b : Double
  c : Double
  pressure_unit : String
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Auditable property correlations used for preliminary process screening.

AntoineCorrelation::vapor_pressure

source

fn AntoineCorrelation::vapor_pressure(self : AntoineCorrelation, temperature : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

BinaryEquilibriumPoint

source

pub(all) struct BinaryEquilibriumPoint {
  liquid_fraction : Double
  vapor_fraction : Double
  first_k_value : Double
  second_k_value : Double
  bubble_pressure : @zhaoyuanjuns/moonbit_extractor/units.Pressure
Pressure
  excess_gibbs_energy : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

A binary equilibrium estimate from activity and vapor-pressure data.

ComponentProperty

source

pub(all) struct ComponentProperty {
  name : String
  molecular_weight : Double
  density : Double
  boiling_temperature : Double
  heat_capacity : Double
  viscosity : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

DensityCorrelation

source

pub(all) struct DensityCorrelation {
  component : String
  reference_temperature : Double
  reference_density : Double
  expansion_coefficient : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

EnvelopeCurve

source

pub(all) struct EnvelopeCurve {
  component : String
  points : Array[EnvelopePoint]
  bubble_pressure : Double
  dew_pressure : Double
  minimum_temperature : Double
  maximum_temperature : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

EnvelopePoint

source

pub(all) struct EnvelopePoint {
  temperature : Double
  pressure : Double
  liquid_fraction : Double
  vapor_fraction : Double
  liquid_composition : Double
  vapor_composition : Double
  k_value : Double
  phase : String
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Screening calculations for binary equilibrium envelopes.

EquilibriumCurve

source

pub(all) struct EquilibriumCurve {
  model : ActivityModel
  points : Array[Double]
  values : Array[Double]
  monotone : Bool
  maximum : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

FlashDiagnostic

source

pub(all) struct FlashDiagnostic {
  name : String
  value : Double
  threshold : Double
  passed : Bool
  message : String
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Diagnostics for an isothermal flash result.

FlashResult

source

pub(all) struct FlashResult {
  vapor_fraction : Double
  liquid_composition : Array[Double]
  vapor_composition : Array[Double]
  feed_composition : Array[Double]
  rachford_rice_residual : Double
  iterations : Int
  converged : Bool
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Flash calculation result for a multicomponent feed.

FlashSensitivity

source

pub(all) struct FlashSensitivity {
  component : Int
  base_fraction : Double
  perturbed_fraction : Double
  change : Double
  normalized_change : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

MixtureProperty

source

pub(all) struct MixtureProperty {
  temperature : Double
  pressure : Double
  composition : Array[Double]
  molecular_weight : Double
  density : Double
  heat_capacity : Double
  viscosity : Double
  boiling_temperature : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

NonIdealActivityModel

source

pub(all) enum NonIdealActivityModel {
  SymmetricMargules(parameter~ : Double)
  TwoSuffixMargules(first_to_second~ : Double, second_to_first~ : Double)
  PolynomialCorrection(first~ : Double, second~ : Double, third~ : Double)
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

A binary liquid activity model for non-ideal equilibrium screening.

PhaseEnvelopePoint

source

pub(all) struct PhaseEnvelopePoint {
  vapor_fraction : Double
  liquid_composition : Array[Double]
  vapor_composition : Array[Double]
  separation : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

PropertyPoint

source

pub(all) struct PropertyPoint {
  temperature : Double
  pressure : Double
  vapor_pressure : Double
  density : Double
  viscosity : Double
  surface_tension : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

PropertySensitivity

source

pub(all) struct PropertySensitivity {
  component : String
  composition_change : Double
  density_change : Double
  viscosity_change : Double
  boiling_change : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

TieLine

source

pub(all) struct TieLine {
  liquid_composition : Double
  vapor_composition : Double
  temperature : Double
  lever_liquid : Double
  lever_vapor : Double
  separation : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

VaporPressureCorrelation

source

pub(all) struct VaporPressureCorrelation {
  reference_temperature_kelvin : Double
  coefficient_zero : Double
  coefficient_one : Double
  coefficient_two : Double
  coefficient_three : Double
  minimum_temperature_kelvin : Double
  maximum_temperature_kelvin : Double
  pressure_unit : @zhaoyuanjuns/moonbit_extractor/units.PressureUnit
PressureUnit
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

Polynomial vapor-pressure correlation in a bounded temperature range.

VaporPressureCorrelation::new

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fn VaporPressureCorrelation::new(reference_temperature~ : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature, coefficient_zero~ : Double, coefficient_one~ : Double, coefficient_two~ : Double, coefficient_three~ : Double, minimum_temperature~ : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature, maximum_temperature~ : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature, pressure_unit~ : @zhaoyuanjuns/moonbit_extractor/units.PressureUnit
PressureUnit) -> VaporPressureCorrelation raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

VaporPressureCorrelation::pressure

source

fn VaporPressureCorrelation::pressure(self : VaporPressureCorrelation, temperature : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature) -> @zhaoyuanjuns/moonbit_extractor/units.Pressure
Pressure raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

VaporPressureCorrelation::relative_pressure_change

source

fn VaporPressureCorrelation::relative_pressure_change(self : VaporPressureCorrelation, first : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature, second : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

VaporPressureCorrelation::slope

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fn VaporPressureCorrelation::slope(self : VaporPressureCorrelation, temperature : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

ViscosityCorrelation

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pub(all) struct ViscosityCorrelation {
  component : String
  reference_temperature : Double
  reference_viscosity : Double
  temperature_sensitivity : Double
} derive(Eq, ToJson, @moonbitlang/core/debug.Debug
Debug)

activity_coefficient

source

fn activity_coefficient(model : NonIdealActivityModel, component_fraction~ : Double, component_index~ : Int) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

activity_factor

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fn activity_factor(model : ActivityModel, x : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

activity_pair

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fn activity_pair(model : NonIdealActivityModel, first_fraction~ : Double) -> ActivityPair raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

Evaluate activity coefficients for a binary liquid composition.

all_components_recovered_above

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fn all_components_recovered_above(result : FlashResult, threshold~ : Double) -> Bool raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

approximate_ten_power

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fn approximate_ten_power(exponent : Double) -> Double

binary_equilibrium_point

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fn binary_equilibrium_point(model : NonIdealActivityModel, first_fraction~ : Double, temperature~ : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature, pressure~ : @zhaoyuanjuns/moonbit_extractor/units.Pressure
Pressure, first_vapor_pressure~ : VaporPressureCorrelation, second_vapor_pressure~ : VaporPressureCorrelation) -> BinaryEquilibriumPoint raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

bubble_pressure

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fn bubble_pressure(liquid_composition : Double, saturation_pressure_one : Double, saturation_pressure_two : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

bubble_temperature_estimate

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fn bubble_temperature_estimate(pressure : Double, normal_boiling_one : Double, normal_boiling_two : Double, liquid_composition : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

build_envelope

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fn build_envelope(component~ : String, temperatures : ArrayView[Double], pressures : ArrayView[Double], relative_volatility : Double) -> EnvelopeCurve raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

capillary_number

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fn capillary_number(viscosity : Double, velocity : Double, surface_tension : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

classify_relative_volatility

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fn classify_relative_volatility(relative_volatility : Double) -> String

component_contribution

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fn component_contribution(property : ComponentProperty, composition : Double) -> (Double, Double, Double, Double)

corrected_k_value

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fn corrected_k_value(k_value~ : Double, correction~ : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

Apply a pressure correction to a K-value while preserving its sign.

density_at

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fn density_at(correlation : DensityCorrelation, temperature : Double, pressure_factor : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

dew_pressure

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fn dew_pressure(vapor_composition : Double, saturation_pressure_one : Double, saturation_pressure_two : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

dew_temperature_estimate

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fn dew_temperature_estimate(pressure : Double, normal_boiling_one : Double, normal_boiling_two : Double, vapor_composition : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

envelope_average_temperature

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fn envelope_average_temperature(curve : EnvelopeCurve) -> Double

envelope_csv

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fn envelope_csv(curve : EnvelopeCurve) -> String

envelope_filter_phase

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fn envelope_filter_phase(curve : EnvelopeCurve, phase : String) -> Array[EnvelopePoint]

envelope_markdown

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fn envelope_markdown(curve : EnvelopeCurve) -> String

envelope_maximum_k

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fn envelope_maximum_k(curve : EnvelopeCurve) -> Double

envelope_minimum_separation

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fn envelope_minimum_separation(curve : EnvelopeCurve) -> Double

envelope_points_at_pressure

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fn envelope_points_at_pressure(curve : EnvelopeCurve, pressure : Double, tolerance : Double) -> Array[EnvelopePoint]

envelope_points_at_temperature

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fn envelope_points_at_temperature(curve : EnvelopeCurve, temperature : Double, tolerance : Double) -> Array[EnvelopePoint]

envelope_recovery_factor

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fn envelope_recovery_factor(curve : EnvelopeCurve, target_separation : Double) -> Double

equilibrium_k_value

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fn equilibrium_k_value(relative_volatility : Double, composition : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

excess_gibbs_energy

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fn excess_gibbs_energy(model : NonIdealActivityModel, first_fraction~ : Double, temperature~ : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

flash_component_recovery

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fn flash_component_recovery(result : FlashResult, component : Int) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

flash_component_split

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fn flash_component_split(result : FlashResult, component : Int) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

flash_diagnostics

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fn flash_diagnostics(result : FlashResult, composition_tolerance? : Double) -> Array[FlashDiagnostic] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

flash_envelope

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fn flash_envelope(feed : ArrayView[Double], k_values : ArrayView[Double], vapor_fractions : ArrayView[Double]) -> Array[PhaseEnvelopePoint] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

flash_recovery_vector

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fn flash_recovery_vector(result : FlashResult) -> Array[Double] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

flash_sensitivity

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fn flash_sensitivity(feed : ArrayView[Double], k_values : ArrayView[Double], component : Int, relative_step? : Double) -> FlashSensitivity raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

interpolate_envelope_point

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fn interpolate_envelope_point(first : EnvelopePoint, second : EnvelopePoint, temperature : Double) -> EnvelopePoint raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

isothermal_flash

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fn isothermal_flash(feed_composition~ : ArrayView[Double], k_values~ : ArrayView[Double], tolerance? : Double, maximum_iterations? : Int) -> FlashResult raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

Solve the isothermal Rachford–Rice flash equation for supplied K-values.

k_value

source

fn k_value(activity_coefficient~ : Double, vapor_pressure~ : @zhaoyuanjuns/moonbit_extractor/units.Pressure
Pressure, system_pressure~ : @zhaoyuanjuns/moonbit_extractor/units.Pressure
Pressure) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

Estimate the K-value of a component from activity and vapor pressure.

limiting_flash_component

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fn limiting_flash_component(result : FlashResult) -> Int raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

liquid_composition_from_k

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fn liquid_composition_from_k(vapor_composition : Double, k_value : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

make_envelope_point

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fn make_envelope_point(temperature : Double, pressure : Double, liquid_composition : Double, relative_volatility : Double) -> EnvelopePoint raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_boiling_temperature

source

fn mixture_boiling_temperature(components : ArrayView[ComponentProperty], composition : ArrayView[Double]) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_component_count

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fn mixture_component_count(mixture : MixtureProperty) -> Int

mixture_composition_distance

source

fn mixture_composition_distance(first : MixtureProperty, second : MixtureProperty) -> Double

mixture_density

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fn mixture_density(components : ArrayView[ComponentProperty], composition : ArrayView[Double]) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_density_factor

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fn mixture_density_factor(mixture : MixtureProperty, reference_density : Double) -> Double

mixture_dominant_component

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fn mixture_dominant_component(mixture : MixtureProperty) -> Int

mixture_excess_density

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fn mixture_excess_density(mixture : MixtureProperty, ideal_density : Double) -> Double

mixture_heat_capacity

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fn mixture_heat_capacity(components : ArrayView[ComponentProperty], composition : ArrayView[Double]) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_minor_fraction

source

fn mixture_minor_fraction(mixture : MixtureProperty) -> Double

mixture_molecular_weight

source

fn mixture_molecular_weight(components : ArrayView[ComponentProperty], composition : ArrayView[Double]) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_normalize_composition

source

fn mixture_normalize_composition(composition : ArrayView[Double]) -> Array[Double] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_pressure_shift

source

fn mixture_pressure_shift(mixture : MixtureProperty, target_pressure : Double, compressibility : Double) -> MixtureProperty

mixture_property

source

fn mixture_property(temperature : Double, pressure : Double, components : ArrayView[ComponentProperty], composition : ArrayView[Double]) -> MixtureProperty raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_property_csv

source

fn mixture_property_csv(properties : ArrayView[MixtureProperty]) -> String

mixture_property_report

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fn mixture_property_report(property : MixtureProperty) -> String

mixture_temperature_shift

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fn mixture_temperature_shift(mixture : MixtureProperty, target_temperature : Double, thermal_expansion : Double) -> MixtureProperty

mixture_viscosity

source

fn mixture_viscosity(components : ArrayView[ComponentProperty], composition : ArrayView[Double]) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

mixture_viscosity_factor

source

fn mixture_viscosity_factor(mixture : MixtureProperty, reference_viscosity : Double) -> Double

phase_composition_difference

source

fn phase_composition_difference(result : FlashResult) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

pressure_correction

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fn pressure_correction(pressure : @zhaoyuanjuns/moonbit_extractor/units.Pressure
Pressure, second_virial_coefficient~ : Double, temperature : @zhaoyuanjuns/moonbit_extractor/units.Temperature
Temperature) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

A pressure correction for a simple vapor-phase fugacity factor.

property_average

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fn property_average(points : ArrayView[PropertyPoint]) -> PropertyPoint

property_csv

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fn property_csv(points : ArrayView[PropertyPoint]) -> String

property_grid

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fn property_grid(temperatures : ArrayView[Double], pressures : ArrayView[Double], vapor_pressure_model : AntoineCorrelation, density_model : DensityCorrelation, viscosity_model : ViscosityCorrelation, reference_surface_tension : Double, critical_temperature : Double) -> Array[PropertyPoint] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

property_maximum

source

fn property_maximum(points : ArrayView[PropertyPoint]) -> PropertyPoint

property_minimum

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fn property_minimum(points : ArrayView[PropertyPoint]) -> PropertyPoint

property_point

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fn property_point(temperature : Double, pressure : Double, vapor_pressure_model : AntoineCorrelation, density_model : DensityCorrelation, viscosity_model : ViscosityCorrelation, reference_surface_tension : Double, critical_temperature : Double) -> PropertyPoint raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

property_report

source

fn property_report(points : ArrayView[PropertyPoint]) -> String

property_sensitivity

source

fn property_sensitivity(baseline : MixtureProperty, perturbed : MixtureProperty, component : String, composition_change : Double) -> PropertySensitivity

relative_volatility

source

fn relative_volatility(k_values : ArrayView[Double], reference_index : Int) -> Array[Double] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

Convert K-values into relative volatility ratios against a reference component.

reynolds_number

source

fn reynolds_number(density : Double, velocity : Double, diameter : Double, viscosity : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

sample_curve

source

fn sample_curve(model : ActivityModel, count : Int) -> EquilibriumCurve raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

surface_tension_at

source

fn surface_tension_at(reference_surface_tension : Double, reference_temperature : Double, temperature : Double, critical_temperature : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

tie_line

source

fn tie_line(liquid_composition : Double, vapor_composition : Double, overall_composition : Double, temperature : Double) -> TieLine raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

tie_line_reconstruct

source

fn tie_line_reconstruct(line : TieLine) -> Double

validate_composition

source

fn validate_composition(composition : ArrayView[Double]) -> Bool

validate_curve

source

fn validate_curve(curve : EquilibriumCurve, tolerance~ : Double) -> Array[String] raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

vapor_composition_from_k

source

fn vapor_composition_from_k(liquid_composition : Double, k_value : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

viscosity_at

source

fn viscosity_at(correlation : ViscosityCorrelation, temperature : Double) -> Double raise @zhaoyuanjuns/moonbit_extractor/domain.ExtractionError
ExtractionError

Source Files

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#ActivityModel

#ActivityModel::equilibrium

#ActivityPair

#AntoineCorrelation

#AntoineCorrelation::vapor_pressure

#BinaryEquilibriumPoint

#ComponentProperty

#DensityCorrelation

#EnvelopeCurve

#EnvelopePoint

#EquilibriumCurve

#FlashDiagnostic

#FlashResult

#FlashSensitivity

#MixtureProperty

#NonIdealActivityModel

#PhaseEnvelopePoint

#PropertyPoint

#PropertySensitivity

#TieLine

#VaporPressureCorrelation

#VaporPressureCorrelation::new

#VaporPressureCorrelation::pressure

#VaporPressureCorrelation::relative_pressure_change

#VaporPressureCorrelation::slope

#ViscosityCorrelation

#activity_coefficient

#activity_factor

#activity_pair

#all_components_recovered_above

#approximate_ten_power

#binary_equilibrium_point

#bubble_pressure

#bubble_temperature_estimate

#build_envelope

#capillary_number

#classify_relative_volatility

#component_contribution

#corrected_k_value

#density_at

#dew_pressure

#dew_temperature_estimate

#envelope_average_temperature

#envelope_csv

#envelope_filter_phase

#envelope_markdown

#envelope_maximum_k

#envelope_minimum_separation

#envelope_points_at_pressure

#envelope_points_at_temperature

#envelope_recovery_factor

#equilibrium_k_value

#excess_gibbs_energy

#flash_component_recovery

#flash_component_split

#flash_diagnostics

#flash_envelope

#flash_recovery_vector

#flash_sensitivity

#interpolate_envelope_point

#isothermal_flash

#k_value

#limiting_flash_component

#liquid_composition_from_k

#make_envelope_point

#mixture_boiling_temperature

#mixture_component_count

#mixture_composition_distance

#mixture_density

#mixture_density_factor

#mixture_dominant_component

#mixture_excess_density

#mixture_heat_capacity

#mixture_minor_fraction

#mixture_molecular_weight

#mixture_normalize_composition

#mixture_pressure_shift

#mixture_property

#mixture_property_csv

#mixture_property_report

ActivityModel

ActivityModel::equilibrium

ActivityPair

AntoineCorrelation

AntoineCorrelation::vapor_pressure

BinaryEquilibriumPoint

ComponentProperty

DensityCorrelation

EnvelopeCurve

EnvelopePoint

EquilibriumCurve

FlashDiagnostic

FlashResult

FlashSensitivity

MixtureProperty

NonIdealActivityModel

PhaseEnvelopePoint

PropertyPoint

PropertySensitivity

TieLine

VaporPressureCorrelation

VaporPressureCorrelation::new

VaporPressureCorrelation::pressure

VaporPressureCorrelation::relative_pressure_change

VaporPressureCorrelation::slope

ViscosityCorrelation

activity_coefficient

activity_factor

activity_pair

all_components_recovered_above

approximate_ten_power

binary_equilibrium_point

bubble_pressure

bubble_temperature_estimate

build_envelope

capillary_number

classify_relative_volatility

component_contribution

corrected_k_value

density_at

dew_pressure

dew_temperature_estimate

envelope_average_temperature

envelope_csv

envelope_filter_phase

envelope_markdown

envelope_maximum_k

envelope_minimum_separation

envelope_points_at_pressure

envelope_points_at_temperature

envelope_recovery_factor

equilibrium_k_value

excess_gibbs_energy

flash_component_recovery

flash_component_split

flash_diagnostics

flash_envelope

flash_recovery_vector

flash_sensitivity

interpolate_envelope_point

isothermal_flash

k_value

limiting_flash_component

liquid_composition_from_k

make_envelope_point

mixture_boiling_temperature

mixture_component_count

mixture_composition_distance

mixture_density

mixture_density_factor

mixture_dominant_component

mixture_excess_density

mixture_heat_capacity

mixture_minor_fraction

mixture_molecular_weight

mixture_normalize_composition

mixture_pressure_shift

mixture_property

mixture_property_csv

mixture_property_report