Download your PDF
Saturated Liquid Ethylene Density Calculator result sheet — free, supported by sponsors. Your download button appears in 20 seconds.
This free download is supported by sponsors — continuing in
20
Your file is generated in your browser when you choose Download — nothing is uploaded. If this calculator returns enough numeric data, the export also includes its best-fit chart alongside the readable table.
WorldCalculate result export
Saturated Liquid Ethylene Density Calculator — result sheet
Interpolate a NIST table of saturated-liquid ethylene molar density from 105 K to 160 K and convert it to an approximate mass density.
Inputs used
Results
Visual chart
Breakdown
Calculation steps
Returned data table
Formula and methodology
Formula: Molar density is linearly interpolated between the tabulated saturated-liquid ethylene values at 5 K intervals from 105 K through 160 K. Mass density in kg/m³ = molar density in mol/L × 28.05316 g/mol, because 1 g/L = 1 kg/m³.
The page is a bounded property-table interpolation for saturated liquid ethylene, not a general equation of state. The saturation-line condition and temperature range are part of the result and must remain attached to any engineering note.
This result follows the calculator's declared inputs, precision, validation boundaries, and model limits.
Input contract
- Temperature on saturation line — K; minimum 105; maximum 160
Worked example
| Input | Value |
|---|---|
| Temperature on saturation line | 120 |
At 120 K, the table value is 22.572 mol/L; the corresponding mass-density conversion is about 633.2 kg/m³ under the stated saturated-liquid convention.
Assumptions and limits
- The fluid is ethylene, C2H4, on its saturated-liquid line.
- Temperature is absolute temperature in kelvins and is within the tabulated 105–160 K range.
- Linear interpolation is used between neighboring 5 K reference points.
- The interpolation is not extrapolated below 105 K or above 160 K.
- The molar mass used for conversion is 28.05316 g/mol.
- Pressure is the saturation pressure corresponding to the entered temperature, not an independent input.
- The result does not describe compressed liquid ethylene away from saturation.
- It does not calculate vapor density, enthalpy, pressure, phase stability, or equipment limits.
- Cryogenic and flammable-fluid handling requires appropriate procedures and qualified review.
- The displayed precision should not be treated as a measurement uncertainty or design tolerance.
Calculator note
Source and methodology
Use the official WorldCalculate methodology policy for the source, formula, precision, and boundary standards behind this calculator.
Planning estimate, not financial, medical, legal, or professional advice. © WorldCalculate — reuse with attribution. Built and curated by Hassan ALRowaie.
No saved result was found. Please run the calculation first, then choose Download again.