Hooman Fatoorehchi
Assistant Professor
School of Chemical Engineering
University of Tehran, Tehran, Iran
Formulas in this page are typed in $\LaTeX$.

Process Engineering

Online Compressor Power Calculator

Based on Joffe's equation; Copyright (C) 2022 by Hooman Fatoorehchi

P1:
P2:
T1:
Cp:
Cv:
z1:
You can calculate the z-factor using the Peng-Robinson EOS by clicking HERE


Natural Gas Compression; Joffe's Formula
The adiabatic theoretical horsepower to compress 1 MMSCFD (i.e. volumetric flow at standard conditions: 60 deg F, 14.65 pisa):

$-w=0.08531 \frac{k}{k-1}T_1 \left[ \left( \frac{P_2}{P_1} \right)^{z\hspace{0.1cm}(k-1)/k}-1 \right]$,

where $k=\frac{C_p}{C_v}$ for gas at suction conditions
$z$ is compressibility factor at suction conditions
$P_1$ is suction pressure, psia
$P_2$ is discharge pressure, psia
$T_1$ is suction-gas temperature, deg R

NOTE: The maximum allowable pressure drop on the tube side of a heat exchanger (for gases) is 10 psi.
Typically, the pressure drop across an HE would be 3 to 10 psi.

NOTE: Reasonable pressure drop per tray (usually sieve tray) is 0.1 psi (~ 3 in H2O).

NOTE: Tower operating pressure is determined most often by the temperature of the available condensing medium, 120 deg F if cooling water (worst summer case) $\rightarrow$ calculate bubble pressure at 120 deg F for reflux drum pressure
OR by the maximum allowable reboiler temperature, (150 psig (saturated) steam = 366 deg F) $\rightarrow$ calculate bubble pressure at 366 deg F for reboiler pressure.


NOTE: (Fahrenheit to Rankine conversion) deg F + 460 = deg R
(Horsepower to kW conversion) 1 HP = 0.7457 ~ 0.746 kW
1 BTU = 1055.06 J

Mother Processes in Petrochemical Industries:
(1) Steam Cracking
Feedstock: Ethane, Propane, Naphtha, or Gas oil depending on availability.
Main Product: Ethylene (building block of petrochemicals).
Noncatalytic Process.

(2) Catalytic Reforming
Feedstock: Naphtha
Main Product: Benzene, Toluene, Xylenes.

(2) Steam Reforming
Feedstock: Methane
Main Product: Syngas (CO and Hydrogen).
Hydrogen is then used to produce ammonia $ \rightarrow $ urea $\rightarrow$ melamine; nitric acid; nitrates; methanol (CO + H2 $\rightarrow$ CH3OH; CO2 + 3 H2 $\rightarrow$ CH3OH + H2O); 2 methanol + O2 $\rightarrow$ 2 formaldehyde + 2 H2O; methanol + CO $\rightarrow$ acetic acid



Process Selection Guide for Natural Gas Dehydration
(Reference: https://www.intechopen.com/chapters/36624)

Last modified: 01/26/2023

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