Online Calculators
Notice Use of the calculators presented within this web site is not a replacement or a substitute for professional engineering evaluation and judgement. These interactive calculators are provided for preliminary equipment design and system evaluation. The final evaluation for any application should be conducted by a qualified engineer experienced in that particular application. And that individual, not Piping News Report, or its employees and representatives, is responsible for the final engineering design and performance of the system or equipment. The calculators provided on this web site are provided for the use of our readers "as is". No warranty, either expressed or implied, is assumed by Piping News Report in regard to the accuracy of the results, or misuse in the application of these calculators. Furthermore, Piping News Report does not assume any liability with regard to any errors, omission or damage resulting from the use of these calculators. In addition, Piping News Report does not warrant, guarantee, or make any representations regarding the use, or the results of use, of the calculators or their accompanying information in terms of their accuracy, validity, completeness, applicability, or compliance with any regulatory code or governmental laws and regulations. Use of the calculators and their information may involve some risk, and the entire risk as to the results and performance of the calculators and their associated information is the accepted responsibility and liability of the user. In accessing this web site you hold Piping News Report and its employees and representatives free and harmless from any responsibility or liability arising from the use of, or reliance on, the interactive calculators and their associated information supplied within this web site. This disclaimer takes precedence over any other statement that may appear in this web site, or in other communications. Piping News Report reserves the right to change or discontinue the interactive calculators contained within this web site at any time. |
Fluid
Flow Calculator
This calculator is used to calculate pipe friction losses
for straight piping handling water and water with varying percentages of ethylene glycol.
The calculator uses an algorithm developed from the basic principles of fluid mechanics.
The program is based on the Darcy-Weisbach equation, the Colebrook equation, and the Moody
equation. The program is intended for use only on straight piping. The program does not
include pressure losses due to elevation differences, or flow through fittings. Fittings
and valves can be factored in by using their straight run of pipe equivalent.
This calculator allows the user to input the fluid type, the fluid temperature, the flow
rate, the pipe size, pipe length, and pipe material. The calculator then determines the
velocity, the Reynolds number, the Moody friction factor, the pipe friction factor (from
the Colebrook equation), the pipe head loss, and the pipe friction loss in PSI. While this
calculator is intended for use on systems handling water and water with varying
percentages of ethylene glycol, later releases will include a wider range of
incompressible fluids (liquid fuels) and compressible fluids (air).
Engineering Units Conversion Calculator
These programs allow users to convert the
quantities for Energy, Pressure, Volume, Density, Specific Volume, Specific Heat
(Entropy), Enthalpy, Viscosity (absolute), and Coefficient of Heat Transfer from their
given units of measure to a desired unit of measure.
Currency Converter
This calculator will convert currency from any amount and any country
specified to an equal amount of currency for any country you select. You simply fill in
the amount and type of currency you hold and indicate the type of currency you wish to
change it to. Click on "Perform Currency Conversion" and the results are given.
Pipe & Tubing
These calculators provide standard properties for pipe and tubing. By
providing the pipe or tubing size, wall schedule and material the results will provide:
Section properties: inside & outside diameter, wall thickness, inside
cross sectional area, transvers metal area, moment of inertia, section modulus, and radius
of gyration.
Surface properties: inside & outside surface area.
Weight: for a variety of common metals.
Heat Exchangers
These calculators will provide graphic displays of TEMA shell & tube
configurations as well as heat transfer data such as Heat Transfer Coefficients, Fouling
Resistance Factors, Heat Exchanger Inlet/Outlet Temperature Prediction
HVAC
This calculator allows users to input a desired flow
rate, a limiting velocity, air pressure, air temperature, the length of the duct, and the
duct material. The program then calculates the duct cross sectional area, the circular
duct diameter, rectangular duct equivalents (with aspect ratios of 1.0 through 4.0), air
density, fluid viscosity, Reynold's number, relative roughness, the Moody friction factor,
the Colebrook friction factor, the pressure loss, and the duct friction loss per unit of
duct length.
Single Phase Pressure Drop in
Piping
The pressure drop calculation presented in this
calculator applies to Newtonian fluids which are incompressible and single phase in
isothermal and steady-state flow situations. The friction factor is calculated rigorously
from the original Colebrook equation.
Two Phase Pressure Drop in Piping
The frictional pressure drop calculation presented here
applies to steady-state, isothermal two phase pipe flow of incompressible Newtonian
fluids. The procedure is based on the "Baker" correlations and flow regime maps.
The procedure automatically handles the complete range of industrially used steel pipe
sizes and schedules.
Pipe Sizing for Single Phase Incompressible Flow
The pipe sizing procedure presented here applies to
Newtonian fluids which are incompressible and single phase in isothermal and steady-state
flow situations. The friction factor is calculated rigorously from the original Colebrook
equation. Piping pressure drop
and rating are treated elsewhere.
Pipe
Rating for Single Phase Incompressible Flow
The pipe rating procedure presented here applies to
Newtonian fluids which are incompressible and single phase in isothermal and steady-state
flow situations. The friction factor is calculated rigorously from the original Colebrook
equation. Piping pressure drop
and sizing are treated elsewhere.
Heat Exchanger Inlet/Outlet
Temperature Prediction
This procedure predicts the thermal behavior of a
single heat exchanger or a bank of identical heat exchangers. It can handle
"TEMA" shell types (E, F, G, and J) as long as there is no change in phase.
Two Phase Flow Horizontal Flow Regime
Map
Flow regime maps that graphically represent the various
flow regimes as determined to exist in horizontal pipe runs.
Two Phase Flow Vertical Flow Regime Map
Flow regime maps that graphically represent the
various flow regimes as determined to exist in vertical pipe runs.
Two Phase Flow Regime
Determination
The two phase flow regime determination procedure
presented here applies to steady-state, isothermal two phase pipe flow of incompressible
Newtonian fluids. The procedure is based on Baker's flow regime maps.
Optimum Dimensions of a Vessel
This procedure calculates the optimum dimensions of a
cylinderical pressure vessel with a known volume with the following restrictions:
Minimum design pressure is 50 PSIG. Input values less than the minimum will be reset by the server.
Minimum valid calculated diameter is 2 ft (0.6 m). Vessels smaller than this minimum are usually fabricated from standard piping. The procedure will not reset the calculated diameter if it falls below this limit..
Maximum valid calculated length is 60 ft (20 m). The procedure will not reset the calculated length if it is above this limit.
Material of construction is carbon steel
Psychrometric Calculator (determine
thermodynamic properties of air)
This calculator is used to compute the
thermodynamic properties of moist air. These properties are used by mechanical engineers
to design Heating Ventilating & Air Conditioning (HVAC) systems and processes.