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Mohamed A. Hassan, CEng MIChemE
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The simulation software should be used and tuned against plant data to verify the model and to be able to accurately predict product yield. This is the brochure of TechnipFMC SPYRO Suite 7, commercial cracking software, used for rigorous simulation of steam cracking.
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We are facing many challenges today regarding estimation of the flow rate of any pipeline or hose installed in our plant. This paper just gives a brief of some equations used in the gas plants to calculate the leakage rate, minimum time required to get a shut-in test, and the maximum pressure drop for new lines. There are many equations to calculate the flow rate of gas through pipe line like: 1. Darcy formula using gas expansion factor which can be used in sonic and subsonic flow. 2. Crane isothermal flow equation 3. Weymouth isothermal flow equation 4. Panhandle isothermal flow equation This paper gives a a quick way to: 1. Calculate the leakage rate from gas line using pressure drop method. 2. Estimate the minimum time required to get a shut-in test on gas transmission line. 3. Estimation of the maximum pressure drop for new lines.
Everyday pipeline engineering calculations
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Vessels are generally sized based on the heat and material balance for governing case. Vapor liquid separation vessels are generally sized based on settling out of 150 µm liquid droplets from vapor stream except in the case of Flare knock-out drum that generally apply 300-600 µm.
Vertical vapor liquid separator
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Mohamed A. Hassan, CEng MIChemE
These guidelines are used as a preliminary design for the feed inlet and outlet nozzles of the separator until the hydraulic calculation is made.
Separator feed characteristics
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Centrifugal compressors are considered as a subclass of dynamic turbo machinery. They achieve the pressure increase by adding kinetic energy to a continuous flow of fluid. This kinetic energy is converted to an increase in pressure in the diffuser where the kinetic energy is converted to pressure energy by decreasing the gas velocity.
Preliminary selection of centrifugal compressor
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Preliminary pipe size
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Hydrate formation is a well-known risk in natural gas wells and pipelines and is managed by temperature control or the injection of hydrate inhibitors, most commonly methanol, which lower the hydrate formation temperature to below the minimum expected operating temperature.
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The simulation software should be used and tuned against plant data to verify the model and to be able to accurately predict product yield. This is the brochure of TechnipFMC SPYRO Suite 7, commercial cracking software, used for rigorous simulation of steam cracking.
TechnipFMC spyro
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We are facing many challenges today regarding estimation of the flow rate of any pipeline or hose installed in our plant. This paper just gives a brief of some equations used in the gas plants to calculate the leakage rate, minimum time required to get a shut-in test, and the maximum pressure drop for new lines. There are many equations to calculate the flow rate of gas through pipe line like: 1. Darcy formula using gas expansion factor which can be used in sonic and subsonic flow. 2. Crane isothermal flow equation 3. Weymouth isothermal flow equation 4. Panhandle isothermal flow equation This paper gives a a quick way to: 1. Calculate the leakage rate from gas line using pressure drop method. 2. Estimate the minimum time required to get a shut-in test on gas transmission line. 3. Estimation of the maximum pressure drop for new lines.
Everyday pipeline engineering calculations
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Mohamed A. Hassan, CEng MIChemE
Vessels are generally sized based on the heat and material balance for governing case. Vapor liquid separation vessels are generally sized based on settling out of 150 µm liquid droplets from vapor stream except in the case of Flare knock-out drum that generally apply 300-600 µm.
Vertical vapor liquid separator
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Mohamed A. Hassan, CEng MIChemE
These guidelines are used as a preliminary design for the feed inlet and outlet nozzles of the separator until the hydraulic calculation is made.
Separator feed characteristics
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Mohamed A. Hassan, CEng MIChemE
Centrifugal compressors are considered as a subclass of dynamic turbo machinery. They achieve the pressure increase by adding kinetic energy to a continuous flow of fluid. This kinetic energy is converted to an increase in pressure in the diffuser where the kinetic energy is converted to pressure energy by decreasing the gas velocity.
Preliminary selection of centrifugal compressor
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Preliminary pipe sizing - technical point of view
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Hydrate formation is a well-known risk in natural gas wells and pipelines and is managed by temperature control or the injection of hydrate inhibitors, most commonly methanol, which lower the hydrate formation temperature to below the minimum expected operating temperature.
Hydrate formation temperature prediction
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The Number of transfer units (NTU) method is used to calculate the rate of heat transfer in heat exchangers when there is insufficient information to calculate the Log-mean temperature difference (LMTD).
Heat exchanger effecctiveness
Heat exchanger effecctiveness
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The flow regime and droplet diameter is important steps in sizing the gas/liquid separators. The selection of flow regime depends on the location of the separators. For example, if the separator is at suction of a compressor, the flow regime should be stratified flow to facilitate liquid separation from gas in separators
Flow regime and droplets diameter calculations
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The measurement of the flow using the differential pressure apparatus is commonly used in the industry, so it is important to know how to calculate the flow rate through an orifice
Flow measurement through orifice
Flow measurement through orifice
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To determine the optimum pipe diameter, you should go make the comparative analysis to determine the most optimum pipe size which reflects the most economic option. This example is for illustration the importance of the the comparative analysis. Note: According to ASME, pipe with 5 in diameter is not standard, but i selected it in the example for illustration only.
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The structure and properties of phase equilibrium diagrams for the azeotropic multi component mixtures are based on the definition of azeotropy. Azeotrope means bubbling without change in general. This means that the vapor generated in a distillation has the same composition of the liquid with which it is in equilibrium.
Azeotropic distillation 1
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Continuing with the previous document "Azeotropic distillation 1", I used Aspen plus for sizing and rating the distillation columns and determining the diameter and height of the column and the tray type with the required down-comer.
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