The document discusses the components and process of a glycol dehydration system used to remove water from natural gas. It describes the major system components including contactors, filters, heat exchangers, pumps, reboilers, and still columns. It also discusses various process variables that impact the dehydration process such as gas and glycol temperatures, glycol circulation rate, and reboiler pressure and temperature. The overall goal of the system is to use glycol like diethylene, triethylene, or tetraethylene glycol to absorb water from the natural gas in a contactor and then regenerate the lean glycol in a reboiler and still column.
ALL ABOUT NATURAL GAS : DEFINITION,FORMATION,PROPERTIES,COMPOSITION,PHASE BEHAVIOR ,CONDITIONING"DEHYDRATION ,SWETENING" AND FINAL PROCESSING TO END USER PRODUCTS
Especially created to understand the basic concept of Natural Gas Dehydration and to describe the popular dehydration method with their process working principles.
ALL ABOUT NATURAL GAS : DEFINITION,FORMATION,PROPERTIES,COMPOSITION,PHASE BEHAVIOR ,CONDITIONING"DEHYDRATION ,SWETENING" AND FINAL PROCESSING TO END USER PRODUCTS
Especially created to understand the basic concept of Natural Gas Dehydration and to describe the popular dehydration method with their process working principles.
Natural Gas (from a natural reservoir or associated to a crude production) can contain acid gas (H2S and/or CO2)..
The Gas Sweetening Process aims to remove part or all of the acid gas.
In petroleum refining, the Crude Distillation Unit (CDU) (often referred to as the Atmospheric Distillation Unit) is usually the first processing equipment through which crude oil is fed. Once in the CDU, crude oil is distilled into various products, like naphtha, kerosene, and diesel, that then serve as feedstocks for all other processing units at the refinery.
Amine Gas Treating Unit - Best Practices - Troubleshooting Guide Gerard B. Hawkins
Amine Gas Treating Unit Best Practices - Troubleshooting Guide for H2S/CO2 Amine Systems
Contents
Process Capabilities for gas treating process
Typical Amine Treating
Typical Amine System Improvements
Primary Equipment Overview
Inlet Gas Knockout
Absorber
Three Phase Flash Tank
Lean/Rich Heat Exchanger
Regenerator
Filtration
Amine Reclaimer
Operating Difficulties Overview
Foaming
Failure to Meet Gas Specification
Solvent Losses
Corrosion
Typical Amine System Improvements
Degradation of Amines and Alkanolamines during Sour Gas Treating
APPENDIX
Best Practices - Troubleshooting Guide
This presentation was created to provide a quick refresher to single-phase fluid flow line sizing. The content of this presentation was obtained from various literature (handbooks and website).
Please provide your comments
Excel sheet Download Link: https://www.scribd.com/document/385945712/PSV-Sizing-Tool-API-Based-Calc-Sheets
PSV Sizing for Blocked Liquid Discharge Condition
PSV Sizing for Blocked Gas Discharge Condition
PSV Sizing for Fire Case of Liquid Filled Vessel
PSV Sizing for Control Valve Fail Open Case
Relief Valve Sizing for Thermal Expansion
Restriction Orifice Sizing for Gas Flow
Restriction Orifice Sizing for Liquid Flow
Single Phase Flow Line Sizing Tool
Gas Control Valve Sizing Tool
Gas Condensate Separation Stages – Design & OptimizationVijay Sarathy
The life cycle of an oil & gas venture begins at the wellhead where subsurface engineers work their way through surveying, drilling, laying production tubing and well completions. Once a well is completed, gathering lines from each well is laid to gather hydrocarbons and transported via a main trunk line to a gas oil separation unit (GOSP) to be processed further to enhance their product value for sales. Gas condensate wells consist of natural gas which is rich in heavier hydrocarbons that are recovered as liquids in separators in field facilities or gas-oil separation plants (GOSP).
The following tutorial is aimed at demonstrating how to optimize and provide the required number of separation stages to process a gas condensate mixture and separate them into their respective vapour phase and liquid phase – termed as “Stage Separation”. Stage separation consists of laying a series of separators which operate at consecutive lower pressures to strip out vapours from the well liquids & resulting in a stabilized liquid. Prior to any hydrocarbon processing in a gas processing plant or a refinery, it is imperative to maximize the liquid recovery as well as provide a stabilized liquid hydrocarbon.
Liquefied Natural Gas (LNG) Production Process ; Production of LNG; LNG industry and Technology (or LNG Value Chain); Liquefaction :Train Size; Compressor Drive Efficiency; Transportation; Pipe; Shipping; Tanker; Major Natural Gas Trade Movements ; Regasification; Storage ; How much does LNG cost?
Natural Gas (from a natural reservoir or associated to a crude production) can contain acid gas (H2S and/or CO2)..
The Gas Sweetening Process aims to remove part or all of the acid gas.
In petroleum refining, the Crude Distillation Unit (CDU) (often referred to as the Atmospheric Distillation Unit) is usually the first processing equipment through which crude oil is fed. Once in the CDU, crude oil is distilled into various products, like naphtha, kerosene, and diesel, that then serve as feedstocks for all other processing units at the refinery.
Amine Gas Treating Unit - Best Practices - Troubleshooting Guide Gerard B. Hawkins
Amine Gas Treating Unit Best Practices - Troubleshooting Guide for H2S/CO2 Amine Systems
Contents
Process Capabilities for gas treating process
Typical Amine Treating
Typical Amine System Improvements
Primary Equipment Overview
Inlet Gas Knockout
Absorber
Three Phase Flash Tank
Lean/Rich Heat Exchanger
Regenerator
Filtration
Amine Reclaimer
Operating Difficulties Overview
Foaming
Failure to Meet Gas Specification
Solvent Losses
Corrosion
Typical Amine System Improvements
Degradation of Amines and Alkanolamines during Sour Gas Treating
APPENDIX
Best Practices - Troubleshooting Guide
This presentation was created to provide a quick refresher to single-phase fluid flow line sizing. The content of this presentation was obtained from various literature (handbooks and website).
Please provide your comments
Excel sheet Download Link: https://www.scribd.com/document/385945712/PSV-Sizing-Tool-API-Based-Calc-Sheets
PSV Sizing for Blocked Liquid Discharge Condition
PSV Sizing for Blocked Gas Discharge Condition
PSV Sizing for Fire Case of Liquid Filled Vessel
PSV Sizing for Control Valve Fail Open Case
Relief Valve Sizing for Thermal Expansion
Restriction Orifice Sizing for Gas Flow
Restriction Orifice Sizing for Liquid Flow
Single Phase Flow Line Sizing Tool
Gas Control Valve Sizing Tool
Gas Condensate Separation Stages – Design & OptimizationVijay Sarathy
The life cycle of an oil & gas venture begins at the wellhead where subsurface engineers work their way through surveying, drilling, laying production tubing and well completions. Once a well is completed, gathering lines from each well is laid to gather hydrocarbons and transported via a main trunk line to a gas oil separation unit (GOSP) to be processed further to enhance their product value for sales. Gas condensate wells consist of natural gas which is rich in heavier hydrocarbons that are recovered as liquids in separators in field facilities or gas-oil separation plants (GOSP).
The following tutorial is aimed at demonstrating how to optimize and provide the required number of separation stages to process a gas condensate mixture and separate them into their respective vapour phase and liquid phase – termed as “Stage Separation”. Stage separation consists of laying a series of separators which operate at consecutive lower pressures to strip out vapours from the well liquids & resulting in a stabilized liquid. Prior to any hydrocarbon processing in a gas processing plant or a refinery, it is imperative to maximize the liquid recovery as well as provide a stabilized liquid hydrocarbon.
Liquefied Natural Gas (LNG) Production Process ; Production of LNG; LNG industry and Technology (or LNG Value Chain); Liquefaction :Train Size; Compressor Drive Efficiency; Transportation; Pipe; Shipping; Tanker; Major Natural Gas Trade Movements ; Regasification; Storage ; How much does LNG cost?
The Economic Comparison Between Dry Natural Gas And Nitrogen Gas For Strippin...inventionjournals
Natural gas isa substantial energy source among other sources of fossil fuels. It is usually produced saturated with water vapor under production conditions. The natural gas dehydration is very paramount in the gas industry to stripthe water vapor existing in the gas production, at low-temperature conditions that may plug the system because of hydrate formation in pipelines. Totake off water vapor from natural gas flow usestriethylene glycol (TEG) in the gas dehydration process. In the glycol method, the wet gas is contactwith leanglycolinan absorber to dehydrate naturalgas and the rich glycol will be recovered and used again. This paper deals with stripping gas in the regenerator of glycol dehydration package with part of dry natural gas instead of nitrogen for stripping water vapor from triethylene glycol and studying the economic comparison between both of them by using modeling and simulation with HYSYS program. The two methods were investigated and evaluated to choose the optimal one with respect to the capital and utility costs, provided that keeping the same specifications and quantity of the glycol purity.In addition, the wet gas from the stripping process can be used to operate texsteam pumps and compressors or recycle with wet gas feed. The model has been built according to the actual process flow diagram. Finally, the results of this model could be considered as a basis on which a new heat and material balance will be developed for the plant.
A Systemic Optimization Approach for the Design of Natural Gas Dehydration PlantIJRES Journal
In designing dehydration units for natural gas, several critical parameters exist which can be varied to achieve a specified dew point depression. This paper studies the effects of varying number of trays in the contactor, glycol circulation rate through the contactor, temperature of the reboiler in the regenerator, amount of stripping gas used and operating pressure of the regenerator on the water content of the gas in a glycol dehydration unit. The effect of incorporating free water knock out (FWKO) tank before the absorber is also presented. An offshore platform in the Arctic region was chosen as the base case of this simulation and was modeled by using ASPEN HYSYS. Results show that the incorporation of FWKOT does not affect the TEG circulation rate required to approach equilibrium.
It will help to the students of Mechanical Engineering. These notes are according to HVAC Subject. Some important topics are here for your good understanding. These are written in easy language, u can understand easily.
CW RADAR, FMCW RADAR, FMCW ALTIMETER, AND THEIR PARAMETERSveerababupersonal22
It consists of cw radar and fmcw radar ,range measurement,if amplifier and fmcw altimeterThe CW radar operates using continuous wave transmission, while the FMCW radar employs frequency-modulated continuous wave technology. Range measurement is a crucial aspect of radar systems, providing information about the distance to a target. The IF amplifier plays a key role in signal processing, amplifying intermediate frequency signals for further analysis. The FMCW altimeter utilizes frequency-modulated continuous wave technology to accurately measure altitude above a reference point.
Student information management system project report ii.pdfKamal Acharya
Our project explains about the student management. This project mainly explains the various actions related to student details. This project shows some ease in adding, editing and deleting the student details. It also provides a less time consuming process for viewing, adding, editing and deleting the marks of the students.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
Saudi Arabia stands as a titan in the global energy landscape, renowned for its abundant oil and gas resources. It's the largest exporter of petroleum and holds some of the world's most significant reserves. Let's delve into the top 10 oil and gas projects shaping Saudi Arabia's energy future in 2024.
2. Mohamed Abdelraof Saad
Glycol Dehydration
The more common liquids in use for
dehydrating natural gas are
Diethylene glycol (DEG)
Triethylene glycol (TEG)
Tetraethylene glycol (TREG).
10. Glycol Reboiler
Gly. Inj. Pump
Glycol
Accumulator
Lean /Rich Gly.
Ex.
Rich Gly.
Flashed
Gas
Gas flow meterSystem Valve
Glycol
Flash
Drum
Glycol
Cartridge
filter Glycol Carbon
filter
Dehydration
tower T-101
Sea Line
Produced
Gas
11. Mohamed Abdelraof Saad
Glycol Dehydration System Components
Inlet Scrubber
Inadequate scrubbing causes about half of all
glycol dehydration system problems.
Free water
Many contaminants include:
1. Oils or hydrocarbons
2. Entrained brine
3. Downhole additives
4. Solids, such as sand and corrosion products
12. PROBLEMS CAUSED BY CONTAMINANTS
PROBLEMSCONTAMINANT
Increases glycol recirculation, reboiler heat duty, and fuel
costs
If the dehydration system becomes overloaded with water,
glycol can carry over from the contactor and/or still .
Sales gas specification may not be achieved
Free Water
Reduce the drying capacity of the glycol With water
present, can cause foaming
Undissolved oils can:
• Plug absorber trays
• Foul heat transfer surfaces in the reboiler
• Increase the viscosity of the glycol
• Light hydrocarbons can flash in the stripping column
and cause loss of glycol and/or damage to the packing
Oils or
Hydrocarbons
13. PROBLEMS CAUSED BY CONTAMINANTS
PROBLEMSCONTAMINANT
Dissolves into glycol
Corrodes steel, especially stainless steel
Deposits on reboiler fire tubes, causing hot spots and
firetube burnout
Brine
Cause foaming, corrosion, and, if they deposit on fire
tubes, hot spots
Downhole
Additives
Promote foaming
Erode valves and pumps
Eventually plug trays and packing
Solids
14. Mohamed Abdelraof Saad
Glycol Dehydration System Components
Contactor
Contactor towers contact the lean glycol with
the wet gas stream.
Scrubbing section in the bottom
Drying (mass transfer) section in the
middle
Glycol cooler and mist extractor in the top
16. Mohamed Abdelraof Saad
Contactor
Scrubbing Section :–
Scrubber integrated into the contactor
Wire mesh mist extractor.
This second stage of scrubbing further
minimizes the contamination of the
glycol and helps prevent the free water
from overloading the system.
18. Mohamed Abdelraof Saad
Contactor
Drying Section :
In the middle section of the
contactor, the gas stream flows
upward and thoroughly
contacts the downward flowing
lean glycol through valve trays,
bubble caps, or packing.
19. Mohamed Abdelraof Saad
Glycol cooler and mist extractor in the top
Its aim is to collect any
glycol droplets which
escape with dry gas to
avoid glycol losses
20. Mohamed Abdelraof Saad
Carryover
can result from
• foam build-up caused by
glycol contamination
• high gas rate. It will happen
continuously when the gas
rate is high enough to agitate
the liquid at the top tray so
that a foam forms that is too
thick for the mist eliminator to
handle.
21. Mohamed Abdelraof Saad
Glycol cooler
-It decrease lean glycol
temperature to
increase affinity of
glycol to absorb water
23. Mohamed Abdelraof Saad
Flash Drum Separator
A two-phase separator with a 5 to 10 minute liquid
retention time prevents excess hydrocarbon vapor
from entering the stripping column
25. Mohamed Abdelraof Saad
Filters
Cartridge filters remove solids, that is, corrosion products.
Activated carbon filters remove hydrocarbon impurities, for
example, well treating chemicals and compressor oils.
26. Mohamed Abdelraof Saad
Filters
• Activated carbon filters remove hydrocarbon impurities, for example, well
treating chemicals and compressor oils.
• They work well until their adsorption capacity is reached. In cases where
the glycol contains appreciable quantities of light hydrocarbons, they
must be changed frequently.
• Most glycol systems cannot be operated successfully without carbon
adsorption.
• There are two types of activated carbon filters.
• Most systems use a carbon canister; however, larger systems use a
loose fill carbon vessel. When the loose fill vessel is used, care must be
taken to trap carbon fines and keep them from entering the glycol
dehydration system. This is especially important when a fresh carbon
bed is put into service.
• Carbon filters should be replaced anytime the level of contaminants in
the glycol solution goes up.
• Monthly test should be run to determine the contamination level.
28. Mohamed Abdelraof Saad
Glycol Pump
Glycol circulation pumps contain the only moving parts in a
glycol dehydration system.
Electric-motor driven
High-pressure gas-operated
High-pressure liquid-operated
30. Mohamed Abdelraof Saad
Still Column
Reflux Coil :
The top of the still column contains a cooling coil that
condenses some of the steam rising from the reboiler.
Providing reflux for the column.
Packing
Still columns usually contain 4 to
8 ft of packing although some
large units use trays.
31. Mohamed Abdelraof Saad
Surge Tank (Accumulator)
The surge tank (accumulator) holds glycol to compensate
for fluctuations in the load on the glycol dehydration
systems
32. Mohamed Abdelraof Saad
OVERFLOW TUBE
The glycol level in the reboiler is maintained above the heating tube
by the location of the overflow tube.
The dried, purified glycol spills into the overflow tube and flows into
the surge tank.
33. Mohamed Abdelraof Saad
Stripping Gas
Adding a stripping gas to the still column increases the glycol
purity produced by the glycol reconcentrator from about
98.5% to 99.9%.
35. Mohamed Abdelraof Saad
Process/Design Variables
Gas Temperature
water content of the inlet gas increases as this
temperature is raised.
Glycol vaporization losses are also increased at the
higher temperature.
Problems can result from too low a temperature (below
50°F) because glycol becomes very viscous.
Lean Glycol Temperature
It should be kept at least 10°F above the inlet gas
temperature to minimize hydrocarbon condensation in
the absorber and subsequent foaming.
36. Mohamed Abdelraof Saad
Process/Design Variables
Glycol Reboiler Temperature
The reboiler temperature controls the concentration of the water in the
glycol.
The glycol concentration increases with higher reboiler temperatures.
The reboiler temperature should never be allowed to remain at or above
the glycol degradation temperatures.
When higher glycol concentrations are required, stripping gas can be
added to the reboiler..
Regenerator Top Temperature
A high temperature can increase glycol losses due to excessive
vaporization.
The recommended temperature in the top of the column is about 225°F.
If the temperature in the top of the column drops too low, too much water
can be condensed and washed back into the regenerator to flood the
column and fill the reboiler with excessive liquids.
37. Mohamed Abdelraof Saad
Process/Design Variables
Reboiler Pressure
Reducing the pressure in the reboiler at a constant
temperature results in higher glycol purity
Glycol Concentration
The water content of the dehydrated gas depends
primarily on the lean glycol concentration
Glycol Circulation Rate
The dew point depression of a saturated gas is a function
of the glycol circulation rate
A typical glycol circulation rate is about three gallons of
glycol per pound of water removed (seven maximum).