The document discusses experiments conducted to improve the efficiency of a ball mill. It outlines the objectives, which were to analyze the existing grinding system, optimize factors affecting efficiency, and generate a standard operating procedure. Experimental results showed that optimizing operating speed to 25 rpm, fill level to 80.6%, media size to 75mm, and adding a grinding aid reduced grinding time from 10-11 hours to 5 hours. Using a jaw or roll crusher to pre-crush feed materials before grinding also decreased grinding time. Based on the results, it was recommended to implement these optimized parameters and use cumi media in the ball mill.
This document discusses catalyst process technology for steam reforming of hydrocarbons. It covers the chemical reactions involved, catalyst design considerations like shape and chemistry, and carbon formation and removal. Key points discussed include the conversion of hydrocarbons to syngas, reforming and shift reactions, factors that influence methane conversion, reformer design, optimizing catalyst shape for heat transfer and pressure drop, using alkali-doped catalysts to prevent carbon formation, and tailored catalyst requirements.
Energy saving in urea plant by modification in heat exchanger and processPrem Baboo
Energy is the prime mover of economic growth and is vital to the sustenance of a modern economy. Improvement in energy
efficiency reduces cost of production & results in environmental benefits, e.g. mitigation of global warming by way of less emission of
Green house gases in the atmosphere. Over the years several energy conservation measures have been taken towards reduction in
specific energy consumption and improvement in energy efficiency. The efforts’ resulted in reduction in specific energy consumption
from 6.27G. Cal/tone of Urea to 5.421 G.Cal/tone of Urea in 2015-16 as shown in the Graph No 1 & 2 with energy & down time.
Further a major modification of all plants is under way. Most of the schemes have been implemented in 2012 and the further
modifications expected to result again reduction of energy consumption for ammonia and Urea plants. This paper described some of
the modification in urea plants implemented recently in May/June 2016.
The explosion hazard in urea process (1)Prem Baboo
The document discusses explosion hazards in the urea production process. Passivation air used in the reactor, stripper, and downstream equipment can form an explosive mixture with the small amount of hydrogen (0.14-0.2%) present in CO2. The HP scrubber is identified as a risky vessel where an explosive mixture could form. Triangular diagrams are used to show combustible and non-combustible gas mixtures. Test results from a fertilizer plant show that optimal oxygen levels are needed to avoid explosions while minimizing ammonia losses. Higher chromium stainless steel grades require less oxygen for passivation than lower grades.
Burner Design, Operation and Maintenance on Ammonia PlantsGerard B. Hawkins
The document discusses burner design, operation, and maintenance on ammonia plants. It covers reformer burner types and designs, including premix and staged burners. It also addresses combustion characteristics like excess air and fuel viscosity effects. Maintenance best practices like checking burner pressures and atomizing steam temperatures are emphasized. Low NOx equipment uses techniques like staged air, fuel, and flue gas recirculation to reduce emissions. Good combustion requires attention to design, operation, maintenance, and partnership among related roles.
Physical significance of non dimensional numbersvaibhav tailor
This document discusses four non-dimensional numbers that are used in heat transfer analysis:
The Nusselt number relates convective heat transfer to conductive heat transfer through a characteristic length and thermal conductivity. The Grashof number compares buoyancy and inertia forces to viscous forces in natural convection. The Prandtl number is the ratio of momentum diffusivity to thermal diffusivity, relating how a fluid conducts momentum and heat. The Reynolds number compares inertial to viscous forces, indicating flow regime from laminar to turbulent. These non-dimensional numbers provide insight into dominant transfer mechanisms in heat transfer problems.
Definition and Requirements
Types of Heat Exchangers
The Overall Heat Transfer Coefficient
The Convection Heat Transfer Coefficients—Forced Convection
Heat Exchanger Analysis
Heat Exchanger Design and Performance Analysis
Heat exchangers transfer heat from one fluid to another. There are two main types: tube-and-shell and plate. Tube-and-shell consists of tubes in a shell where fluids flow inside and outside the tubes. Plate heat exchangers use plates to separate fluids which flow between plates in alternating channels. Heat exchangers can operate in parallel, counter, or cross flow configurations. Performance tests determine the overall heat transfer coefficient and identify any fouling issues.
The document discusses experiments conducted to improve the efficiency of a ball mill. It outlines the objectives, which were to analyze the existing grinding system, optimize factors affecting efficiency, and generate a standard operating procedure. Experimental results showed that optimizing operating speed to 25 rpm, fill level to 80.6%, media size to 75mm, and adding a grinding aid reduced grinding time from 10-11 hours to 5 hours. Using a jaw or roll crusher to pre-crush feed materials before grinding also decreased grinding time. Based on the results, it was recommended to implement these optimized parameters and use cumi media in the ball mill.
This document discusses catalyst process technology for steam reforming of hydrocarbons. It covers the chemical reactions involved, catalyst design considerations like shape and chemistry, and carbon formation and removal. Key points discussed include the conversion of hydrocarbons to syngas, reforming and shift reactions, factors that influence methane conversion, reformer design, optimizing catalyst shape for heat transfer and pressure drop, using alkali-doped catalysts to prevent carbon formation, and tailored catalyst requirements.
Energy saving in urea plant by modification in heat exchanger and processPrem Baboo
Energy is the prime mover of economic growth and is vital to the sustenance of a modern economy. Improvement in energy
efficiency reduces cost of production & results in environmental benefits, e.g. mitigation of global warming by way of less emission of
Green house gases in the atmosphere. Over the years several energy conservation measures have been taken towards reduction in
specific energy consumption and improvement in energy efficiency. The efforts’ resulted in reduction in specific energy consumption
from 6.27G. Cal/tone of Urea to 5.421 G.Cal/tone of Urea in 2015-16 as shown in the Graph No 1 & 2 with energy & down time.
Further a major modification of all plants is under way. Most of the schemes have been implemented in 2012 and the further
modifications expected to result again reduction of energy consumption for ammonia and Urea plants. This paper described some of
the modification in urea plants implemented recently in May/June 2016.
The explosion hazard in urea process (1)Prem Baboo
The document discusses explosion hazards in the urea production process. Passivation air used in the reactor, stripper, and downstream equipment can form an explosive mixture with the small amount of hydrogen (0.14-0.2%) present in CO2. The HP scrubber is identified as a risky vessel where an explosive mixture could form. Triangular diagrams are used to show combustible and non-combustible gas mixtures. Test results from a fertilizer plant show that optimal oxygen levels are needed to avoid explosions while minimizing ammonia losses. Higher chromium stainless steel grades require less oxygen for passivation than lower grades.
Burner Design, Operation and Maintenance on Ammonia PlantsGerard B. Hawkins
The document discusses burner design, operation, and maintenance on ammonia plants. It covers reformer burner types and designs, including premix and staged burners. It also addresses combustion characteristics like excess air and fuel viscosity effects. Maintenance best practices like checking burner pressures and atomizing steam temperatures are emphasized. Low NOx equipment uses techniques like staged air, fuel, and flue gas recirculation to reduce emissions. Good combustion requires attention to design, operation, maintenance, and partnership among related roles.
Physical significance of non dimensional numbersvaibhav tailor
This document discusses four non-dimensional numbers that are used in heat transfer analysis:
The Nusselt number relates convective heat transfer to conductive heat transfer through a characteristic length and thermal conductivity. The Grashof number compares buoyancy and inertia forces to viscous forces in natural convection. The Prandtl number is the ratio of momentum diffusivity to thermal diffusivity, relating how a fluid conducts momentum and heat. The Reynolds number compares inertial to viscous forces, indicating flow regime from laminar to turbulent. These non-dimensional numbers provide insight into dominant transfer mechanisms in heat transfer problems.
Definition and Requirements
Types of Heat Exchangers
The Overall Heat Transfer Coefficient
The Convection Heat Transfer Coefficients—Forced Convection
Heat Exchanger Analysis
Heat Exchanger Design and Performance Analysis
Heat exchangers transfer heat from one fluid to another. There are two main types: tube-and-shell and plate. Tube-and-shell consists of tubes in a shell where fluids flow inside and outside the tubes. Plate heat exchangers use plates to separate fluids which flow between plates in alternating channels. Heat exchangers can operate in parallel, counter, or cross flow configurations. Performance tests determine the overall heat transfer coefficient and identify any fouling issues.
This document discusses heat exchangers, including their types, advantages, disadvantages, and applications. It describes the main types of heat exchangers as shell and tube, double pipe, plate type, and finned tube. Shell and tube heat exchangers are the most widely used due to their lower cost compared to plate type and ability to handle higher pressures than double pipe. Plate type heat exchangers offer higher efficiency but higher initial cost. Heat exchangers are commonly used in chemical, petrochemical, food, and other industrial processes to transfer heat between fluids.
Shell and Tube Heat Exchanger in heat TransferUsman Shah
Shell and tube heat exchangers consist of a bundle of tubes enclosed in a cylindrical shell. Fluids flow through either the tubes or shell to facilitate heat transfer between the two fluids. They are widely used in chemical processes due to their ability to achieve a large heat transfer surface area in a compact volume. Key components include tubesheets, baffles, support rods and segmented baffles which direct fluid flow across the tube bundle for efficient heat transfer. Design considerations include allocating the more corrosive or fouling fluid to the tubeside for easier cleaning and maintenance.
Computer aided process design and simulation (Cheg.pptxPaulosMekuria
knowledge-based system for conceptual design
3. Aspen Process Economic Analyzer: economic evaluation
of process alternatives, sensitivity analysis, optimization.
4. Aspen Batch: batch process design and scheduling.
5. Aspen Custom Modeler: object-oriented environment for
rigorous modeling of non-standard unit operations.
6. Aspen Process Optimization: steady state optimization
and dynamic optimization of processes.
7. Aspen PIMS: plant information management system.
8. Aspen Petroleum Supply Chain: supply chain modeling.
9. Aspen One: plant-wide real-time optimization.
10. Aspen InfoPlus.21: plant information management.
The document discusses heat transfer equipment and heat exchangers. It defines a heat exchanger as a device that transfers thermal energy between two or more fluids at different temperatures without mixing the fluids. Heat exchangers can be classified based on their transfer process, number of fluids, degree of surface compactness, construction, flow arrangement, and heat transfer mechanism. Common examples include shell-and-tube exchangers, radiators, condensers, evaporators, and cooling towers.
Waste heat recovery provides opportunities to improve energy efficiency in industrial processes. Capturing lost heat from exhaust gases, furnaces, and other equipment can provide an emission-free substitute for fuels and electricity. Existing technologies like recuperators and regenerators can often recover 10-50% of lost heat. Lower temperature waste heat below 400°F can also be recovered and used for space heating, hot water, or low temperature industrial processes. Challenges include the low temperature differences available, corrosion from flue gas condensation, and finding suitable end uses for the recovered heat. Advanced materials and designs are exploring ways to further improve waste heat recovery across a wide range of industrial applications.
HEAT EXCHANGERS. Heat exchangers are devices that facilitate the exchange of heat between two fluids that are at different temperature while keeping them from mixing with each other.
2. Double Pipe Heat Exchangers
3. A typical double pipe heat exchanger basically consists of a tube or pipe fixed concentrically inside a larger pipe or tube They are used when flow rates of the fluids and the heat duty are small (less than 5 kW) These are simple to construct, but may require a lot of physical space to achieve the desired heat transfer area.
4. Double-pipe exchangers is the generic term covering a range of jacketed 'U' tube exchangers normally operating in countercurrent flow of two types which is true double pipes and multitubular hairpins. One fluid flows through the smaller pipe while the other fluid flows through the annular space between the two pipes. Two types of flow arrangement: Parallel flow Counter flow
5. • The fluids may be separated by a plane wall but more commonly by a concentric tube (double pipe) arrangement shown in fig. If both the fluids move in the same direction, the arrangement is called a parallel flow type. In the counter flow arrangement the fluids move in parallel but opposite directions. In a double pipe heat exchanger, either the hot or cold fluid occupies the annular space and the other fluid moves through the inner pipe. The method of solving the problem using logarithmic mean temperature difference is typical and more iteration must be done. So it takes more time for the problem to solve. Therefore another method is practiced for solving this type of problems. This method is known as Effectiveness and Number of Transfer Units or simply ε-NTU method.“Effectiveness of heat exchangers is defined as actual heat transfer rate by maximum possible heat transfer rate”.The LMTD method may be applied to design problems for which the fluid flow rates and inlet temperatures, as well as a desired outlet temperature, are prescribed.
6. Application of Double Pipe Heat Exchanger Pasteurization or sterilization of food and bioproducts Condensers and evaporators of air conditioners Radiators for internal combustion engines Charge air coolers and intercoolers for cooling supercharged engine intake air of diesel engines.
Furnaces are used to heat materials and change their shape or properties. There are different types of furnaces classified by their heat source (combustion or electric), how material is charged (batch or continuous), and heat recovery methods. Efficient furnaces aim to uniformly heat materials to the desired temperature using minimal fuel and labor. Common furnace types include combustion furnaces fueled by oil, gas, or coal and electric furnaces. Continuous furnaces transport material through the furnace on conveyors, pushers, or walking beams and are used for steel reheating.
This document presents information about heat exchangers. It begins with an introduction that defines a heat exchanger as a device that brings two fluid streams into thermal contact to transfer heat from one to the other. It then discusses classifications of heat exchangers based on contact type, construction, flow arrangement, and surface compactness. Common heat exchangers like tubular, plate, and extended surface types are described. The document also covers flow arrangements like parallel, counter-current, and cross flow. It presents the heat transfer mechanisms and governing equation for heat exchangers and lists factors that influence efficiency such as temperature difference, conducting materials, fluid turbulence, velocity, and surface area.
This document provides an overview of Kern's method for designing shell-and-tube heat exchangers. It begins with objectives and an introduction to Kern's method. It then outlines the design procedure algorithm and provides an example application. The example involves designing an exchanger to sub-cool methanol condensate using brackish water as the coolant. The document walks through each step of the Kern's method design process for this example, including calculating properties, determining duties, selecting tube/shell parameters, and estimating heat transfer coefficients.
This document provides an overview of different types of heat exchangers. It begins with an introduction to heat exchangers and their basic functions. It then describes several common types of heat exchangers including recuperators, regenerators, plate heat exchangers, shell and tube heat exchangers, and fin tube heat exchangers. It also discusses potential problems with heat exchangers such as fouling and corrosion and provides some precautions and considerations for heat exchanger design and cost.
The document describes heat conduction through plane walls, cylinders, and spheres under steady-state conditions. It introduces the concepts of thermal resistance, resistance networks, and one-dimensional heat transfer. Equations are presented to calculate heat transfer rates and temperature distributions based on thermal properties and surface temperatures for multi-layered systems with conduction and convection. Special cases like contact resistance and critical insulation thickness are also covered.
The document discusses shell and tube heat exchangers. It describes shell and tube heat exchangers as consisting of a shell with tubes inside that allow two fluids to transfer heat between each other without mixing. It discusses the basic components and layout of shell and tube heat exchangers. Common types are also presented, including U-tube, straight-tube, and multi-pass configurations. Reasons for the popularity of shell and tube designs in process industries are their ability to provide a large surface area to volume ratio for heat transfer in an easily constructed form.
A heat exchanger transfers heat between two fluids or a fluid and a surface. It can be classified based on transfer processes, number of fluids, construction, heat transfer mechanisms, compactness, flow arrangement, number of passes, and surface type. Recuperators and regenerators are types of surface heat exchangers that transfer heat via convection between fluids separated by a thin wall. Direct contact heat exchangers transfer heat by partially or completely mixing hot and cold fluid streams. Standards from the Tubular Exchanger Manufacturers Association classify heat exchangers by size, denoted by shell diameter and tube length, and type, denoted by stationary head, shell, and rear head configuration.
The document discusses different types of heat exchangers: direct contact, direct transfer (recuperative), and storage (regenerative). Direct transfer type heat exchangers like shell and tube, plate and frame transfer heat continuously through a dividing wall without mixing fluids. Storage type heat exchangers temporarily store heat and transfer it between fluids. Common applications of shell and tube heat exchangers include food/beverage, marine, air processing, and chemicals. Plate heat exchangers are used for milk pasteurization and brine cooling. Storage heat exchangers are used in steel melting and blast furnaces.
The document is a lab report from a chemical engineering class at Koya University. It details an experiment conducted by 8 students to determine the cloud point and pour point of an oil sample. The introduction discusses cloud point and pour point theory. The procedure describes how the cloud point and pour point were measured using a thermometer, test jar, and cooling bath. The results table lists the cloud point and pour point temperatures measured for two samples. Discussions by each student analyze how adding hydrotropes or salt would affect the oil solution and why thermometer readings are important.
Pre-reforming
Flow-schemes
Feed-stocks
Catalyst handling, loading & start-up
Benefits of a pre-reformer
Case studies
Effects upon primary reformer
Data analysis
Reactor temperature profiles
Catalyst management
Summary
This document summarizes information from a workshop on implementing energy efficiency in re-heating furnaces in the steel industry. It discusses the types and components of furnaces, how they operate, best practices for efficient operation including maintaining the proper temperature, draft, capacity utilization, and using ceramic coatings. The document aims to educate on optimizing furnace efficiency to reduce energy use and costs in steel manufacturing.
The document summarizes the process for producing ammonia from natural gas and/or naphtha. Key steps include:
1) Desulphurization of the hydrocarbon feedstock using hydrogenation and ZnO absorption to remove sulfur.
2) Reforming the desulphurized feedstock with steam and air at high pressure and temperature in multiple reactors to produce synthesis gas containing hydrogen, nitrogen, carbon dioxide and carbon monoxide.
3) Purifying the synthesis gas through shift conversion and CO2/CO removal to increase hydrogen yield before sending the gas to the ammonia synthesis loop.
A heat exchanger transfers heat between two fluids that are separated by a conductive wall. It consists of tubes through which one fluid passes and a shell that holds the tubes for the other fluid. Heat is transferred from the hot to cold fluid through the tube walls. Common applications include cooling engine fluids, hydrocarbon processing, and waste heat recovery. Heat exchangers are designed through an iterative process of selecting configuration parameters, calculating heat transfer and pressure drop, and adjusting the design as needed.
The document describes the design and construction of heat exchangers. It discusses key components of double pipe heat exchangers like inner and outer pipes, return bends, and support lugs. It also explains components of shell and tube heat exchangers such as tubes, tube sheets, bonnets, channels, nozzles, baffles, and pass partition plates. Additionally, it covers classification of heat exchangers, flow arrangements, fouling factors, heat transfer calculations, and pressure drop analysis for heat exchanger design.
Heat exchangers allow the transfer of heat between two fluids without direct contact. The main types are shell-and-tube, plate, air-cooled, and spiral. Shell-and-tube exchangers consist of tubes in a shell and are the most common, used across many industries. Plate exchangers use corrugated plates clamped together with gaskets to direct fluid flow. Spiral and air-cooled exchangers provide alternatives for applications where fouling is a problem.
This document discusses heat exchangers, including their types, advantages, disadvantages, and applications. It describes the main types of heat exchangers as shell and tube, double pipe, plate type, and finned tube. Shell and tube heat exchangers are the most widely used due to their lower cost compared to plate type and ability to handle higher pressures than double pipe. Plate type heat exchangers offer higher efficiency but higher initial cost. Heat exchangers are commonly used in chemical, petrochemical, food, and other industrial processes to transfer heat between fluids.
Shell and Tube Heat Exchanger in heat TransferUsman Shah
Shell and tube heat exchangers consist of a bundle of tubes enclosed in a cylindrical shell. Fluids flow through either the tubes or shell to facilitate heat transfer between the two fluids. They are widely used in chemical processes due to their ability to achieve a large heat transfer surface area in a compact volume. Key components include tubesheets, baffles, support rods and segmented baffles which direct fluid flow across the tube bundle for efficient heat transfer. Design considerations include allocating the more corrosive or fouling fluid to the tubeside for easier cleaning and maintenance.
Computer aided process design and simulation (Cheg.pptxPaulosMekuria
knowledge-based system for conceptual design
3. Aspen Process Economic Analyzer: economic evaluation
of process alternatives, sensitivity analysis, optimization.
4. Aspen Batch: batch process design and scheduling.
5. Aspen Custom Modeler: object-oriented environment for
rigorous modeling of non-standard unit operations.
6. Aspen Process Optimization: steady state optimization
and dynamic optimization of processes.
7. Aspen PIMS: plant information management system.
8. Aspen Petroleum Supply Chain: supply chain modeling.
9. Aspen One: plant-wide real-time optimization.
10. Aspen InfoPlus.21: plant information management.
The document discusses heat transfer equipment and heat exchangers. It defines a heat exchanger as a device that transfers thermal energy between two or more fluids at different temperatures without mixing the fluids. Heat exchangers can be classified based on their transfer process, number of fluids, degree of surface compactness, construction, flow arrangement, and heat transfer mechanism. Common examples include shell-and-tube exchangers, radiators, condensers, evaporators, and cooling towers.
Waste heat recovery provides opportunities to improve energy efficiency in industrial processes. Capturing lost heat from exhaust gases, furnaces, and other equipment can provide an emission-free substitute for fuels and electricity. Existing technologies like recuperators and regenerators can often recover 10-50% of lost heat. Lower temperature waste heat below 400°F can also be recovered and used for space heating, hot water, or low temperature industrial processes. Challenges include the low temperature differences available, corrosion from flue gas condensation, and finding suitable end uses for the recovered heat. Advanced materials and designs are exploring ways to further improve waste heat recovery across a wide range of industrial applications.
HEAT EXCHANGERS. Heat exchangers are devices that facilitate the exchange of heat between two fluids that are at different temperature while keeping them from mixing with each other.
2. Double Pipe Heat Exchangers
3. A typical double pipe heat exchanger basically consists of a tube or pipe fixed concentrically inside a larger pipe or tube They are used when flow rates of the fluids and the heat duty are small (less than 5 kW) These are simple to construct, but may require a lot of physical space to achieve the desired heat transfer area.
4. Double-pipe exchangers is the generic term covering a range of jacketed 'U' tube exchangers normally operating in countercurrent flow of two types which is true double pipes and multitubular hairpins. One fluid flows through the smaller pipe while the other fluid flows through the annular space between the two pipes. Two types of flow arrangement: Parallel flow Counter flow
5. • The fluids may be separated by a plane wall but more commonly by a concentric tube (double pipe) arrangement shown in fig. If both the fluids move in the same direction, the arrangement is called a parallel flow type. In the counter flow arrangement the fluids move in parallel but opposite directions. In a double pipe heat exchanger, either the hot or cold fluid occupies the annular space and the other fluid moves through the inner pipe. The method of solving the problem using logarithmic mean temperature difference is typical and more iteration must be done. So it takes more time for the problem to solve. Therefore another method is practiced for solving this type of problems. This method is known as Effectiveness and Number of Transfer Units or simply ε-NTU method.“Effectiveness of heat exchangers is defined as actual heat transfer rate by maximum possible heat transfer rate”.The LMTD method may be applied to design problems for which the fluid flow rates and inlet temperatures, as well as a desired outlet temperature, are prescribed.
6. Application of Double Pipe Heat Exchanger Pasteurization or sterilization of food and bioproducts Condensers and evaporators of air conditioners Radiators for internal combustion engines Charge air coolers and intercoolers for cooling supercharged engine intake air of diesel engines.
Furnaces are used to heat materials and change their shape or properties. There are different types of furnaces classified by their heat source (combustion or electric), how material is charged (batch or continuous), and heat recovery methods. Efficient furnaces aim to uniformly heat materials to the desired temperature using minimal fuel and labor. Common furnace types include combustion furnaces fueled by oil, gas, or coal and electric furnaces. Continuous furnaces transport material through the furnace on conveyors, pushers, or walking beams and are used for steel reheating.
This document presents information about heat exchangers. It begins with an introduction that defines a heat exchanger as a device that brings two fluid streams into thermal contact to transfer heat from one to the other. It then discusses classifications of heat exchangers based on contact type, construction, flow arrangement, and surface compactness. Common heat exchangers like tubular, plate, and extended surface types are described. The document also covers flow arrangements like parallel, counter-current, and cross flow. It presents the heat transfer mechanisms and governing equation for heat exchangers and lists factors that influence efficiency such as temperature difference, conducting materials, fluid turbulence, velocity, and surface area.
This document provides an overview of Kern's method for designing shell-and-tube heat exchangers. It begins with objectives and an introduction to Kern's method. It then outlines the design procedure algorithm and provides an example application. The example involves designing an exchanger to sub-cool methanol condensate using brackish water as the coolant. The document walks through each step of the Kern's method design process for this example, including calculating properties, determining duties, selecting tube/shell parameters, and estimating heat transfer coefficients.
This document provides an overview of different types of heat exchangers. It begins with an introduction to heat exchangers and their basic functions. It then describes several common types of heat exchangers including recuperators, regenerators, plate heat exchangers, shell and tube heat exchangers, and fin tube heat exchangers. It also discusses potential problems with heat exchangers such as fouling and corrosion and provides some precautions and considerations for heat exchanger design and cost.
The document describes heat conduction through plane walls, cylinders, and spheres under steady-state conditions. It introduces the concepts of thermal resistance, resistance networks, and one-dimensional heat transfer. Equations are presented to calculate heat transfer rates and temperature distributions based on thermal properties and surface temperatures for multi-layered systems with conduction and convection. Special cases like contact resistance and critical insulation thickness are also covered.
The document discusses shell and tube heat exchangers. It describes shell and tube heat exchangers as consisting of a shell with tubes inside that allow two fluids to transfer heat between each other without mixing. It discusses the basic components and layout of shell and tube heat exchangers. Common types are also presented, including U-tube, straight-tube, and multi-pass configurations. Reasons for the popularity of shell and tube designs in process industries are their ability to provide a large surface area to volume ratio for heat transfer in an easily constructed form.
A heat exchanger transfers heat between two fluids or a fluid and a surface. It can be classified based on transfer processes, number of fluids, construction, heat transfer mechanisms, compactness, flow arrangement, number of passes, and surface type. Recuperators and regenerators are types of surface heat exchangers that transfer heat via convection between fluids separated by a thin wall. Direct contact heat exchangers transfer heat by partially or completely mixing hot and cold fluid streams. Standards from the Tubular Exchanger Manufacturers Association classify heat exchangers by size, denoted by shell diameter and tube length, and type, denoted by stationary head, shell, and rear head configuration.
The document discusses different types of heat exchangers: direct contact, direct transfer (recuperative), and storage (regenerative). Direct transfer type heat exchangers like shell and tube, plate and frame transfer heat continuously through a dividing wall without mixing fluids. Storage type heat exchangers temporarily store heat and transfer it between fluids. Common applications of shell and tube heat exchangers include food/beverage, marine, air processing, and chemicals. Plate heat exchangers are used for milk pasteurization and brine cooling. Storage heat exchangers are used in steel melting and blast furnaces.
The document is a lab report from a chemical engineering class at Koya University. It details an experiment conducted by 8 students to determine the cloud point and pour point of an oil sample. The introduction discusses cloud point and pour point theory. The procedure describes how the cloud point and pour point were measured using a thermometer, test jar, and cooling bath. The results table lists the cloud point and pour point temperatures measured for two samples. Discussions by each student analyze how adding hydrotropes or salt would affect the oil solution and why thermometer readings are important.
Pre-reforming
Flow-schemes
Feed-stocks
Catalyst handling, loading & start-up
Benefits of a pre-reformer
Case studies
Effects upon primary reformer
Data analysis
Reactor temperature profiles
Catalyst management
Summary
This document summarizes information from a workshop on implementing energy efficiency in re-heating furnaces in the steel industry. It discusses the types and components of furnaces, how they operate, best practices for efficient operation including maintaining the proper temperature, draft, capacity utilization, and using ceramic coatings. The document aims to educate on optimizing furnace efficiency to reduce energy use and costs in steel manufacturing.
The document summarizes the process for producing ammonia from natural gas and/or naphtha. Key steps include:
1) Desulphurization of the hydrocarbon feedstock using hydrogenation and ZnO absorption to remove sulfur.
2) Reforming the desulphurized feedstock with steam and air at high pressure and temperature in multiple reactors to produce synthesis gas containing hydrogen, nitrogen, carbon dioxide and carbon monoxide.
3) Purifying the synthesis gas through shift conversion and CO2/CO removal to increase hydrogen yield before sending the gas to the ammonia synthesis loop.
A heat exchanger transfers heat between two fluids that are separated by a conductive wall. It consists of tubes through which one fluid passes and a shell that holds the tubes for the other fluid. Heat is transferred from the hot to cold fluid through the tube walls. Common applications include cooling engine fluids, hydrocarbon processing, and waste heat recovery. Heat exchangers are designed through an iterative process of selecting configuration parameters, calculating heat transfer and pressure drop, and adjusting the design as needed.
The document describes the design and construction of heat exchangers. It discusses key components of double pipe heat exchangers like inner and outer pipes, return bends, and support lugs. It also explains components of shell and tube heat exchangers such as tubes, tube sheets, bonnets, channels, nozzles, baffles, and pass partition plates. Additionally, it covers classification of heat exchangers, flow arrangements, fouling factors, heat transfer calculations, and pressure drop analysis for heat exchanger design.
Heat exchangers allow the transfer of heat between two fluids without direct contact. The main types are shell-and-tube, plate, air-cooled, and spiral. Shell-and-tube exchangers consist of tubes in a shell and are the most common, used across many industries. Plate exchangers use corrugated plates clamped together with gaskets to direct fluid flow. Spiral and air-cooled exchangers provide alternatives for applications where fouling is a problem.
The document discusses the Klarex non-fouling heat exchanger, which prevents fouling from accumulating inside the tubes. It works by continuously circulating metallic anti-fouling particles with the fluid to prevent fouling from starting and to improve heat exchange. The particles are distributed uniformly through a multiple path system and their quantity can be adjusted. The Klarex exchanger remains clean indefinitely, requires no maintenance, and operates reliably for many years without interruption.
This document provides an introduction to fouling of heat exchangers. Fouling refers to the accumulation of unwanted deposits on heat exchanger surfaces, which reduces heat transfer efficiency. Deposits can include crystalline, biological, corrosion products or particulate matter depending on the fluid passing through. Fouling occurs due to a combination of the fluid constituents and operating conditions. Common foulants include inorganic materials, airborne dusts, waterborne solids and microorganisms. The book aims to provide a comprehensive review of fouling including fundamental science, models, practical design/operation approaches and cleaning techniques.
Heat exchangers are devices that transfer heat between two fluids to control the temperature of one fluid. There are various types of heat exchangers that differ based on their flow arrangement, surface compactness, construction technique, and whether they use direct or indirect contact between fluids. Common examples include shell and tube heat exchangers, which contain multiple tubes in a shell, and plate heat exchangers, which use metal plates to transfer heat. Coaxial heat exchangers consist of an inner corrugated tube within an outer tube to efficiently transfer heat between fluids flowing separately within the tubes.
There are four different designs of heat exchangers shell and tube, plate, regenerative, intermediate fluids or solids. The most typical type is shell and tube designs. This includes multiple finned tubes. One of fluids runs through tubes while other fluids runs over them, causing it to be heated or cooled. In plate exchangers fluids flows through battles.
01 17-12 itp tools training and other resources -pump-fan-motor focus panelPreston Roberts
The Advanced Manufacturing Office (AMO) within the U.S. Department of Energy provides resources and support to help U.S. manufacturers improve their energy efficiency and reduce costs. The AMO conducts research and development on advanced technologies and also supports technology deployment through tools, training, assessments and standards to facilitate adoption of energy efficient practices. The AMO website provides software tools, case studies, technical guides and information on energy management standards and certification programs to help companies save energy.
This document discusses heat transfer equipment and heat exchangers. It defines a heat exchanger as a device that transfers thermal energy between two or more fluids at different temperatures without mixing the fluids. Heat exchangers can be classified based on their transfer process, number of fluids, degree of surface compactness, construction, flow arrangements, and heat transfer mechanisms. Common types include shell and tube, plate and frame, extended surface, and regenerative heat exchangers. Heat exchangers have applications in industries like chemical plants, power production, and heating/cooling systems.
Some nice content for engineering freaks and people interested in the processes in which this special heat exchangers are used (industrial ventilation, gas transport & storage & extraction, rendering, diesel power, cooling and compression).
Fouling, in technical language, it is the general term of unwanted material which is accumulating on surfaces, such as inside pipes, machines or heat exchanger.
This training course is an introduction to the fouling mitigation technologies for heat exchangers like Shell & Tube heat exchangers, Air Cooled heat exchangers, and Compact Type heat exchangers. The course will provide details on the maintenance aspects of several heat exchanger types in relation to process and mechanical design. Many case studies will be presented to show failures, mismatches. The thermal and mechanical design aspect in relation to fouling behavior is conducted using sophisticated computer software based on HTRI software. Attendees will be oered problem case studies in order to reach solutions on their own.
A heat exchanger transfers heat between two fluids through tube walls. There are two main types: tubular and extended surface. Tubular exchangers include shell-and-tube, U-tube, and double pipe designs. Shell-and-tube exchangers contain tubes in a shell separated by baffles to direct flow. Heat is transferred through the tube walls from one fluid inside the tubes to the other outside. Manufacturing involves forming, welding, inspection, assembly, testing, and documentation. Materials, design, fabrication, and testing must meet codes and standards.
NUMERICAL METHODS IN STEADY STATE, 1D and 2D HEAT CONDUCTION- Part-IItmuliya
This document discusses numerical methods for solving steady-state 1D and 2D heat conduction problems. It describes the relaxation method, Gaussian elimination method, and Gauss-Siedel iteration method for solving systems of simultaneous algebraic equations arising in heat conduction analyses. The Gaussian elimination and matrix inversion methods use matrix operations to systematically eliminate variables. The Gauss-Siedel iteration method iteratively solves for each variable using the most recently calculated values of other variables until convergence is reached. Examples are provided to illustrate each numerical solution technique.
This document contains slides on transient heat conduction from a lecture. It discusses lumped system analysis where the internal conduction resistance is negligible compared to the surface convection resistance. For lumped systems, the temperature at any point in the solid varies only with time. It introduces the Biot and Fourier numbers which are used to determine if lumped system analysis can be applied for a given solid geometry and time. The temperature distribution equation for lumped systems is presented.
The document discusses the lumped element method (LEM) for analyzing transient heat transfer problems. It defines a lumped system as one where the interior temperature remains uniform over time. The lumped element approach provides a simplification to heat transfer calculations using a lumped parameter called the time constant. The document also covers using the method of separation of variables to solve the heat equation for transient conduction problems, reducing the partial differential equation to ordinary differential equations that can be solved. It provides an example of applying separation of variables to a one-dimensional conduction problem between fixed temperatures.
The document discusses heat conduction equations. It begins by stating the learning objectives, which are to explain heat transfer concepts and solve one-dimensional heat conduction problems. It then derives the general heat conduction equation for one-dimensional conduction in a plane wall or long cylinder. The equation relates the temperature gradient to heat generation and transient effects using variables like thermal conductivity, density and heat capacity.
This document provides an overview of centrifugal pump training, covering:
- Centrifugal pump theory and how pumps work using atmospheric pressure
- Common pump terms like head, static head, total head, and NPSH
- How to read centrifugal pump curves and understand a pump's operating range
- The information needed to submit a pump inquiry
- How to draw system curves to select the proper pump
- Parallel and series pump operation and cavitation causes
- Explaining NPSH and the affinity laws for pump speed and performance changes
- Troubleshooting pumps using pressure and vacuum gauges
The document provides an overview of an industrial training at Reliance Industries Limited's refinery in Jamnagar, India. It discusses the refining process, including fractional distillation of crude oil in atmospheric and vacuum distillation towers. Key components of an oil refinery are described, such as desalters, heat exchangers, storage tanks, pumps, compressors, and piping. Centrifugal pumps are commonly used and their components and operating characteristics like Net Positive Suction Head are explained. The training helped link the student's classroom knowledge to practical applications in industry.
Heat exchangers allow the transfer of heat between two or more fluids without mixing them. There are several types including shell and tube, plate, and finned tube. Heat exchangers can be classified based on their application (e.g. boilers, condensers), shape (e.g. double pipe, plate and frame), or fluid flow configuration (e.g. cocurrent, countercurrent, crossflow). Proper heat exchanger design and material selection depends on the application and fluids involved.
Power Plant Regenerative feed heating and design aspects of Feed Heaters.This is a ppt for beginners in Power Plant Engineering.Also discusses Heat Transfer and Rankine cycle.
This document discusses methods for assessing the energy performance of heat exchangers over time. It describes calculating the overall heat transfer coefficient U to determine if fouling or other issues have reduced efficiency. The procedure involves monitoring operating parameters, calculating thermal properties, and determining U by measuring the heat duty, surface area, and log mean temperature difference. An example application to a liquid-liquid exchanger is provided, comparing test data to design specifications to identify potential fouling issues.
ABSTRACT
Heat/light/electrical energy is out today’s necessity and has scarcity also. Energy conservation is key requirement of any industry at all times.
In general, industries use heat energy for conservation of raw material to finished product. The source of heat energy is generally saturated or super heated steam. The steam generation is common use one boiler with carity of fuels. Whatever may be the fuel the generation should be as economy as possible which adds to the product cost. Further the usage of steam and recycling steam condensate back to boiler is an art depending on plant layouts.
In this project the steam generator is water tube boiler fired with rice husk. The steam is transferred to the tyre/tube moulds where tyres/tubes are cured while the heat is rejected to the tyres the condensate forms and this condensate is put back to the boiler. While doing so the steam is also stopped back to boiler without rejecting complete heat to the product. This gets flashed into atmosphere at feed water tank. The science of separation of condensate from steam saves energy. Better the separation more the fuel conservation.
In the steam generator the fuel is burnt to heat the water and form steam. This fuel burnt flue gas carries lot of energy, out through chimney. Prior to exhausting through the heat left in flue need to be recovered, through heat recovery mechanisms’. In this project an air-preheater condensate heat recovery unit is the major energy consuming station.
1) The document analyzes heat transfer in a double pipe heat exchanger with helical tape inserts in the annulus of the inner pipe using computational fluid dynamics (CFD).
2) A 3D model is developed and simulations are run using the SST k-ω turbulent model to analyze how helical tape inserts influence heat transfer and pressure drop at different pitch lengths and Reynolds numbers.
3) The results show that helical tape inserts increase the heat transfer rate but also increase pressure drop due to flow disruption. Nusselt number and friction factor are found to correlate well with Reynolds number for enhancing heat transfer.
This document appears to be the introduction or cover page of a lab manual for a Heat Transfer lab course. It provides information about the university and engineering college where the course is taught, and lists the name and identification information for the student. It also lists the experiments that will be conducted in the lab course, including determining thermal conductivity, studying heat exchangers, measuring emissivity, and analyzing heat transfer through fins, composite walls, and during convection. The document provides an overview of the lab course and experiments but no detailed information.
Heat/light/electrical energy is out today’s necessity and has scarcity also. Energy conservation is key requirement of any industry at all times.
In general, industries use heat energy for conservation of raw material to finished product. The source of heat energy is generally saturated or super heated steam. The steam generation is common use one boiler with carity of fuels. Whatever may be the fuel the generation should be as economy as possible which adds to the product cost. Further the usage of steam and recycling steam condensate back to boiler is an art depending on plant layouts.
In this project the steam generator is water tube boiler fired with rice husk. The steam is transferred to the tyre/tube moulds where tyres/tubes are cured while the heat is rejected to the tyres the condensate forms and this condensate is put back to the boiler. While doing so the steam is also stopped back to boiler without rejecting complete heat to the product. This gets flashed into atmosphere at feed water tank. The science of separation of condensate from steam saves energy. Better the separation more the fuel conservation.
In the steam generator the fuel is burnt to heat the water and form steam. This fuel burnt flue gas carries lot of energy, out through chimney. Prior to exhausting through the heat left in flue need to be recovered, through heat recovery mechanisms’. In this project an air-preheater condensate heat recovery unit is the major energy consuming station.
The document discusses the steps for designing a heat exchanger. It begins by introducing the basic heat exchanger equation that relates heat transfer rate, surface area, and temperature difference. It then outlines 14 steps for heat exchanger design, which include: 1) assuming tube dimensions and material, 2) fouling factors, 3) tube material properties, 4) determining temperature points, 5) calculating the log mean temperature difference, 6) correction factors, 7) mean temperature difference, 8) heat transfer coefficient, 9) required surface area, 10) number of tubes, 11) tube pitch and bundle diameter, 12) floating head type, 13) shell diameter, and 14) baffle spacing. The goal is to use these steps
This document discusses heat exchangers, including their types, performance parameters, and design methodologies. It introduces the log mean temperature difference method for relating heat transfer rate to inlet/outlet temperatures. It also describes the effectiveness-NTU method, where effectiveness is defined as the ratio of actual to maximum possible heat transfer, and NTU is the number of transfer units. Sample problems demonstrate the use of these methods to determine required surface areas, heat transfer rates, and outlet temperatures for given heat exchanger configurations and operating conditions.
Recognize numerous types of heat exchangers, and classify them.
Develop an awareness of fouling on surfaces, and determine the overall heat transfer coefficient for a heat exchanger.
Perform a general energy analysis on heat exchangers.
Obtain a relation for the logarithmic mean temperature difference for use in the LMTD method, and modify it for different types of heat exchangers using the correction factor.
Develop relations for effectiveness, and analyze heat exchangers when outlet temperatures are not known using the effectiveness-NTU method.
Know the primary considerations in the selection of heat exchangers.
Numerical Modeling and Simulation of a Double Tube Heat Exchanger Adopting a ...IJERA Editor
This document presents a numerical model and simulation of a double tube heat exchanger using a "black box" approach. It first uses commercial CFD software to simulate the heat exchanger and generate outlet temperature results. It then develops a linear model to predict the outlet temperatures based on governing equations, considering the heat exchanger a black box. The linear model assumes steady state, constant properties, and approximates the logarithmic mean temperature difference with an arithmetic mean. Results from both methods are generated and compared to experimental data to validate the linear approximation. Comparisons show the linear model agrees well with experiments, justifying its use to analyze double tube heat exchangers.
High Pressure Die Casting Cooling calculation with application of ThermodynamicsIRJET Journal
This document discusses calculations for cooling channel design in high pressure die casting tools. It begins with an overview of high pressure die casting and importance of cooling. Thermodynamic principles of heat transfer via conduction, convection and radiation are explained. Equations for heat transfer rate via different modes are provided. An example calculation is presented for a die casting tool producing an aluminum contactor housing. Total heat input, weight of molten aluminum, and heat transfer coefficients are calculated. Based on the calculations, cooling channel length and depth are determined as 299.53mm and 15.23mm for the moving side, and 258.74mm and 22.56mm for the fixed side. This resolves prior soldering issues.
This document discusses estimating the hottest spot temperature in power transformer windings using different cooling methods. It presents the mathematical formulation of the heat conduction equation for solving temperature distribution numerically using the finite element method. The selected model is a 32MVA transformer with two cooling methods: Non-Directed Oil-Forced (NDOF) cooling and Directed Oil-Forced (DOF) cooling. Equations are provided for calculating heat transfer coefficients, boundary conditions, and temperature gradients needed to solve the heat conduction equation.
This document describes a computational and experimental investigation of fluid flow and heat transfer through a shell and tube heat exchanger. A group of students simulated the heat exchanger using ANSYS software to study heat transfer in counter and parallel flow configurations with and without baffles. The simulation results showed increased effectiveness when baffles were used and in counter flow. The simulated results agreed well with experimental data and heat transfer concepts. Future work is proposed to study pressure drop and varying baffle designs.
The document provides details on the design and construction of shell and tube heat exchangers. It describes the key components of a shell and tube heat exchanger including the shell, tubes, tube sheets, bonnet, channel, pass partition plates, nozzles, baffles, tie rods, and flanges. It also explains the functions of each component and provides examples of different types of components like baffles, joints between tubes and tube sheets, and impingement plates.
This document discusses heat exchangers and their analysis. It begins by listing the objectives of classifying heat exchangers, determining heat transfer coefficients, and analyzing heat exchangers using effectiveness-NTU and LMTD methods. Several types of heat exchangers are then described, including compact, shell-and-tube, regenerative, plate-frame, and condensers/boilers. Methods for determining overall heat transfer coefficient and fouling factors are provided. The document concludes by explaining the LMTD and effectiveness-NTU methods for analyzing heat exchangers.
Optimization of a Shell and Tube Condenser using Numerical MethodIJERA Editor
The purpose of this study was to investigate the effect of installation of the tube external surfaces, their parameter and variable in a shell-and-tube condenser. Variation of heat transfer coefficient with each variable of shell and tube condenser was measured each test. The optimization tube outside diameter size was analyzed and use extended surface area attached tube with tube material and tube layout and arrangement (Number of tube a triangular or hexagonal arrangement) on shell-and tube condenser. The computer programming was used to get faster output in less time. Results suggest that mean heat transfer coefficient in variable condition were mainly at velocity is fixed. And also average additional surfaces and tube layout and the arrangement comparison with the quantity of the heat transfer.
The document describes heat exchangers and experiments conducted using a shell and tube heat exchanger and a plate heat exchanger. It discusses three types of fluid flow - parallel, counter, and cross-flow. Experiments were conducted with both exchangers under parallel and counter-flow configurations. Temperature and flow rate data was collected and used to calculate effectiveness, heat transfer coefficients, and log mean temperature difference. The results showed that the counter-flow configuration had higher effectiveness compared to parallel flow in both exchangers.
Heat transfer laboratory HEAT EXCHANGERSoday hatem
1. The document discusses heat exchangers and describes an experiment using a shell and tube heat exchanger. The objectives are to evaluate heat transfer coefficients, LMTD, heat transfer, and heat loss. Water is used as the hot and cold fluids flowing in counter-current configuration.
2. Key aspects covered include types of heat exchangers, theory behind heat transfer calculations, experimental procedures, results which did not match theory due to bubbles, and conclusions that objectives were still met despite non-ideal results.
3. The shell and tube heat exchanger uses water, with hot water inside tubes and cold water in the shell space. Heat is transferred between the streams in counter-current flow. Calculations
This document discusses the advantages of considering compact heat exchangers like plate-and-frame exchangers early in the process design stage. Plate-and-frame exchangers can be significantly smaller than traditional shell-and-tube exchangers while meeting the same heat transfer needs. Specifying design requirements without considering the characteristics of different exchanger types can lead to oversized and more expensive designs. Charts are provided to help estimate the required area of plate-and-frame exchangers for preliminary sizing.
This document discusses the advantages of considering compact heat exchangers like plate-and-frame exchangers early in the process design stage. Plate-and-frame exchangers can be significantly smaller than traditional shell-and-tube exchangers while meeting the same heat transfer needs. Specifying design requirements without considering the unique capabilities of different exchanger types can lead to oversized and more expensive designs. Charts are provided to help estimate the required area of plate-and-frame exchangers for preliminary sizing.
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This is a prior version, please see: https://www.slideshare.net/slideshow/ai-explanations-as-two-way-experiences-led-by-users-5e6d/269981688
In human communication, explanations serve to increase understanding, overcome communication barriers, and build trust. They are, in most cases, dialogues. In computer science, AI explanations (“XAI”) map how an AI system expresses underlying logic, algorithmic processing, and data sources that make up its outputs. One-way communication.
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Heat exchanger training 02. 25. 15
1. Process Training - Heat Exchanger
Heat Exchanger Calculations
By Sharon Wenger
February 26, 2015
1
2. Overview
Introduction
Basic Heat Transfer
Conduction
Convection
Radiation
Types of Exchangers
Shell & Tube
Hairpin
Plate & Frame
Brazed Plate
Welded Plate
Finned Tube TEMA Heat Exchangers
Heat Transfer Calculation Formulas
General
Sensible Heating or Cooling of Fluids
Steam Condensing
Heating of Cooling a Solid
Terminology and Definitions
Working Problems
Work Example 1 - Shell and Tube Heat Exchanger Calculation
Work Example 2 - Mozambique LNG PJ FEED - DeC2 OVHD Condenser (251-E-1006)
2
3. Basic Heat Transfer
There are three forms of heat transfer.
Conduction
Convection
Radiation
Conduction
Heat flow through a solid medium due to the temperature
difference across the solid. The temperature difference is the
driving force for heat transfer.
Conduction heat transfer is governed by Fourier's Law
Where k is the thermal conductivity (W/m.K) and is a
characteristic of the wall material. The minus sign is a
consequence of the fact that heat is transferred in the
direction of decreasing temperature.
3
7. Fouling
Over a period of time, deposits or coatings form on the tube surfaces. This is called
fouling or scaling of heat exchangers. The deposits usually have low thermal conductivity
and offer additional high conductive resistance to heat transfer. This additional resistance
reduces the overall heat transfer coefficient for the exchanger. Therefore, the fouling
resistance factor also known as dirt resistance (Rd) is added to the overall coefficient
under clean conditions to obtain the overall coefficient under service conditions
7
8. What is Heat Exchanger
Heat exchangers are equipment that facilitate heat transfer between fluids. The heat transfer surface
area is either the inner or outer surface area of the inside pipe, depending on which is chosen as the
reference.
8
15. Temperature Difference
FT is the LMTD correction factor. The value of FT is depends upon the stream
inlet and outlet temperatures and the exchanger geometry
16. Approach of a Temperature Difference (ATD)
16
What is Approach of a Temperature Difference (ATD)
That is to transfer heat from the refrigerant coolant
temperature difference between the tow, and that is the
approach of a temperature difference, Shown in Fig. below. It
must be large enough to provide a flow of heat, necessary to
achieve the required system capacity.
17. Main heat transfer equation
Q = UAΔTm
where,
Q = rate of heat transfer
U = mean overall heat transfer coefficient
A = heat transfer surface area
ΔTm = logarithmic mean temperature difference
Q = m Cp T
Q = rate of heat transfer, Btu/hr
m = flow rate, pounds/hr
Cp = heat capacity, Btu/pound/F
T = temperature change, F
Q = mphase_change
Q = rate of heat transfer, Btu/hr
mphase_change = mass that changes phase, pounds/hr
= heat of vaporization, Btu/pound
17
19. Estimating Heat Transfer Calculation Formulas
19
Most of the formula listed below are “rules of thumb” for quick estimation purposes
and are limited in their application. The estimation is under standard temperatures and
pressures.
20. “Quick” Heat Transfer Calculation Formulas – for Estimation
General
Liquid:
20
–
Btu
hr
= kW × 3412 = HP × 2544
–
Lbs
hr
= GPM x Density 8.022 = GPM × 501.375 × Specific Gravity
Specific Gravity = Density/62.4 Psia = Psig+14.7
–
Btu
hr
= Tons of Refrigeration × 12000
–
Btu
hr
= Evaporative Cooling Tower Tons x 15000
– SCFM of air = [ACFM x (psig + 14.7) x 528] / [(Temp + 460) x 14.7]
– SCFM of air = Lbs/ Hr of air / 4.5 (at atmospheric temperature and pressure)
21. Heat Transfer Calculation Formulas
Sensible Heating or Cooling of Fluids
21
– Btu/hr = Lbs./ Hr × Specific Heat × Specific Gravity × Temp Rise (K)
– Btu/hr = GPM × Temp Rise x K
water = 500 K
30% glycol = 470 K
40% glycol = 450 K
50% glycol = 433K
hydraulic oil = (210 – 243) K
– For Air, Btu/hr = 1.085 x SCFM × Temp Rise
22. Heat Transfer Calculation Formulas
Steam Condensing
22
Btu/hr = Lbs./ Hr x Latent Heat
Heating or cooling a solid
Btu/hr for Solids = Lbs./Hr x Specific Heat x Delta-T
23. Work Example 1 - Shell and Tube Heat Exchanger Calculation
23
Solved Example 1:
Given:
24. Work Example 1 - Shell and Tube Heat Exchanger Calculation
24
Find:
25. Work Example 1 - Shell and Tube Heat Exchanger Calculation
25
Solve Steps:
28. Work Example 1 - Shell and Tube Heat Exchanger Calculation
28
29. Work Example 1 - Shell and Tube Heat Exchanger Calculation
29
30. Work Example 1 - Shell and Tube Heat Exchanger Calculation
30
31. Work Example 1 - Shell and Tube Heat Exchanger Calculation
31
32. Work Example 1 - Shell and Tube Heat Exchanger Calculation
32
33. Work Example 1 - Shell and Tube Heat Exchanger Calculation
33
34. Working Problem 2 –
Mozambique LNGFEED - DeC2 OVHD Condenser (251-E-1006)
Do we have to have all the required information to design a heat
exchanger? Not necessary. That is where we use the quick calculation
formulas to design it
Example 2 - Working Problem from Mozambique LNG FEED - DeC2
OVHD Condenser (251-E-1006)
34
35. What are the Min Information Req. to Design a Heat Exchanger
Depends
1) Pre-FEED
2) FEED
3) EPC detailed design.
In case 1) and 2) we only have minimum amount of information,
can we prepare a quick budget design? Yes!
In case 3) we have all the detail information to design for a
particular application, by using program such as HTRI will help us
optimize a design result.
35
36. Information Required to Design a Heat Exchanger
Fluid Properties
1. Fluid Composition and Percentage
2. Specific Heat
3. Viscosity, cp
4. Specific Gravity or Density
5. Thermal Conductivity
6. Latent Heat, (if phase change)
7. Operating Pressure and Temperature
Support Information
1. Allowable Pressure Drop
2. Fouling Factor
3. Design Pressure
4. Design Temperature
36
37. Work Example 2 - Mozambique LNG FEED – Deethanizer OVHD Condenser (251-
E-1006)
Steps to solve the problem
1. Gather all the Information Required to
Design a Heat Exchanger
2. PFD
3. HMB
4. Find the streams in and out to the
Exchanger
37
Calculated
What information are available?
38. Approach of a Temperature Difference (ATD)
Condensate Supply Temp. (°C) = achieve T (-16) – rise T (-3) – ATD (-3) = -22.3 (°C)
38
Streams
Hot Side Cold Side
112 113 374 375
Temperature [C] -0.14 -16.3 -22.3 -19.3
Pressure [bara] 26.7 26.7 2.5 2.5
Mass Flow [kg/h] 3980 3980 4500 4500
39. Calculate Heat Exchanger Duty Required
39
Streams 1 2 3 4
Temperature [C] tc1
tc2
Th1
Th2
-0.14 -16.3 -22.3 -19.3
Pressure [bara] 26.7 26.7 2.5 2.5
Mass Flow [kg/h] 3980 3980 4500 4500
ΔTLM
(°C) 11.35
UA (Kw/°C) 33 - 40 From Go-By
For UA = 33 Q (Kw) = 375
For UA = 40 Q (Kw) = 454
Result UniSim Results
Q = UA ΔTLM
The Purpose of this course is to review the fundamental basic heat transfer forms and heat transfer equations.
The goal is to achieve sizing heat exchangers with minimum available information by using the basic heat transfer equations.
What are we going to cover today?
We will cover next page
Basic Heat Transfer
Types of Exchangers
Heat Transfer Calculation Formulas
Working Problems
Lets first review basic heat transfer – next page
How many forms of heat transfer?
As we learned in school-There are three forms of heat transfer
There are
Conduction
Convection
Radiation
I am not going to read and explain all this three forms, you may read them late. The purpose I am showing here is to show you how the heat transfer equations are derived.
These are the basic fundamental equations
When we sized the heat exchanger we need to make sure to check that the U clean is greater than U dirty. Normally the ratio at least is 1.1
Now we have refreshed heat transfer basics , here is the picture of shell and tube heat exchanger. It shows you how the heat transfer happens between Hot and cold sides
In order to size heat exchanger correctly, we need to know what type of exchanger we are designing,
Here are the basic Types of Heat Exchangers
In the oil and gas industry we use TEMA Types as a standard design
Remember there are many parts attached to heat exchanger. They are all need to take consideration. But not in this course.
The basic flow Patten are 1) parallel flow or 2) counter –flow.
Here schematic to show how to do log mean temperature difference calculation
Obtaining the Ft correction factor can be found in GPSA Book.
The graph can be found in GPSA Chapter 9 for shell and tube exchangers. Chapter 10 for Air Coolers,
This slide shows you how to read the graph to find Ft correction factor.
The other important factor we need to consider for sizing heat exchanger is Approach of a temperature difference. This number you can find in the basis of design document.
Now we know all about heat transfers. The real work is to design a heat exchanger. By doing that we need to know which equation we need to use.
There are the main heat transfer equations
In process calculation we always have to check material balance and heat balance. The above equation is used to check heat balance. Then to find out either process missing variable or utility variable.
The equations I am going to show you today are rules of thumb for quick estimation or check purposes.
In order to size heat exchanger, what do we need to know?
types of the fluids,
heat transfer surface area and
forms of heat transfer
We are often asked what information we require to design a heat exchanger. It depends on the project phases
Do we have to have all the required information to design a heat exchanger? Not necessary. That is where we use the quick calculation formulas to design it
Information Required to Design a Heat Exchanger
1) Any program or excel spreadsheet requires all the above information
In this case PFDs.
First We need to know what is the Approach of a Temperature Difference (ATD). This information is from licensor. In the basis of design