This presentation is to show how to design heat exchanger from process simulation data to complete mechanical design by using two software HTRI and COMPRESS in seamless streamline Auto duping data.
This document discusses various thermodynamic diagrams used for boiler calculations, including:
- Temperature-heat (T-Q) diagrams which show the heat transfer characteristics of heat exchangers and boiler components.
- Temperature-entropy (T-s) diagrams which represent the phases of steam/water and can display steam processes.
- Pressure-enthalpy (p-h) diagrams which make it easy to visualize the heat load shares on different boiler surfaces.
- Enthalpy-entropy (Mollier) diagrams which allow determining steam properties from two known parameters like pressure and temperature.
These diagrams provide useful visualization tools for designing and analyzing boiler performance and steam processes.
Heat exchangers transfer thermal energy between two or more fluids at different temperatures. They are classified based on their transfer process, geometry, heat transfer mechanism, and flow arrangement. Shell-and-tube heat exchangers consist of a set of tubes in a shell container and are the most important type, used across many industries. Their design involves calculating the heat transfer rate, selecting appropriate materials and geometry, and ensuring optimal fluid velocities and pressure drops within design limits.
The document discusses heat exchangers, which transfer heat from one medium to another. It classifies heat exchangers based on their processes, fluid motion direction, mechanical design, and physical state of fluids. It then describes several common types of heat exchangers - shell and tube, plate, adiabatic wheel, plate fin, and pillow plate. It notes that shell and tube exchangers use tubes to transfer heat between two fluids, while plate exchangers use thin stacked plates. Heat exchangers have applications in engines, industries like oil/gas and chemicals, power generation, and HVAC systems like air conditioners and furnaces.
Boiler feed and pump sizing c-b and grundfos july 2016(1)lorenzo Monasca
Presentacion realizada por la empresa Cleaver Brooks y Grundfos
Pasos a seguir de como seleccionar una bomba de agua de alimentacion a una caldera de media presion.
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.
This document presents a rule-of-thumb design procedure for wet cooling towers that can be used for power plant cycle optimization. It begins with defining the design problem and specifying inlet/outlet water temperatures and ambient wet-bulb temperature. It then provides methods to calculate the outlet air temperature, tower characteristic, loading factor, and other key parameters. These include using the average of inlet/outlet water temperatures to approximate outlet air temperature, graphically integrating the Merkel equation to determine tower characteristic, and using graphs to determine the optimum loading factor based on design conditions. The goal is to provide simplified methods for estimating cooling tower dimensions, performance, costs and other details needed for power plant analysis without requiring detailed iterative design calculations.
A heat exchanger transfers heat between two fluids. There are various types including shell and tube, plate and frame, and air cooled. A shell and tube heat exchanger consists of tubes, a shell, baffles, and nozzle inlets and outlets. Proper design of the baffle cut, spacing, and orientation is important for efficient heat transfer and to prevent bypass and leakage streams from reducing effectiveness. Sealing strips are also used to block leakage paths and improve performance.
CENTRIFUGAL COMPRESSOR SETTLE OUT CONDITIONS TUTORIALVijay Sarathy
Centrifugal Compressors are a preferred choice in gas transportation industry, mainly due to their ability to cater to varying loads. In the event of a compressor shutdown as a planned event, i.e., normal shutdown (NSD), the anti-surge valve is opened to recycle gas from the discharge back to the suction (thereby moving the operating point away from the surge line) and the compressor is tripped via the driver (electric motor or Gas turbine / Steam Turbine). In the case of an unplanned event, i.e., emergency shutdown such as power failure, the compressor trips first followed by the anti-surge valve opening. In doing so, the gas content in the suction side & discharge side mix.
Therefore, settle out conditions is explained as the equilibrium pressure and temperature reached in the compressor piping and equipment volume following a compressor shutdown
Centrifugal Compressors
SECTION ONE - ANTI-SURGE PROTECTION AND THROUGHPUT REGULATION
0 INTRODUCTION
1 SCOPE
2 MACHINE CHARACTERISTICS
2.1 Characteristics of a Single Compressor Stage
2.2 Characteristic of a Multiple Stage Having More
Than One Impeller
2.3 Use of Compressor Characteristics in Throughput
Regulation Schemes
3 MECHANISM AND EFFECTS OF SURGE
3.1 Basic Flow Instabilities
3.2 Occurrence of Surge
3.3 Intensity of Surge
3.4 Effects of Surge
3.5 Avoidance of Surge
3.6 Recovery from Surge
4 CONTROL SCHEMES INCLUDING SURGE PROTECTION
4.1 Output Control
4.2 Surge Protection
4.3 Surge Detection and Recovery
5 DYNAMIC CONSIDERATIONS
5.1 Interaction
5.2 Speed of Response of Antisurge Control System
6 SYSTEM EQUIPMENT SPECIFICATIONS
6.1 The Antisurge Control Valve
6.2 Non-return Valve
6.3 Pressure and flow measurement
6.4 Signal transmission
6.5 Controllers
7 TESTING
7.1 Determination of the Surge Line
7.2 Records
8 INLET GUIDE VANE UNITS
8.1 Application
8.2 Effect on Power Consumption of the Compressor
8.3 Effect of Gas Conditions, Properties and Contaminants
8.4 Aerodynamic Considerations
8.5 Control System Linearity
8.6 Actuator Specification
8.7 Avoidance of Surge
8.8 Features of Link Mechanisms
8.9 Limit Stops and Shear Links
APPENDICES
A LIST OF SYMBOLS AND PREFERRED UNITS
B WORKED EXAMPLE 1 COMPRESSOR WITH VARIABLE INLET PRESSURE AND VARIABLE GAS COMPOSITION
C WORKED EXAMPLE 2 A CONSTANT SPEED ~ STAGE COMPRESSOR WITH INTER-COOLING
D WORKED EXAMPLE 3 DYNAMIC RESPONSE OF THE ANTISURGE PROTECTION SYSTEM FOR A SERVICE AIR COMPRESSOR RUNNING AT CONSTANT SPEED
E EXAMPLE OF INLET GUIDE VANE REGULATION
FIGURES
2.1 TYPICAL COMPRESSOR STAGE CHARACTERISTIC PLOTTED WITH FLOW AT DISCHARGE CONDITIONS
2.2 TYPICAL COMPRESSOR STAGE CHARACTERISTIC PLOTTED WITH FLOW AT INLET CONDITIONS
2.3 PERFORMANCE CHARACTERISTICS OF A COMPRESSOR STAGE AT VARYING SPEEDS
2.4 SYSTEM WORKING POINT DEFINED BY INTERSECTION OF PROCESS AND COMPRESSOR CHARACTERISTICS
2.5 DISCHARGE THROTTLE REGULATION
2.6 BYPASS REGULATION
2.7 INLET THROTTLE REGULATION
2.8 INLET GUIDE VANE REGULATION
2.9 VARIABLE SPEED REGULATION
3.1 GAS PULSATION LEVELS FOR A CENTRIFUGAL COMPRESSOR
3.2 REPRESENTATION OF CYCLIC FLOW DURING SURGE OF LONG PERIOD
3.3 TYPICAL WAVEFORM OF DISCHARGE PRESSURE DURING SURGE
3.4 MULTIPLE SURGE LINE FOR A MULTISTAGE CENTRIFUGAL COMPRESSOR
3.5 TYPICAL MULTIPLE SURGE LINES FOR SINGLE STAGE AXIAL-FLOW COMPRESSOR
4.1 GENERAL SCHEMATIC FOR COMPRESSORS OPERATING IN PARALLEL TO FEED MULTIPLE USER PLANTS
4.2 ILLUSTRATION OF SAFETY MARGIN BETWEEN SURGE POINT AND SURGE PROTECTION POINT AT WHICH ANTISURGE SYSTEM IS ACTIVATED
4.3 ANTISURGE SYSTEM FOR COMPRESSOR WITH FLAT PERFO ..........
DESIGN OF VENT GAS COLLECTION AND DESTRUCTION SYSTEMS Gerard B. Hawkins
DESIGN OF VENT GAS COLLECTION AND DESTRUCTION SYSTEMS
CONTENTS
1 INTRODUCTION
1.1 Purpose
1.2 Scope of this Guide
1.3 Use of the Guide
2 ENVIRONMENTAL ISSUES
2.1 Principal Concerns
2.2 Mechanisms for Ozone Formation
2.3 Photochemical Ozone Creation Potential
2.4 Health and Environmental Effects
2.5 Air Quality Standards for Ground Level Concentrations of Ozone, Targets for Reduction of VOC Discharges and Statutory Discharge Limits
3 VENTS REDUCTION PHILOSOPHY
3.1 Reduction at Source
3.2 End-of-pipe Treatment
4 METHODOLOGY FOR COLLECTION & ASSESSMENT OF PROCESS FLOW DATA
4.1 General
4.2 Identification of Vent Sources
4.3 Characterization of Vents
4.4 Quantification of Process Vent Flows
4.5 Component Flammability Data Collection
4.6 Identification of Operating Scenarios
4.7 Quantification of Flammability Characteristics for Combined Vents
4.8 Identification, Quantification and Assessment of Possibility of Air Ingress Routes
4.9 Tabulation of Data
4.10 Hazard Study and Risk Assessment
4.11 Note on Aqueous / Organic Wastes
4.12 Complexity of Systems
4.13 Summary
5 SAFE DESIGN OF VENT COLLECTION HEADER SYSTEMS
5.1 General
5.2 Process Design of Vent Headers
5.3 Liquid in Vent Headers
5.4 Materials of Construction
5.5 Static Electricity Hazard
5.6 Diversion Systems
5.7 Snuffing Systems
6 SAFE DESIGN OF THERMAL OXIDISERS
6.1 Introduction
6.2 Design Basis
6.3 Types of High Temperature Thermal Oxidizer
6.4 Refractories
6.5 Flue Gas Treatment
6.6 Control and Safety Systems
6.7 Project Program
6.8 Commissioning
6.9 Operational and Maintenance Management
APPENDICES
A GLOSSARY
B FLAMMABILITY
C EXAMPLE PROFORMA
D REFERENCES
DOCUMENTS REFERRED TO IN THIS PROCESS GUIDE
TABLE
1 PHOTOCHEMICAL OZONE CREATION POTENTIAL REFERENCED
TO ETHYLENE AS UNITY
FIGURES
1 SCHEMATIC OF TYPICAL VENT COLLECTION AND THERMAL OXIDIZER SYSTEM
2 TYPICAL KNOCK-OUT POT WITH LUTED DRAIN
3 SCHEMATIC OF DIVERSION SYSTEM
4 CONVENTIONAL VERTICAL THERMAL OXIDIZER
5 CONVENTIONAL OXIDIZER WITH INTEGRAL WATER SPARGER
6 THERMAL OXIDIZER WITH STAGED AIR INJECTION
7 DOWN-FIRED UNIT WITH WATER BATH QUENCH
8 FLAMELESS THERMAL OXIDATION UNIT
9 THERMAL OXIDIZER WITH REGENERATIVE HEAT RECOVERY
10 TYPICAL PROJECT PROGRAM
11 TYPICAL FLAMMABILITY DIAGRAM
12 EFFECT OF DILUTION WITH AIR
13 EFFECT OF DILUTION WITH AIR ON 100 Rm³ OF FLAMMABLE GAS
VARIOUS METHODS OF CENTRIFUGAL COMPRESSOR SURGE CONTROLVijay Sarathy
This document discusses four methods of surge control for centrifugal compressors: 1) controlling surge with a simple minimum flow cold bypass between the discharge and suction sides; 2) controlling surge by altering compressor speed to meet discharge pressure requirements; 3) controlling surge by altering inlet guide vanes or compressor speed to reset cold bypass flow; 4) controlling surge by correlating differential pressure across the compressor to reset minimum cold bypass flow.
A reciprocating compressor uses pistons driven by a crankshaft to compress gases. It can operate from vacuum to very high pressures. The document discusses the key components of a reciprocating compressor system including cylinders, valves, coolers, pulsation suppression devices, piping, instrumentation, and controls. Process calculations like pipe sizing, blowdown analysis, and hydrate predictions are required. A process simulation and PFD provide design details. Capacity control methods include speed variation, clearance pockets, and suction unloaders.
What is heat exchanger & its Functions
Types of Heat Exchangers
Compact Heat Exchangers
Part of Fin Plate Heat Exchangers
Advantages & Disadvantages of Fin Plate Exchangers
Materials & Manufacturing
Overall Heat transfer Coefficient & Fouling Factor
LMTD Method
Effectiveness - NTU Method
Steam ejector working principle
An ejector is a device used to suck the gas or vapour from the desired vessel or system. An ejector is similar to an of vacuum pump or compressor. The major difference between the ejector and the vacuum pump or compressor is it had no moving parts. Hence it is relatively low-cost and easy to operate and maintenance free equipment.
This document discusses heat exchangers and includes the following key points:
- It describes different types of heat exchangers including concentric-tube, cross-flow, shell-and-tube, and compact heat exchangers.
- It discusses the overall heat transfer coefficient and factors that influence it such as convection, conduction, fins, and fouling.
- It introduces the log mean temperature difference (LMTD) method for calculating heat transfer in heat exchangers and how LMTD is evaluated for different flow configurations.
- It provides an example problem demonstrating how to determine the overall heat transfer coefficient and heat transfer rate for a heat recovery device.
The document discusses nucleate boiling, which involves the transformation of liquid to vapor at a solid-liquid interface due to convection heat transfer. Bubbles form on the heating surface and grow before detaching. Heat transfer coefficients depend on factors like excess temperature, surface properties, and fluid properties. Nucleate boiling is important for processes like steam production, refrigeration, drying, and distillation. The document describes different boiling regimes including natural convection boiling and nucleate boiling, and provides correlations to calculate heat transfer in nucleate pool boiling. It also discusses peak heat flux and provides an example calculation.
Shell and tube heat exchangers are commonly used in various industries. They work by transferring heat between two fluids flowing through the shell side and tube side. Key components include the shell, tubes, tubesheet, baffles, and connections. Design considerations include materials selection, codes and standards compliance, strength calculations for pressure components, and hydrostatic testing. Detailed drawings are required to communicate the design to manufacturers.
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.
Gas Compression Stages – Process Design & OptimizationVijay Sarathy
The following tutorial demonstrates how to estimate the required number of compression stages and optimize the individual pressure ratio in a multistage centrifugal compression system.
This paper relates two heat sinks, a medical suction device, a household oven, and an industrial control valve as examples
that illustrate how SolidWorks® Flow Simulation can help design engineers create the best possible product designs
when dealing with heat transfer and fluid flow problems. SolidWorks Flow Simulation is an intelligent, easy-to-use
computational fluid dynamics (CFD) program that will facilitate the work of design engineers who use SolidWorks 3D
CAD software for design creation.
Application of Pinch Technology in Refrigerator Condenser Optimization by Usi...ijtsrd
Refrigeration is the major application area of thermodynamics, in which the heat is transferred to higher temperature region from a lower temperature region. Refrigerators are the devices which produce refrigeration and the refrigerators which operate on the cycles are called refrigeration cycles. Pinch technology and computational fluid dynamics CFD is key for study the condenser and enhance the better option for new design. Pinch Analysis also known as process integration, heat integration, energy integration, or pinch technology is method for minimizing the energy costs of a process by reusing the heat energy in the process streams rather than outside utilities. Mr. Mayur B. Ramteke | Prof. S. K. Bawne "Application of Pinch Technology in Refrigerator Condenser Optimization by Using CFD" Published in International Journal of Trend in Scientific Research and Development (ijtsrd), ISSN: 2456-6470, Volume-5 | Issue-6 , October 2021, URL: https://www.ijtsrd.com/papers/ijtsrd46440.pdf Paper URL : https://www.ijtsrd.com/engineering/mechanical-engineering/46440/application-of-pinch-technology-in-refrigerator-condenser-optimization-by-using-cfd/mr-mayur-b-ramteke
The document describes a proposed heat exchanger design project to recover waste heat from laundry processes. Dirty wash water at 67°C is currently dumped, while clean water is heated to 70°C using an electric water heater. It is proposed to install a heat exchanger to preheat the water and reduce electricity costs. The heat exchanger design must be optimized to maximize annual savings over a 10-year period considering capital costs, operating costs, and a 10% interest rate. Several heat exchanger concepts will be analyzed and the optimal design selected.
IRJET- Performance Evaluation of Automobile RadiatorIRJET Journal
This document discusses performance evaluation of automobile radiators. It begins with an abstract that outlines the goal of studying and analyzing the thermal behavior of automobile radiators using the LMTD and ε-NTU methods. It then provides background on radiators and their role in removing waste heat from engines. The literature review summarizes previous studies on optimizing radiator design parameters like tube pitch and airflow velocity. The problem statement discusses the need to improve radiator performance as engines have become more powerful. The experimental scheme and design parameters sections outline the planned study to evaluate radiator prototypes using different parameters. In conclusions, the work aims to enhance radiator performance by altering convective heat transfer coefficients and provide easier radiator design using case
The document discusses optimizing the design of an air cooled heat exchanger (ACHE) by analyzing how fin geometric parameters and tube configuration affect performance. Commercial software will be used to optimize the design to minimize temperature difference and total annual cost. Key parameters that will be varied include fin radial clearance, fin diameter, fin height, tube pitch, number of tube rows, and air velocity.
This document provides guidance on the design and rating of shell and tube heat exchangers. It discusses fundamentals of heat transfer calculations and selection of appropriate heat transfer models. Key considerations in the thermal design of shell and tube heat exchangers include process parameters, mechanical design factors such as tube dimensions and layout, and selection of heat transfer correlations. Software tools can help optimize the design but require experience to achieve practical designs.
Validation of Design Parameters of Radiator using Computational ToolIRJET Journal
This document discusses the validation of design parameters for automobile radiators using computational tools. It presents two case studies where the thermal performance of radiators is analyzed using the log mean temperature difference (LMTD) and number of transfer units (NTU) methods and the results are compared to those from a computational software tool (HXCombine). The results show good agreement between the manual calculations and software outputs, validating the use of computational tools for radiator design. Parameters like heat transfer rate, outlet temperatures, effectiveness and heat transfer area are compared for both case studies. This research demonstrates that computational tools can accurately analyze and design radiator performance.
1. The document presents the design of a microprocessor cooling system to keep the temperature of an Intel Pentium 4 processor below 55°C. Equations are provided to calculate the temperature, heat flux, efficiency, and effectiveness of a heat sink design.
2. A proposed design uses 24 aluminum fins that is within budget and keeps the processor temperature at 52.77°C. The overall height of 24.5mm is less than the maximum of 25mm.
3. Calculations show the design has a heat removal rate of 802 W/m^2, fin efficiency of 23.9%, total efficiency of 24.4%, and effectiveness of 6.1. The design meets all constraints.
Mechwell Industries provides engineering services including computational fluid dynamics (CFD) analysis. They analyzed the performance of an exhaust gas recirculation (EGR) cooler using CFD to determine the heat transfer rate and pressure drops on the gas and coolant sides. They created 3D models of the gas and coolant sections, applied boundary conditions and material properties, then simulated the flows. The CFD analysis found the gas side had a 5 kPa pressure drop and outlet temperature of 99°C, while the coolant side had a 0.5 kPa pressure drop and outlet temperature of 205°C, determining the heat transfer between the sections.
Design and Thermal Analysis of an Automotive Radiator for enhancing Flow Unif...IRJET Journal
This document describes a study to improve flow uniformity in an automotive radiator through computational fluid dynamics (CFD) analysis and design optimization. The researchers first modeled a single-pass radiator in CAD software and performed CFD analysis, finding non-uniform flow. They then redesigned the radiator as a three-pass system by lowering tube size. CFD analysis of the new design showed improved flow uniformity, lower pressure drops, and more uniform streamlines. Thermal analysis found the three-pass radiator achieved a lower coolant outlet temperature and higher heat rejection rate than the single-pass version. In summary, modifying a single-pass radiator to a three-pass design through reduced tube sizing was
IRJET-V9I12214.Comparative Computational analysis of performance parameters f...IRJET Journal
This document presents a computational analysis comparing the performance of a shell and tube heat exchanger using different working fluids and a helical insert. It analyzes heat transfer rate, overall heat transfer coefficient, and effectiveness using water, SiO2 nanofluid at 0.4% volume fraction, and a helically twisted insert. The nanofluid and insert improve performance by increasing turbulence and the heat transfer coefficient compared to water alone. Calculations of nanofluid properties, heat exchanger parameters, and a performance evaluation criterion are presented. CFD analysis in SolidWorks is used to simulate and validate the virtual heat exchanger model against experimental results.
This document provides an overview of the methodology for heat exchanger design. It discusses that heat exchanger design is a complex, multidisciplinary process that involves specifying requirements, evaluating design concepts, detailed sizing and optimization. Key considerations in the design process include thermal and hydraulic design of the exchanger, mechanical design to ensure structural integrity, and manufacturing factors that influence cost. The methodology involves iterative thermal modeling, mechanical analysis, and consideration of manufacturing to arrive at an optimized design.
Robust Algorithm Development for Application of Pinch Analysis on HENIJERA Editor
Since its genesis, Pinch Analysis is continuously evolving and its application is widening, reaching new horizons. The original concept of pinch approach was quite clear and, because of flexibility of this approach, innumerable applications have been developed in the industry. Consequently, a designer gets thoroughly muddled among these flexibilities. Hence, there was a need for a rigorous and robust model which could guide the optimisation engineer on deciding the applicability of the pinch approach and direct sequential step of procedure in predefined workflow, so that the precision of approach is ensured. Exploring the various options of a novice hands-on algorithm development that can be coded and interfaced with GUI and keeping in mind the difficulties faced by designers, an effort was made to formulate a new algorithm for the optimisation activity. As such, the work aims at easing out application hurdles and providing hands-on information to the Developer for use during preparation of new application tools. This paper presents a new algorithm, the application which ensures the Developer does not violate basic pinch rules. To achieve this, intermittent check gates are provided in the algorithm, which eliminate violation of predefined basic pinch rules, design philosophy, and Engineering Standards and ensure that constraints are adequately considered. On the other side, its sequential instruction to develop the pinch analysis and reiteration promises Maximum Energy Recovery (MER).
Design of Heat Exchanger Network for VCM Distillation Unit Using Pinch Techno...IJERA Editor
In process industries, heat exchanger networks represent an important part of the plant structure. The purpose of the networks is to maximize heat recovery, thereby lowering the overall plant costs. In process industries, during operation of any heat exchanger network (HEN), the major aim is to focus on the best performance of the network As in present condition of fuel crises is one of the major problem faced by many country & industrial utility is majorly depend on this. There is technique called process integration which is used for integrate heat within loop so optimize the given process and minimize the heating load and cooling load .In the present study of heat integration on VCM (vinyl chloride monomer) distillation unit, Heat exchanger network (HEN) is designed by using Aspen energy analyzer V8.0 software. This software implements a methodology for HEN synthesis with the use of pinch technology. Several heat integration networks are designed with different ΔT min and total annualized cost compared to obtain the optimal design. The network with a ΔT min of 90C is the most optimal where the largest energy savings are obtained with the appropriate use of utilities (Save 15.3764% for hot utilities and 47.52% for cold utilities compared with the current plant configuration). Percentage reduction in total operating cost is 18.333%. From calculation Payback Period for new design is 3.15 year. This save could be done through a plant revamp, with the addition of two heat exchangers. This improvement are done in the process associated with this technique are not due to the use of advance unit operation, but to the generation of heat integration scheme. The Pinch Design Method can be employed to give good designs in rapid time and with minimum data.
IRJET- CFD Analysis of Double Pipe Heat Exchanger with Different Inner Se...IRJET Journal
This document analyzes the heat transfer performance of a double pipe heat exchanger with circular and square inner sections using computational fluid dynamics (CFD). CFD simulations were conducted using ANSYS Fluent to analyze temperature contours and heat transfer rates. The results showed that the square inner section heat exchanger absorbed more heat from the hot fluid and had a higher heat flow rate than the circular section design, with the cold fluid outlet temperature being higher for the square section. In conclusion, the square inner section design exhibited better heat transfer performance compared to the conventional circular section design for this type of heat exchanger.
This document provides guidelines for selecting and sizing heat exchangers commonly used in industrial processes. It covers different types of heat exchangers like shell and tube, plate heat exchangers and their basic design considerations. The guidelines help engineers understand heat exchanger design and selection methods. It includes topics like heat transfer theory, examples of heat exchanger sizing calculations and specification sheets for heat exchanger design.
Recent advances in semiconductor technology show the improvement of fabrication on
electronics appliances in terms of performance, power density and even the size. This great achievement
however led to some major problems on thermal and heat distribution of the electronic devices. This
thermal problem could reduce the efficiency and reliability of the electronic devices. In order to minimize
this thermal problem, an optimal cooling techniques need to be applied during the operation. There are
various cooling techniques have been used and one of them is passive pin fin heat sink approach. This
paper focuses on inline pin fin heat sink, which use copper material with different shapes of pin fin and a
constant 5.5W heat sources. The simulation model has been formulated using COMSOL Multiphysics
software to stimulate the pin fin design, study the thermal distribution and the maximum heat profile.
Sushilkumar M. Jogdankar is a CFD project leader with over 10 years of experience in CFD modeling. He has expertise in areas such as heat transfer simulation, fluid dynamics, conjugate analysis, and multiphase flow modeling. He is proficient in simulation tools such as ANSYS Fluent, ANSYS CFX, ANSA, and Gambit. Jogdankar is currently seeking new opportunities where he can apply his technical and leadership skills.
This presentation discusses data center cooling technologies. It provides a brief history of data centers and outlines ASHRAE thermal guidelines for operating envelopes and temperature change requirements. The presentation then reviews common cooling system types including computer room air conditioners, computer room air handlers, and water-side economizers. It also examines heat rejection options and trends toward higher supply air/water temperatures to improve efficiency.
To design central air conditioning System by determining the amount of cooling load required for rooms in mechanical Engg. dept (second floor) of Mct-RGIT, and estimate/select the suitable cooling system according to required calculated load.
Objective of this Case Study.
Calculate Heat gains through spaces.
Select Appropriate design condition for cooling.
Determine peak load condition.
Find the required AC System.
Determine the cooling load analysis.
Perform Computational Fluid Dynamics (CFD) for required system.
Similar to Compress heat exchanger design w notes (20)
Neom: The Futuristic
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Nestled within the breathtaking landscapes of Saudi Arabia, Neom is an
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Building Accessibility into your Design SystemsResolute
Accessibility is transforming from a mere buzzword to a crucial design principle, essential for creating inclusive experiences that cater to all users, including those with disabilities. Overlooking accessibility can alienate potential users, highlighting the importance of incorporating it to ensure equality and a seamless user experience. At the heart of ensuring consistent, quality experiences lies the concept of a design system, defined by Diana as "the single source of truth" for all teams involved in product development.
Integrating accessibility within design systems from the outset is not only more efficient and cost-effective but also fosters a cohesive and inclusive digital environment across design, development, and product management, ensuring that products serve everyone's needs right from the beginning.
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Product And Design Portfolio - Hemant Nagwekar 2024Hemant Nagwekar
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Artificial Intelligence (AI) is revolutionizing the field of architectureMostafa Abd Elrahman
Artificial Intelligence (AI) is revolutionizing the field of architecture,
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2. Outline
Introduction
Why we need to use a systematic approach to design heat exchangers
What factors are needed to design a quality heat exchanger
How do we approach that goal
What are a Process engineers responsibilities
What are the Mechanical engineers responsibilities
What tools are available in-house for heat exchanger design
Heat Exchanger design codes
An example of step by step design for a heat exchanger
2
Heat Exchanger Design training
3. INTRODUCTION
The objective of this training is to provide a concise review of the key issues involved in Heat Exchanger
design. At the start of the heat exchanger design, process and mechanical considerations are crucial. It
needs to be clearly understood what we want to achieve. The calculations in the software program
relies on careful considered input. Engineering judgment must be used to evaluate both thermal and
hydraulic the design results.
So what are the key parameters we should consider to produce a quality design?
The Data Sheet is the final product, all the hard work will be inputted here. When complete it is ready
to be issued to vendors, manufactures for quote.
Client often decide which Vendors to select.
Therefore, we want to produce a quality design to demonstrate we know how to design heat
exchangers.
How do we approach this goal?
Process Considerations
Mechanical Considerations
Construction Considerations
3
Heat Exchanger Design training
4. INTRODUCTION
Process Considerations
− How many heat exchangers are required?
− What duty?
− What type of utility (air, water, steam, hot oil) is required?
Mechanical Considerations
− What is the Lead Time and Cost?
Construction Considerations
Not covered here
4
Heat Exchanger Design training
5. Systematic Approach – the following steps are suggested
5
Ho do we approach to design a quality heat Exchanger?
6. Optimization possibilities
Is Optimization possible?
Pinch Technology is one of the optimize heat exchanger design methods. The results of the pinch
technology will targets for:
1. Calculate utility requirements
2. Estimate exchanger requirements
3. Overview of energy flows for entire process
4. Overall view of entire steam/power system
5. Potential energy saving in a process
6. Targets to aim for
• Quantity of exchangers (# shells, total area)
• Utility Capital cost targets
6
Process Considerations
7. Data Extraction
To start the Pinch Analysis, we need
to extract the necessary thermal data
from process simulations as shown in
Figure 1.
Figures (a) & (b) on next page shows
an example represented by the two
process Flow sheets. We now apply
the pinch analysis principles to design
the heat exchanger.
* Pinch Technology (JGCA-1303-0132)
Example: Condenser Design
7
Fig. 1
Fig. 1 Work Steps Required*
9. Optimization possibilities
9
Example: Condenser design (cont.)
Table 1 shows the thermal extraction data for Pinch Analysis. Streams 1 & 2 are hot steams (heat sources).
Streams 3 & 4 are cold streams (heat sinks). Assume a minimum temperature difference of 10o C. The hot utility
is steam at 200o C and the cold utility is cooling water in the range 25 o C to 30 o C. Figures (a) & (b) represent a
graphical construction of the target for minimum energy consumption for the process.
Fig. 2 Construction of Composite CurvesTable 1
10. Example: Condenser design (cont.)
10
The minimum energy target for the process. The hot and cold composite curves are now overlapped on one another. Fig. (a), separating them by the
minimum temperature difference ∆Tmin = 10 C.
Fig. (b) shows the minimum hot utility (QHmin)
As you can see, using Pinch Analysis we are able to set targets for minimum energy consumption based on heat and material balance information prior
to heat exchanger design. This allows us to quickly identify any energy saving at an early stage.
For more details refer to JGCA-1303-0132 Pinch Technology
DETERMINING THE ENERGY TARGETS
11. The Pinch Principle
11
The point where ∆Tmin is observed is
known as the “Pinch” and recognizing
its implications allow energy targets
to be realized in practice.
One above and one below the pinch,
as shown in Fig. (a). The system
above the pinch requires a heat input,
The system below the pinch rejects
heat, so is a net heat source. To
restore the heat balance, the hot
utility must be increased by the same
amount, that is, α units., therefore the
cold utility requirement also increases
by α units. In conclusion, the
consequence of a cross-pinch heat
transfer (α) is that both the hot and
cold utility will increase by the cross-
pinch duty (α).
DETERMINING THE ENERGY TARGETS
Example: Condenser design (cont.)
12. Systematic Approach – the following steps are suggested
There are two disciplines whose goal is to generate the HX datasheet. Process Engineer and Mechanical Engineer.
Process Responsibilities are:
◦ Selection of heat transfer models
◦ Define Fluid Composition for both shell side and tube side
◦ Define Operating Pressure and Temperature
◦ Define shell side and tube side allowable Pressure limits
◦ Define shell side and tube side velocity limits.
◦ Define Gravity or Density
◦ Define Specific Heat
◦ Define Viscosity, cp
◦ Define Fouling Factor for shell side and tube side
◦ Define Thermal Conductivity
◦ Define Latent Heat, (if phase change)
◦ Complete optimum thermal design
◦ Complete internal Process verification and checking and pass the Data Sheet to Mechanical
12
Ho do we approach to design a quality heat Exchanger?
13. Optimizing Heat Exchanger Process and Cost Effectiveness
Mechanical engineer shall use the Data Sheet from process and import the
data into COMPRESS. Then complete the mechanical design and complete
the mechanical sections of the Data Sheet.
Mechanical engineer responsibilities are:
1. Confirm the type of exchanger configuration.
2. Set upper and lower design limits on shell diameter
3. Set upper and lower design limits on tube length.
4. Specify both shell and tube side layout
5. Specify pitch, material, baffle cut, baffle spacing and clearances.
6. Prepare Material Requisition
7. Complete Technical Bid Evaluation on bids
Items 1 to 5 are covered in the following sections.
13
Mechanical
14. Tools are available in-house for design the exchangers
There are two software programs in house
1) HTRI,
2) COMPRESS.
HTRI is best used for process thermal design and to produce TEMA
Datasheet.
COMPRESS is used to design the complete exchanger. Tubesheet(s), tubes,
expansion joint, shell, channels, flanges, head closures, nozzles, etc.
COMPRESS will generate shell side & tube side hydrotest conditions based
on the input design conditions.
There are four ways to create a heat exchanger in COMPRESS.
1. Start from “File” and select “New heat exchanger”.
2. Pressing “Ctrl T” on your keyboard
3. Import an HTRI designed file
4. To Start a File click on the heat exchanger icon found on the main menu
14
Mechanical Design Software
15. Two methods are used in COMPRESS design.
a) TEMA
b) UHX methods.
When to use TEMA or UHX methods.
• When rating an existing exchanger built to TEMA.
• When supplying new equipment where TEMA has been specified in addition to UHX.
Regardless which option is selected, for new exchanger design. ASME is mandatory for tubesheet
design
15
COMPRESS Heat Exchanger introduction
How does COMPRESS work
16. COMPRESS has a built in interface with HTRI.
COMPRESS can read and write HTRI’S Xist files
COMPRESS directly importing an existing HTRI file to complete the mechanical design
COMPRESS / HTRI interface enables shell and tube heat exchanger files design interchangeable
COMPRESS can analyze all components design conditions simultaneously
COMPRESS has built-in Design codes to check and evaluate components design conditions
• Such as ASME VIII UHX, TEMA, or both ASME VIII UHX & TEMA and more
16
How does COMPRESS work
18. Example by import an HTRI designed file
Before starting COMPRESS to design a heat exchanger, a few things are required. Open COMPRESS, on the lower right
corner, select the Mode, units, Div. and revision to set up the calculation Mode.
https://support.codeware.com/link/portal/9185/9191/Article/352/COMPRESS-Heat-Exchanger-Tutorial
18
COMPRESS Heat Exchanger introduction
19. Step 1: Start the Heat Exchanger Wizard
19
The following screenshots are example from COMPRESS
20. 20
This is the HTRI File Import Values. The color code indicate four results
The following screenshots are example from COMPRESS
21. Step 2: Edit an existing Heat Exchanger
21
The following screenshots are example from COMPRESS
In Fig. (b), α amount of heat is transferred from above the pinch, below the pinch. The system above the pinch, which was before in heat balance with QHmin, now loses α units of heat to the system below the pinch. Fig. 3.5(b) also shows γ amount of external cooling above the pinch and β amount of external heating below the pinch. The external cooling above the pinch of γ amount increases the hot utility demand by the same amount. Therefore on an overall basis both the hot and cold utilities are increased by γ amount. Similarly external heating below the pinch of β amount increases the overall hot and cold utility requirement by the same amount (i.e. β).
Once the pinch has been identified, it is possible to consider the process as two separate systems:
First Process Engineer to prepare the thermal rating part of datasheet them move to mechanical engineer to complete the datesheet.
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
The TEMA & ASME VIII UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME VIII requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parThe TEMA standard is used to evaluate the tubesheet, tube, and shell. If this option is selected then further TEMA details will need to be specified in the TEMA option selection box.
ameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
The heat exchanger components may be evaluated using TEMA, ASE UHX. or both.
In design mode, COMPRESS selects tube sheet thickness such that it meets the ASME requirements.
The governing design condition specified in the heat exchanger wizard is automatically used in the vessel component in ASME section 8 div. 1 calculations. The only way to change design parameters such as internal design pressure or temperature for heads, and shells is Through the heat exchanger dialogs provided by COMPRESS. This is done intentionally to preserve the integrity of the design.
First. Select te defaults you wish to use or create a new defaults file that may be used for future projects.
Depending on customer requirements. It may be better to create a new defaults file so that it may be used for future projects. Three options available. There are Fixed/Stationary Tube sheets. U-tube. And Floating Tube sheet.
The TEMA & ASME VIII UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME VIII requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parThe TEMA standard is used to evaluate the tubesheet, tube, and shell. If this option is selected then further TEMA details will need to be specified in the TEMA option selection box.
ameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
The heat exchanger components may be evaluated using TEMA, ASE UHX. or both.
In design mode, COMPRESS selects tube sheet thickness such that it meets the ASME requirements.
The governing design condition specified in the heat exchanger wizard is automatically used in the vessel component in ASME section 8 div. 1 calculations. The only way to change design parameters such as internal design pressure or temperature for heads, and shells is Through the heat exchanger dialogs provided by COMPRESS. This is done intentionally to preserve the integrity of the design.
First. Select te defaults you wish to use or create a new defaults file that may be used for future projects.
Depending on customer requirements. It may be better to create a new defaults file so that it may be used for future projects. Three options available. There are Fixed/Stationary Tube sheets. U-tube. And Floating Tube sheet.
The heat exchanger components may be evaluated using TEMA, ASE UHX. or both.
In design mode, COMPRESS selects tube sheet thickness such that it meets the ASME requirements.
The governing design condition specified in the heat exchanger wizard is automatically used in the vessel component in ASME section 8 div. 1 calculations. The only way to change design parameters such as internal design pressure or temperature for heads, and shells is Through the heat exchanger dialogs provided by COMPRESS. This is done intentionally to preserve the integrity of the design.
First. Select te defaults you wish to use or create a new defaults file that may be used for future projects.
Depending on customer requirements. It may be better to create a new defaults file so that it may be used for future projects. Three options available. There are Fixed/Stationary Tube sheets. U-tube. And Floating Tube sheet.
These conditions typically include operating , start up, shut down, hydrotest, and upset conditions.
When no hydrotest conditions are specified then COMPRESS will generate shell side and tube side hydrotest conditions based on the input design conditions
The heat exchanger components may be evaluated using TEMA, ASE UHX. or both.
In design mode, COMPRESS selects tube sheet thickness such that it meets the ASME requirements.
The governing design condition specified in the heat exchanger wizard is automatically used in the vessel component in ASME section 8 div. 1 calculations. The only way to change design parameters such as internal design pressure or temperature for heads, and shells is Through the heat exchanger dialogs provided by COMPRESS. This is done intentionally to preserve the integrity of the design.
First. Select te defaults you wish to use or create a new defaults file that may be used for future projects.
Depending on customer requirements. It may be better to create a new defaults file so that it may be used for future projects. Three options available. There are Fixed/Stationary Tube sheets. U-tube. And Floating Tube sheet.
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
If design a new HX . MSME UHX is mandatory. If you are re-rating and existing HX. Then option to select TEMA is available. The TEMA STANDARD IS USED TO EVALUATE THE BUBE SHEET, TUBE, AND SHELL. IF THIS OPTION IS selected than further TEMA details will need to be specified in the TEMA option selection box which will appear below.
The ASME option uses section 8 div. 1 UHX to evaluate the tube sheets. Tubes. Channel. And the shell.
For the ASME and TEMA option both methods are performed simultaneously allowing the designer to select either as the bases for design. When this option of active the larger required thickness of the two methods will be used.
Bothe TEMA and UHX are based on the same theory. TEMA makes certain simplifying assumptions. Where as UHX is more rigorous. Some notable differences are in the way UHX considers the tubesheet unperforated area to be a solid rim.. This detail is not included in TEMA. UHX considers the stiffening effect of the tube bundle and tubes on the tubesheet through the coefficient “F”. Also, UHX accounts for the edge displacements and rotations of the tube sheet and attached integral shell and/or channel. The question sometimes arises as to when to use both methods. One application is when rating an existing exchanger built to TEMA. Another is when supplying new equipment where TEMA has been specified in addition to UHX.
For more background information on UHX. Please refer to the UHX White paper found on the support page of Codeware’s website. Regardless which option is selected here, ass components other than the tubesheet are calculated per ASME section div. 1. Because we are design a new exchanger. ASME is mandatory for tub sheet design. If the ASME calculation method has been specified than shell bands are available. This option is only applicable when the shell is integrals with the tube sheet. This option is used to increase the thickness of the shell adjacent to the tube sheet.. Different materials of construction may be specified for the shell and shell bands. Shell bands may be used to optimize the tube sheet thickness even when the shell and channel stresses are not excessive.. Also, they may be used to decease the tubesheet thickness. The next option. Use Operating Temperatures for Load Cases 4-7 is for load case involving deferential expansion. The additional inputs will be needed at a later point if this option is checked
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
If design a new HX . MSME UHX is mandatory. If you are re-rating and existing HX. Then option to select TEMA is available. The TEMA STANDARD IS USED TO EVALUATE THE BUBE SHEET, TUBE, AND SHELL. IF THIS OPTION IS selected than further TEMA details will need to be specified in the TEMA option selection box which will appear below.
The ASME option uses section 8 div. 1 UHX to evaluate the tube sheets. Tubes. Channel. And the shell.
For the ASME and TEMA option both methods are performed simultaneously allowing the designer to select either as the bases for design. When this option of active the larger required thickness of the two methods will be used.
Bothe TEMA and UHX are based on the same theory. TEMA makes certain simplifying assumptions. Where as UHX is more rigorous. Some notable differences are in the way UHX considers the tubesheet unperforated area to be a solid rim.. This detail is not included in TEMA. UHX considers the stiffening effect of the tube bundle and tubes on the tubesheet through the coefficient “F”. Also, UHX accounts for the edge displacements and rotations of the tube sheet and attached integral shell and/or channel. The question sometimes arises as to when to use both methods. One application is when rating an existing exchanger built to TEMA. Another is when supplying new equipment where TEMA has been specified in addition to UHX.
For more background information on UHX. Please refer to the UHX White paper found on the support page of Codeware’s website. Regardless which option is selected here, ass components other than the tubesheet are calculated per ASME section div. 1. Because we are design a new exchanger. ASME is mandatory for tub sheet design. If the ASME calculation method has been specified than shell bands are available. This option is only applicable when the shell is integrals with the tube sheet. This option is used to increase the thickness of the shell adjacent to the tube sheet.. Different materials of construction may be specified for the shell and shell bands. Shell bands may be used to optimize the tube sheet thickness even when the shell and channel stresses are not excessive.. Also, they may be used to decease the tubesheet thickness. The next option. Use Operating Temperatures for Load Cases 4-7 is for load case involving deferential expansion. The additional inputs will be needed at a later point if this option is checked
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
If design a new HX . MSME UHX is mandatory. If you are re-rating and existing HX. Then option to select TEMA is available. The TEMA STANDARD IS USED TO EVALUATE THE BUBE SHEET, TUBE, AND SHELL. IF THIS OPTION IS selected than further TEMA details will need to be specified in the TEMA option selection box which will appear below.
The ASME option uses section 8 div. 1 UHX to evaluate the tube sheets. Tubes. Channel. And the shell.
For the ASME and TEMA option both methods are performed simultaneously allowing the designer to select either as the bases for design. When this option of active the larger required thickness of the two methods will be used.
Bothe TEMA and UHX are based on the same theory. TEMA makes certain simplifying assumptions. Where as UHX is more rigorous. Some notable differences are in the way UHX considers the tubesheet unperforated area to be a solid rim.. This detail is not included in TEMA. UHX considers the stiffening effect of the tube bundle and tubes on the tubesheet through the coefficient “F”. Also, UHX accounts for the edge displacements and rotations of the tube sheet and attached integral shell and/or channel. The question sometimes arises as to when to use both methods. One application is when rating an existing exchanger built to TEMA. Another is when supplying new equipment where TEMA has been specified in addition to UHX.
For more background information on UHX. Please refer to the UHX White paper found on the support page of Codeware’s website. Regardless which option is selected here, ass components other than the tubesheet are calculated per ASME section div. 1. Because we are design a new exchanger. ASME is mandatory for tub sheet design. If the ASME calculation method has been specified than shell bands are available. This option is only applicable when the shell is integrals with the tube sheet. This option is used to increase the thickness of the shell adjacent to the tube sheet.. Different materials of construction may be specified for the shell and shell bands. Shell bands may be used to optimize the tube sheet thickness even when the shell and channel stresses are not excessive.. Also, they may be used to decease the tubesheet thickness. The next option. Use Operating Temperatures for Load Cases 4-7 is for load case involving deferential expansion. The additional inputs will be needed at a later point if this option is checked
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
If design a new HX . MSME UHX is mandatory. If you are re-rating and existing HX. Then option to select TEMA is available. The TEMA STANDARD IS USED TO EVALUATE THE BUBE SHEET, TUBE, AND SHELL. IF THIS OPTION IS selected than further TEMA details will need to be specified in the TEMA option selection box which will appear below.
The ASME option uses section 8 div. 1 UHX to evaluate the tube sheets. Tubes. Channel. And the shell.
For the ASME and TEMA option both methods are performed simultaneously allowing the designer to select either as the bases for design. When this option of active the larger required thickness of the two methods will be used.
Bothe TEMA and UHX are based on the same theory. TEMA makes certain simplifying assumptions. Where as UHX is more rigorous. Some notable differences are in the way UHX considers the tubesheet unperforated area to be a solid rim.. This detail is not included in TEMA. UHX considers the stiffening effect of the tube bundle and tubes on the tubesheet through the coefficient “F”. Also, UHX accounts for the edge displacements and rotations of the tube sheet and attached integral shell and/or channel. The question sometimes arises as to when to use both methods. One application is when rating an existing exchanger built to TEMA. Another is when supplying new equipment where TEMA has been specified in addition to UHX.
For more background information on UHX. Please refer to the UHX White paper found on the support page of Codeware’s website. Regardless which option is selected here, ass components other than the tubesheet are calculated per ASME section div. 1. Because we are design a new exchanger. ASME is mandatory for tub sheet design. If the ASME calculation method has been specified than shell bands are available. This option is only applicable when the shell is integrals with the tube sheet. This option is used to increase the thickness of the shell adjacent to the tube sheet.. Different materials of construction may be specified for the shell and shell bands. Shell bands may be used to optimize the tube sheet thickness even when the shell and channel stresses are not excessive.. Also, they may be used to decease the tubesheet thickness. The next option. Use Operating Temperatures for Load Cases 4-7 is for load case involving deferential expansion. The additional inputs will be needed at a later point if this option is checked
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
If design a new HX . MSME UHX is mandatory. If you are re-rating and existing HX. Then option to select TEMA is available. The TEMA STANDARD IS USED TO EVALUATE THE BUBE SHEET, TUBE, AND SHELL. IF THIS OPTION IS selected than further TEMA details will need to be specified in the TEMA option selection box which will appear below.
The ASME option uses section 8 div. 1 UHX to evaluate the tube sheets. Tubes. Channel. And the shell.
For the ASME and TEMA option both methods are performed simultaneously allowing the designer to select either as the bases for design. When this option of active the larger required thickness of the two methods will be used.
Bothe TEMA and UHX are based on the same theory. TEMA makes certain simplifying assumptions. Where as UHX is more rigorous. Some notable differences are in the way UHX considers the tubesheet unperforated area to be a solid rim.. This detail is not included in TEMA. UHX considers the stiffening effect of the tube bundle and tubes on the tubesheet through the coefficient “F”. Also, UHX accounts for the edge displacements and rotations of the tube sheet and attached integral shell and/or channel. The question sometimes arises as to when to use both methods. One application is when rating an existing exchanger built to TEMA. Another is when supplying new equipment where TEMA has been specified in addition to UHX.
For more background information on UHX. Please refer to the UHX White paper found on the support page of Codeware’s website. Regardless which option is selected here, ass components other than the tubesheet are calculated per ASME section div. 1. Because we are design a new exchanger. ASME is mandatory for tub sheet design. If the ASME calculation method has been specified than shell bands are available. This option is only applicable when the shell is integrals with the tube sheet. This option is used to increase the thickness of the shell adjacent to the tube sheet.. Different materials of construction may be specified for the shell and shell bands. Shell bands may be used to optimize the tube sheet thickness even when the shell and channel stresses are not excessive.. Also, they may be used to decease the tubesheet thickness. The next option. Use Operating Temperatures for Load Cases 4-7 is for load case involving deferential expansion. The additional inputs will be needed at a later point if this option is checked
All conditions are investigated simultaneously. The heat exchanger components may be evaluated using ASME UHX,, TEMA, or both ASME UHX & TEMA. The TEMA & ASME UHX option provides the tubesheet design thickness from both design codes allowing the nominal tubesheet thickness assignment to be based on either set of design rules. COMPRESS requires that the tube sheet thickness meets the ASME requirements.
The governing design condition, neglecting hydrotest conditions, specified in the heat exchanger wizard is automatically used for the vessel component ASME VIII-1 calculations (e.g. shell, channels, head closures, nozzles). It is not permissible to change the design parameters such as internal design pressure/temperature of individual components. These values must be changed through the heat exchanger wizard.
If design a new HX . MSME UHX is mandatory. If you are re-rating and existing HX. Then option to select TEMA is available. The TEMA STANDARD IS USED TO EVALUATE THE BUBE SHEET, TUBE, AND SHELL. IF THIS OPTION IS selected than further TEMA details will need to be specified in the TEMA option selection box which will appear below.
The ASME option uses section 8 div. 1 UHX to evaluate the tube sheets. Tubes. Channel. And the shell.
For the ASME and TEMA option both methods are performed simultaneously allowing the designer to select either as the bases for design. When this option of active the larger required thickness of the two methods will be used.
Bothe TEMA and UHX are based on the same theory. TEMA makes certain simplifying assumptions. Where as UHX is more rigorous. Some notable differences are in the way UHX considers the tubesheet unperforated area to be a solid rim.. This detail is not included in TEMA. UHX considers the stiffening effect of the tube bundle and tubes on the tubesheet through the coefficient “F”. Also, UHX accounts for the edge displacements and rotations of the tube sheet and attached integral shell and/or channel. The question sometimes arises as to when to use both methods. One application is when rating an existing exchanger built to TEMA. Another is when supplying new equipment where TEMA has been specified in addition to UHX.
For more background information on UHX. Please refer to the UHX White paper found on the support page of Codeware’s website. Regardless which option is selected here, ass components other than the tubesheet are calculated per ASME section div. 1. Because we are design a new exchanger. ASME is mandatory for tub sheet design. If the ASME calculation method has been specified than shell bands are available. This option is only applicable when the shell is integrals with the tube sheet. This option is used to increase the thickness of the shell adjacent to the tube sheet.. Different materials of construction may be specified for the shell and shell bands. Shell bands may be used to optimize the tube sheet thickness even when the shell and channel stresses are not excessive.. Also, they may be used to decease the tubesheet thickness. The next option. Use Operating Temperatures for Load Cases 4-7 is for load case involving deferential expansion. The additional inputs will be needed at a later point if this option is checked