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Heat Exchanger Design
Mechanical Engineering Department
By Sharon Wenger
June 11, 2015
Heat Exchanger Design training
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
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
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
Systematic Approach – the following steps are suggested
5
Ho do we approach to design a quality heat Exchanger?
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
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*
Example: Condenser Design (Cont.)
8
Process Flow Sheet
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
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
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.)
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?
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
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
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
 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
17
The following screenshots are example from COMPRESS
Exchanger design codes
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
Step 1: Start the Heat Exchanger Wizard
19
The following screenshots are example from COMPRESS
20
This is the HTRI File Import Values. The color code indicate four results
The following screenshots are example from COMPRESS
Step 2: Edit an existing Heat Exchanger
21
The following screenshots are example from COMPRESS
22
The following screenshots are example from COMPRESS
23
Report summary
The following screenshots are example from COMPRESS
24
Report summary
The following screenshots are example from COMPRESS
25
The following screenshots are example from COMPRESS
26
The following screenshots are example from COMPRESS
27
 HTRI Fundamentals of Exchanger Design
 COMPRESS , BUILD 7500
 COMPRESS REPORT RGX6_663-E016, Provided by -
Leonard Stephen Thill, san, Principal Piping – Lead Piping Stress Specialist, Stress &
Static Equipment
References
28
THE END
29
Special Thanks

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Compress heat exchanger design w notes

  • 1. Heat Exchanger Design Mechanical Engineering Department By Sharon Wenger June 11, 2015 Heat Exchanger Design training
  • 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*
  • 8. Example: Condenser Design (Cont.) 8 Process Flow Sheet
  • 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
  • 17. 17 The following screenshots are example from COMPRESS Exchanger design codes
  • 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
  • 22. 22 The following screenshots are example from COMPRESS
  • 23. 23 Report summary The following screenshots are example from COMPRESS
  • 24. 24 Report summary The following screenshots are example from COMPRESS
  • 25. 25 The following screenshots are example from COMPRESS
  • 26. 26 The following screenshots are example from COMPRESS
  • 27. 27  HTRI Fundamentals of Exchanger Design  COMPRESS , BUILD 7500  COMPRESS REPORT RGX6_663-E016, Provided by - Leonard Stephen Thill, san, Principal Piping – Lead Piping Stress Specialist, Stress & Static Equipment References

Editor's Notes

  1. Once This work has done we can prepare HT DS.
  2. 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:
  3. First Process Engineer to prepare the thermal rating part of datasheet them move to mechanical engineer to complete the datesheet.
  4. 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.
  5. 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.
  6. 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.
  7. 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
  8. 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.
  9. 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
  10. 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
  11. 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
  12. 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
  13. 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
  14. 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