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No. 64 September 2008

news from AspenTech - heat exchanger design excellence through research
 

In this issue....

What's New aspenONE V7.0

Aspen HTFS Research Network

Aspen HTFS Annual Questionnaire

Customer Presentations at 2008 UGMs

UGM 2009

Training

Current Products

To Contact Us

 

 

Aspen Exchanger Design & Rating - What's New in V7.0

Product Name Changes in aspenONE V7.0
With the release of aspenONE V7.0, AspenTech has elected to adopt functional names for several of its key Process Engineering products.

The new names will reflect the function/role that products perform as standalone, or as part of the overall Aspen Engineering suite. The old and new product names are shown below:

Old Name New Name  Short Name
Aspen HTFS+ Aspen Exchanger Design & Rating EDR
Aspen Tasc+ Aspen Shell & Tube Exchanger  Shell&Tube
Aspen Acol+ Aspen Air Cooled Exchanger  AirCooled
Aspen Teams Aspen Shell & Tube Mechanical  Shell&TubeMech
Aspen Plate+ Aspen Plate Exchanger  Plate
Aspen FiredHeater Aspen Fired Heater  FiredHeater


Aspen Exchanger Design & Rating (EDR) User Interface (formerly Aspen HTFS+ Design System)

V7.0 includes both improvements to the user interface as well as technical enhancements to the methods and correlations used by the various programs. Some of the highlights of the new release are documented in the following sections. Detailed documentation providing complete information on all changes will be supplied with the product update. Immediately below are enhancements which apply to the EDR-UI.

Copy/Paste Functionality Added for Aspen Simulation Workbook
Aspen Simulation Workbook provides easy and robust integration between AspenTech's process simulators and Microsoft® Excel, allowing you to deploy models to a wider range of users without writing a single line of code. As a core element of AspenTech's aspenONE™ Process Engineering applications, Aspen Simulation Workbook is tightly integrated with the Aspen Plus®, Aspen HYSYS®, Aspen Custom Modeler®, and the Aspen Exchanger Design & Rating product families.

A new Copy/Paste functionality has been added to the Shell&Tube, AirCooled, Plate, FiredHeater, and Shell&TubeMech programs which will allow input and result variables shown in the EDR user interface to be copy/pasted into Aspen Simulation Workbook for full run-time integration.

Aspen Properties Package Displays Component Names
When Aspen Properties is selected as the physical property package, the user will now see Component names as well as the formula in the component list.

Plots of Physical Properties Now Available on Properties Form
A new tab has been added to the Physical Properties forms to show plots of all physical properties at all pressure levels. Properties can be plotted against temperature or specific enthalpy. Various controls are available for zoom-in/out, printing, copying, or saving the plots. Plots can be immediately viewed by merely selecting the desired X and Y variables shown on the left hand side of the form.

Component Properties Now Available on Properties Form
A new tab has been added to the Physical Properties form to show key component constants. These include: molecular weight, critical pressure, critical temperature, liquid molar volume, normal boiling point, accentric factor, and dipole moment.

New Plots for Interval Analysis
A new tab on the interval analysis result forms allow the user to view plots of the values displayed in the interval analysis tables. The plot below shows 2 exchanger in series with each unit having 2 tube passes. A variety of parameters listed on the left hand side of the form can be plotted against the physical location in the exchanger(s) or the heat load. Various controls are available for zoom-in/out, printing, copying, or saving the plots.

Aspen Shell & Tube Exchanger (formerly Aspen Tasc+)

Rigorous simulation of reboilers in Aspen Plus and HYSYS Columns
A new interface has been provided within the Aspen Plus and HYSYS simulators to allow the EDR Shell&Tube program to perform rigorous reboiler calculations for the simulator column models. These allow for both kettle and thermosiphon calculations in design, simulation and rating modes.


The new column interface supports multiple column configurations

Rapid Design of Thermosiphon Reboilers
Tasc+ has always handled rigorous simulation of horizontal or vertical thermosiphon reboilers. This capability has been expanded with the release of Shell&Tube, to include a rapid Design mode as well as a Checking (Rating) model.

The Design calculation produces an optimized horizontal or vertical thermosiphon geometry with a user-defined cold stream flow. The option allows the user to simply specify the effect of inlet and outlet pipework losses as fractions of the available driving head. Alternatively users may specify pipework and fittings in detail.

Many users may prefer to finalize their design in simulation mode which continues to be available for “fixed flow” or “find flow” calculations.


Piping default dimensions are now available for supporting
the new design mode for thermosiphons

When Fixed Flow thermosiphon calculations are performed, any pressure inconsistencies around the thermosiphon loop are reported, both by a Results Warning and in the Thermosiphon Piping output. This allows you to evaluate their significance, and either re-specify the thermosiphon to eliminate the inconsistencies, or run in Find Flow mode which converges to a balanced loop with no inconsistencies. The main Thermosiphon Piping output tab has also been improved, showing flow conditions at both the exchanger outlet and at return to the column, so any flashing in the return line will be evident.

Debottlenecking with hiTRAN® Wire Matrix inserts
The proprietary hiTRAN wire matrix inserts, manufactured by Cal Gavin, are often used to improve the performance of tubular heat exchangers. These can now be modeled using Shell&Tube. There are two calculation options: one is "Find Insert", which identifies the particular insert appropriate to your tube size and exchanger duty; the other uses a specified insert identifier to simulate the performance of that particular enhancement device. Insert identifiers correspond to the part numbers of installed devices or those found using the "Find Insert" method described above. The inserts are primarily intended for single phase duties. Approximate results are also provided, however, when some or all of the duty is two-phase.

Please contact Cal Gavin directly for access to their integrated program for modeling hiTRAN with Aspen Shell&Tube.

Dealing with Acoustic Resonance - De-resonating Baffles
One of the conditions reported in the vibration output is the possibility of Acoustic Resonance. Often users will employ de-resonating baffles to protect against this form of tube vibration phenomena. Users may now specify the number and location of de-resonating baffles and these will be fully accounted for in the Shell&Tube vibration calculations. At present these special baffles will not appear in the tube layout but if they require the removal of tubes, you can simply specify the remaining number of tubes for the correct appraisal in thermal-hydraulic calculations.

Condensation Over a Temperature Range
In condensation over a temperature range, previous Tasc+ versions determine the surface area required to cool the vapour-gas to the required outlet temperature. This continues to be the default method in Shell&Tube V7.0. However, in practice, when the outlet temperature is above the bubble point, the vapour-gas and condensate outlet temperatures can be different. Shell&Tube V7.0 provides a new option in which the calculation is weighted towards the area required to cool the condensate to the required outlet temperature. This will usually give higher overall heat transfer coefficients than the default method, and is similar to the method used by the Hetran program. There is a new input item in the Program Options form to allow selection of the appropriate method.

Calculating Stream Outlet Composition
Often designers will require knowledge of the detailed composition of streams leaving an exchanger. For example, a condenser may be designed to recover a solvent and the release of that material to atmosphere may be prescribed by environmental legislation. Where physical properties are calculated using one of the internal property packages like Aspen Properties® or COMThermo®, users are provided with a new output table which lists the inlet and outlet composition on a component basis including: mass fraction; mole fraction and addressing which component fractions are in liquid and vapor phases.

Modelling Shellside Viscous Flow
Following extensive research, a correction has been incorporated in the shell side heat transfer calculations for viscous flows where the cross flow Reynolds number is less than 30. The correction allows for the cumulative effect of ineffective mixing between the bulk of the flow and the fluid close to the tube wall within the tube bundle. It has the effect of reducing the heat transfer coefficient. Corrections factors in the range of 0.7 to 0.9 will typically be experience with highly viscous flows. However, with large tube bundles and very low Reynolds numbers more substantial corrections may be seen.

Selecting ASME and ISO Nominal Nozzle Sizes
A new input item has been provided to allow users to select nominal nozzle sizes from a list of all standard ASME and ISO pipe sizes. This input can be used to set the actual outside diameters of the nozzles.

Aspen Air Cooled Exchanger (formerly Aspen Acol+)

New Airside Methods for Heat Transfer and Pressure Drop
From our ongoing research on finned tube bundle performance we have recently developed the HTFS3-AC methods. These have been optimised specifically for application to air cooler tube bundles. They are most applicable for geometries and process conditions in the following ranges:

Tube outside diameter: 25.4 and 31.75 mm
Fin height: 10.55 to 15.9 mm
Fin frequency: 350 to 433 fpm
Fin thickness: 0.28 to 0.47 mm
Fin tip clearance: 3 to 10 mm
Air face velocity between 1 and 9.5 m/s
Air temperature between 0 and 100 deg C

HTFS3-AC is the default method for air cooler geometries and process conditions within the above ranges. It is fully documented in the Research Report: RS1197.

The pressure drop predictions of the HTFS3-AC method are on average about 4% lower than those of the general HTFS3a method, but larger differences are possible depending on air velocity and temperature. Heat transfer predictions of the HTFS3-AC method are on average within 2% of the HTFS3a method, but larger differences arise at the extremes of the air face velocity range.

The following extract from the AirCooled Recap table shows how designing a process air cooled heat exchanger using the new HTFS3-AC method can indicate operational cost savings approaching 20%.

Radiation Heat Transfer Option Extended
A new input for radiation heat transfer calculations in heat recovery applications allows the user to specify the mole fraction of radiating species in the flue gas. In previous versions of Acol+ a default value of 0.22 was used in the calculations. The value of the input mole fraction will affect the radiation heat transfer coefficient.

Maximum Tube per Row Increased From 99 to 200
The previous program versions limited the number of tubes per row to 99. We have expanded this limit to now allow up to 200 tubes per row. We have also incorporated some additional error checking into the program to catch geometry combinations which the program may not be able to accommodate.

Aspen Fired Heater (formerly Aspen FiredHeater)

Aspen Properties Package Option Added
Additional power has been added to the property options available in FiredHeater. Users may now select components, VLE methods and mixture calculations from Aspen Properties® in addition to COMThermo® and the B-JAC property databanks.

Fired Heater Inlet Pressure and Checking Calculation Options
For Fired Heater V7.0, in addition to the existing calculation where outlet pressure is calculated from a specified inlet pressure, there are several new pressure calculation options for each process stream. These are:

Fired Heater Diagrams
Three types of diagrams have been added to FiredHeater for V7.0. These are developments of diagrams seen in the heritage FIHR program.

a) Overall layout diagram is located on the Heater Geometry|Gas Flow|Heater diagram tab. This shows the: basic firebox layout; number of convection banks; presence of stack and air-preheat.

b) Connections diagram: located on the Heater Geometry|Convection Banks|Connections diagram tab. This shows the flow of each process stream through the firebox and convection banks (e.g., Figure 1).

c) Firebox diagram: located on the Heater Geometry|Firebox |Firebox diagram tab, is a detailed scale diagram of the tube arrangement in the firebox. It shows: tube diameter; number; location; orientation and separation (e.g., Figure 2).


Figure 1: Typical Connections Diagram


Figure 2: Typical Firebox Diagram views

Aspen Shell & Tube Mechanical (formerly Aspen Teams)

Stress Analysis Improved
The stress analysis of a shell-and-tube heat exchanger has been improved with these ASME code changes:

Added Calculation of Maximum Positive/Negative Axial Expansion
Aspen Shell & Tube Mechanical can now calculate the maximum positive and negative axial expansion. This calculation is performed for fixed tubesheet units without expansion joints. The program can now provide the maximum positive and negative axial expansion (the amount the tubes can move in reference to the shell without the exchanger being overstressed).

Expanded Design/Operating Load Conditions to 13
Aspen Shell & Tube Mechanical can simultaneously perform the calculations for up to 13 design/operating load conditions. The user can now enter operating pressures and temperatures to cover a range of conditions that an exchanger will experience during operation. The design selected by the program will satisfy all stated conditions of pressures and temperatures. This capability will greatly simplify designs that need to comply with many different conditions. The overall mechanical design quality is highly dependent on the correct thermal data transferred to Shell & Tube Mechanical, thus emphasizing the importance of transfer of information from Shell & Tube Exchanger.

Wind and Seismic Load Calculations Updated
The wind and seismic loads calculation methods have been updated to the latest standards, the International Building Code (2006) and the Minimum Design Loads for Buildings and Other Structures (ASCE 7-05).

Improved the Tube-to-Tubesheet Joint Load Calculations
The tube-to-tubesheet joint loads calculations for floating tubesheet exchangers have been improved in completeness and presentation. The factor ¦T, used to account for the relative thermal expansion of the tubes and tubesheet, has been further refined. It can now take account of the condition where an expanded-only joint can weaken to the point at which it no longer provides adequate joint strength. In such cases, a message will be issued to alert the user of this potential danger.

Learn more about V7 - Sign up for the webinar series, request a demo, and see what else is new in this game-changing release. Click here

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Aspen HTFS Research Network

Since its formation in 1968 HTFS has worked with the industry to develop state of the art models and methods for process heat transfer and related equipment using both in-house and collaborative research. This essential requirement of research has continued after HTFS became part of Aspen Technology in 2002. Much of the modeling information that is generated through the continuing programme of analytical and experimental research is proprietary in nature. Our software licensees benefit from this modeling information because it forms the basis of technical developments in our software.

Our research brings improved design which offers capital and operating savings whilst still providing assurance on specification performance. Some recent direct benefits we can demonstrate include:

  • Advanced flooded evaporator model for Shell&Tube (potential 30% capital saving)
  • Improved airside pressure drop methods for AirCooled (demonstrating around 20% lower operating cost - see our description on Aspen Air Cooled Exchanger above)
  • Advanced handling of multicomponent condensation (showing potential 19% capital saving)
  • Post dryout heat transfer modelling (similar capital savings to the above)
The above are just of few examples of the competitive advantage our research can bring to our customers.

In addition to these benefits delivered through our software releases, there is another, more immediate way of tapping into the benefits of our on-going research activity and that is through the Aspen HTFS Research Network. Using the Research Network our customers can have direct on-line access to the research based modeling and design information. In addition the Research Network licensees can also enjoys some special privileges. They can participate in the Aspen HTFS Industrial Review Panels, which discuss the on-going development of software and research before it reaches the wider customer base.

Following are some of the unique benefits that can be derived by subscribing to the Research Network.

  • Access to core HTFS technology and expertise developed over the years
  • Insight into the methods and models that are used in our heat transfer equipment design programs
  • Partnership with Aspen HTFS through participation in the Industrial Review Panels
  • Validation and QA of the models and methods in software
  • Other practical uses of the Research Network information, e.g, for troubleshooting or performance monitoring of heat exchangers
The information available in the Aspen HTFS Research Network can be grouped in four different areas:

HTFS Handbook: a comprehensive reference to heat exchanger theory and practice. It contains 142 process sheets which describe various physical processes such as boiling and condensation, 52 equipment sheets which describe various equipments such as fired heaters, reboilers etc and 244 method sheets which describe calculation procedures in stepwise manner, along with a worked example. There are some 35 Handbook sheets which cover other important topics.

HTFS Design Reports: detailed derivation and comparisons of design methods; validation of design procedures and description of the technical methods used in the Aspen Exchanger Design & Rating (EDR) programs.

HTFS Research Reports: generated from our extensive and on-going research programme over the years. Currently there are more than 1200 Research reports, with more being added each year.

HTFS HEATFLO: a database containing bibliographic references to over 120,000 high quality experimental and theoretical research papers in the field of applied heat transfer and fluid flow relevant to the needs of the chemical process and power industries.

This wealth of information facilitates:

  • Improved design: by enabling full understanding of the heat exchange models, assumptions and correlations used within AspenTech's heat exchanger software, to help ensure quality designs.
  • Improved process operations: by providing access to a knowledge base to optimize and troubleshoot plant performance.
  • Increased engineering efficiency: by providing data for the development or update of in-house models, correlations and tools to ensure these are based on the latest and most accurate methodology.
The Aspen HTFS Research Network can thus be regarded as a comprehensive reference to the science and technology supporting the Aspen EDR thermal design programs.

Searching the Aspen HTFS Research Network
To enable fast and easy retrieval of the relevant information the contents can be searched using the powerful Google Search Application.

This has also been enhanced recently to allow the user to target their search to specific document types such as the Handbook, Research Reports, Design Reports. By clicking the link "or Search by section (Handbook etc)" which appears underneath the search box; a new window will open allowing the user to select the required section(s) to search.

Once in the Google results page you can further refine your results by accessing additional advanced search features such as searching within the results, restricting the search words to the document title only etc.

Search Example
Suppose we want to find a research report on two-phase pressure drop models and correlation for serrated fins which are commonly used for boiling applications in plate fin heat exchangers. We enter the search string "serrated fin two-phase pressure drop" and restrict the search to the Aspen HTFS Research Reports section.

From the search results we find that the most relevant Research Report is RS1125.

We open the RS1125 and obtain information on modeling methodology for two-phase pressure drop in serrated fins. However, the two-phase correlations need information for single phase friction factors which is documented in Aspen HTFS Handbook Sheet YM12.

The cross linking allows the user to click on the link for YM12 to open that document too.

The search facility and cross links make it so easy to find the information that you need!

If you do not have a license to access the Aspen HTFS Research Network already then contact your nearest AspenTech sales office for a quote or e-mail us at htfs@aspentech.com.

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Aspen Exchanger Design & Rating Annual Questionnaire

Each year we broadcast out to our users an annual questionnaire. The questionnaire provides our group with very important feedback as to how well we are meeting the requirements of our users. The questionnaire covers an exhaustive set of questions surrounding each of our products. The responses provide us valuable feedback as to what we are doing well and where we need to improve. The questionnaire also provides information in regards to what future program enhancements and improvements are most needed to best meet the needs of our overall customer base.

The top three program development requests from the recent questionnaire are shown below for our thermal design programs. You will see as we begin to make public our future product plans that many of these items are included in our roadmap for release in the near future.

Aspen Shell & Tube Exchanger (formerly Tasc+)

  1. Improved calculations of combined heat and mass transfer (particularly for mixture condensation).
  2. Design and simulation of a range of different series/parallel arrangements, for example multiple shells with cold fluid in parallel and hot fluid in series (with identical shell geometries).
  3. Allow different numbers of tubes per pass in the thermal calculations.

Aspen Air Cooled Exchanger (formerly Acol+)

  1. Allow gas-side condensation in heat transfer calculations for gas cooling applications.
  2. Improved calculations of effect of phase separation on exchanger thermal performance for non-isothermal condensers.
  3. Provide interfaces to manufacturers' fan selection software (Moore, Howden, Cofimco).
Aspen Plate Exchanger (formerly Plate+)
  1. Improved heat transfer and pressure drop methods for boiling and condensation.
  2. Simulation of heat exchangers similar to Compabloc
  3. Simulation of plate and shell heat exchanger
Aspen Fired Heater (formerly FiredHeater)
  1. Improved modeling of peak heat fluxes and peak wall temperatures in firebox tubes.
  2. Include a simple model for thermal performance of an air preheater.
  3. Option to find firing rate by varying one fuel flow, with other fuels fixed.
Aspen MUSE (will become Aspen Plate Fin Exchanger with V7.1)
  1. Flow distribution calculations among cores
  2. Detailed modeling, e.g. heat transfer variation across the width of each layer.
  3. Simplified Exchanger Geometry Input, based on the layers which make up the exchanger.
The questionnaire is just one means by which you can influence future program direction. We want to thank all of you who recently responded to the questionnaire and hope to have an even greater response from you next year.

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Customer Presentations at AspenTech User Conferences - Spring 2008

The 2008 AspenTech User Conferences were held in the Spring of 2008 in Houston, TX and Berlin, Germany. These incorporated full sessions on EDR and attracted many customers from the HTFS and B-JAC user communities. The following indicates the general level of attendance.

Venue Customer
Attendance
Companies
Represented
Houston389132
Berlin 329 110

The Heat Exchanger sessions were attended by in excess of 88. We also held highly successful courses on Tasc+, Condenser Design and Operation and on Heat Exchangers for Process Engineers using HYSYS.

From our survey of customer feedback on the conferences it was clear that many attendees found the Customer Presentations particularly valuable. We will continue these sessions at our 2009 User Conference. We would urge you to look out for the call for papers and consider presenting at this event which will draw together many leading industry practioners.

A summary of the 2008 presentations follows.

Integrating Exchanger Design into the Whole Process Design Cycle: presented by A. Venables and M. Jansen of ENGlobal. This presentation discussed the engineering life cycle and the benefits achieved on an actual revamp project by taking advantage of the aspenONE integrated solution.

Representing Process Fouling in Design and Monitoring Fouling on Exchangers Using Aspen Tasc+: presented by Kal Zimmerman of Fluor Corporation. A discussion of fouling and its impact on heat exchanger design was given. The session covered the various types of fouling, factors affecting the rate of fouling, and practical ways of reducing the size of heat exchangers by minimizing the fouling resistance and reducing the tendency to foul.

Migration from HTFS / B-JAC to HTFS+ within Sasol: presented by Ralph Grob of Sasol Technology. Sasol has done most of the designs for Heat Exchange applications on either B-JAC or HTFS software. In recent years AspenTech has migrated this software to HTFS+. Dr. Grob discussed Sasol's strict governance procedures necessary to ensure the "new" programs adhered to existing specifications and that results from old and new applications were consistent. The links to Aspen Plus were also reviewed to see that the detailed models from Aspen Plus were able to better use the HTFS+ applications and provide results in a meaningful manner to the engineers at Sasol.

Quiz for Heat Exchanger Selection & Design: presented by M. Shah of Worley Parsons. Mr. Shah's presentation was given in two parts, the first section discussed a number of topics including necessary information to perform the heat exchanger design calculations along with vibration; heat exchanger component selection; practical values of heat transfer coefficients; TEMA; mechanical design constraint; fabrication issues; transport and piping limitations. The second section discussed step by step procedure for selection and design of exchangers; covering detailed methodology of analyzing exchanger design, using manual techniques in conjunction with commercial software.

Improvement of In-House Compression Tool with Integration of Tasc+: presented by Andreas Allenspach of Burckhardt Compression AG. Mr. Allenspach discussed integrating their in-house compressor design and selection program with Tasc+ through a Microsoft based COM interface and the resulting projected benefits achieved through better process and equipment optimization, reduction in errors and increased sales.

Optimisation of a Large Feed/Effluent Heat Exchanger Revamp by the use of Tasc+ and hiTRAN® Wire Matrix Elements: presented by Peter Drögemüller of Cal Gavin Ltd, U.K. The presentation focussed on integrating Cal Gavin's Wire Matrix Elements with the latest version of Tasc+. Resulting benefits on a feed/effluent revamp project included: higher duties from an existing exchanger; elimination of a replacement heat exchanger; reduction in fuel costs for a fired heater and a reduction in CO2 emissions.

Experience with Modeling a Wide Range of Process Exchangers using Tasc+: presented by Oleg Pajalic of Perstorp AB. The company has used both the HTFS and B-JAC programs for heat exchanger design since 1996. Mr. Pajalic discussed the close agreement obtained between AspenTech program prediction and actual exchanger performance. He presented reference to plant data on a considerable number of heat exchangers over a wide range of process applications.

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Worldwide AspenTech User Conference - May 2009

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Training

Check out our training web site at: support.aspentech.com/supportpublictrain/TrainHome.htm

Full course descriptions can be viewed and you can register online.

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Current Products

Register at
support.aspentech.com/supportpublicasp/RegisterBegin.asp to enable you to download the latest patches, receive relevant monthly e-Bulletins, search Knowledge Base for solutions and submit & track your own enquiries.

EDR products
Aspen Shell & Tube Exchanger V7.0

Design and performance simulation of all your shell and tube heat exchanger requirements, including thermosyphons.

Aspen Shell & Tube Mechanical V7.0
Mechanical design of shell and tube heat exchangers.

Aspen Air Cooled Exchanger V7.0
Software for design and performance simulation of air cooled heat exchangers and simulation of heat recovery units, air conditioning and refrigeration exchangers.

Aspen Plate Exchanger V7.0
Design, rating and performance simulation of plate heat exchangers.

Aspen Fired Heater V7.0
Simulating the performance or rating the burner fuel flow rates for process fired heaters.

HTFS Research Network TM www.htfs.com/resnet.asp
The HTFS knowledge base developed over the past 35 years. This includes online access to our proprietary methods within the Handbook, Research Reports and Design Reports via the web. Customers can also have a close involvement in directing our research and the evolution of our products through participation in Review Panels.

Review Panel Chairmen
Tubular Heat Exchangers    Jim McNaught
Furnaces & Fired Heaters    David Oakley
Compact Heat Exchangers   Vishwas Wadekar

Other products
Aspen MUSETM V7.0
- soon to be replaced by Aspen Plate Fin
Performance simulation layer by layer, crossflow calculation and 'first-shot' thermal design of multistream plate-fin heat exchangers.

Aspen APLETM 2006.5
A single package for design, rating and performance simulation of gasketed plate and frame heat exchangers (support will cease as of 31st December 2008).

Aspen FIHRTM 2006.5
Simulation of fired process heaters, including radiant and convection sections with multiple process streams. (support will cease as of 31st December 2009).

Aspen FRANTM 2006.5
Rating and performance simulation of power plant feedwater heaters.

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To contact us                                         

E-mail: htfs@aspentech.com
Web: www.htfs.com

Development centre
Reading, UK
Tel:+44 (0)118 9226405
Fax:+44 (0)118 9226401

Details of further office locations can be found at: www.aspentech.com/corporate/locations.cfm
 
Technical Support Centres
e-mail: esupport@aspentech.com

See the website for a complete list of phone & Toll-free numbers in your area
support.aspentech.com/SupportPublic/centers.html

Europe and Africa (EMEA)
+ 44 (0)118 9226555
Middle East (EMEA)
+965 4610790

North America, Latin America (NALA)
+ 1 888 996 7100 (Toll-free from US, Canada, Mexico)
+ 1 718 221 5500 (from outside US, Canada, Mexico)

Asia and Pacific Region
00 44 22 132920 (Japan)
10 800 120 712 2160 (China)
000 800001 0020/6020 (India)
00798 14 800 7569 (Korea)
800 120 5022 (Singapore)
1 800 203224 (Australia)

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Aspen Technology, Inc., Worldwide Headquarters, 200 Wheeler Road,
Burlington, MA 01803, USA
Tel:+1 781 221 6400 1030