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Condenser Critique 2.0

Software for sizing and testing the performance of shell and tube cooler condensers

ü

Save money by operating your condensers efficiently
ü Calculate condenser operating costs
ü Optimise use of cooling water
ü Calculate saturation in vapour/gas mixtures
ü Calculate condenser pressure losses
ü Test effect of any process change on condensers
 
Free Condenser Critique Example Spreadsheet!
Click here to download a full read only example of Condenser Critique. (Excel 97, 2000 or 2003 required)
 
Condenser Critique has been developed on the principles of the Colburn & Hougen method. It utilises spreadsheets to provide the user with a method for sizing and testing condensers handling vapour/gas mixtures.

Shell and tube condensers come in different sizes, are used in various applications and all require large amounts of cooling water. Their use in the vacuum field where very low pressure losses are required imposes special requirements.

Detailed insight into the performance of these condensers can lead to reduction in operating costs if cooling water can be more effectively utilised. It will also assist in predicting the behaviour of such condensers where fouling/ scale and variation in operating conditions need to be considered. At the design stage, it provides a useful aid when establishing the relationship between performance, capital costs and operating costs.

Software Specification
The software comprises a series of dedicated multi-page spreadsheets which are run under Microsoft 2000 or 2003 for Windows 2000/XP based IBM compatible PC’s.

A 30 day e-mail and fax support service is provided.
The software comes with comprehensive electronic documentation and examples.
Customisable installation via state of the art setup software.
Please note that Microsoft Excel is not supplied with Condenser Critique.

Payback on the software cost is usually achieved within days once operating parameters have been optimised!

The software comprises worksheets which provide the following functionality:

  • Composition and conditions of vapour/gas mixtures
  • Saturation in vapour/gas mixtures
  • Condensation parameters: Colburn & Hougen method using "j" factor
  • Condenser physical parameters
  • Condenser pressure losses - Kern's method for shell side
  • Cost of purchase and installation
  • Condenser operating and total costs
  • De-superheating in condensers
  • Steam condensation on horizontal tubes
  • Optimum use of cooling water
  • Condenser data summary
  • Selected parameters for vapours and gases
  • Assorted fouling factors
  • Data for some physical properties of air, selected gases, water and selected vapours

Condenser Critique comes with comprehensive documentation and examples.
 

Specific uses of Condenser Critique 2.0
Condenser Critique has a wide variety of uses, with some the most useful being as follows:
  • Examination of the effect of controlling parameters on performance prior to condenser purchase
  • Establishing of limits for fouling coefficients on cooling water side of condenser
  • Establishing of limits and the effect of air leakage in vacuum condensers
  • Establishing the effect of changes in cooling water temperature; seasonal or operational
  • Checking of the performance of operating condensers
  • Optimisation of cooling water usage
  • Any desired process change can be tested for effect on condenser performance without interfering with plant operation
  • When composition of the non-condensables or the vapour needs to be changed, the effect on condenser performance can be tested.
Principle of Software Operation
Stage 1

The user is invited to select between five and twelve segments for the condenser and to select vapour bulk temperatures for each segment. At this stage the thermal duty and cooling water requirements are established.

Stage 2
Estimated values for the interface temperatures are input and, using iteration procedure, the correct interface temperature is established for each segment in sequence. On completion, the surface area and length for each section, as well as the relevant parameters for each segment are available.

Stage 3
A method is provided for estimating the pressure loss for the condenser. This is crucial where condensers are used in vacuum systems, bearing in mind that the permitted limits for pressure loss are fundamental to condenser selection and design and to the feasibility of vacuum system.

N.B. This software deals with condensation of single component vapours only.

 
Example Condenser Data Summary Output
CND12  Condenser data summary                
                 
Calculation reference               :   CONDCHMPA            
Calculation object                      :   Updating for presentation and costs            
If condenser  for vacuum duty  :   Standard example C & H            
Calculation date and time        :   11-Aug-03   10:13:37        
                 
Gas/vapour composition:            kg/h   Mol. Wt.    
Non condensables   Nitrogen   1,270.000   28.016    
Condensing vapour   Water vapour   4,131.389   18.016    
                 
Condenser physical parameters:                
              Sections: 9
Exchanger tube   Arrangement:   Triangular     Number: 88
Shell/tubesheet material   (-)   C/MS     Tube clearance: 6.350
Tube   Material   C/MS     Tube passes: 1
Baffle   % cut   45     Number: 30
Nozzle diameter, mm   Inlet:   350.00     Outlet: 150
                 
Calc. diameter of tube bundle   mm   262.63        
Inside shell diameter - used   mm   605.63        
Shell bundle clearance allowance   mm   343.00        
Baffle spacing   mm   421.00        
Outside tube diameter   mm   19.05        
Tube wall thickness   mm   1.651        
Total length of tubes - calculated   m   13.116     Available m: 12.63
Thickness of tube sheet   mm   35.000        
Outside condensing surface - calculated   m^2   65.762     Available m^2: 66.52
Min. shell section area for flow   m^2   0.102        
Equivalent tube diameter   mm   18.542        
                 
Pressure losses:                
Condenser total pressure loss   mbar   43.529        
Shell side pressure loss   mbar   39.847        
Nozzle pressure loss, mbar   inlet   2.233     outlet: 1.45
                 
Condenser conditions:                
Inlet vapour/gas mass flow rate   kg/m^2.h   52,961.19        
Pressure at condenser inlet   mbar   1,013.00        
Gas/vapour inlet temperature   oC   95.02        
Gas/vapour outlet temperature   oC   40.00        
CW temp. at inlet to condenser   oC   25.00        
CW temp. at outlet from condenser   oC   60.00