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This is a design model for Multiple-effect distillation parallel feed configuration (MED-PF). It consists of multiple stages or "effects". In each stage the feed water is heated by steam in tubes, usually by spraying saline water onto them. Some of the water evaporates, and this steam flows into the tubes of the next stage (effect), heating and evaporating more water. Each stage essentially reuses the energy from the previous stage, with successively lower temperatures and pressures after each one. Additionally, between stages this steam uses some heat to preheat incoming saline water. User can assign the following:

1- Top steam temperature, oC.

2- Inlet feed temperature, oC.

3- Last effect temperature, oC.

4- Performance parameters for the pumps and end condenser unit.

5- Feed and brine salinities ratio.

6- Cost analysis has been added to the 2nd version file.

 

** Watch the tutorial video at:

https://www.youtube.com/watch?v=MRaoFR5xNWU&t=35s

**MatLab-SimuLink should be used to run the model.
email us for the password (msherafeldin@gmail.com)

Copyright © 2007 by Mohamed A. Sharaf Eldean Ayoub
All rights reserved. No part of this work may be reproduced, distributed, or transmitted in any form or by any means, including photocopying, recording, or other electronic or mechanical methods, without the prior written permission of the publisher (Mohamed A. Sharaf Eldean Ayoub). For permission requests, write to the publisher, addressed “Attention: Permissions Coordinator,” at the address below.

 

REDS Software Library

https://www.redslibrary.com

Kuala Lumpur Malaysia

mohamedsheraf@redslibrary.com

00601139795943

All Rights Reserved

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Multi Effect Distillation Parallel Feed (MED-PF)

SKU: DESmedpf
€220.00 Regular Price
€218.00Sale Price
  • User can reform his model based on his need. Simulink (64bit) is used for model creation. Please run the model from its folder and set the matlab bath to the same file folder.

  • You can request a discount coupon from us before download.

© Created in 2017 by  REDS Library. All rights reserved.

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