Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Question Regarding Mass Balance Around A Crystalliser In A Sugar Refin


This topic has been archived. This means that you cannot reply to this topic.
7 replies to this topic
Share this topic:
| More

#1 yanparker

yanparker

    Brand New Member

  • Members
  • 4 posts

Posted 23 November 2013 - 12:15 PM

Hello,

I am working in a team trying to do a mass balance for a sugar refinery. The units consist mainly of affination, clarification, decolorization, crystallization, and drying. We have been given the required output specifications (in terms of pol, invert, ash etc) and the output flowrate. We have started to work out the mass balance backwards. So far, we have been using typical values as assumptions.

 

But we have been facing some problems with the crystallization part...

There are 3 sugars coming out of 3 centrifuges and a final molasse.

We have not been able to find out how the values are affected in each of the set of vacuum pans, mixer and centrifuges(there are 3 set). Could you kindly advice on how we can proceed.

 

Thanking you in advance



#2 curious_cat

curious_cat

    Gold Member

  • Members
  • 475 posts

Posted 23 November 2013 - 12:57 PM

I think you need to provide specific details, numbers & a sketch before anyone can help you much on this. 



#3 breizh

breizh

    Gold Member

  • Admin
  • 6,723 posts

Posted 24 November 2013 - 01:46 AM

http://www.sugartech...ugals/index.php

 

Consider this resource Engineering Guide ( specific to Sugar plant and engineering) to support your query . As stated by Curious cat lack of information is not helping us to help you.

 

Breizh


Edited by breizh, 24 November 2013 - 01:50 AM.


#4 yanparker

yanparker

    Brand New Member

  • Members
  • 4 posts

Posted 24 November 2013 - 09:25 PM

Cristalizacao_Three_Boilings.jpg

 

 

Here is a picture of the units. Basically, we have a set of unit operations for the sugar refinery, and we have to do a simple mass balance. Since we have been given the desired output ( 99.5 % pol, 0.05 invert, 0.05 Ash, 0.06 % moisture),, and the flowrate 28 kg/s,

we have been working the mass balance backwards.

 

For example, in the dryer, which is the last unit after crystallisation, we have assumed the initial moisture content to be 0.8% based on some typical values.

 

So we know what is coming out of the crystallisation ( including the colour which is 50 IU).

 

But since the crystallisation is divided into three parts, and has 3 different sugar that are mixed together, we find it a bit difficult to find a way to calculate the mass balance. Do you have any suggestions?

 

Thanks a lot!



#5 breizh

breizh

    Gold Member

  • Admin
  • 6,723 posts

Posted 24 November 2013 - 11:26 PM   Best Answer

http://www.nzifst.or...qseparation.htm

 

Consider these resource to support your study . You will find examples about the technology and the balances .

 

Breizh



#6 yanparker

yanparker

    Brand New Member

  • Members
  • 4 posts

Posted 25 November 2013 - 12:31 AM

http://www.nzifst.or...qseparation.htm

 

Consider these resource to support your study . You will find examples about the technology and the balances .

 

Breizh

Thank you very much!! We have been very late with our mass balance, being stuck at this seemingly complicated part. Now we have a good idea how to proceed!

Thanks again!



#7 JJDR

JJDR

    Brand New Member

  • Members
  • 1 posts

Posted 01 December 2013 - 03:23 PM

Hi i am actually doing a design on the same topic as you, and I am having the same difficulties, I will be grateful if you could help me with the mass balance! Thanking you in advance.



#8 ashishmishra1234

ashishmishra1234

    Junior Member

  • ChE Plus Subscriber
  • 19 posts

Posted 15 January 2014 - 03:18 AM

You can also go through sugarmill.co.in






Similar Topics