1. Attachment "Assignment" is the whole complete assignment.
2. Attachment " Proposed PFD" is the proposed PFD by the group. Note that this might not be correct. Please check and correct as you see fit.
3. Attachment " Proposed Mass Balance" is the proposed Mass Balance calculation from the group. Please check and correct as you see fit.
Dateline is the 20th of March but since this is group work, I am required to submit certain part of the assignment be certain weeks.
With reference to the Attachment "Assignment", POINT 2 details what is required and POINT 3 details the specification of the requirement. Please complete everything as stated in POINT 2.
Note that all answers and calculations must be detail and justified. Any literature txt must be reference.
Please do not wait till you finish everything before you submit to me. please submit to me once job is done as I will need to discuss with my grup members.
There are 10 parts of the project which is stated in POINT 2 of the assignment. I require 3 parts to be given per week.
5th March: 2.1 to 2.3,
10th March: 2.4 to 2.6 and
15nd March: 2.7 to 2.10
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Deadline is mentioned above.
PRICE : $ 50
Chemical engineer (Masters' degree) with experience in equipment design, energy and mass balance, PFD design/optimization and academic writing.
Ready to begin your task now.
plant design and evaluation is one of my job daily tasks, to achieve what you want i can use computer simulation kits that i usually use in my plant design tasks
I am a professional process engineer and I can do this project for you. I already completed several real life projects. The total buggets of these projects was more than 238 million dollars. For details about this project please feel free to contact with me.
Hello Sir I am a chemical engineer I recently passed out in 2014 Batch I have completely read your assignment. Although I don't understand that you have missed the 5 march deadline( I am new here). I can totally supervise this project and deliver it on time. I have read the attachments and they are in NO WAY complete and authentic for e.g the heat exchanger only energy balance is done and sizing is not done.
1. For PFD I will use Visio
2. For heat exchangers i will use D.Q kern Heat Transfer
3. For sizing reactor i will use chemical kinetics.
4. Absorber and cooling can be designed by richardson and coulson or any other book.
I assure you the Quality will be more than satisfactory.
Regards,
Waqar Farooq