Category: Chemical Engineering

Hello!! i need you to answer the questions which in the Doc by hand writing. Clear, detailed and recognizable hand writing would be great!!! Thank you so much

Hello!! i need you to answer the questions which in the Doc by hand writing. Clear, detailed and recognizable hand writing would be great!!! Thank you so much

PFD, stream table, reaction kinetics, and specification of the major equipment of the dimethyl ether production unit are provided in the attached file.
a) Use the skills you acquired (diagrams and conceptual chemical process design) and provide a detailed process description for the DME production process. Review Douglas’s method and provide detailed information about process chemistry, input/output stream structure, recycle structure(s), separation systems, utility, and the possibility of heat integration. You can use calculations in Part “b” for a more detailed and specific description. (limit: 500 words)
b) Use engineering heuristics to size the following major equipment:
– E-201, E-202, E-203, E-204
– P-201 A/B, P-203 A/B
– R-201
– T-201, T-202
– V-201, V-203
Follow (step-by-step) heuristic rules for each piece of equipment and provide sufficient details and reasoning for your calculations. Compare your findings with specifications reported in Table B.1.3.
NOTE: The whole concept of heuristics is to make an engineering-based estimate based on well-accepted rules of thumbs. If any required information for part b is missing, use the stream table, process diagram, and database available (Aspen Properties or a simple Google search – with mentioning the reference) to make a logical estimate.
Hints:
E-201 => The temperature for MPS can be found in the text (Page 215) or from Aspen. To estimate Q, calculate the sensible heat and heat of condensation. Even if your numbers are not close to those from the equipment summary, I want to see your cal

PFD, stream table, reaction kinetics, and specification of the major equipment of the dimethyl ether production unit are provided in the attached file.
a) Use the skills you acquired (diagrams and conceptual chemical process design) and provide a detailed process description for the DME production process. Review Douglas’s method and provide detailed information about process chemistry, input/output stream structure, recycle structure(s), separation systems, utility, and the possibility of heat integration. You can use calculations in Part “b” for a more detailed and specific description. (limit: 500 words)
b) Use engineering heuristics to size the following major equipment:
– E-201, E-202, E-203, E-204
– P-201 A/B, P-203 A/B
– R-201
– T-201, T-202
– V-201, V-203
Follow (step-by-step) heuristic rules for each piece of equipment and provide sufficient details and reasoning for your calculations. Compare your findings with specifications reported in Table B.1.3.
NOTE: The whole concept of heuristics is to make an engineering-based estimate based on well-accepted rules of thumbs. If any required information for part b is missing, use the stream table, process diagram, and database available (Aspen Properties or a simple Google search – with mentioning the reference) to make a logical estimate.
Hints:
E-201 => The temperature for MPS can be found in the text (Page 215) or from Aspen. To estimate Q, calculate the sensible heat and heat of condensation. Even if your numbers are not close to those from the equipment summary, I want to see your cal

PFD, stream table, reaction kinetics, and specification of the major equipment of the dimethyl ether production unit are provided in the attached file.
a) Use the skills you acquired (diagrams and conceptual chemical process design) and provide a detailed process description for the DME production process. Review Douglas’s method and provide detailed information about process chemistry, input/output stream structure, recycle structure(s), separation systems, utility, and the possibility of heat integration. You can use calculations in Part “b” for a more detailed and specific description. (limit: 500 words)
b) Use engineering heuristics to size the following major equipment:
– E-201, E-202, E-203, E-204
– P-201 A/B, P-203 A/B
– R-201
– T-201, T-202
– V-201, V-203
Follow (step-by-step) heuristic rules for each piece of equipment and provide sufficient details and reasoning for your calculations. Compare your findings with specifications reported in Table B.1.3.
NOTE: The whole concept of heuristics is to make an engineering-based estimate based on well-accepted rules of thumbs. If any required information for part b is missing, use the stream table, process diagram, and database available (Aspen Properties or a simple Google search – with mentioning the reference) to make a logical estimate.
Hints:
E-201 => The temperature for MPS can be found in the text (Page 215) or from Aspen. To estimate Q, calculate the sensible heat and heat of condensation. Even if your numbers are not close to those from the equipment summary, I want to see your cal

PFD, stream table, reaction kinetics, and specification of the major equipment of the dimethyl ether production unit are provided in the attached file.
a) Use the skills you acquired (diagrams and conceptual chemical process design) and provide a detailed process description for the DME production process. Review Douglas’s method and provide detailed information about process chemistry, input/output stream structure, recycle structure(s), separation systems, utility, and the possibility of heat integration. You can use calculations in Part “b” for a more detailed and specific description. (limit: 500 words)
b) Use engineering heuristics to size the following major equipment:
– E-201, E-202, E-203, E-204
– P-201 A/B, P-203 A/B
– R-201
– T-201, T-202
– V-201, V-203
Follow (step-by-step) heuristic rules for each piece of equipment and provide sufficient details and reasoning for your calculations. Compare your findings with specifications reported in Table B.1.3.
NOTE: The whole concept of heuristics is to make an engineering-based estimate based on well-accepted rules of thumbs. If any required information for part b is missing, use the stream table, process diagram, and database available (Aspen Properties or a simple Google search – with mentioning the reference) to make a logical estimate.
Hints:
E-201 => The temperature for MPS can be found in the text (Page 215) or from Aspen. To estimate Q, calculate the sensible heat and heat of condensation. Even if your numbers are not close to those from the equipment summary, I want to see your cal

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1, The Assignment is based on Lecture notes 5.2–5.4, and may be similar to the example from Tutorial 6 PFR Isothermal Examples which I will provide to you.
2, please finish this question step by step, using the equations from the lecture notes or Tutorial 6.
3, I will also provide you the non-Isothermal Examples if you need them, I’m not sure if the assignment needs non-Isothermal Examples

I am applying for Ph.D. in chemical engineering to US and Canadian universities.
I already have a 850 words-statement of purpose.I need somebody to refine it, paraphrase some of the A.I. text. Then, provide similarity free report for this work.

-Key words (5-10 key words)
-Experimental (2-3 pages)
Materials
Methods
-Future work (half-page)
Literature review (2-4 pages)
Mainly journal papers, books, book chapters and conferences
All about material used in water/oil separation