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	<id>https://design.cbe.cornell.edu/api.php?action=feedcontributions&amp;feedformat=atom&amp;user=165.124.128.106</id>
	<title>processdesign - User contributions [en]</title>
	<link rel="self" type="application/atom+xml" href="https://design.cbe.cornell.edu/api.php?action=feedcontributions&amp;feedformat=atom&amp;user=165.124.128.106"/>
	<link rel="alternate" type="text/html" href="https://design.cbe.cornell.edu/index.php?title=Special:Contributions/165.124.128.106"/>
	<updated>2026-05-02T06:24:05Z</updated>
	<subtitle>User contributions</subtitle>
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	<entry>
		<id>https://design.cbe.cornell.edu/index.php?title=Define_product_and_feed&amp;diff=327</id>
		<title>Define product and feed</title>
		<link rel="alternate" type="text/html" href="https://design.cbe.cornell.edu/index.php?title=Define_product_and_feed&amp;diff=327"/>
		<updated>2014-01-17T20:17:58Z</updated>

		<summary type="html">&lt;p&gt;165.124.128.106: Created page with &amp;quot;Authors: Michael Gleeson, Sean Kelton, Thomas Considine  ==Introduction==  ==Primary Products==  ==Primary Raw Materials==&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;Authors: Michael Gleeson, Sean Kelton, Thomas Considine&lt;br /&gt;
&lt;br /&gt;
==Introduction==&lt;br /&gt;
&lt;br /&gt;
==Primary Products==&lt;br /&gt;
&lt;br /&gt;
==Primary Raw Materials==&lt;/div&gt;</summary>
		<author><name>165.124.128.106</name></author>
	</entry>
	<entry>
		<id>https://design.cbe.cornell.edu/index.php?title=Main_Page&amp;diff=326</id>
		<title>Main Page</title>
		<link rel="alternate" type="text/html" href="https://design.cbe.cornell.edu/index.php?title=Main_Page&amp;diff=326"/>
		<updated>2014-01-17T20:12:09Z</updated>

		<summary type="html">&lt;p&gt;165.124.128.106: /* Design Basis */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;&amp;lt;!-- Header table. Introduction. --&amp;gt;&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot; style=&amp;quot;padding:5px&amp;quot; valign=&amp;quot;top&amp;quot; width = &amp;quot;1080&amp;quot;&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&#039;&#039;&#039;Welcome to the Northwestern University Chemical Process Design Open Textbook.&#039;&#039;&#039; &amp;lt;br /&amp;gt;&lt;br /&gt;
This electronic textbook is a student-contributed open-source text covering the materials used in our chemical engineering capstone design courses at Northwestern.&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
If you have any comments or suggestions on this open textbook, please contact [//www.mccormick.northwestern.edu/directory/profiles/Fengqi-You.html  Professor Fengqi You].&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
&amp;lt;br /&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;font size=&amp;quot;5&amp;quot;&amp;gt;Northwestern University Chemical Process Design Open Text Book&amp;lt;/font&amp;gt;&lt;br /&gt;
----&lt;br /&gt;
&lt;br /&gt;
&amp;lt;!-- Table of Contents --&amp;gt;&lt;br /&gt;
__TOC__&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot;&lt;br /&gt;
|- valign=&amp;quot;top&amp;quot; style=&amp;quot;border: 1px solid red; padding:1px&amp;quot;&lt;br /&gt;
| &lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot; style=&amp;quot;border: 1px solid darkgray; padding:5px;&amp;quot; width=&amp;quot;590&amp;quot;&lt;br /&gt;
|- valign=&amp;quot;top&amp;quot;&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
= Chemical Process Design Theory and Method =&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==Design Basis==&lt;br /&gt;
# [[Define product and feed]]&lt;br /&gt;
# Preliminary market analysis and plant capacity&lt;br /&gt;
# [[Site condition and design]]&lt;br /&gt;
# [[Block Flow Diagram| Block flow diagram]]  &lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Process Flow Diagram==&lt;br /&gt;
# Process alternatives and flowsheeting&lt;br /&gt;
# Reactors&lt;br /&gt;
# Separation processes &lt;br /&gt;
# Process hydraulics: Hydraulic systems, pressure drop, valves, pumps, and compressors&lt;br /&gt;
# [[Heat Transfer Equipment| Heat transfer equipment: Heat exchangers, boilers, condensers, heaters and coolers]]&lt;br /&gt;
# Utility systems&lt;br /&gt;
# Pressure vessels&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Process Economics==&lt;br /&gt;
# Estimation of capital&lt;br /&gt;
# Estimation of production cost and revenue&lt;br /&gt;
# Engineering economic analysis&lt;br /&gt;
# Sensitivity analysis and design optimization &lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Other Process Design Considerations==&lt;br /&gt;
# Process safety&lt;br /&gt;
# Process hazards &lt;br /&gt;
# Environmental concerns&lt;br /&gt;
# Controls and P&amp;amp;ID &lt;br /&gt;
|}&lt;br /&gt;
| width=&amp;quot;5&amp;quot; height=&amp;quot;100%&amp;quot; border=&amp;quot;0&amp;quot; |&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot; style=&amp;quot;border: 1px solid darkgray&amp;quot; padding:5px; width=&amp;quot;480&amp;quot;&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
=Chemical Process Design Projects=&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
== Examples ==&lt;br /&gt;
* [[Sugar Cane Ethanol Plant]] (2011)&lt;br /&gt;
* Other examples&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Glycerol to propylene glycol==&lt;br /&gt;
* Design 1 (2014)&lt;br /&gt;
* Design 2 (2014)&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==Succinic acid to 1,4-butanediol==&lt;br /&gt;
* Design 1 (2014)&lt;br /&gt;
* Design 2 (2014)&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==Hydrogen Student Design Contest==&lt;br /&gt;
* Drop-in Hydrogen Fueling (2014)&lt;br /&gt;
|}&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&#039;&#039;&#039;Guide to Use Wiki&#039;&#039;&#039;&lt;br /&gt;
* [[Editing_help| Quick Guide to MediaWiki Editing]]&lt;br /&gt;
* [//meta.wikimedia.org/wiki/Help:Contents MediaWiki User&#039;s Guide]&lt;br /&gt;
* [//www.mediawiki.org/wiki/Manual:FAQ MediaWiki FAQ]&lt;/div&gt;</summary>
		<author><name>165.124.128.106</name></author>
	</entry>
	<entry>
		<id>https://design.cbe.cornell.edu/index.php?title=Site_condition_and_design&amp;diff=285</id>
		<title>Site condition and design</title>
		<link rel="alternate" type="text/html" href="https://design.cbe.cornell.edu/index.php?title=Site_condition_and_design&amp;diff=285"/>
		<updated>2014-01-16T18:39:16Z</updated>

		<summary type="html">&lt;p&gt;165.124.128.106: /* Cost */ some info&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;Title: Site condition and design&lt;br /&gt;
&lt;br /&gt;
Authors: Alex Chandel, etc&lt;br /&gt;
&lt;br /&gt;
Stewards: Alex Chandel, etc&lt;br /&gt;
&lt;br /&gt;
Date Revised: 1/14/2014&lt;br /&gt;
&lt;br /&gt;
== Introduction == &lt;br /&gt;
All chemical processes require land for chemical storage, process equipment, and labor facilities.&lt;br /&gt;
&lt;br /&gt;
== Geographical selection ==&lt;br /&gt;
The location surrounding a chemical plant can substantially influence its construction costs and operating costs, and may affect long-term profitability. Thus it is important to choose an appropriate location for every facility.&lt;br /&gt;
&lt;br /&gt;
=== Factors considered ===&lt;br /&gt;
==== Natural resources ====&lt;br /&gt;
Proximity to continental and underwater oil deposits, natural gas, coal mines, and other resources.&lt;br /&gt;
&lt;br /&gt;
==== Weather ====&lt;br /&gt;
Its influence on ambient temperature and thus on utility cost.{{citation needed}} Also rain and humidity, and the sensitivity of the process to water exposure.&lt;br /&gt;
&lt;br /&gt;
==== Proximity to related chemical operations ====&lt;br /&gt;
Oil rigs are found in the gulf, and oil refineries on its shore. Biofuel production plants are found in the midwest.{{citation needed}}&lt;br /&gt;
&lt;br /&gt;
==== Laws and regulations ====&lt;br /&gt;
Some states are more friendly to chemical engineering operations, or may impose additional regulations. Property costs, property taxes, corporate income taxes, and environmental contamination fines will vary between states.&lt;br /&gt;
&lt;br /&gt;
=== Cost ===&lt;br /&gt;
All of the above criteria ultimately influence the capital and operating costs of a plant, and its expected lifespan.&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;TC = r K + w L&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Local wages, prices of chemical feedstock, shipping costs, and utilities all contribute to total operating costs. &lt;br /&gt;
&lt;br /&gt;
Property prices, rental fees, taxes, and existing company property in the area contribute to recurring investment costs.&lt;br /&gt;
&lt;br /&gt;
=== Common locations ===&lt;br /&gt;
There are many common locations for chemical processes, often specific to one or more industries.&lt;br /&gt;
&lt;br /&gt;
==== The Gulf of Mexico ====&lt;br /&gt;
==== Texas - petrochemical refineries ====&lt;br /&gt;
==== Louisiana ====&lt;br /&gt;
==== Alaska ====&lt;br /&gt;
==== (China) ====&lt;br /&gt;
==== (Arabian peninsula) ====&lt;br /&gt;
==== etc ====&lt;br /&gt;
&lt;br /&gt;
== Site design ==&lt;br /&gt;
Once a region is selected, the building and process equipment themselves must be laid out.&lt;br /&gt;
&lt;br /&gt;
=== Footprint ===&lt;br /&gt;
Areas with greater land costs require vertically oriented equipment.{{citation needed}}&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
* Towler?&lt;br /&gt;
&lt;br /&gt;
== External links==&lt;br /&gt;
* (Relevant wikipedia article)&lt;/div&gt;</summary>
		<author><name>165.124.128.106</name></author>
	</entry>
	<entry>
		<id>https://design.cbe.cornell.edu/index.php?title=Main_Page&amp;diff=112</id>
		<title>Main Page</title>
		<link rel="alternate" type="text/html" href="https://design.cbe.cornell.edu/index.php?title=Main_Page&amp;diff=112"/>
		<updated>2014-01-09T18:28:46Z</updated>

		<summary type="html">&lt;p&gt;165.124.128.106: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;&amp;lt;!-- Header table. Introduction. --&amp;gt;&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot; style=&amp;quot;padding:5px&amp;quot; valign=&amp;quot;top&amp;quot; width = &amp;quot;1080&amp;quot;&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&#039;&#039;&#039;Welcome to the Northwestern University Chemical Process Design Open Textbook.&#039;&#039;&#039; &amp;lt;br /&amp;gt;&lt;br /&gt;
This electronic textbook is a student-contributed open-source text covering the materials used in our chemical engineering capstone design courses at Northwestern.&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
If you have any comments or suggestions on this open textbook, please contact [//www.mccormick.northwestern.edu/directory/profiles/Fengqi-You.html  Professor Fengqi You].&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
&amp;lt;br /&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;font size=&amp;quot;5&amp;quot;&amp;gt;Northwestern University Chemical Process Design Open Text Book&amp;lt;/font&amp;gt;&lt;br /&gt;
----&lt;br /&gt;
&lt;br /&gt;
&amp;lt;!-- Table of Contents --&amp;gt;&lt;br /&gt;
__TOC__&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot;&lt;br /&gt;
|- valign=&amp;quot;top&amp;quot; style=&amp;quot;border: 1px solid red; padding:1px&amp;quot;&lt;br /&gt;
| &lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot; style=&amp;quot;border: 1px solid darkgray; padding:5px;&amp;quot; width=&amp;quot;590&amp;quot;&lt;br /&gt;
|- valign=&amp;quot;top&amp;quot;&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
= Chemical Process Design Theory and Method =&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==Design Basis==&lt;br /&gt;
# Define product and feed&lt;br /&gt;
# Preliminary market analysis and plant capacity&lt;br /&gt;
# Site condition and design&lt;br /&gt;
# [[Block Flow Diagram| Block flow diagram]]  &lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Process Flow Diagram==&lt;br /&gt;
# Process alternatives and flowsheeting&lt;br /&gt;
# Reactors&lt;br /&gt;
# Separation processes &lt;br /&gt;
# Process hydraulics: Hydraulic systems, pressure drop, valves, pumps, and compressors&lt;br /&gt;
# [[Heat transfer equipment|Heat transfer equipment: Heat exchangers, boilers, condensers, heaters and coolers]]&lt;br /&gt;
# Utility systems&lt;br /&gt;
# Pressure vessels&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Process Economics==&lt;br /&gt;
# Estimation of capital&lt;br /&gt;
# Estimation of production cost and revenue&lt;br /&gt;
# Engineering economic analysis&lt;br /&gt;
# Sensitivity analysis and design optimization &lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
==Other Process Design Considerations==&lt;br /&gt;
# Process safety&lt;br /&gt;
# Process hazards &lt;br /&gt;
# Environmental concerns&lt;br /&gt;
# Controls and P&amp;amp;ID &lt;br /&gt;
|}&lt;br /&gt;
| width=&amp;quot;5&amp;quot; height=&amp;quot;100%&amp;quot; border=&amp;quot;0&amp;quot; |&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
{| class=&amp;quot;wikitable&amp;quot; style=&amp;quot;border: 1px solid darkgray&amp;quot; padding:5px; width=&amp;quot;480&amp;quot;&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
&lt;br /&gt;
=Chemical Process Design Projects=&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
== Examples ==&lt;br /&gt;
* Sugar Cane Ethanol Plant (2011)&lt;br /&gt;
* Other examples&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==Glycerol to propylene glycol==&lt;br /&gt;
* Design 1&lt;br /&gt;
* Design 2&lt;br /&gt;
* Design 3&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==3-Hydroxypropionic acid to 1,3-propanediol==&lt;br /&gt;
* Design 1&lt;br /&gt;
* Design 2&lt;br /&gt;
* Design 3&lt;br /&gt;
|-&lt;br /&gt;
|&lt;br /&gt;
==Succinic acid to 1,4-butanediol==&lt;br /&gt;
* Design 1&lt;br /&gt;
* Design 2&lt;br /&gt;
* Design 3&lt;br /&gt;
|}&lt;br /&gt;
|}&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&#039;&#039;&#039;Guide to Use Wiki&#039;&#039;&#039;&lt;br /&gt;
* [[Editing_help| Quick Guide to MediaWiki Editing]]&lt;br /&gt;
* [//meta.wikimedia.org/wiki/Help:Contents MediaWiki User&#039;s Guide]&lt;br /&gt;
* [//www.mediawiki.org/wiki/Manual:FAQ MediaWiki FAQ]&lt;/div&gt;</summary>
		<author><name>165.124.128.106</name></author>
	</entry>
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