Latest Downloads
-
Crane Fluid Flow Examples in MS ExcelArt Montemayor - Jan 31 2012 08:22 PM
-
Surface Tension of Pure Liquidsankur2061 - Jan 24 2012 02:43 PM
-
Filament Yarn Quench Air Systemankur2061 - Jan 18 2012 05:03 PM
-
Gravity Tank Drainage Calculator for Uniform Cross Sectionsstudent88 - Dec 19 2011 03:16 PM
-
Gravity Tank Drainage Calculator for Hemispherical Cross Sectionsstudent88 - Dec 19 2011 03:14 PM
-
Gravity Tank Drainage Calculator for Cylindrical Cross Sectionsstudent88 - Dec 19 2011 03:13 PM
-
Drainage Between Two Reservoirsstudent88 - Dec 19 2011 03:11 PM
-
Cooling Tower Water Loss CalculatorDB Shah - Dec 19 2011 02:24 PM
-
Equivalent Length Calculations for Pipes and Valvesankur2061 - Nov 17 2011 09:00 AM
-
Slurry Pump Calculation 1.1mramono - Nov 10 2011 05:10 PM
Popular Store Titles
Tank Jacket Calculator
Specification Sheet Collection
PIPESIZE
Relief Valve Sizing
Rupture Disc Sizing
Recent Status Updates
-
Chris HaslegoNew blog entry - Revisiting the Reputation System - http://www.cheresources.com/invision/blog/1/entry-205-revisiting-the-reputation-system/
-
Govind Manglanihey anyone knows how energy is conserved in a petroleum refinery ...i need a overveiw of enery conservation method in major units.Like fcc,reformin,ADU,VDU etc..
Chemical and Process Engineering Resources
Latest Blog Entries
Energy Conservation in Distillation
Dec 13 2010 02:33 PM | Chris HaslegoShare this topic:
The preferred method of separation in the chemical industry, distillation, is a very energy intensive process. Fine tuning your distillation columns (and in some cases, making major changes) can save your company thousands of dollars a year or more. Consider the following distillation column shown in Figure 1 and detailed in Table 1:
| Figure 1: Distillation Column |
We'll examine this column and with some help from the Tower Pricing and Sizing Add-In, we'll see how small changes can save you money in energy costs.
Check the Product Purity
Rating: Little to no investment
Many companies tend to excessively purify products and sometimes with good reason. However, purifying to 98% when 95% is acceptable is just not necessary. In this case, the reflux rate should be decreased in small increments until the desired purity is obtained. In our example, the current reboiler duty will require $68,000 in low pressure steam per year. However, if the purity is decreased and the duty in the reboiler decreases by 5% (down to 2545 MJ/h), the cost of steam decreases to $64,500.
Summary: Excess purification was causing increased spending in the amount of $3,500 per year in the reboiler alone.
Seasonal Operating Pressure Adjustment
Rating: Little or no investment
For plants that are in locations that experience winter climates, the operating pressure can be reduced according to a decrease in cooling water temperatures. Although lowering the pressure in our column would actually be an expense since it's under vacuum, this would not always be the case. The lower pressure will facilitate separation thus lowering energy consumption.
Summary: Take advantage of lower temperatures outside.
Summary: One example of heat integration yields an annual savings of $5,300 per year. A good economic analysis of this option will tell you if it's right for your situation.
Feed Temperature (C) | 90.0 |
| Feed Pressure (kPa) | 19.0 |
| Top Pressure (kPa) | 6.5 |
| Bottom Pressure (kPa) | 15.8 |
| Reflux Ratio | 12.2 |
| Rmin | 1.18 |
| Feed Stage | 9 |
| Number of Actual Trays | 31 |
| Tray Efficiency | 78% |
| Diameter (m) | 1.2 |
| Length (m) | 22 |
| Flooding | 53% |
| Condenser Heat Duty (MJ/h) | -2726 |
| Reboiler Heat Duty (MJ/h) | 2679 |
| Acrylic Acid Purity | 99.9% |


FB



