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How to determine the amount of stripping steam required in a vacuum distillation unit?

2010-05-27View Original

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The main purpose of stripping is to raise the flash point, initial boiling point, and 10% cut point of the side-product. However, too much stripping steam increases the gas-phase load and energy consumption, while too little leads to substandard products. How should this amount be determined?
Reply #22010-05-27
The side stream typically accounts for 3–4% of the mass of the material being stripped, while at the bottom of the tower it is 1–2%. In actual production, adjustments are made based on the product’s boiling range, in conjunction with other methods, allowing for flexible application.
Reply #32010-05-27
Make adjustments based on the product’s flash point, and then observe the changes in the top pressure; if there are significant changes, it indicates that the gas lift volume is too high
Reply #42010-05-27
The amount of stripping steam required is related to the content of light fractions that need to be distilled off. In China, a typical amount of stripping steam used is 2% to 4% of the weight of the oil being stripped. The stripping steam employed in refineries is superheated steam with a pressure of 0.3 to 0.4 MPa and a temperature of 400 to 450°C.
Reply #52010-05-27
The amount of stripping steam is also related to the distillation temperature of diesel; it mainly affects the 10% point temperature. The amount of stripping steam cannot be used to adjust the 10% temperature of diesel, as that would result in high energy consumption. Stripping steam is used to adjust the flash point of diesel, while the 10% temperature is adjusted using the distillation temperature.
Reply #62010-05-27
Using Aspen or ProII to conduct sensitivity analysis, the resulting curves can shed some light on certain issues, hehe!
Reply #72010-06-08
Our hydrocracking unit uses medium-pressure steam at 3.5 MPa and 410 degrees for stripping!
Reply #82010-06-08
The side stream typically accounts for 3–4% of the mass of the material being stripped, while at the bottom of the tower it is 1–3%.
Reply #92010-06-08
Reply to 1# jmg801117: The choice is simple. First, ensure the quality of the product; determine how much stripping is necessary to achieve a satisfactory flash point. Stripping is used to raise the product’s flash point, and once the flash point meets the requirements, the amount of stripping needed remains stable – any excess would result in inefficiency in terms of energy use. The theoretical data is for reference only; the actual amount used should be determined based on ensuring product quality.

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