Best practices in treating liquefied petroleum gas are defined
Advantages of removing H2S before the LPG unit and energy optimization of the LPG splitter
This article presents the basic engineering design of a liquefied petroleum gas (LPG) recovery unit at the Khuzestan oil refinery, Iran. This refinery, like other oil refineries, consists of one LPG recovery unit. The feed to the LPG recovery unit comes from three different sources. The first feed is from a catalytic cracking reforming (CCR) unit that is completely sweet with no H2S content. The second feed is from a hydrocracking unit that is sour and has H2S content. The third feed comes from a stabilizer in the crude distillation unit (CDU) which is also sour and has H2S and mercaptan contents.
To continue reading please, log in to hydrocarbonprocessing.com.
Subscribe now for premium access and unlimited access to the site, including archived articles and the process handbooks. Start a free trial to gain access to articles from the current issue of Hydrocarbon Processing.
Already have an account?
Subscribe today and gain unlimited and immediate access to the site. Plus, you'll receive the next 12 issues of the magazine in your choice of print or digital format. Start your subscription today.
Start a free trial and gain immediate access to the current issue of the magazine plus additional, select content.
30 Day Trial