i have stream with light oil component
hydrogen, Methane, Ethane, H2S this in gas phase
Propane, Iso-Butane, n-Butane, iso-pentane, n-pentane in liquid phase
what i need from this stream is Propane, Iso-Butane, n-Butane, iso-pentane, n-pentane
my Question
can i use distillation column to separate thim so i get hydrogen, Methane, Ethane, H2S and some of propane
is there any problem by using distillatin column because i get H2s with the feed
i am thinking to treat the H2S after it distill with other gases
persantage of H2s is 0.1%
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Distillation Column
Started by normal2500, Oct 30 2006 09:25 AM
5 replies to this topic
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#1
Posted 30 October 2006 - 09:25 AM
#2
Posted 30 October 2006 - 01:10 PM
normal2500:
It is completely acceptable to do your distillation first and then remove the H2S from the overhead gas product of the distillation.
If you are not interested in retaining propane in the distillation bottoms liquid product, then you are talking about what is commonly known as a depropanizer and you can use an ordinary distillation tower operating at about 10 to 13 atmospheres presure and 310 K temperature (depending on the cooling water supply temperature for the overhead condenser ). The overhead product gas will contain some of your butanes, almost all of your propane and all of your ethane, methane and H2S.
If you are interested in retaining about 70% or more of the propane in the bottoms product, then you will need to operate at about 15 to 20 atmospheres and use what is commonly known as a reboiled de-ethanizer or a reboiled absorber system ... which is a good bit more complex than a simple depropanizer.
It is completely acceptable to do your distillation first and then remove the H2S from the overhead gas product of the distillation.
If you are not interested in retaining propane in the distillation bottoms liquid product, then you are talking about what is commonly known as a depropanizer and you can use an ordinary distillation tower operating at about 10 to 13 atmospheres presure and 310 K temperature (depending on the cooling water supply temperature for the overhead condenser ). The overhead product gas will contain some of your butanes, almost all of your propane and all of your ethane, methane and H2S.
If you are interested in retaining about 70% or more of the propane in the bottoms product, then you will need to operate at about 15 to 20 atmospheres and use what is commonly known as a reboiled de-ethanizer or a reboiled absorber system ... which is a good bit more complex than a simple depropanizer.
#3
Posted 01 November 2006 - 04:05 AM
Thanks for your answer.
can i ask you another question
After i spreat the gases what is the beat and industrial way to separate the H2S from the other Gases.
can i ask you another question
After i spreat the gases what is the beat and industrial way to separate the H2S from the other Gases.
#4
Posted 01 November 2006 - 02:24 PM
normal2500:
Most large oil refineries use aqueous solutions of either diethanolamine (DEA) or monoethanol amine (MEA) to remove the H2S and recover it as a concentrated stream of H2S gas. Those processes are called "amine sweetening". The concentrated H2S is then fed to a Claus process which converts the H2S to elemental sulfur.
Visit http://www.bre.com/p...esweetening.asp for a process description and for a flow sheet of the amine process.
Most large oil refineries use aqueous solutions of either diethanolamine (DEA) or monoethanol amine (MEA) to remove the H2S and recover it as a concentrated stream of H2S gas. Those processes are called "amine sweetening". The concentrated H2S is then fed to a Claus process which converts the H2S to elemental sulfur.
Visit http://www.bre.com/p...esweetening.asp for a process description and for a flow sheet of the amine process.
#5
Posted 03 November 2006 - 11:28 PM
First use a water scrubber to separate hydrogen sulphide gas then go for membrane separation.
#6
Posted 12 November 2006 - 05:57 AM
another Q and sorry
whan i use Zinc Oxide to remove H2S, can i use Hysys
or i do hand calculation
whan i use Zinc Oxide to remove H2S, can i use Hysys
or i do hand calculation
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