US2011232327A1PendingUtilityA1

Method for Processing Off Gas

Assignee: NANDA RAJEEVPriority: Mar 24, 2010Filed: Mar 24, 2010Published: Sep 29, 2011
Est. expiryMar 24, 2030(~3.7 yrs left)· nominal 20-yr term from priority
F25J 3/0219F25J 3/0233F25J 3/0238F25J 3/0242F25J 2200/02F25J 2200/40F25J 2200/74F25J 2205/04F25J 2210/12F25J 2230/08F25J 2230/30F25J 2235/02F25J 2245/02F25J 2270/14F25J 2270/18F25J 2270/66F25J 2270/902
41
PatentIndex Score
0
Cited by
0
References
0
Claims

Abstract

A method for recovering C 2 and higher weight hydrocarbons, or alternatively C 3 and higher weight hydrocarbons, from off gas, such as refinery off gas, wherein the method avoids the need to significantly compress contaminated off gas in most cases, and is robust in response to pressure and temperature variations in the off gas feed.

Claims

exact text as granted — not AI-modified
1 . A method for processing an off gas inlet stream to recover C 2  and higher weight hydrocarbons, comprising the steps of
 cooling said off gas inlet stream to form a partially condensed hydrocarbon feed,   separating a condensed portion from said partially condensed hydrocarbon feed, and   distilling said condensed portion to recover C 2  and higher weight hydrocarbons as product.   
     
     
         2 . The method of  claim 1 , wherein the step of cooling said off gas inlet stream to form a partially condensed hydrocarbon feed additionally comprises the step of using a portion of said product as part or all of a refrigerant used to provide said cooling. 
     
     
         3 . The method of  claim 1 , wherein the step of cooling said off gas inlet stream to form a partially condensed hydrocarbon feed additionally comprises the step of using a portion of said off gas inlet stream as part or all of a refrigerant used to provide said cooling. 
     
     
         4 . The method of  claim 1 , wherein the step of cooling said off gas inlet stream to form a partially condensed hydrocarbon feed additionally comprises the step of using a closed loop refrigeration system to provide said cooling. 
     
     
         5 . The method of  claim 1 , additionally comprising the steps of
 recovering vapor from said step of distilling said condensed portion of said partially condensed hydrocarbon feed to recover C 2  and higher weight hydrocarbons as product,   cooling said vapor to form reflux,   separating a vapor portion from said reflux, and   using part of said vapor portion of said reflux as part or all of a refrigerant used to provide said cooling.   
     
     
         6 . The method of  claim 5 , additionally comprising the step of
 distilling a liquid portion of said reflux to recover C 2  and higher weight hydrocarbons as product.   
     
     
         7 . The method of  claim 1 , additionally comprising the steps of
 separating a vapor portion from said partially condensed hydrocarbon feed,   compressing said vapor portion, and   distilling said compressed vapor portion to recover C 2  and higher weight hydrocarbons as product.   
     
     
         8 . The method of  claim 1 , additionally comprising the steps of
 separating a vapor portion from said partially condensed hydrocarbon feed,   compressing said vapor portion,   cooling said compressed vapor portion to partially condense said compressed vapor portion,   separating a liquid portion from said partially condensed vapor portion, and   distilling said separated liquid portion to recover C 2  and higher weight hydrocarbons as product.   
     
     
         9 . A method for processing an off gas inlet stream to recover C 3  and higher weight hydrocarbons, comprising the steps of
 cooling said off gas inlet stream to form a partially condensed hydrocarbon feed,   separating a condensed portion from said partially condensed hydrocarbon feed, and   distilling said condensed portion to recover C 3  and higher weight hydrocarbons as product.   
     
     
         10 . The method of  claim 9 , wherein the step of cooling said off gas inlet stream to form a partially condensed hydrocarbon feed additionally comprises the step of using a portion of said product as part or all of a refrigerant used to provide said cooling. 
     
     
         11 . The method of  claim 9 , wherein the step of cooling said off gas inlet stream to form a partially condensed hydrocarbon feed additionally comprises the step of using a portion of said off gas inlet stream as part or all of a refrigerant used to provide said cooling. 
     
     
         12 . The method of  claim 9 , wherein the step of cooling said off gas inlet stream to form a partially condensed hydrocarbon feed additionally comprises the step of using a closed loop refrigeration system to provide said cooling. 
     
     
         13 . The method of  claim 9 , additionally comprising the steps of
 recovering vapor from said step of distilling said condensed portion of said partially condensed hydrocarbon feed to recover C 3  and higher weight hydrocarbons as product,   cooling said vapor to form reflux,   separating a vapor portion from said reflux, and   using part of said vapor portion of said reflux as part or all of a refrigerant used to provide said cooling.   
     
     
         14 . The method of  claim 13 , additionally comprising the step of
 distilling a liquid portion of said reflux to recover C 3  and higher weight hydrocarbons as product.   
     
     
         15 . The method of  claim 9 , additionally comprising the steps of
 separating a vapor portion from said partially condensed hydrocarbon feed,   compressing said vapor portion, and   distilling said compressed vapor portion to recover C 3  and higher weight hydrocarbons as product.   
     
     
         16 . The method of  claim 9 , additionally comprising the steps of
 separating a vapor portion from said partially condensed hydrocarbon feed,   compressing said vapor portion,   cooling said compressed vapor portion to partially condense said compressed vapor portion,   separating a liquid portion from said partially condensed vapor portion, and   distilling said separated liquid portion to recover C 3  and higher weight hydrocarbons as product.

Join the waitlist — get patent alerts

Track US2011232327A1 — get alerts on status changes and closely related new filings.

We store only your email — no account needed. See our privacy policy.