US2017253807A1PendingUtilityA1

Recycle of process condensate impurities in tigas

Assignee: HALDOR TOPSØES ASPriority: Nov 17, 2014Filed: Nov 17, 2015Published: Sep 7, 2017
Est. expiryNov 17, 2034(~8.3 yrs left)· nominal 20-yr term from priority
C10L 1/06C10L 2270/023C10G 2400/02C10G 3/49C10G 2300/202C10G 2300/4081C10L 2290/10Y02P30/20C10G 2/32C10L 2200/0423C10G 3/42C10G 2/30
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Claims

Abstract

The present application relates to a plant and a hydrocarbon production process comprising the steps of (i) in a conversion step converting at least a feed stream thereby obtaining a conversion effluent stream comprising water, hydrocarbons such as raw gasoline, unreacted and/or partially reacted feed and/or inerts, (ii) In a separator separating the conversion effluent stream into at least a raw gasoline stream, a recycle stream and a process condensate stream comprising water and oxygenates, (iii) mixing the feed stream and the recycle stream upstream the conversion step, and (iv) adding at least part of the process condensate stream to the feed stream and/or the recycle stream and/or the mixed feed-recycle stream from step (iii).

Claims

exact text as granted — not AI-modified
1 . A hydrocarbon production process comprising the steps of
 (i) in a conversion step converting at least a feed stream thereby obtaining a conversion effluent stream comprising water, hydrocarbons such as raw gasoline, unreacted and/or partially reacted feed and/or inerts,   (ii) in a separator separating the conversion effluent stream into at least a raw gasoline stream, a recycle stream and a process condensate stream comprising water and oxygenates,   (iii) mixing the feed stream and the recycle stream upstream the conversion step, and   (iv) adding at least part of the process condensate stream to the feed stream and/or the recycle stream and/or the mixed feed-recycle stream from step (iii).   
     
     
         2 . A hydrocarbon production process according to  claim 1  wherein the oxygenates are separated from the process condensate and added to the feed stream and/or the recycle stream and/or the mixed feed-recycle stream as a recovered oxygenate stream. 
     
     
         3 . A hydrocarbon production process according to  claim 1 , wherein the produced hydrocarbons comprise a mixture of hydrocarbons in the C2-C13 range, preferably comprising C5+. 
     
     
         4 . A hydrocarbon production process according to  claim 1 , wherein the feed comprises methanol, raw methanol, other alcohols, ketones, aldehydes, ethers and/or H 2 /CO mixtures. 
     
     
         5 . A hydrocarbon production process according to  claim 1 , wherein the mixing of at least part of the process condensate comprising oxygenates into the feed stream, recycle stream and/or mixed feed-recycle stream is carried out by quenching the at least part of the process condensate into the feed stream and/or the recycle stream and/or the mixed feed-recycle stream by a spray nozzle. 
     
     
         6 . A hydrocarbon production process according to  claim 1 , wherein the process condensate is added to a stream upstream a heat exchanger. 
     
     
         7 . A plant comprising a converter, means for feeding a feed stream to the converter, a separator, means for returning at least part of a recycle stream from the separator to the converter, and means for mixing at least part of a process condensate from the separator into the means for feeding the feed stream and/or into the means for returning at least part of the recycle stream upstream the converter. 
     
     
         8 . A plant according to  claim 7 , comprising further means for separating oxygenates from the process condensate. 
     
     
         9 . A plant according to  claim 8  wherein the means for separating oxygenates from the process condensate comprises a distillation unit and/or a stripper unit. 
     
     
         10 . Raw gasoline produced by the process according to  claim 1 . 
     
     
         11 . Raw gasoline produced by the plant according to  claim 7 .

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