US2012000244A1PendingUtilityA1
Heat pump distillation for <50% light component in feed
Est. expiryJun 30, 2030(~4 yrs left)· nominal 20-yr term from priority
Y02B30/52Y02P20/10C07C 7/04B01D 3/007B01D 1/28
37
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Claims
Abstract
A process is presented for the separation of a hydrocarbon mixture having less than 50% of the light component in the feedstream. The process provides an energy efficiency through drawing off a vapor stream from the rectifying section of a distillation column, and using recompression of the vapor to provide a portion of the heat for reboiling a portion of the bottoms stream exiting the stripping section of the distillation column.
Claims
exact text as granted — not AI-modified1 . A process for the separation of a light component from a mixture of hydrocarbons, comprising:
passing a feedstream to a distillation column at a position between the rectifying section and the stripping section, wherein the feed comprises less than 50% light components, and wherein the distillation column has an overhead vapor stream and a bottoms liquid stream; passing the overhead vapor stream to a first heat pump compressor, thereby creating a compressed overhead vapor stream; passing the compressed overhead vapor stream to the vapor side of a first reboiler heat exchanger, thereby creating a partially condensed overhead stream; drawing off a side vapor stream from the rectifying section at a draw off port, thereby creating a side draw stream; passing the side draw stream to a second heat pump compressor, thereby creating a compressed side draw stream; passing the compressed side draw stream to the vapor side of a second reboiler heat exchanger, thereby creating a cooled compressed side draw stream; passing a first portion of the bottoms liquid stream to the liquid side of the first reboiler heat exchanger, thereby creating a first vapor bottoms stream; and passing a second portion of the bottoms liquid stream to the liquid side of the second reboiler heat exchanger.
2 . The process of claim 1 wherein the compressed overhead stream is totally condensed.
3 . The process of claim 1 further comprising passing a portion of the condensed overhead stream to the top of the rectifying section.
4 . The process of claim 1 further comprising partially condensing the compressed side draw stream, thereby creating a partially condensed compressed side draw stream.
5 . The process of claim 4 further comprising passing the partially condensed compressed side draw stream back to the rectifying section.
6 . The process of claim 1 further comprising passing the cooled compressed side draw stream back to the rectifying section.
7 . The process of claim 6 wherein the cooled compressed side draw stream is passed to below the draw off port.
8 . The process of claim 1 wherein the side draw stream is drawn from a tray positioned within 10 trays to the tray having the greatest temperature gradient per tray in the rectifying section.
9 . The process of claim 8 wherein the side draw stream is drawn from a tray proximate to the tray having the greatest temperature gradient per tray in the rectifying section.
10 . The process of claim 1 wherein the side draw stream is drawn from the lower half of the rectifying section.
11 . A process for the separation of a light component from a mixture of hydrocarbons, comprising:
passing a feedstream to a distillation column at a position between the rectifying section and the stripping section, wherein the feed comprises less than 50% light components, and wherein the distillation column has a overhead vapor stream and a bottoms liquid stream; passing the overhead vapor stream to a first heat pump compressor, thereby creating a compressed overhead vapor stream; passing the compressed overhead vapor stream to the vapor side of a first reboiler heat exchanger, thereby creating a condensed overhead stream; drawing off a side vapor stream from the rectifying section at a draw off port, thereby creating a side draw stream, wherein the draw off port is at a tray position that is within 10 trays of the tray having the greatest temperature gradient; passing the side draw stream to a second heat pump compressor, thereby creating a compressed side draw stream; passing the compressed side draw stream to the vapor side of a second reboiler heat exchanger, thereby creating a cooled compressed side draw stream, wherein the cooled compressed side draw stream is partially condensed; passing a first portion of the bottoms liquid stream to the liquid side of the first reboiler heat exchanger, thereby creating a first vapor bottoms stream; and passing a second portion of the bottoms liquid stream to the liquid side of the second reboiler heat exchanger.
12 . The process of claim 11 further comprising passing a portion of the condensed overhead stream to the top of the rectifying section.
13 . The process of claim 11 further comprising passing the partially condensed compressed side draw stream back to the rectifying section.
14 . The process of claim 13 wherein the cooled compressed side draw stream is passed to below the draw off port.
15 . The process of claim 11 further comprising totally condensing the compressed side draw stream.
16 . The process of claim 15 further comprising passing the totally condensed compressed side draw stream back to the rectifying section.
17 . The process of claim 16 wherein the cooled compressed side draw stream is passed to below the draw off port.
18 . The process of claim 11 wherein the side draw stream is drawn from the lower half of the rectifying section.
19 . The process of claim 11 wherein the side draw stream is drawn from a tray proximate to the tray having the greatest temperature gradient per tray in the rectifying section.
20 . The process of claim 11 wherein the side draw stream is drawn from the lower half of the rectifying section.Join the waitlist — get patent alerts
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