Systems and processes for upgrading natural gas liquids from shale gas
US-2021116172-A1 · Apr 22, 2021 · US
US9328292B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9328292-B2 |
| Application number | US-201313974365-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 23, 2013 |
| Priority date | Aug 23, 2013 |
| Publication date | May 3, 2016 |
| Grant date | May 3, 2016 |
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A method for improving efficiency of sponge absorption includes providing cold flash drum liquid to an inlet of a cold stripper to produce a cold stripper net overhead vapor stream rich in liquid petroleum gas, and separately providing hot flash drum liquid to an inlet of a hot stripper to produce a hot stripper net overhead vapor stream rich in hydrogen. The cold stripper net overhead vapor stream and the hot stripper net overhead vapor stream are separately routed to a sponge absorber to recover a liquid petroleum gas output stream using sponge oil. In particular, the cold stripper net overhead vapor stream and the hot stripper net overhead vapor stream are separately routed to the sponge absorber at different tray locations.
Opening claim text (preview).
What is claimed is: 1. A sponge oil absorbing device comprising: a cold stripper receiving a feed of cold flash drum liquid from a cold flash drum and providing, as an output, cold stripper net overhead vapor; a hot stripper receiving a feed of hot flash drum liquid from a hot flash drum and providing, as an output, hot stripper net overhead vapor; a sponge absorber including a first inlet and a second inlet, wherein said first inlet receives the cold stripper net overhead vapor output from said cold stripper and said second inlet receives the hot stripper net overhead vapor output from said hot stripper, and wherein the cold stripper overhead vapor and the hot stripper overhead vapor are separately routed to said sponge absorber. 2. The sponge oil absorbing device of claim 1 , wherein said first inlet is positioned at a first feed tray on said sponge absorber and said second inlet is positioned at a second feed tray above said first inlet. 3. The sponge oil absorbing device of claim 2 further comprising an amine scrubber interposed between said cold stripper and said first inlet for removing one or more impurities from the cold stripper net overhead vapor. 4. The sponge oil absorbing device of claim 2 further comprising an amine scrubber interposed between said hot stripper and said second inlet for removing one or more impurities from the hot stripper net overhead vapor. 5. The sponge oil absorbing device of claim 1 , further comprising: a condenser receiving, as an input, the hot stripper net overhead vapor, said condenser cooling and at least partially condensing the hot stripper net overhead vapor to separate a hot stripper net overhead liquid from the hot stripper net overhead vapor, wherein the hot stripper net overhead liquid is recycled by mixing the hot stripper net overhead liquid with the cold flash drum liquid and providing to said cold stripper as an input. 6. The sponge oil absorbing device of claim 1 , further comprising: a deethanizer receiving, as an input feed, sponge absorber bottoms and producing as output a deethanized liquid petroleum gas hydrocarbon stream and an net overhead vapor stream, wherein the deethanizer net overhead vapor stream combines with one or more of the cold stripper net overhead vapor stream and the hot stripper net overhead vapor stream to form a combined net overhead vapor; an amine scrubber receiving, as input, the combined net overhead stream; and a de-butaniser receiving the deethanized liquid petroleum gas hydrocarbon stream and producing a liquid petroleum gas stream and a light naphtha stream.
by contacting with liquids; Regeneration of used liquids · CPC title
Purification by absorption in liquids · CPC title
Fuel gas · CPC title
with liquid absorbents · CPC title
by gas-liquid contact · CPC title
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