Pipeline arrangement for utilizing a gas comprising biomethane
US-9222048-B1 · Dec 29, 2015 · US
US9687808B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9687808-B2 |
| Application number | US-201414339739-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 24, 2014 |
| Priority date | Jul 26, 2013 |
| Publication date | Jun 27, 2017 |
| Grant date | Jun 27, 2017 |
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A method and system for controlling a hydrocracker and fractionator reaction loop is disclosed. The method and system utilizes a sidedraw tray within the fractionator distillation zone upon which liquid is collected. This liquid is withdrawn as a sidedraw stream. The withdrawal of the liquid from the sidedraw tray is controlled based on the level of liquid on the sidedraw tray rather than at a set or determined flow rate. The sidedraw stream is separated into a first stream and a product stream. Unlike other processes where the flow rate of the product stream is set and the internal reflux flow rate varies, the method involves fixing the flow rate of the first stream that is returned to the distillation zone of the fractionators with the flow rate of the product stream being set so as to control the liquid level on the sidedraw tray.
Opening claim text (preview).
That which is claimed is: 1. A method of controlling the operation of a fractionator and hydrocracker reaction loop, wherein said method comprises: providing a fractionator for receiving a hydrocracker effluent yielded from a hydrocracker reactor as a fractionator feed, wherein said fractionator defines a distillation zone that includes a bottom zone, an upper zone, and an intermediate zone between said bottom zone and said upper zone, wherein said intermediate zone has a sidedraw tray; introducing said fractionator feed into said bottom zone of said fractionator; collecting on said sidedraw tray a liquid level of hydrocarbons having a desired boiling range; withdrawing a sidedraw stream of said hydrocarbon from said sidedraw tray; separating said sidedraw stream into a first stream and a product stream; introducing said first stream to said distillation zone; responsive to a difference between a measured flow of said first stream and a desired flow of said first stream, controlling the flow of said first stream; responsive to a difference between a measured liquid level on said sidedraw tray and a desired liquid level on said sidedraw tray, controlling the flow of said product stream; and passing said product stream downstream of said fractionator. 2. A method according to claim 1 , wherein the step of separating said sidedraw stream further comprises: separating said sidestraw stream into a second stream; and controlling the flow of said second stream responsive to a difference between a measured flow of said second stream and a desired flow of said second stream. 3. A method according to claim 2 , further comprising: introducing said first stream into said bottom zone; and introducing said second stream into said upper zone. 4. A method according to claim 1 , further comprising: monitoring a bottoms yield of said fractionator; and adjusting in response to changes in said bottoms yield said hydrocracker reactor conditions. 5. A method according to claim 1 , wherein said sidedraw tray is sealed and does not permit the overflow of liquid.
Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions (C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06) · CPC title
Controlling or regulating · CPC title
Controlling or regulating · CPC title
Recycling aspects · CPC title
controlling the flow · CPC title
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