Voc refining apparatus
US-2018345214-A1 · Dec 6, 2018 · US
US9869511B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9869511-B2 |
| Application number | US-201414516683-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 17, 2014 |
| Priority date | Dec 6, 2013 |
| Publication date | Jan 16, 2018 |
| Grant date | Jan 16, 2018 |
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A method for separating a feed stream in a distillation tower comprising maintaining a controlled freeze zone (CFZ) section in the distillation tower, receiving a freezing zone liquid stream in a spray nozzle assembly in the CFZ section, wherein the spray nozzle assembly comprises a plurality of outer spray nozzles on an outer periphery of the spray nozzle assembly and at least one inner spray nozzle interior to the outer spray nozzles, wherein each outer spray nozzle is configured to spray the freezing zone liquid stream along a central spray axis, and wherein the central spray axis of at least one of the outer spray nozzles is not parallel to a CFZ wall, and spraying the freezing zone liquid stream through the spray nozzle assembly into the CFZ section to keep a temperature and pressure at which the solid and the hydrocarbon-enriched vapor stream form.
Opening claim text (preview).
What is claimed is: 1. A method for producing hydrocarbons comprising: maintaining a controlled freeze zone section in a distillation tower that receives a freezing zone liquid stream to form a solid and a hydrocarbon-enriched vapor stream in the controlled freeze zone section; maintaining a spray assembly in the controlled freeze zone section, wherein the spray assembly comprises a first type of spray nozzle on an outer periphery of the spray nozzle assembly and a second type of spray nozzle interior to the first type of spray nozzle in the spray assembly, wherein the first type of spray nozzle orients spray at a first angle with respect to a controlled freeze zone wall and the second type of spray nozzle orients spray at a second angle with respect to the controlled freeze zone wall, wherein the first angle and the second angle are different, and wherein the first angle is configured such that the spray liquid does not impinge on the controlled freeze zone wall; injecting the freezing zone liquid stream into the controlled freeze zone section through the spray assembly at a temperature and pressure at which the solid and the hydrocarbon-enriched vapor stream form; and extracting the hydrocarbon-enriched vapor stream from the distillation tower. 2. The method of claim 1 , wherein injecting the freezing zone liquid stream into the controlled freeze zone section through the spray assembly comprises flowing the freezing zone liquid stream through a side of the controlled freeze zone section. 3. The method of claim 1 , wherein injecting the freezing zone liquid stream into the controlled freeze zone section through the spray assembly comprises flowing the freezing zone liquid stream through a top of the controlled freeze zone section. 4. The method of claim 1 , wherein the first angle is configured by angling at least one of the first type of spray nozzles towards the interior of the tower and varying the distribution of the spray liquid coming out of at least one of the first type of spray nozzles in a pattern to keep the sprayed freezing zone liquid stream away from the controlled freeze zone wall. 5. The method of claim 1 , wherein the first angle may be defined by a longitudinal spray nozzle axis and a longitudinal controlled freeze zone wall axis and wherein the first angle is from 0 to 60 degrees. 6. The method of claim 1 , wherein the first angle creates an elongated ellipsoid spray projection. 7. The method of claim 1 , wherein the second angle may be defined by a longitudinal spray nozzle axis and a longitudinal controlled freeze zone wall axis and wherein the second angle is from 0 to 60 degrees.
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