Method of removing co2 from a contaminated hydrocarbon stream
US-2018259251-A1 · Sep 13, 2018 · US
US10329182B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10329182-B2 |
| Application number | US-201615385056-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 20, 2016 |
| Priority date | Dec 20, 2016 |
| Publication date | Jun 25, 2019 |
| Grant date | Jun 25, 2019 |
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A method of separating solids from a slurry or suspension is disclosed. The method includes: providing a slurry or suspension containing solids and liquid to an input port of a first side of a filter, the filter providing a filtering size between 2 microns and 70 microns; providing a liquid discharge port on a second side of the filter which receives the liquid that passes through the filter; and separating the solids from the liquid by pressing the solids into a pressure regulating solids discharge port on the first side of the filter, thereby compacting solids on the first side of the filter, forcing at least some of the liquid of the slurry or suspension through the first side of the filter to the second side of the filter causing pressure regulated solids to be discharged through a pressure regulating solids discharge port into a pressurized chamber.
Opening claim text (preview).
The invention claimed is: 1. A method for separating solids and liquids comprising: providing a first vessel comprising a solids compactor, a slurry inlet, a filter medium, a fluid outlet, and a solids outlet, wherein the filter medium is outside the solids compactor, the slurry inlet is located towards a first end of the first vessel, and the solids outlet is located towards a second end of the first vessel; providing a second vessel in communication with the first vessel through the solids outlet; passing a slurry stream, comprising a feed solid and a feed liquid, through the slurry inlet into the first vessel; compacting the slurry stream with the solids compactor towards the second end of the first vessel, wherein compacting the slurry stream drives a portion of the feed liquid out of the slurry through the filter medium and out the fluid outlet as a liquid product stream, leaving a solids product stream in the first vessel; passing the solids product stream out of the first vessel through the solids outlet into the second vessel; and melting the solids product stream in the second vessel; wherein, as the solids outlet restricts flow of the solids product stream sufficient for a backpressure to be built towards the second end of the first vessel, the solids compactor is enabled to compact the solids without the slurry stream passing through the solids outlet. 2. The invention of claim 1 , wherein the feed solid comprises carbon dioxide. 3. The invention of claim 2 , wherein the slurry is below a temperature of −56.6° C. 4. The invention of claim 1 , wherein the filter medium is constructed at least partially from materials selected from the group consisting of mesh, stainless steel, metal, ceramic, carbon, fibrous materials, plastic, diamond, an interstitially formed material, and combinations thereof. 5. The invention of claim 1 , wherein the filter medium is a sintered mesh filter with two or more mesh screens sintered together, each mesh screen having a filtering size between 2 microns and 70 microns. 6. The invention of claim 1 , wherein the solids compactor is selected from the group consisting of screws, augers, pistons, tapered wedges, or combinations thereof. 7. The invention of claim 1 , wherein the vessel further comprises a temperature sensor or a pressure sensor inserted into the slurry inlet. 8. The invention of claim 1 , wherein the solids outlet comprises a tapered channel, an orifice, or a spring-loaded valve. 9. The invention of claim 1 , further comprising adjusting an opening of the solids outlet to adjust the backpressure. 10. The invention of claim 9 , wherein adjusting the opening of the solids outlet comprises movement of an actuator. 11. The invention of claim 1 , wherein the second vessel comprises a gas outlet and the second vessel is maintained at a pressure by regulating discharge of gases through the gas outlet.
arranged for outward flow filtration · CPC title
using screws (B01D29/6476 takes precedence) · CPC title
open-ended {the arrival of the mixture to be filtered and the discharge of the concentrated mixture are situated on both opposite sides of the filtering element} · CPC title
Filters in combination with devices for the removal of gas, air purge systems · CPC title
using screw filters · CPC title
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