Methods and systems for separating compounds
Methods and systems for separating a desublimatable compound from hydrocarbons is disclosed. A feed fluid stream, consisting of a hydrocarbon and a desublimatable compound, is passed into an upper chamber of a vessel. The feed fluid stream is cooled in the upper chamber, thereby desublimating a portion of the desublimatable compound out of the feed liquid stream to form a product gas stream and a desublimatable compound snow which is collected in the lower chamber of the vessel. A lower portion of the desublimatable compound snow is melted to form a liquid desublimatable compound stream such that an upper portion of the solid desublimatable compound snow remains as an insulative barrier between the upper chamber and the liquid desublimatable compound stream. The liquid desublimatable compound stream is removed at a rate that matches a production rate of the solid desublimatable compound snow, thereby maintaining the insulative barrier.
1. A method for continuously separating a desublimatable compound from hydrocarbons comprising:
providing a vessel comprising an upper chamber and a lower chamber;
passing a feed fluid stream into the upper chamber, the feed fluid stream comprising a hydrocarbon and a desublimatable compound;
cooling the feed fluid stream in the upper chamber, thereby desublimating a portion of the desublimatable compound out of the feed fluid stream to form a solid desublimatable compound snow and a product gas stream;
collecting the solid desublimatable compound snow in the lower chamber;
melting a lower portion of the solid desublimatable compound snow to form a liquid desublimatable compound stream such that an upper portion of the solid desublimatable compound snow remains as an insulative barrier that physically separates the upper chamber from all of the liquid desublimatable compound stream;
removing the liquid desublimatable compound stream at a rate that matches a production rate of the solid desublimatable compound snow, thereby maintaining the insulative barrier; and
removing the product gas stream from the upper chamber.
2. The method of claim 1 , wherein the desublimatable compound is selected from the group consisting of carbon dioxide, sulfur oxides, nitrogen oxides, carbon monoxide, and combinations thereof.
3. The method of claim 1 , wherein the hydrocarbon is selected from the group consisting of methane, ethane, propane, and combinations thereof.
4. The method of claim 1 , wherein cooling the feed fluid stream comprises flashing a cold liquid stream into the upper chamber, thereby reducing the temperature of the upper chamber, the cold liquid stream comprising the hydrocarbon.
5. The method of claim 4 , further comprising passing a portion of the product gas stream through a refrigeration loop to produce the cold liquid stream.
6. The method of claim 1 , wherein melting comprises injecting a warm liquid desublimatable compound stream into the lower chamber.
7. The method of claim 1 , wherein melting comprises heating the lower chamber with a heating element.
8. A method for continuously separating components comprising:
providing a vessel comprising an upper chamber and a lower chamber;
passing a feed fluid stream into the upper chamber, the feed fluid stream comprising methane and carbon dioxide;
flashing a cold liquid stream into the upper chamber, thereby reducing the temperature of the upper chamber, wherein the cold liquid stream comprises methane;
desublimating the carbon dioxide out of the feed fluid stream to form a solid carbon dioxide snow and a product gas stream;
collecting the solid carbon dioxide snow in the lower chamber;
melting a lower portion of the solid carbon dioxide snow to form a liquid carbon dioxide stream such that an upper portion of the solid carbon dioxide snow remains as an insulative barrier that physically separates the upper chamber from all of the liquid carbon dioxide stream;
removing the liquid carbon dioxide stream at a rate that matches a production rate of the solid carbon dioxide snow, thereby maintaining the insulative barrier; and
removing the product gas stream from the upper chamber.
9. The method of claim 8 , wherein the feed fluid stream comprises at least 20 wt % carbon dioxide, is at least 25 bar, and is less than −55° C.
10. The method of claim 8 , wherein the feed fluid stream comprises C2+ natural gas components.
11. The method of claim 8 , wherein the cold liquid stream comprises no more than 3 wt % carbon dioxide, is at least 50 bar, and is less than −102° C.
12. The method of claim 8 , further comprising passing a portion of the product gas stream through a refrigeration loop to produce the cold liquid stream.
13. The method of claim 8 , wherein melting comprises injecting a warm liquid carbon dioxide stream into the lower chamber.
14. The method of claim 8 , wherein melting comprises heating the lower chamber with a heating element.
15. A system for continuously separating components comprising:
a vessel comprising an upper chamber and a lower chamber;
the upper chamber comprising a feed gas inlet, a cooling source, and a product gas outlet;
the lower chamber comprising a product liquid outlet and a heat source;
the feed gas inlet passing a feed gas stream through the feed gas inlet into the upper chamber, the feed gas stream comprising a hydrocarbon and a desublimatable compound;
wherein the cooling source cools the feed gas stream, thereby desublimating a portion of the desublimatable compound out of the feed gas stream to form a solid desublimatable compound snow and a product gas stream, the solid desublimatable compound snow falling into the lower chamber;
wherein a heat source melts a lower portion of the solid desublimatable compound snow in the lower chamber to form a liquid desublimatable compound stream in a manner that an upper portion of the solid desublimatable compound snow remains as an insulative barrier that physically separates the upper chamber from all of the liquid desublimatable compound stream;
the product liquid outlet configured to remove the liquid desublimatable compound stream at a rate that matches a production rate of the solid desublimatable compound snow, thereby maintaining the insulative barrier; and
the product gas outlet configured to remove the product gas stream from the upper chamber.
16. The system of claim 15 , further comprising a refrigerant loop configured to receive, cool, and compress a portion of the product gas stream to form a cold liquid stream and wherein the cooling source is a result of flashing the cold liquid stream into the upper chamber.
17. The system of claim 15 , wherein the heat source an inductive resistance heater embedded in or attached to walls of the lower chamber.
18. The system of claim 15 , wherein the heat source is an indirect-contact heat exchanger.
19. The system of claim 15 , wherein the lower chamber comprises an auger configured to convey the solids towards the product liquid outlet as the solids melt.
20. The system of claim 15 , wherein the desublimatable compound is selected from the group consisting of carbon dioxide, sulfur oxides, nitrogen oxides, carbon monoxide, and combinations thereof.