System with a direct contact desublimating heat exchanger and temperature regulation
A process to prevent fouling using a desublimating heat exchanger is disclosed. An outlet stream from the desublimating heat exchanger may be split into a plurality of parallel streams. The parallel streams may be sent through a plurality of discrete unit operations, and the unit operations may change the temperature of at least one of the parallel streams. Parallel streams of differing temperature may emerge from the unit operations. The parallel streams which are of a similar temperature may be mixed to form a warm stream and a cool stream. The warm stream and the cool stream may be sent to a mixing chamber. A mixed stream of substantially uniform temperature may emerge from the mixing chamber, and the mixed stream may be recycled back to the desublimating heat exchanger. The mixing chamber may be separate from the desublimating heat exchanger, or the parallel streams of differing temperature may be mixed in the desublimating heat exchanger.
1. A method for removing a component from a gas stream, comprising:
passing a liquid outlet stream out of a desublimating heat exchanger, the liquid outlet stream being at a temperature T 1 and comprising a cryogenic contact fluid and a solute, a solid, or a combination of the solute and the solid;
splitting the liquid outlet stream into a plurality of liquid streams;
passing the plurality of liquid streams through unit operations, resulting in a plurality of liquid product streams each at different temperatures, wherein a warm liquid product stream comprises a warmest of the plurality of liquid product streams and a cold liquid product stream comprises a coldest of the plurality of liquid product streams;
passing the warm liquid product stream into the mixing chamber at a first location and passing the cold liquid product stream into the mixing chamber at a second location, wherein the first and the second location are different;
mixing the warm liquid product stream and the cold liquid product stream results in a recycle liquid stream, and wherein a portion of the solute freezes in the mixing chamber.
2. The invention of claim 1 , wherein there are three liquid streams in the plurality of liquid streams and the cold liquid product stream is mixed with next coldest of the plurality of liquid product streams before the warm liquid product stream is mixed with the cold liquid product stream.
3. The invention of claim 1 , wherein there are three liquid streams in the plurality of liquid streams and the warm liquid product stream is mixed with next warmest of the plurality of liquid product streams before the warm liquid product stream is mixed with the cold liquid product stream.
4. The invention of claim 1 , wherein there are four liquid streams in the plurality of liquid streams and the warm liquid product stream is mixed with a next warmest of the plurality of liquid product streams and the cold liquid product stream is mixed with a next coldest of the plurality of liquid product streams before the warm liquid product stream is mixed with the cold liquid product stream.
5. The invention of claim 1 , wherein the unit operations comprise a screw press, a second heat exchanger, or a separation unit.
6. The invention of claim 1 , wherein the liquid outlet stream is saturated with a compound selected from the group consisting of carbon dioxide, nitrogen oxide, sulfur dioxide, nitrogen dioxide, sulfur trioxide, hydrogen sulfide, hydrogen cyanide, water, hydrocarbons, and combinations thereof.
7. The invention of claim 1 , wherein the mixing chamber is a second desublimating heat exchanger.
8. The invention of claim 1 , further comprising passing the recycle liquid stream into the desublimating heat exchanger.