Fractional condensation processes, apparatuses and systems
The present invention provides fractional condensation apparatuses, systems and methods that can recover volatile products from highly diluted liquid and vapor feed mixtures with high purity and recovery yield, both in batch and continuous distillation, while being also designed to achieve low-cost and efficient recovery processes. Single apparatuses and columns can be connected to each other to expand or shrink the column length for desired separation. The apparatuses, systems and methods can be applied to separate mixtures with both narrow and wide boiling point ranges.
1. A process for recovering ethanol from a feed mixture comprising:
(a) introducing the feed mixture into a fractional condensation apparatus;
(b) fractionally condensing the feed mixture in the fractional condensation apparatus to form a first condensed fluid and a first vapor, the feed mixture having a temperature between about 30° C. and about 60° C. before fractional condensing;
(c) condensing the first vapor in a top condenser to form a second condensed fluid and a second vapor, the top condenser having a temperature between about 6° C. and about 11° C.; and
(d) condensing the second vapor in a product condenser to form a cold product stream, the product condenser having a temperature that is below the temperature of the top condenser;
wherein the feed mixture contains between about 1 mol % and about 5 mol % of ethanol, at least about 5 mol % water, and at least about 90 mol % gases selected independently from the group consisting of N 2 , O 2 and CO 2 , or mixtures thereof; whereby a concentration of ethanol in the cold product stream of at least about 80 wt % and a recovery of at least about 60 wt % is obtained.
2. The process of claim 1 , wherein the top condenser is an integral part of the fractional condensation apparatus.
3. The process of claim 1 , wherein the feed mixture is a vapor feed with a concentration of ethanol of between about 1.0 and about 3.0 mol % and a temperature of between about 37° C. and about 38° C. before fractional condensing, and the top condenser has a temperature between about 6° C. and about 9° C.
4. The process of claim 1 , wherein the feed mixture is a vapor feed with a concentration of the ethanol of between about 1.0 and about 3.0 mol % and a temperature of between about 54° C. and about 56° C. before fractional condensing, and the top condenser has a temperature between about 7° C. and about 11° C.
5. The process of claim 1 , wherein the feed mixture is a vapor feed with a concentration of ethanol of between about 1.5 mol % and about 2.5 mol % and a temperature of between about 37° C. and about 38° C. before fractional condensing, the top condenser has a temperature between about 6° C. and about 9° C., the method further comprising providing a total cooling duty of not more than (PEU) 6 MJ/kg ethanol to recover the ethanol with a concentration of at least about 80 wt % in the product stream and a recovery of at least about 90 wt %.
6. The process of claim 1 , wherein the feed mixture is a vapor feed with a concentration of ethanol of between about 1.5 mol % and about 2.5 mol % and a temperature of between about 55° C. and about 56° C. before fractional condensing, the top condenser has a temperature between about 7.5° C. and about 9.5° C., the method further comprising providing a total cooling duty of not more than (PEU) 8 MJ/kg ethanol to recover the ethanol with a concentration of at least about 80 wt % in the product stream and a recovery of at least about 90 wt %.
7. The process of claim 1 , wherein the feed mixture is a vapor feed with a concentration of ethanol of between about 1.5 mol % and about 2.5 mol % and a temperature of between about 37° C. and about 38° C. before fractional condensing, the top condenser has a temperature between about 7° C. and about 8° C., the method further comprising providing a total cooling duty of not more than (PEU) 6 MJ/kg ethanol to recover the ethanol with a concentration of at least about 85 wt % and a recovery of at least about 95 wt %.
8. The process of claim 1 , wherein the product condenser has a temperature of between about −25° C. and about −45° C.
9. The process of claim 1 , wherein the product condenser has a temperature of about −35° C.
10. The process of claim 1 , wherein the product condenser further produces a cold vent stream, and the method further comprises heating the cold product stream and the cold vent stream by providing cooling duty to the fractional condensation apparatus.
11. The process of claim 1 , wherein the fractional distillation apparatus has a temperature profile from entry of the feed mixture to exit of the first condensed fluid which is controlled to improve recovery and concentration of the volatile organic compound in the product stream.