Liquid sorbent-enhanced ammonia production
The present disclosure relates to a method that includes, in a first zone, contacting an ammonia-rich gas comprising ammonia with an ammonia-lean liquid sorbent resulting in the reversible transfer of at least a portion of the ammonia from the ammonia-rich gas to the ammonia-lean liquid sorbent, thereby forming an ammonia-rich liquid sorbent and an ammonia-lean gas and, in a second zone, removing at least a portion of the ammonia from the ammonia-rich liquid sorbent to form gaseous ammonia and regenerate the ammonia-lean liquid sorbent.
1 . A method comprising:
in an ammonia synthesis reactor, reacting H 2 and N 2 to form an ammonia-rich gas;
in a first zone, contacting the ammonia-rich gas with an ammonia-lean liquid sorbent comprising an acid (HA) resulting in reversible transfer of ammonia from the ammonia-rich gas to the ammonia-lean liquid sorbent, thereby forming an ammonia-rich liquid sorbent and an ammonia-lean gas; and
in a second zone, removing ammonia from the ammonia-rich liquid sorbent to form gaseous ammonia and regenerate the ammonia-lean liquid, wherein:
the acid comprises at least one of CsH 2 PO 4 , HB x F y , HSO 3 C a F b , H 3 PMo 12 O 40 ·12H 2 O, H 3 PW 12 O 40 ·nH 2 O, H 4 SiW 12 O 40 ·pH 2 O, or a combination thereof,
1≤x≤20,4≤y≤42,1≤a≤10,3≤b≤21,6≤n≤24, and 6≤p≤29.
2 . The method of claim 1 , wherein the regenerated ammonia-lean liquid sorbent is cycled back to the first zone.
3 . The method of claim 1 , wherein:
the first zone is maintained at a first pressure, and
the second zone is maintained at a second pressure that is lower than the first pressure.
4 . The method of claim 3 , wherein the first pressure is between 5 bar and 300 bar.
5 . The method of claim 3 , wherein the second pressure is between 0 bar and 100 bar.
6 . The method of claim 1 , wherein:
the first zone is maintained at a first temperature, and
the second zone is maintained at a second temperature that is lower than the first temperature.
7 . The method of claim 6 , wherein the first temperature is between 100° C. and 600° C.
8 . The method of claim 6 , wherein the second temperature is between 100° C. and 600° C.
9 . The method of claim 1 , wherein:
the ammonia-rich liquid sorbent comprises a complex of ammonia and the acid ((NH 4 )A),
the reversible transfer of ammonia comprises a reaction defined by HA+y NH 3 (NH 4 ) y A x , wherein 1≤y≤10.
10 . The method of claim 9 , wherein the ammonia-rich liquid sorbent further comprises water in which the acid is present as at least one of a solute, a suspension, or a combination thereof.
11 . The method of claim 1 , wherein at least one of the first zone or the second zone is integrated into a single unit operation that includes the ammonia synthesis reactor.
12 . The method of claim 1 , wherein the first zone and the second zone are integrated into a single unit operation that is physically separate from the ammonia synthesis reactor.
13 . The method of claim 1 , wherein the first zone is positioned within a first contained volume comprising at least one of a vessel, a tank, a column, a shell, or a combination thereof.
14 . The method of claim 1 , wherein the ammonia-rich gas further comprises at least one of unreacted H 2 or N 2 .
15 . The method of claim 14 , wherein the ammonia-lean gas further comprises the unreacted H 2 or N 2 and the ammonia-lean gas is recycled to the reactor.
16 . The method of claim 1 , transferring heat from the ammonia-rich gas to the ammonia-lean gas.
17 . The method of claim 13 , wherein:
the first contained volume has a high point and a low point, and
the ammonia-rich gas and the ammonia-lean liquid sorbent are both configured to enter at the low point.
18 . The method of claim 13 , wherein:
the first contained volume has a high point and a low point, and
the ammonia-rich gas and the ammonia-lean liquid sorbent are both configured to enter at the high point.
19 . The method of claim 13 , wherein:
the first contained volume has a high point and a low point, and
the ammonia-lean liquid sorbent is configured to enter at the high point, and
the ammonia-rich gas is configured to enter at the low point.
20 . The method of claim 13 , wherein:
the first contained volume has a high point and a low point, and
the ammonia-lean liquid sorbent is configured to enter at the low point, and
the ammonia-rich gas is configured to enter at the high point.
21 . The method of claim 1 , wherein the acid further comprises at least one of an alkyl phosphoric acid, a benzyl phosphoric acid, a perfluoroalkyl phosphoric acids, or a combination thereof.