Removal of gaseous nh3 from an nh3 reactor product stream

Abstract

The present invention is directed to the removal of ammonia from an ammonia reactor product stream. Systems and methods of the present invention enable ammonia to be synthesized and removed using a broader range of process conditions than are possible with current industrial practices. In particular, the systems and methods enable the use of higher temperatures, lower pressures, and higher reactant flows.

1 - 20 . (canceled) 
     
     
         21 . An ammonia synthesis and storage system, comprising:
 a reactor configured to produce ammonia from an input gas stream, the input gas stream comprising a nitrogen gas and a hydrogen gas;   a first heat exchanger configured to receive a product gas stream from the reactor and cool the product gas stream to produce a cooled product gas stream, wherein the product gas stream comprises at least one of an ammonia gas, an unspent nitrogen gas, and an unspent hydrogen gas;   at least one adsorption cartridge configured to adsorb at least a portion of the ammonia gas from the cooled product gas stream; and   at least one desorption device to desorb at least a portion of the adsorbed ammonia from the at least one adsorption cartridge.   
     
     
         22 . The system of claim  1 , wherein the first heat exchanger is further configured to remove heat from the reactor. 
     
     
         23 . The system of claim  1 , further comprising:
 a second heat exchanger configured to remove heat from the reactor.   
     
     
         24 . The system of claim  1 , further comprising:
 a liquefaction condenser, the liquefaction condenser configured to remove at least a portion of the ammonia gas from the cooled product stream prior to ammonia gas being adsorbed from the cooled product stream by the at least one adsorption cartridge.   
     
     
         25 . The system of claim  1 , wherein the input gas stream further comprises a recycled gas stream comprising a recycled amount of ammonia gas, a recycled amount of nitrogen gas, and a recycled amount of hydrogen gas. 
     
     
         26 . The system of claim  1 , further comprising at least one product stream valve, wherein the at least one product stream valve directs the cooled product gas stream to one or more of the at least one adsorption cartridges. 
     
     
         27 . The system of claim  1 , further comprising at least one post adsorber valve, wherein the at least one post adsorber valve directs a recycled stream to the reactor. 
     
     
         28 . The system of claim  7 , wherein the recycled stream comprises at least one of a recycled nitrogen gas, a recycled hydrogen gas, and a recycled ammonia gas. 
     
     
         29 . The system of claim  7 , further comprising at least one recycling pump to recycle the recycled stream. 
     
     
         30 . The system of claim  1 , wherein each of the at least one adsorption cartridges comprise molecular sieves. 
     
     
         31 . The system of claim  1 , wherein each of the at least one adsorption cartridges are regenerated. 
     
     
         32 . The system of claim  7 , further comprising at least one ammonia detector that detects an amount of ammonia in the recycled stream. 
     
     
         33 . The system of claim  10 , wherein at least one of the molecular sieves comprises a 4A, 5A, 13X, or larger molecular sieve and wherein the molecular sieve comprises a pore size of between about 3.4 angstroms and about 10 nm. 
     
     
         34 . The system of claim  10 , wherein a material of the molecular sieve is an alkaline oxide aluminosilicate or an alkaline oxide borosilicate. 
     
     
         35 . The system of claim  1 , wherein the desorption device is a compressor and wherein the compressor reduces a pressure of the at least one adsorption cartridges to desorb the ammonia from the at least one of the adsorption cartridge. 
     
     
         36 . A method for producing ammonia, comprising:
 introducing an input gas stream comprising a nitrogen gas and a hydrogen gas into a reactor;   reacting the input gas stream in the reactor to form a product gas stream, wherein the product gas stream comprises at least one of an ammonia gas, the nitrogen gas, and the hydrogen gas;   cooling the product gas stream with a heat exchanger to produce a cooled product gas stream;   adsorbing at least a portion of the ammonia gas from the cooled product gas stream with at least one adsorption cartridge to produce ammonia on the at least one adsorption cartridge; and   desorbing the ammonia from the at least one adsorption cartridge with at least one desorbing apparatus.   
     
     
         37 . The method of claim  16 , further comprising:
 removing at least a portion of the ammonia gas from the cooled product stream with a liquefaction condenser prior to adsorbing at least a portion of the ammonia gas from the cooled product stream with at least one adsorption cartridge.   
     
     
         38 . The method of claim  16 , wherein the at least one adsorption cartridge comprises a molecular sieve, wherein a pore size of the molecular sieve is between about 3.4 angstroms and about 10 nm, and wherein the at least one adsorption cartridge is reusable. 
     
     
         39 . The method of claim  16 , further comprising directing the cooled product gas stream with at least one product gas stream valve to the at least one adsorption cartridge, and closing the at least one product gas stream valve to remove ammonia from the at least one adsorption cartridge after detecting ammonia in the recycled gas stream. 
     
     
         40 . The method of claim  16 , wherein the at least one desorbing apparatus is a compressor and a heater, wherein the compressor reduces a pressure of the at least one adsorption cartridge to desorb the ammonia from the at least one adsorption cartridge, and wherein the heater increases a temperature of the at least one adsorption cartridge.