Process for the recovery of hydrogen from ammonia purge gases

Claim 2

A process for synthesizing ammonia from hydrogen and nitrogen comprising: a. introducing to and reacting in an ammonia synthesis reaction zone a nitrogen and hydrogen-containing reactor feed gas at a superatmospheric synthesis pressure to produce ammonia; b. withdrawing an ammonia-containing reaction effluent from said ammonia synthesis reaction zone and recycling said reaction effluent to said ammonia synthesis reaction zone in an ammonia synthesis loop; c. introducing a synthesis feed gas into said ammonia synthesis loop, said synthesis feed gas being at substantially said superatmospheric synthesis pressure and comprising nitrogen, hydrogen, and at least one of methane and argon; d. removing ammonia from the reaction effluent in said ammonia synthesis loop; e. removing a purge stream from said ammonia synthesis loop in an amount sufficient to maintain the volume percent of inert contaminants in the reactor feed gas less than about 25 volume percent, said purge stream containing ammonia and being at substantially said superatmospheric synthesis pressure; f. removing ammonia from said purge stream comprising contacting said purge stream with an absorbent comprising water to provide a purge stream containing less than about 0.5 volume percent ammonia and water vapor; g. contacting said purge stream having an ammonia concentration less than about 0.5 volume percent with a separation membrane, said purge stream contacted with the separation membrane being at a superatmospheric pressure to provide a driving force for hydrogen permeation through the separation membrane, said separation membrane having a feed side and a permeate exit side at a lower total pressure and exhibiting selective permeation of hydrogen as compared to the permeation of each of methane and argon and exhibiting permeability of ammonia; h. permeating through and recovering from the permeate exit side of said separation membrane a permeating gas comprising water and at least about 20 percent of the hydrogen in the purge stream; i. removing from the feed side of said separation membrane a non-permeating gas; j. maintaining said permeating gas at a pressure of substantially at least said total pressure at said permeate exit side of the separation membrane; and k. combining said permeating gas with a gas passing to said ammonia synthesis reaction zone.

Claim 3

The process of claim 1 wherein the purge stream has an ammonia concentration of less than about 0.1 volume percent when contacted with the separation membrane.

Claim 4

The process of claim 1 wherein the permeating gas is dried prior to being introduced into said ammonia synthesis reaction zone.

Claim 5

The process of claim 2 wherein the permeating gas is combined with the synthesis feed gas prior to introducing the synthesis feed gas into the ammonia synthesis loop.

Claim 6

The process of claim 4 wherein the permeating gas is combined with the synthesis feed gas at a point where the permeating gas is at a slightly higher pressure than the synthesis feed gas.

Claim 7

The process of claim 5 wherein the synthesis feed gas is compressed in at least two stages to said superatmospheric synthesis pressure, and said permeating gas is introduced into said synthesis feed gas between two of the compression stages.

Claim 8

The process of claim 2 wherein the permeating gas is compressed to substantially said superatmospheric synthesis pressure and directly introduced into said ammonia synthesis loop.

Claim 9

The process of claim 5, 6 or 7 wherein the pressure drop across the separation membrane is at least about 20 atmospheres.

Claim 10

The process of claim 2, 4 or 7 wherein the purge stream is removed from said ammonia synthesis loop upstream of the removal of ammonia from the ammonia-containing gas.

Claim 11

A process for synthesizing ammonia from hydrogen and nitrogen comprising: a. introducing to and reacting in an ammonia synthesis reaction zone containing an ammonia synthesis catalyst a nitrogen and hydrogen-containing reactor feed gas said reactor gas also containing inert contaminants comprising at least one of methane and argon at a superatmospheric synthesis pressure of about 100 to 350 atmospheres absolute to produce ammonia, said reactor feed gas having a mole ratio of hydrogen to nitrogen of about 2.9:1 to 3.3:1; b. withdrawing an ammonia-containing reaction effluent from said ammonia synthesis reaction zone and recycling said reaction effluent to said ammonia synthesis reaction zone in an ammonia synthesis loop, said reaction effluent comprising hydrogen, nitrogen, ammonia and at least one of methane and argon wherein the reaction effluent comprises about 10 to 25 volume percent ammonia; c. removing a purge stream from said ammonia synthesis loop in an amount sufficient to maintain the volume percent of inert contaminants in the reactor feed gas less than about 25 volume percent; d. removing ammonia from said purge stream to provide a purge stream containing less than about 0.1 volume percent ammonia, said removal being effected by cooling said purge gas at substantially said superatmospheric synthesis pressure to coalesce ammonia, separating the coalesced ammonia from the purge stream and then scrubbing the purge stream with water; e. contacting said purge stream having ammonia removed with a separation membrane, said purge stream when contacted with the separation membrane being at a pressure of at least substantially said superatmospheric pressure, said separation membrane having a feed side and a permeate exit side and exhibiting selective permeation of hydrogen as compared to the permeation of each of methane and argon and exhibiting permeability of ammonia; f. providing said permeate exit side of said separation membrane at a total pressure at least about 50 atmospheres less than the total pressure at said feed side of the membrane; g. permeating through and recovering from the permeate exit side of said separation membrane a permeating gas comprising water vapor and at least about 20 percent of the hydrogen in the purge stream; h. removing from the feed side of said separation membrane a non-permeating gas which is at substantially the same pressure of the purge stream contacting the feed side of the separation membrane; i. maintaining said permeating gas at a pressure of substantially at least said total pressure at said premeate exit side of the separation membrane; j. combining said permeating gas with a gas passing to said ammonia synthesis reaction zone, said permeating gas being dried prior to entering the ammonia synthesis reaction zone; k. introducing a synthesis feed gas into said ammonia synthesis loop after said purge stream has been withdrawn from the ammonia synthesis loop, said synthesis feed gas being at substantially said superatmospheric synthesis pressure and comprising nitrogen, hydrogen, and at least one of methane and argon, wherein the mole ratio of hydrogen to nitrogen is less than the mole ratio of hydrogen to nitrogen in the reactor feed gas and is about 2.7:1 to 3.2:1; and l. removing ammonia from the ammonia synthesis loop after introducing the synthesis feed gas into the ammonia synthesis loop.

Claim 12

A process for synthesizing ammonia from hydrogen and nitrogen comprising: a. introducing to and reacting in an ammonia synthesis reaction zone containing an ammonia synthesis catalyst a nitrogen and hydrogen-containing reactor feed gas said reactor gas also containing inert contaminants comprising at least one of methane and argon at a superatmospheric synthesis pressure of about 100 to 350 atmospheres absolute to produce ammonia, said reactor feed gas having a mole ratio of hydrogen to nitrogen of about 2.9:1 to 3.3:1; b. withdrawing an ammonia-containing reaction effluent from said ammonia synthesis reaction zone and recycling said reaction effluent to said ammonia synthesis reaction zone in an ammonia synthesis loop, said reaction effluent comprising hydrogen, nitrogen, ammonia and at least one of methane and argon wherein the reaction effluent comprises about 10 to 25 volume percent ammonia; c. removing a purge stream from said ammonia synthesis loop in an amount sufficient to maintain the volume percent of inert contaminants in the reactor feed gas less than about 25 volume percent; d. removing ammonia from said purge stream to provide a purge stream containing less than about 0.1 volume percent ammonia, said removal being effected by cooling said purge gas at substantially said superatmospheric synthesis pressure to coalesce ammonia, separating the coalesced ammonia from the purge stream and then scrubbing the purge stream with water; e. contacting said purge stream having ammonia removed with a separation membrane, said purge stream when contacted with the separation membrane being at a pressure of at least substantially said superatmospheric pressure, said separation membrane having a feed side and a permeate exit side and exhibiting selective permeation of hydrogen as compared to the permeation of each of methane and argon and exhibiting permeability of ammonia; f. providing said permeate exit side of said separation membrane at a total pressure at least about 50 atmospheres less than the total pressure at said feed side of the membrane; g. permeating through and recovering from the permeate exit side of said separation membrane a permeating gas comprising water vapor and at least about 20 percent of the hydrogen in the purge stream; h. removing from the feed side of said separation membrane a non-permeating gas which is at substantially the same pressure of the purge stream contacting the feed side of the separation membrane; i. maintaining said permeating gas at a pressure of substantially at least said total pressure at said premeate exit side of the separation membrane; j. combining said permeating gas with a gas passing to said ammonia synthesis reaction zone, said permeating gas being dried prior to entering the ammonia synthesis reaction zone; k. introducing a synthesis feed gas into said ammonia synthesis loop after said purge stream has been withdrawn from the ammonia synthesis loop, said synthesis feed gas being at substantially said superatmospheric synthesis pressure and comprising nitrogen, hydrogen, and at least one of methane and argon, wherein the mole ratio of hydrogen to nitrogen is less than the mole ratio of hydrogen to nitrogen in the reactor feed gas and is about 2.7:1 to 3.2:1; and l. removing ammonia from the ammonia synthesis loop after introducing the synthesis feed gas into the ammonia synthesis loop.

Claim 13

The process of claim 10 wherein the separation membrane exhibits a separation factor for hydrogen over methane is at least about 10.

Claim 14

The process of claim 10 or 11 wherein the permeating gas comprises about 60 to essentially 100 volume percent hydrogen.

Claim 15

The process of claim 10 wherein the permeating gas comprises about 40 to 80 percent of the hydrogen in the purge gas.

Claim 16

The process of claim 10 wherein the reactor feed gas introduced into the ammonia synthesis reaction zone comprises about 0.5 to 5 volume percent ammonia, about 2 to 15 volume percent methane, and about 2 to 10 volume percent argon.

Claim 17

The process of claim 10 wherein the permeating gas is combined with the synthesis feed gas prior to introducing the synthesis feed gas into the ammonia synthesis loop.

Claim 18

The process of claim 15 wherein the permeating gas is at a slightly higher pressure than the synthesis feed gas when combined.

Claim 19

The process of claim 16 wherein the synthesis feed gas is compressed in at least two stages to said superatmospheric synthesis pressure, and said permeating gas is combined with said synthesis feed gas between two of the compression stages.

Claim 20

The process of claim 17 wherein said synthesis feed gas contains water, water is removed from the synthesis feed gas prior to its introduction into the ammonia synthesis loop, and the permeating gas is combined with the synthesis feed gas prior to said water removal.

Claim 21

The process of claim 10 wherein the permeating gas is compressed to substantially said superatmospheric synthesis pressure and directly introduced into said ammonia synthesis loop.

Claim 22

A process for synthesizing ammonia from hydrogen and nitrogen comprising: a. introducing to and reacting in an ammonia synthesis reaction zone a nitrogen and hydrogen-containing reactor feed gas at a superatmospheric synthesis pressure to produce ammonia; b. withdrawing an ammonia-containing reaction effluent from said ammonia synthesis reaction zone and recycling said reaction effluent to said ammonia synthesis reaction zone in an ammonia synthesis loop; c. introducing a synthesis feed gas into said ammonia synthesis loop, said synthesis feed gas being at substantially said superatmospheric synthesis pressure and comprising nitrogen, hydrogen, and at least one of methane and argon; d. removing ammonia from the reaction effluent in said ammonia synthesis loop; e. removing a purge stream from said ammonia synthesis loop in an amount sufficient to maintain the volume percent of inert contaminants in the reactor feed gas less than about 25 volume percent, said purge stream containing ammonia and being at substantially said superatmospheric synthesis pressure; f. removing ammonia from said purge stream to provide a purge stream containing less than about 0.1 volume percent ammonia; g. contacting said purge stream having an ammonia concentration less than about 0.1 volume percent with a separation membrane, said purge stream when contacted with the separation membrane being at a superatmospheric pressure to provide a driving force for hydrogen permeation through the separation membrane, said separation membrane having a feed side and a permeate exit side at a lower total pressure and exhibiting selective permeation of hydrogen as compared to the permeation of each of methane and argon and exhibiting permeability of ammonia; h. permeating through and recovering from the permeate exit side of said separation membrane a permeating gas comprising at least about 20 percent of the hydrogen in the purge stream; i. removing from the feed side of said separation membrane a non-permeating gas; j. maintaining said permeating gas at a pressure of substantially at least said total pressure at said permeate exit side of the separation membrane; and k. combining said permeating gas with a gas passing to said ammonia synthesis reaction zone.

Claim 23

A process for synthesizing ammonia from hydrogen and nitrogen comprising: a. introducing to and reacting in an ammonia synthesis reaction zone a nitrogen and hydrogen-containing reactor feed gas at a superatmospheric synthesis pressure to produce ammonia; b. withdrawing an ammonia-containing reaction effluent from said ammonia synthesis reaction zone and recycling said reaction effluent to said ammonia synthesis reaction zone in an ammonia synthesis loop; c. introducing a synthesis feed gas into said ammonia synthesis loop, said synthesis feed gas being at substantially said superatmospheric synthesis pressure and comprising nitrogen, hydrogen, and at least one of methane and argon; d. removing ammonia from the reaction effluent in said ammonia synthesis loop; e. removing a purge stream from said ammonia synthesis loop in an amount sufficient to maintain the volume percent of inert contaminants in the reactor feed gas less than about 25 volume percent, said purge stream containing ammonia and being at substantially said superatmospheric synthesis pressure; f. removing ammonia from said purge stream to provide a purge stream containing less than about 0.1 volume percent ammonia; g. contacting said purge stream having an ammonia concentration less than about 0.1 volume percent with a separation membrane, said purge stream when contacted with the separation membrane being at a superatmospheric pressure to provide a driving force for hydrogen permeation through the separation membrane, said separation membrane having a feed side and a permeate exit side at a lower total pressure and exhibiting selective permeation of hydrogen as compared to the permeation of each of methane and argon and exhibiting permeability of ammonia; h. permeating through and recovering from the permeate exit side of said separation membrane a permeating gas comprising at least about 20 percent of the hydrogen in the purge stream; i. removing from the feed side of said separation membrane a non-permeating gas; j. maintaining said permeating gas at a pressure of substantially at least said total pressure at said permeate exit side of the separation membrane; and k. combining said permeating gas with a gas passing to said ammonia synthesis reaction zone.

Claim 24

The process of claim 20 wherein the permeating gas is combined with the synthesis feed gas prior to introducing the synthesis feed gas into the ammonia synthesis loop.

Claim 25

The process of claim 21 wherein the permeating gas is combined with the synthesis feed gas at a point where the permeating gas is at a slightly higher pressure than the synthesis feed gas.

Claim 26

The process of claim 22 wherein the synthesis feed gas is compressed in at least two stages to said superatmospheric synthesis pressure, and said permeating gas is introduced into said synthesis feed gas between two of the compression stages.

Claim 27

The process of claim 20 wherein the permeating gas is compressed to substantially said superatmospheric synthesis pressure and directly introduced into said ammonia synthesis loop.

Claim 28

The process of claim 20, 21 or 24 wherein the pressure drop across the separation membrane is at least about 20 atmospheres.

Claim 29

The process of claim 20, 21 or 24 wherein the purge stream is removed from said ammonia synthesis loop upstream of the removal of ammonia from the ammonia-containing gas.