Recovery of hydrogen and ammonia from purge gas

Claim 3

A method as claimed in claim 1 in which after recovery from said adsorber, regenerating gas is combined with the remainder of the hydrogen rich gas stream for return to the ammonia synthesis reactor.

Claim 4

A method as claimed in claim 1 in which after the ammonia adsorber has been regenerated it is cooled ready for re-use in adsorption mode by passing through it a cooling gas provided from the hydrogen-rich gas stream.

Claim 5

A method as claimed in claim 3 in which the ammonia adsorber includes at least three adsorption zones arranged so that while at least one is in adsorption mode, at least a second is being regenerated and at least a third is being cooled subsequent to regeneration, and regeneration gas for said second zone is provided by heating cooling gas recovered from said third zone.

Claim 6

A method as claimed in claim 1 in which the cooling of the substantially ammonia-free compressed purge gas to partially condense it is assisted by passing said gas in indirect heat exchange with a refrigerant.

Claim 7

A method as claimed in claim 5 in which the refrigerant comprises liquid ammonia provided by expanding ammonia formed in the ammonia synthesis.

Claim 8

A method as claimed in claim 5 in which the refrigerant comprises liquid ammonia obtained by cooling the compressed purge gas to condense a part of its ammonia content prior to removing ammonia therefrom by adsorption in said ammonia adsorber, and expanding condensed ammonia thereby obtained.

Claim 9

A method as claimed in claim 7 in which said purge gas contains more than 2 mole % ammonia and the compressed purge gas is cooled to reduce the ammonia content to not greater than 2% by condensation prior to removing ammonia by adsorption in said ammonia adsorber.

Claim 10

A method as claimed in claim 1 in which the regenerating gas is provided by heating a portion of the hydrogen-rich gas stream, the heat being provided by combustion of a fuel gas provided from the evaporated condensate.

Claim 11

A method as claimed in claim 9 in which the regenerating gas is heated with superheated steam and heat for producing the superheated stream is provided by combustion of a fuel gas provided from the evaporated condensate.

Claim 12

Apparatus for recovering ammonia and hydrogen values from a purge gas from an ammonia synthesis recycle stream, the apparatus comprising an ammonia adsorber unit having an inlet for purge gas to be treated and an outlet for treated purge gas and including at least three adsorption zones and said unit being constructed and arranged for cyclic operation such that in successive periods each zone is (a) connected between said inlet and said outlet and is in adsorption mode, (b) thereafter undergoes regeneration and then (c) is cooled ready for re-use in adsorption mode, and in each period at least one zone is connected between said inlet and outlet and is in adsorption mode, at least a second is undergoing regeneration and at least a third is undergoing cooling ready for re-use in adsorption mode; means for passing cooling gas through said at least third zone to cool it; means for providing heated regeneration gas to said at least second zone; and means for recovering regeneration gas from said at least second zone; a cryogenic separation unit including a heat exchanger, an expansion valve and a vapour-liquid separator, said heat exchanger having a first passageway having an inlet adapted to be connected for flow of fluid thereto from the outlet for the treated purge gas from said adsorption unit and an outlet connected for flow of fluid therefrom to the inlet of said separator, a second passageway having an inlet connected for flow of fluid thereto from the vapour outlet of said separator and an outlet, and a third passageway having an inlet for flow of fluid thereto from the low pressure outlet of said expansion valve the inlet of which is connected for flow of fluid thereto from the liquid outlet of the separator, and an outlet; and in which the outlet of said second heat exchanger passageway is connected (a) to said means for providing heated regeneration gas whereby a first portion of the vapour recovered from said vapour/liquid separator is passed to said second zone as regeneration gas and (b) to a product gas pipeline.

Claim 13

Apparatus for recovering ammonia and hydrogen values from a purge gas from an ammonia synthesis recycle stream, the apparatus comprising an ammonia adsorber unit having an inlet for purge gas to be treated and an outlet for treated purge gas and including at least three adsorption zones and said unit being constructed and arranged for cyclic operation such that in successive periods each zone is (a) connected between said inlet and said outlet and is in adsorption mode, (b) thereafter undergoes regeneration and then (c) is cooled ready for re-use in adsorption mode, and in each period at least one zone is connected between said inlet and outlet and is in adsorption mode, at least a second is undergoing regeneration and at least a third is undergoing cooling ready for re-use in adsorption mode; means for passing cooling gas through said at least third zone to cool it; means for providing heated regeneration gas to said at least second zone; and means for recovering regeneration gas from said at least second zone; a cryogenic separation unit including a heat exchanger, an expansion valve and a vapour-liquid separator, said heat exchanger having a first passageway having an inlet adapted to be connected for flow of fluid thereto from the outlet for the treated purge gas from said adsorption unit and an outlet connected for flow of fluid therefrom to the inlet of said separator, a second passageway having an inlet connected for flow of fluid thereto from the vapour outlet of said separator and an outlet, and a third passageway having an inlet for flow of fluid thereto from the low pressure outlet of said expansion valve the inlet of which is connected for flow of fluid thereto from the liquid outlet of the separator, and an outlet; and in which the outlet of said second heat exchanger passageway is connected (a) to said means for providing heated regeneration gas whereby a first portion of the vapour recovered from said vapour/liquid separator is passed to said second zone as regeneration gas and (b) to a product gas pipeline.

Claim 14

Apparatus as claimed in claim 11 in which the means for providing heated regeneration gas to said at least second zone comprises means for heating cooling gas recovered from said at least third zone and providing the heated gas as regeneration gas to said at least second zone, and the outlet of said second heat exchanger passageway is connected for fluid flow to the inlet to said at least third zone whereby said first portion of vapour recovered from said vapour/liquid separator is passed first to said third zone as said cooling gas and thence to said second zone as said regeneration gas.

Claim 15

Apparatus as claimed in claim 11, which includes a second conduit for passing gas recovered from said at least second zone to said product gas pipeline.

Claim 16

Apparatus as claimed in claim 11 further including a fourth passageway in said heat exchanger and means for supplying a refrigerant thereto in indirect heat exchange relationship with said purge gas in said first passageway to assist the cooling of said purge gas.

Claim 17

Apparatus as claimed in claim 14 and further including means for condensing a part of the ammonia content of the purge gas prior to passing the purge gas to said adsorber unit, and means for expanding liquid ammonia thereby obtained and providing it as said refrigerant to said fourth passageway.