Abstract: A method and apparatus for producing carbon monoxide by cryogenic distillation is presented.

Abstract: A method and an apparatus for producing carbon dioxide by cryogenic distillation is provided.

Abstract: A method and apparatus for producing carbon monoxide by cryogenic distillation is provided.

Abstract: The invention provides an installation for the production of hydrogen and/or carbon monoxide and/or a mixture of hydrogen and carbon monoxide, by separating a mixture to be processed (1) which contains at least carbon monoxide and hydrogen. Said installation comprises a production apparatus (9), for producing a feed mixture (3), a separating unit (BF), means for supplying the feed mixture to the separating unit, means for collecting hydrogen and/or carbon monoxide and/or a mixture of both products (7, 8), derived from the separating unit, means for drawing off at least one recycling gas (6) from the separating unit, means for returning said recycling gas upstream of the separating unit, for separating said gas simultaneously with the feed mixture from the production apparatus and means for modifying the rate and composition of said feed mixture, by modifying the operation of the production apparatus, according to the rate and composition of said at least one recycling gas.

Abstract: Systems and methods are disclosed for a gas production system to efficiently maintain a pressure of a gaseous output stream within a tight pressure range when the system changes normal operation to backup operation. In one preferred embodiment, during normal operation a backup vaporizer is kept in cold standby by directing a small portion of a liquefied gas stream away from the main heat exchanger to the backup vaporizer. In this way, the backup vaporizer is able to respond immediately to a shutdown of the main gas production system. During normal operation, the output of the backup vaporizer is recombined with the gaseous output stream to any avoid loss of product thereby increasing efficiency.

Abstract: Method and system for removing impurities such as chlorine, chloramines, and ammonia from a hydrogen gas. One embodiment of the invention provides for passing the hydrogen gas through a first scrubbing unit having a reducing agent in solution to at least partially remove chlorine and chloramines from the hydrogen gas. The hydrogen gas may be passed from the first scrubbing unit through a second scrubbing unit having an acid in solution to at least partially remove ammonia from the hydrogen gas.

Abstract: The invention provides an installation for the production of hydrogen and/or carbon monoxide and/or a mixture of hydrogen and carbon monoxide, by separating a mixture to be processed (1) which contains at least carbon monoxide and hydrogen. Said installation comprises a production apparatus (9), for producing a feed mixture (3), a separating unit (BF), means for supplying the feed mixture to the separating unit, means for collecting hydrogen and/or carbon monoxide and/or a mixture of both products (7, 8), derived from the separating unit, means for drawing off at least one recycling gas (6) from the separating unit, means for returning said recycling gas upstream of the separating unit, for separating said gas simultaneously with the feed mixture from the production apparatus and means for modifying the rate and composition of said feed mixture, by modifying the operation of the production apparatus, according to the rate and composition of said at least one recycling gas.

Abstract: Systems and methods are disclosed for a gas production system to efficiently maintain a pressure of a gaseous output stream within a tight pressure range when the system changes normal operation to backup operation. In one preferred embodiment, during normal operation a backup vaporizer is kept in cold standby by directing a small portion of a liquefied gas stream away from the main heat exchanger to the backup vaporizer. In this way, the backup vaporizer is able to respond immediately to a shutdown of the main gas production system. During normal operation, the output of the backup vaporizer is recombined with the gaseous output stream to any avoid loss of product thereby increasing efficiency.

Abstract: Systems and methods are disclosed for the power efficient production of high-pressure gaseous oxygen product. In a preferred embodiment, a liquid oxygen stream is pumped to a low to medium pressure and warmed within a first heat exchanger such as a brazed aluminum plate fin heat exchanger. The liquid oxygen stream is then pumped to a further pressure and then vaporized in a second heat exchanger to produce a high-pressure gaseous oxygen stream. In an embodiment, a high-pressure air stream may be utilized in the second heat exchanger for vaporizing the oxygen stream and cooling the air stream. The air stream may be utilized as a feed for the cryogenic air unit. A portion of the air stream at a medium pressure may be utilized in the first heat exchanger. A portion of the air stream may also be expanded to recover energy.

Abstract: Systems and methods are disclosed for the power efficient production of high-pressure gaseous oxygen product. In a preferred embodiment, a liquid oxygen stream is pumped to a low to medium pressure and warmed within a first heat exchanger such as a brazed aluminum plate fin heat exchanger. The liquid oxygen stream is then pumped to a further pressure and then vaporized in a second heat exchanger to produce a high-pressure gaseous oxygen stream. In an embodiment, a high-pressure air stream may be utilized in the second heat exchanger for vaporizing the oxygen stream and cooling the air stream. The air stream may be utilized as a feed for the cryogenic air unit. A portion of the air stream at a medium pressure may be utilized in the first heat exchanger. A portion of the air stream may also be expanded to recover energy.

Abstract: A mixture containing oxygen is introduced into a distillation column (1); an intermediate stream, substantially free from impurities heavier than oxygen, is withdrawn (at 17) at a level of the column located above the point (4) of introduction of the air, the point (22) of withdrawal being separated from this point (4) of introduction by a distillation section (6), particularly with packing; the stream withdrawn (at 17) is sent to an oxygen purification column (2), and a reflux liquid is distributed over the section (6) by a distributor (9). A predetermined non-uniformity of the distribution of the reflux liquid over the upper surface (8) of the section (6) is effected in at least one localized region (23) of this surface.

Abstract: A mixture containing oxygen is introduced into a distillation column (1); an intermediate stream, substantially free from impurities heavier than oxygen, is withdrawn (at 17) at a level of the column located above the point (4) of introduction of the air, the point (22) of withdrawal being separated from this point (4) of introduction by a distillation section (6), particularly with packing; the stream withdrawn (at 17) is sent to an oxygen purification column (2), and a reflux liquid is distributed over said section (6) by means of a distributor (9).