4 results about "Carbon dioxide scrubber" patented technology

A contaminant removal system for removing contaminants from an environment includes a water management system and a carbon dioxide removal system. The water management system is configured to remove water from a cabin air stream using a first liquid sorbent to produce a dehumidified cabin air stream, and includes a water scrubber and a water stripper. The carbon dioxide removal system is configured to remove carbon dioxide from the dehumidified cabin air stream using a second liquid sorbent, and includes a carbon dioxide scrubber and a carbon dioxide stripper.

A regenerable carbon dioxide scrubber includes at least a first housing compartment including an inlet, an outlet, and an interior region. A sorbent material is located within the interior region of the first housing compartment, in which the sorbent material (a) attracts and / or retains carbon dioxide from an air supply passing through the sorbent material at an operating temperature below about 100° C. and (b) releases carbon dioxide at a regenerating temperature above about 150° C. A rebreather including the regenerable carbon dioxide scrubber may be used to scrub carbon dioxide from a user's exhaled air.

The invention relates to a method for providing a hydrogen stream (7) in a facility (2) for providing the hydrogen stream (7), wherein a carbon-containing energy carrier stream (3) is fed to a syngas reactor assembly (4) in order to obtain a syngas stream (5) comprising hydrogen and carbon oxides, the syngas reactor assembly (4) obtains the syngas stream (5) from the energy carrier stream (3) by means of an autothermal reforming process, the syngas stream (5) is fed to a shifting apparatus (15a-c), a water-gas shift reaction taking place in the shifting apparatus (15a-c) in order to react at least part of the carbon monoxide of the syngas stream (5) with steam from the syngas stream (5) in order to form carbon dioxide and hydrogen, the syngas stream (5) is fed, downstream of the shifting apparatus (15a-c), to a carbon dioxide scrubber (30) in order to scrub at least part of the carbon dioxide from the syngas stream (5), a flash gas stream is released from a regeneration stage of the carbon dioxide scrubber (30), said flash gas stream being fed to a heating device of the facility (2) for an underfiring process, and the syngas stream (5) is at least partly fed, downstream of the carbon dioxide scrubber (30), to a separating assembly (6) in order to separate the syngas stream (5) at least into a hydrogen stream (7) comprising hydrogen and a carbon oxide-containing exhaust gas stream (8). The method is characterized in that, prior to being fed to the syngas reactor assembly (4), the energy carrier stream (3) is fed to a saturation stage (11), in which preheated condensate (12) accumulated in the facility (2) is fed to the energy carrier stream (3), and in that during the process of feeding the syngas stream to the shifting apparatus (15a-c), at least 80% of the steam fraction of the syngas stream (5) is already present as the syngas stream (5) exits the syngas reactor assembly (4). The invention likewise relates to a corresponding facility (2) for providing a hydrogen stream (7).

The ammonia production system comprises a syngas compressor upstream from the ammonia synthesis module includes an ammonia reactor. The ammonia reactor is fluidly coupled to the chiller which is in fluid communication with a carbon dioxide scrubber. The scrubber removes unreacted syngas. The unreacted syngas is recycled through a IGV controlled recycle compressor using a fixed speed driver. The delivery side of the recycle compressor is in fluid communication with the ammonia reactor. A portion of the recycle stream is delivery through an expander to the syngas make up compressor.