Method for generating O2-rich gas from air using water

Patent metadata

Field	Value
Publication number	US-9878280-B1
Application number	US-201514590239-A
Country	US
Kind code	B1
Filing date	Jan 6, 2015
Priority date	Jan 6, 2015
Publication date	Jan 30, 2018
Grant date	Jan 30, 2018

Abstract

The present disclosure is directed to a method for enriching an inlet air stream utilizing a number of enrichment sub-units connected in series, where each enrichment sub-unit conducts both a dissolution and degasification cycle. Each enrichment sub-unit comprises a compressor, an aeration unit, a deaeration unit, and a pump for the recirculation of water between the aeration and deaeration units. The methodology provides a manner in which the relationship between the respective Henry's coefficients of the oxygen and nitrogen in water may be exploited to enrich the O 2 volume percent and diminish the N 2 volume percent over repeated dissolution and degasification cycles. By utilizing a number of enrichment sub-units connected in series, the water contained in each enrichment sub-unit acts to progressively increase the O 2 volume percent. Additional enrichment sub-units may be added and utilized until the O 2 volume percent equals or exceeds a target O 2 volume percent. In a particular embodiment, air having a general composition of about 78 vol. % N 2 and 21 vol. % O 2 is progressively enriched to provide a final mixture of about 92% vol. % O 2 and 8% vol. % N 2 .

First claim

What is claimed is:

1. A process for enriching an inlet gas stream using water comprising:
identifying a target O 2 volume percent, where the target O 2 volume percent is at least 90% volume percent of O 2 ;
obtaining an enrichment sub-unit where the enrichment sub-unit comprises,
a compressor where the compressor comprises a compressor inlet and a compressor outlet,
an aeration unit containing water and comprising a gas inlet in fluid communication with the compressor outlet, where the aeration unit surrounds a volume of the water and surrounds an exhaust gas mixture, and where a first pressure acts on a surface of the volume of the water and where the volume of the water is at a first temperature, and where the aeration unit further comprises a water inlet and an aerated water outlet and an exhaust gas outlet, where the aerated water outlet is in fluid communication with the volume of the water, and where the exhaust gas outlet is in fluid communication with the exhaust gas mixture,
a deaeration unit in fluid communication with the aerated water outlet, where the deaeration unit comprises an enriched gas outlet and a deaerated water outlet and surrounds a deaeration volume in fluid communication with the enriched gas outlet, where the deaeration volume has a second pressure and a second temperature, where the second pressure is at least 30 atm less than the first pressure and where the second pressure is greater than the saturation pressure of water at the second temperature, where the first temperature of the volume of the water in the aeration unit is within 20° C. of the second temperature of the deaeration volume of the deaeration unit,
a pump comprising a pump suction and a pump discharge, where the pump suction is in fluid communication with the deaerated water outlet of the deaeration unit and the pump discharge is in fluid communication with the water inlet of the aeration unit;
producing a compressor discharge by receiving the inlet gas stream at an initial pressure at the compressor inlet, where the initial pressure is less than the first pressure, and where the inlet gas stream has an initial O 2 volume percent and an initial N 2 volume percent and comprises an initial O 2 quantity and an initial N 2 quantity, where the initial O 2 volume percent is a volume percent of O 2 in the inlet gas stream and the initial N 2 volume percent is a volume percent of N 2 in the inlet gas stream, where the initial O 2 volume percent is less than the target O 2 volume percent, and where the initial O 2 quantity is a mass of O 2 in the inlet gas stream and the initial N 2 quantity is a mass of N 2 in the inlet gas stream, and compressing the inlet gas stream with the compressor to generate a compressor discharge at the compressor outlet, thereby producing the compressor discharge;
producing an aerated water by directing some portion of the compressor discharge to the gas inlet of the aeration unit and injecting the some portion of the compressor discharge into the aeration unit and generating contact between the some portion of the compressor discharge and some portion of the water of the aeration unit, and generating a dissolved oxygen and a dissolved nitrogen in the water of the aeration unit, where the dissolved oxygen is a portion of the initial O 2 quantity dissolved in the water of the aeration unit and where the dissolved nitrogen is a portion of the initial N 2 quantity dissolved in the water of the aeration unit, and generating the aerated water, where the aerated water is a solution comprising the dissolved oxygen and the dissolved nitrogen as solutes and the water of the aeration unit as a solvent, and allowing at least another portion of the initial N 2 quantity to enter the exhaust gaseous mixture, and separating the exhaust gaseous mixture and the aerated water in the aeration unit such that the exhaust gaseous mixture is in fluid communication with the exhaust gas outlet and the aerated water is in fluid communication with the aerated water outlet, and discharging some portion of the exhaust gaseous mixture through the exhaust gas outlet, thereby producing the aerated water;
producing a deaerated water and an enriched gaseous mixture by discharging a quantity of the aerated water from the aerated water outlet of the aeration unit and directing the quantity of the aerated water to the deaeration volume of the deaeration unit, and allowing some portion of the dissolved oxygen and some portion of the dissolved nitrogen to transfer from the quantity of the aerated water at the second pressure and generate the enriched gaseous mixture and the deaerated water in the degasification vessel, where the enriched gaseous mixture comprises a degassed O 2 and a degassed N 2 and where the deaerated water comprises some portion of the aerated water less the degassed O 2 and the degassed N 2 , and separating the enriched gaseous mixture and the deaerated water in the deaeration unit such that the enriched gaseous mixture is in fluid communication with the enriched gas outlet of the deaeration unit and the deaerated water is in fluid communication with the deaerated water outlet of the deaeration unit, thereby producing the deaerated water and the enriched gaseous mixture;
producing an outlet gas stream by discharging the enriched gaseous mixture from the enriched gas outlet of the deaeration unit, where the outlet gas stream has a final O 2 volume percent and a final N 2 volume percent, where the final O 2 volume percent is a volume percent of O 2 in the outlet gas stream and the final N 2 volume percent is a volume percent of the N 2 in the outlet gas stream, and where the final O 2 volume percent is greater than the initial O 2 volume percent and the final N 2 volume percent is less than the initial N 2 volume percent, thereby producing the outlet gas stream;
producing a replenished water by drawing the deaerated water through the deaerated water outlet of the deaeration unit into the pump inlet and pumping the deaerated water through the pump outlet and through the water inlet and adding the replenished water to the water of the aeration unit using the pump, thereby producing the replenished water;
continuing to conduct the producing the compressor discharge step, the producing the aerated water step, the producing the deaerated water and the enriched gaseous mixture step, the producing the outlet gas mixture step, and the producing the replenished water step by utilizing some portion of the replenished water as the some portion of the water of the naeration unit;
adding an additional enrichment sub-unit comprising an additional compressor, an additional aeration unit, an additional deaeration unit, and an additional pump, and repeating the producing the compressor discharge step, the producing the aerated water step, the producing the deaerated water and the enriched gaseous mixture step, the producing the outlet gas stream step, the producing the replenished water step, and the continuing to conduct step, by using the additional compressor of the additional enrichment sub-unit for the compressor of the enrichment sub-unit, and by using the additional aeration unit of the additional enrichment sub-unit for the aeration unit of the enrichment sub-unit, and by using the additional deaeration unit of the additional enrichment sub-unit for the deaeration unit of the enrichment sub-unit, and by using the additional pump of the additional enrichment sub-unit for the pump of the enrichment sub-unit, and by using the outlet gas stream as the inlet gas stream, and generating an additional outlet gas stream at an additional gas outlet of the additional deaeration unit;
repeating the adding step until the additional outlet gas stream has the final O 2 volume percent greater than or equal to the target O 2 volume percent, thereby enriching the inlet air stream using water.

Assignees

• Nakano Anna
• Nakano Jinichiro
• Bennett James P
• Us Dept Energy

Inventors

• Nakano Anna
• Nakano Jinichiro
• Bennett James P

Classifications

• B01D53/1406 Primary

  Multiple stage absorption · CPC title

• B01D2257/40

  Nitrogen compounds · CPC title

• B01D53/1418

  Recovery of products · CPC title

• B01D53/14

  by absorption · CPC title

• B01F3/04

  Operations & Transport · mapped topic