# US 2014/0190348 A1 · Product gas concentrator utilizing vacuum swing adsorption and method associated therewith > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 2014/0190348 A1 - Document ID: US20140190348A1 - Status: Published application - Kind: A1 - Application number: 13/790,473 - Filed: 2013-03-08 - Published: 2014-07-10 - Earliest claimed: 2013-01-09 - Assignees: Invacare Corporation - Applicants: Invacare Corporation - Inventors: Joseph B. Richey, II; William J. Daniels - Web page: https://patentgrep.com/patent/US20140190348A1 ## CPC - B01D 53/0476: {Vacuum pressure swing adsorption} - B01D 53/0423: {Beds in columns} - B01D 53/053: with storage or buffer vessel - B01D 2256/12: Oxygen - B01D 2257/102: Nitrogen - B01D 2259/40007: Controlling pressure or temperature swing adsorption - B01D 2259/40009: using sensors or gas analysers - B01D 2259/402: using two beds - B01D 2259/4533: for medical purposes - Y02C 20/40: of CO2 - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - Y02C: CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG] ## Abstract Systems and methods associated with providing a concentrated product gas utilizing a vacuum swing adsorption process are provided. In one embodiment, the system includes first and second sieve beds, a scavenger pump, and a controller. In one embodiment, the method includes: separating one or more adsorbable components from a source gaseous mixture via first and second sieve beds in alternating and opposing filling and purging cycles of a vacuum swing adsorption process to form the concentrated product gas and pressurizing the concentrated gas for delivery to a user. Other embodiments include selectively controlling a variable restrictor based at least in part on a desired output setting to selectively provide flow between the first and second sieve beds such that the flow for at least one output setting is different from the flow for at least one other output setting in relation to corresponding filling cycles. ## Claims ### Claim 1 An apparatus for providing a concentrated product gas, comprising: first and second sieve beds arranged to separate one or more adsorbable components from a source gaseous mixture in alternating filling and purging cycles to form the concentrated product gas using a vacuum swing adsorption process; a first pump arranged to deliver the concentrated product gas formed by the first and second sieve beds; and a controller to control the alternating filling and purging cycles of the vacuum swing adsorption process. ### Claim 2 (depends on 1) The apparatus of claim 1, wherein the concentrated product gas formed by the first and second sieve beds is at an ambient or less than ambient pressure, and wherein the first pump provides the concentrated product gas at a pressure above the ambient pressure. ### Claim 3 (depends on 2) The apparatus of claim 2, wherein the first pump comprises: a first pump inlet; and a first pump outlet; wherein the first and second sieve beds include at least one sieve bed outlet; and wherein the concentrated product gas formed by the first and second sieve beds flows from the at least one sieve bed outlet to the first pump inlet and the concentrated product gas is provided from the first pump outlet. ### Claim 4 (depends on 2) The apparatus of claim 2, further comprising a first sensor to sense the pressure of the concentrated product gas provided by the first pump, wherein the controller further controls actuation of the first pump based at least in part on a first sensor output signal. ### Claim 5 (depends on 4) The apparatus of claim 4, wherein the controller turns off the first pump when the first sensor output signal reaches a first predetermined value and turns on the first pump when the first sensor output signal reaches a second predetermined value. ### Claim 6 (depends on 5) The apparatus of claim 5, wherein the first predetermined value is different than the second predetermined value. ### Claim 7 (depends on 1) The apparatus of claim 1, further comprising an accumulator to store the concentrated product gas at a pressure above an ambient pressure. ### Claim 8 (depends on 7) The apparatus of claim 7, further comprising a first pressure switch to sense an accumulator pressure, wherein the accumulator pressure is the pressure of the concentrated product gas stored in the accumulator, and wherein the first pressure switch controls actuation of the first pump based at least in part on the accumulator pressure. ### Claim 9 (depends on 1) The apparatus of claim 1, wherein the first pump is further arranged to draw exhaust gas from the first and second sieve beds during the alternating filling and purging cycles. ### Claim 10 (depends on 1) The apparatus of claim 1, further comprising a second pump arranged to draw exhaust gas from the first and second sieve beds during the alternating filling and purging cycles. ### Claim 11 (depends on 10) The apparatus of claim 10, further comprising a pump assembly, wherein the pump assembly comprises the first pump and the second pump. ### Claim 12 (depends on 1) The apparatus of claim 1, further comprising: an input device adapted to select a desired output setting for the concentrated product gas from a plurality of output settings; a valve assembly to selectively provide an adjustable flow between the first and second sieve beds; and wherein the controller is in operative communication with the input device and the valve assembly to selectively control the adjustable flow between the first and second sieve beds based at least in part on the desired output setting such that the flow between the first and second sieve beds for at least one output setting is different from the flow between the first and second sieve beds for at least one other output setting in relation to corresponding vacuum swing adsorption cycles. ### Claim 13 (depends on 12) The apparatus of claim 12, wherein the valve assembly comprises a pressure equalization valve to selectively provide a second adjustable flow between the first and second sieve tanks; and wherein the controller is in operative communication with the pressure equalization valve to selectively control the pressure equalization valve. ### Claim 14 (depends on 1) The apparatus of claim 1, wherein the controller is in operative communication with the first and second sieve beds to selectively control the alternating filling and purging cycles over a plurality of predetermined altitude ranges while maintaining an acceptable purity level for the concentrated product gas. ### Claim 15 (depends on 1) The apparatus of claim 1, further comprising: an input device adapted to select a desired output setting for the concentrated product gas from a plurality of output settings; a pressure sensor monitoring a pressure of the concentrated product gas; and a conserver valve comprising an output connection associated with a user, a vent connection associated with a vent port, and a gas connection associated with the concentrated product gas, wherein the output connection is switched from the vent connection to the gas connection and vice versa; and wherein the controller is in operative communication with the input device and the pressure sensor to selectively switch the conserver valve to selectively dispense the concentrated product gas based at least in part on the selected output setting and the monitored pressure. ### Claim 16 (depends on 15) The apparatus of claim 15, further comprising: a flow sensor monitoring a flow indicative of a breathing cycle for the user; wherein the controller is in operative communication with the flow sensor, determines a breathing characteristic of the user based at least in part on the monitored flow, and selectively switches the conserver valve based at least in part on the determined breathing characteristic. wherein the controller determines a start time for dispensing a bolus of concentrated product gas to the user via the output connection based at least in part on a relation between the determined breathing characteristic and a trigger threshold indicative of inhalation. ### Claim 17 (depends on 1) The apparatus of claim 1, further comprising at least one product tank to store the concentrated product gas at an ambient or less than ambient pressure. ### Claim 18 (depends on 1) The apparatus of claim 1, further comprising: a sieve bed and product tank assembly, comprising: the first sieve bed; and a product tank to store the concentrated product gas at an ambient or less than ambient pressure; and a sieve bed and accumulator assembly, comprising: the second sieve bed; and an accumulator to store the concentrated product gas at a pressure above an ambient pressure. ### Claim 19 An apparatus for providing a concentrated product gas, comprising: means for separating one or more adsorbable components from a source gaseous mixture in alternating filling and purging cycles to form the concentrated product gas using a vacuum swing adsorption process; means for pumping to deliver the concentrated product gas formed by the means for separating one or more adsorbable components from a source gaseous mixture; and means for controlling the alternating filling and purging cycles of the vacuum swing adsorption process. ### Claim 20 An method of providing a concentrated product gas, comprising: separating one or more adsorbable components from a source gaseous mixture in alternating filling and purging cycles to form the concentrated product gas using a vacuum swing adsorption process; and pumping the concentrated product gas formed by the vacuum swing adsorption process at a pressure above an ambient pressure.