Portable carbon dioxide absorption system

Abstract

Various embodiments of a portable carbon dioxide (CO2) absorption device that may remove excess CO2 from a closed environment are disclosed herein. The absorption device is reusable and configured for many environments.

Claims

1. A portable carbon dioxide absorption machine comprising: a housing defining an inlet and an outlet; a blower in fluid communication with the outlet and with a manifold system the blower being disposed within the housing, wherein the blower pulls air from the manifold system into the housing, and pushes the air from the housing through the outlet; the manifold system comprising a manifold housing defining an expansion chamber; the expansion chamber disposed within the housing, wherein the expansion chamber filters and reduces a velocity of air pulled by the blower; a carbon dioxide absorbing device disposed within the housing, the carbon dioxide absorbing device in fluid communication with the inlet and the manifold system, wherein the carbon dioxide absorbing device absorbs carbon dioxide from the air entering the inlet; and a power supply disposed within the housing, wherein the power supply is in electrical communication with the blower.

2. The portable carbon dioxide absorption machine of claim 1, wherein the blower generates a negative pressure to draw air external to the housing through the carbon dioxide absorbing machine and the manifold system.

3. The portable carbon dioxide absorption machine of claim 1, wherein the inlet of the housing has an inlet width greater than an outlet width of the outlet of the housing.

4. The portable carbon dioxide absorption machine of claim 1, wherein an exterior opening of the outlet comprises at least one of a screen coupled to an inner diameter of the exterior opening of the outlet, a mesh coupled to the inner diameter of the exterior opening of the outlet, or a plurality of holes defined by the housing.

5. The portable carbon dioxide absorption machine of claim 1, wherein the carbon dioxide absorbing device comprises a carbon dioxide absorbing material that absorbs the carbon dioxide from the air entering the inlet.

6. The portable carbon dioxide absorption machine of claim 1, wherein the carbon dioxide absorbing device is configured to be removed and replaced from the housing.

7. The portable carbon dioxide absorption machine of claim 1, wherein the carbon dioxide absorbing device houses a carbon dioxide absorbent in a removable canister cartridge.

8. The portable carbon dioxide absorption machine of claim 1, wherein the carbon dioxide absorbing device houses a carbon dioxide absorbent in a refillable canister.

9. The portable carbon dioxide absorption machine of claim 1, wherein the manifold system is configured to include a plurality of baffles.

10. The portable carbon dioxide absorption machine of claim 1, wherein the manifold system is configured to include cyclonic separation.

11. The portable carbon dioxide absorption machine of claim 1, further comprising: a sensor disposed within or proximal to at least one of the inlet, the outlet, the housing, the blower, the manifold system, or the carbon dioxide absorbing device, where the sensor monitors an environmental concentration of CO2 proximal to the sensor.

12. The portable carbon dioxide absorption machine of claim 1, wherein the portable carbon dioxide absorption machine is operable to be operated remotely.

13. The portable carbon dioxide absorption machine of claim 1, further comprising a vented covering engaged to an exterior opening of the outlet and the inlet.

14. A method for automatically reducing a concentration of carbon dioxide (CO.sub.2) in an enclosed environment using a portable carbon dioxide absorption machine, the method comprising: providing a portable carbon dioxide absorption machine in an enclosed environment, the portable carbon dioxide absorption machine comprising: an housing defining an inlet and an outlet, a blower in fluid communication with the outlet and with a manifold system, the blower being disposed within the housing, wherein the blower pulls air from the manifold system, and pushes air from the housing through the outlet, the manifold system comprising a manifold housing defining an expansion chamber, the expansion chamber, disposed within the housing, wherein the expansion chamber filters and reduces a velocity of air pulled by the blower, and a carbon dioxide absorbing device disposed within the housing, the carbon dioxide absorbing device in fluid communication with the inlet and the manifold system, wherein the carbon dioxide absorbing device absorbs carbon dioxide from the air entering the inlet; continuously measuring an environmental concentration level of CO.sub.2 in the enclosed environment using a sensor in communication with a control system of the portable carbon dioxide absorption machine; determining, at the control system if the environmental concentration level of CO.sub.2exceeds a predetermined threshold; continuously or intermittently operating the blower of the portable carbon dioxide absorption machine to draw the air into the portable carbon dioxide absorption machine such that the concentration of CO.sub.2 emitted from the portable carbon dioxide absorption machine is less than the environmental concentration level of CO.sub.2; and ceasing operation of the blower when the environmental concentration level of CO.sub.2 falls below the predetermined threshold.

15. The method of claim 14, further comprising: filtering the air entering the portable carbon dioxide absorption machine to capture and remove dust or other particulates from the enclosed environment.

16. The method of claim 14, further comprising: setting the predetermined threshold based upon a measurement of a volume of the enclosed environment and an anticipated increase in concentration levels of CO.sub.2 within the enclosed environment.

17. The method of claim 14, wherein operation of the blower is ceased automatically.

18. A method of manufacturing a portable carbon dioxide absorption machine comprising: providing a housing including an inlet and an outlet; disposing a blower within the housing such that the blower is in fluid communication with the outlet and with a manifold system, wherein the blower pulls air from the manifold system and pushes air from the housing through the outlet; configuring the manifold system to comprise a manifold housing defining an expansion chamber, wherein the expansion chamber is disposed within the housing and filters the air and reduces a velocity of the air pulled in by the blower; disposing a carbon dioxide absorbing device within the housing, the carbon dioxide absorbing device in fluid communication with the inlet and the manifold system, wherein the carbon dioxide absorbing device absorbs carbon dioxide from the air entering the inlet; and disposing a power supply within the housing, wherein the power supply is in electrical communication with the blower.

19. The method of claim 18, further comprising configuring an exterior opening of the outlet to comprise at least one of a screen coupled to an inner diameter of the exterior opening of the outlet, a mesh coupled to the inner diameter of the exterior opening of the outlet, or a plurality of holes defined by the housing.

20. The method of claim 18, further comprising disposing within the carbon dioxide absorbing device a carbon dioxide absorbing material that absorbs the carbon dioxide from the air entering the inlet.

Description

BRIEF DESCRIPTION OF FIGURES

(1) The application file contains at least one photograph executed in color. Copies of this patent application publication with color photographs will be provided by the Office upon request and payment of the necessary fee.

(2) FIG. 1 is a front perspective view of a portable carbon dioxide absorption system with portions of the exterior housing removed according to one embodiment.

(3) FIG. 2 is a rear perspective view of a portable carbon dioxide absorption system with portions of the exterior housing removed according to one embodiment.

(4) FIG. 3 is a rear elevation view of a portable carbon dioxide absorption system with portions of the exterior housing removed according to one embodiment.

(5) FIG. 4 is a side elevation view of a portable carbon dioxide absorption system with portions of the exterior housing removed according to one embodiment.

(6) FIG. 5 is a top plan view of a portable carbon dioxide absorption system according to one embodiment.

(7) FIG. 6 is a front elevation view of a portable carbon dioxide absorption system with portions of the exterior housing removed according to one embodiment.

(8) FIG. 7 is a front perspective view of a portable carbon dioxide absorption system with the exterior housing in place according to one embodiment.

(9) FIG. 8 is a front perspective view of a portable carbon dioxide absorption system with the exterior housing in place according to one embodiment.

(10) FIGS. 9-14 are various views of an internal component assembly of a portable carbon dioxide absorption system according to various embodiments.

(11) FIG. 15 is a schematic drawing of a control system and power system according to one embodiment.

(12) FIGS. 16, 17A and 17B are example schematics of a controller and control circuit, respectively.

(13) FIGS. 18-31 are photographs of another embodiment of the portable carbon dioxide absorption system according to another embodiment.

(14) FIG. 32 is a graph showing CO.sub.2 absorption levels over time with the portable carbon dioxide absorption system operating in various states, of according to one embodiment.

(15) FIG. 33 is a table showing CO.sub.2 absorption levels over time with the portable carbon dioxide absorption system operating in various states, of according to one embodiment.

(16) Any dimensions in the figures are merely for example and do not necessarily limit the size of the devices depicted.

DETAILED DESCRIPTION

(17) The present disclosure relates to a lightweight and portable carbon dioxide absorbing system for removing or scrubbing carbon dioxide gas from the air. The system may be configured for a wide variety of environments. For example, the carbon dioxide absorbing system may maintain or reduce CO.sub.2 levels in airplanes before, during, and after flight.

(18) The United States Federal Aviation Administration (FAA) classifies dry ice as a hazardous material. The FAA has published guidelines for determining dry ice capacities in aircraft. Per the FAA Advisory Circular, 91-76A, Hazard Associated with Sublimation of Solid Carbon Dioxide (dry Ice) Aboard Aircraft, the exposure to CO.sub.2 in the aircraft should not exceed 0.5% CO.sub.2 by volume (v/v). Sublimed CO.sub.2 is colorless and odorless and at high concentrations in a confined/small/limited/enclosed space, such as an airplane, can cause aircrew incapacitation.

(19) Gaseous CO.sub.2 produced from the sublimation of dry ice or produced from other sources is also regulated. The FAA notes that sublimed solid CO.sub.2 produces excess CO.sub.2 gas and this may be dangerous in confined spaces where there is no ventilation or ventilation rates are low. This condition is exacerbated during airplane engine starts and de-icing of the airplane where the power packs or electrical infrastructure is shut down and all ventilation and air exchange is stopped.

(20) The sublimation rate depends on environmental conditions such as temperature and pressure, the physical properties of the dry ice such as surface area, and the quality of the packaging such as insulated versus non-insulated materials. The FAA has developed a standard formula to provide a rule of thumb for dry ice loading; the product of the desired CO.sub.2 concentration, 0.5% v/v, the total volume of the aircraft and the complete number of air exchanges per hour proportional to two standard sublimation rates: 1% per hour and 2% per hour. Therefore, for a sublimation rate, when the number of air exchanges is doubled, then the permissible capacity for transported volumes of dry ice also doubles. Conversely, if the air exchanges are reduced relative to a determined sublimation rate, then the permissible capacity of dry ice that can be transported is also reduced by half.

(21) In various aspects, modern aircraft may recycle as much as 50% of cabin-ventilated air, instead of providing 100% fresh air exchange. This reduction in volume of complete air exchanges per hour therefore leads to a reduction in permissible dry ice shipping capacities. As a reduced dry ice capacity would affect the volume and timeline for the transport of perishable items, food, medicine, and/or biological materials, a means to maintain safe CO.sub.2 levels is needed.

(22) The Portable Carbon Dioxide Absorption Machine (PCDAM) of the present disclosure is well suited to reduce or maintain CO.sub.2 levels in confined environments. As CO.sub.2 gas is denser than air, the CO.sub.2 gas displaces air and remains low to the floor or ground. The PCDAM can be conveniently and easily placed in the cockpit and supernumerary and operated even when the plane is powered down, without the airplane's power packs or network, to maintain safe CO.sub.2 concentration levels. The PCDAM can be turned on during de-icing and engine starting events where it will maintain a safe environment for the aircrew, reduce the number of delayed shipments, and increase the overall air transport dry ice capacity where employed.

(23) The PCDAM may also be scaled up or down or reconfigured to fit a variety of spaces and environments. For example, besides freighter or cargo airplanes, the PCDAM may also be used in food processing environments, where carbon dioxide is a food additive, a propellant, acidity regulator, leavening agent, or used to remove caffeine. Similarly, the PCDAM may be used in beverage manufacturing facilities and breweries where CO.sub.2 is used to carbonate soft drinks, aid in fermentation, and to rapidly cool grapes to prevent spontaneous fermentation prior to processing. The PCDAM is also suitable for many other industrial applications. These include, but are not limited to, facilities where welding, metal working and construction are performed, as CO.sub.2 gas is a shielding gas for welding or a pressurized propellant for portable pneumatic tools. These industrial applications also include any facility with a fire suppression system, as these typically include large amounts of liquid and gas carbon dioxide at various pressures. After a fire, it is desirable to remove the dense carbon dioxide gas to aid in rescue and recovery. The PCDAM may also be used in a biological facilities, slaughterhouses, and laboratories where high rates of photosynthesis or bacterial and waste decomposition generate volumes of CO.sub.2.

(24) In commercial refrigeration applications, a carbon dioxide based refrigerant may be used, while in oil extraction operations, carbon dioxide gas may be injected into wells at high pressures. Both applications involve large volumes of CO.sub.2 that may adversely affect operators if a leak or other accident occurs. Similarly, large volumes of CO.sub.2 are used or produced in cement production, foundries, and power plants, all of which benefit from controlling levels of CO.sub.2 in the local environment.

(25) In general, the PCDAM has a small portable configuration. By way of example and not limitation, the PCDAM may be lightweight (approximately less than 18 kg or 40 lb.) and compact (approximately the size of a carry-on suitcase). In one example, the PCDAM 10 may be approximately 14 inches wide9 inches deep24 inches tall.

(26) In various embodiments, The Portable Carbon Dioxide Absorption Machine (PCDAM) 10, as shown in FIGS. 1-8, includes one or more blower/fans 100, one or more CO.sub.2 absorbing devices 200, a manifold 300, a power system 400, a control system 500, a fluid conduit arrangement 600, and a housing 700. Embodiments of the one or more blower/fans 100, the one or more CO.sub.2 absorbing devices 200, the manifold 300, and the fluid conduit arrangement 600 as assembled are shown without the housing in FIGS. 9-14.

(27) The blower/fan 100 is an air-moving device capable of flow rates in the range of 20-60 cubic feet per minute, according to one embodiment. The blower includes an inlet that is in fluid communication with the CO.sub.2 devices 200 and the manifold 300 via the fluid conduit system 600. According to one embodiment, when in operation, the blower/fan 100 generates a positive pressure to push air, generally indicated by air flow 800 in FIG. 2, through the manifold 300 and out through the CO.sub.2 devices 200. Alternately, in other embodiments, the blower/fan 100 generates a negative pressure to draw air, indicated by airflow 900, in through the CO.sub.2 devices 200, through the manifold 300, and out of the housing 700.

(28) During operation, the air in the local environment is recycled at approximately 20-50 cubic feet per minute. The PCDAM 10 may reduce the level of CO.sub.2 by 0.05-0.15% (v/v) per minute or to acceptable levels. In other embodiments, the PCDAM device operates at a maximum flow rate for maximum CO.sub.2 absorption. Alternatively, the PCDAM may operate to provide a gradual or metered reduction in CO.sub.2 concentration. In this embodiment, the PCDAM may continuously monitor the environment and maintain a specific CO.sub.2 concentration by varying the flow rate of air through the absorbing devices. By way of example, the flow rate may be varied via a potentiometer or similar component.

(29) In various embodiments, the blower/fan 100 has a blower configuration wherein air is counter-currently pushed by a blower/fan by a wheel (not shown) driven by a fully enclosed brushless motor that is suitable for dirty, dusty and/or damp environments. In various other embodiments, the blower/fan 100 has a fan configuration wherein a propeller pushes air out of the blower/fan.

(30) In operation, the PCDAM reduced CO.sub.2 levels using a variety of means. In one embodiment, the PCDAM 10 includes one or more CO.sub.2 absorbing devices 200 configured to permit air to drawn in through an inlet portion 120 and an outlet portion 210. The outlet portion 210 generally has a width greater than that of the inlet portion 120 to decrease the velocity of air leaving the absorbing device 200; this ensures laminar flow, consistent rates of reaction and low buoyancy to prevent the release of dust, dirt, or particulates to the surrounding environment. In various embodiments, the outlet portion 210 includes a screen, mesh, or multiple openings 230, as shown in FIG. 5 and FIG. 22, to permit the release of air, while preventing undesired objects from entering or leaving the devices. The outlet portion 210 may be positioned generally opposite the inlet 120 and contain a CO.sub.2 absorbing material in such a configuration to maximize airflow therethrough.

(31) For example, the CO.sub.2 absorbing device 200 may incorporate a solid CO.sub.2 absorbing material 240. For example, the CO.sub.2 absorbent 240 may include one or more derivatives of ammonia (i.e., an amine such as monoethanolamine, among others). In other embodiments, the CO.sub.2 absorbent 240 may be composed of one or more minerals. The mineral or minerals are typically provided in powder form, while in other embodiments, forms of the mineral material may be provided. These include, but are not limited to solid, semi-solid, or liquid compositions. Typically, the minerals are chemically configured as oxides, so the CO.sub.2 reacts with the minerals to form carbonate. Preferably, the absorbent material 240 is suitable for disposal with general waste and not subject to hazardous waste procedures.

(32) One advantage of the PCDAM 10 is the interchangeability of the CO.sub.2 absorbing devices 200. After a period of operation, each CO.sub.2 absorbing device 200 may be removed and replaced to provide continual reduction of CO.sub.2 levels in the environment. In one embodiment, The CO.sub.2 absorbent devices house the absorbent 240 in convenient canister cartridges for practical and quick replacement of the media. In other embodiments, the absorbing device 200 may use refillable canisters.

(33) After air entering the PCDAM flows through the blower/fan 100, the airflow enters a filtering manifold system 300 where it is expanded and thus filtered to capture dust or other particulates prior to flowing through the CO.sub.2 absorbing devices 200, preventing this potential matter from being emitted to the surrounding environment through the outlet portion 210. In one aspect, the positive pressure generated by the blower/fan 100 draws environmental air into the manifold system 300 and then through the CO.sub.2 absorbing devices 200. As shown in FIGS. 6 and 11-12, the manifold system 300 includes a manifold housing 310 that defines an expansion chamber 320 having an expanded control volume sufficient to momentarily reduce the velocity of air traversing the manifold 300 system. In other embodiments, the manifold system 300 may be configured to use baffles or cyclonic separation. Residual dust from CO.sub.2 absorbent 240, any other foreign particulates, and/or moisture produced from the absorption of CO.sub.2 in the CO.sub.2 absorbing device 200, are collected within the manifold chamber 320. In one embodiment, the manifold system 300 functions similar to a vacuum trap, and separates the blower/fan 100 input portion 110 of the fluid conduit system 600 from the manifold inlet side 320 of the fluid conduit system, thus protecting the blower/fan 100 and the external environment 20. In another embodiment, the manifold system 300 functions similar to a dropout box, flash evaporator or expansion chamber, and separates the blower/fan 100 input portion 120 of the fluid conduit system 600 from the manifold inlet side 320 of the fluid conduit system.

(34) As shown in several figures, the air drawn in to the PCDAM 10 is directed through the components of the system by the fluid conduit system 600. The conduit system 600 includes plurality of fluid transporting conduits to permit controlled fluid communication between the external environment 20, the fan/blower 100, the CO.sub.2 absorbing devices 200, and the manifold device 300. In various embodiments, the fluid conduit system 600 may be constructed of any suitable material including but not limited to poly (vinyl chloride) (PVC) piping or tubing. In various embodiments, any other suitable materials may be used. To increase the lifespan of the PCDAM, it is desirable to use non-corrosive or non-reactive materials for the fluid conduit system, including the bushings, joints, or other fittings. By way of example, the conduit system may include flexible or rigid conduits composed of polypropylene, polycarbonate, polyethylene, fiberglass, chlorinated polyvinyl chloride (CPVC), polypipe, aluminum, copper, galvanized metal, rubber, butyl, nitrile rubber (e.g., buna-n), buna-s, silicone, neoprene, urethane, ethylene propylene diene monomer (EPDM) rubber, fluoroelastomer, or combinations thereof.

(35) As shown in FIGS. 3, 6, 15, 16, 17A and 17B, the PCDAM 10 is powered by a power system 400 and controlled by a control system 500. In various embodiments, the power system 400 includes a battery 410, which may be rechargeable according to at least one embodiment. In one embodiment, the battery may be charged off the plane and loaded prior to flight with a battery life of over 4 hours of continuous run time. In other embodiments, the battery may be charged by any external power supply. For example, the power system 400 may include an internal charger that charges the battery using any suitable external power supply, including those available on the plane. It has been observed that a critical time for CO.sub.2 sublimation without proper ventilation is during de-icing or engine start events where the ventilation systems are shut down and closed off to the outside. The battery 410 may be secured to the housing, as shown in FIGS. 23-25.

(36) In other embodiments, the PCDAM 10 is powered by direct wiring to an external power supply or plugged into an outlet of an external power system, generally indicated as 430, as shown in FIGS. 20-21. Yet in other embodiments, a combination of a battery and external power supply may provide extended use in remote locations. For example, the PCDAM 10 may operate at maximum performance level when engaged to an external power source, such as an alternating current (AC) power source, when the battery is depleted or charging.

(37) In various embodiments, the control system 500, as shown in FIGS. 3, 6, and 15, 16, 17A and 17B, includes one or more processors or controllers 510 mounted on a printed circuit board 520. The control system may include other components including, but not limited to, relays 530, terminals 540, converters 545, switches 550, and control modules 560. As shown in various embodiments, the control system is in electrical communication with both the battery 410 and an external power system 420. The control system may also include sensors to monitor CO.sub.2 levels in the environmental air, alarms, displays, audio/visual indicators, generally indicated as 580, or combinations thereof, that allow a user to observe operation of the PCDAM 10, including the charging status of the battery 410. By way of example and not limitation, a schematic for one embodiment of a controller 510 is shown in FIG. 16, while FIGS. 17A and 17B illustrate an example circuit diagram of a control system circuit 570. The controllers and circuits shown in FIGS. 16, 17A and 17B are provided as illustrative examples only and do not limit the scope of the systems and components used to power and control the PCDAM 10.

(38) According to various embodiments, the PCDAM 10 may operate in a continuous operation mode to provide continual CO.sub.2 monitoring and absorption. Alternatively, the control system 500 may operate the PCDAM in an intermittent mode where the environmental CO.sub.2 levels are monitored and the blower/fan 100 is activated when a threshold value for CO.sub.2 concentration has been reached and the PCDAM automatically operates to reduce the CO.sub.2 level. In yet another configuration, the PCDAM 10 may be operated remotely as desired.

(39) The housing 700 is typically a rigid structure that protects the internal components of the PCDAM 10. By way of example and not limitation, the housing 700 may be composed primarily of aluminum. As shown in FIGS. 2 and 5, among others, the top surface of the housing includes one or more apertures 720 aligned with each of the CO.sub.2 absorption devices 200. In one aspect, the housing 700 functions as a faraday cage to intrinsically shield the interior components from static electric fields and certain types of harmful electromagnetic pulses for reliable and safe use in hospitals, laboratories, airplanes, and military applications where sensitive electronics may be present. As shown in FIGS. 1 and 2, among others, the housing 700 may include one or more support structures 705 and one or more access panels 710 or vents 715 to permit access to the interior of the housing. Similarly, the housing may include several openings 720 where the exhaust portion 210 and the inlet portions 120 of the absorbing devices 200 are in fluid communication with the environment external to the housing 700, as shown in FIGS. 5 and 22. In one aspect, the outlet portions 210 and inlet portion 120 may protrude from the housing 700. In other embodiments, the outlet portions 210 and inlet portion 120 may be flush with the exterior surface of the housing 700 or remain below the exterior surface of the housing. For example, when the outlet portions 210 and inlet portion 120 are recessed below the exterior surface, the openings 720 may remain separate and distinct or they may be configured as a single contiguous opening. Regardless of opening configuration, when the outlet portions 210 and inlet portion 120 are recessed below the exterior surface, the openings 720 may optionally have a protective screen or other vented covering.

(40) In various other embodiments, the openings 720 and corresponding fan inlet portion 120 and absorbing device outlet port(s) 210 are not proximal to one another, nor are they limited to the top surface of the housing 700. For example, the openings 720 and corresponding fan inlet port(s) 120 and absorbing device outlet portions 210 may be positioned on any other portion of the housing, including but not limited to the front, back, sides, and bottom portions (when the device is elevated or not resting on a solid surface).

(41) Various embodiments of the PCDAM 10 may be used to perform to various processes and methods for automatically reduce CO.sub.2 concentrations and maintain suitable CO.sub.2 concentrations in an enclosed environment. By way of example, after placing the PCDAM 10 in the enclosed environment, the environmental concentration level of CO.sub.2 in the enclosed environment may be continuously measured using a sensor in communication with the control system 500 of the PCDAM. Based upon the measured data, the processor 510 of the control system 500 determines if the environmental concentration level of CO.sub.2 exceeds a predetermined threshold. In one aspect, the threshold is determined at least in part on the volume of the enclosed area and the anticipated increase in CO.sub.2. While monitoring the environmental CO.sub.2 levels, the processor 510 continuously or intermittently operates the blower 100 to draw environmental air into the PCDAM 10. As previously described, the PCDAM 10 absorbed CO.sub.2 from air travelling through the device, thus the concentration of CO.sub.2 in the air emitted from the PCDAM 10 is less than the environmental concentration level, thereby reducing the environmental concentration level. Lastly, once the environmental CO.sub.2 level is below the threshold, the controller 510 automatically reduces or ceases operation of the blower 100.

(42) FIGS. 32 and 33 display experimental performance data for an embodiment of the PCDAM 10. In one experiment, an isolated controlled space or control volume (e.g. a room) was filled with carbon dioxide (CO.sub.2) gas at a constant rate of 7.4 liters per minute. The experiment was conducted in two parts, both under the same conditions. In the first part, a control experiment was conducted where the PCDAM off, and in the second part the PCDAM was in operation. A calibrated CO.sub.2 Data logger was used in the first part of the experiment to record real-time concentrations of CO.sub.2, recorded as % volume/volume (v/v). Similarly, Drager Pac 7000 CO.sub.2 gas monitor was used in the second part of the experiment to record real-time concentrations of CO.sub.2, as % volume/volume (v/v). The Drager Pac 7000 CO.sub.2 gas monitor was worn by a person, disposed in a seated position within the room to provide an accurate simulation.

(43) As shown in FIG. 32, the line 1000 indicated as the % CO.sub.2 Alpha 1 level, illustrates the 0.5% CO.sub.2 (5,000 parts of CO.sub.2 per million parts of air) gas (v/v) concentration exposure limit used by the Department of Labor (DOL) and Occupational Safety and Health Administration (OSHA) as an 8-hour time weighted average Permissible Exposure Limit (PEL) in general industries. In one embodiment, the PCDAM 10 operates in an automated mode for continuous atmosphere monitoring where the PCDAM automatically initiates and stops absorption at a specific concentration or a specific threshold. This threshold data an instructions to operates the PCDAM 10 may be stored in memory and executed by a processor of a computing device. By way of example and not limitation the threshold may correspond to the DOL and OSHA PEL. Similarly, data related to the volume or absorbency of the CO.sub.2 absorption material 240 may be stored in memory such that an alarm or other indicator is triggered when the absorbent material is at 10%, 5% or requires immediate replacement.

(44) The elevated line 1002, indicated as % CO.sub.2 with Machine Off-Part 1 represents the increase or rate of volumetric growth of % CO.sub.2 gas (v/v) concentration in the room while filling the room at a rate of approximately 7.4 liters of CO.sub.2 per minute for approximately 89 minutes with the PCDAM 10 turned off. It can be deduced from the data shown that the concentration of CO.sub.2 in the room quickly climbs to approximately 5% CO.sub.2 gas (v/v) level in the first 71 minutes. Conversely, the line 1004, indicated as Drager Pac 7000 ReadingsPart 2, illustrates the actual readings taken in the room with the PCDAM on, while the room is filled with carbon dioxide (CO.sub.2) gas at a constant rate of 7.4 liters of CO.sub.2 per minute (similar to part 1). As shown, the PCDAM 10 held the % CO.sub.2 gas (v/v) concentration level to 0.0% CO.sub.2 gas (v/v) under these conditions for the first 71 minutes (11:29 am-12:40 pm) and below the PEL for a full 75 minutes (11:29 am-12:44 pm).

(45) As shown, the PCDAM 10 kept the room under the alpha 1 PEL of 0.5% CO.sub.2 gas (v/v) for the first 75 minutes. It can be extrapolated that approximately 530 total liters of CO.sub.2 gas or over 7 liters of CO.sub.2 gas/per minute was absorbed over this 75 minute period to achieve this control.

(46) While the present disclosure has been described referring to various embodiments, it will be understood that these embodiments are illustrative and that the scope of the disclosure is not limited to them. Many variations, modifications, additions, and improvements are possible. More generally, embodiments in accordance with the present disclosure have been described in the context of particular implementations. Functionality may be separated or combined through components differently in various embodiments of the disclosure or described with different terminology. These and other variations, modifications, additions, and improvements may fall within the scope of the disclosure as defined in the claims that follow.

(47) It is believed that the present disclosure and many of its attendant advantages will be understood by the foregoing description, and it will be apparent that various changes may be made in the form, construction, and arrangement of the components without departing from the disclosed subject matter or without sacrificing all of its material advantages. The form described is merely explanatory, and the following claims intend to encompass and include such changes.