B01D2259/40086

Filter Conditioning Unit For High-Volume Sampling Filters

Disclosed is a filter conditioning unit for cleaning and conditioning high-volume sampling (HVS) filters. The unit includes, among other elements, a filter tray suitable for holding one or more HVS filters, a manifold in which the filter tray is inserted, and an optional enclosure for safety. The manifold is suitable for heating the filter tray and filters therein to a desired temperature while purge gas is introduced to the manifold. Also described herein is a method of using the filter conditioning unit.

Method for controlling an adsorption dryer for the treatment of compressed gas

A method for controlling an adsorption dryer for the treatment of compressed gas includes vessels therein and a valve arrangement for selectively feeding upstream compressed gas to, and outputting dried downstream compressed gas from, the vessels. Compressed gas is fed to at least one of the vessels in a process phase for drying the compressed gas through liquid adsorption by the desiccant bed and removing the adsorbed liquid from the bed in the vessels in a regeneration phase. An ambient value occurring outside both the vessels and downstream compressed gas output is measured. Additional steps include determining a characteristic value based on the measured ambient value, matching the value to criteria associated with stored regeneration phase parameter settings, determining a regeneration phase parameter setting based on the matching of the value, and applying the parameter setting to the regeneration phase for setting a parameter of the regeneration phase.

SYSTEM AND PROCESS FOR CARBON DIOXIDE REMOVAL OF AIR OF PASSENGER CABINS OF VEHICLES

The present invention relates to systems and methods for conrolling the atmosphere in the cabin (1) of a vehicle. The system comprises a carbon dioxide removal conduit (2) comprising a regenerable carbon dioxide removal chamber (5,6) containing a carbon dioxide sorbent material and a regeneration circuit (7) arranged to expel the desorbed carbon diocide at a location exterior (8) of the cabin (1) The system is operable to maintain a carbon dioxide level below 1000 ppm in the passenger cabin for a period of at least 5 minutes while restricting the flow of air from outside the vehicle into the passenger cabin to 10 L/s or less.

HYDROGEN PURIFICATION
20220306469 · 2022-09-29 · ·

A plant and method for hydrogen purification are provided, which comprise a Swing Adsorption (SA) stage and a recycle of purged gaseous impurities.

Thermal insulation of a membrane module for mitigating evaporative fuel emissions of automobiles

A thermal insulation system for mitigating evaporative fuel emissions of an automobile may include a membrane component and a thermal component connected to the membrane component. The thermal component may be configured for condensing, in the membrane component or in the thermal component, fuel vapor generated from a fuel tank of an automobile.

Continuously Regenerable Scrubber
20220266189 · 2022-08-25 · ·

Regeneration of a fluid medium can be accomplished using a continuously regenerable scrubber, which, in its various embodiments, combines valve functions and sorbent material, such as amine beds, into one component, dramatically reducing size and mass of scrubber. Sorbent material beds rotate continuously past breathing gas vent loop ports for scrubbing CO.sub.2/H.sub.2O and then past vacuum ports for regenerating the sorbent material. Typically, a first fluid output is connected to a lower header fluid output and a second, sweeping fluid source connected to a lower header fluid input. A motor spins the substantially circular bed assembly at a predetermined speed which allows adsorption or absorption as well as desorption of materials flowing through the sorbent material.

Apparatus and System for Swing Adsorption Processes Related Thereto

Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit may provide access to the adsorbent material within the adsorbent bed unit without having to remove one or more of valves, conduits and manifolds.

MANUFACTURE AND REMANUFACTURE OF VOLATILE ANAESTHETIC AGENTS USING SUPERCRITICAL FLUIDS
20220233798 · 2022-07-28 ·

An anaesthetic halocarbon capture system is provided. The system includes a pressure-intolerant sleeve containing filter material for capturing one or more types of anaesthetic halocarbon prior to supercritical fluid extraction, and a pressure-tolerant housing into which the sleeve can be inserted so as to permit exposure of the sleeve contents to pressures required for supercritical fluid extraction.

Method and system for drying compressed air

Drying compressed air while utilizing a method for preemptive overload avoidance of moisture to a desiccant bed, including a recovery control process. The method may include a purge means, an initialization period for pre-learning to develop usage-profile log performance summary to compare against real-time data and a protocol for a normal state, a recovery state and a supplemental purge state and means to reestablish normal operations. A procedure for standby and overload alarm alerting states are also described. The purge means may be fixed rate or modulating. The system may have cycle times decrementing or incrementing stepwise in a predetermined or varying time frame to respond to on-going trending data in order to correct imbalance loading conditions by adjusting drying and regenerating cycle times, thus affording a stable delivery of quality dewpoint compressed air to the dryer output.

Carbon-negative combustion through the use of molecular transfer systems and disguisement of gas constituents
20210404380 · 2021-12-30 ·

Disclosed are methods, processes, systems, and compositions of matter that enable the transfer of targeted constituents from a dilute state to a final concentrated state. Exemplary dilute constituents are carbon dioxide or humidity as found in air or other gases; and exemplary final states, respectively, are purified carbon dioxide or condensed water. Such transfer from dilute sources is understood generally to require more energy consumption as the source phase becomes more dilute in the targeted constituent. The present invention shows how a different governing principle, i.e. reactive disguisement, is applied to create a concentrated final state without relying on heat flow or pressure swings to actively concentrate a targeted constituent. The primary field of invention is chemical separation.