Patent classifications
B01D53/0423
System and process for carbon dioxide removal of air of passenger cabins of vehicles
The present invention relates to systems and methods for controlling 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 dioxide 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.
Self-Supporting Structures Having Active Materials
A method and system for manufacturing and using a self-supporting structure in processing unit for adsorption or catalytic processes. The self-supporting structure has greater than 50% by weight of the active material in the self-supporting structure to provide a foam-geometry structure providing access to the active material. The self-supporting structures, which may be disposed in a processing unit, may be used in swing adsorption processes and other processes to enhance the recovery of hydrocarbons.
RECEIVER INTEGRATED WITH SEPARATOR
One or more techniques and/or systems are disclosed for an integrated, dual-chamber, gas separator-receiver. The integrated, dual-chamber, gas separator-receiver can comprise a first and second column, which is integrated, and plumbed together. A source gas can be input through an inlet in the first column, and a target gas, separated from the source gas, can be output through an outlet in the second column. The first column can contain agents that dry the source gas, and separate the target gas from the source gas. The source gas can then be fed into the second column, where it is stored under pressure, at least until needed by some target operation that utilizes the target gas.
Pretreatment equipment for hydrocarbon gas to be liquefied and shipping base equipment
Provided are a liquefaction pretreatment facility for a hydrocarbon gas and the like in which, an influence of contained hydrogen sulfide and oxygen on liquefaction pretreatment can be reduced. In a liquefaction pretreatment facility for a hydrocarbon gas, adsorption vessels are each connected to a treatment gas line configured to supply a hydrocarbon gas containing water, hydrogen sulfide, and oxygen and are each packed with synthetic zeolite for adsorbing and removing water in the hydrocarbon gas. A regeneration gas line is configured to supply a heated regeneration gas to the adsorption vessels to regenerate the synthetic zeolite having adsorbed water through heating. A temperature control system is configured to control a heating temperature of the regeneration gas so that a temperature in the adsorption vessel during regeneration of the synthetic zeolite is less than 230 C., which is a set temperature.
PRESSURE SWING ADSORPTION INTEGRATION IN STEAM CRACKING ETHYLENE PLANTS FOR IMPROVED HYDROGEN RECOVERY
A process is provided for increasing the recovery of high-purity hydrogen from a steam cracking process in situations where byproduct methane yield is high relative to hydrogen. After a hydrocarbon gas stream is sent through a cold box and demethanizer, a small proportion of methane is sent through a pressure swing adsorption unit separately from a gas stream that contains hydrogen to increase high-purity hydrogen recovery by about 6%.
ADSORPTION VESSELS HAVING REDUCED VOID VOLUME THROUGH THE USE OF NON-POROUS, LOW-DENSITY FILLER MATERIAL TO REDUCE VOIDS
Adsorption vessels and systems utilizing adsorption vessels are provided herein. In one embodiment, an adsorption vessel for receiving a fluid mixture and for separating a component from therein includes a vessel wall extending from a bottom end to a top end and defining a vessel chamber. A bottom inlet is formed in the bottom end of the adsorption vessel for introducing the fluid mixture to the vessel chamber. A filler material having a total porosity of less than about 25% and a density less than about 900 kg/m3 or an insert or both are positioned in the top void volume to increase overall performance of the adsorbent vessel.
Halocarbon recycling methods and systems
A method for capturing halocarbon from a gas, the method comprising processing gas containing halocarbon with material which is undamaged by exposure to supercritical fluid. A method for reclaiming halocarbon from a material, the method comprising exposing the material to a supercritical fluid. A module for processing a gas containing halocarbon, the module comprising material for capturing halocarbon from a gas, wherein the module is arranged to withstand supercritical fluid.
Swing adsorption processes using zeolite structures
The present disclosure describes the use of a specific adsorbent material in a rapid cycle swing adsorption to perform dehydration of a gaseous feed stream. The adsorbent material includes a zeolite 3A that is utilized in the dehydration process to enhance recovery of hydrocarbons.
Method to prepare a CO2 adsorbent and capture CO2
A CO.sub.2 adsorbent that includes MIL-100(Fe) and various amounts of carbon nanotubes that are dispersed therein, and a method of capturing CO.sub.2 with a CO.sub.2 adsorbent that includes an adsorbent matrix of a zeolite and/or a metal organic framework and carbon nanotubes that are dispersed within the adsorbent matrix. Various embodiments of the CO.sub.2 adsorbent and the method of capturing CO.sub.2 are also provided.
CO2 capture and storage method
A CO.sub.2 adsorbent that includes MIL-100(Fe) and various amounts of carbon nanotubes that are dispersed therein, and a method of capturing CO.sub.2 with a CO.sub.2 adsorbent that includes an adsorbent matrix of a zeolite and/or a metal organic framework and carbon nanotubes that are dispersed within the adsorbent matrix. Various embodiments of the CO.sub.2 adsorbent and the method of capturing CO.sub.2 are also provided.