The present disclosure relates to a purge system for a vapor compression system including an emission canister. The emission canister includes a load cell disposed in an interior of the emission canister, a base supported by the load cell, and an adsorbent material disposed on the base. The adsorbent material is configured to adsorb a refrigerant flowing through the emission canister, and the load cell is configured to monitor a weight of the adsorbent material and the refrigerant within the emission canister.

The present disclosure relates to a purge system for a vapor compression system including an emission canister having an adsorbent material disposed therein. The purge system also includes a heating system configured to transfer thermal energy to the adsorbent material, where the heating system includes a first heating element and a second heating element disposed within the emission canister and extending along a central axis of the emission canister. The first heating element and the second heating element are configured to distribute the thermal energy transferred to the adsorbent material disposed within the emission canister to release refrigerant from the adsorbent material.

Sorbent compositions, comprising a solid sorbent, a dispersive agent, and optionally a capture agent for enhanced wet-Flue Gas Desulfurization (wFGD) or wet scrubber unit function in a flue gas pollutant control stream is disclosed. The sorbent composition may include a sorbent with a dispersive agent, designed to enhance the dispersion of the sorbent in an aqueous sorption liquid of a wet scrubber unit, and therefore may be especially useful in EGU or industrial boiler flue gas streams that include one or more wet scrubber units. The sorbent composition may also include a capture agent useful in sequestering mercury and bromine, as well as other contaminants that may include arsenic, selenium and nitrates.

An apparatus and method for purifying a raw hydrogen gas stream of chloramines and chlorine is provided. The explosive chloramines compounds can be effectively captured by the carbon adsorbent without accumulating on the carbon surface. Rather, the chloramines are converted via decomposition, into non-explosive products with catalytic effect of the carbon material. Chlorine reacts with impregnated reducing agent on the carbon surface to form the solid products, which can be adsorbed on the carbon surface. The purified hydrogen gas contains little to no trace of chloramines and chlorine impurities, thereby making the hydrogen gas suitable for liquid hydrogen production.

Zeolite catalysts and systems and methods for preparing and using zeolite catalysts having the CHA crystal structure are disclosed. The catalysts can be used to remove nitrogen oxides from a gaseous medium across a broad temperature range and exhibit hydrothermal stable at high reaction temperatures. The zeolite catalysts include a zeolite carrier having a silica to alumina ratio from about 15:1 to about 256:1 and a copper to alumina ratio from about 0.25:1 to about 1:1.

The exhaust gas rectifier has an exhaust gas deflector disposed at an upstream side with respect to a urea water injection device in a direction in which exhaust gas flows. The exhaust gas deflector includes a plurality of individual regions which have an opening part through which the exhaust gas passes. The plurality of the individual regions are arranged in one direction. The opening ratio in the plurality of the individual regions is different in one direction.

Extractive agent compounds are disclosed, with exemplary compounds having Formula (I): ##STR00001##
wherein R.sup.a and R.sup.b are independently selected from the group consisting of an oxygen radical, a hydrogen radical, and a hydrocarbyl radical having from about 1 to about 20 carbon atoms, and wherein R.sup.2-R.sup.6 are independently selected from the group consisting of halo, a hydrogen radical, and a hydrocarbyl radical having from about 1 to about 20 carbon atoms, and further wherein at least two of R.sup.2-R.sup.6 are halo. Also disclosed are extractive distillation processes, comprising distilling a liquid mixture comprising ethylbenzene, a further C.sub.8 aromatic compound, and an extractive agent compound as described herein. The extractive agent contributes to improved separability of ethylbenzene from the further C.sub.8 aromatic compound. The separability may be quantified in terms of increasing relative volatility of ethylbenzene to the further C.sub.8 aromatic compound or may alternatively be quantified in terms of a competitive factor, D, as described herein.

Process for conditioning a container including a granular material A enabling the adsorption of the nitrogen contained in a feed gas stream, including a step of injecting, into the container, a gas or a gas mixture G such that the adsorption capacity of the material A with respect to G is less than 10 Ncm.sup.3/g at 25 C. and 1 atm.

A novel integrated filter device for the concurrent capture, filtration or separation of particle, chemicals, vapors and or/gasses from liquid or solid flows. The device has a filtration macrostructure substrate and a thin film coating over the macrostructure substrate which allows for compact and efficient capture, filtration and separations. Device may serve as a platform for chemical reactions. The device minimized problems associated with traditional filters, chemical sorbents or reactors and provided for enhanced collection and analysis of target materials. The methodology for construction also allows for modular assembly in various arrangements including a stacked configuration. The devices may be used collaboratively and cooperatively with other collection and separation technologies.

A method of adsorption allows separation of a first fluid component from a fluid mixture comprising at least the first fluid component in an adsorptive separation system having a parallel passage adsorbent contactor with parallel flow passages having cell walls which include an adsorbent material. The method provides for transferring heat from the heat of adsorption in a countercurrent direction along at least a portion of the contactor during adsorption and transferring heat in either axial direction along the contactor and/or a direction transverse to the axial direction, to provide at least a portion of the heat of desorption during a desorption step. A carbon dioxide separation process to separate carbon dioxide from flue gas also includes steps transferring heat from adsorption or for desorption along the parallel passage adsorbent contactor.