A sorbent for capture of ethylene gas includes an amorphous precipitated silica material having a BET surface area of at least 200 m.sup.2/g and an organic compound in the form of an amine, an imine or an amide bound to a surface of the amorphous precipitated silica material. The organic compound is configured for chemisorption of ethylene. An ethylene gas filtration system for a refrigerator includes an ethylene gas filter including the sorbent and a fan. The ethylene gas filter is mounted in conjunction with the fan such that gas is actively circulated through the ethylene gas filter by means of the fan. The organic compound may be triisopropanolamine, polyethylenimine or polyamide.

An organic matter decomposition catalyst that contains a perovskite type complex oxide represented by A.sub.xB.sub.yM.sub.zO.sub.w, wherein A contains 90 at % or more of at least one element selected from the group consisting of Ba and Sr, B contains 80 at % or more of Zr, M is at least one element selected from the group consisting of Mn, Co, Ni, and Fe, y+z=1, x>1, z<0.4, and w is a positive value that satisfies electrical neutrality.

A system and process for the recovery of at least one halogenated hydrocarbon from a gas stream. The recovery includes adsorption by exposing the gas stream to an adsorbent with a lattice structure having pore diameters with an average pore opening of between about 5 and about 50 angstroms. The adsorbent is then regenerated by exposing the adsorbent to a purge gas under conditions which efficiently desorb the at least one adsorbed halogenated hydrocarbon from the adsorbent. The at least one halogenated hydrocarbon (and impurities or reaction products) can be condensed from the purge gas and subjected to fractional distillation to provide a recovered halogenated hydrocarbon.

A weatherization system for a wellhead methane emission reduction system is described. The weatherization system reduces green-house gas emission into the atmosphere and reduces the effects of weather on the methane emission reduction system. The weatherization system includes a stack assembly connected to a housing of the reduction system by a housing adapter. The stack assembly includes a stack adapter and a stack cover, which collectively helps protect the methane emission reduction system and prevents weather or atmospheric factors from entering the housing. The weatherization system may include one or more sensors for measuring the effects of weather or degradation of at least one of the weatherization system and the methane emission reduction system.

Axial-radial flow reactor comprising a catalytic bed (1) of a hollow cylindrical shape, having a vertical axis (2), a base (5), a radial gas inlet section (3b), an axial gas inlet section (6) and a radial gas outlet section (4b), wherein the catalytic bed (1) comprises: a first cylindrical annular region (10) containing a layer of a first catalyst (A) and a layer of a second catalyst (B), the layer of the first catalyst being above the layer of the second catalyst; a second cylindrical annular region (9) coaxial to the first annular region and containing only the first catalyst (A).

A reclaiming method is disclosed including conducting evaporation by introducing a part of the absorbent to recover CO.sub.2 or H.sub.2S in a gas in a closed system recovery unit and separating a degraded substance contained in the absorbent from the absorbent to be introduced into an evaporator and obtain recovery steam containing an absorbent and CO.sub.2 or H.sub.2S by a heating section that is provided on a circulation line that circulates in the evaporator; and removing ionic degraded substance by cooling the concentrate obtained in the evaporation and removing an ionic degraded substance in the concentrate after the cooling, wherein a purified concentrate from which the ionic degraded substance has been removed is reused as a purified absorbent.

A device for the destruction of biohazardous converts harmful waste products into environmentally friendly discharge in compliance with environmental protection agency (EPA) standards. The device includes a waste disposal chamber where a crucible resides. The crucible contains a basket for holding the waste which is heated through induction coils that surround the crucible. The waste is vaporized and ionized in a vacuum forming a waste gas and drawn through a catalytic converter and a hot plasma jet via vacuum suction. The waste gas is then exhausted via a discharge duct where is it condensed by a heat exchanger further refining the waste gas into environmentally friendly molecules such as carbon dioxide. The waste destruction device further includes a programmable logic controller and user interface to control the device. Once the waste destruction process is completed, a compressor passes compressed air over the crucible to rapidly cool the crucible,

The EFEM comprises: a transfer chamber in which a transfer robot is disposed, a first fan that forms a downward air flow in the transfer chamber, a gas return space that circulates the gas flowing downward in the transfer chamber above the first fan, a box that communicates with the transfer chamber and is provided with a gas outlet, and a connecting and disconnecting means configured to switch connection and disconnection of the box to and from the transport chamber. A circulation path in which gas circulates is formed by the transfer chamber, the gas return space, and the box. When the transfer chamber and the box are separated by the connecting and disconnecting means, a shortened circulation path is formed in which the gas circulates without passing through the box.

An evaporative emission control canister system comprises an initial adsorbent volume having an effective incremental adsorption capacity at 25 C. of greater than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane, and at least one subsequent adsorbent volume having an effective incremental adsorption capacity at 25 C. of less than 35 grams n-butane/L between vapor concentration of 5 vol % and 50 vol % n-butane, an effective butane working capacity (BWC) of less than 3 g/dL, and a g-total BWC of between 2 grams and 6 grams. The evaporative emission control canister system has a two-day diurnal breathing loss (DBL) emissions of no more than 20 mg at no more than 210 liters of purge applied after the 40 g/hr butane loading step.

Disclosed are methods and systems for removing submicron particles from a gas stream, in particular from urea prilling off-gas, wherein a Venturi ejector is used. A method comprises contacting a gas stream containing submicron particles in a Venturi ejector with an injected high velocity scrubbing liquid to provide a pumping action, wherein the scrubbing liquid has an initial velocity of at least 25 m/s and wherein the ratio of scrubbing liquid and gas flow is between 0.0005 and 0.0015 (m.sup.3/h)/(m.sup.3/h).