A method of capturing CO.sub.2 and converting the captured CO.sub.2 into useful byproducts includes providing a material including a material matrix holding an ionic liquid, exposing the material to a source of thermal energy to capture CO.sub.2 within the material, removing the material from exposure to the source of thermal energy, and washing the material with a solution to convert the captured CO.sub.2 and wash the converted, captured CO.sub.2 from the material as filtrate. Materials and systems for capturing CO.sub.2 and converting the captured CO.sub.2 into useful byproducts are also provided.

An industrial air pollution removal system that eliminates unwanted gases from the environment includes a four-step process. The first step is an investigatory process to gather all the properties of the stack as flow rate, gas types, and hottest point of the stack. A second step captures either through water in the vat phase or sublimation of carbon dioxide and mercury into slabs of dry ice. In the byproducts, internal uses can be found to defray costs. A third step is the transportation of vat phase by truck and dry ice in refrigerated truck. A fourth step is the fractionalization center will recycle the captured emissions, such as separation of particulate matter, distillation for the liquid, sublimation of the dry ice and mercury, and using a dry ice processing plant. The goal is the sale of recycled materials as raw materials, conserve natural resources, and to positively affect climate change.

A system for directly capturing and measuring greenhouse gasses from a mixture of gasses over a wide range of concentrations from ambient air to combustion exhaust products including: an emissions capture reaction vessel; a reaction media container configured to house a volume of reaction media, the reaction media configured to extract a constituent gas from gas flowing through the emissions capture reaction vessel and capture constituent gas; an intake and exhaust manifold configured to receive and release, respectively a portion of a gas stream via a first access tap on the exhaust stack; a computer system comprised of sensors and actuators connected to a network to directly measure efficiency and uptake of a system, and a fan arranged within the housing and configured to influence the amount and speed of the gas stream processed.

A gas processing furnace according to the present invention includes: a hollow cylindrical furnace body including a gas processing space therein; a non-transferred plasma jet torch for supplying a plasma jet into the gas processing space; and an electric heater for heating a region of the gas processing space to which the plasma jet is supplied.

A gas combustion treatment device that subjects an ammonia-containing gas, a hydrogen cyanide-containing gas, and a hydrogen sulfide-containing gas to combustion treatment includes: a first combustion unit configured to introduce therein fuel, the ammonia-containing gas, the hydrogen cyanide-containing gas, and air and burn and reduce the fuel and the gases at an air ratio lower than 1; a second combustion unit provided downstream of the first combustion unit and configured to burn and reduce, in a reducing atmosphere, nitrogen oxide in a first combustion gas sent from the first combustion unit; and a third combustion unit provided downstream of the second combustion unit and configured to introduce therein hydrogen sulfide-containing gas with air in addition to a second combustion gas sent from the second combustion unit.

A particle detecting module includes a main body, a particle monitoring base, an actuator, a heater and a sensor. The main body has a first and a second compartment. The main body has an inlet, a hot gas exhausting opening and an outlet. The inlet and the hot gas exhausting opening are in fluid communication with the first compartment. The outlet is in fluid communication with the second compartment. A communicating opening is communicated with the first and the second compartment. The particle monitoring base is disposed between the first compartment and the supporting partition plate. The first compartment is heated to maintain a monitor standard level of humidity in the first compartment. The sensor is disposed adjacent to the supporting partition plate and located in a monitoring channel of the particle monitoring base, thereby monitoring the gas. The particle detecting module can be applied to a slim portable device.

A fluid delivery system for an exhaust aftertreatment system includes a pump disposed within an outer housing. A filter assembly is in fluid communication with the pump and also disposed within the outer housing. A tubular filter medium is disposed within a pump housing. An elongated first compensation element is disposed within an elongated aperture of the filter medium. A support ring is associated with the pump housing and includes a plurality of flexible arms. Second and third compensation elements are also provided to contract in response to expansion of fluid within the pump housing due to freezing and expand in response to thawing of the fluid.

The present disclosure generally relates to systems and methods for the combustive abatement of waste gas formed during the manufacture of semiconductor wafers. In particular, the systems described herein are capable of combusting air-polluting perfluorocarbons, including those having high greenhouse gas indexes such as hexafluoroethane (C.sub.2F.sub.6) and tetrafluoromethane (CF.sub.4), as well as particulate-forming silicon dioxide precursors, such as silane (SiH.sub.4) and tetraethoxysilane (Si(OC.sub.2H.sub.5).sub.4, abbreviated TEOS), with greater efficiency and lower energy usage than prior abatement systems. More particularly, and in one preferred embodiment, the present disclosure is directed to a waste gas abatement system that utilizes a combination of non-combustible and combustible gases (or gas mixtures) for thermal combustion, which are directed through multiple permeable interior surfaces of a reaction chamber, efficiently combusting waste gas and preventing undesirable accumulation of solid particulate matter on the chamber surfaces.

A system for reducing the release of hydrocarbons emitted from a hydrocarbon source into the atmosphere includes a hydrocarbon supply conduit configured to receive the emitted hydrocarbons. In addition, the system includes an air supply conduit coupled to an air source. Further, the system includes a combustion device coupled to an outlet end of the hydrocarbon supply conduit and an outlet end of the air supply conduit. The combustion device is configured to receive the hydrocarbons from the hydrocarbon supply conduit and the air from the air supply conduit, and combust the hydrocarbons. Still further, the system includes a catalytic converter spaced apart from the combustion device and a transfer conduit extending from an outlet of the combustion device to an inlet of a catalytic converter. The catalytic converter is configured to receive the combustion products and any un-combusted hydrocarbons from the transfer conduit, and oxidize the un-combusted hydrocarbons.

A heating system for compressed parts capable of controlling process atmosphere and pressure includes an accommodating body, a heating device, an atmosphere controlling device, and a processing pressure adjusting device. The heating device is disposed inside or outside of the accommodating body to heat a component to be heated, so as to remove an impurity within the component to be heated. The atmosphere controlling device transports a reaction gas, such as hydrogen, oxygen, water vapor, or plasma, into a cavity for reacting with the impurity within the component to be heated. A phase transition or a chemical reaction can be carried out, such that the impurity is gasified, oxidized, carbonized, or disintegrated. The processing pressure adjusting device uses an inert gas (e.g., a nitrogen gas or an argon gas) to control the processing pressure in the cavity to be from 800 Torr to 10.sup.2 Torr.