An odor filter, preferably utilized on vents of human waste containers, provides a multi-stage construction having a variety of media calculated to remove specific gasses with acid and base impregnated filter media as well as potentially regular activated charcoal. The filter construction can be provided with a multi-diameter connection capability, at least one replacement indicator and/or a safety release to assist in at least one of under-pressure and/or overpressure situations.

Aspects of the present disclosure are directed to mixtures and methods for pneumatically conveying powdered materials. A method includes providing a pneumatic conveyance system with a gas stream having a gas velocity; providing particles of sorbent material having a median sorbent particle size d.sub.50, sorbent from 1 m to 28 m; injecting the particles of sorbent material into the gas stream; providing particles of erodant material having a median erodant particle size d.sub.50, erodant of at least 150 m, where the erodant material is provided in an amount from 0.5% to 3% by weight of the particles of sorbent material; and injecting the particles of erodant material into the gas stream, where the gas velocity is sufficient to entrain the particles of sorbent material and sufficient to convey the particles of erodant material. A mixture of sorbent material and erodant material is also disclosed.

To provide an aldehyde scavenger and a method for removing aldehydes by using the same, for quickly and continuously capturing aldehydes. An aldehyde scavenger comprising at least one O-substituted hydroxylamine or at least one chemically acceptable salt thereof, is used against an aldehyde generation source.

Production of lime (calcium oxide: CaO) from limestone (CaCO.sub.3) is one of the oldest natural chemical processes and this process is reversible, per FIG. 4 (CaCO.sub.3.fwdarw.CaO+CO.sub.2 under 500 to 600 C. heat). Subsequently when lime is exposed to the moving air; carbon dioxide (CO.sub.2) in the air will react with the lime and lime will convert back to limestone. By repeating same limestone to lime chemical process, lime and carbon dioxide (CO.sub.2) will be created. After separating and storing the carbon dioxide (CO.sub.2), process will be repeated continuously, using the same lime.

Disclosed herein is a method of regenerating a sorbent of gas in a capture process of said gas, wherein the capture process comprises recirculating the sorbent between a gas capturing system and regenerating reactor system, the method comprising the regenerating reactor system performing the steps of: receiving a solid sorbent to be regenerated, wherein the sorbent is a sorbent of carbon dioxide gas; generating heat by combusting a fuel with an oxidising agent in the presence of a catalyst; regenerating the sorbent by using the generated heat to indirectly heat the sorbent so that the sorbent releases carbon dioxide gas; outputting the regenerated sorbent; and outputting the released carbon dioxide gas. Advantages of the gas capture system include a higher efficiency than known techniques.

A process and a device for treating a flow of furnace gas with a pressure of more than 1 bar flowing through a channel. A powder agent, such as a powder comprising alkali reagents, such as lime, and/or absorbents, such as activated coal, is injected under an overpressure into the furnace gas flow via an injector which is positioned centrally within the channel. The powder agent may be fluidized. The pressure for injecting the powder may be adjusted by controlling the volume of fluidization gas vented via a venting outlet.

The invention includes systems, methods, compositions, and processes for designing, manufacturing, and utilizing carbon dioxide-sequestering substrates that can fully or partially replace natural sand in coastal engineering applications. These engineered substrates can offset demand for scarce native sand resources, while also effecting the conversion of gaseous carbon dioxide to dissolved or solid-phase products thereby offsetting impacts of anthropogenic climate change.

Disclosed herein is a method of regenerating a sorbent of gas in a capture process of said gas, wherein the capture process comprises recirculating the sorbent between a gas capturing system and regenerating reactor system, the method comprising the regenerating reactor system performing the steps of: receiving a solid sorbent to be regenerated, wherein the sorbent is a sorbent of carbon dioxide gas; generating heat by combusting a fuel with an oxidising agent in the presence of a catalyst; regenerating the sorbent by using the generated heat to indirectly heat the sorbent so that the sorbent releases carbon dioxide gas; outputting the regenerated sorbent; and outputting the released carbon dioxide gas. Advantages of the gas capture system include a higher efficiency than known techniques.

A contaminated gas stream can be passed through an in-line mixing device, positioned in a duct containing the contaminated gas stream, to form a turbulent contaminated gas stream. One or more of the following is true: (a) a width of the in-line mixing device is no more than about 75% of a width of the duct at the position of the in-line mixing device; (b) a height of the in-line mixing device is no more than about 75% of a height of the duct at the position of the in-line mixing device; and (c) a cross-sectional area of the mixing device normal to a direction of gas flow is no more than about 75% of a cross-sectional area of the duct at the position of the in-line mixing device. An additive can be introduced into the contaminated gas stream to cause the removal of the contaminant by a particulate control device.

A contaminated gas stream can be passed through an in-line mixing device, positioned in a duct containing the contaminated gas stream, to form a turbulent contaminated gas stream. One or more of the following is true: (a) a width of the in-line mixing device is no more than about 75% of a width of the duct at the position of the in-line mixing device; (b) a height of the in-line mixing device is no more than about 75% of a height of the duct at the position of the in-line mixing device; and (c) a cross-sectional area of the mixing device normal to a direction of gas flow is no more than about 75% of a cross-sectional area of the duct at the position of the in-line mixing device. An additive can be introduced into the contaminated gas stream to cause the removal of the contaminant by a particulate control device.