Wastewater leaching chambers and leaching channels are disclosed. The chambers may include a recess for receiving a wastewater supply, the recess serving to lower the overall height of the combined chamber and supply. The recess also configured to tightly seat the supply and form a gap therebetween. Leaching channels having a high aspect ratio may also be coupled to or otherwise in fluid communication with the chamber.

A biomass-derived protein compound has a high concentration of protein and can be made to have a very low concentration of fat and water; even when the biomass feedstock has a high fat concentration. The biomass-derived protein compound may be a whole protein that is non-denatured and enzymatically digestible. This unique protein compound can be produced from molecules from more than one source organism, including various animals and/or plant feedstocks. The unique protein compound is derived from a unique biomass method and apparatus for the treatment of a biomass stream to extract and separate an essentially solvent-free product from the biomass stream. In this unique method the solids content of the biomass stream is increased by bringing the biomass stream into contact with a moderately pressurized liquefied gas solvent, to create a high solids content biomass stream and introducing the high solids content biomass stream to an extraction apparatus.

The subject of this invention is to use beneficial reactive support media or biofilms in the form of reactive support bases or stratums that provide structural (including dimensions) or biochemical benefits to the growth or function (including agglutination) of biofilms. The functional aspect includes the provision of reactivity to a polymeric, cellulosic or silicic framework. The functions are supplied to the structural media during manufacture, conditioning, regeneration or during colonization of biofilms. The structural support media may include biodegradable or refractory polymers/plastics, alginates or uronic acids or extracted bacterial EPS. These materials are reacted, retained or removed based on their physical characteristics.

The present disclosure provides an exemplary process for a system that may remove particulate from industrial water fluids using a Particulate Removal System (PRS). In some aspects, this system may treat water pulled from different Industrial Fluid Systems (IFS) while doing continuous monitoring and quality tests of the water. In some embodiments, the system may use sensors and other technology to allow for the system to periodically self-clean itself allowing for maximum efficiency and accuracy while also cleaning the water from the IFS. In some implementations, the water from the IFS may be filtered through a Particulate Trap Mechanism (PTM) to ensure that particulate including dissolved material has been removed from the water and separated from possible contamination throughout the system. In some aspects the system may be used for continuous and direct measurement of water quality and automatic chemical level adjustment by systems to maintain a desired range or setpoints.

The invention relates to a process for recovering ammonia from an initial aqueous mixture comprising ammonium ions and ammonium salts, the process comprising providing an initial aqueous mixture, desorbing ammonia using humid, heated air to obtain a desorbing liquid phase and a desorbing gas phase, separating the desorbing liquid phase, mixing the desorbing gas phase with a capture gas to obtain a gas mixture, and condensing the gas mixture to obtain a condensate comprising ammonium ions and salt, and an outlet gas. The desorbing liquid phase comprises ammonium ions and ammonium salts in a total concentration of less than 100 ppm. The capture gas comprises carbon dioxide in an amount of at least 50,000 ppm. The total concentration of ammonium ions and ammonium salts in the condensate is higher than the total concentration in the initial aqueous mixture. The invention further relates to a system for performing an ammonium recovery process, a composting system, a composting process and a system for composting and recovering ammonia.

According to one embodiment, a container for removing antimicrobials from an antimicrobial composition includes a container body having an exterior and an interior. The interior is at least partially filled with carbon granules configured to remove a portion of the antimicrobials in the antimicrobial composition. The interior is further filled with a liquid to at least a level that completely submerges each of the carbon granules. The container further includes an agitator configured to agitate at least a portion of the carbon granules. The container further includes a drain and a drainage valve. The location of the drainage valve is configured to prevent the drainage valve from lowering a current level of the liquid below the level that completely submerges each of the carbon granules.

According to one embodiment, a container for removing antimicrobials from an antimicrobial composition includes a container body having an exterior and an interior. The interior is at least partially filled with carbon granules configured to remove a portion of the antimicrobials in the antimicrobial composition. The interior is further filled with a liquid to at least a level that completely submerges each of the carbon granules. The container further includes an agitator configured to agitate at least a portion of the carbon granules. The container further includes a drain and a drainage valve. The location of the drainage valve is configured to prevent the drainage valve from lowering a current level of the liquid below the level that completely submerges each of the carbon granules.

This invention provides a cleaning and biocidal composition containing stabilized active bromine for treating hard surfaces contaminated with proteinaceous and fatty residues.

An anaerobic digestion system is provided that includes a blend tank operable to control and perform pre-treatment of feedstock. An anaerobic digester is operable to digest the feedstock provided from the blend tank in a totally enclosed oxygen-free environment within a specific temperature range. A bio-mass tank processes liquid digestate from the anaerobic digester. One or more baffles are positioned in the digester, with the one or more baffles providing for plug flow through at least a portion of the digester to create baffled zones that are at least partially operable independently of adjacent baffled zones. A bio-mass tank processes liquid digestate from the anaerobic digester. An energy source is coupled to the anaerobic digester.

A bioprocess comprises regulating pH of trade effluent wastewater, adding and mixing a first bio-additive, adding and mixing a flocculant/coagulant, filtering through a filter device, adding, mixing of a second bio-additive with aeration, and adding and mixing of a third bio-additive with aeration. Treatment can be discontinued or continued by adding and mixing of hydrogen peroxide with aeration, and optionally exposing treated effluent to UV disinfectant. The treated effluent can be recycled or disposed. Compositions of bio-additives 1, 2 and 3 comprise a group of highly selective and effective microorganisms and enzymes that are immobilized on carrier support matrices from a group of alginate, chitosan, polyacrylamides, k-carrageenan and agarose.