The invention provides a method of treating waste comprising the steps of: providing an electrochemical cell comprising a cathode, and an anode; supplying a waste stream comprising an organic compound which is a liquid or dissolved in a solvent and contacting the anode and cathode with the waste stream; electrochemically oxidising the organic compound at the anode; supplying oxygen to the cathode; electrochemically reducing the oxygen at the cathode; wherein the cathode comprises a poison resistant oxygen reduction catalyst.

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.

According to one embodiment, a method for removing antimicrobial material from a composition includes providing a container that contains a plurality of carbon elements such as granules, rocks and sheets. The carbon elements are submerged with a liquid and a composition that includes an antimicrobial material is deposited in the container. The carbon elements are configured to remove the antimicrobial material from the composition. The level of the liquid in the container is monitored and controlled to maintain a submerged condition of the carbon elements.

The present invention relates to a continuous on-board drying method for Antarctic krill and a continuous on-board processing method of shelled Antarctic krill. The drying method includes the following steps: 1) subjecting fishing materials to cleaning, sorting, and dewatering with a vibrating screen, 2) rapidly heating the krill to the temperature of up to 70? C. using infra-red rays; 3) hot-air drying; 4) impurity removal by vacuum; 5) cooling to obtain dried krill. The processing method includes the following steps: a) subjecting fishing materials to cleaning, sorting, and dewatering with a vibrating screen; b) rapidly heating the krill to the temperature of up to 70? C. using infra-red rays; c) hot-air drying; d) subjecting the dried krill to shelling treatment to separate shell from meat, to obtain shelled krill; e) impurity removal by vacuum to obtain shelled krill product. The methods in the present invention are highly efficient, energy saving, green and environmental protection, and the krill products have high quality and safety.

The present invention relates to a continuous on-board drying method for Antarctic krill and a continuous on-board processing method of shelled Antarctic krill. The drying method includes the following steps: 1) subjecting fishing materials to cleaning, sorting, and dewatering with a vibrating screen; 2) rapidly heating the krill to the temperature of up to 70? C. using infra-red rays; 3) hot-air drying; 4) impurity removal by vacuum; 5) cooling to obtain dried krill. The processing method includes the following steps: a) subjecting fishing materials to cleaning, sorting, and dewatering with a vibrating screen; b) rapidly heating the krill to the temperature of up to 70? C. using infra-red rays; c) hot-air drying; d) subjecting the dried krill to shelling treatment to separate shell from meat, to obtain shelled krill; e) impurity removal by vacuum to obtain shelled krill product. The methods in the present invention are highly efficient, energy saving, green and environmental protection, and the krill products have high quality and safety.

The invention relates to methods and apparatuses for treating a condensate stream from a condenser that contains odorous compounds, such as various condensate streams produced in a rendering process. In one embodiment, the condensate stream is treated by adding an oxidizer to the liquid condensate stream to oxidize odor-causing compounds in the stream prior to being treated in a waste water pre-treatment system. In this manner, the odor resulting from these compounds can be reduced or eliminated.

An efficient and economical wastewater treatment system is disclosed. The wastewater treatment system may comprise a first sump for receiving wastewater to be treated. The first sump includes a ring that acts a first focal point to gather the waste and remove solids. Suspended solids are transported from the first sump, through one or more filters, and sent to a second sump. The second sump is preferably in communication with one or more protein skimmers. The second sump preferably includes one or more secondary focal points for gathering suspended solids to be further treated by the one or more protein skimmers. The second sump may include a partition wall that separates the second sump into a main tank and a gathering tank. One or more collecting chambers may be disposed in the gathering tank. Inlet conduits disposed within the main tank create a cross-flow or horizontal vortex that forces water to cascade over the partition wall into the one or more collecting chambers. Each collecting chamber preferably includes a suction line in communication with a protein skimmer. The suction line is positioned within the collecting chamber to divert and reverse the flow of water from the cascading flow over the partition wall to separate and retain suspended solids around the suction line to be transported to a protein skimmer. The first and secondary focal points advantageously do not use chemicals to gather the wastewater. The second sump may be in communication with a third sump, which may be in communication with one or more additional protein skimmers and an outlet pipe for sending treated water out the third sump. The resulting treated water has no smell and is potable. The wastewater treatment system is also significantly less costly in terms of start-up costs compared to conventional systems.

A system and method for cracking sludge, comprising first and second decant vessels for receiving and continuous processing, which decant vessels include an outlet for decanting selectively separated watery residue to a drain and cracked decanted SPN solids to a transport, with graduated heat matrix processing of the sludge at sensor-monitored temperature and dwell time for cracking the sludge, and a programmable controller responsive to temperature and level sensors for adjusting the heat media communicated through the heat matrix and for determining completion of a sludge cracking process, with a heat member providing pre-process agitation of the sludge as an influent filing the decant vessel and elevating the temperature to a pre-process temperature over ambient.

Processes, methods, and systems are disclosed for treatment and removal of peracetic acid (PAA), quaternary ammonia compounds (Quat), hydrogen peroxide, chlorine, chloramines, chlorinated organics, surfactants, and other such chemicals from wastewater pretreatment processes typically employed by livestock processing, meat processing, and/or food processing plants that generate wastewater outflows. Treatment and/or removal these chemicals commonly found in such wastewater allows the further treatment of the wastewater downstream by commonly employed biological wastewater treatment processes such as anaerobic, anoxic, or aerobic suspended growth activated sludge processes; anaerobic, anoxic, or aerobic fixed growth, IFAS, moving bed bioreactor (MBBR) or Membrane Bioreactor (MBR) processes; anaerobic lagoons; anaerobic fluidized bed or fixed bed processes; and/or, anaerobic sludge digestion processes commonly employed for biochemical oxygen demand (BOD) removal, ammonia removal, total nitrogen removal, and/or phosphorus removal.

An induced sludge bed anaerobic reactor includes a vessel in which a septum is positioned to maintain solids in wastewater being treated toward a lower portion of the reactor. The septum is configured to prevent or minimize rising bacteria from exiting the vessel and to minimize clogging of the vessel. A first example septum is disclosed that is based on a linear vane design. A second example septum is disclosed that is based on a concentric vane design. A third example septum is disclosed that is based on a radial vane design that may include one or more sections. Further, septums may be layered one atop another to further minimize rising bacteria from exiting the vessel and to further minimize clogging of the vessel. Finally, a septum is attached to the inside of the vessel so as to allow it to move allowing any clogging waste floating under the septum to exit the vessel.