Patent classifications
C05F1/02
MICROWAVE HEATING APPLIED TO ANIMAL-BASED PRODUCTS
A system for processing animal-based material is disclosed that includes at least one microwave generator, at least one microwave guide operatively connecting the at least one microwave generator to at least a first conveyor unit. The first conveyor unit is provided in a first housing that includes at least one opening configured to receive microwave energy via a first microwave guide and the first conveyor unit is configured to receive and process a quantity of animal-based material, which includes heating the animal-based material to a first temperature by applying microwave energy to the animal-based material within the first housing.
MICROWAVE HEATING APPLIED TO ANIMAL-BASED PRODUCTS
A system for processing animal-based material is disclosed that includes at least one microwave generator, at least one microwave guide operatively connecting the at least one microwave generator to at least a first conveyor unit. The first conveyor unit is provided in a first housing that includes at least one opening configured to receive microwave energy via a first microwave guide and the first conveyor unit is configured to receive and process a quantity of animal-based material, which includes heating the animal-based material to a first temperature by applying microwave energy to the animal-based material within the first housing.
System for resource recovery from poultry processing wastewater
A system for recovering fat, oil and grease (FOG) from wastewater has multiple annular flotation zones in a concentric configuration surrounding a central column to create progressively increasing surface areas for FOG and solid particles flotation. Each flotation zone may be equipped with an independent pressurized micro air and/or ozone bubbles distribution system. The FOG is recovered in the first flotation zone without chemical additions. Coagulant and flocculant may be added in the second flotation zone to maximize removals of biochemical oxygen demand (BOD), total suspended solids (TSS), and colloidal particulates and produce clear effluent. Magnesium chloride is added in the third flotation zone to remove phosphorus and to form struvite particulates that can be used as fertilizer. Since both organic loading and solid loading in the treated effluent are significantly reduced, poultry processing plants can more easily meet wastewater treatment plant discharge limits and avoid surcharges.
Integrated waste conversion system and method
An entirely water-based, energy self-sufficient, integrated in-line waste management system is provided for comprehensive conversion of all organic fractions of municipal and wider community waste to fuels suitable for use in transportation, with all solid residues converted to high nutrition compost. The system is based on a combination of pre-treatment, involving alkaline hydrolysis and saponification; three-way separation of the pre-treated waste into different streams that are each directed to suitable further processing including fuel production; which includes biodiesel generation in a continuous-flow catalytic esterification unit, and anaerobic digestion to produce methane or other small molecule biofuel. Remaining solids are converted to compost in a quasi-continuous process.
Integrated waste conversion system and method
An entirely water-based, energy self-sufficient, integrated in-line waste management system is provided for comprehensive conversion of all organic fractions of municipal and wider community waste to fuels suitable for use in transportation, with all solid residues converted to high nutrition compost. The system is based on a combination of pre-treatment, involving alkaline hydrolysis and saponification; three-way separation of the pre-treated waste into different streams that are each directed to suitable further processing including fuel production; which includes biodiesel generation in a continuous-flow catalytic esterification unit, and anaerobic digestion to produce methane or other small molecule biofuel. Remaining solids are converted to compost in a quasi-continuous process.
LIVESTOCK CARCASS TREATMENT SYSTEM USING ULTRA-HIGH TEMPERATURE MICROORGANISMS
The present invention relates to a carcass treatment system 1. Such a carcass treatment system 1 ferments and decomposes carcasses by hyperthermophile of 85 to 110° C. and aerobic conditions, and comprises a mobile fermentation process unit 3 for transferring to an onset site of disease and treating the livestock carcass by hyperthermophile; or a burial fermentation process unit 5 for excavating a burial site 6 near the outbreak site of disease and treating the livestock carcass by hyperthermophile; a base treatment unit 7 for secondarily processing the livestock carcass treated primarily by the mobile fermentation process unit 3 or the burial fermentation process unit 5 with hyperthermophile, wherein the primary treatment is performed by treating with hyperthermophile at fermentation temperature of 85 to 110° C. for 8-15 days to decompose flesh of the carcass, and the secondary treatment is performed by treating with hyperthermophile for 2-4 weeks.
LIVESTOCK CARCASS TREATMENT SYSTEM USING ULTRA-HIGH TEMPERATURE MICROORGANISMS
The present invention relates to a carcass treatment system 1. Such a carcass treatment system 1 ferments and decomposes carcasses by hyperthermophile of 85 to 110° C. and aerobic conditions, and comprises a mobile fermentation process unit 3 for transferring to an onset site of disease and treating the livestock carcass by hyperthermophile; or a burial fermentation process unit 5 for excavating a burial site 6 near the outbreak site of disease and treating the livestock carcass by hyperthermophile; a base treatment unit 7 for secondarily processing the livestock carcass treated primarily by the mobile fermentation process unit 3 or the burial fermentation process unit 5 with hyperthermophile, wherein the primary treatment is performed by treating with hyperthermophile at fermentation temperature of 85 to 110° C. for 8-15 days to decompose flesh of the carcass, and the secondary treatment is performed by treating with hyperthermophile for 2-4 weeks.
MANUFACTURING METHOD OF ORGANIC FERTILIZER WITH PROTEINS AND HYDROLYSED AMINO ACIDS AND RESULTING ORGANIC FERTILIZER
It is a manufacturing method (10) of organic fertilizer (FG) obtained from the disposal of fish such as carcasses and viscera; said manufacturing method (10) of organic fertilizer (FG) consists of two sequential operational stations, namely the feeding station (FT), which is connected to the controlled hydrolysis station (ETH) using a set of equipment (CP) fed by steam, compressed air, fuel gas, water-soluble lewis acid, drinking water stored in tanks, reservoirs, chiller, among other equipment used to obtain the organic fertilizer (FG).
PROCESSING APPARATUS, PROCESSING METHOD, AND POWDER BODY
Provided is a processing apparatus for processing water-containing organic matters. The processing apparatus includes: a processing tank configured to store the water-containing organic matters; a stirring unit configured to stir the water-containing organic matters; a heater configured to heat the processing tank; an exhaust unit configured to exhaust gas from the processing tank at a rate from 1 m.sup.3/min to 300 m.sup.3/min; and an ion gas supply unit configured to supply ion gas into the processing tank with the exhaustion of the gas from the interior of the processing tank, the ion gas having an ion density of at least 2,000,000 pcs/cc, wherein the heater heats an interior of the processing tank while the stirring unit stirs the water-containing organic matters, and the ion gas is supplied into the processing tank according to the exhaustion by the exhaust unit, whereby processing the water-containing organic matters.
Method for producing organic molecules from fermentable biomass
The process for producing organic molecules from fermentable biomass includes a step of anaerobic fermentation (5) producing volatile fatty acids (6), these precursors being transformed into final organic molecules by non-fermentation means. It also includes at least the following steps: a) extracting (9) at least one portion of the volatile fatty acids from the fermentation medium in such a way that the production of fermentation metabolites by the microorganisms (M) is not affected, and introducing a portion of the liquid phase (11) containing microorganisms from the extraction (9), b) synthesizing (13) organic molecules from the fermentation metabolites or from the volatile fatty acids extracted in step a)-c) continuing steps a) to b) until the final molecules are obtained, in terms of amount and quality. The invention also relates to an installation for implementing the process.