Process, Apparatus and System for Treatment of Animal Effluent
AssigneeGarry Robert Nunn
InventorGarry Robert Nunn
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Abstract
A process of preparing a microbe digested liquid plant nutrient containing metabolites, amino acids and polypeptides, comprising the steps of partial composting of animal effluent solids; adding the partially composted animal effluent to a vessel containing water and held in suspension; the aqueous dispersion is thoroughly aerated for up to 4 days. Solids and liquids are subsequently removed from the metabolic reactor, separated and used as plant nutrients.
Claims24
A process for treating animal effluent comprising the steps of:
- a) subjecting the animal effluent to conditions under which at least partial aerobic digestion of the animal effluent is effected;
- b) The partially aerobic microbe digested solids are then held under anaerobic conditions to maintain the ammonia, sugars and saccharide levels formed at the peak of microbe activity in the solid phase. Sealing the semi-composted manures at this point is vital for the successful aerobic liquid microbe digestion stage to follow.
- c) dispersing a solid digestate produced in step a) in an aqueous medium;
- d) aerating the aqueous dispersion of step b) in the presence of soluble silica and/or germanium;
- and
- e) separating solids from liquids from the aerated aqueous dispersion.
The process wherein the animal effluent is mixed with the cellulosic material in a weight ratio (% w/w) of 40:60 to 60:40 animal effluent:cellulosic material.
The process, wherein the moisture content of the mixture is in a range of about 40 to 70% w/w.
The process according to any one of claims wherein subjecting the animal effluent to conditions under which at least partial aerobic digestion of the animal effluent is effected comprises storing the mixture of animal effluent and cellulosic material in the presence of oxygen or an oxygen rich atmosphere for a period of between 1 week and two months.
The process according to any one of claims, wherein the mixture attains a temperature in a range of about 60° C. to about 85° C. under said conditions.
The process according to any one of claims, wherein the process comprises treating the cellulosic material with a surfactant.
The process, wherein the cellulosic material is mixed with the surfactant in an amount of 0.5 to 5 litres surfactant per tonne of cellulosic material.
The process, wherein the mixture of cellulosic material and surfactant is formed prior to mixing the cellulosic material with the animal effluent.
The process, wherein the cellulosic material and surfactant mixture is subjected to aerobic conditions for a period of at least one month prior to mixing the treated cellulosic material with the animal effluent.
The process wherein the surfactant is mixed with the cellulosic material at or around the same time as it is mixed with the animal effluent.
The process wherein the semi-composted manure and carbon is then held under anaerobic conditions to prevent further aerobic breakdown of the sugars and sacharides to form CO2 and dissipation of ammonia.
The process according to any one of the preceding claims, wherein the step of dispersing the solid digestate in an aqueous medium comprises mixing the solid digestate with water or an aqueous solution in a weight/volume ratio in a range of 1 kg of solid digestate to about 2.5 to 50 litres water or aqueous solution.
The process according to any one of the preceding claims, wherein the aqueous dispersion of the solid digestate further comprises one or more additives selected from a group comprising surfactants, aerobic microbial innoculants or precursors thereof, soluble silica and/or germanium, a nitrogen source, and a microbial energy source.
The process, wherein the additives are soluble silica and/or germanium.
The process, wherein the one or more additives is added at or around the same time as dispersing the solid digestate in the aqueous medium.
The process, wherein the one or more additives is added to the aqueous dispersion.
The process, wherein the one or more additives is added to the solid digestate before it is mixed with water or the aqueous solution.
The process, wherein the aqueous solution contains the one or more additives prior to mixing with the solid digestate.
The process according to any one of the preceding claims, wherein the step of aerating the aqueous dispersion comprises passing an aerating medium at a positive pressure through the aqueous dispersion at a rate in the range of 0.5 m3 to 5.0 m3 aerating medium per 100 L water per hour.
The process according to any one of the preceding claims, wherein the step of aerating the aqueous dispersion is performed for a period of up to 4 days.
An apparatus for treating animal effluent comprising a vessel for containing an aqueous dispersion of a solid digestate, wherein the solid digestate is produced by at least partially aerobically digesting the animal effluent, the vessel having a plurality of inlets for receiving an aerating medium, and a discharge outlet for discharging the aerated aqueous dispersion.
The apparatus, wherein the discharge outlet is in fluid communication with a separator, whereby the separator is arranged, in use, to separate solids from liquids in the aerated aqueous dispersion.
A system for treating animal effluent comprising:
- a source of animal effluent;
- an aerobic digester for at least partially aerobically digesting the animal effluent;
- a vessel for containing an aqueous dispersion of a solid digestate, wherein the solid digestate is produced by at least partially aerobically digesting the animal effluent in the aerobic digester, the vessel having a plurality of inlets for receiving an aerating medium, and a discharge outlet for discharging the aerated aqueous dispersion;
- a separator in fluid communication with the discharge outlet, wherein the separator is arranged, in use, to separate solids from liquids in the aerated aqueous dispersion;
- and
- first and second conveyors to transfer the animal effluent from the source of said animal effluent to the aerobic digester, and to transfer the digestate from the aerobic digester to the vessel, respectively.
Dependencies are inferred from the claim text.