Methods for producing melanin and inorganic fertilizer from fermentation leachates

Abstract

Melanin or inorganic fertilizers are produced from fermentation leachates or from low-cost nutrient-rich solutions. The method for producing the melanin or inorganic fertilizer comprises repetitive trophic cycling in the controlled conditions of primary and secondary bioreactors. Nutrients are cycled between microorganisms such as bacteria, yeast and fungi and black soldier fly larvae, Hermetia illucens . Polysaccharides are partly converted into natural melanins or inorganic fertilizer, which are difficult to biodegrade and hence accumulate in the bioreactors. The method can employ, as a source of nutrients, leachates produced from food waste or from sugar-rich liquid waste of the food industry. These leachates can be used raw or can be augmented with low-cost sugar-rich solutions such as molasses, hydrolyzed cellulose or starch. The method is inexpensive and does not require the use of expensive chemically-defined culture media.

What is claimed is: 
     
         1 . A method for producing a secondary leachate for use in producing inorganic fertilizer from the secondary leachate comprising the steps of:
 (a) providing a primary processing bioreactor, a fermentation medium and a microbial culture comprising microorganisms, wherein the microorganisms in the microbial culture comprise  Lactobacillus  bacteria;   (b) fermenting the fermentation medium with the microbial culture in the primary processing bioreactor, thereby producing a primary leachate, wherein the primary leachate comprises microorganisms derived from the microbial culture and/or naturally occurring microorganisms acquired during the fermentation step;   (c) isolating or removing the primary leachate from the primary processing bioreactor;   (d) providing the primary leachate isolated or removed from the primary processing bioreactor, a secondary processing bioreactor,  Hermetia illucens  (black soldier fly) larvae (BSFL), and a cellulose-based substrate;   (e) culturing the BSFL in an aerated culture with the primary leachate isolated or removed from the primary processing bioreactor and the cellulose-based substrate in the secondary processing bioreactor under suboptimal culture conditions for culture of the BSFL, thereby producing a secondary leachate, wherein the suboptimal culture condition is suboptimal temperature, high density, chemical stress, acidification, presence of toxic secondary metabolites, and/or nutrient starvation; and   (f) isolating or removing the secondary leachate from the secondary processing bioreactor, wherein the secondary leachate from the secondary processing bioreactor comprises inorganic fertilizer; and   (g) extracting or isolating the inorganic fertilizer from the secondary leachate.   
     
     
         2 . The method of  claim 1  wherein the inorganic fertilizer comprises ammonium, phosphate, carbonate and/or micronutrients. 
     
     
         3 . The method of  claim 1  wherein the step of extracting, isolating or deriving the inorganic fertilizer comprises the step of evaporating, titrating for changing the pH, filtering, centrifuging, dialyzing and/or lyophilizing the inorganic fertilizer. 
     
     
         4 . The method of  claim 1  wherein, in the step of culturing the BSFL with the primary leachate, the BSFL density is maintained at a larvae:liquid ratio, wherein the larvae:liquid ratio is 1 kg of larvae:1 kg of liquid to 1 kg of larvae:5 kg of liquid. 
     
     
         5 . The method of  claim 1  wherein the step of culturing the BSFL with the primary leachate further comprises adding BSFL to the secondary processing bioreactor to maintain the BSFL density at a larvae:liquid ratio, wherein the larvae:liquid ratio is 1 kg of larvae:1 kg of liquid to 1 kg of larvae:5 kg of liquid. 
     
     
         6 . The method of  claim 1  wherein the step of culturing the BSFL with the primary leachate proceeds for 10-20 days. 
     
     
         7 . The method of  claim 1  wherein the fermentation medium is organic waste. 
     
     
         8 . The method of  claim 7  wherein the organic waste is food waste, plant waste, compost, cellulosic residues, cellulose-rich waste, starch-rich waste, or protein-rich waste. 
     
     
         9 . The method of  claim 1  wherein the step of fermenting the fermentation medium with the microbial culture is conducted under anaerobic or microaerobic conditions. 
     
     
         10 . The method of  claim 1  wherein the microorganisms in the microbial culture are bacteria, yeast and/or fungi. 
     
     
         11 . The method of  claim 1  wherein the microorganisms in the microbial culture further comprise  Clostridium  and/or  Acetobacter  bacteria. 
     
     
         12 . The method of  claim 1  wherein the providing step (a) comprises providing a microbial culture that is a mixed microbial culture. 
     
     
         13 . The method of  claim 1  wherein the steps of (a) providing a primary processing bioreactor, a fermentation medium and a microbial culture comprising microorganisms, (b) fermenting the fermentation medium with the microbial culture in the primary processing bioreactor, thereby producing a primary leachate, and (c) isolating or removing the primary leachate from the fermentation medium, are repeated in sequence (a)-(c) at least 1-5 times. 
     
     
         14 . The method of  claim 1  comprising the step of monitoring the chemical composition of the primary leachate. 
     
     
         15 . The method of  claim 14  wherein the step of monitoring the chemical composition of the primary leachate is conducted prior to the step of isolating or removing the primary leachate from the primary processing bioreactor. 
     
     
         16 . The method of  claim 1  wherein the step of isolating or removing the primary leachate from the primary processing bioreactor is conducted at a point at which the fermentation becomes inefficient. 
     
     
         17 . The method of  claim 1  wherein the step of isolating or removing the primary leachate from the primary processing bioreactor is conducted when the pH of the leachate is 3.4−4.0±0.4. 
     
     
         18 . The method of  claim 1  wherein the step of culturing the BSFL comprises the step of adding an additive to the secondary processing bioreactor. 
     
     
         19 . The method of  claim 18  wherein the additive comprises carbohydrate, cellulose and/or starch. 
     
     
         20 . The method of  claim 19  wherein the carbohydrate is a sugar. 
     
     
         21 . The method of  claim 1  wherein the nutrient starvation is a nitrogen-poor and/or phosphorus-poor condition as defined by the classical Redfield ratio of approximately C:N:P=106:16:1. 
     
     
         22 . The method of  claim 1  wherein the culture in the secondary bioreactor comprises bacteria, yeast and/or fungi, and wherein the bacteria, yeast and/or fungi are derived from the primary leachate or are naturally occurring and introduced naturally from the environment into the culture in the secondary processing bioreactor.