http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-100472969-B1

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filingDate 2002-08-21-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2005-03-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2005-03-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-100472969-B1
titleOfInvention Manufacturing method of a liquefied fertilizer
abstract An object of the present invention is to provide a method for producing a high-quality liquid fertilizer in a short time without the generation of odor of organic waste, such as food waste, serving, livestock manure, food and slaughterhouse by-products.n n n To this end, the present invention, when the organic waste is broken into large foreign matters and removal of foreign matters, when the salt content is high, pre-treatment such as desalination treatment is stored and cultured in the aerobic maturation process when entering the first aerobic fermentation tank (1) Corrosive microorganisms that excrete polyphenolic metabolites and soil microbial strains that have mutual symbiosis with these microorganisms are supplied to supply air from the blower 22 to reduce the occurrence of odor by performing first aerobic fermentation. Next, the organic waste transfer pump (2) was sent to the vibrating screen (3) and the dehydrator (4) to send the dehydrated cake which dehydrated the solids from the organic waste to the compost, and to the dehydration liquid storage tank (5). In the case of livestock manure by the dehydration liquid feed pump (6), it is reused as the return water for the housekeeping and the rest is sent to the aerobic maturation tank (7). Humification grade) is more than 90% to corrode the organic material and then sent to the strain sedimentation tank (8), the strain transported pump (10) when the corroded sludge precipitates concentrated on the lower part of the strain sedimentation tank (8). By the organic waste inlet, storage and the first aerobic fermentation tank (1), aerobic maturation tank (7) to the front end of the return to the strain culture tank (11).n n n In the strain culture tank (11), pellets (13) and soluble minerals formed by molding marine corrosive acid colloidal micelles formed by depositing marine diatoms, seaweeds, plankton, etc. Bio-reactor filled with activated minerals such as Pumice containing a large amount of minerals and ferrite minerals (magnetite) with magnetic properties 12) is provided, the strain culture tank (11) is supplied to the strain precipitated in the strain sedimentation separation tank (8) and aerated when the aeration, the strain and the corroded sludge together with air While circulating the bioreactor 12, a chelated organic acid mineral, an activating material, an enzyme, and the like are supplied from pellets 13, active minerals 14, and magnetic ferrite minerals of marine corrosive acid colloid micelles. Excretion of phenolic metabolites When a culture medium in which corrosive microorganisms and soil microorganisms which are mutually related to these microorganisms are actively metabolized is cultured, it is sent to the aerobic maturation tank (7), whereby the whole system is connected to the corrosive microorganisms and these microorganisms. As the soil microorganisms are transformed into the predominantly growing environment, the growth of pathogenic microorganisms and harmful microorganisms such as decayed and perishable microorganisms is suppressed and odor occurrence is reduced, and organic substances are insoluble in water. It is converted into a non-volatile safe corrosive and becomes a mature liquid fertilizer.n n n In order to facilitate the formation of corrosive substances, the storage and the first aerobic fermentation tank (1) and strain culture are carried out because a smooth reaction occurs in the range of +250 to +300 mV in the ORP (Oxidation Reduction Potential) value in the system. The oxidation reduction potential (ORP) is adjusted by supplying the oxidation water of the oxidation water storage tank 19 so that the oxidation reduction potential (ORP) of the tank 11 is maintained in the range of +250 to +300 mV.n n n The matured liquid ratio is sent to the liquid ratio intermediate storage tank 15 and then transferred to the liquid ratio storage tank 17 by the liquid ratio transfer pump 16.n n n In particular, in the present invention, organic waste is hardly generated in the liquefaction process of organic waste, and since the maturity period is short, the facility cost is low and a large amount of useful materials for plant growth are contained, so that it can be a high quality organic fertilizer. It is expected to be widely used as a resource for organic waste such as serving, livestock manure, food waste, food and slaughterhouse by-products.
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