TH36738A - The process for producing granular organic matter - Google Patents

Abstract

DC60 (26/12/43) This invention involves a process for the production of granular organic matter. Where the precipitation Obtained in the sedimentation tank from the methane fermentation fluid Being treated by using the air in the aeration tank is filled in the Flow that is waste of fermentation From this invention A process has been prepared for the production of physically stable granular organic compounds. Along with a decrease in the increase in coherence that occurs While producing organic material That is a pellet from a fluid that is a waste of fermentation. This invention deals with a process for the production of granular organic matter where the precipitated portion obtained in the sedimentation tank from the methane fermentation fluid. Processed using air in the aerated tank is added to the waste fluid of this invention. A process is being prepared for the production of granular organic substances. Physically stable Along with a decrease in the increase in coherence that occurs While producing pellet organic matter from fermentation waste fluid

Claims (8)

1. The process for the production of pellet organic compounds consists of the following steps: (a) the import of Fluids that are waste of fermentation (b) anaerobic fermentation The fluid that is the waste of such fermentation to obtain the water produced by the decomposition (c) the aeration of the water produced from the degradation (d) the water conduction. The aerated fermentation is precipitated to obtain the sludge fraction (e) drying or dehydration of the sludge (f) mixing the dry or dehydrated portion of the sludge. Fermentation without air and (g) granulation Of a mixture of waste fluids of fermentation With the sludge fraction used from step (f) 2. Process according to claim 1, where the anaerobic waste fermentation fluid is concentrated until the solid has a content of 20 to 60 percent 3. Process according to claim 1 or 2, where after the sludge is mixed with A fluid that is a fermentation waste that has not been aeration Inorganic fertilizers are added to 4. Process according to claim 3, where the anaerobic waste fluid is alcohol from. Fluid that is waste of fermentation 5. Process according to claim 4 where the sludge is dried or dehydrated. Until the solids have a content of 15 to 55 percent 6. Process according to claim 5, where after the sludge is mixed with Fermentation waste fluid that has not been aeration Inorganic fertilizers are added to 7. Process according to claim 6, where at least one inorganic fertilizer is selected from a group containing phosphoric acid diammonium phosphate double su. Lime Superphosphate, Super Phosphate of Lime, Potassium Chloride Ammonium sulphate, ammonium chloride, urea and magnesium sulphate 8. Organic fertilizers containing organic substances that make it The pellets obtained by the process are described in claim 7 9. Process according to claim 3 whereby the waste fluid of the pellets is usually an airtight fermentation at 30 to 60 ° C for 3 days to 2 weeks 1 0. Process according to claim 9 whereby composting water is exposed to air at a flow rate of 0.2 to 1.2 wm for 1 to 7 1 1. Process according to claim 10 where part Family mixed with Anaerobic fermentation waste fluid of 30-200% by weight / weight 1 2. Process according to claim 11, where the sludge is mixed with the non-aerobic fermentation waste fluid. 50-100% of air was given by weight / weight 1 3. Process according to claim 3 where the sludge was dried or dehydrated. Until the solids amounted to 15 to 55 percent 1 4. Process according to claim 13 where after the sludge was mixed with the airtight fermentation fluid, the sludge was Inorganic fertilizers are added to 1. 5. Process according to claim 14, where the inorganic fertilizer consists of at least one inorganic fertilizer selected from the phosphorous acid group. Eric Diammonium Phosphate Double Superphosphate of Lime Lime Superphosphate Potassium Sulphate, Potassium Chloride Ammonium sulphate, ammonium chloride, urea and magnesium sulphate 1 6. Organic fertilizers containing organic granular substances obtained by the process as described in Clause 15 1 7. Organic fertilizers containing organic compounds that cause The pellets are obtained by the process described in claim 14 1 8. Process according to claim 3 whereby the waste fluid of fermentation The fermentation was free of air at 30 to 60 ° C for 3 days to 2 weeks. Composting wastes that are anaerobic alcohol Composting fluids 2 0. Organic fertilizers containing process-derived organic matter as described in claim 3 2. 1. Process according to claim 4, where the waste fermentation fluid is fermented without air at 30 to 60 ° C for 3 days to 2 weeks 2. 2. Process according to claim 21 where fermentation liquor is exposed to air with a flow rate of 0.2 to 1.2 wm for 1 to 7 days. 3. Process according to claim 22 in which the sludge is mixed with Fluid containing 30-200% anaerobic waste waste by water / weight 2 4. Process according to claim 23 in which the sheave is mixed with Fluid that is a waste of 50-100% anaerobic fermentation by w / weight 2 5. Organic fertilizers that contain organic substances that are made possible in the process as described in claim 4 2. 6.Organic fertilizers containing process organic matter as described in claim 5 2. 7.Organic fertilizers containing process-derived organic substances as described in claim 6 2. 8.Organic fertilizers containing process organic matter as described in claim 1 or 2.