Apparatus and method for manure reclamation
An improved system for processing a liquid manure and producing organic fertilizer includes equipment for separating various components of the liquid manure having different nitrogen to phosphorous ratios and then mixing these components so as to produce an organic fertilizer with a predetermined nitrogen to phosphorus ratio. The system includes equipment for separating a first manure component that contains about 15 percent soluble phosphorus and about 20 percent soluble nitrogen, equipment for adding a flocculant material to the liquid manure aqueous solution, equipment for separating a second manure component that contains about 40 percent partially soluble phosphorus and about 30 percent partially soluble nitrogen, equipment for performing direct current electrocoagulation cleaning of the liquid manure aqueous solution and separating a third manure component that contains about 45 non-soluble phosphorus and about 10 percent non-soluble nitrogen and equipment for performing clarifying cleaning of the liquid manure aqueous solution and separating a fourth manure component that contains about 40 percent non-soluble nitrogen and no phosphorous.
1. A method for processing liquid manure comprising:
transferring said liquid manure into an input station;
separating a first manure component and a first overflow liquor from said liquid manure at a first processing station via a first mechanical separation equipment;
adding a flocculant material to said first overflow liquor at said first processing station;
separating a second manure component and a second overflow liquor from said first overflow liquor at a second processing station via a second mechanical separation equipment;
performing direct current electrocoagulation cleaning of said second overflow liquor at a third processing station and separating a third manure component and a third overflow liquor; and
performing clarifying cleaning of said third overflow liquor at an output station and separating a fourth manure component and water.
2. The method of claim 1 further comprising homogenizing said liquid manure at said input station.
3. The method of claim 1 further comprising discharging said water from said output station.
4. The method of claim 1 wherein said flocculant material comprises a complex carbohydrate compound.
5. The method of claim 4 wherein said complex carbohydrate compound comprises one of Fycosyllactose (C 18 H 32 O 15 ), Difucosyllactose (C 24 H 42 ) 19 ), Lacto-N-tetraose (C 26 H 45 NO 21 ), Lacto-N-fucopentaose I(C 32 H 55 NO 25 ), Lacto-N-difucohexaose I(C 38 H 65 NO 29 ), Lacto-N-fucopentaose III, Monofucosyllacto-N-hexaose (C 46 H 78 N 2 O 35 ), Difucosyllacto-N-hexaose (a) (C 52 H 88 N 2 O 39 ), Difucosyllacto-N-neohexaose, Difucosyl-para-lacto-N-hexaose, Trifucosyllacto-N-hexaose (C 58 H 98 N 2 O 43 ), Trifucosyl-para-lacto-N-hexaose, Sialyllactose (C 23 H 39 NO 19 ), Sialyllacto-N-tetraose (C 37 H 62 N 15 O 29 ), Monofucosyl, monosialyllactose (C 29 H 49 NO 23 ), Monosialyl, monofucosyllacto-N-neotetraose (C 43 H 72 N 2 O 33 ), Disialyllactose-N-tetraose (C 48 H 79 N 3 O 37 ), A-pentasaccharide (C 32 H 55 NO 24 ), B-pentasaccharide (C 30 H 52 O 24 ), Oligomannose-3 (C 35 H 58 N 2 O 26 ), Oligomannose-5 (C 46 H 78 N 2 O 36 ), Oligomannose-6 (C 52 H 88 N 2 O 41 ), Oligomannose-7D1 (C 58 H 98 N 2 O 46 ), Oligomannose-7D2, Oligomannose-7D3, Oligomannose-8D1D3, Oligomannose-8D1D2 (C 64 H 108 N 2 O 51 ), Oligomannose-8D2D3, Oligomannose-9 (C 70 H 118 N 2 O 56 ), Asialo-biantennary (C 62 H 104 N 4 O 46 ), Asialo-biantennary with core substituted fucose (C 68 H 114 N 4 O 50 ), Disialyl-biantennary (C 84 H 138 N 6 O 62 ), Oligomannose-3 substituted with fucose and xylose (C 45 H 76 N 2 O 34 ), Oligomannose2(a) (C 28 H 48 N 2 O 21 , Oligomannose-4 (C 40 H 68 N 2 O 31 ), Lacto-N-hexaose, Lacto-N-neohexaose, Monosialyl LNnH, Monosialyl monofucosyl LnnH, Disialyl monofucosyl LNH, Chitobiose, or Maltotriose.
6. The method of claim 1 wherein said first mechanical separation equipment comprises a screw press.
7. The method of claim 1 wherein said second mechanical separation equipment comprises a plate filter press.
8. The method of claim 1 where said flocculant material comprises one of lime, iron, aluminum, wollostonite, calcium, starches, proteins, gelatin, animal glue, polymeric compounds or food grade polymers.
9. The method of claim 1 further comprising passing said liquid manure through a pre-thickener station.
10. The method of claim 1 wherein said first manure component comprises about 15 percent soluble phosphorus and about 20 percent soluble nitrogen.
11. The method of claim 1 wherein said second manure component comprises about 40 percent partially soluble phosphorus and about 30 percent partially soluble nitrogen.
12. The method of claim 1 wherein said third manure component comprises about 45 percent non-soluble phosphorus and about 10 percent non-soluble nitrogen.
13. The method of claim 1 wherein said fourth manure component comprises about 40 percent non-soluble nitrogen and no phosphorous.
14. The method of claim 1 further comprising stabilizing any of said manure components by adding a stabilizing component.
15. The method of claim 14 wherein said stabilizing component comprises one of lime, wollostonite, calcium carbonate, complex carbohydrates, or calcium.
16. The method of claim 1 further comprising mixing a first amount of said first manure component, a second amount of said second manure component, a third amount of said third manure component and/or a fourth amount of said fourth manure component to obtain a fertilizer comprising a desired nitrogen to phosphorous ratio.
17. The method of claim 16 wherein any of said first, second, third or fourth amounts is in the range of 0 to 100 percent and the sum thereof being 100 percent.
18. The method of claim 16 wherein said third manure component comprises about 45 percent non-soluble phosphorus and about 10 percent non-soluble nitrogen and said fourth manure component comprises about 40 percent non-soluble nitrogen and no phosphorous and wherein equal amounts of said third manure component and said fourth manure component are mixed to obtain a fertilizer with a nitrogen to phosphorous ratio of 7:1.
19. The method of claim 16 wherein said first manure component comprises about 15 percent soluble phosphorus and about 20 percent soluble nitrogen and said fourth manure component comprises about 40 percent non-soluble nitrogen and no phosphorous and wherein equal amounts of said first manure component and said fourth manure component are mixed to obtain a fertilizer with a nitrogen to phosphorous ratio of 30:1.
20. A method for processing milk house waste (MHW) and foot bath waste (FBW) comprising:
collecting said MHW and FBW, wherein said MHW and FBW comprise metal compounds and short chain carbon compounds;
performing direct current electrocoagulation cleaning of said MHW and FBW, thereby separating inactive oxides of said metal compounds, said short chain carbon compounds and an overflow liquor; and
performing clarifying cleaning of said overflow liquor and separating a solid component and water.
21. The method of claim 20 wherein said metal compounds comprise zinc sulfate or copper sulfate and said inactive oxides of said metal compounds comprise zinc oxide or copper oxide, respectively.