Pseudomonas fluorescens N1 and use thereof

Abstract

This application relates to Pseudomonas fluorescens N1, and usage therefor in solid waste recycling based on full bionic simulation combined with a microorganism. Light, temperature, gas and heat conditions in cyclic transformation of organic carbon in soil are simulated, and solid waste is mixed and stacked in the soil or between hills, wherein the solid waste is basically blended according to the carbon-nitrogen ratio, alkalinity or acidity, and water content of the solid waste, and no turning is performed according to the principle of anaerobic fermentation. By introducing high-carbon, high-salt, alkaline or acidic liquid waste using a bionic head cover during stacking, the anaerobic fermentation process is controlled to stop at an acid production stage so that organic acids produced are fully mixed with the solid waste, and the nutrients in the solid waste are released by using acidic materials and thus become nutritional elements for acidic material chelation.

Claims

1. A method for modifying solid waste by a microorganism synergistically with coal gangue material, comprising the following steps: (1) adding coal gangue to magnesium slag in an amount of 10-15% by volume of the magnesium slag, mixing thoroughly, sieving to control a particle size of the mixed material to be 2-5 mm, and stacking for 5-10 days; (2) adding vinegar dregs in an amount of 20-30% by volume of the magnesium slag, mixing thoroughly, and adjusting the pH value to 5.5-6.5 using a wood vinegar liquid; and (3) spraying Pseudomonas fluorescens N1 registered in the China General Microbiological Culture Collection Center under the accession number CGMCC No. 23192 or Pseudomonas fluorescens N1 registered in the China General Microbiological Culture Collection Center under the accession number CGMCC No. 23192+Xanthomonas campestris mixed in an equal solution volume onto the mixed material surface, and spraying water in an amount of 0.50-1.00 m.sup.3/m.sup.3 mixed material per day for 30-40 days.

2. The method of claim 1, wherein the solid waste is heavy metal contaminated soil.

3. The method of claim 2, further comprising a step of: (4) adding phosphate rock powder in an amount of 5-10% by volume of the total materials, and mixing thoroughly, thus creating a substrate for cultivation.

Description

DETAILED DESCRIPTION OF THE INVENTION

(1) The technical solutions in the embodiments of this application will be described clearly and completely. Obviously, the described embodiments are only a part of the embodiments of this application, rather than all the embodiments. Based on the embodiments in this application, all the other embodiments obtained by a person of ordinary skill in the art without manufacturing any inventive effort fall within the scope of protection of this application.

(2) The technical principle of this application is: proportioning the raw material of pre-treated solid waste substrate according to the result of modification: following the basic nutrient principle, acidity; alkalinity, salinity value, hydrophilicity, carbon-nitrogen ratio, introducing the functional bacterial flora to regulate the micro-ecology of the root growth: using the seedling pot to hold the substrate and planting into the plant; and intensively piling up between the seedling pot and seedling pot and adding untreated solid waste substrate for gap filling appropriately to build a micro-soil moisture preservation environment, utilizing the maintenance of plant root microenvironment; and after new branches have sprouted, transplanting the plants with the seedling pot. Depending on the purpose of transplanting, the bottom of the seedling pot is opened with a sized hole. For conventional greening, the hole size is less than 5 centimeters to fix the plant. For soil and water conservation greening, the hole size is increased to 15 centimeters or more to release more roots. Most of the root system remains inside the solid waste substrate for adsorption and passivation of various types of polluted toxic and hazardous substances for phytoremediation.

(3) The Xanthomonas of this application is Xanthomonas campestris NRRLB-1459, but is not limited to this species, all Xanthomonas thereof may fulfill this application. The Pseudomonas of this application is Pseudomonas fluorescens N1, but is not limited to this species, all Pseudomonas thereof may fulfill this application. The above strain should be adjusted to a concentration of roughly 10.sup.9 cells per milliliter (OD600=1.0).

Example 1: A Method for Modifying Solid Waste by a Microorganism Synergistically with Coal Gangue Material Included the Following Steps

(4) (1) Coal gangue was added to magnesium slag in an amount of 13% by volume of the magnesium slag and mixed thoroughly. The mixed material was sieved to control the particle size to be 2 mm and stacked for 8 days. (2) Vinegar dregs were added in an amount of 20% by volume of the magnesium slag and mixed thoroughly. The pH value of the mixed material was adjusted to 5.5 using a wood vinegar liquid. (3) Pseudomonas fluorescens N1 was sprayed on the material surface. Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 35 days.

Example 2: A Method for Modifying Solid Waste by a Microorganism Synergistically with Coal Gangue Material Included the Following Steps

(5) (1) Coal gangue was added to magnesium slag in an amount of 13% by volume of the magnesium slag and mixed thoroughly. The mixed material was sieved to control the particle size to be 2 mm and stacked for 8 days. (2) Vinegar dregs were added in an amount of 20% by volume of the magnesium slag and mixed thoroughly. The pH value of the mixed material was adjusted to 5.5 using a wood vinegar liquid (3) Xanthomonas campestris was sprayed on the material surface. Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 35 days.

Example 3: A Method for Modifying Solid Waste by a Microorganism Synergistically with Coal Gangue Material, Included the Steps of

(6) (1) Coal gangue was added to magnesium slag in an amount of 10% by volume of the magnesium slag and mixed thoroughly. The mixed material was sieved to control the particle size to be 2 mm and stacked for 8 days. (2) Vinegar dregs were added in an amount of 30% by volume of the magnesium slag and mixed thoroughly. The pH value of the mixed material was adjusted to 5.5 using a wood vinegar liquid. (3) Pseudomonas fluorescens N1+Xanthomonas campestris (mixed with equal solution volume) were sprayed on the material surface. Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 35 days.

Example 4: A Method for Remedying Heavy Metal Contaminated Soil by a Microorganism Synergistically with Coal Gangue Material Included the Following Steps

(7) (1) Coal gangue was added to magnesium slag in an amount of 15% by volume of the magnesium slag and mixed thoroughly. The mixed material was sieved to control the particle size to be 5 mm and stacked for 10 days. (2) Vinegar dregs or wood vinegar liquid was added to adjust the pH value to 5.5. (3) Pseudomonas fluorescens N1 and Xanthomonas campestris (mixed with equal solution volume) were sprayed on the material surface. Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 30 days.

Example 5: A Method for Preparing a Cultivation Substrate from a Solid Waste Modified by a Microorganism Synergistically with Coal Gangue Included the Following Steps

(8) (1) Coal gangue was added to magnesium slag in an amount of 10% by volume of the magnesium slag and mixed thoroughly. The mixed material was sieved to control the particle size to be 3 mm and stacked for 5 days. (2) Vinegar dregs were added in an amount of 30% by volume of the magnesium slag and mixed thoroughly: The pH value of the mixed material was adjusted to 5.5 using a wood vinegar liquid. Wood vinegar liquid: pH 3.3, contains 53.0% total amino acids. (3) Phosphate rock powder was added in an amount of 8% by volume of the total materials and mixed thoroughly. (4) Pseudomonas fluorescens N1 and Xanthomonas campestris (mixed with equal solution volume) were sprayed on the material surface. The Carbon-nitrogen ratio was adjusted to about 25:1. Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 30 days so that the phosphate-solubilizing bacterium could release organic acids continuously to form a cultivation substrate.

Further Optionally

(9) (5) the substrate was placed in a seedling pot and transplanted with a plant. Slags were filled with no porous between the seeding pots, a micro-moisture-preservation environment can be created to promote rapid root growth. (6) When a sprout is germinated or a new leaf is expanded, the plant is sold or the ecology is remedied in situ.

(10) The phosphate-solubilizing bacterium is preferably Pseudomonas fluorescens.

(11) The Xanthomonas can be Xanthomonas campestris.

(12) When the carbon-nitrogen ratio is adjusted in step (4), ammonia water and nitrogen fertilizer are selected as the nitrogen source, and straw agricultural waste is selected as the carbon source.

(13) Step (4) further comprises, with reference to the content of the main nutrients in the substrate for cultivation, calculating and adding the corresponding nitrogen fertilizers (urea, KNO.sub.3, NH.sub.4H.sub.2PO.sub.4, etc.), phosphorus fertilizers (calcium superphosphate, etc. (cured phosphorus)+potassium dihydrogen phosphate), potassium fertilizers (KNO.sub.3, KH.sub.2PO.sub.4, etc.) to the substrate.

Example 6: A Method for Recycling Solid Waste Based on Full Bionic Simulation Combined with a Microorganism Included the Following Steps

(14) (1) Coal gangue with a particle size of 3 mm was stacked at the bottom at a stacking thickness of 6 m. (2) A bionic swamp mixture, specifically a mixture of sludge, kitchen waste and fly ash was stacked on the first layer of coal gangue, and the water content of the mixture was adjusted to 60% so that the fermentation water met the basic requirements of anaerobic fermentation. At the same time, the carbon-nitrogen ratio was adjusted to be 35:1, pH 5.5, salinity 20%, and composting thickness 3 m, for anaerobic fermentation. (3) Steps (1)-(2) were repeated alternately and multi-layer composting was performed according to a stacking treatment amount to improve stacking efficiency and total treatment amount. (4) A bionic swamp cover head was laid on the uppermost layer of the stacked layer, wherein the bionic swamp cover head consists of crushed straw and mushroom dregs mixed according to a volume ratio of 3:2, and the crushed particle size of the two components was 3 cm. During the anaerobic fermentation process, a functional microorganism eluent, a carbon-nitrogen ratio eluent, a pH value adjustment eluent and a high-salt eluent for the lower stacked layer can be transported via the bionic swamp cover head, and at the same time the use of the bionic swamp cover head to adjust the damp-heat energy storage of the bottom stacked layer can be facilitated. A solar membrane for energy collection was provided on the bionic swamp. In the microorganism eluent, the microorganism was an acidogenic anaerobic fermentation microorganism, preferably Pseudomonas fluorescens N1. Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 60 days. (5) An induction probe was provided at the bottom of the bionic swamp cover head to feed back the temperature and humidity of the fermentation stack in time, and when the temperature is too high or too low; the condition was controlled by delivering the eluent at a certain temperature. The temperature was maintained at 30 C. and humidity was maintained at 60%.

Example 7: A Method for Recycling Solid Waste Based on Full Bionic Simulation Combined with a Microorganism Included the Following Steps

(15) (1) Coal gangue and magnesium slag with a particle size of 3 mm were stacked at the bottom, wherein the amount of the coal gangue addition was 10% of the volume of the magnesium slag. Then vinegar dregs were added in an amount of 30% by volume of the magnesium slag and mixed uniformly. The mixture was stacked at a thickness of 6 m. (2) A mixture of sludge, kitchen waste and fly ash was stacked on the first layer, and the water content of the mixture was adjusted to 60% so that the fermentation water meets the basic requirements of anaerobic fermentation. At the same time, the carbon-nitrogen ratio was adjusted to be 35:1, pH 5.5, salinity 20%, and composting thickness 3 m, for anacrobic fermentation. (3) Steps (1)-(2) were repeated alternately and multi-layer composting was performed according to a stacking treatment amount to improve stacking efficiency and total treatment amount. (4) A bionic swamp cover head was laid on the uppermost layer of the stacked layer, wherein the bionic swamp cover head consists of straw and mushroom dregs mixed according to a volume ratio of 3:2, and the crushed particle size of the two components was 3 cm. During the anaerobic fermentation process, a functional microorganism eluent, a carbon-nitrogen ratio eluent, a pH value adjustment eluent and a high-salt cluent for the lower stacked layer can be transported via the bionic swamp cover head, and at the same time the use of the bionic swamp cover head to adjust the damp-heat energy storage of the bottom stacked layer can be facilitated. A solar membrane for energy collection was provided on the bionic swamp. In the microorganism cluent, the microorganism was an acidogenic anaerobic fermentation microorganism, preferably Pseudomonas fluorescens and Xanthomonas campestris (mixed with equal solution volume). Water was sprayed in an amount of 1.00 m.sup.3/m.sup.3 material per day for 50 days. (5) An induction probe was provided at the bottom of the bionic swamp cover head to feed back the temperature and humidity of the fermentation stack in time, and when the temperature is too high or too low; the condition was controlled by delivering the eluent at a certain temperature. The temperature was maintained at 30 C. and humidity was maintained at 60%.

Experiment I: Experiment on Solid Waste Modified by a Microorganism Synergistically with Coal Gangue Material as Substrate

(16) Experiment method: The organic acid produced by microorganisms in the process of growth and reproduction can not only reduce the pH value in the soil environment but also directly release the phosphorus in the fixed-state phosphate into the soil. This experiment is mainly to study the process parameters of modifying solid waste magnesium slag by a microorganism synergistically with coal gangue. The specific method is described in Example 3. The solid waste is modified by comparing the proportions of magnesium slag, coal gangue and vinegar dregs with different proportions, and the phosphate-solubilizing bacterium and Xanthomonas spp. to form a substrate for plant growth and cultivation. After 35 days of reforming, the substrate water content (%), substrate aeration rate (the maximum volume of heavy oxygen per square meter of the substrate, unit: m.sup.3/m.sup.2), effective phosphorus content (mg/kg), and organic acid (oxalic acid) content (mg/kg) can be calculated and determined. Each treatment can be averaged in triplicate. Pseudomonas fluorescens powder (viable effective bacteria 300 billion cfu/mL) in the control group was purchased from Jiangsu Changzhou Lanling Pharmaceutical Co. Ltd. Bacillus wettable powder (effective viable bacteria 1 billion cfu/mL) was purchased from Zhejiang Tonglu Huifeng Biochemical Co. Ltd.

(17) TABLE-US-00001 TABLE 1 Solid waste modification experiment table Magnesium Coal Vinegar slag gangue dregs Phosphate- Experiment Volume Volume Volume solubilizing pH No part part part bacterium Xanthomonas value 1 100 5 10 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 2 100 10 10 fluorescens Xanthomonas 5.5 fluorescensNI campestris 3 100 15 10 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 4 100 5 20 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 5 100 10 20 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 6 100 15 20 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 7 100 5 30 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 8 100 10 30 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris 9 100 15 30 Pseudomonas Xanthomonas 5.5 fluorescensNI campestris Control 1 100 10 30 Pseudomonas 5.5 fluorescensNI Control 2 100 10 30 Xanthomonas 5.5 campestris Control 3 100 10 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris Control 4 100 30 Pseudomonas Xanthomonas 5.5 fluorescensN1 campestris Control 5 100 10 30 Pseudomonas Xanthomonas 5.0 fluorescensNI campestris Control 6 100 10 30 Pseudomonas Xanthomonas 6.0 fluorescensN1 campestris Control 7 100 10 30 Bacillus Xanthomonas 5.5 campestris Control 8 100 10 30 Pseudomonas Xanthomonas 5.5 fluorescens campestris powder

(18) TABLE-US-00002 TABLE 2 Influence of different modification conditions on the indexes of solid waste-reformed substrate Effective Oxalic Substrate Substrate phosphorus acid water aeration Experiment content content content rate No (mg/kg) (mg/kg) (%) (m.sup.3/m.sup.2) 1 765.43 13.43 47.2 0.39 2 818.48 14.32 48.3 0.41 3 830.09 14.56 50.0 0.41 4 770.97 13.52 48.5 0.38 5 829.43 14.66 50.4 0.42 6 830.23 14.78 52.8 0.43 7 795.36 13.11 55.4 0.43 8 880.61 15.60 58.3 0.45 9 873.50 14.69 57.5 0.43 Control 1 823.43 12.32 51.4 0.19 Control 2 765.01 11.47 52.1 0.20 Control 3 754.57 13.45 42.3 0.17 Control 4 330.40 10.22 51.4 0.13 Control 5 570.47 14.43 52.6 0.31 Control 6 475.78 10.13 53.9 0.30 Control 7 612.52 11.23 49.9 0.33 Control 8 872.89 14.93 58.02 0.41
Experimental Results

(19) Different coal gangue contents affect the effective phosphorus content of the substrate and the production of organic acids. All other experiments had higher effective phosphorus content in the substrate compared to Control 4 without added coal gangue. Among them, best results were obtained when the coal gangue content was 10-15 volume parts. The adsorption capacity of coal gangue modified by microorganisms is very strong, and it directly releases phosphorus from the fixed-state phosphate. The content of organic acids (glycolic acid) was also highest in Experiment 8. Glycolic acid is the most representative type of organic acid and one of the important organic acids required for plant growth. By synergistically modifying the solid waste magnesium slag and coal gangue with Pseudomonas fluorescens (Control 8 or strain Experiment 8 of this application) and Xanthomonas, the organic acids in the solid waste can be released, thereby promoting plant growth. In addition, Control 7 showed that, in comparison with the other microorganisms, the effect of phosphate-solubilizing and organic acid-releasing thereof was not as good as that of using the combination of Pseudomonas fluorescens+Xanthomonas of this application, and the comprehensive physical and chemical properties of the improved solid waste-reformed substrate were superior to those of using one of the microorganisms alone, such as Controls 1 and 2.

(20) Different pH values have different effects on the phosphate-solubilizing effect of the strains. After 30 days of modification on the solid waste, for the effective phosphorus content compared to Controls 5 and 6, the effect of phosphate-solubilizing as well as the production of organic acids was weaker at pH 5.0 and 6.0, and a higher amount of dissolved phosphorus could be produced at pH 5.5. Experiment 8 had the highest effective phosphorus content and organic acid content at pH 5.5. The results showed that the effect of phosphate-solubilizing and organic acid production is good in the acidic solid waste substrate environment.

(21) This application is the first to use magnesium slags as a hydrophobic raw material and vinegar dregs as a hydrophilic raw material, and through the reasonable proportioning of the two materials, combined with the adjustment of particle size, to achieve the water content and aeration of the substrate suitable for plant cultivation. The comparative example showed that the volume ratio of magnesium slags and vinegar dregs at 100:30 can achieve the best effect on the water content and aeration of the substrate. Compared with the magnesium slag solid waste without coal gangue, the substrate aeration can be significantly reduced, and compared with the magnesium slag solid waste without vinegar dregs, the substrate water content can be also significantly reduced.

(22) Experiment II: Orthogonal Design Analysis Affecting the Remediation Capacity of Solid Waste-Reformed Substrate

(23) Experiment method: to find the factors and optimal combinations affecting the remediation capacity of the solid waste-reformed substrate on heavy metal contaminated soil and the phosphate-solubilizing effect of effective phosphorus, and to provide the theoretical basis for the optimal combination of remediation technologies after solid waste reforming. The three conditions of material particle size A (2 mm for level 1, 3 mm for level 2, and 5 mm for level 3), the amount of coal gangue addition B (percentage of magnesium slag volume) (10% for level 1, 13% for level 2, and 15% for level 3), and phosphate-solubilizing bacterium dosage C (0.50 m.sup.3/m.sup.3 for level 1, 0.80 m.sup.3/m.sup.3 for level 2, and 1.00 m.sup.3/m.sup.3 for level 3) were taken as the variables, the heavy metal lead removal rate and effective phosphorus content as indicators to select the optimal combination, L9 (33) orthogonal table. The lead removal rate was specifically prepared to simulate lead-contaminated soil. Based on 30% water content, a certain concentration of Pb(NO.sub.3).sub.2 solution was added to the substrate soil, and the Pb content in the soil was controlled to be 200 mg/L. The mixture was homogenized and placed in a constant temperature incubator to stabilize for 90 d. The contaminated soil was taken out every 10 d, and added with deionized water, and the relative water content of the soil was controlled to be about 30% by the mass method. Various materials of the experiment levels mentioned above were added to simulate the remediation for 30 days and determine the Pb.sup.2+ concentration and effective phosphorus content. The removal rate of heavy metal lead= (C0-C1)/C0, where C0-the lead concentration (mg/L) of the initial solution before the experiment; C1-the lead concentration (mg/L) of the residue after adsorption. Each treatment can be averaged in triplicate.

(24) TABLE-US-00003 TABLE 3 Orthogonal design table affecting the remediation capacity of solid waste-reformed substrate A B C Material Amount of Phosphate- Lead Effective particle coal gangue solubilizing removal phosphorus size addition bacterium dosage rate (%) (mg/kg) 1 1 1 75.4 854.09 1 2 2 76.6 859.23 1 3 3 89.1 878.78 2 1 2 69.9 609.8 2 2 3 93.8 873.8 2 3 1 83.5 735.5 3 1 3 71.2 764.49 3 2 1 89.4 751.27 3 3 2 94.5 779.86 K1 80.37 72.17 82.77 B > A > C K2 82.40 86.60 80.33 K3 85.03 89.03 84.70 R 4.67 16.87 4.37 Optimum level A3 B3 C3 of lead removal rate K1 864.03 742.79 780.29 A > C > B K2 739.70 828.10 749.63 K3 765.21 798.05 839.02 R 124.33 85.31 89.39 Optimum level A1 B2 C3 of effective phosphorus

(25) Experiment Results: as can be seen from the table above, through the study we have concluded that the factors affecting the remediation capacity of solid waste-reformed substrate are mainly based on the particle size of material A, the amount of coal gangue addition B, and the phosphate-solubilizing bacterium dosage C. The optimal scheme affecting the remediation capacity of solid waste-reformed substrate for heavy metal lead pollution was A3B3C3, i.e., a mixed substrate of 5 mm crushed particle size, 15% coal gangue addition, and 1.00 m.sup.3/m.sup.3 phosphate-solubilizing bacterium dosage. The optimal scheme for the phosphate-solubilizing effect of solid waste-reformed substrate is A1B2C3, i.e. a mixed substrate of 2 mm particle size, 13% coal gangue addition, and 1.00 m.sup.3/m.sup.3 phosphate-solubilizing bacterium dosage.

(26) The order of influence of each factor is the ability to remedy heavy metal lead pollution: B (amount of coal gangue addition)>A (crushed particle size)>C (phosphate-solubilizing bacterium dosage). The phosphate-solubilizing effect of the solid waste-reformed substrate: A (crushed particle size)>C (phosphate-solubilizing bacterium dosage)>B (amount of coal gangue addition).

(27) Experiment III: Influence of Phosphorus Ore Powder on the Promotion of Phosphate-Solubilizing by Phosphate-Solubilizing Bacterium

(28) Experiment method: this experiment mainly studied the influence of added phosphorus ore powder on the promotion of phosphate-solubilizing by phosphate-solubilizing bacterium. The specific method refers to Example 5, where the other parameter variables remain unchanged and only the amount of phosphorite powder addition is varied. By comparing the addition of different proportions of phosphorus ore powder (the amount of phosphorus ore powder addition is the percentage by volume of the total material of magnesium slag, coal gangue, and vinegar dregs), using the strain of phosphate-solubilizing bacterium and Xanthomonas spp. synergistically, the solid waste can be modified to form a substrate for plant growth and cultivation and the parameters of the influence of phosphorus ore powder on the promotion of phosphate-solubilizing by phosphate-solubilizing bacterium can be derived. Among them, the remediation was simulated for 30 days, and the effective phosphorus content was determined. Each treatment can be averaged in triplicate.

(29) TABLE-US-00004 TABLE 4 Influence of the amount of different phosphate ore powder addition on the promotion of phosphate-solubilizing by phosphate-solubilizing bacterium Amount of phosphorus Effective Experiment ore powder addition phosphorus content No Total material volume % (mg/kg) 10 5 878.97 11 8 923.65 12 10 891.01 13 13 889.92

(30) Experiment Results: this application concludes that the addition of a certain amount of phosphorus ore powder can further promote the efficacy of the phosphate-solubilizing bacterium, which can further degrade the insoluble phosphorus in its ore powder into soluble phosphate, which can be used as a substrate together with the solid waste, and provide sufficient elements for the plant cultivation substrate. The addition of phosphate rock powder in this experiment has a significant effect on the promotion of phosphate-solubilizing by phosphate-solubilizing bacterium. With other parameters unchanged, only the amounts of phosphate rock powder additions were changed. By comparing the addition of different proportions of phosphorus ore powder (the amount of phosphorus ore powder addition is the percentage by volume of the total material of magnesium slag, coal gangue, and vinegar dregs), using the strain of phosphate-solubilizing bacterium and Xanthomonas spp. synergistically, the solid waste can be modified to form a substrate for plant growth and cultivation and the parameters of the influence of phosphorus ore powder on the promotion of phosphate-solubilizing by phosphate-solubilizing bacterium are derived. As in Experiment 11, when the amount of phosphate rock powder addition was 8%, the effect of phosphate-solubilizing was the best, and when it exceeded 8%, the effect of phosphate-solubilizing was not significantly increased. In production practice, a certain amount of phosphate rock powder can be added in combination with cost considerations to further promote the efficacy of phosphate-solubilizing bacterium.

(31) Experiment IV: Optimization Scheme for Solid Waste Combination Based on Full Bionic Simulation

(32) Experiment method: the solid waste combination based on full bionic simulation of this application, in combination with the production of organic acids by microorganisms in the process of growth and reproduction, can not only reduce the pH value in the soil environment but also directly release the phosphorus in the fixed-state phosphate into the soil. This experiment mainly studies the solid waste combination based on full bionic simulation and optimizes the process parameters. The specific method is referred to Example 6. By comparing different ratios and combinations of modified solid wastes to form a substrate for plant growth and cultivation, we calculated and measured the effective phosphorus content (mg/kg) and organic acid (glycolic acid) content (mg/kg) in the bottom solid waste layer after 60 days of transformation. Each treatment can be averaged in triplicate.

(33) TABLE-US-00005 TABLE 5 Solid waste combination optimization experiment based on full bionic simulation Kitchen Effective Oxalic waste Sludge Fly ash Water Carbon- phosphorus acid Experiment Volume Volume Volume content nitrogen Salinity content content No part part part % ratio % (mg/kg) (mg/kg) 14 100 50 30 60 35:1 20 853.21 14.87 15 100 50 50 60 35:1 20 834.02 14.33 16 100 50 10 60 35:1 20 810.35 13.43 17 100 40 10 60 35:1 20 798.03 13.59 18 100 10 20 60 35:1 20 674.25 10.83 19 100 10 40 60 35:1 20 678.02 10.00 20 100 10 50 60 35:1 20 690.34 11.01 Control 9 100 50 60 35:1 20 776.20 11.08 Control 10 100 30 60 35:1 20 650.35 10.46 Control 11 100 50 30 60 35:1 20 861.82 14.39 replaced with desulfurized ash Control 12 100 50 30 80 35:1 20 673.03 10.31 Control 13 100 50 30 40 35:1 20 653.93 10.46 Control 14 100 50 30 60 40:1 20 664.38 10.45 Control 15 100 50 30 60 25:1 20 804.23 13.01 Control 16 100 50 30 60 35:1 10 626.94 11.25 Control 17 100 50 30 60 35:1 30 796.03 12.93
Experimental Results

(34) Different parameters of full bionic simulation can effective phosphorus content and organic acid production of solid waste. Compared with Controls 9 and 10 without adding sludge or fly ash (or desulfurized ash), the effective phosphorus content of solid waste decomposed by the full bionic simulation formula of other experiments is higher. The best results were obtained when the volume ratio of kitchen waste: sludge: fly ash (or desulphurization ash) was 100:50:30. The adsorption capacity of coal gangue modified by microorganisms is very strong, and it directly releases phosphorus from the fixed-state phosphate. The content of organic acids (glycolic acid) was also highest in Experiment 14. Glycolic acid is the most representative type of organic acid and one of the important organic acids required for plant growth. By synergistically modifying the solid waste with microorganisms and a full-bionic swamp, the organic acids in the solid waste can be released, thereby promoting plant growth.

(35) During the reaction process, we found that the control of water content, salinity, and carbon-nitrogen ratio in the full bionic simulation swamp reaction is very important, and its effect on the fermentation effect of solid waste is different. After 60 days of reforming the solid waste test field, it was concluded that the highest fermentation and decomposition effect was achieved when the carbon-nitrogen ratio was adjusted to 35:1, salinity was 20%, and water content was 60%. It indicates that the phosphate-solubilizing and promotion of organic acid production in an acidic solid waste substrate environment is effective. In the process, the effective phosphorus content and acid production are both high. At the same time, the parameter could maintain the acidic environment and promote the persistent decomposition effect of microorganisms. Too high carbon-nitrogen ratio is not conducive to microbial acid production reaction, 25-35:1 is able to produce more organic acids, thus promoting the decomposition of solid waste. Too high and too low salt concentrations also affect the process of acid production. When the salt concentration is about 20%, the effect of acid production is better. The water content of biomimetic simulated swamp mixture is also an important factor affecting the microbial fermentation reaction. When the water content is 60%, the fermentation reaction of solid waste is superior.

(36) Experiment V: Optimization Scheme of Full Bionic Cover Head Combination

(37) Experiment method: the full bionic cover head combination of this application works with microorganisms to produce organic acids during growth and reproduction. Using a bionic simulation of the natural process of organic carbonite production, combined with the conditions of biofermentation for acid production, and using the carbon-nitrogen ratio, pH, and salinity in the waste liquid, acid production can be regulated. This experiment is mainly to study the combination of a full bionic cover head to optimize the conditions of process parameters. Specifically, the bionic swamp cover head was laid in the uppermost layer of the solid waste pile, and the environment was adjusted by adjusting the components of the bionic swamp cover head, so as to control the anaerobic fermentation environment of the bionic swamp mixture and solid waste in the lower layer, and to provide the most suitable anaerobic fermentation conditions. The specific method is referred to Example 6. The conditions suitable for solid waste fermentation were derived by comparing different ration combinations of cover heads in the uppermost layer of the bionic swamp mixture. Each treatment can be averaged in triplicate. After 60 days of fermentation, the ammonia nitrogen content (mg/L) in the mixture layer and the effective phosphorus content (mg/kg) in the bottommost solid waste layer were determined.

(38) TABLE-US-00006 TABLE 6 Simulation parameter optimization experiment table for full bionic cover head Mushroom Crushed Effective Straw dregs particle Ammonia phosphorus Experiment volume volume size Humidity nitrogen content No part part cm Temperature % mg/L (mg/kg) 21 3 2 3 30 60 665.61 853.21 22 3 1 3 30 60 613.43 846.38 23 1 1 3 30 60 600.38 814.29 24 1 3 3 30 60 610.24 841.53 25 2 3 3 30 60 634.01 851.28 Control 18 3 2 5 30 60 635.90 828.39 Control 19 3 2 3 40 60 528.92 736.94 Control 20 3 2 3 30 40 528.01 728.22 Control 21 3 2 3 30 80 562.35 730.26 Control 22 3 3 30 60 503.35 669.45 Control 23 2 3 30 60 525.73 673.57

(39) Experiment Results: the simulated bionic cover head can be moderately insulated and moisturized. Anaerobic fermentation conditions can be further adjusted by controlling the temperature of the cover head. Because in the anaerobic fermentation process, a lot of heat will be produced. The simulation bionic cover head can maintain a certain temperature, the temperature should be controlled to be not too high to affect the microbial fermentation. Humidity regulation is also a key factor in further maintaining the anaerobic fermentation of solid waste. Through the experiment, we found the suitable temperature and humidity affecting the fermentation of the bionic swamp mixture, that is, the results were better at 30 C. temperature and 60% humidity, and the conditioning was suitable for putrefaction and fermentation of the lower bionic swamp mixture, with ammonia nitrogen release as high as 665.61 mg/L, and effective phosphorus release from the solid waste as high as 853.21 mg/kg.

(40) The simulated bionic cover head of this application is obtained through a large number of experiments and comparisons. The optimal ratio of straw to mushroom dregs is 3:2 by volume, and the fermentation effect is optimal when the crushed particle size is 3 cm. With reference to Controls 22 and 23, the simulated bionic cover head of this application had a superior insulation and moisturizing and fermentation-promoting effect after combination compared to the simulated bionic cover head composed by adding one ingredient.

(41) While the foregoing is directed to the preferred examples of the present invention, other and further examples of the invention may be devised without departing from the basic scope thereof, and the scope thereof is determined by the claims that follow. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of this application are included within the scope of this application.