METHOD FOR ENHANCING METHANOGENESIS IN ANAEROBIC DIGESTION OF MUNICIPAL SLUDGE BY UTILIZING A FILTER SCREEN STRUCTURE

Abstract

The disclosure relates to a method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure, comprising: arranging a filter screen structure with titanium or titanium alloy as the framework and Fe.sub.3O.sub.4 as the coating in the anaerobic digestion system to accelerate the rate of hydrolysis and acidification, and increase the proportion of methane in biogas. Compared with the prior art, the disclosure increases the contact between Fe.sub.3O.sub.4 and anaerobic microorganisms by means of the screen structure; the stable crystal structure of Fe.sub.3O.sub.4 ensures the sustainability as an electron carrier while enriching electroactive microorganisms; titanium or titanium alloy, as a material with high strength, corrosion resistance, good biocompatibility, and good conductivity, can form a good match with Fe.sub.3O.sub.4 and assist in promoting the electron transfer; the disclosure has the advantages of low cost, high income, no need of repeated dosing and stable effect, and could strengthen the oxidation and decomposition of organic matter in the anaerobic digestion, accelerate the rate of methanogenesis, and increase the gas production.

Claims

1. A method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure, comprising: arranging a filter screen structure with titanium or titanium alloy as the framework and Fe.sub.3O.sub.4 as the coating in the anaerobic digestion system to accelerate the rate of hydrolysis and acidification, and increase the proportion of methane in biogas.

2. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 1, wherein the framework is a woven mesh made of titanium or titanium alloy wire, and the woven mesh has a mesh of 10-200, a wire diameter of 0.25 mm-0.5 mm, and a mesh size of 0.1 mm-2 mm.

3. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 1, wherein Fe.sub.3O.sub.4 coating is prepared by a way of micro-arc oxidation, in which water-soluble aminated Fe.sub.3O.sub.4 nanoparticles, calcium salt, phosphate salt and weak acid is used as solutes to form an electrolyte, and Fe.sub.3O.sub.4/TiO.sub.2 coating is generated on the surface of titanium or titanium alloy.

4. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 1, wherein the anaerobic digestion system has an anaerobic digestion reactor, and the filter screen structure is laid at the feed inlet of the anaerobic digestion reactor.

5. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 4, wherein the feed inlet is arranged in the middle and lower part of the anaerobic digestion reactor, and the filter screen structure is laid below the feed inlet in the anaerobic digestion reactor near the feed inlet.

6. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 4, wherein the method uses the digested sludge that operates stably in an anaerobic digestion reactor as an inoculum, and the municipal sludge as a substrate to produce methane by anaerobic fermentation under the conditions of pH=7.0, the temperature of 35-65° C., and a stirring speed of 80-120 r/min.

7. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 6, wherein the substrate is the remaining sludge in the secondary settling tank or the sludge subjected to gravity concentration and dehydration, and has a total solid content of 2% to 8%, and a volatile solid content of 51.9% to 70.8%.

8. The method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure according to claim 1, wherein the anaerobic digestion reactor is operated in batch, semi-continuous or continuous mode.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0021] FIG. 1 is a schematic diagram of an anaerobic digestion experimental device with a filter screen structure in Example 1.

[0022] FIG. 2 is a cross-sectional schematic view of section 1-1 in FIG. 1.

[0023] FIG. 3 is a graph showing the influence of different iron materials on the amount of electron transfer.

[0024] FIG. 4 shows the X-ray diffraction (XRD) spectrum of Fe.sub.3O.sub.4 before and after anaerobic treatment, wherein FIG. 4(a) shows the spectrum of Fe.sub.3O.sub.4 before anaerobic treatment, and FIG. 4(b) shows the spectrum of Fe.sub.3O.sub.4 after anaerobic treatment.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0025] FIG. 3 shows the influence of the related different iron materials on the amount of electron transfer. From top to bottom, FIG. 3 shows the influence of adding magnetite, hematite, ferrihydrite and iron atoms, and not adding above materials to the system on the amount of electron transfer. It can be seen that the experimental group with Fe.sub.3O.sub.4 added has the highest electron transfer rate, which reflects the advantages of Fe.sub.3O.sub.4 in accelerating the electron transfer rate and promoting the progress of biochemical reactions.

[0026] The present disclosure provides a method for enhancing methanogenesis in anaerobic digestion of municipal sludge by utilizing a filter screen structure, comprising: arranging a filter screen structure with titanium or titanium alloy as the framework and Fe.sub.3O.sub.4 as the coating in the anaerobic digestion system to accelerate the rate of hydrolysis and acidification, and increase the proportion of methane in biogas.

[0027] In one embodiment, the framework is a woven mesh made of titanium or titanium alloy wire, and the woven mesh has a mesh of 10-200, a wire diameter of 0.25 mm-0.5 mm, and a mesh size of 0.1 mm-2 mm.

[0028] In one embodiment, Fe.sub.3O.sub.4 coating is prepared by a method of micro-arc oxidation, in which water-soluble aminated Fe.sub.3O.sub.4 nanoparticles, calcium salt, phosphate salt and weak acid is used as solutes to form an electrolyte, and Fe.sub.3O.sub.4/TiO.sub.2 coating is generated on the surface of titanium or titanium alloy.

[0029] In one embodiment, the anaerobic digestion system has an anaerobic digestion reactor, and the filter screen structure is laid at the feed inlet of the anaerobic digestion reactor.

[0030] In one embodiment, the feed inlet is arranged in the middle and lower part of the anaerobic digestion reactor, and the filter screen structure is laid below the feed inlet in the anaerobic digestion reactor near the feed inlet.

[0031] In one embodiment, the method uses the digested sludge that operates stably in an anaerobic digestion reactor as an inoculum, and the municipal sludge as a substrate to produce methane by anaerobic fermentation under the conditions of pH=7.0, the temperature of 35-65° C., and a stirring speed of 80-120 r/min.

[0032] In one embodiment, the substrate is the remaining sludge in the secondary settling tank or the sludge subjected to gravity concentration and dehydration, and has a total solid (Total Solid, TS) content of 2% to 8%, and a volatile solid (Volatile Solid, VS) content of 51.9% to 70.8%.

[0033] In one embodiment, the anaerobic digestion reactor is operated in batch, semi-continuous or continuous mode.

[0034] The present disclosure will be described in detail below with reference to the drawings and specific examples.

Example 1

[0035] In the batch methanogenesis experiment, a method for enhancing methanogenesis in anaerobic digestion of municipal sludge was implemented. The remaining sludge in the secondary settling tank (VS=51.9%-70.8%, TS=1.8%-5.1%) was used as the substrate, and the anaerobic digestion sludge in the reactor that operates stably (VS=35.6%-47.9%, TS=2.5%-5.2%) was used as inoculation mud. A batch methanogenesis experiment was performed in a 500 mL serum bottle. The experimental device was shown in FIG. 1. The cross-sectional schematic view of section 1-1 in FIG. 1 was shown in FIG. 2. It can be seen from FIG. 2 that in this example, four brackets were provided along the circumferential direction on the side wall of the serum bottle to support the filter screen structure (the shaded part in FIG. 2), the feed tube was inserted from the upper part of the serum bottle and the feed inlet extended into the serum bottle.

[0036] In an experimental group, a filter screen structure with titanium mesh as the framework and Fe.sub.3O.sub.4 as the coating was placed in the middle of the serum bottle, while in a control group, a filter screen structure was not equipped, and at the same time a blank group was set to eliminate the influence of the inoculated mud. The experiment was carried out in a shaker in an air bath with the temperature of 37-55° C. at a speed rate of 80-120 r/min During the experiment, the gas production and ratio were monitored, and before and after anaerobic digestion, the TS and VS were measured.

[0037] Compared with the control group in this example, the experimental group with a titanium mesh coated with Fe.sub.3O.sub.4 increased the gas production rate of the system and reached the maximum gas production at 13 days (the control group was 17 days), increased the proportion of methane gas in gas production from 63% to more than 75%, accelerated the rate of hydrolysis and acidification effectively, and increased the proportion of methane.

Example 2

[0038] In the semi-continuous methanogenesis experiment, a method for enhancing methanogenesis in anaerobic digestion of municipal sludge was implemented. The sludge subjected to gravity concentration (VS=51.9%-70.8%, TS=3.8%-5.1%) was used as the substrate, and the anaerobic digestion sludge in the reactor that operates stably (VS=35.6%-47.9%, TS=2.5%-5.2%) was used as inoculation mud. A semi-continuous methanogenesis experiment was performed in a reactor with a working volume of 2 L.

[0039] In an experimental group, a filter screen structure with titanium mesh as the framework and Fe.sub.3O.sub.4 as the coating was placed at the 0.5 L position (near the feed inlet) of the reactor, while in a control group, a filter screen structure was not equipped. The semi-continuous reactors of the experimental group and the control group were first added with 2 L of inoculum mud, and were operated under the following conditions: 200 mL feeding and 200 mL outgoing per day, and SRT=10 d. The reactors were heated by a water bath with the temperature of 37-55° C., while being stirred at a rate of 80-120 r/min, and the stirring is stopped for 1 minute every 1 minute. During the experiment, the contents of TS, VS, and VFA (volatile fatty acids) of the feeding and outgoing materials were monitored, and the gas production and ratio were determined.

[0040] Compared with the control group in this example, the experimental group with a semi-continuous reactor with a filter screen structure had a shortened start-up time, accelerated the rate of methanogenesis of 18.4%, had no accumulated VFA, increased the proportion of methane in the gas production from 65% to 78%, and maintained stable operation.

Example 3

[0041] In the continuous methanogenesis experiment, a method for enhancing methanogenesis in anaerobic digestion of municipal sludge was implemented.

[0042] The remaining sludge in the secondary settling tank (VS=51.9%-70.8%, TS=1.8%-5.1%) was used as the substrate, and the anaerobic digestion sludge in the reactor that operates stably (VS=35.6%-47.9%, TS=2.5%-5.2%) was used as inoculation mud. A continuous methanogenesis experiment was performed in a reactor with a working volume of 4 L.

[0043] In an experimental group, a filter screen structure with titanium mesh as the framework and Fe.sub.3O.sub.4 as the coating was placed at the 0.8 L position (near the feed inlet) of the reactor, while in a control group, a filter screen structure was not equipped. The semi-continuous reactors of the experimental group and the control group were first added with 4 L of inoculum mud, and started up by continuous feeding and outgoing, with SRT=20d. The reactor were heated by a water bath with the temperature of 37-55° C., while being stirred at a rate of 80-120 r/min, and the stirring is stopped for 2 minute every 1 minute. During the experiment, the contents of TS, VS, and VFA in the feeding and outgoing materials were monitored, and the gas production and ratio were determined.

[0044] Compared with the control group in this example, the experimental group had been successfully started up in the first SRT, while the accumulated VFA appeared in the control group. The experimental group showed stronger adaptability and recovered to stability faster than the control group when the two reactors were operating stably and under reducing the SRT from 20d to 15d and then further reducing to 10d. It has been proved that the reactor equipped with the filter screen with the titanium mesh as the framework and Fe.sub.3O.sub.4 as the coating has a stable operation effect.

[0045] The X-ray diffraction (XRD) spectrum of Fe.sub.3O.sub.4 before and after anaerobic treatment was shown in FIG. 4. Comparing FIG. 4(a) and FIG. 4(b), it can be seen that the crystal form of Fe.sub.3O.sub.4 remains well before and after the reaction, showing that it is stable in physico-chemical property and can be reused.

[0046] The foregoing description for the embodiments is to facilitate the understanding and use of the present disclosure by those skilled in the art. Those skilled in the art can obviously make various modifications to these embodiments and apply the general principles described herein to other embodiments without creative work. Therefore, the present disclosure is not limited to the above-mentioned embodiments. According to the content of the present disclosure, all improvements and modifications made by those skilled in the art without departing from the scope of the present disclosure should fall within the protection scope of the present disclosure.