CN204644347U - Compound material secondary high-temperature anaerobic fermentation efficiently prepares the device of biogas - Google Patents
Compound material secondary high-temperature anaerobic fermentation efficiently prepares the device of biogas Download PDFInfo
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- CN204644347U CN204644347U CN201520096867.1U CN201520096867U CN204644347U CN 204644347 U CN204644347 U CN 204644347U CN 201520096867 U CN201520096867 U CN 201520096867U CN 204644347 U CN204644347 U CN 204644347U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
The utility model discloses the device that a kind of compound material secondary high-temperature anaerobic fermentation efficiently prepares biogas, this device comprises: first, second one-level anaerobically fermenting; First one-level anaerobic fermentation tank connects First Heat Exchanger one end, and the other end of First Heat Exchanger connects the first one-level anaerobic fermentation tank and B grade anaerobic fermentation tank respectively; Second one-level anaerobic fermentation tank connects second interchanger one end, and the other end of the second interchanger connects the second one-level anaerobic fermentation tank and B grade anaerobic fermentation tank respectively; B grade anaerobic fermentation tank is provided with biogas interfacing conveyor.The method comprises: (1) is by Classification of materials; (2) respectively pre-treatment is carried out to the material of classification; (3) coagulation material and second-stage treatment material is prepared; (4) send into B grade anaerobic fermentation tank and reflux; (5) biogas that B grade anaerobic fermentation tank produces is collected.It is stable, strong to the tolerance of ammonia nitrogen, soda acid and VFA (VFA) that the utility model has device long-time running, the advantage that factor of created gase is high.
Description
Technical field
The utility model relates to biogas preparation field, is specifically related to the device that a kind of compound material secondary high-temperature anaerobic fermentation efficiently prepares biogas.
Background technology
City and countryside wastes are important source of pollution, polluted-water, soil and air.China's stream pollution 60% derives from livestock feces of livestock and poultry, and environmental improvement is very urgent.Owing to adopting conventional environmental protection treatment means to be investments of a negative benefit, bring huge burden to government.Adopt utilization of waste material resource utilization mode, no matter existing technology is the production of solid fertilizer or the utilization of biogas, all cannot realize real industrialization because rate of return on investment is low.
China utilizes the technology: history of anaerobically fermenting generation biogas long.At the end of 2010 (the Ministry of Agriculture's statistic data), China process agricultural wastes biogas engineering quantity reached 3556, but the benefit of its project scale and generation and World Developed Countries gap huge.Principal feature is that project scale is little, and pond holds at 1000m
3above biogas engineering only accounts for 9%, and biogas ultimate production only has 17.6% of Germany, and year marsh gas power generation amount is 0.16% of Germany.The biogas engineering of China's process agricultural organic waste is due to relative small scale, again away from cities and towns, the biogas produced only has on a small quantity that (marsh gas power generation gas consumption only accounts for about 2.53% of total gas production for generating and central gas supply, central gas supply amount is less than 1% of total gas production), a large amount of biogas only for production, the life of plant self, does not realize industrialization.Municipal wastes is as changing food waste simultaneously, although municipal sludge etc. have the process of country subsidy, still construction project shortage economic benefit cannot industrialization.
In recent years, many companies have been had to be engaged in the design of the rural culture industry refuse large-sized biogas engineering that is raw material for raw material or changing food waste, construction and construction at home.Its general nature technically adopts mesophilic digestion technology, adopts high-temperature technology extremely individually, adopts single material in the majority, also has small part to adopt multiple compound material, large-sized biogas engineering design gas deliverability about 20,000 sides, half that actual gas deliverability is not enough.The aerogenesis scale of engineering is at 5000m
3/ below d is in the majority.Engineer equipment level is lower, and volume aerogenesis load best level is at 1-1.5m
3/ m
3.d, the biogas of generation prepares bio-natural gas, and because gas deliverability is low, construction investment return ability, cannot form marketing development.
Treatment method changing rejected material to useful resource of the prior art is a lot, and it is most popular technology that anaerobically fermenting prepares biogas, this process characteristic:
1, material source comprises the materials such as feces of livestock and poultry, stalk, changing food waste, municipal sludge, industrial waste.
2, the function of collection and preprocessing part is the centralized collection to material, and material is pulverized by the materials such as impurity such as stone, sand, plastics, tree root in pretreated effect removal material simultaneously.
3, the pretreated material of one-level product pump functional promotion enters one grade fermemtation tank.
4, one grade fermemtation tank adopts intermediate temperature anaerobic fermentation technology, temperature controls 35-45 DEG C or high-temperature anaerobic fermentation technology, and temperature controls at 52-55 DEG C, and fermentor tank adopts the full mixed anaerobic fermentor tank of overhead, establish in tank body around water pipe for heating, the water conservancy residence time is 15-20 days.One-level anaerobic fermentation tank is material main fermentation tank, and most of biogas produces and is transported into second order fermentation tank.
5, after the fermentation of secondary product pump conveying one grade fermemtation tank, material enters B grade anaerobic fermentation tank.
6, B grade anaerobic fermentation tank adopts the complete mixed fermentor tank stirred bottom the formula film of top, and the water conservancy residence time is 3-5 days, and major function comprises two portions, and first: gas can be collected as gas storage holder; Second: material is fully fermented further.
7, the natural pond liquid completely that ferments is transported to natural pond liquid processing unit by natural pond liquid pump.
8, hot water boiler provides circulating hot water to be connected with hot water sleeve pipe in fermentor tank to heat to fermentor tank, ensure high temperature in pond.
There is following shortcoming in prior art:
1, material is not classified and is carried out pretreatment unit together, strengthens difficulty because material properties is different to pre-treatment.
2, mixture enters one grade fermemtation tank together, the residence time is 15-20 days, one grade fermemtation tank is system main fermentation tank, anaerobically fermenting is divided into product acid phase and methane phase stage, because the composition of various material is different, the lag time in acidication stage is very large, the hydrolytic acidification time of such as pig manure only need 3 days just can and the acidication demands 5 days of changing food waste, carcass acidication phases-time is longer, so mixture is hydrolyzed, acidifying can cause material probability of becoming sour to be increased, even single material reduces owing to producing acid phase PH, the optimum environment in methane phase stage is the most applicable under weak basic condition simultaneously, so the growth of methanogen can be suppressed, greatly affect gas producing efficiency, simultaneously the sour environment that needs of acidication section and time also can not fully can complete due to the interference of methane phase section, the insufficient of acidication section also can reduce methanogenic efficiency.
3, the residence time of B grade anaerobic fermentation tank is 3-5 days, and this part mainly bears the collection of fermentation residual air and the effect as biogas storage cabinet, does not have promoter action to fermentation overall process.
4, fermentor tank establishes ring-type circulating pipe to ensure the temperature of fermentor tank in adopting, and the hot water line of fermentor tank fouling can cause heat by conduction reduced capability, and long-time running needs to add Iarge-scale system heat supplied, if keeped in repair, the necessary shutdown system of cleaning fouling, tank body empties and just can complete, and maintenance cost is high.
5, the second order fermentation system aerogenesis load of this kind of form is low, anti-ammonia nitrogen, pH and voltaile fatty acid ability, and system is very easy to acidifying fluctuation of service, is on duty mutually especially for fatty and that protein content is high material processing power.
Utility model content
Provide hereinafter about brief overview of the present utility model, to provide about the basic comprehension in some of the present utility model.Should be appreciated that this general introduction is not summarize about exhaustive of the present utility model.It is not that intention determines key of the present utility model or integral part, neither intended limitation scope of the present utility model.Its object is only provide some concept in simplified form, in this, as the preorder in greater detail discussed after a while.
The object of the utility model embodiment is the defect for above-mentioned prior art, provides a kind of stable, anti-pH, ammonia nitrogen and voltaile fatty acid ability is strong and factor of created gase is high compound material secondary high-temperature anaerobic fermentation efficiently to prepare the device of biogas.
To achieve these goals, the technical scheme that the utility model is taked is:
Anaerobically fermenting prepares a device for biogas, comprising: the first one-level anaerobic fermentation tank and the second one-level anaerobic fermentation tank;
Described first one-level anaerobic fermentation tank connects First Heat Exchanger one end, and the other end of described First Heat Exchanger connects the first one-level anaerobic fermentation tank and B grade anaerobic fermentation tank respectively;
Described second one-level anaerobic fermentation tank connects second interchanger one end, and the other end of described second interchanger connects the second one-level anaerobic fermentation tank and B grade anaerobic fermentation tank respectively;
Described B grade anaerobic fermentation tank is provided with biogas interfacing conveyor.
The utility model also provides a kind of anaerobically fermenting to prepare the method for biogas, comprises the following steps:
(1) material is divided into two classes:
First kind material is the refuse be fermented;
Equations of The Second Kind material is not by the product of anaerobically fermenting;
(2) respectively pre-treatment is carried out to the material of classification;
(3) first kind material after pretreatment enters the first one-level anaerobic fermentation tank, the temperature controlled in the first one-level anaerobic fermentation tank arrives preset temp, and turn on agitator stirs, and stops for first scheduled time, then through First Heat Exchanger heating, coagulation material is obtained;
Equations of The Second Kind material after pretreatment enters the second one-level anaerobic fermentation tank, the temperature controlled in the second one-level anaerobic fermentation tank arrives preset temp, and turn on agitator stirs, and stops for second scheduled time, then through the second interchanger heating, second-stage treatment material is obtained;
(4) coagulation material sends into B grade anaerobic fermentation tank with predetermined feed time, and then with predetermined return time, mass transport is returned the first one-level anaerobic fermentation tank; Described predetermined feed time and predetermined return time hocket;
Second-stage treatment material sends into B grade anaerobic fermentation tank with predetermined feed time, and then with predetermined return time, mass transport is returned the second one-level anaerobic fermentation tank;
Described predetermined feed time and predetermined return time hocket;
(5) material in B grade anaerobic fermentation tank is stirred, and the temperature controlled in B grade anaerobic fermentation tank and the water conservancy residence time, collect the biogas that B grade anaerobic fermentation tank produces.
Preferably, the preset temp of described first one-level anaerobic fermentation tank is 40-50 DEG C, and the preset temp of described second one-level anaerobic fermentation tank is 50-55 DEG C, and described first scheduled time is 2-5 days, and described second scheduled time is 5-10 days.First scheduled time be described first kind material in the first one grade fermemtation tank water conservancy residence time, described second scheduled time is that Equations of The Second Kind material is in the second one grade fermemtation tank water conservancy residence time.
Preferably, the predetermined feed time of described coagulation material is 15-20 minute, and the predetermined return time passing back into the first one-level anaerobic fermentation tank is 15-20 minute; The predetermined feed time of described second-stage treatment material is 30-45 minute, and the predetermined return time passing back into the second one-level anaerobic fermentation tank is 30-45 minute;
And/or;
Temperature in described B grade anaerobic fermentation tank is 52-55 DEG C, and the water conservancy residence time is 15-20 days; Temperature control change every day of described B grade anaerobic fermentation tank is positive and negative is less than 1 DEG C.
Preferably, the first kind material industrial waste that comprises excrement of animals and fermented; Described Equations of The Second Kind material comprises sick dead pig, butchers refuse, changing food waste, municipal sludge and other industrial wastes.
Preferably, the biogas that B grade anaerobic fermentation tank produces enters subsequent disposal through Cemented filling, for generating electricity or being bio-natural gas by biogas purifying.
Compared with prior art, the beneficial effects of the utility model are:
The utility model is based on the biogas engineering of industrialized level, and project scale is not less than daily output biogas 2 ten thousand stere.Technique aerogenesis load of the present utility model is high, and volumetric loading is 2-3 times of present domestic best level.Adopt compound material high-temperature anaerobic fermentation technology of the present utility model, the investor of engineering and operator can be made to obtain investment repayment fast, environment protection treating project is become energy plant, realize the industrialized development of bio-natural gas.It is stable, strong to the tolerance of ammonia nitrogen, soda acid and VFA (VFA) that the utility model has device long-time running, the advantage that factor of created gase is high.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 prepares the structural representation of the device of biogas for anaerobically fermenting that the utility model embodiment provides.
Reference numeral:
1.1-first one-level anaerobic fermentation tank, 1.2-First Heat Exchanger, 1.3-first one-level product pump, 1.4-first crusher, 1.5-first secondary product pump;
2.1-second one-level anaerobic fermentation tank, 2.2-second interchanger, 2.3-second one-level product pump, 2.4-second crusher, 2.5-second secondary product pump;
3-B grade anaerobic fermentation tank;
4-hot water boiler;
5-natural pond liquid pump;
6-agitator.
Embodiment
For making the object of the utility model embodiment, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in the utility model embodiment, technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.The element described in an accompanying drawing of the present utility model or a kind of embodiment and feature can combine with the element shown in one or more other accompanying drawing or embodiment and feature.It should be noted that for purposes of clarity, accompanying drawing and eliminate expression and the description of parts that have nothing to do with the utility model, known to persons of ordinary skill in the art and process in illustrating.Based on the embodiment in the utility model, those of ordinary skill in the art are not paying the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
See Fig. 1, a kind of compound material secondary high-temperature anaerobic fermentation efficiently prepares the device of biogas, comprising: the first one-level anaerobic fermentation tank 1.1 and the second one-level anaerobic fermentation tank 2.1;
First one-level anaerobic fermentation tank 1.1 connects First Heat Exchanger 1.2 one end, and the other end of First Heat Exchanger 1.2 connects the first one-level anaerobic fermentation tank 1.1 and B grade anaerobic fermentation tank 3 respectively;
Second one-level anaerobic fermentation tank 2.1 connects second interchanger 2.2 one end, and the other end of the second interchanger 2.2 connects the second one-level anaerobic fermentation tank 2.1 and B grade anaerobic fermentation tank 3 respectively;
B grade anaerobic fermentation tank 3 is provided with biogas interfacing conveyor.
Anaerobically fermenting of the present utility model is adopted to prepare the device of biogas, to classification modulation and the acidication of compound material, especially to Equations of The Second Kind material, due to protein and lipid content high, need to obtain sufficient acidication and hydrolysis of organic matter be amino acid, glycerine and lipid acid thus be hydrolyzed to the fermentation that small-molecule substance is conducive to next step further.Improve the factor of created gase of anaerobically fermenting.
Preferably, the first one-level anaerobic fermentation tank 1.1 connects the first one-level product pump 1.3, first one-level anaerobic fermentation tank 1.1 and connects by the first crusher 1.4 one end that first secondary product pump 1.5, first secondary product pump 1.5 connects First Heat Exchanger 1.2;
Second one-level anaerobic fermentation tank 2.1 connects the second one-level product pump 2.3, second one-level anaerobic fermentation tank 2.1 and connects by the second crusher 2.4 one end that second secondary product pump 2.5, second secondary product pump 2.5 connects the second interchanger 2.2.
Also consider before the charging of secondary product pump that arranging crusher makes material fully pulverize further, guarantee fully contacting of material and fermentative microflora, secondary product pump runs in sequential fed mode, in non-feed time section, secondary product pump considers that Matter Transfer returns one grade fermemtation tank, be fed into B grade anaerobic fermentation tank in feed time section by secondary product pump, guarantee that one-level and B grade anaerobic fermentation tank keep the temperature of tank body by heated material by this kind of mode.
Preferably, First Heat Exchanger 1.2 and the second interchanger 2.2 are tubular heat exchanger, and First Heat Exchanger 1.2 is connected hot water boiler 4 respectively with the second interchanger 2.2.
The utility model adopts the external heat system of fermentor tank, by tubular heat exchanger to heating material, traditional fermentor tank establishes ring-type circulating pipe to ensure the temperature of fermentor tank in adopting, the hot water line of fermentor tank fouling can cause heat by conduction reduced capability, long-time running needs to add Iarge-scale system heat supplied, if keeped in repair, the necessary shutdown system of cleaning fouling, tank body empties and just can complete, maintenance cost is high, adopt external heat system, material is heated by tubular heat exchanger, by adding the temperature that hot feed keeps in fermentor tank.The easy to clean of tubular heat exchanger considers tubular heat exchanger for subsequent use simultaneously, and during system maintenance maintenance, system still can normally be run.
Preferably, B grade anaerobic fermentation tank 3 is also connected with natural pond liquid pump 5, and natural pond liquid pump 5 is for being transported to natural pond liquid processing unit by the natural pond liquid completely that ferments.
Preferably, the first one-level anaerobic fermentation tank 1.1, second one-level anaerobic fermentation tank 2.1 and B grade anaerobic fermentation tank 3 include the agitator 6 being arranged on tank body top.
The utility model is by sequential fed and discharge method, and the start-stop of the same frequency of adjoint agitator can increase the capacity of resisting impact load of fermentor tank simultaneously, and with fermentative microflora sufficient reacting, system cloud gray model is more sane.
Below by specific embodiment, the method that anaerobically fermenting of the present utility model prepares biogas is further detailed:
Embodiment 1
The utility model also provides a kind of anaerobically fermenting to prepare the method for biogas, comprises the following steps:
See Fig. 1, material is divided into two classes by (1), and whether material is according to being that refuse after fermentation is divided into two large classes:
First kind material is the refuse be fermented; For cow dung+pig manure, this material is owing to have passed through anaerobic digestion, so material is hydrolyzed by force and easily again to the surge capability of soda acid.
Equations of The Second Kind material is not by the product of anaerobically fermenting; Be specially changing food waste;
(2) respectively pre-treatment is carried out to the material of classification:
First kind material is transported to material storage pond through tank car and is removed sandstone, wooden unit, plastics etc. in material through pre-processing devices such as grid, crusher, settling pits, and the equipment of preprocessing part is determined according to practical situation.
Equations of The Second Kind material is transported to material storage pond through tank car and is removed sandstone, wooden unit, plastics etc. in material through pre-processing devices such as grid, separator, crusher, settling pits, and the equipment of preprocessing part is determined according to the concrete material situation in engineering.
(3) first kind material after pretreatment is promoted by the first one-level product pump 1.3 and enters the second one-level anaerobic fermentation tank 1.1, control temperature in the first one-level anaerobic fermentation tank 1.1 within the scope of 45-55 DEG C, and agitator stirs, stop 3 days in the first one-level anaerobic fermentation tank 1.1, then broken through the first crusher 1.4, be transported to First Heat Exchanger 1.2 through the first secondary product pump 1.5 again to heat, obtain coagulation material;
Equations of The Second Kind material second one-level product pump 2.3 after pretreatment promotes and enters the second one-level anaerobic fermentation tank 2.1, control temperature in the second one-level anaerobic fermentation tank 2.1 within the scope of 50-55 DEG C, and agitator stirs, stop 6 days in the second one-level anaerobic fermentation tank 1.1, then broken through the second crusher 2.4, be transported to the second interchanger 2.2 through the second secondary product pump 2.5 again to heat, obtain second-stage treatment material;
First one-level anaerobic fermentation tank of the present utility model and the second one-level anaerobic fermentation tank are provided with the full mixed fermentation tank of top formula agitator, the function of one-level anaerobic fermentation tank plays the effect of modulation and acidication to material, the acidication of material completes in one-level anaerobic fermentation tank, first kind material is the raw material be fermented, hydrolytic acidification time requires short, material itself has the good surge capability pH value to soda acid in acidication stage pH value at 6-7, does not produce excessive pH impact to follow-up B grade anaerobic fermentation.Equations of The Second Kind material is the material be not fermented, and after acidication, pH drops to 3-5, and the sugar in material, fat and protein can be broken down into amino acid, glycerine and lipid acid thus be hydrolyzed to the fermentation that small-molecule substance is conducive to next step further.First kind material after modulation and acidifying and Equations of The Second Kind material promote through crusher and tubular heat exchanger through secondary product pump, heating material are met high temperature anaerobic temperature condition and enter B grade anaerobic fermentation tank.
(4) first material handlings send into B grade anaerobic fermentation tank with predetermined feed time, and predetermined feed time is 15 minutes, and then with predetermined return time, mass transport is returned the first one-level anaerobic fermentation tank 1.1, and predetermined return time is 15 minutes; Described predetermined feed time and predetermined return time hocket; Namely send into B grade anaerobic fermentation tank 3 and be back to the second one-level anaerobic fermentation tank 1.1 and hocket;
Second material handling sends into B grade anaerobic fermentation tank with predetermined feed time, and predetermined feed time is 30 minutes, and then with predetermined return time, mass transport is returned the second one-level anaerobic fermentation tank 2.1, and predetermined return time is 30 minutes; Similarly, described predetermined feed time and predetermined return time hocket; Namely send into B grade anaerobic fermentation tank and be back to the second one-level anaerobic fermentation tank 2.1 and hocket;
Secondary product pump of the present utility model adopts sequential fed mode, first material handling was that feed time sends into B grade anaerobic fermentation tank by the first secondary product pump with 15 minutes, within 15 minutes subsequently, by the first secondary product pump, mass transport is returned the first one-level anaerobic fermentation tank for return time, time-interleavedly to carry out.Second material handling also adopts sequential fed mode, and feeding manner is identical with the first material handling mode, and the second material handling charging and circulation feed back time are respectively 30 minutes.
(5) material in B grade anaerobic fermentation tank 3 is stirred, and the temperature controlled in B grade anaerobic fermentation tank 3 is 52 DEG C and the water conservancy residence time is 15 days, collects the biogas that B grade anaerobic fermentation tank 3 produces.
The biogas that B grade anaerobic fermentation tank produces enters subsequent disposal through Cemented filling, for generating electricity or being bio-natural gas by biogas purifying.
Agitator in B grade anaerobic fermentation tank makes material fully mix in fermentor tank, it is main aerogenesis unit, in tank, pH is the optimal ph environment in methane phase stage at 7-9, the methane phase stage of material completes at this, the charging separating B grade anaerobic fermentation tank simultaneously due to acidication and methane phase stage completely adopts sequence batch (, every day, inlet amount was very little compared with the tank volume of second order fermentation tank, be less than 1/15th of the volume of B grade anaerobic fermentation tank, so very little to the impact load of reactor, can ensure that anaerobic fermentation tank does not produce to become sour, the operation of long-term efficient stable.
The utility model is classified according to different materials, sends into fermentor tank and ferment after reaching good pretreating effect.
Material is divided into two large classes to carry out each self-modulation and acidication respectively, one-level anaerobically fermenting major function comprises two aspects, one is the modulating action to material, two is that the Hydrolysis Acidification of material completes at one grade fermemtation tank, because acidication section is completely independently, material can be made like this to obtain best acidulated condition, material is divided into two large classes according to different in kind, can arrange the water conservancy residence time according to material different properties makes acidication abundant, can play sufficient acidication especially to fat and the high material of protein content.
B grade anaerobic fermentation tank is entered by the mode material of intermittent feeding, B grade anaerobic fermentation is based on the methane phase stage, due to charging be interval a small amount of be small to the volume impulse of B grade anaerobic fermentation tank, so the optimum condition environment of methane phase section fully can be ensured, make B grade anaerobic fermentation stable, aerogenesis load is high, and the volume aerogenesis load of this technology is 2-3 times of domestic existing best level.
One-level anaerobic fermentation tank of the present utility model and B grade anaerobic fermentation tank all adopt tank external heating mode, are kept the temperature of fermentor tank by the mode of tubular heat exchanger heated material.One grade fermemtation tank temperature controls in scope of design, and B grade anaerobic fermentation tank temperature controls at 52-55 DEG C, and every day, temperature variation was positive and negatively less than 1 DEG C.
Embodiment 2
Substantially the same manner as Example 1, difference is: first kind material is cow dung+chicken manure, and Equations of The Second Kind material is carcass and butchers refuse, stops 4 days in the first one-level anaerobic fermentation tank, stops 8 days in the second one-level anaerobic fermentation tank.
It is 15 minutes that predetermined first kind material feeding enters the B grade anaerobic fermentation tank time, and predetermined return time is 15 minutes; It is 45 minutes that predetermined Equations of The Second Kind material feeding enters the B grade anaerobic fermentation tank time, and predetermined return time is 45 minutes;
Temperature in B grade anaerobic fermentation tank is 52 DEG C, and the water conservancy residence time is 18 days, and B grade anaerobic fermentation tank temperature variation every day is positive and negative is less than 1 DEG C.
Embodiment 3
Substantially the same manner as Example 1, difference is: first kind material is pig manure, and Equations of The Second Kind material is municipal sludge.Stop 2 days in the first one-level anaerobic fermentation tank, stop 10 days in the second one-level anaerobic fermentation tank.
It is 20 minutes that predetermined first kind material feeding enters the B grade anaerobic fermentation tank time, and predetermined return time is 20 minutes; It is 45 minutes that predetermined Equations of The Second Kind material feeding enters the B grade anaerobic fermentation tank time, and predetermined return time is 45 minutes;
Temperature in B grade anaerobic fermentation tank is 52 DEG C, and the water conservancy residence time is 20 days, to control in B grade anaerobic fermentation tank every day temperature variation at positive and negative 1 DEG C.
Below by a concrete embodiment, effect of the present utility model is described:
Realize production and the benign ecological cycles of mass-producing pig-breeding industry, must environment protection be done well.The reasonable disposal and utilization of ight soil, corpse and sewage is the key link of environmental protection.Utilize the biogas engineering of anaerobic fermentation technology of the present utility model, pollutent can be processed, kill sick body microorganism wherein and parasite, make again plant area's water quality not contaminated, the growth for live pig provides good living environment, realizes large scale of pig farm.The biogas simultaneously produced can generate electricity as the renewable energy resources or carry out purification bio-natural gas by selling generating or Sweet natural gas realizes the investment repayment of project to biogas.
1, design considerations
Pig manure: 800 tons/day (TS=17%);
Pig corpse: 20 tons/day.
2, other design considerations
Transportation cost: pig manure per ton 20 yuan, every dead pig 20 yuan (in 30 kilometer radius);
Cost of land: 150,000/mu;
Concentrated organic fertilizer selling price: free, not as income;
Sweet natural gas CNG selling price: 4.0 yuan/cube;
Handling dead pig is subsidized: 80 yuan/head;
Ight soil acquisition cost: 40 yuan/ton.
3, technical process is see Fig. 1.
4, design variable
| Title | Biogas engineering |
| Fermentation raw material 1 (ton/sky) | Pig manure (800 tons) |
| Fermentation raw material 2 (pig corpse, ton/sky) | 20 |
| Zymotechnique | Secondary high-temperature anaerobic fermentation |
| Fermentation vat holds (cubic meter) | 30000 |
| The volumetric loading (m3/m3.d) of fermentation | 2.67 |
| Engineering aerogenesis scale (biogas cubic meter/sky) | 80000 |
| Concentrated organic fertilizer (ton/sky) | 200 tons |
| For heat energy (biogas cubic meter/sky) needed for system heating | 10000 |
| Bio-natural gas output (cubic meter/sky) | 38500 |
| Floor space (mu) | 30 mu |
| Total installed capacity | 1600KW |
| The electricity charge (unit/degree) | 0.8 |
| Bio-natural gas selling price (unit/cubic meter) | 4.0 |
| Concentrated organic fertilizer price (yuan/ton) | Use without compensation |
5. economic analysis
5.1 transportation cost economic analysis
| Title | Biogas engineering |
| Fermentation raw material (ton/sky) | Pig manure (800 tons) |
| Pig corpse treatment capacity (head/sky) | 800 |
| Pig manure transportation cost (unit/sky) | 1.6 ten thousand |
| Pig corpse transportation cost (unit/sky) | 2.4 ten thousand |
| Pig fiscal subsidy (unit/sky) | 6.4 ten thousand |
| Ight soil acquisition cost (unit/sky) | 3.2 ten thousand |
| Profit every day (unit) | 0.2 ten thousand |
Note: government completely for the collection of ight soil and dead pig, makes up the transportation cost of dead pig and ight soil, so transportation cost can be ignored in economic analysis to the fiscal subsidy of dead pig.
5.2 economic analysis summary tables
This project does not consider any subsidy, runs based on perfect marketization.
6, technology of the present utility model compared with the prior art
In the utility model the various embodiments described above, the sequence number of embodiment is only convenient to describe, and does not represent the quality of embodiment.The description of each embodiment is all emphasized particularly on different fields, in certain embodiment, there is no the part described in detail, can see the associated description of other embodiments.
In the embodiments such as apparatus and method of the present utility model, obviously, each parts or each step reconfigure after can decomposing, combine and/or decomposing.These decompose and/or reconfigure and should be considered as equivalents of the present utility model.Simultaneously, in the description above to the utility model specific embodiment, the feature described for a kind of embodiment and/or illustrate can use in one or more other embodiment in same or similar mode, combined with the feature in other embodiment, or substitute the feature in other embodiment.
Should emphasize, term " comprises/comprises " existence referring to feature, key element, step or assembly when using herein, but does not get rid of the existence or additional of one or more further feature, key element, step or assembly.
Although last it is noted that described the utility model and advantage thereof in detail above, be to be understood that and can carry out various change when not exceeding the spirit and scope of the present utility model limited by appended claim, substituting and converting.And scope of the present utility model is not limited only to the specific embodiment of process, equipment, means, method and step described by specification sheets.One of ordinary skilled in the art will readily appreciate that from disclosure of the present utility model, can use perform the function substantially identical with corresponding embodiment described herein or obtain and its substantially identical result, existing and that will be developed in the future process, equipment, means, method or step according to the utility model.Therefore, appended claim is intended to comprise such process, equipment, means, method or step in their scope.
Claims (5)
1. compound material secondary high-temperature anaerobic fermentation efficiently prepares a device for biogas, it is characterized in that, comprising: the first one-level anaerobic fermentation tank and the second one-level anaerobic fermentation tank;
Described first one-level anaerobic fermentation tank connects First Heat Exchanger one end, and the other end of described First Heat Exchanger connects the first one-level anaerobic fermentation tank and B grade anaerobic fermentation tank respectively;
Described second one-level anaerobic fermentation tank connects second interchanger one end, and the other end of described second interchanger connects the second one-level anaerobic fermentation tank and B grade anaerobic fermentation tank respectively;
Described B grade anaerobic fermentation tank is provided with biogas interfacing conveyor.
2. device according to claim 1, it is characterized in that, described first one-level anaerobic fermentation tank connects the first one-level product pump, and described first one-level anaerobic fermentation tank connects the first secondary product pump by the first crusher, and described first secondary product pump connects one end of described First Heat Exchanger;
Described second one-level anaerobic fermentation tank connects the second one-level product pump, and described second one-level anaerobic fermentation tank connects the second secondary product pump by the second crusher, and described second secondary product pump connects one end of described second interchanger.
3. device according to claim 1, is characterized in that, first and second interchanger described is tubular heat exchanger, and first and second interchanger described connects hot water boiler respectively.
4. device according to claim 1, is characterized in that, described B grade anaerobic fermentation tank is also connected with natural pond liquid pump, and described natural pond liquid pump is used for the natural pond liquid completely that ferments to be transported to natural pond liquid processing unit.
5. the device according to any one of claim 1-4, is characterized in that, described first one-level anaerobic fermentation tank, the second one-level anaerobic fermentation tank and B grade anaerobic fermentation tank include the agitator being arranged on tank body top.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105907800A (en) * | 2016-06-28 | 2016-08-31 | 农业部沼气科学研究所 | Pre-inoculated anaerobic fermentation device and process thereof |
| CN109628274A (en) * | 2018-12-28 | 2019-04-16 | 河南恒天久大实业有限公司 | A kind of multistage cellular-type full mixed anaerobic reaction device |
-
2015
- 2015-02-10 CN CN201520096867.1U patent/CN204644347U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105907800A (en) * | 2016-06-28 | 2016-08-31 | 农业部沼气科学研究所 | Pre-inoculated anaerobic fermentation device and process thereof |
| CN109628274A (en) * | 2018-12-28 | 2019-04-16 | 河南恒天久大实业有限公司 | A kind of multistage cellular-type full mixed anaerobic reaction device |
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