CN107337480A - A kind of poultry manure handling process - Google Patents

A kind of poultry manure handling process Download PDF

Info

Publication number
CN107337480A
CN107337480A CN201610281657.9A CN201610281657A CN107337480A CN 107337480 A CN107337480 A CN 107337480A CN 201610281657 A CN201610281657 A CN 201610281657A CN 107337480 A CN107337480 A CN 107337480A
Authority
CN
China
Prior art keywords
biogas
drying
fermentation
poultry manure
handling process
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610281657.9A
Other languages
Chinese (zh)
Inventor
丁传祥
丁洁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yangzhou Yu Yu Environmental Protection Technology Co Ltd
Original Assignee
Yangzhou Yu Yu Environmental Protection Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yangzhou Yu Yu Environmental Protection Technology Co Ltd filed Critical Yangzhou Yu Yu Environmental Protection Technology Co Ltd
Priority to CN201610281657.9A priority Critical patent/CN107337480A/en
Publication of CN107337480A publication Critical patent/CN107337480A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C9/00Fertilisers containing urea or urea compounds
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05DINORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
    • C05D9/00Other inorganic fertilisers
    • C05D9/02Other inorganic fertilisers containing trace elements
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F3/00Fertilisers from human or animal excrements, e.g. manure
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/102Removal of contaminants of acid contaminants
    • C10L3/104Carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P5/00Preparation of hydrocarbons or halogenated hydrocarbons
    • C12P5/02Preparation of hydrocarbons or halogenated hydrocarbons acyclic
    • C12P5/023Methane
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/44Deacidification step, e.g. in coal enhancing
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/54Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
    • C10L2290/542Adsorption of impurities during preparation or upgrading of a fuel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Zoology (AREA)
  • Microbiology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Molecular Biology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Inorganic Chemistry (AREA)
  • Fertilizers (AREA)

Abstract

The present invention relates to a kind of poultry manure handling process, including fermentation, methane purification, exhaust-gas treatment and biogas residue drying, fermentation:Poultry manure is poured into ferment at constant temperature is carried out in fermentation tank, adjust 35 43 DEG C of temperature inside fermentation tank, it is 6.8 7.4 to control the pH value inside fermentation tank, adds additive during the fermentation;Biogas treatment:Biogas caused by fermentation tank is subjected to absorption refining by Amine Solutions, then by the gas compression after purification and bottling;Biogas residue is dried:Excrement is sent into the upper auger of dryer by biogas residue caused by fermentation tank by feeding device and carries out first time drying, the temperature of drying is 300 500 DEG C, after drying, second is carried out by dryer to dry, the temperature of drying is 200 400 DEG C, and the water content after biogas residue drying is 10% 20%;Biogas residue processing:Dried excrement is added into various trace elements, granular organic fertilizer, packing and selling are made after being pulverized and sieved, the present invention can realize the abundant processing to poultry manure.

Description

A kind of poultry manure handling process
Technical field
The present invention relates to excrement and urine treatment technology field, more particularly to a kind of poultry manure handling process.
Background technology
With the adjustment of agricultural structure and the change of resident's dietary structure, the cultivation of China various regions Industry is quickly grown, and is thereby produced substantial amounts of feces of livestock and poultry, is not only polluted environment, causes poultry The problems such as fowl growth and health, while also have impact on the sustainable development of aquaculture.Current Poultry excrement and urine disposal technology mainly has the methods of seasoning, chemical method, but this several method is present Some more obstinate harmful levels of pathogens, pest and disease damage and weed seeds can not thoroughly be killed by, and be easily caused Secondary pollution, consumption quantity of energy is big, and a large amount of foul smell, and processing time long fertilizer damage are distributed during processing Lose the problems such as also more serious;
At present, government's throwing huge fund progress keypoint treatment, construction pollution treatment facility, formulation livestock and poultry pasture reach Discharge technology is marked, oxygen consumption aeration industry pollution treatment technique is generally used in built pollution treatment facility, by High in equipment operating cost, project builds up rear many plants and is difficult to bear, what some units were built up Processing system is not run for a long time, and equipment has rusty stains, and a large amount of pollution treatment inputs could not receive due Effect.Prior art is except returning field as fertilizer by a solid-states manure fermentation or feeding brid guano is expanded Outside the feed of fish, a large amount of liquid dungs are developed not as a kind of resource, so that animal dung Water turns into the pollution sources of water quality for a long time;
Application publication number is the A of CN 105016803 patent:At a kind of recycling of feces of livestock and poultry Reason method, a kind of recycling processing method of feces of livestock and poultry, it is characterised in that specific steps are such as Under:(1) on the sunny side, wide 2*3m fermentation bed, brick a height of 0.1- from the ground are built in ventilation 0.3m, stalk thick one layer of 2-3cm of place mat, is easy to bottom ventilation to supply oxygen;(2) by feces of livestock and poultry Separation of solid and liquid is carried out with solid-liquid separating machine;(3) by after separation of solid and liquid solid feces of livestock and poultry poultry and it is aqueous The auxiliary material for 8-10% is measured by 3:1 part by weight is mixed, by auxiliary material weight 0.1-0.2 % zymophyte powder layering is added in fermentate, then excrement, auxiliary material and zymophyte powder are stirred It is placed on after even in fermentation bed;(4) height of fermentation heap is 1-2m, width 1.2-1.4m, The cumulative volume of fermentation heap is 1.5-1.8m 3, is mechanically or manually overturned once per 7-9d, is sent out Temperature reaches 50-60 DEG C after ferment 24-36h, and organic fertilizer is obtained after 5-20d;(5) by solid-liquid point For liquid feces of livestock and poultry from after with being pumped into tune manure pit, the TS concentration for making pig manure is 6-8%; (6) pig manure in manure pit will be adjusted to be promoted in USR reactors with cutting pump to be fermented; (7) caused biogas enters the progress of flexible diaphragm type gas storage holder after sulphur removal and purification in USR reactors Storage, the biogas of storage deliver to subscriber unit and are used to generate electricity or are burnt for surrounding user;(8)USR Caused biogas residue carries out separation of solid and liquid through screw extruder in reactor, the solid biogas residue warp after separation With entering orchard and the cereal crops on periphery, the biogas slurry after separation in biogas slurry pond through storing for organic fertilizer car With entering orchard and the cereal crops on periphery afterwards, the auxiliary material is one in stalk, straw and sawdust Kind is two or more;The patent simply carries out preliminary treatment to excrement, and production capacity is small;
The A of Authorization Notice No. CN 104193426:A kind of manure fermentation dries the method that a step is completed With equipment, it is impossible to sufficiently excrement is handled, makes full use of poultry manure.
The content of the invention
It is an object of the invention to provide a kind of poultry manure handling process, solves family in the prior art Poultry manure processing is difficult, the low technical problem of fermentation efficiency;
The technical scheme that the present invention solves above-mentioned technical problem is as follows:
A kind of poultry manure handling process, comprises the following steps:
Fermentation:Poultry manure is poured into ferment at constant temperature is carried out in fermentation tank, controlled inside fermentation tank PH value is 6.8-7.4, adds additive during the fermentation, generates biogas and biogas residue;
Biogas treatment:Biogas caused by fermentation tank is subjected to absorption refining by Amine Solutions, so Afterwards by the gas compression after purification and bottling;
Biogas residue is dried:Excrement is sent into dryer by biogas residue caused by fermentation tank by feeding device First time drying is carried out in cage, after drying, second is carried out by dryer and dries, biogas residue Water content after drying is 10%-20%;
Biogas residue processing:Dried excrement is added into trace element, is made after being pulverized and sieved Granular organic fertilizer, you can.
On the basis of above-mentioned technical proposal, the present invention can also do following improvement:
Further, the pH value in the fermentation is adjusted by adding acetic acid or lime, is used The beneficial effect of this step is that the fermentation process pH value of the present invention is adjusted by acetic acid and lime, Because when PH is higher or lower than certain value, the fermentation to biogas has certain inhibitory action;
Further, the additive in the fermentation includes appointing in aspergillus niger, active carbon powder or urea Anticipate one or more kinds of combinations, the beneficial effect using this step is by additive, can be promoted Enter the fermentation of poultry manure, improve fermentation efficiency;
Further, the Amine Solutions of the biogas treatment include one-level amine, secondary amine, tertiary amine or A kind of solution or a variety of mixed solutions in sterically hindered amines, the beneficial effect using this step is to pass through Amine Solutions absorb biogas, carry out methane purification;
Further, the temperature for carrying out ferment at constant temperature is 35-43 DEG C;
Further, the temperature of second of drying is 200-400 DEG C;
Further, during the biogas residue drying, hot blast, the temperature of hot blast are passed through into dryer Spend for 400-500 DEG C, the beneficial effect using this step is dried by hot blast, so can Reduce the moisture content of excrement;
Further, the trace element in the biogas residue processing is one in boron, copper, iron, manganese, zinc Kind or multiple element, the beneficial effect using this step be by entering trace element, so can be square Just organic fertilizer is made in biogas residue;
The purpose of the present invention is that poultry manure is fully handled, and fermentation process of the invention is main By ferment at constant temperature, inventor has found by many experiments and research, in 35-43 DEG C of temperature Under, the gas production highest of biogas;
The present invention carries out PH regulation by adding acetic acid or lime, because inventor sends out in research Existing, when PH is higher than 8.5 or less than 6.5, biogas fermentation can be suppressed, through many experiments, When PH is located at 6.8-7.4, biogas fermentation efficiency high;
The present invention be to the method for purification of biogas by absorption refining method, i.e., using Amine Solutions come The carbon dioxide in biogas is absorbed,, can by heating under reduced pressure by pressurizeing come absorbing carbon dioxide , so can be to organic amine so that the Amine Solutions after absorbing carbon dioxide are discharged into carbon dioxide Solution is recycled;
The present invention is by repeated drying, reduces the water content inside biogas residue, and drying time regards biogas residue Depending on the water content of script;
After the present invention is handled biogas residue, the organic fertilizer of production contains a variety of necessary to crops Nutrient, test and assert through academy of agricultural sciences relevant expert, wherein nitrogenous about 2.6%, phosphorus content is about For 3.5%, potassium content about 2.5%, crude protein is about 16-25%, and organic matter is about 45%.
Beneficial effects of the present invention:
1. the present invention can be by the excrement of moisture content 65% by high temperature drying, sterilization, decomposition Organic fertilizer of the moisture content formed below 15% is dried etc. process, so as to realize the abundant profit to excrement With;
2. the organic fertilizer that the present invention makes has various nutrient elements necessary to crops, through scientific research department Door detection is assert:Nitrogen content is 2.6% in the fertilizer, phosphorus content 3.5%, potassium content 2.5%, Crude protein is 16-25%, organic matter 45%.It is the optimal from fertilizer of pollution-free green food plantation Material;
3. the production capacity of the present invention is larger, can continuously run;
4. the Shi of the present invention is good with the uniformity of Fan Wei Guang ﹑ product dryings;
5. the present invention also can reach the purpose of sterilization and deodorization while drying, pass through drying and heat Wind can be sterilized and deodorization;
The present invention reduces feeding cost, reduced environmental pollution with good effect for opening up feed resource Fruit.
Embodiment
The principles and features of the present invention are described below, and example is served only for explaining this hair It is bright, it is not intended to limit the scope of the present invention.
The present invention can be by the excrement of moisture content 65% by high temperature drying, sterilization, decomposition etc. Organic fertilizer of the moisture content that process drying forms below 15%, makes full use of so as to realize to excrement; Various nutrient elements necessary to the organic fertilizer that the present invention makes has crops, are detected through scientific research department Assert:Nitrogen content is 2.6% in the fertilizer, phosphorus content 3.5%, potassium content 2.5%, and crude protein is 16-25%, organic matter 45%.It is that the optimal of pollution-free green food plantation selects fertilizer;The present invention Production capacity it is larger, can continuously run;The Shi of the present invention is uniform with Fan Wei Guang ﹑ product dryings Property is good;The present invention also can reach the purpose of sterilization and deodorization while drying, and pass through drying and heat Wind can be sterilized and deodorization;The present invention reduces feeding cost, subtracted for opening up feed resource Few environmental pollution has good result.
Embodiment 1:
A kind of poultry manure handling process, including fermentation, methane purification, exhaust-gas treatment and biogas residue are dried Dry step:
Fermentation:Poultry manure is poured into ferment at constant temperature is carried out in fermentation tank, adjusted inside fermentation tank 35 DEG C of temperature, it is 6.8 to control the pH value inside fermentation tank, adds additive during the fermentation;
Biogas treatment:Biogas caused by fermentation tank is subjected to absorption refining by Amine Solutions, so Afterwards by the gas compression after purification and bottling;
Biogas residue is dried:Excrement is sent into dryer by biogas residue caused by fermentation tank by feeding device First time drying is carried out in upper auger, the temperature of drying is 300 DEG C, after drying, passes through drying Machine, which carries out second, dries, and the temperature of drying is 200 DEG C, and the water content after biogas residue drying is 10%;
Biogas residue processing:Dried excrement is added into various trace elements, made after being pulverized and sieved Into granular organic fertilizer, packing and selling.
Wherein, the pH value in the fermentation is adjusted by adding acetic acid;
Wherein, the additive in the fermentation is aspergillus niger;
Wherein, the Amine Solutions in the biogas treatment are one-level amine;
Wherein, during the biogas residue drying, hot blast, the temperature of hot blast are passed through into dryer For 400 DEG C;
Wherein, the trace element in the biogas residue processing is boron;
Organic fertilizer produced by the invention contains various nutrient elements necessary to crops, through academy of agricultural sciences Relevant expert, which tests, to be assert, wherein nitrogenous is 2.6%, phosphorus content 3.5%, containing potassium 2.5%, slightly Albumen is 16-25%, organic matter 45%;
Because organic fertilizer fertility is big, holding effect is long, is approved by users, the head of many clients It is exactly organic fertilizer to select fertilizer, and organic fertilizer is the main original of various compoiste fertilizers, bio-fertilizer again Material;So the market prospects of the present invention are quite wide, the economic benefit that it is created is considerable 's;
Embodiment 2
A kind of poultry manure handling process, including fermentation, methane purification, exhaust-gas treatment and biogas residue are dried Dry step:
Fermentation:Poultry manure is poured into ferment at constant temperature is carried out in fermentation tank, adjusted inside fermentation tank 43 DEG C of temperature, it is 7.4 to control the pH value inside fermentation tank, adds additive during the fermentation;
Biogas treatment:Biogas caused by fermentation tank is subjected to absorption refining by Amine Solutions, so Afterwards by the gas compression after purification and bottling;
Biogas residue is dried:Excrement is sent into dryer by biogas residue caused by fermentation tank by feeding device First time drying is carried out in upper auger, the temperature of drying is 500 DEG C, after drying, passes through drying Machine, which carries out second, dries, and the temperature of drying is 400 DEG C, and the water content after biogas residue drying is 20%;
Biogas residue processing:Dried excrement is added into various trace elements, made after being pulverized and sieved Into granular organic fertilizer, packing and selling.
Wherein, the pH value in the fermentation is adjusted by adding lime;
Wherein, the additive in the fermentation is the mixture of active carbon powder and urea;
Wherein, the Amine Solutions in the biogas treatment are secondary amine, tertiary amine and steric hindrance Mixed solution in amine;
Wherein, during the biogas residue drying, hot blast, the temperature of hot blast are passed through into dryer For 500 DEG C;
Wherein, the trace element in the biogas residue processing is copper, iron, manganese, the complex element of zinc;
Embodiment 3
A kind of poultry manure handling process, including fermentation, methane purification, exhaust-gas treatment and biogas residue are dried Dry step:
Fermentation:Poultry manure is poured into ferment at constant temperature is carried out in fermentation tank, adjusted inside fermentation tank 39 DEG C of temperature, it is 7.1 to control the pH value inside fermentation tank, adds additive during the fermentation;
Biogas treatment:Biogas caused by fermentation tank is subjected to absorption refining by Amine Solutions, so Afterwards by the gas compression after purification and bottling;
Biogas residue is dried:Excrement is sent into dryer by biogas residue caused by fermentation tank by feeding device First time drying is carried out in upper auger, the temperature of drying is 400 DEG C, after drying, passes through drying Machine, which carries out second, dries, and the temperature of drying is 300 DEG C, and the water content after biogas residue drying is 15%;
Biogas residue processing:Dried excrement is added into various trace elements, made after being pulverized and sieved Into granular organic fertilizer, packing and selling.
Wherein, the pH value in the fermentation is adjusted by adding acetic acid or lime;
Wherein, the additive in the fermentation be aspergillus niger, active carbon powder and urea one kind or Person's many kinds of substance;
Wherein, the Amine Solutions in the biogas treatment be one-level amine, secondary amine, tertiary amine and A kind of solution or a variety of mixed solutions in sterically hindered amines;
Wherein, during the biogas residue drying, hot blast, the temperature of hot blast are passed through into dryer For 450 DEG C;
Wherein, the trace element in the biogas residue processing is one kind in boron, copper, iron, manganese, zinc Or multiple element;
Presently preferred embodiments of the present invention is the foregoing is only, is not intended to limit the invention, it is all at this Within the spirit and principle of invention, any modification, equivalent substitution and improvements made etc., it all should wrap It is contained within protection scope of the present invention.

Claims (9)

1. a kind of poultry manure handling process, it is characterised in that comprise the following steps:
Fermentation:Poultry manure is poured into ferment at constant temperature is carried out in fermentation tank, control the pH value inside fermentation tank to be 6.8-7.4, additive is added during the fermentation, generate biogas and biogas residue;
Biogas treatment:Biogas caused by fermentation tank is subjected to absorption refining by Amine Solutions, then will purification Gas compression afterwards and bottling;
Biogas residue is dried:Excrement is sent into the cage of dryer by biogas residue caused by fermentation tank by feeding device Row is dried for the first time, after drying, is carried out second by dryer and is dried, the water content after biogas residue drying For 10%-20%;
Biogas residue processing:Dried excrement is added into trace element, being made after being pulverized and sieved granular has Machine fertilizer, you can.
2. poultry manure handling process according to claim 1, it is characterised in that in the fermentation PH value is adjusted by adding acetic acid or lime.
3. poultry manure handling process according to claim 1, it is characterised in that adding in the fermentation Agent is added to include any one in aspergillus niger, active carbon powder or urea or two or more combinations.
4. poultry manure handling process according to claim 1, it is characterised in that the biogas treatment Amine Solutions include a kind of solution or a variety of mixing in one-level amine, secondary amine, tertiary amine or sterically hindered amines Solution.
5. according to the poultry manure handling process described in claim any one of 1-4, it is characterised in that it is described enter The temperature of row ferment at constant temperature is 35-43 DEG C.
6. according to the poultry manure handling process described in claim any one of 1-4, it is characterised in that described The temperature of first drying is 300-500 DEG C.
7. according to the poultry manure handling process described in claim any one of 1-4, it is characterised in that described The temperature of secondary drying is 200-400 DEG C.
8. according to the poultry manure handling process described in claim any one of 1-4, it is characterised in that the natural pond During slag is dried, hot blast is passed through into dryer, the temperature of hot blast is 400-500 DEG C.
9. according to the poultry manure handling process described in claim any one of 1-4, it is characterised in that the natural pond Trace element in Slag treatment includes any one in boron, copper, iron, manganese or zinc or multiple element.
CN201610281657.9A 2016-04-29 2016-04-29 A kind of poultry manure handling process Pending CN107337480A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610281657.9A CN107337480A (en) 2016-04-29 2016-04-29 A kind of poultry manure handling process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610281657.9A CN107337480A (en) 2016-04-29 2016-04-29 A kind of poultry manure handling process

Publications (1)

Publication Number Publication Date
CN107337480A true CN107337480A (en) 2017-11-10

Family

ID=60222687

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610281657.9A Pending CN107337480A (en) 2016-04-29 2016-04-29 A kind of poultry manure handling process

Country Status (1)

Country Link
CN (1) CN107337480A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108702997A (en) * 2018-05-24 2018-10-26 广西壮族自治区林业科学研究院 A method of promoting Characteristics of Soil Fertility Under Eucalyptus Plantations using biogas residue
CN109053262A (en) * 2018-09-27 2018-12-21 苏州极汇科技有限公司 A kind of preparation process devices and methods therefor proportion of compound fertilizer
CN110422978A (en) * 2018-07-13 2019-11-08 江苏普朗德节能科技有限公司 A kind of high-efficiency livestock and poultry waste anaerobic fermentation method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101275150A (en) * 2008-05-13 2008-10-01 江苏省农业科学院 Fermentation method for changing methane into resource by using water hyacinth and application of product produced thereby
CA2759898A1 (en) * 2009-04-29 2010-11-04 Lanzatech New Zealand Limited Improved carbon capture in fermentation
CN102086417A (en) * 2009-12-02 2011-06-08 青岛天人环境股份有限公司 Method for purifying marsh gas and recovering elemental sulfur and carbon dioxide
CN103172239A (en) * 2011-12-23 2013-06-26 潮州市绿岛生态农业有限公司 Biogas production method by livestock and poultry manure fermentation
CN105272397A (en) * 2015-10-12 2016-01-27 沙湾县亚宁农业科技开发有限公司 Fertilizer preparation apparatus and method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101275150A (en) * 2008-05-13 2008-10-01 江苏省农业科学院 Fermentation method for changing methane into resource by using water hyacinth and application of product produced thereby
CA2759898A1 (en) * 2009-04-29 2010-11-04 Lanzatech New Zealand Limited Improved carbon capture in fermentation
CN102086417A (en) * 2009-12-02 2011-06-08 青岛天人环境股份有限公司 Method for purifying marsh gas and recovering elemental sulfur and carbon dioxide
CN103172239A (en) * 2011-12-23 2013-06-26 潮州市绿岛生态农业有限公司 Biogas production method by livestock and poultry manure fermentation
CN105272397A (en) * 2015-10-12 2016-01-27 沙湾县亚宁农业科技开发有限公司 Fertilizer preparation apparatus and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108702997A (en) * 2018-05-24 2018-10-26 广西壮族自治区林业科学研究院 A method of promoting Characteristics of Soil Fertility Under Eucalyptus Plantations using biogas residue
CN110422978A (en) * 2018-07-13 2019-11-08 江苏普朗德节能科技有限公司 A kind of high-efficiency livestock and poultry waste anaerobic fermentation method
CN109053262A (en) * 2018-09-27 2018-12-21 苏州极汇科技有限公司 A kind of preparation process devices and methods therefor proportion of compound fertilizer
CN109053262B (en) * 2018-09-27 2021-09-03 哈尔滨市益农化肥有限公司 Preparation process device and method proportioning of compound fertilizer

Similar Documents

Publication Publication Date Title
CN102173931B (en) Animal manure carbon fertilizer and production method thereof
CN103918479B (en) Scale steer ration field waste comprehensive utilization process
CN105016803A (en) Resourceful treatment method for excrement of livestock
CN104803723A (en) Preparation process of ecological organic fertilizer
CN103664287B (en) A kind of biological organic fertilizer utilizing waterplant to prepare
CN107417395A (en) A kind of livestock-raising utilization of waste as resource method
CN108383671A (en) A kind of organic fertilizer and production technology
CN110407424A (en) A kind of dystopy fermentation bed processing animals and plants waste method
CN104003773A (en) Biological organic fertilizer and preparation method thereof
CN108794113A (en) A kind of reed fermentation organic fertilizer and preparation method thereof
CN106966832A (en) A kind of ecological organic fertilier and preparation method thereof
CN107337480A (en) A kind of poultry manure handling process
EP2828225B1 (en) Method for composting spent mushroom compost
CN107488052A (en) A kind of poultry manure processing unit and its technique
CN113526986A (en) Method for preparing biochar from livestock and poultry manure
CN115806449A (en) Full resource utilization method of livestock and poultry manure
CN108299032A (en) A method of quickly preparing organic fertilizer
RU2214990C1 (en) Method for processing organic waste products
CN112661545A (en) Method suitable for treating livestock and poultry manure by using ectopic fermentation bed in mountainous area
CN107759263A (en) A kind of organic fertilizer production technique
CN106396998A (en) Organic fertilizer with both insecticidal and fertilizing effects and preparation method thereof
CN109864002B (en) Padding for livestock breeding, preparation method thereof and bedding
CN110066024A (en) A kind of livestock and poultry farm resource utilization and zero release of pollutant method
CN106007830A (en) Manure fermenting compound bacterium solution and application thereof
CN111978110A (en) Method for preparing granular organic fertilizer

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20171110

RJ01 Rejection of invention patent application after publication