CN110386745A - A kind of method and apparatus of livestock and poultry cultivation waste production humic acid - Google Patents
A kind of method and apparatus of livestock and poultry cultivation waste production humic acid Download PDFInfo
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- CN110386745A CN110386745A CN201910771150.5A CN201910771150A CN110386745A CN 110386745 A CN110386745 A CN 110386745A CN 201910771150 A CN201910771150 A CN 201910771150A CN 110386745 A CN110386745 A CN 110386745A
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- Prior art keywords
- separator
- multiphase
- high temperature
- livestock
- humic acid
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- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 239000004021 humic acid Substances 0.000 title claims abstract description 28
- 244000144972 livestock Species 0.000 title claims abstract description 26
- 239000002699 waste material Substances 0.000 title claims abstract description 26
- 244000144977 poultry Species 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims description 19
- 238000000605 extraction Methods 0.000 claims abstract description 29
- 230000036284 oxygen consumption Effects 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 239000003054 catalyst Substances 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims description 20
- 238000007254 oxidation reaction Methods 0.000 claims description 20
- 230000003647 oxidation Effects 0.000 claims description 19
- 239000007787 solid Substances 0.000 claims description 13
- 241001465754 Metazoa Species 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 239000000523 sample Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 3
- 238000006555 catalytic reaction Methods 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 241000283690 Bos taurus Species 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000003616 anti-epidemic effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 235000001674 Agaricus brunnescens Nutrition 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- -1 multiphase mixer 1 Chemical compound 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 208000012153 swine disease Diseases 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/26—Treatment of water, waste water, or sewage by extraction
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a kind of equipment of livestock and poultry cultivation waste production humic acid, belong to livestock and poultry cultivation waste processing arts, it includes the multiphase mixer for being sequentially communicated setting, catalyst tank, high temperature anaerobic biochemical reactor, high temperature oxygen consumption biochemical reactor and multiphase separator, the liquid object output end of multiphase separator is provided with extraction separator, to extract humic acid.Setting of the invention reduces the waste of resource, while reducing the pollution of environment so that livestock and poultry cultivation waste, that is, excrement is utilized and recycles.
Description
Technical field
The present invention relates to livestock and poultry cultivation waste processing arts more particularly to a kind of livestock and poultry cultivation waste to produce humic acid
Method and apparatus.
Background technique
With the fast development of China's animal husbandry, the scale of current breeding enterprise is also quickly to intensive, rule
The direction of modelling is advanced, and at the same time, the cultivation of this scale but exposes various problems very serious, these problems
Middle most serious surely belongs to problem of environmental pollution, such as certain large-scale milk cattle cultivating enterprises, cultivation pasture in large scale due to cultivating
Raising scale all reaches ten thousand or more, and ten thousand cow head pasture light are that the excrement generated can reach 70,000 tons or more every year, and often at present
But there is variety of problems for the processing techniques such as excrement produced by daily itself, for example excrement is generated natural pond by fermentation process
The processing mode of gas, fermentation method is limited in the temperature condition that north cold area generates biogas, and processing capacity is opposite
Obviously unable to do what one wishes in so huge excrement production capacity, more fatal is that will lead to natural pond if pasture carries out Antiepidemic sterilizing
Certain mushrooms necessary to gas generates are to being killed, to affect generation biogas, in view of this this harmless treatment mode is simultaneously
Harmless treatment cannot be really carried out, and be with the anti-epidemic measure of livestock-raising is inconsistent, and cultivates the anti-of place
Epidemic disease disinfection is to guarantee one of the essential measure of health of institute raise livestock.Furthermore the livestock by being raised generates excrement
Just, urine, the constituent of cleaning and sterilizing waste water is complicated, after simple process after manufactured organic fertilizer application with wastewater treatment
Discharge afterwards also can constitute serious pollution hidden trouble to environment；It was supported at this several years in different in ten thousand cow head pastures of modern animal husbandry
Growing the event that area occurs in succession is exactly that this serious consequence most intuitively embodies.
Summary of the invention
The object of the invention is that providing a kind of method and apparatus of livestock and poultry cultivation waste production humic acid, have to fowl
Animal manure is just handled and is utilized, while the advantages of reduce environmental pollution.
To achieve the goals above, the technical solution adopted by the present invention is that: a kind of livestock and poultry cultivation waste production humic acid
Equipment, including multiphase mixer, catalyst tank, high temperature anaerobic biochemical reactor, high temperature oxygen consumption biochemical reactor, multiphase separator
And extraction separator, the output end of the multiphase mixer are connected to by pipeline with the input terminal of high temperature anaerobic biochemical reactor,
The catalyst tank is connected to by delivery pipe with multiphase internal mixer, the output end and height of the high temperature anaerobic biochemical reactor
The input terminal of warm oxygen consumption biochemical reactor is connected to by pipeline, the output end and multi-phase separation of the high temperature oxygen consumption biochemical reactor
The input pipe of device is connected to by pipeline, and the liquid object output end of the multiphase separator and the input terminal of extraction separator pass through pipe
Road connection setting, the extract output end of the extraction separator are provided with discharge nozzle.
Preferably, the solid content output end of the multiphase separator is provided with and communicated with oxidation reactor by pipeline.
Preferably, the intermediate output end of the extraction separator is connected by the input terminal of pipeline and oxidation reactor
It is logical.
Preferably, the high temperature anaerobic biochemical reactor and high temperature oxygen consumption biochemical reactor are all made of fermentor.
Preferably, the multiphase separator uses solid gas liquid three phase separator.
Preferably, further including controller, the multiphase mixer, high temperature anaerobic biochemical reactor, high temperature oxygen consumption are biochemical
Probe is provided in reactor, multiphase separator and extraction separator, multiple probes are connect with controller signals.
A kind of method of livestock and poultry cultivation waste production humic acid, comprising the following steps:
S1, fowl and animal excrement is transported in multiphase mixer；
Catalyst is conveyed in S2, Xiang Duoxiang mixer, and the material in multiphase mixer is stirred, and mixes multiphase
Material in device is uniformly mixed, and completes the homogenizing of material；
S3, the material after homogenizing is successively conveyed into high temperature anaerobic biochemical reactor and the progress of high temperature oxygen consumption biochemical reactor
Anaerobism and aerobic reaction processing then convey material into being separated by solid-liquid separation in multiphase separator；
S4, the liquid object isolated in multiphase separator is conveyed into carrying out in extraction separator carrying out in extraction separator
Extraction, obtains humic acid.
It is carried out at oxidation preferably, the solid content that the multiphase separator in S3 is isolated is conveyed into oxidation reactor
Reason.
It is aoxidized preferably, remaining centre after extraction separator extraction in S4 is delivered into oxidation reactor
Processing.
Compared with the prior art, the advantages of the present invention are as follows:
One, fowl and animal excrement is utilized, so that waste utilizes the reduction wasting of resources again；
Two, fowl and animal excrement is carried out that the pollution for reducing fowl and animal excrement to environment is uniformly processed；
Three, unharmful substance discharges in treatment process, reduces environmental pollution；
Four, fowl and animal excrement is effectively treated, prevents excrement accumulation to a large amount of bacteriums brought by pasture, reduces fowl
The probability of dirty swine disease.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the embodiment of the present invention；
Fig. 2 is the attachment structure schematic diagram of each equipment and controller in the embodiment of the present invention.
In figure: 1, multiphase mixer；2, catalyst tank；3, high temperature anaerobic biochemical reactor；4, high temperature oxygen consumption biochemical reaction
Device；5, multiphase separator；6, extraction separator；7, oxidation reactor.
Specific embodiment
The invention will be further described below.
Embodiment:
As shown in Figure 1, a kind of equipment of livestock and poultry cultivation waste production humic acid, including multiphase mixer 1, catalyst tank 2,
High temperature anaerobic biochemical reactor 3, high temperature oxygen consumption biochemical reactor 4, multiphase separator 5 and extraction separator 6.
As shown in Figure 1, catalyst tank 2 is inside delivery pipe and multiphase mixer 1 by being connected to, when fowl and animal excrement be conveyed into it is more
After mixing in device 1, the catalyst in catalyst tank 2 is entered inside multiphase mixer 1 by delivery pipe, and multiphase mixing will catalysis
Agent is uniformly mixed with fowl and animal excrement, so that the matter homogenizing in multiphase mixer 1, reaches the fluctuation vibration for reducing material chemical component
Width makes the chemical component uniformity of material.Multiphase mixer 1 selects the auspicious LR-1000 type blender of dragon in the present embodiment.
As shown in Figure 1, the output end of multiphase mixer 1 is connected by the input terminal of pipeline and high temperature anaerobic biochemical reactor 3
It is logical, so that material is carried out anaerobic reaction.The input of the output end and high temperature oxygen consumption biochemical reactor 4 of high temperature anaerobic biochemical reactor 3
End is connected to by pipeline, and material is made to carry out oxygen consumption reaction.High temperature anaerobic biochemical reactor 3 and high temperature oxygen consumption are raw in the present embodiment
Change reactor 4 and be all made of fermentor, and fermentor selects great FJG001 type fermentor.Being reacted by anaerobic reaction with oxygen consumption makes
The organic matter obtained in material converts inorganic matter.
As shown in Figure 1, the input pipe of the output end of high temperature oxygen consumption biochemical reactor 4 and multiphase separator 5 is connected by pipeline
Logical, multiphase separator 5 works so that solid content is separated with liquid object.Multiphase separator 5 uses clear and rich science and technology QRUASB type solid gas
Liquid three phase separator, to carry out effective multi-phase separation.
As shown in Figure 1, the liquid object output end of multiphase separator 5 is connected to the input terminal of extraction separator 6 by pipeline
Setting, the extract output end of extraction separator 6 are provided with discharge nozzle, and extraction gains are humic acid.The extraction of extraction separator 6
Remaining intermediate is connected to by pipeline with the input terminal of oxidation reactor 7 after the completion of taking.The solid content of multiphase separator 5 exports
End is connected to oxidation reactor 7, obtains water and solids after solid content and intermediate progress oxidation reaction, solids is humic acid
Humic acid fertilizer long-term cropping can be used in fertilizer product, operator, reuses crop and feeds poultry formation circulation.In this implementation
Oxidation reactor 7 selects Fenton TLFD type oxidation reactor in example.
As shown in Fig. 2, the equipment of livestock and poultry cultivation waste production humic acid further includes controller and is separately positioned on multiphase
In mixer 1, high temperature anaerobic biochemical reactor 3, high temperature oxygen consumption biochemical reactor 4, multiphase separator 5 and extraction separator 6
Probe, multiple probes are connect with controller signals.It is associated with by different probe electric signals with control parameter, realizes operation respectively
State modulator and overall intelligence control.
A kind of structure of the equipment of livestock and poultry cultivation waste production humic acid provided by the invention is described in detail in above content,
Corresponding with above equipment system, the present invention also provides a kind of methods of livestock and poultry cultivation waste production humic acid.
A kind of method of livestock and poultry cultivation waste production humic acid, comprising the following steps:
S1, fowl and animal excrement is transported in multiphase mixer 1；
Catalyst is conveyed in S2, Xiang Duoxiang mixer 1, and the material in multiphase mixer 1 is stirred, and keeps multiphase mixed
Material in clutch 1 is uniformly mixed, and completes the homogenizing of material；
S3, the material after homogenizing is successively conveyed into high temperature anaerobic biochemical reactor 3 and high temperature oxygen consumption biochemical reactor 4 into
Row anaerobism and aerobic reaction processing, then convey material into being separated by solid-liquid separation in multiphase separator 5, by multiphase separator 5
The solid content isolated, which is conveyed into oxidation reactor 7, carries out oxidation processes；
S4, it the liquid object isolated in multiphase separator 5 is conveyed into extraction separator 6 carries out in extraction separator 6
It is extracted, obtains humic acid, remaining centre, which delivers into, after extraction separator 6 is extracted carries out oxygen in oxidation reactor 7
Change processing.
Used herein a specific example illustrates the principle and implementation of the invention, and above embodiments are said
It is bright to be merely used to help understand method and its core concept of the invention；At the same time, for those skilled in the art, foundation
Thought of the invention, there will be changes in the specific implementation manner and application range, will to change and improvement of the invention
It is possible, the conception and scope without exceeding accessory claim defined, in conclusion the content of the present specification should not manage
Solution is limitation of the present invention.
Claims (9)
1. a kind of equipment of livestock and poultry cultivation waste production humic acid, which is characterized in that including multiphase mixer (1), catalyst tank
(2), high temperature anaerobic biochemical reactor (3), high temperature oxygen consumption biochemical reactor (4), multiphase separator (5) and extraction separator (6),
The output end of the multiphase mixer (1) is connected to by pipeline with the input terminal of high temperature anaerobic biochemical reactor (3), the catalysis
Agent slot (2) by being connected to inside delivery pipe and multiphase mixer (1), the output end of the high temperature anaerobic biochemical reactor (3) and
The input terminal of high temperature oxygen consumption biochemical reactor (4) by pipeline be connected to, the output end of the high temperature oxygen consumption biochemical reactor (4) with
The input pipe of multiphase separator (5) is connected to by pipeline, the liquid object output end and extraction separator of the multiphase separator (5)
(6) input terminal is connected to by pipeline to be arranged, and the extract output end of the extraction separator (6) is provided with discharge nozzle.
2. a kind of equipment of livestock and poultry cultivation waste production humic acid according to claim 1, which is characterized in that the multiphase
The solid content output end of separator (5) is provided with and communicated with oxidation reactor (7) by pipeline.
3. a kind of equipment of livestock and poultry cultivation waste production humic acid according to claim 2, which is characterized in that the extraction
The intermediate output end of separator (6) is connected to by pipeline with the input terminal of oxidation reactor (7).
4. a kind of equipment of livestock and poultry cultivation waste production humic acid according to claim 1, which is characterized in that the high temperature
Anaerobic biochemical reactor (3) and high temperature oxygen consumption biochemical reactor (4) are all made of fermentor.
5. a kind of equipment of livestock and poultry cultivation waste production humic acid according to claim 1, which is characterized in that the multiphase
Separator (5) uses solid gas liquid three phase separator.
6. a kind of equipment of livestock and poultry cultivation waste production humic acid described in any one claim according to claim 1~5,
It is characterized in that, further including controller, the multiphase mixer (1), high temperature anaerobic biochemical reactor (3), high temperature oxygen consumption are biochemical
It is provided with probe in reactor (4), multiphase separator (5) and extraction separator (6), it is multiple described to connect with controller signals
It connects.
7. a kind of method of livestock and poultry cultivation waste production humic acid, which comprises the following steps:
S1, fowl and animal excrement is transported in multiphase mixer (1)；
Catalyst is conveyed in S2, Xiang Duoxiang mixer (1), and the material in multiphase mixer (1) is stirred, and keeps multiphase mixed
Material in clutch (1) is uniformly mixed, and completes the homogenizing of material；
S3, the material after homogenizing is successively conveyed into high temperature anaerobic biochemical reactor (3) and high temperature oxygen consumption biochemical reactor (4) into
Row anaerobism and aerobic reaction processing then convey material into being separated by solid-liquid separation in multiphase separator (5)；
S4, the liquid object isolated in multiphase separator (5) is conveyed into progress extraction separator (6) in extraction separator (6)
In extracted, obtain humic acid.
8. a kind of method of livestock and poultry cultivation waste production humic acid according to claim 7, which is characterized in that will be in S3
The solid content that multiphase separator (5) is isolated, which is conveyed into oxidation reactor (7), carries out oxidation processes.
9. a kind of method of livestock and poultry cultivation waste production humic acid according to claim 7, which is characterized in that will extract in S4
Remaining centre, which delivers into, after taking separator (6) to extract carries out oxidation processes in oxidation reactor (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910771150.5A CN110386745A (en) | 2019-08-21 | 2019-08-21 | A kind of method and apparatus of livestock and poultry cultivation waste production humic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910771150.5A CN110386745A (en) | 2019-08-21 | 2019-08-21 | A kind of method and apparatus of livestock and poultry cultivation waste production humic acid |
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| Publication Number | Publication Date |
|---|---|
| CN110386745A true CN110386745A (en) | 2019-10-29 |
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ID=68289132
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| CN201910771150.5A Pending CN110386745A (en) | 2019-08-21 | 2019-08-21 | A kind of method and apparatus of livestock and poultry cultivation waste production humic acid |
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|---|---|---|---|---|
| CN101358209A (en) * | 2008-08-25 | 2009-02-04 | 彭美忠 | Technique for preparing biogas by high-temperature anaerobic zymosis method using animal manure as raw material |
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| CN103626608A (en) * | 2013-11-06 | 2014-03-12 | 北京博文合众生物科技有限公司 | Technology and process for preparing biological humic acid fertilizer by use of pig manure |
| WO2014124500A1 (en) * | 2013-02-18 | 2014-08-21 | Crc Care Pty Ltd | A system for processing organic waste |
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| CN108658638A (en) * | 2018-08-06 | 2018-10-16 | 北京开元信节能科技有限公司 | A kind of device with anaerobic fermentation and medium temperature oxidization combination operation production organic fertilizer |
| CN109052897A (en) * | 2018-08-03 | 2018-12-21 | 煤科集团杭州环保研究院有限公司 | A kind of method that animal waste Treatment and recovery utilizes |
| CN109401759A (en) * | 2018-11-13 | 2019-03-01 | 四川锐源能环科技有限公司 | A kind of livestock and poultry cultivation waste harmless resource processing system and method |
-
2019
- 2019-08-21 CN CN201910771150.5A patent/CN110386745A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101358209A (en) * | 2008-08-25 | 2009-02-04 | 彭美忠 | Technique for preparing biogas by high-temperature anaerobic zymosis method using animal manure as raw material |
| CN102173507A (en) * | 2011-01-12 | 2011-09-07 | 南京加德绿色能源研发有限公司 | Method for comprehensively recycling fecal sewage of large-scale livestock and poultry farms and farmland crop straws |
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Application publication date: 20191029 |
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