CN109650975A - A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely - Google Patents
A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely Download PDFInfo
- Publication number
- CN109650975A CN109650975A CN201910145922.4A CN201910145922A CN109650975A CN 109650975 A CN109650975 A CN 109650975A CN 201910145922 A CN201910145922 A CN 201910145922A CN 109650975 A CN109650975 A CN 109650975A
- Authority
- CN
- China
- Prior art keywords
- stirring rod
- vinasse
- stalk
- tailing
- shaft
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely, comprising the following steps: one, stalk treatment process: stalk is spare by second-time breakage；Two, vinasse tailing treatment technology: are passed through air, ethyl alcohol is set to generate acetic acid, and original starch also reacts and generates acetic acid, make tailing acidified, decomposition or decomposed, three, be granulated: 1) vinasse that step 2 obtains and Tailings mixture being delivered into mixing fermentor by the stalk broken again that screw conveyor and step 1 obtain simultaneously, stirring at 3-5 days, while stirring into mixture sprinkling decomposition of cellulose and tailing functional flora；2) after fermentation maturity 5-12 days, drying obtains finished product after being granulated.The technique and system, which can have, obtains the high organic fertilizer of fertility, and with short production cycle.
Description
Technical field
The present invention relates to a kind of production technologies of biomass organic fertilizer, specifically design it is a kind of using vinasse, stalk and
The technique of the wastes such as gangue production organic fertilizer.
Background technique
In recent years, domestic scholar expert proposes to need to change the simple sight pursued high yield and ignore environmental protection one after another
It reads, abandons " chemical industry agricultural ", substantially " lose weight " for arable land, actively turn to and come in " green ecological agricultural " road for development.In agricultural
Development under the new situation there is an urgent need to research and develop the new and high technology of new and effective bio-organic fertilizer and vanguard technology, gradually
Traditional fertilizer is substituted, the negative effect for the various historical accumulations that arable soil occurs during improvement fertilizer application, this is also can
The inevitable requirement of sustainable agriculture development.
Biological organic fertilizer is mainly with rural area fowl and animal excrement, agricultural crop straw, the organic waste of processing of farm products, city
House refuse is raw material, and functional microbial microbial inoculum is added, by continuous pool aerobic fermentation technology, reach fast deodorization,
Decomposed, dehydration, ultimately forms high-efficiency activated new-type fertilizer.
In recent years, agricultural production waste agricultural crop straw is increasingly becoming the new source of environmental pollution, there are many drawbacks,
Bottleneck problem as rural environmental protection.
In addition, as the industrialization fast development of Chinese traditional liquor industry size is (see national last decade white wine yield column
Figure, data are arranged by Zhong Shang industrial research institute), the comprehensive resource recycling of maximum by-product spirit stillage also perplexs always
Brewed spirit enterprise.
And it is usually highly difficult to digest these wastes, in addition, to solve the problems, such as that chemical fertilizer abuse is also a very disaster
Topic.
Summary of the invention
The object of the present invention is to provide one kind, comprehensively utilize Common Waste, the vinasse that are used, stalk, bastard coal
Stone becomes the technique and fertilizer of agricultural environmental protection type fertilizer.
To achieve the goals above, the present invention the following steps are included:
One, stalk treatment process
1) stalk is crushed to the quarter butt of 1-3cm long using straw crusher；
2) broken moisture content of straws is adjusted to 15-23%；
3) stalk for obtaining step 2) carries out second-time breakage；
Two, tailing treatment technology
1) vinasse are directly passed through into the second screw rod bulking machine from the bottom end of vinasse fermentation tank and is transported to tailing acidifying fermentation tank
In, through the temperature inside air-cooled or water-cool control the second screw rod bulking machine in 105-110 degrees Celsius；
2) vinasse after extruding are directly sent into tailing acidifying fermentation tank by the second screw conveyor；
3) tailing is broken into the particle of 1-3mm by crusher,
4) broken tailings particles are stored in powder holding vessel after proportion；
5) it by the Tailings transportation after proportion to the discharge port of the second screw rod bulking machine, is mixed with the vinasse of extruding；
6) be passed through air into tailing acidifying fermentation tank, after testing pH value between 6.5-7.5 when complete tailing
Acidification is decomposed；
Three, it is granulated
1) vinasse that step 2 obtains and the stalk that Tailings mixture copper is obtained by screw conveyor and step 1 are same
When deliver into mixing fermentor, stirring at 3-5 days, stirring while, sprays the function of decomposition of cellulose and tailing into mixture
It can flora；
2) after fermentation maturity 5-12 days, the particle of 1-2mm is ground into after low temperature drying, through granulation after obtain at
Product.
Preferably, second-time breakage is completed using crusher or screw rod bulking machine, when using screw rod bulking machine, passes through water cooling
Or the maximum temperature in air-cooled control screw rod bulking machine is in 105-115 degree Celsius range；
Preferably, the functional flora includes cellulase activity bacterium and aspergillus niger.
Further, the feeding assembly of the mixing fermentor includes feed hopper, and feed hopper includes top cover, with screw rod extruding
The discharge port of machine and screw conveyor can open the sealing connection unloaded, and the bottom end of feed hopper is connected to coaxial pillar buoy, column
The bottom end of shape cylinder is connected to a coaxial conically shaped, and the material spreading cone that a cone angle is not more than conically shaped, bulk cargo are fixed in conically shaped
Gap between the conical surface of cone and the inner wall of conically shaped is within the scope of 2-5cm；
It further include a shaft, feed hopper is stretched out on shaft top, and shaft is coaxial with feed hopper, and top passes through transmission mechanism
By speed reducer or motor drive, shaft, which is located on the part on pillar buoy top, fixes the first stirring rod, the first stirring rod it is vacant
Diagonally downward, for tilt angle within the scope of 15-35 degree, the first stirring rod has multiple groups, every group of 2-8 root, and the first of same group stirs at end
The fixed point for mixing bar and shaft is located in the same horizontal position, and same group of the first stirring rod is uniformly distributed along the axis of shaft,
Within the scope of 2-3cm, the first stirring rod is taken up space vertical in gap between the vacant end and pillar buoy inner wall of first stirring rod
It is the 1/5-1/3 of pillar buoy to height；
The second stirring rod is fixed below the first stirring rod, the second stirring rod is horizontally disposed, and the second stirring rod has multiple groups,
Every group of 2-8 root, same group of the second stirring rod and the fixed point of shaft are located in the same horizontal position, and same group second stirring
Bar is uniformly distributed along shaft axis, and the gap between the vacant end and pillar buoy inner wall of the second stirring rod is within the scope of 1-2cm, and
Longitudinal height that two stirring rods are taken up space is the 1/3-1/2 of pillar buoy；
In the fixed third stirring rod in the lower section of the second stirring rod, the vacant end of third stirring rod is located at continuous helicoid
On, between the 3-6cm in the gap between the vacant end and pillar buoy inner wall of third stirring rod, angle that third stirring rod tilts down
For degree between 10-25 degree, third stirring rod has multiple groups, and third of the every group of continuous helicoid in 360 degree of shaft, every group is stirred
It mixes bar to be uniformly distributed, and quantity is in 6-10 root；
In fixed the 4th stirring rod of 2-6 root in the bottom end of shaft, the 4th stirring rod protrudes into the sky between material spreading cone and conically shaped
In gap, and do not contact material spreading cone and conically shaped.
Further, the vacant end of third stirring rod is linked together by metallic rod or wire.
Further, the bottom end of material spreading cone and conically shaped gap is stretched out at the vacant end of the 4th stirring rod, into mixing
In fermentor.
Further, more air inlet pipe are fixed in the tailing acidifying fermentation tank, air inlet pipe is in tailing acidifying fermentation tank
It is uniformly distributed in longitudinal extent, equally distributed venthole is opened up in air inlet pipe.
The beneficial effects of the present invention are:
1, stalk is broken by two-stage, wherein being crushed the progress for being conducive to broken process after controlling humidity again, reduces
Energy consumption；
Furthermore in second-time breakage one of option be can effectively be shortened by the extruding of stalk cellulose decomposition when
Between, improve production efficiency；
2, preliminary decomposition is carried out to tailing by the acetic acid generated using vinasse, does not need to carry out tailing in meticulous powder
Mill reduces power consumption, and accelerates the decomposition rate of later period tailing, the rate for release of building up fertility；
3, the organic fertilizer that manufacture is not less than common chemical fertilizer or compound fertilizer's fertility is able to produce by process above and equipment,
The discharge for reducing waste, turns waste into wealth, and efficiently uses, and reduces environmental pressure, improves the effect of the utilization of resources.
Detailed description of the invention
Fig. 1 is technique flow device system.
Fig. 2 is the feed pipe component of mixing fermentor.
Fig. 3 is mine tailing acidification decomposition technique device systems
Specific embodiment
Invention is described in detail with reference to the accompanying drawing.
As shown in Figures 1 to 3, a kind of vinasse of microbe-mediated, stalk, gangue entirely first biological organic fertilizer production technology and
System, as shown in Figure 1, comprising the following steps:
One, stalk treatment process
1) stalk is crushed to the quarter butt of 1-3cm long using straw crusher；
2) broken moisture content of straws is adjusted to 15-23%；
3) stalk that step 2) obtains is crushed again.
4) purpose being crushed again is the rate in order to accelerate cellulose decomposition in stalk, and broken mode can be selected again
It selects using crusher, also or by screw rod bulking machine, is existed by the maximum temperature in water cooling or air-cooled control screw rod bulking machine
In 105-115 degree Celsius range；The decomposition for being cellulose using maximum difficult point of stalk, cellulose are main groups of stalk
Point, it can just be made to the fertilizer quickly absorbed by crop by separation structure, but to lead to by flora come decomposition of cellulose
It often to take a substantial amount of time, therefore pass through the swollen machine of screw rod, the water in stalk gasifies in bulking machine, loses in exit moment
Pressure makes structure become loosely, to be conducive to subsequent fermentation and decompose, the time of subsequent fermentation can be greatly decreased；
Two, tailing treatment technology
1) vinasse are directly passed through into the second screw rod bulking machine from the bottom end of vinasse fermentation tank and is transported to tailing acidifying fermentation tank
In, why will be to vinasse through the temperature inside air-cooled or water-cool control the second screw rod bulking machine in 105-110 degrees Celsius
Just extruding, it is therefore intended that dispersion vinasse.Because the vinasse through everfermentation are still very sticky, in order to allow it can with mine tailing
Be sufficiently mixed, also for it is subsequent can better air inlet, therefore to vinasse carry out extruding；
2) vinasse after extruding are directly sent into tailing acidifying fermentation tank by the second screw conveyor；
3) tailing is broken into the particle of 1-3mm by crusher, and the grinding of tailing, the growth of one grade energy consumption of every drop is simultaneously
It is not linear increase, usually bigger than linear increase amount is more, and especially in partial size lower than after 1mm, the time of grinding will be grown
Very much.And the suction of the components such as the particle size of tailing and potassium contained therein, phosphorus has direct relationship, partial size is smaller, these
It is faster for the speed of separating out of the component of plant production.As gangue contain Fe2O3, CaO in varying numbers, MgO, Na2O,
K2O, P2O5, SO3 and micro rare element (gallium, vanadium, titanium, cobalt).By under solid fermentation process microorganisms slacking
Gradually dissolution release separate out, is directly absorbed and utilized for plant.Such as low grade potassium mine, potassium is necessary three kinds of crop growth
One of basic nutrition element, Potassium In Plants account for the 0.2~4.1% of dry matter content, are only second to nitrogen.In plant growth and development mistake
Cheng Zhong, potassium take part in the activation of 60 kinds or more enzyme systems, the transport of photosynthesis and assimilation products, the metabolism of carbohydrate
With the processes such as the synthesis of protein；Potassium can also enhance the anti-adversity abilities such as disease and insect resistance, resistant to lodging, drought resisting and the cold-resistant of crop, from
And the arable land potassium deficiency of the yield and quality about 70% of crop can be improved, about 45% arable land severe potassium deficiency, nitrogen in China's fertilizer,
Phosphorus, potassium ratio are 1:0.4:0.16, and much smaller than the 1:0.5:0.4 of developed country, these have become limitation crop yield and quality
An important factor for raising.By microorganism to the slow organic weathering research of low grade potassium miberal powder, it is available to improve plant
K element concentration, while being also that the minerals in arable land are supplemented, restore soil fertility, extend fertilizer efficiency.For another example low-grade phosphate ore is utilized and is ground
The phosphate rock resource for studying carefully 80% or more China is mid low grade phosphate rock.Mid low grade phosphate rock powder is total with the microorganism with Soluble phosphorus function
With application, the phosphorus of slightly solubility is gradated as the available phosphorus source of plant, promotion plant by slow biologic weathering process
Growth.
4) broken tailings particles are stored in powder holding vessel after proportion；
5) it by the Tailings transportation after proportion to the discharge port of the second screw rod bulking machine, is mixed with the vinasse of extruding；
6) be passed through air into tailing acidifying fermentation tank, after testing pH value between 6.5-7.5 when complete tailing
Acidification is decomposed.It allows remaining alcohol to pass through reacting for aerobic bacteria with oxygen, generates acetic acid, and remaining starch or grape in vinasse
Sugar also can generate acetic acid by the reaction of aerobic bacteria, and C2H5OH+O2===CH3COOH+H2O decomposes tailing using acetic acid
In calcium carbonate, make that tailing decomposes or quality becomes loose, be conducive to the precipitation of the wherein components such as potassium, phosphorus；
Three, it is granulated
1) after the vinasse and Tailings mixture copper obtained step 2 are by screw conveyor and the extruding of step 1 acquisition
Stalk deliver into mixing fermentor simultaneously, stirring at 3-5 days, while stirring into mixture spraying function flora, function
Energy flora includes that cellulase activity bacterium is used to decompose tailing for decomposition of cellulose, aspergillus niger；
2) after fermentation maturity 5-12 days, the particle of 1-2mm is ground into after low temperature drying, through granulation after obtain at
Product.
By above step, complete first biological organic fertilizer of quick release fertility can be produced, and can will be contracted the production time
Short 1/4-1/3, greatly improves production efficiency.
Stalk, the spirit stillage, three element fertilizer of gangue produced using process above and equipment, total production time 10
It.It and be by the mixture production time that straw bulking and tailing are acidified is 22 days.With North Jiangsu Area " Xu wheat 856 " product
It kind is research object, the fertilizer produced using process above and compound fertilizer (Jiangsu Heng Kang Fei Ye Co., Ltd get profit rich compound fertilizer)
And it does not apply fertilizer and compares test as a control group.Amount of application is 150kg/hm2, 3 repetitions, each plot area
100m2 amounts to 12 trial zones.By completely planting it, wheat average after conversion of receiving are as follows: control group 485.3
Kg/acre, 536.5 kgs/acre of compound fertilizer's group, apply public using the wheat per mu yield 532.4 of three element fertilizers of process above production
Pound/acre.It can be seen that biggish gap is had no using the effect of technique production fertilizer and common compound fertilizer, it can be as compound fertilizer
Substitute is promoted and applied on a large scale.
Step 3-1) in the feeding assembly 30 of mixing fermentor need to carry out special design because to guarantee fertilizer
The uniform mixing it is necessary to guarantee stalk and vinasse Tailings mixture of material component will uniformly, but two kinds of compositional viscosities are all larger,
Therefore to guarantee in the little particle fertilizer of finished product component uniformly it is necessary to being designed to feeding assembly 30.It includes feed hopper 31,
Feed hopper includes top cover, can open the sealing unloaded with the discharge port of screw rod bulking machine and screw conveyor and be connected to, do so
It is to be also convenient for adjustment gas component, the bottom end of feed hopper 31 is connected to coaxial pillar buoy 32, pillar buoy in order to avoid temperature is scattered and disappeared
32 bottom end is connected to a coaxial conically shaped 37, and the material spreading cone that a cone angle is not more than conically shaped 37 is fixed in conically shaped 37
39, the gap between the conical surface of material spreading cone 39 and the inner wall of conically shaped 37 is within the scope of 2-5cm；
It further include a shaft 33, feed hopper 31 is stretched out on 33 top of shaft, and shaft and feed hopper 31 are coaxial, and top passes through
For transmission mechanism by speed reducer or motor drive, shaft 33, which is located on the part on 32 top of pillar buoy, fixes the first stirring rod 34, the
Diagonally downward, for tilt angle within the scope of 15-35 degree, the first stirring rod 34 has multiple groups, every group of 2-8 at the vacant end of one stirring rod 34
Root, same group of the first stirring rod and the fixed point of shaft 33 are located in the same horizontal position, and same group of the first stirring rod 34
Axis along shaft 33 is uniformly distributed, and the gap between 32 inner wall of vacant end and pillar buoy of the first stirring rod 34 is in 2-3cm model
In enclosing, longitudinal height that the first stirring rod 34 is taken up space is the 1/5-1/3 of pillar buoy；The effect of first stirring rod 34 is mainly
In order to which material to be fed down into pillar buoy, and play the role of certain breaing up object and stirring material；
The second stirring rod 35 is fixed in the lower section of the first stirring rod 34, the second stirring rod 35 is horizontally disposed, the second stirring rod
35 have multiple groups, every group of 2-8 root, and same group of the second stirring rod 35 and the fixed point of shaft 33 are located in the same horizontal position, and
Same group of the second stirring rod 35 is uniformly distributed along shaft axis, between the vacant end and pillar buoy inner wall of the second stirring rod 35 between
For gap within the scope of 1-2cm, longitudinal height that the second stirring rod 35 is taken up space is the 1/3-1/2 of pillar buoy；Second stirring rod 35
Main function be to break up and mixed material,
In the fixed third stirring rod 36 in the lower section of the second stirring rod 35, the vacant end of third stirring rod 36 is located at continuous spiral shell
On radial facing, and metallic rod can be used for the vacant end of third stirring rod 36 or wire links together；Third stirring rod 36
Effect mainly conveys downwards material, but since in order to guarantee that material dispersion is uniform, the revolving speed of shaft 33 can quickly, therefore
Third stirring rod 36 is substituted for spiral flow deflector, the speed that material conveys downwards will be too fast, therefore uses continuous bar
Replace flow deflector, and in order to reduce the speed of conveying, between 32 inner wall of vacant end and pillar buoy of third stirring rod 36 between
Between the 3-6cm of gap, in this way, the angle that third stirring rod 36 tilts down is between 10-25 degree, third stirring rod 36 has more
Group, third stirring rod 36 of the every group of continuous helicoid in 360 degree of shaft, every group is uniformly distributed, and quantity is in 6-10 root；
In fixed the 4th stirring rod 38 of 2-6 root in the bottom end of shaft 33, the 4th stirring rod 38 protrudes into material spreading cone 39 and conically shaped
In gap between 37, and material spreading cone and conically shaped 37 are not contacted.
The foregoing is merely the preferred embodiment of the present invention, are not intended to restrict the invention, for those skilled in the art
For member, the invention may be variously modified and varied.All any modifications in spirit of that invention and principle, made are equal
Replacement, improvement etc., should all be included in the protection scope of the present invention.
Claims (7)
1. a kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system, including following step entirely
It is rapid:
One, stalk treatment process
1) stalk is crushed to the quarter butt of 1-3cm long using straw crusher；
2) broken moisture content of straws is adjusted to 15-23%；
3) stalk for obtaining step 2) carries out second-time breakage；
Two, tailing treatment technology
1) vinasse are directly passed through the second screw rod bulking machine from the bottom end of vinasse fermentation tank to be transported in tailing acidifying fermentation tank, is led to
The temperature inside air-cooled or water-cool control the second screw rod bulking machine is crossed in 105-110 degrees Celsius；
2) vinasse after extruding are directly sent into tailing acidifying fermentation tank by the second screw conveyor；
3) tailing is broken into the particle of 1-3mm by crusher,
4) broken tailings particles are stored in powder holding vessel after proportion；
5) it by the Tailings transportation after proportion to the discharge port of the second screw rod bulking machine, is mixed with the vinasse of extruding；
6) be passed through air into tailing acidifying fermentation tank, after testing pH value between 6.5-7.5 when complete tailing acidification
It decomposes；
Three, it is granulated
1) vinasse that step 2 obtains and the stalk that Tailings mixture copper is obtained by screw conveyor and step 1 are defeated simultaneously
It is fed into mixing fermentor, stirring at 3-5 days, stirring while sprays the function bacterium of decomposition of cellulose and tailing into mixture
Group；
2) after fermentation maturity 5-12 days, it is ground into the particle of 1-2mm after low temperature drying, obtains finished product after being granulated.
2. the vinasse of microbe-mediated according to claim 1, stalk, gangue entirely first biological organic fertilizer production technology and
System, which is characterized in that second-time breakage is completed using crusher or screw rod bulking machine, when using screw rod bulking machine, passes through water
Maximum temperature in cold or air-cooled control screw rod bulking machine is in 105-115 degree Celsius range.
3. the vinasse of microbe-mediated according to claim 1, stalk, gangue entirely first biological organic fertilizer production technology and
System, which is characterized in that the functional flora includes cellulase activity bacterium and aspergillus niger.
4. the vinasse of microbe-mediated according to claim 1, stalk, gangue entirely first biological organic fertilizer production technology and
System, which is characterized in that the feeding assembly of the mixing fermentor includes feed hopper, and feed hopper includes top cover, with screw rod extruding
The discharge port of machine and screw conveyor can open the sealing connection unloaded, and the bottom end of feed hopper is connected to coaxial pillar buoy, column
The bottom end of shape cylinder is connected to a coaxial conically shaped, and the material spreading cone that a cone angle is not more than conically shaped, bulk cargo are fixed in conically shaped
Gap between the conical surface of cone and the inner wall of conically shaped is within the scope of 2-5cm；
It further include a shaft, feed hopper is stretched out on shaft top, and shaft is coaxial with feed hopper, and top is by transmission mechanism by subtracting
Fast machine or motor drive, shaft, which is located on the part on pillar buoy top, fixes the first stirring rod, and the vacant end of the first stirring rod is inclined
Obliquely, for tilt angle within the scope of 15-35 degree, the first stirring rod has multiple groups, every group of 2-8 root, same group of the first stirring rod
It is located in the same horizontal position with the fixed point of shaft, and same group of the first stirring rod is uniformly distributed along the axis of shaft, first
Within the scope of 2-3cm, the first stirring rod is taken up space longitudinal high in gap between the vacant end and pillar buoy inner wall of stirring rod
Degree is the 1/5-1/3 of pillar buoy；
Fix the second stirring rod below the first stirring rod, the second stirring rod is horizontally disposed, and the second stirring rod has a multiple groups, and every group
2-8 root, same group of the second stirring rod and the fixed point of shaft are located in the same horizontal position, and same group of the second stirring rod edge
Shaft axis is uniformly distributed, and within the scope of 1-2cm, second stirs in the gap between the vacant end and pillar buoy inner wall of the second stirring rod
Mix the 1/3-1/2 that longitudinal height that bar is taken up space is pillar buoy；
In the fixed third stirring rod in the lower section of the second stirring rod, the vacant end of third stirring rod is located on continuous helicoid, the
Between the 3-6cm in the gap between the vacant end and pillar buoy inner wall of three stirring rods, the angle that third stirring rod tilts down exists
Between 10-25 degree, third stirring rod has multiple groups, third stirring rod of the every group of continuous helicoid in 360 degree of shaft, every group
It is uniformly distributed, and quantity is in 6-10 root；
In fixed the 4th stirring rod of 2-6 root in the bottom end of shaft, the 4th stirring rod is protruded into the gap between material spreading cone and conically shaped,
And do not contact material spreading cone and conically shaped.
5. the vinasse of microbe-mediated according to claim 4, stalk, gangue entirely first biological organic fertilizer production technology and
System, which is characterized in that the vacant end of third stirring rod is linked together by metallic rod or wire.
6. the vinasse of microbe-mediated according to claim 4, stalk, gangue entirely first biological organic fertilizer production technology and
System, which is characterized in that the bottom end of material spreading cone and conically shaped gap is stretched out at the vacant end of the 4th stirring rod, is sent out into mixing
In fermentation tank.
7. first biological organic fertilizer is raw entirely for the vinasse of microbe-mediated according to claim 1-6, stalk, gangue
Production. art and system, which is characterized in that more air inlet pipe are fixed in the tailing acidifying fermentation tank, air inlet pipe is acidified in tailing and sends out
It is uniformly distributed in the longitudinal extent of fermentation tank, equally distributed venthole is opened up in air inlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910145922.4A CN109650975A (en) | 2019-02-27 | 2019-02-27 | A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910145922.4A CN109650975A (en) | 2019-02-27 | 2019-02-27 | A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109650975A true CN109650975A (en) | 2019-04-19 |
Family
ID=66123838
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910145922.4A Pending CN109650975A (en) | 2019-02-27 | 2019-02-27 | A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109650975A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112279243A (en) * | 2020-10-21 | 2021-01-29 | 太原理工大学 | Coal gangue-sludge-based activated carbon, preparation method thereof and application thereof in mediating and strengthening anaerobic digestion of sewage |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101830746A (en) * | 2009-03-09 | 2010-09-15 | 上海园康富硒生物科技有限公司 | Method for producing selenium-enriched organic fertilizer |
| CN102701826A (en) * | 2012-06-16 | 2012-10-03 | 中国有色桂林矿产地质研究院有限公司 | Method for stacking tailings for reclamation |
| CN102992915A (en) * | 2012-11-30 | 2013-03-27 | 张有聪 | Method for preparing environment-friendly and high-efficiency biological organic fertilizer by using distilled spirit vinasse |
| CN106748208A (en) * | 2016-12-29 | 2017-05-31 | 常熟市添源环保科技有限公司 | A kind of preparation method of vinasse composite highly effective biological organic fertilizer |
| CN108164300A (en) * | 2016-12-07 | 2018-06-15 | 深圳市祁科作物科技有限公司 | A kind of fermentation tank and its fermentation process and purposes |
| CN207552204U (en) * | 2017-11-27 | 2018-06-29 | 黑龙江省畜牧研究所 | A kind of automation tank body organic fertilizer fermentation equipment |
| CN108911810A (en) * | 2018-09-03 | 2018-11-30 | 贵州大学 | With the method for phosphorite tailings and Maotai-flavor liquor vinasse production organic fertilizer |
-
2019
- 2019-02-27 CN CN201910145922.4A patent/CN109650975A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101830746A (en) * | 2009-03-09 | 2010-09-15 | 上海园康富硒生物科技有限公司 | Method for producing selenium-enriched organic fertilizer |
| CN102701826A (en) * | 2012-06-16 | 2012-10-03 | 中国有色桂林矿产地质研究院有限公司 | Method for stacking tailings for reclamation |
| CN102992915A (en) * | 2012-11-30 | 2013-03-27 | 张有聪 | Method for preparing environment-friendly and high-efficiency biological organic fertilizer by using distilled spirit vinasse |
| CN108164300A (en) * | 2016-12-07 | 2018-06-15 | 深圳市祁科作物科技有限公司 | A kind of fermentation tank and its fermentation process and purposes |
| CN106748208A (en) * | 2016-12-29 | 2017-05-31 | 常熟市添源环保科技有限公司 | A kind of preparation method of vinasse composite highly effective biological organic fertilizer |
| CN207552204U (en) * | 2017-11-27 | 2018-06-29 | 黑龙江省畜牧研究所 | A kind of automation tank body organic fertilizer fermentation equipment |
| CN108911810A (en) * | 2018-09-03 | 2018-11-30 | 贵州大学 | With the method for phosphorite tailings and Maotai-flavor liquor vinasse production organic fertilizer |
Non-Patent Citations (2)
| Title |
|---|
| 李延云: "《农作物秸秆饲料加工技术》", 31 July 2006, 中国轻工业出版社 * |
| 王敦球等: "《固体废物处理工程》", 31 August 2015, 中国环境科学出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112279243A (en) * | 2020-10-21 | 2021-01-29 | 太原理工大学 | Coal gangue-sludge-based activated carbon, preparation method thereof and application thereof in mediating and strengthening anaerobic digestion of sewage |
| CN112279243B (en) * | 2020-10-21 | 2022-05-17 | 太原理工大学 | Coal gangue-sludge-based activated carbon, preparation method thereof and application thereof in mediating and strengthening anaerobic digestion of sewage |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209522781U (en) | A kind of organic waste anaerobic fermentation biogas residue fertilizer producing system | |
| CN101891544A (en) | Functional bioorganic and semi-organic fertilizers and preparation method thereof | |
| CN105523861A (en) | Suspension-type vinasse fermented liquid fertilizer and preparation method thereof | |
| CN106518215A (en) | Method for preparing organic fertilizer by harmless treatment and reutilization of waste mushroom resources | |
| CN104366680B (en) | One breeding hen feed automatic processing apparatus and chicken feed preparation method | |
| CN104692847A (en) | Method for producing high-macroelement liquid organic special fertilizer | |
| CN106616005A (en) | Method for producing fish feed by using filtered sludge from sugar factory | |
| CN102367458A (en) | Method for preparing methane by pretreating asparagus straws with NaOH | |
| CN103772056B (en) | Organic biological active fertilizer utilizing swollen quick-fried technology to produce and preparation method thereof | |
| CN107344880A (en) | A kind of method that ultrasonic wave prepares fertilizer with alkali Combined Treatment agricultural wastes | |
| CN109384484A (en) | Low-energy-consumption high-efficiency farm fermentation cabin | |
| CN109650975A (en) | A kind of vinasse of microbe-mediated, stalk, gangue first biological organic fertilizer production technology and system entirely | |
| CN105523788A (en) | Distiller's grain anaerobic oxygen consumption secondary fermentation organic fertilizer and preparation method thereof | |
| CN107032854A (en) | The method that stalk fermentation biogas residue prepares organic fertilizer | |
| CN202385711U (en) | Prawn biological feed manufacturing system | |
| CN104230422A (en) | Method for producing bio-organic fertilizer by utilizing beer lees | |
| CN107129347A (en) | A kind of preparation method of the slow control organic fertilizer of charcoal base | |
| CN208732964U (en) | A kind of device of the useless fruit harmless treatment of honey shaddock | |
| CN107344881A (en) | The method that agricultural wastes prepare fertilizer is handled under the conditions of a kind of ozone | |
| CN101343641A (en) | Marsh gas fermentation technique with calcium carbonate as buffering agent for centralized air feed | |
| CN105777351B (en) | Preparation method of pig manure fermentation-free low-cost organic fertilizer | |
| CN104355693A (en) | Organic fertilizer | |
| CN215440273U (en) | Complete production equipment for selenium-rich foliar fertilizer | |
| CN1083457A (en) | Bioorganic compound fertilizer and manufacture method | |
| CN112279694B (en) | Granulator for straw fermentation biofertilizer |
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 | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190419 |
|
| WD01 | Invention patent application deemed withdrawn after publication |