CN106397064A - Method for producing biological organic fertilizer by using waste vegetable leaves as main material - Google Patents
Method for producing biological organic fertilizer by using waste vegetable leaves as main material Download PDFInfo
- Publication number
- CN106397064A CN106397064A CN201611134922.7A CN201611134922A CN106397064A CN 106397064 A CN106397064 A CN 106397064A CN 201611134922 A CN201611134922 A CN 201611134922A CN 106397064 A CN106397064 A CN 106397064A
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- Prior art keywords
- dish leaf
- fermentation
- temperature
- vegetable leaves
- waste vegetable
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- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/80—Soil conditioners
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D1/00—Fertilisers containing potassium
-
- 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
- C05F17/50—Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment
-
- 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
- C05F17/90—Apparatus therefor
- C05F17/964—Constructional parts, e.g. floors, covers or doors
- C05F17/971—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material
-
- 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
The invention discloses a method for producing a biological organic fertilizer by using waste vegetable leaves as a main material. The method comprises the following steps: A. separation; B. crushing; C. precipitation; D. dewatering; E. drying; F. proportioning; and G. fermentation. The hot air drying has favorable dewatering effect, and increases the temperature of the vegetable leaves; the hot vegetable leaves are immediately mixed with the other raw materials into a heap and subjected to fermentation, thereby increasing the initial temperature of the fermentation heap, being beneficial to quick reproduction of fermentative bacteria and enhancing the fermentation efficiency. The traditional fermentation heap can be heated to 60 DEG C after three days, but the fermentation heap in the invention can be heated to 60 DEG C within one day, so the production efficiency is obviously enhanced. Besides, the traditional fermentation heap needs to be overturned to avoid the overhigh temperature which is not beneficial to fermentation. In the invention, a radiating tube is inserted into the fermentation heap to perform heat dissipation, so that the temperature is always kept within the appropriate ranged, and the heat overturning is not needed, thereby saving the time; and thus, the whole fermentation process can be completed by 7-8 days, so the fermentation time is greatly shorter than that of the traditional fermentation heap.
Description
Technical field
The present invention relates to organic fertilizer production technical field is and in particular to one kind produces biological organic with waste vegetable leaves for major ingredient
Fertile method.
Background technology
In a lot of vegetable places of production, the trade market of vegetable will produce substantial amounts of abandoned vegetable leaf daily, if directly abandoned
Pollute the environment, these abandoned vegetables have certain nutritive value, therefore, recycling is the feasible side processing useless dish leaf
One of formula.Useless dish leaf can be used for making fertilizer or feedstuff, and the patent of invention of Application No. 201110058132.6 discloses
A kind of recycling production process of discarded vegetable leaves, it makes the technique of fertilizer and includes following operation：(1) waste vegetable leaves sorting：
Manually corrupt dish leaf is sorted out from discarded dish leaf；(2) the non-putrid vegetable leaves putrid vegetable leaves selected are carried out break process, by it
It is broken into the strip fragment of 2 to 10 mm in sizes；Extrusion dehydration process is carried out to fragment, makes the moisture content of dish leaf drop to 50%
To between 60%；To dehydration after dish leaf fragment be dried process, dried dish leaf fragment moisture control 10% to
Between 15%；Separating twice is carried out to dried dish leaf fragment, after pulverizing, carries out sub-sieve with the screen cloth of 60 mesh；To sub-sieve out
Dish leaf powder packed, manufacture dish leaf feed meal；(3), the dish leaf that addles sorting out in operation (1) is carried out broken place
Reason, is broken into the dish leaf fragment that addles of 2 to 10 mm in sizes；Extrusion dehydration process is carried out to fragment, makes the aqueous of fragment
Rate drops between 50% to 60%；Brown coal, chicken manure, Nicotiana tabacum L. powder and fermentation is added in the dish leaf fragment that addles after dewatering
Bacterium, carries out heap ridge fermentation after being uniformly mixed, when fermentation heap internal temperature rises to 65-70 DEG C, carry out turning process, turn over
When pile-after-fermentation thing temperature is down to room temperature, carry out heap ridge fermentation again, after three to five heap ridge fermentations, fermented product is fully rotten
Ripe, make organic fertilizer.In above-mentioned technique, because the temperature of material when just starting to ferment is very low, need through longer time
Just 65-70 DEG C can be warming up to, the time that fermentation procedure takies is more, less efficient.
Content of the invention
It is an object of the invention to provide a kind of method producing biological organic fertilizer for major ingredient with waste vegetable leaves, shorten fermentation
Time, improve production efficiency.
The object of the present invention is achieved like this：A kind of method producing biological organic fertilizer for major ingredient with waste vegetable leaves, bag
Include following steps：
A, sorting：By the stone in waste vegetable leaves, plastics, metal impurities detection；
B, broken：Waste vegetable leaves cutting and crushing is become the rectangular block that length is 1cm～3cm；
C, precipitation：The dish leaf that step B is obtained puts into sedimentation tank precipitation, isolates the juice producing during cutting and crushing, dish leaf contains
Water rate is reduced to 75%～85%；
D, dehydration：The dish leaf that step C is obtained carries out extrusion dehydration, makes the moisture content of dish leaf be reduced to 45%～55%；
E, drying：Obtain dish leaf using the hot blast that temperature is 1000 DEG C～1200 DEG C to step D to dry, make the aqueous of dish leaf
Rate is reduced to 25%～35%, and the temperature of dish leaf is increased to 100 DEG C～120 DEG C；
F, dispensing：The dish leaf that step E is obtained uniformly is mixed with chicken manure, sheep stool, humic acidss, zymocyte, plant ash, wood flour, its
In, the mass percent of each component is respectively dish leaf 40%～45%, chicken manure 10%～20%, sheep stool 10%～20%, and humic acidss 5%～
15%, zymocyte 1%～5%, plant ash 10%～15%, wood flour 10%～15%, after mixing, the temperature of mixture is 40 DEG C～50 DEG C；
G, fermentation：The mixture that step F is obtained temperature be 30 DEG C～60 DEG C environment in code to become height be 1.5m～2m
Fermentation heap；In 1 day, the temperature of fermentation heap is increased to 55 DEG C～65 DEG C, ambient temperature is reduced to 15 DEG C～25 DEG C, Ran Houxiang
Insert radiating tube in fermentation heap, make the temperature of fermentation heap be maintained at 55 DEG C～65 DEG C, then after 6～7 days, obtain having of maturation
Machine is fertile.
Further, step B and C are carried out in broken drying all-in-one machine, the top setting of described broken drying all-in-one machine
There is feed hopper, be internally provided with screen plate, the top of described screen plate is provided with discharge door, and sets between screen plate and feed hopper
It is equipped with a pair of cutting blade；Dish leaf enters broken drying all-in-one machine by feed hopper, is got rid of after cutting blade cutting
On screen plate, juice is flowed into the lower section of screen plate after screen plate and discharges.
Further, step D to roller extruding all-in-one in carry out, described to roller extrude all-in-one top be provided with into
Material mouth, is provided with a pair of compression roller, is provided with top clearance between two compression rollers below described charging aperture, described compression roller
Lower section is provided with transmission mechanism；Dish leaf falls between a pair of compression roller by charging aperture, and two compression rollers rotate, and dish leaf are brought into crowded
Pressure gap, divides moisture in extrusion dish leaf, then dish leaf drops on transmission mechanism and is transported to subsequent processing by transmission mechanism.
Further, described transmission mechanism is transmission carrier bar.
Further, step E is carried out in rotary kiln, and described rotary kiln is obliquely installed, and dish leaf is from the upper port of rotary kiln
Enter rotary kiln and move downward, hot blast enters from the lower port of rotary kiln, and hot blast is inversely contacted with dish leaf, takes away the water of dish leaf
Point, so that the temperature of dish leaf is raised simultaneously.
Further, in step E, using air-introduced machine, the high-temperature hot-air obtaining through heat exchange is passed through rotary kiln, high-temperature hot-air
Can be to directly obtain through electrical heating or obtain with high temperature flue-gas from boiler heat exchange.
Further, in step F, zymocyte include colloid bacillus cereus, bacillus subtilises, Brevibacillus laterosporus,
One or more of clothing bacillus cereuss, lactic acid bacteria bacillus and yeast.
Further, after step G, by dry, broken for fertilizer, pelletize, packaging.
The invention has the beneficial effects as follows：Dehydration includes the mode of hot-air seasoning, and not only dehydrating effect is good, also add dish leaf
Temperature, high temperature dish leaf mixed that combine code is in heaps is fermented immediately, increased the initial temperature of fermentation heap, favorably with other raw materials
In zymocyte Fast-propagation, improve the efficiency of fermentation.Through test, traditional fermentation heap can will be warming up to through 3 days about
60 DEG C, and the fermentation heap of the present invention only needs to 1 day to be just warming up to 60 DEG C, production efficiency significantly improves.Additionally, traditional sends out
Ferment heap needs turning, is unfavorable for avoid temperature too high fermenting, and the present invention is dissipated by insertion radiating tube in fermentation heap
Heat, makes temperature remain in suitable scope it is not necessary to turning, saves the time, whole sweat 7 to 8 days can be complete
Become, greatly shorten compared with traditional fermentation time.
Brief description
Fig. 1 is the schematic diagram that the present invention crushes drying all-in-one machine.
Fig. 2 is that the present invention extrudes the schematic diagram of all-in-one to roller.
Fig. 3 is the schematic diagram of rotary kiln of the present invention.
Reference：1 broken drying all-in-one machine；2 screen plates；3 discharge doors；4 feed hoppers；5 cutting blades；
6 pairs of rollers extrude all-in-one；7 charging apertures；8 compression rollers；9 transmission mechanisms；10 rotary kilns.
Specific embodiment
The present invention is further described with reference to the accompanying drawings and examples.
As shown in Figure 1, Figure 2 and Figure 3, a kind of method producing biological organic fertilizer for major ingredient with waste vegetable leaves of the present invention,
Comprise the following steps：
A, sorting：By the stone in waste vegetable leaves, plastics, metal impurities detection, to avoid damaging following process equipment；
B, broken：Waste vegetable leaves cutting and crushing is become the rectangular block that length is 1cm～3cm；
C, precipitation：The dish leaf that step B is obtained puts into sedimentation tank precipitation, isolates the juice producing during cutting and crushing, dish leaf contains
Water rate is reduced to 75%～85%；Substantial amounts of moisture is contained, during cutting and crushing, moisture can flow out from facet, Jing Guojian in dish leaf
After single precipitation, moisture can be leached, reduce the moisture content of dish leaf, mitigate weight.
D, dehydration：The dish leaf that step C is obtained carries out extrusion dehydration, makes the moisture content of dish leaf be reduced to 45%～55%；
E, drying：Obtain dish leaf using the hot blast that temperature is 1000 DEG C～1200 DEG C to step D to dry, make the aqueous of dish leaf
Rate is reduced to 25%～35%, and the temperature of dish leaf is increased to 100 DEG C～120 DEG C；When hot blast is contacted with dish leaf, not only can take away dish
The moisture of leaf surface, also kills most of pathogenic bacteria on dish leaf surface, dish leaf is heated to higher temperature.
F, dispensing：The dish leaf that step E is obtained uniformly is mixed with chicken manure, sheep stool, humic acidss, zymocyte, plant ash, wood flour
Close, wherein, the mass percent of each component is respectively dish leaf 40%～45%, chicken manure 10%～20%, sheep stool 10%～20%, humic acidss
5%～15%, zymocyte 1%～5%, plant ash 10%～15%, wood flour 10%～15%, after mixing, the temperature of mixture is 40 DEG C～50
℃.Chicken manure, sheep stool are the fertilizer of high-quality, and the content of N P and K is high, can strengthen fertilizer efficiency.Humic acidss energy improved soil structure,
Be conducive to the growth of crops.Plant ash contains substantial amounts of potassium element and various trace elements, such as calcium, magnesium, silicon, sulfur and ferrum,
The micronutrient elements such as manganese, copper, zinc, boron, molybdenum, are conducive to preferably meeting plant growing needs.Wood-working factory can produce greatly
The discarded wood flour of amount, sawdust etc., direct discarding can bring very big pressure to environment, and wood flour, sawdust by fermentation after can conduct
Fertilizer, therefore, the present invention adds wood flour, realizes twice laid, further improves fertilizer efficiency simultaneously.In this step, first will weigh
Chicken manure well, sheep stool, humic acidss, zymocyte, plant ash, wood flour pile a pile, after the completion of step E, add high temperature dish leaf immediately
Enter stockpile to be stirred mixing, reduce heat as much as possible and scatter and disappear.After stirring, carry out a yard heap fermentation at once.
G, fermentation：The mixture that step F is obtained temperature be 30 DEG C～60 DEG C environment in code become height be 1.5m～
The fermentation heap of 2m；In 1 day, the temperature of fermentation heap is increased to 55 DEG C～65 DEG C, ambient temperature is reduced to 15 DEG C～25 DEG C, so
Insert radiating tube in backward fermentation heap, make the temperature of fermentation heap be maintained at 55 DEG C～65 DEG C, then after 6～7 days, obtain maturation
Fertilizer.Fermentation can be carried out in the room of setting vent window, and in available step E, the hot blast after dish leaf is by room
Temperature is increased to 30 DEG C～60 DEG C, monitors the temperature of fermentation heap at any time, when temperature is increased to 55 DEG C～65 DEG C, opens ventilation
Window, makes the temperature in room be reduced to 15 DEG C～25 DEG C, when the temperature of fermentation heap continues to rise, inserts radiating tube, radiating tube
Thick bamboo tube or steel pipe, the heat within release fermentation heap, it is to avoid the temperature of fermentation heap is too high can be adopted.The quantity of radiating tube and insert
Enter depth to be adjusted according to the temperature change of fermentation heap.
Dehydration includes the mode of hot-air seasoning, and not only dehydrating effect is good, also add the temperature of dish leaf, high temperature dish leaf is immediately
Mix with other raw materials that combine code is in heaps is fermented, increased the initial temperature of fermentation heap, be conducive to zymocyte Fast-propagation, carry
The efficiency of high fermentation.Through test, traditional fermentation heap will can be warming up to 60 DEG C through 3 days about, and the fermentation of the present invention
Heap only needs to 1 day to be just warming up to 60 DEG C, and production efficiency significantly improves.Additionally, traditional fermentation heap needs turning, to avoid
Temperature too high and be unfavorable for ferment, the present invention pass through in fermentation heap insert radiating tube radiated, so that temperature is remained at
It is not necessary to turning in suitable scope, save the time, traditional fermentation mode needs the time of at least two weeks, and the present invention
Whole sweat can complete for 7 to 8 days, and fermentation time greatly shortens compared with traditional fermentation mode.
Broken process and dehydration procedure can be using prior art it is preferred that step B and C enter in broken drying all-in-one machine 1
OK, the top of described broken drying all-in-one machine 1 is provided with feed hopper 4, is internally provided with screen plate 2, the top of described screen plate 2
It is provided with discharge door 3, and between screen plate 2 and feed hopper 4, be provided with a pair of cutting blade 5；It is broken that dish leaf passes through feed hopper 4 entrance
Broken drying all-in-one machine 1, is got rid of on screen plate 2 after cutting blade 5 cutting, and juice flows into after passing through screen plate 2 and filters
The lower section of plate 2 is simultaneously discharged.Dish leaf is cut into slices while rotation by cutting blade 5, and after cutting, dish leaf is under the drive of cutting blade 5
Get rid of on screen plate 2, make the moisture on dish leaf surface depart from dish leaf in the presence of inertia.Roller is extruded with the charging aperture 7 of all-in-one 6
May be disposed at the lower section of discharge door 3, after the completion of crushing and precipitating, dish leaf is released discharge door 3 and can fall in charging aperture 7, from
Without other transports or transmitting device.
Further, step D is carried out in roller extruding all-in-one 6, and the described top extruding all-in-one 6 to roller is provided with
Charging aperture 7, is provided with a pair of compression roller 8, is provided with top clearance between two compression rollers 8 below described charging aperture 7, described crowded
The lower section of pressure roller 8 is provided with transmission mechanism 9；Dish leaf falls between a pair of compression roller 8 by charging aperture 7, and two compression rollers 8 rotate,
Dish leaf is brought into top clearance, divides moisture in extrusion dish leaf, then dish leaf drops on transmission mechanism 9 and transported by transmission mechanism 9
To subsequent processing.
Described transmission mechanism 9 is transmission carrier bar.Transmission carrier bar itself has gap, and the moisture in dish leaf can be made to discharge.
Step E is carried out in rotary kiln 10, and described rotary kiln 10 is obliquely installed, and dish leaf enters from the upper port of rotary kiln 10
Rotary kiln 10 simultaneously moves downward, and hot blast enters from the lower port of rotary kiln 10, and hot blast is inversely contacted with dish leaf, takes away the water of dish leaf
Point, so that the temperature of dish leaf is raised simultaneously.Rotary kiln 10 constantly rotates during running, and dish leaf can be along rotary kiln 10
Automatically moving downward, and constantly can overturn in rotary kiln 10, thus being fully contacted with hot blast, improving dehydration rate and dehydration
Efficiency.
In step E, using air-introduced machine, the high-temperature flue gas that raw coal combustion produces are collected, high-temperature flue gas are after gas-gas heat exchange
Heat energy is converted air, obtains high-temperature hot-air being passed through in rotary kiln 10 and dish leaf is dried.The raw coal consumption of factory is big, produces
Raw substantial amounts of waste gas, these waste gas have higher temperature, and directly discharge not only contaminated air, also wastes heat energy, therefore, this
These high-temp waste gas are collected by invention, for the drying of dish leaf, take full advantage of the energy, save production cost.
Zymocyte can adopt existing arbitrary strain, selects according to demand, in step F, zymocyte includes colloid spore
One of bacillus, bacillus subtilises, Brevibacillus laterosporus, Bacillus licheniformis, lactic acid bacteria bacillus and yeast
Or it is multiple.
After fermenting, by dry, broken for fertilizer, pelletize, packaging.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for the skill of this area
For art personnel, the present invention can have various modifications and variations.All within the spirit and principles in the present invention, made any repair
Change, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (8)
1. a kind of method with waste vegetable leaves for major ingredient production biological organic fertilizer is it is characterised in that comprise the following steps：
A, sorting：By the stone in waste vegetable leaves, plastics, metal impurities detection；
B, broken：Waste vegetable leaves cutting and crushing is become the rectangular block that length is 1cm～3cm；
C, precipitation：The dish leaf that step B is obtained puts into sedimentation tank precipitation, isolates the juice producing during cutting and crushing, dish leaf contains
Water rate is reduced to 75%～85%；
D, dehydration：The dish leaf that step C is obtained carries out extrusion dehydration, makes the moisture content of dish leaf be reduced to 45%～55%；
E, drying：Obtain dish leaf using the hot blast that temperature is 1000 DEG C～1200 DEG C to step D to dry, make the aqueous of dish leaf
Rate is reduced to 25%～35%, and the temperature of dish leaf is increased to 100 DEG C～120 DEG C；
F, dispensing：The dish leaf that step E is obtained uniformly is mixed with chicken manure, sheep stool, humic acidss, zymocyte, plant ash, wood flour, its
In, the mass percent of each component is respectively dish leaf 40%～45%, chicken manure 10%～20%, sheep stool 10%～20%, and humic acidss 5%～
15%, zymocyte 1%～5%, plant ash 10%～15%, wood flour 10%～15%, after mixing, the temperature of mixture is 40 DEG C～50 DEG C；
G, fermentation：The mixture that step F is obtained temperature be 30 DEG C～60 DEG C environment in code to become height be 1.5m～2m
Fermentation heap；In 1 day, the temperature of fermentation heap is increased to 55 DEG C～65 DEG C, ambient temperature is reduced to 15 DEG C～25 DEG C, Ran Houxiang
Insert radiating tube in fermentation heap, make the temperature of fermentation heap be maintained at 55 DEG C～65 DEG C, then after 6～7 days, obtain having of maturation
Machine is fertile.
2. according to claim 1 a kind of with waste vegetable leaves for major ingredient produce biological organic fertilizer method it is characterised in that：
Step B and C are in broken drying all-in-one machine（1）In carry out, described broken drying all-in-one machine（1）Top be provided with feed hopper（4）,
It is internally provided with screen plate（2）, described screen plate（2）Top be provided with discharge door（3）, and screen plate（2）With feed hopper（4）
Between be provided with a pair of cutting blade（5）；Dish leaf passes through feed hopper（4）Enter broken drying all-in-one machine（1）, through cutting blade
（5）Got rid of in screen plate after cutting（2）On, juice passes through screen plate（2）Flow into screen plate afterwards（2）Lower section and discharge.
3. according to claim 2 a kind of with waste vegetable leaves for major ingredient produce biological organic fertilizer method it is characterised in that：
Step D is extruding all-in-one to roller（6）In carry out, described to roller extrude all-in-one（6）Top be provided with charging aperture（7）, institute
State charging aperture（7）Lower section is provided with a pair of compression roller（8）, two compression rollers（8）Between be provided with top clearance, described compression roller
（8）Lower section be provided with transmission mechanism（9）；Dish leaf passes through charging aperture（7）Fall in a pair of compression roller（8）Between, two compression rollers（8）
Rotate, dish leaf is brought into top clearance, divides moisture in extrusion dish leaf, then dish leaf drops in transmission mechanism（9）Upper and by transmitting
Mechanism（9）It is transported to subsequent processing.
4. according to claim 3 a kind of with waste vegetable leaves for major ingredient produce biological organic fertilizer method it is characterised in that：
Described transmission mechanism（9）For transmitting carrier bar.
5. a kind of method producing biological organic fertilizer for major ingredient with waste vegetable leaves according to claim 1,2,3 or 4, it is special
Levy and be：Step E is in rotary kiln（10）In carry out, described rotary kiln（10）It is obliquely installed, dish leaf is from rotary kiln（10）Upper end
Mouth entrance rotary kiln（10）And move downward, hot blast is from rotary kiln（10）Lower port enter, hot blast inversely contacts with dish leaf, carries
Walk the moisture of dish leaf, so that the temperature of dish leaf is raised simultaneously.
6. according to claim 5 a kind of with waste vegetable leaves for major ingredient produce biological organic fertilizer method it is characterised in that：
In step E, using air-introduced machine, the high-temperature hot-air obtaining through heat exchange is passed through rotary kiln（10）.
7. according to claim 1 a kind of with waste vegetable leaves for major ingredient produce biological organic fertilizer method it is characterised in that：
In step F, zymocyte includes colloid bacillus cereus, bacillus subtilises, Brevibacillus laterosporus, Bacillus licheniformis, lactic acid bacteria
One or more of bacillus and yeast.
8. according to claim 1 a kind of with waste vegetable leaves for major ingredient produce biological organic fertilizer method it is characterised in that：
After step G, by dry, broken for fertilizer, pelletize, packaging.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611134922.7A CN106397064A (en) | 2016-12-11 | 2016-12-11 | Method for producing biological organic fertilizer by using waste vegetable leaves as main material |
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| CN201611134922.7A CN106397064A (en) | 2016-12-11 | 2016-12-11 | Method for producing biological organic fertilizer by using waste vegetable leaves as main material |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108821816A (en) * | 2018-07-04 | 2018-11-16 | 合肥欧语自动化有限公司 | A kind of automated production equipment of liquid state organic fertilizer |
| CN112552084A (en) * | 2020-11-27 | 2021-03-26 | 岳阳佰胜智慧环保科技有限公司 | Organic matter garbage treatment system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102172260A (en) * | 2011-03-11 | 2011-09-07 | 通海县福慧科技有限公司 | Recycling production process of discarded vegetable leaves |
| CN104266474A (en) * | 2014-09-03 | 2015-01-07 | 嘉善圣莱斯绒业有限公司 | Vibratory drying and processing device |
| CN104291886A (en) * | 2014-10-21 | 2015-01-21 | 陕西省微生物研究所 | Composite organic fertilizer prepared from vegetable wastes and preparation method of composite organic fertilizer |
| CN104839437A (en) * | 2015-04-30 | 2015-08-19 | 李而宏 | Method for producing feed from waste vegetable leaf juice |
| CN205167127U (en) * | 2015-11-27 | 2016-04-20 | 淳安县绿之源苗木专业合作社 | Rattan cutting reducing mechanism |
-
2016
- 2016-12-11 CN CN201611134922.7A patent/CN106397064A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102172260A (en) * | 2011-03-11 | 2011-09-07 | 通海县福慧科技有限公司 | Recycling production process of discarded vegetable leaves |
| CN104266474A (en) * | 2014-09-03 | 2015-01-07 | 嘉善圣莱斯绒业有限公司 | Vibratory drying and processing device |
| CN104291886A (en) * | 2014-10-21 | 2015-01-21 | 陕西省微生物研究所 | Composite organic fertilizer prepared from vegetable wastes and preparation method of composite organic fertilizer |
| CN104839437A (en) * | 2015-04-30 | 2015-08-19 | 李而宏 | Method for producing feed from waste vegetable leaf juice |
| CN205167127U (en) * | 2015-11-27 | 2016-04-20 | 淳安县绿之源苗木专业合作社 | Rattan cutting reducing mechanism |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108821816A (en) * | 2018-07-04 | 2018-11-16 | 合肥欧语自动化有限公司 | A kind of automated production equipment of liquid state organic fertilizer |
| CN112552084A (en) * | 2020-11-27 | 2021-03-26 | 岳阳佰胜智慧环保科技有限公司 | Organic matter garbage treatment system |
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Application publication date: 20170215 |
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