CN205528503U - Device of fertilizer is jointly prepared to thermal acid generator and thermokalite - Google Patents
Device of fertilizer is jointly prepared to thermal acid generator and thermokalite Download PDFInfo
- Publication number
- CN205528503U CN205528503U CN201620249395.3U CN201620249395U CN205528503U CN 205528503 U CN205528503 U CN 205528503U CN 201620249395 U CN201620249395 U CN 201620249395U CN 205528503 U CN205528503 U CN 205528503U
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- Prior art keywords
- cylinder
- rotor
- acid
- kettle body
- pulverizing
- 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.)
- Expired - Fee Related
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- 239000002253 acid Substances 0.000 title claims abstract description 30
- 239000003337 fertilizer Substances 0.000 title claims abstract description 23
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 title claims abstract description 14
- 239000003513 alkali Substances 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims description 56
- 238000010298 pulverizing process Methods 0.000 claims description 28
- 238000007599 discharging Methods 0.000 claims description 10
- 239000002562 thickening agent Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 7
- 238000010008 shearing Methods 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims description 6
- 230000004308 accommodation Effects 0.000 claims description 5
- 239000002361 compost Substances 0.000 claims description 5
- 239000000654 additive Substances 0.000 claims description 4
- 230000000996 additive effect Effects 0.000 claims description 4
- 239000002154 agricultural waste Substances 0.000 abstract description 16
- 238000000034 method Methods 0.000 abstract description 14
- 239000000463 material Substances 0.000 abstract description 13
- 239000003895 organic fertilizer Substances 0.000 abstract description 7
- 239000007787 solid Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 230000004720 fertilization Effects 0.000 abstract description 3
- 230000002262 irrigation Effects 0.000 abstract description 3
- 238000003973 irrigation Methods 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 229930013930 alkaloid Natural products 0.000 abstract description 2
- 150000003797 alkaloid derivatives Chemical class 0.000 abstract description 2
- 150000004676 glycans Chemical class 0.000 abstract description 2
- 229930182470 glycoside Natural products 0.000 abstract description 2
- 150000002338 glycosides Chemical class 0.000 abstract description 2
- 235000021049 nutrient content Nutrition 0.000 abstract description 2
- 150000007524 organic acids Chemical class 0.000 abstract description 2
- 229920001282 polysaccharide Polymers 0.000 abstract description 2
- 239000005017 polysaccharide Substances 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract 2
- 239000002585 base Substances 0.000 abstract 1
- 238000009264 composting Methods 0.000 abstract 1
- 238000000605 extraction Methods 0.000 abstract 1
- 235000014666 liquid concentrate Nutrition 0.000 abstract 1
- 102000004169 proteins and genes Human genes 0.000 abstract 1
- 108090000623 proteins and genes Proteins 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- 238000000855 fermentation Methods 0.000 description 4
- 230000004151 fermentation Effects 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 150000003112 potassium compounds Chemical class 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000002671 adjuvant Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- -1 white matter Substances 0.000 description 2
- 241000239290 Araneae Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 210000004885 white matter Anatomy 0.000 description 1
Classifications
-
- 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
Landscapes
- Fertilizers (AREA)
Abstract
The utility model discloses a device of fertilizer is jointly prepared to thermal acid generator and thermokalite, the device mixes the machine including rubbing, rub the sour reation kettle and the alkali reation kettle that mix the machine and connect the parallelly connected setting in low reaches, sour reation kettle and alkali reation kettle's low reaches are equipped with sour acid -base regulating reservoir and solid -liquid separation machine, the concentrated machine and the aerobic composting workshop in low reaches are connected respectively to the solid -liquid separation machine. The utility model discloses can be used to handle the agricultural wastes of all types, be particularly useful for agricultural wastes's such as fresh spoil, the incomplete body of fresh plant utilization, system's and method for, but materials such as the organic acid in the efficient extraction discarded object, alkaloid, protein, polysaccharide, glycoside, the liquid concentrate fertilizer that makes can adapt to fertilization method such as burette, sprinkling irrigation, spraying, use simple, take effect fast, organic fertilizer becomes thoroughly decomposed completely, and nutrient content is high, uses safe effectively.
Description
Technical field
This utility model belongs to agricultural wastes resource reutilization technology field, relates more specifically to a kind of heat
The device preparing fertilizer such as Liquid Fertilizer and fertilizer is combined in acid with thermokalite.
Background technology
At present, in the vast rural area of China, there are problems in the agricultural wastes utilization of resources: lacks corresponding
Technology and equipment, simple, backward in technique to the process technique of agricultural wastes, disposal ability and utilize rule
Mould is very limited, and the most primary problem is exactly that existing agricultural waste utilization mode can cause environment
Pollute.Major part resource can only be discarded or burn, and utilization rate is the lowest, and such as agricultural crop straw is many as fuel
Carrying out such disposable Land use systems that burns, not only capacity usage ratio only has 10%, and in combustion process
The a large amount of nitrogen oxides, sulfur dioxide, Hydrocarbon and the flue dust that produce can direct atmosphere pollutions.And for example raise
Poultry manure the most unprocessed a lot of direct returning to farmland, calcium that such Land use systems not only makes wherein to contain,
The nutrient substance such as phosphorus are not used, and the environment such as the waters of severe contamination periphery, soil, affect human body
Healthy.
Many studies have shown that both at home and abroad, agricultural wastes are used as fertilizer both can solve the problem of outlet of garbage,
Can improve again and fertilizing soil simultaneously.But, it is the most single that prior art processes agricultural wastes method, many
For agricultural wastes are directly fermented, the solid organic fertilizer made often because nutrition content low,
The reasons such as production technology is simple, dog-eat-dog of the same trade, economic benefit is very limited.
Additionally, many can only the process in one or a few garbage, and processing procedure of this method has pollution
The problem of thing secondary emission.In addition, along with technology such as the development of agriculture cultivation technology, drip irrigation and spray irrigation
Application more extensive, solid organic fertilizer has been difficult to the such fertilization mode of adaptation.
It addition, additionally, fresh animal corpse high for water content, perishable, intractable, fresh plant
The agricultural wastes that residuum etc. are fresh, owing to its competent cell content is high, traditional fermentation process is difficult to control to
The condition of fermentation and direction, the fertilizer quality that fermentation obtains is unstable.
Further, traditional fermentation process does not has selectivity to the product of gained, it is impossible to give up for difference
Composition and the feature of gurry utilize to greatest extent, recycle poor effect.
Therefore, for current technology present situation, need the technology with preferable conformability and promotional value badly,
Break through current a kind of mode only with a kind of or obstacle of a few garbage, improve agricultural wastes profit
By present situation backward in technique, that utilization rate is low.
Utility model content
The problem existed for above-mentioned prior art, the purpose of this utility model is to provide a kind of hot acid and heat
Alkali Combined Treatment various agricultural garbage also recycles the device preparing concentrated liquid fertilizer with organic fertilizer, this dress
Put and can be used for processing all types of agricultural wastes, be particularly suited for fresh animal corpse, fresh plant residual
The utilization of the agricultural wastes such as body, described device can effectively extract the organic acid in garbage, alkaloid, egg
The materials such as white matter, polysaccharide, glycoside, obtained concentrated liquid fertilizer is adapted to dropper, sprays, sprays
Fertilization mode, uses simple, instant effect；Organic fertilizer becomes thoroughly decomposed completely, and nutrient content is high, and using safety has
Effect.
For reaching above-mentioned purpose, the technical scheme that this utility model is taked is as follows: provide a kind of hot acid and thermokalite
Combining the device preparing fertilizer, described device includes rubbing mixer, and described rubbing mixer connects downstream also
The acid reaction still of connection setting and alkali reaction still, the downstream of described acid reaction still and alkali reaction still is provided with acid-alkali accommodation
Pond and solid-liquid separating machine, described solid-liquid separating machine connects thickener and the aerobic compost workshop in downstream respectively；Institute
State rubbing mixer to include rubbing frame, described rubbing frame is installed with pulverizing cylinder, described pulverizing
The axis horizontal of cylinder is arranged, and described rubbing frame is rotatablely equipped with the rotor driven by the first power set,
Described rotor runs through described pulverizing cylinder, is sequentially provided with feed zone, tear section in described pulverization cylinder body vertically
With shearing section, it is positioned on the described pulverizing cylinder of described feed zone and offers charging aperture, described pulverizing cylinder
Tail end offers discharging opening, and the described rotor being positioned at described feed zone is provided with feeding screw；Tear described in being positioned at
The described rotor of the section of splitting is provided with some moving knife, and some described moving knife are along the axial of described rotor and at described turn
The surface of son is arranged in the shape of a spiral, and the described pulverizing cylinder being positioned at described tear section is provided with and described moving knife pair
The some stationary knifes answered；The described rotor being positioned at described shearing section is provided with some dynamic shears, described dynamic shears edge
Axially extending and with described rotor the axis of described rotor has angle, and is positioned at the described powder of described shearing section
Broken cylinder is provided with some quiet shears.
Combine in the device preparing fertilizer at described hot acid of the present utility model with thermokalite, preferred as one
Technical scheme, described pulverizing cylinder is upper is provided with screen cloth in described discharging opening position.
Combine in the device preparing fertilizer at described hot acid of the present utility model with thermokalite, preferred as one
Technical scheme, described acid reaction still includes vertically arranged reaction kettle body, is positioned at described in described reaction kettle body
The bottom of reaction kettle body is provided with escape pipe, is provided with agitating auger, described reaction kettle body in described reaction kettle body
Outer wall be provided with heating coil, the periphery of described reaction kettle body is enclosed with heat-insulation layer, and described heating coil is positioned at
Between described heat-insulation layer and reaction kettle body.
Combine in the device preparing fertilizer at described hot acid of the present utility model with thermokalite, preferred as one
Technical scheme, described thickener includes being driven and the concentration cylinder of horizontally set by the second power set, described
Concentrating in cylinder and have reaction chamber, described reaction chamber one end is feed end, and the other end is discharge end, described in enter
Material end is provided with feeding cylinder, is rotatablely equipped with the feed auger driven by the 3rd power set in described feeding cylinder,
Described feeding cylinder is provided with additive inlet port, and described discharge end is provided with the squeezing driven by the 4th power set and takes off
Chiragra Spider Conch revolves.
After have employed technique scheme, described device of the present utility model achieves many beneficial effects, example
As:
(1) owing to having set gradually feed zone, tear section in pulverization cylinder body and having sheared section, feed zone can meet
Agricultural wastes enter to be pulverized cylinder and carries the most continuously, and tear section is possible not only to meet the freshest moving
Thing corpse, the tear of fresh plant residuum, it is also possible to tentatively crushed by some hard garbages, shear
The bulk materials that tear section carries can be shredded by section further, and especially plant residue material, at this
Region more can fully be pulverized, and improves the combination property of this pulverizer, and this utility model seriality is strong,
Production efficiency is high.
(2) it is provided with heating coil due to alkali reaction still, is provided with agitating auger in reaction kettle body, in course of reaction
In so that material is easier to mix homogeneously, further increases production efficiency.
As it has been described above, this utility model provides a kind of hot acid combines the device preparing fertilizer with thermokalite, described
Device is designed by unique structure, such that it is able to obtain many beneficial effects, in the agriculture waste utilization of resources
Field has a good application prospect and potentiality.
Accompanying drawing explanation
Fig. 1 is the process frame chart of this utility model embodiment；
Fig. 2 is the structural representation rubbing mixer in this utility model embodiment；
Fig. 3 is the structural representation of acid reaction still in this utility model embodiment；
Fig. 4 is the structural representation of thickener in this utility model embodiment；
Wherein, in Fig. 1 to Fig. 4, each number designation refer to respectively following concrete meaning, element and/
Or parts.
In figure: 1, agricultural wastes, 2, rub mixer, 201, rub frame, 202, pulverize cylinder,
203, feed zone, 204, tear section, 205, shear section, 206, charging aperture, 207, discharging opening, 208,
Stationary knife, 209, quiet shears, 210, rotor, 211, feeding screw, 212, moving knife, 213, dynamic shears,
214, screen cloth, 3, acid reaction still, 301, reaction kettle body, 302, escape pipe, 303, agitating auger, 304,
Heating coil, 305, heat-insulation layer, 306, outlet nozzle, 4, alkali reaction still, 5, acid-alkali accommodation pond, 6, solid
Liquid separator, 7, thickener, 701, concentrate cylinder, 702, feed end, 703, discharge end, 704, anti-
Answer chamber, 705, feeding cylinder, 706, feed auger, 707, material inlet, 708, additive inlet port, 709,
Discharge barrel, 710, press dewatering spiral, 711, material outlet, 8, aerobic compost workshop, 9, nitrogenous,
Phosphorus, potassium compound and chelated microelement complex, 10, organic-inorganic concentrated liquid fertile, 11, adjuvant,
12, organic fertilizer, 13, sour or sour solution, the solution of 14, alkali or alkali.
Detailed description of the invention
With embodiment, this utility model is further illustrated below in conjunction with the accompanying drawings.But these exemplary embodiments
Purposes and purpose are only used for enumerating this utility model, not constitute real protection scope of the present utility model and appoint
Any restriction of what form, more non-is confined to this by protection domain of the present utility model.
Shown in as common in Fig. 1-4, this utility model provides a kind of hot acid and combines the dress preparing fertilizer with thermokalite
Putting, described device includes rubbing mixer 2, rubs mixer 2 and connects the acid reaction still 3 that downstream is arranged in parallel
With alkali reaction still 4, the downstream of acid reaction still 3 and alkali reaction still 4 is provided with acid-alkali accommodation pond 5 and solid-liquid separating machine
6, agricultural wastes 1 are entered by rubbing mixer 2, respectively enter acid reaction still 3 and alkali is anti-after being pulverized and mixed
Answer still 4, acid reaction still 3 adds sour or sour solution 13, alkali reaction still 4 adds alkali or alkali
Solution 14, is neutralized regulation in the acid-alkali accommodation pond 5 in downstream, and solid-liquid separating machine 6 connects downstream respectively
Thickener 7 and aerobic compost workshop 8, thickener 7 adds nitrogenous, phosphorus, potassium compound and chelating is micro-
Secondary element complex 9, reacted prepared organic-inorganic concentrated liquid fertilizer 10, make in aerobic compost workshop 8
Organic fertilizer 12 is prepared with adjuvant 11；Rub mixer 2 to include rubbing frame 201, rub in frame 201
Being installed with pulverizing cylinder 202, the axis horizontal pulverizing cylinder 202 is arranged, and rubs and rotates in frame 201
Being provided with the rotor 210 driven by the first power set, rotor 210 runs through pulverizing cylinder 202, rotor 210
It is coaxially disposed with pulverizing cylinder 202, in pulverizing cylinder 202, is sequentially provided with feed zone 203, tear section vertically
204 and shear section 205, be positioned on the pulverizing cylinder 202 of feed zone 203 and offer charging aperture 206, pulverize
The tail end of cylinder 202 offers discharging opening 207, the position being located away from charging aperture 206 of discharging opening 207,
The rotor 210 being positioned at feed zone 203 is provided with feeding screw 211, and feeding screw 211 is the most frequent
Using, depending on the parameter such as its rotation direction, diameter, pitch is according to conveying capacity, those skilled in the art can join
Examine prior art to use, do not repeat them here；The rotor 210 being positioned at tear section 204 is provided with some moving knife
212, the cylinder 202 of pulverizing being positioned at tear section 204 is provided with the some stationary knifes 208 corresponding with moving knife 212,
Some moving knife 212 axially and arranging in the shape of a spiral on the surface of rotor 210 along rotor 210, corresponding,
Pulverize the stationary knife 208 on cylinder 202 the most vertically and to arrange in the shape of a spiral at the inner surface pulverizing cylinder 202；
The rotor 210 being positioned at shearing section 205 is provided with some dynamic shears 213, is positioned at the pulverizing cylinder shearing section 205
202 are provided with some quiet shears 209.Dynamic shears 213 along the axially extending of rotor 210 and with rotor 210
Axis has angle, and the angle of quiet shears 209 is corresponding with the angle of dynamic shears 213.
It is positioned at discharging opening 207 position on described pulverizing cylinder 202 and is provided with screen cloth 214, in shattering process, full
The fragment of foot screen cloth 214 mesh number falls from discharging opening 207, and continues quilt more than the fragment of screen cloth 214 mesh number
Broken, further increase use function of the present utility model.
Described acid reaction still 3 includes vertically arranged reaction kettle body 301, is positioned at reactor in reaction kettle body 301
The bottom of body 301 is provided with escape pipe 302, and escape pipe 302 is provided with some outlet nozzles 306, escape pipe 302
Connecting source of the gas, be provided with agitating auger 303 in reaction kettle body 301, the outer wall of reaction kettle body 301 is provided with and adds hot plate
Pipe 304, the periphery of reaction kettle body 301 is enclosed with heat-insulation layer 305, and heating coil 304 is positioned at heat-insulation layer 305
And between reaction kettle body 301, add sour or sour solution 13 in reaction kettle body 301, use stirring spiral shell simultaneously
Rotation 303 is stirred, outlet nozzle 306 produces bubble so that material is easier to mix homogeneously, it is to avoid stir
Mix the stirring dead angle produced when spiral 303 stirs, improve production efficiency.
Structural reference acid reaction still 3 structure of described alkali reaction still 4, its difference is, at alkali reaction still 4
The solution 14 of interior interpolation alkali or alkali is stirred.
Described thickener 7 includes being driven and the concentration cylinder 701 of horizontally set by the second power set, concentrates cylinder
Having reaction chamber 704 in body 701, reaction chamber 704 one end is feed end 702, and the other end is discharge end 703,
Feed end 702 is provided with feeding cylinder 705, is rotatablely equipped with by the 3rd power set driving in feeding cylinder 705
Feed auger 706, feeding cylinder 705 is provided with material inlet 707 and additive inlet port 708, contains for interpolation
Nitrogen, phosphorus, potassium compound and chelated microelement complex 9, discharge end 703 is provided with and is driven by the 4th power set
Dynamic press dewatering spiral 710, equally, discharge end 703 is provided with discharge barrel 709, press dewatering spiral 710
Rotation is installed in discharge barrel 709, and discharge barrel 709 is provided with press-area and material outlet 711, charging
Using feed auger 706, discharging uses press dewatering spiral 710, and organic-inorganic concentrated liquid fertilizer 10 is by pressing
Squeezing dewatering spiral 710 to discharge from drying zone, the dregs that squeezing obtains are discharged by material outlet 711 so that thing
Material reaction forms a continuous process, further increases production efficiency.
Should be appreciated that the purposes of these embodiments is merely to illustrate this utility model and is not intended to limit this practicality
Novel protection domain.Additionally, it will also be appreciated that after having read technology contents of the present utility model, this
This utility model can be made various change, amendment and/or modification by skilled person, and all these is of equal value
Within form falls within the protection domain that the application appended claims is limited equally.
Claims (4)
1. the device preparing fertilizer combined by hot acid with thermokalite, and described device includes rubbing mixer, described
Rub mixer and connect acid reaction still and alkali reaction still, described acid reaction still and the alkali reaction that downstream is arranged in parallel
The downstream of still is provided with acid-alkali accommodation pond and solid-liquid separating machine, and described solid-liquid separating machine connects the concentration in downstream respectively
Machine and aerobic compost workshop；Described rubbing mixer includes rubbing frame, and described rubbing frame fixedly mounts
Having pulverizing cylinder, the axis horizontal of described pulverizing cylinder is arranged, and described rubbing frame is rotatablely equipped with by the
The rotor that one power set drive, described rotor runs through described pulverizing cylinder, in described pulverization cylinder body vertically
It is sequentially provided with feed zone, tear section and shears section, being positioned on the described pulverizing cylinder of described feed zone and offer
Charging aperture, the tail end of described pulverizing cylinder offers discharging opening, is positioned on the described rotor of described feed zone and sets
There is feeding screw；The described rotor being positioned at described tear section is provided with some moving knife, and some described moving knife are along institute
State axially and arranging in the shape of a spiral on the surface of described rotor of rotor, be positioned at the described pulverizing of described tear section
Cylinder is provided with the some stationary knifes corresponding with described moving knife；If the described rotor being positioned at described shearing section is provided with
Dry dynamic shears, the described dynamic shears axis along the axially extending of described rotor and with described rotor has angle,
The described pulverizing cylinder being positioned at described shearing section is provided with some quiet shears.
2. the device preparing fertilizer combined by hot acid as claimed in claim 1 with thermokalite, it is characterised in that: institute
Stating pulverizing, cylinder is upper is provided with screen cloth in described discharging opening position.
3. the device preparing fertilizer combined by hot acid as claimed in claim 1 with thermokalite, it is characterised in that: institute
State acid reaction still and include vertically arranged reaction kettle body, be positioned at bottom described reaction kettle body in described reaction kettle body
Being provided with escape pipe, described escape pipe is provided with some outlet nozzles, is provided with agitating auger in described reaction kettle body,
The outer wall of described reaction kettle body is provided with heating coil, and the periphery of described reaction kettle body is enclosed with heat-insulation layer, described
Heating coil is between described heat-insulation layer and reaction kettle body.
4. the hot acid as described in any one of claim 1-3 combines the device preparing fertilizer, its feature with thermokalite
It is: described thickener includes being driven and the concentration cylinder of horizontally set, described concentration by the second power set
Having reaction chamber in cylinder, described reaction chamber one end is feed end, and the other end is discharge end, described feed end
Feeding cylinder is installed, in described feeding cylinder, is rotatablely equipped with the feed auger driven by the 3rd power set, institute
Stating feeding cylinder and be provided with additive inlet port, described discharge end is provided with the press dewatering driven by the 4th power set
Spiral.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620249395.3U CN205528503U (en) | 2016-03-20 | 2016-03-20 | Device of fertilizer is jointly prepared to thermal acid generator and thermokalite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620249395.3U CN205528503U (en) | 2016-03-20 | 2016-03-20 | Device of fertilizer is jointly prepared to thermal acid generator and thermokalite |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205528503U true CN205528503U (en) | 2016-08-31 |
Family
ID=56786581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620249395.3U Expired - Fee Related CN205528503U (en) | 2016-03-20 | 2016-03-20 | Device of fertilizer is jointly prepared to thermal acid generator and thermokalite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205528503U (en) |
-
2016
- 2016-03-20 CN CN201620249395.3U patent/CN205528503U/en not_active Expired - Fee Related
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 |