CN102658053B - A kind of High-tower compound fertilizer slurry emulsifier - Google Patents
A kind of High-tower compound fertilizer slurry emulsifier Download PDFInfo
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- CN102658053B CN102658053B CN201210128750.8A CN201210128750A CN102658053B CN 102658053 B CN102658053 B CN 102658053B CN 201210128750 A CN201210128750 A CN 201210128750A CN 102658053 B CN102658053 B CN 102658053B
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Abstract
A kind of High-tower compound fertilizer slurry emulsifier, comprise blender, blender top is provided with charging aperture, bottom is provided with the first discharging opening and the second discharging opening, inside is provided with the first batch mixing chamber and the second batch mixing chamber, and described first batch mixing chamber is connected with the second batch mixing chamber, and the first batch mixing chamber is placed in above the second batch mixing chamber, be provided with agitator in first batch mixing chamber, in the second batch mixing chamber, be provided with emulsifier; Described charging aperture is connected with the first batch mixing chamber, and described first discharging opening is connected with the top in the second batch mixing chamber, and the second discharging opening is connected with the bottom in the second batch mixing chamber; The object of the invention is to provide a kind of High-tower compound fertilizer slurry emulsifier, and incomplete to solve prior art emulsification, large granular materials is deposited in device bottom, also wants the problem of regular deslagging after stopping production, and the thickness achieving slip is separated.
Description
Technical field
The present invention relates to a kind of emulsifier unit, particularly a kind of High-tower compound fertilizer slurry emulsifier.
Background technology
In high tower compound fertilizer granulation process, whether slip mixes is the key factor affecting product appearance and finished product grain.Increasing slip mixing arrangement in original high tower technological process is the general solution of one that current domestic high tower compound fertilizer granulation solves slip mixture homogeneity.But, high-tower granulation slip mixing arrangement domestic at present adopts the mode of low in and high out mostly, and volume is larger, a kind of emulsion mixing device of inner employing, adopt flow-stopping plate to be blocked by slip in groove tank middle and lower part, material will be concentrated by emulsifier, through emulsifier emulsification, then by high-position discharge mouth discharge.
Thus existing exist following shortcoming:
1, structural volume is large, takes up room more.
2, emulsification is incomplete, and large granular materials precipitation bottom, not through Over emulsfication, also wants regular deslagging after stopping production, thus operating efficiency and of low quality.
3, because the discharging opening of equipment is located at top, so material will be deposited on equipment bottom, thus when producing into the composite fertilizer of different cultivars, also to put clean cleaning equipment, its complicated operation, increasing labour intensity, easily causing waste.
4, the fineness of slip differs, and can not reach the effect that thickness is separated.
Summary of the invention
The object of the invention is to provide a kind of High-tower compound fertilizer slurry emulsifier, and incomplete to solve prior art emulsification, large granular materials is deposited in device bottom, also wants the problem of regular deslagging after stopping production, and the thickness achieving slip is separated.
Above-mentioned High-tower compound fertilizer slurry emulsifier comprises blender, and blender top is provided with charging aperture, and bottom is provided with the first discharging opening and the second discharging opening, and inside is provided with the first batch mixing chamber and the second batch mixing chamber,
Described first batch mixing chamber is connected with the second batch mixing chamber, and the first batch mixing chamber is placed in above the second batch mixing chamber, is provided with agitator in the first batch mixing chamber, is provided with emulsifier in the second batch mixing chamber;
Described charging aperture is connected with the first batch mixing chamber;
Described first discharging opening is connected with the top in the second batch mixing chamber, and the second discharging opening is connected with the bottom in the second batch mixing chamber.
Adopt technical scheme of the present invention, because fertilizer enters in blender from the charging aperture of top, discharging opening is from below sent, so solve the technical problem that granule materials is deposited in device bottom, and fertilizer first stirs through agitator, and then carry out emulsification through emulsifier, make the mixing and emulsifying degree of fertilizer higher, to solve the incomplete technical problem of prior art emulsification, all the time there is thickness difference in the slip due to emulsification, so the higher slip of emulsification degree will float on the surface of slip, thus can discharge through the first discharging opening, comparatively the slip of alligatoring is then discharged by the second discharging opening, be separated with the thickness reaching slip.
Preferably, described blender comprises the first cylindrical shell and the second cylindrical shell, and the first cylindrical shell connects up and down with the second cylindrical shell, and described first batch mixing chamber is located in the first cylindrical shell, and the second batch mixing chamber is located in the second cylindrical shell.
Owing to blender to be divided into the first cylindrical shell and the second cylindrical shell, so this equipment can be dismantled as less parts, thus to decrease difficulty during equipment delivery, and blender is split as two parts, also make the maintenance of equipment become easier.
Preferably, comprise rotating shaft, rotating shaft is located in the first cylindrical shell and the second cylindrical shell, and described agitator is mixing cutter, and described emulsifier is emulsification cutter, and mixing cutter and emulsification cutter are all located in rotating shaft.
Preferably, in described rotating shaft, cover has bearing block, and bearing block is located at above the first cylindrical shell.
Preferably, the bottom of described second cylindrical shell is provided with conically shaped, and cone tank is connected with the second cylindrical shell.
Preferably, agitator is provided with in described conically shaped.
Preferably, described rotating shaft extends in conically shaped through the second batch mixing chamber, and described agitator is spiral crushing cutter, and spiral crushing cutter is located in rotating shaft.
By spiral crushing cutter, micronization processes is carried out to fertilizer slurry, ensure that the degree of refinement of fertilizer slurry.
Preferably, be provided with dead knife in described second cylindrical shell, dead knife is around outside emulsification cutter.
Preferably, described dead knife is cartridge type dead knife, and the barrel of cartridge type dead knife is provided with multiple cinclides, and the side of cinclides is blade.
Cartridge type dead knife and emulsification cutter interact, and carry out refinement, emulsification treatment with this to fertilizer slurry, make its emulsion quality better.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 is the structural representation of cartridge type dead knife of the present invention;
Fig. 3 is the top view of cartridge type dead knife of the present invention;
Fig. 4 is the structural representation of cartridge type dead knife cinclides of the present invention.
Detailed description of the invention
Embodiments of the invention as shown in Figure 1, comprise blender, and blender comprises the first cylindrical shell 3 and the second cylindrical shell 4, first cylindrical shell 3 connects with the second cylindrical shell about 4.
The barrel of described first cylindrical shell 3 is provided with charging aperture, inside is provided with the first batch mixing chamber 31, charging aperture is connected with the first batch mixing chamber 31, the barrel of the second cylindrical shell 4 is provided with the first discharging opening, bottom is provided with the second discharging opening, inside is provided with the second batch mixing chamber 41, first discharging opening and is all connected with the second batch mixing chamber 41 with the second discharging opening, and the first batch mixing chamber 31 is connected with the second batch mixing chamber 41.
In described first cylindrical shell 3 and the second cylindrical shell 4, cross-under has rotating shaft 10, rotating shaft 10 is by motor 1 driven rotary, in rotating shaft 10, also cover has bearing block 2, bearing block 2 connects with the top of the first cylindrical shell 3, the top of the first cylindrical shell 3 is located at by motor 1, rotating shaft 10 is provided with mixing cutter 9 and emulsification cutter 7, the top of rotating shaft 10 is located at by mixing cutter 9, it is made to be located in the first batch mixing chamber 31, the bottom of rotating shaft 10 is located at by emulsification cutter 7, it is made to be located at the inside in the second batch mixing chamber 41, owing to blender to be divided into the first cylindrical shell 3 and the second cylindrical shell 4, so this equipment can be dismantled as less parts, thus difficulty during equipment delivery is decreased, and blender is split as two parts, also the maintenance of equipment is made to become easier.
Described second cylindrical shell 4 inside is also provided with cartridge type dead knife 8, and emulsification cutter 7 wraps in the inner by cartridge type dead knife 8, and the barrel of cartridge type dead knife 8 is provided with multiple cinclides 81, and the side of cinclides 81 is blade.
The bottom of described second cylindrical shell 4 is provided with conically shaped 5, and cone tank 5 is connected with the second cylindrical shell 4, and described rotating shaft 10 extends in conically shaped 5 through the second batch mixing chamber 41, and the rotating shaft 10 in conically shaped 5 is provided with spiral crushing cutter 6.
During use, first fertilizer is knocked down in the first batch mixing chamber 31 through charging aperture, then rotating shaft 10 starts to rotate, thus mix cutter 9 to stir to the fertilizer in the first batch mixing chamber 31, make it mix, after fertilizer mixes, fertilizer will enter the second batch mixing chamber 41, now emulsification cutter 7 is followed rotating shaft 10 and is rotated, and with cartridge type dead knife 8 acting in conjunction, make fertilizer emulsification complete.
Because the thin matter of the fertilizer slurry after emulsification will float on the surface of slip, then flowed out by the first discharging opening on the second cylindrical shell 4, there is no completely broken contamination precipitation in lower taper cylinder 5, after spiral crushing cutter 6 further fragmentation, flow out from the bottom of conically shaped 5, to complete whole emulsion process.
Adopt technical scheme of the present invention, because fertilizer enters in blender from the charging aperture of top, discharging opening is from below sent, so solve the technical problem that granule materials is deposited in device bottom, and fertilizer first stirs through mixing cutter 9, and then active force is applied to fertilizer through emulsification cutter 7 and cartridge type dead knife 8 simultaneously, make the mixing and emulsifying degree of fertilizer higher, to solve the incomplete technical problem of prior art emulsification, again because the present invention carries out discharge at twice, first time discharges the thin matter of fertilizer slurry, second time discharge also first carries out micronization processes to fertilizer slurry, not only enable fertilizer slurry reach thickness to be separated, and ensure that the refinement of fertilizer slurry is abundant.
The protection domain being also considered as patent that the basis of above embodiment is improved.
Claims (1)
1. a High-tower compound fertilizer slurry emulsifier, is characterized in that: comprise blender, and blender top is provided with charging aperture, and bottom is provided with the first discharging opening and the second discharging opening, and inside is provided with the first batch mixing chamber and the second batch mixing chamber,
Described first batch mixing chamber is connected with the second batch mixing chamber, and the first batch mixing chamber is placed in above the second batch mixing chamber, is provided with agitator in the first batch mixing chamber, is provided with emulsifier in the second batch mixing chamber, and described emulsifier is emulsification cutter;
Described charging aperture is connected with the first batch mixing chamber;
Described first discharging opening is connected with the top in the second batch mixing chamber, and the second discharging opening is connected with the bottom in the second batch mixing chamber;
Described blender comprises the first cylindrical shell and the second cylindrical shell, and the first cylindrical shell connects up and down with the second cylindrical shell, and described first batch mixing chamber is located in the first cylindrical shell, and the second batch mixing chamber is located in the second cylindrical shell;
Be provided with dead knife in described second cylindrical shell, described dead knife is cartridge type dead knife, and cartridge type dead knife is around outside emulsification cutter;
The upper port of described cartridge type dead knife aims at the lower port of the first cylindrical shell, and the lower port of cartridge type dead knife is lower than the first discharging opening;
Rotating shaft is located in the first cylindrical shell and the second cylindrical shell, and described agitator is mixing cutter, and mixing cutter and emulsification cutter are all located in rotating shaft;
In described rotating shaft, cover has bearing block, and bearing block is located at above the first cylindrical shell;
The bottom of described second cylindrical shell is provided with conically shaped, and cone tank is connected with the second cylindrical shell;
Agitator is provided with in described conically shaped;
Described rotating shaft extends in conically shaped through the second batch mixing chamber, and described agitator is spiral crushing cutter, and spiral crushing cutter is located in rotating shaft;
The barrel of cartridge type dead knife is provided with multiple cinclides, and the side of cinclides is blade.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210128750.8A CN102658053B (en) | 2012-04-27 | 2012-04-27 | A kind of High-tower compound fertilizer slurry emulsifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210128750.8A CN102658053B (en) | 2012-04-27 | 2012-04-27 | A kind of High-tower compound fertilizer slurry emulsifier |
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| Publication Number | Publication Date |
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| CN102658053A CN102658053A (en) | 2012-09-12 |
| CN102658053B true CN102658053B (en) | 2015-10-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201210128750.8A Active CN102658053B (en) | 2012-04-27 | 2012-04-27 | A kind of High-tower compound fertilizer slurry emulsifier |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110523307A (en) * | 2019-10-08 | 2019-12-03 | 江西科伦药业有限公司 | A kind of low-temperature nano grade high-shear emulsifying device |
| CN113546536B (en) * | 2021-07-28 | 2022-09-06 | 吉林隆源农业服务有限公司 | Prevent high tower compound fertilizer production of sediment with thick liquids circulation formula emulsification device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2210713Y (en) * | 1994-10-07 | 1995-10-25 | 蒋继伟 | Sedimentation and rotay-flow sizing machine |
| CN1400039A (en) * | 2001-07-26 | 2003-03-05 | 上海威宇机电制造有限公司 | Composite stirring equipment |
| CN201045136Y (en) * | 2007-06-01 | 2008-04-09 | 张立省 | Novel highly effective mixing device for tower flux granulating composite fertilizer |
| CN201088907Y (en) * | 2007-09-17 | 2008-07-23 | 陶裕兴 | High-shear vertical emulsifying machine |
| CN201618539U (en) * | 2009-09-04 | 2010-11-03 | 罗星健 | High-efficient non-sealing vertical mixer |
| CN102423651A (en) * | 2011-08-22 | 2012-04-25 | 浙江恒丰泰减速机制造有限公司 | Overflow pipeline type high-speed dispersion machine |
-
2012
- 2012-04-27 CN CN201210128750.8A patent/CN102658053B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2210713Y (en) * | 1994-10-07 | 1995-10-25 | 蒋继伟 | Sedimentation and rotay-flow sizing machine |
| CN1400039A (en) * | 2001-07-26 | 2003-03-05 | 上海威宇机电制造有限公司 | Composite stirring equipment |
| CN201045136Y (en) * | 2007-06-01 | 2008-04-09 | 张立省 | Novel highly effective mixing device for tower flux granulating composite fertilizer |
| CN201088907Y (en) * | 2007-09-17 | 2008-07-23 | 陶裕兴 | High-shear vertical emulsifying machine |
| CN201618539U (en) * | 2009-09-04 | 2010-11-03 | 罗星健 | High-efficient non-sealing vertical mixer |
| CN102423651A (en) * | 2011-08-22 | 2012-04-25 | 浙江恒丰泰减速机制造有限公司 | Overflow pipeline type high-speed dispersion machine |
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| CN102658053A (en) | 2012-09-12 |
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Effective date of registration: 20161008 Address after: 518105 third industrial zone, riverside, Songgang street, Shenzhen, Guangdong, Baoan District Patentee after: Batian Ecological Engineering Co., Ltd., Shenzhen Patentee after: GUIZHOU BATIAN ECOLOGICAL ENGINEERING CO., LTD. Address before: 518105 third industrial zone, riverside, Songgang street, Shenzhen, Guangdong, Baoan District Patentee before: Batian Ecological Engineering Co., Ltd., Shenzhen |