CN200945423Y - High tower granulation fused slurry mixing tank - Google Patents
High tower granulation fused slurry mixing tank Download PDFInfo
- Publication number
- CN200945423Y CN200945423Y CN200620077474.7U CN200620077474U CN200945423Y CN 200945423 Y CN200945423 Y CN 200945423Y CN 200620077474 U CN200620077474 U CN 200620077474U CN 200945423 Y CN200945423 Y CN 200945423Y
- Authority
- CN
- China
- Prior art keywords
- mixing tank
- cylinder
- cylindrical shell
- mixing channel
- slurry mixing
- 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 - Lifetime
Links
- 238000002156 mixing Methods 0.000 title claims abstract description 25
- 239000002002 slurry Substances 0.000 title claims abstract description 18
- 238000005469 granulation Methods 0.000 title claims abstract description 12
- 230000003179 granulation Effects 0.000 title claims abstract description 12
- 238000002844 melting Methods 0.000 claims abstract description 16
- 230000008018 melting Effects 0.000 claims abstract description 16
- 238000003756 stirring Methods 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 230000008878 coupling Effects 0.000 claims description 4
- 238000010168 coupling process Methods 0.000 claims description 4
- 238000005859 coupling reaction Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 5
- 239000003337 fertilizer Substances 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 241000276489 Merlangius merlangus Species 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- DHKHZGZAXCWQTA-UHFFFAOYSA-N [N].[K] Chemical compound [N].[K] DHKHZGZAXCWQTA-UHFFFAOYSA-N 0.000 description 1
- YUWBVKYVJWNVLE-UHFFFAOYSA-N [N].[P] Chemical compound [N].[P] YUWBVKYVJWNVLE-UHFFFAOYSA-N 0.000 description 1
- WZLMXYBCAZZIRQ-UHFFFAOYSA-N [N].[P].[K] Chemical compound [N].[P].[K] WZLMXYBCAZZIRQ-UHFFFAOYSA-N 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- QLULGSLAHXLKSR-UHFFFAOYSA-N azane;phosphane Chemical compound N.P QLULGSLAHXLKSR-UHFFFAOYSA-N 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical class [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 1
- 235000011151 potassium sulphates Nutrition 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
Images
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- Fertilizers (AREA)
Abstract
The utility model discloses a mixing tank, in particular to a mixing tank used in chemical industry for granulation fused slurry mixing tank, which comprises a motor, a cylinder, and a cover fixed on the cylinder, wherein the cover and the cylinder are provided with a feed inlet and a discharging outlet respectively; the motor is connected with the cover via a frame; the stirring shaft is fixed with a stirring paddle. The utility model is characterized in that: a flow guide cylinder is arranged in the cylinder, and a steam heating coiled pipe system is arranged between the flow guide cylinder and the cylinder. The mixing tank has the advantages of constant melt temperature, reasonable structure, and easy use, and enhances the evenness degree of the stir operation and the stir efficiency. The mixing tank is widely used in chemical industry for melting slurry.
Description
Technical field: the utility model relates to a kind of mixing channel, relates in particular to a kind of mixing channel that is used for melting charge slurry in industries such as chemical industry.
Technical background: in agricultural production, be extensive use of various fertilizer; mainly be chemical fertilizer of simple substance and contain nitrogen; phosphorus; the polyelement composite fertilizer of potassium and other nutrient; wherein the production method of compound fertilizer mainly contains granulating method; slurry process; extrusion and blending method etc.; they are with urea; ammonium nitrate; the phosphorus ammonium; coarse whiting; potassium chloride; potassium sulfates etc. carry out secondary operations and make the compound fertilizer that contains various nutrient elements such as nitrogen phosphorus potassium; for example; a kind of ammonium nitrate one urea melting slip drum granulating is produced the method for granular complex fertilizer; in this production technology; at first be with an amount of ammonium nitrate; the urea raw material in mixing channel under 100-140 ℃ of temperature conditions Hybrid Heating become melting charge slurry; then with melting charge slurry by shower nozzle atomizing and with fine silt nitrogen phosphorus; nitrogen potassium or nitrogen; phosphorus; the granulation in rotary drum granulator of potassic fertilizer and filler, the material after the granulation obtains granular nitrogen after the cooler cooling; phosphorus; K compound fertilizer.There is following shortcoming aborning in present employed melting charge slurry mixing channel: 1. owing to material when stirring directly flows out from discharging opening under situation about fully not mixing sometimes, melting charge slurry is mixed inhomogeneous, and the compound fertilizer of production be can't meet the quality requirement; 2. electrical heating is mainly adopted in the heating of melting charge slurry, and electric heating equipment is subjected to the influence of extraneous factor on the one hand easily, and heating does not reach desirable effect; Often damage needing repairing on the other hand, reduced production efficiency, improved production cost.
Summary of the invention: characteristics such as the utility model purpose is to provide a kind of improved high-tower granulation melting charge slurry mixing channel, and it is even to have melt temperature, rational in infrastructure, easy to use, the efficient of fusion is greatly improved.
The utility model is achieved in that a kind of high-tower granulation melting charge slurry mixing channel, comprise motor, cylindrical shell, cover plate and heating system, described cover plate is fixed on the described cylindrical shell, on described cover plate and cylindrical shell, be respectively arranged with charging aperture and discharging opening, described motor connects on the cover board by support, described motor is fixed with shaft by shaft coupling, be fixed with stirring arm on the described shaft, it is characterized in that: be provided with guide shell in described inner barrel, between described guide shell and cylindrical shell, be provided with the steam(-)coil system.
The utility model compared with prior art has following advantage:
1. characteristics such as it makes steam heated method, and it is even to have melt temperature, and is rational in infrastructure, easy to use make the temperature of fusion reach desirable effect;
2. owing to adopted guide shell, make material constantly upwards upset when mixing stirring, return the bottom of guide shell then by the thermal treatment zone, so continuous circulation mixes stirring and has improved the uniformity and the efficient that stir.
3. because the mixing channel bottom is provided with evacuation port, made things convenient for the cleaning of mixing channel.
Description of drawings: Fig. 1 is the structural representation of the utility model high-tower granulation melting charge slurry mixing channel
1. motor 2. shaft couplings 3. charging apertures 4. cover plates 5. cylindrical shells 6. shafts 7. guide shells 8. stirring arms 9. steam(-)coil systems 10. discharging openings, 11. supports, 12. evacuation ports
The specific embodiment: as can be seen from Figure 1, a kind of high-tower granulation melting charge slurry mixing channel, comprise motor 1, cylindrical shell 5, cover plate 4 and heating system, described cover plate 4 is fixed on the described cylindrical shell 5, on described cover plate 4 and cylindrical shell 5, be respectively arranged with charging aperture 3 and discharging opening 10, described motor 1 is connected on the cover plate 4 by support 11, described motor 1 is fixed with shaft 6 by shaft coupling 2, be fixed with stirring arm 8 on the described shaft 6, it is characterized in that: be provided with guide shell 7 in described cylindrical shell 5 inside.
In order to make the melt temperature uniform high-efficiency, the heating system that is provided with between described guide shell 7 and cylindrical shell 5 is a steam(-)coil system 9.
The cleaning of mixing channel is provided with evacuation port 12 in the bottom of described cylindrical shell 5 for convenience.
Claims (3)
1. high-tower granulation melting charge slurry mixing channel, comprise motor (1), cylindrical shell (5), cover plate (4) and heating system, described cover plate (4) is fixed on the described cylindrical shell (5), on described cover plate (4) and cylindrical shell (5), be respectively arranged with charging aperture (3) and discharging opening (10), described motor (1) is connected on the cover plate (4) by support (11), described motor (1) is fixed with shaft (6) by shaft coupling (2), be fixed with stirring arm (8) on the described shaft (6), it is characterized in that: be provided with guide shell (7) in described cylindrical shell (5) inside.
2. high-tower granulation melting charge slurry mixing channel according to claim 1 is characterized in that: described heating system is steam(-)coil system (9).
3. high-tower granulation melting charge slurry mixing channel according to claim 1 is characterized in that: the cleaning of mixing channel for convenience is provided with evacuation port (12) in the bottom of described cylindrical shell (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200620077474.7U CN200945423Y (en) | 2006-08-15 | 2006-08-15 | High tower granulation fused slurry mixing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200620077474.7U CN200945423Y (en) | 2006-08-15 | 2006-08-15 | High tower granulation fused slurry mixing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200945423Y true CN200945423Y (en) | 2007-09-12 |
Family
ID=38732484
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200620077474.7U Expired - Lifetime CN200945423Y (en) | 2006-08-15 | 2006-08-15 | High tower granulation fused slurry mixing tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200945423Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101391904B (en) * | 2008-10-24 | 2012-05-23 | 江苏阿波罗复合肥有限公司 | Urea melting apparatus |
| CN109395647A (en) * | 2018-11-19 | 2019-03-01 | 宁波富理电池材料科技有限公司 | A kind of double ultrasound couple devices and the method for preparing lithium-rich manganese-based anode material presoma and its positive electrode |
-
2006
- 2006-08-15 CN CN200620077474.7U patent/CN200945423Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101391904B (en) * | 2008-10-24 | 2012-05-23 | 江苏阿波罗复合肥有限公司 | Urea melting apparatus |
| CN109395647A (en) * | 2018-11-19 | 2019-03-01 | 宁波富理电池材料科技有限公司 | A kind of double ultrasound couple devices and the method for preparing lithium-rich manganese-based anode material presoma and its positive electrode |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: He Guangyu Document name: Notification to Pay the Fees |
|
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 225453 No. 98, Tai Chang Road, Hongqiao Industrial Park, Taixing, Jiangsu (Jiangsu Jinli Chemical Machinery Co., Ltd.) Patentee after: He Guangyu Address before: 214537, No. 2, North Road, Xinqiao Town, Xinqiao Town, Jiangsu City, Jingjiang province (Jingjiang Jinli chemical equipment factory) Patentee before: He Guangyu |
|
| CX01 | Expiry of patent term |
Granted publication date: 20070912 |
|
| EXPY | Termination of patent right or utility model |