CN201058849Y - Humic fertilizer soil fluidized fermentation tower - Google Patents
Humic fertilizer soil fluidized fermentation tower Download PDFInfo
- Publication number
- CN201058849Y CN201058849Y CNU2007201412964U CN200720141296U CN201058849Y CN 201058849 Y CN201058849 Y CN 201058849Y CN U2007201412964 U CNU2007201412964 U CN U2007201412964U CN 200720141296 U CN200720141296 U CN 200720141296U CN 201058849 Y CN201058849 Y CN 201058849Y
- Authority
- CN
- China
- Prior art keywords
- tower
- cone
- utility
- flow guiding
- shaped flow
- 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
Links
- 239000002689 soil Substances 0.000 title claims abstract description 11
- 239000003337 fertilizer Substances 0.000 title description 7
- 238000000855 fermentation Methods 0.000 title description 2
- 230000004151 fermentation Effects 0.000 title description 2
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- YYRMJZQKEFZXMX-UHFFFAOYSA-L calcium bis(dihydrogenphosphate) Chemical compound [Ca+2].OP(O)([O-])=O.OP(O)([O-])=O YYRMJZQKEFZXMX-UHFFFAOYSA-L 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000019691 monocalcium phosphate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Fertilizers (AREA)
Abstract
The utility model relates to a fluidized drying tower for humic fertile soil, wherein, the top and the bottom of a tower body are respectively provided with a feed port and a discharge port. The structure design of the utility model is characterized in that: a cone-shaped flow guiding body with a trumpet-shaped opening upwards is arranged inside the tower body; the cone angle alpha of the cone-shaped flow guiding body is 15-90 degrees; the side of the cone-shaped flow guiding body is fixed with the tower body through a mounting rack; an air inlet pipe enters from the bottom of the tower body and extends into the cone-shaped flow guiding body. The utility model has the advantages of simple structure, convenient use and low cost.
Description
Technical field
The utility model is a kind of soil ulmin loam fluidized drying tower, belongs to the technical field of structures of engineering goods.
Background technology
Tower is generally still moisture higher to the soil ulmin composting material of slaking by fermentation, needs the drying processed, as is processed into organic-inorganic compound mixed fertilizer, also need add calcium superphosphate etc. according to the needs of filling a prescription, and other inorganic fertilizers also need drying.Handle this class chemical fertilizer product at present and use mode drying treatment such as stack gas heat rejector mobile rotary furnace, belt stove or thermal pit fixed bed.
Along with the direction of fertilizer towards efficient, compound (organic and inorganic) slow develops, require to realize granulating, so mixing the water content of granulating the back, fertilizer becomes an important indicator.As previously shown, if the material after the During High-Temperature Composting can bring difficulty without the requirement of drying plant drying and dehydrating with regard to the incompatibility granulating working procedure, if dry, air-dry, the temperature of so natural climate, wet weather, bulk cargo stirs, dust, the capital is brought the part introduced contaminants into and is entered fertilizer, becomes the objectionable impurities composition, also can cause bulk cargo to blow away loss etc.
Summary of the invention
The purpose of this utility model designs at present technical requirement just a kind of soil ulmin loam fluidized drying tower is provided, its objective is for the material after the compost treatment provide a high-efficiency cleaning, easy reliably, drying means cheaply, for realizing that granulation provides a guarantee.The utility model device adopts the mentality of designing of fluidized bed, and improved on this basis and be designed to a kind of soil ulmin loam fluidized drying tower, it can accelerate heat transfer rate, enlarges the mass transfer specific surface area, accelerate dewatering speed, fully carried out heat exchange.
The purpose of this utility model realizes by following measure:
This kind soil ulmin loam fluidized drying tower, the top of its body of the tower and bottom are respectively opening for feed and discharge port, its structural design features is: loud-speaker shape opening taper baffle up is installed in body of the tower, its cone angle is 15～90 °, the central lines of its medullary ray and body of the tower, fixedly connected with body of the tower by erecting frame in its side, blast pipe from body of the tower bottom enter and the taper baffle that stretches.
Description of drawings
Fig. 1 is the one-piece construction synoptic diagram of the utility model device
Embodiment
Below with reference to drawings and Examples the utility model device is further described:
Shown in accompanying drawing 1, this kind soil ulmin loam fluidized drying tower, the top of its body of the tower 1 and bottom are respectively opening for feed 2 and discharge port 3, body of the tower 1 is columned cylindrical shell, its height and diameter are determined by treatment capacity, body of the tower 1 can be used Steel Concrete, also available steel plate structure is made, in body of the tower 1, loud-speaker shape opening taper baffle 4 up is installed, its length is 1/3rd of body of the tower 1 length, its cone angle is 30 °, the central lines of its medullary ray and body of the tower 1, its side are fixedlyed connected with body of the tower 1 by erecting frame 5, blast pipe 6 from body of the tower 1 bottom enter and the taper baffle 4 that stretches.
During the utility model device busy, drying air stream directly blows in the taper baffle 4 from the blast pipe 6 of body of the tower 1 bottom, and formation rotation type air current, can be in taper baffle 4, stir material from bottom to up, be fountain attitude cyclic drying, significantly enlarged the dry surface in contact of gas-solid, reach and accelerate the exsiccant purpose.The complete feed layer is stirred continuously simultaneously.Because organic soil ulmin density unevenness is even, causes fluidizing velocity variant, carries out so will operate with the slowest processing condition, material is longer at dwell time in the tower.So batch operation method of once emitting when taking material totally to reach processing requirement.
That the utility model device has is simple in structure, easy to use, cost is low, dry mass is high Advantage.
Claims (1)
1. soil ulmin loam fluidized drying tower, top of its body of the tower (1) and bottom are respectively opening for feed (2) and discharge port (3), it is characterized in that: loud-speaker shape opening taper baffle (4) up is installed in body of the tower (1), its cone angle is 15～90 °, the central lines of its medullary ray and body of the tower (1), fixedly connected with body of the tower (1) by erecting frame (5) in its side, blast pipe (6) bottom body of the tower (1), enter and the taper baffle (4) that stretches.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201412964U CN201058849Y (en) | 2007-04-02 | 2007-04-02 | Humic fertilizer soil fluidized fermentation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201412964U CN201058849Y (en) | 2007-04-02 | 2007-04-02 | Humic fertilizer soil fluidized fermentation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201058849Y true CN201058849Y (en) | 2008-05-14 |
Family
ID=39407311
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201412964U Expired - Fee Related CN201058849Y (en) | 2007-04-02 | 2007-04-02 | Humic fertilizer soil fluidized fermentation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201058849Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928162A (en) * | 2009-04-02 | 2010-12-29 | 邵海锋 | Static aerobic fermentation drying tower and application |
| CN104154731A (en) * | 2014-08-03 | 2014-11-19 | 浙江海亮环境材料有限公司 | Air interchanger for primary drying of SCR denitration catalyst and air interchanging method of air interchanger |
-
2007
- 2007-04-02 CN CNU2007201412964U patent/CN201058849Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928162A (en) * | 2009-04-02 | 2010-12-29 | 邵海锋 | Static aerobic fermentation drying tower and application |
| CN104154731A (en) * | 2014-08-03 | 2014-11-19 | 浙江海亮环境材料有限公司 | Air interchanger for primary drying of SCR denitration catalyst and air interchanging method of air interchanger |
| CN104154731B (en) * | 2014-08-03 | 2016-03-02 | 浙江海亮环境材料有限公司 | For air interchanger and the air exchanging method thereof of the drying of SCR denitration one-level |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: YANG YUNQI Free format text: FORMER OWNER: BEIJING YINGRUI WEIYE HIGH-TECH. CO., LTD. Effective date: 20080418 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20080418 Address after: Beijing City, Haidian District Zhongguancun Huangzhuang 814 Building No. 207, zip code: 100080 Patentee after: Yang Yunqi Address before: Room 2105, block B, digital building, No. 2, Zhongguancun Avenue, Beijing, 100081 Patentee before: Beijing Yingrui Weiye High-Tech. Co., Ltd. |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080514 Termination date: 20100402 |