CN203310231U - Drying equipment for granular wet materials - Google Patents
Drying equipment for granular wet materials Download PDFInfo
- Publication number
- CN203310231U CN203310231U CN2013202181430U CN201320218143U CN203310231U CN 203310231 U CN203310231 U CN 203310231U CN 2013202181430 U CN2013202181430 U CN 2013202181430U CN 201320218143 U CN201320218143 U CN 201320218143U CN 203310231 U CN203310231 U CN 203310231U
- Authority
- CN
- China
- Prior art keywords
- level
- order
- stage
- dry bucket
- thermal current
- 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
- 238000001035 drying Methods 0.000 title claims abstract description 37
- 239000000463 material Substances 0.000 title claims abstract description 29
- 239000002912 waste gas Substances 0.000 abstract 4
- 230000015572 biosynthetic process Effects 0.000 description 6
- 239000008187 granular material Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
Drying equipment for granular wet materials comprises a hopper, a first-stage hot air flow pipe, a first-stage drying bucket, a first-stage waste gas port, a first-stage material outlet, a second-stage hot air flow pipe, a second-stage drying bucket, a second-stage waste gas port and a second-stage material outlet, wherein the hopper and the first-stage hot air flow pipe are respectively connected with the upper portion of the first-stage drying bucket, the first-stage waste gas port is formed in a position, near the upper portion, of the lateral wall of the first-stage drying bucket, the first-stage material outlet is formed under the first-stage drying bucket and is connected with the second-stage drying bucket, the second-stage hot air flow pipe is connected with the upper portion of the second-stage drying bucket, the second-stage waste gas port is installed in a position, near the upper portion, of the lateral wall of the second-stage drying bucket, and the second-stage material outlet is located right under the second-stage drying bucket. The drying equipment for granular wet materials has the advantages of being simple in principle structure, reasonable in distribution of hot air flow and uniform in drying effect, and largely improving efficiency.
Description
Technical field
The utility model relates to granular wet stock drying structure field, particularly a kind of granular wet stock drying equipment.
Background technology
At present, existing equipment is generally thermal current to the dry run of granular wet stock and directly dries up, and causes dried product humidity inhomogeneous, and drying effect is bad, and efficiency is low simultaneously.
The utility model content
The purpose of this utility model is in order to meet the granular material uniform drying, to raise the efficiency, and the spy provides a kind of granular wet stock drying equipment.
The utility model provides a kind of granular wet stock drying equipment, it is characterized in that: described granular wet stock drying equipment, comprise hopper 1, first order thermal current pipe 2, the dry bucket 3 of the first order, first order exhaust outlet 4, first order material outlet 5, second level thermal current pipe 6, the dry bucket 7 in the second level, second level exhaust outlet 8, second level material outlet 9;
Wherein: hopper 1 is connected with the top of the dry bucket 3 of the first order respectively with first order thermal current pipe 2, first order exhaust outlet 4 is arranged in the position of the dry bucket of the first order 3 top sections of sidewall, with first order thermal current pipe 2 with respect to becoming 180 ° of layouts, first order material outlet 5 is arranged on the below of the dry bucket 3 of the first order, is connected with the dry bucket 7 in the second level;
Second level thermal current pipe 6 is connected with the top of the dry bucket 7 in the second level, second level exhaust outlet 8 is arranged on the top position of sidewall of the dry bucket 7 in the second level, and with second level thermal current pipe 6 with respect to becoming 180 ° of layouts, second level material outlet 9 be positioned at the dry bucket 7 in the second level under.
The air-flow incident direction of first order thermal current pipe 2 becomes 60 ° of layouts with the axis direction angle of the dry bucket 3 of the first order, is convenient to realize that granular wet stock is at the dry bucket of the first order 3 interior formation whirlpool shapes.
The air-flow incident direction of second level thermal current pipe 6 becomes 60 ° of layouts with the axis direction angle of the dry bucket 7 in the second level, is convenient to realize that granular wet stock is at second level drying bucket 7 interior formation whirlpool shapes.
First order thermal current pipe 2 is 1:7 with the diameter ratio of the dry bucket 3 of the first order, is convenient to strengthen the hot gas flow.
Second level thermal current pipe 6 is 1:10 with the diameter ratio of the dry bucket 7 in the second level, the hot gas flow is less than the thermal current in first order thermal current pipe 2, to prevent that granular material comparatively dry in the dry bucket 7 in the second level from, along 8 discharges of second level exhaust outlet, polluting and wasting.
The material of the dry bucket 3 of the first order and the dry bucket 7 in the second level is corrosion resistant plastic material spare.
Advantage of the present utility model:
Granular wet stock drying equipment described in the utility model, theory structure is simple, the hot gas flow distribution is reasonable, drying effect all with, efficiency improves greatly.
The accompanying drawing explanation
Below in conjunction with drawings and the embodiments, the utility model is described in further detail:
Fig. 1 is granular wet stock drying equipment theory structure schematic diagram;
Fig. 2 is the first order dry bucket upper surface charging aperture and air flow inlet deployment scenarios schematic diagram;
Fig. 3 is the second level dry bucket upper surface charging aperture and air flow inlet deployment scenarios schematic diagram;
In figure, 301 is the material inlet of the dry bucket of the first order, and 302 is the import of the dry bucket of first order thermal current, and 701 is the material inlet of the dry bucket in the second level, the thermal current import of the dry bucket in 702 second level.
The specific embodiment
The present embodiment provides a kind of granular wet stock drying equipment, it is characterized in that: described granular wet stock drying equipment, comprise hopper 1, first order thermal current pipe 2, the dry bucket 3 of the first order, first order exhaust outlet 4, first order material outlet 5, second level thermal current pipe 6, the dry bucket 7 in the second level, second level exhaust outlet 8, second level material outlet 9;
Wherein: hopper 1 is connected with the top of the dry bucket 3 of the first order respectively with first order thermal current pipe 2, first order exhaust outlet 4 is arranged in the position of the dry bucket of the first order 3 top sections of sidewall, with first order thermal current pipe 2 with respect to becoming 180 ° of layouts, first order material outlet 5 is arranged on the below of the dry bucket 3 of the first order, is connected with the dry bucket 7 in the second level;
Second level thermal current pipe 6 is connected with the top of the dry bucket 7 in the second level, second level exhaust outlet 8 is arranged on the top position of sidewall of the dry bucket 7 in the second level, and with second level thermal current pipe 6 with respect to becoming 180 ° of layouts, second level material outlet 9 be positioned at the dry bucket 7 in the second level under.
The air-flow incident direction of first order thermal current pipe 2 becomes 60 ° of layouts with the axis direction angle of the dry bucket 3 of the first order, is convenient to realize that granular wet stock is at the dry bucket of the first order 3 interior formation whirlpool shapes.
The air-flow incident direction of second level thermal current pipe 6 becomes 60 ° of layouts with the axis direction angle of the dry bucket 7 in the second level, is convenient to realize that granular wet stock is at second level drying bucket 7 interior formation whirlpool shapes.
First order thermal current pipe 2 is 1:7 with the diameter ratio of the dry bucket 3 of the first order, is convenient to strengthen the hot gas flow.
Second level thermal current pipe 6 is 1:10 with the diameter ratio of the dry bucket 7 in the second level, the hot gas flow is less than the thermal current in first order thermal current pipe 2, to prevent that granular material comparatively dry in the dry bucket 7 in the second level from, along 8 discharges of second level exhaust outlet, polluting and wasting.
The material of the dry bucket 3 of the first order and the dry bucket 7 in the second level is corrosion resistant plastic material spare.
The present embodiment provides a kind of granular wet stock drying equipment, it is characterized in that: described granular wet stock drying equipment, comprise hopper 1, first order thermal current pipe 2, the dry bucket 3 of the first order, first order exhaust outlet 4, first order material outlet 5, second level thermal current pipe 6, the dry bucket 7 in the second level, second level exhaust outlet 8, second level material outlet 9;
Wherein: hopper 1 is connected with the top of the dry bucket 3 of the first order respectively with first order thermal current pipe 2, first order exhaust outlet 4 is arranged in the position of the dry bucket of the first order 3 top sections of sidewall, with first order thermal current pipe 2 with respect to becoming 180 ° of layouts, first order material outlet 5 is arranged on the below of the dry bucket 3 of the first order, is connected with the dry bucket 7 in the second level;
Second level thermal current pipe 6 is connected with the top of the dry bucket 7 in the second level, second level exhaust outlet 8 is arranged on the top position of sidewall of the dry bucket 7 in the second level, and with second level thermal current pipe 6 with respect to becoming 180 ° of layouts, second level material outlet 9 be positioned at the dry bucket 7 in the second level under.
The air-flow incident direction of first order thermal current pipe 2 becomes 60 ° of layouts with the axis direction angle of the dry bucket 3 of the first order, is convenient to realize that granular wet stock is at the dry bucket of the first order 3 interior formation whirlpool shapes.
The air-flow incident direction of second level thermal current pipe 6 becomes 60 ° of layouts with the axis direction angle of the dry bucket 7 in the second level, is convenient to realize that granular wet stock is at second level drying bucket 7 interior formation whirlpool shapes.
First order thermal current pipe 2 is 1:7 with the diameter ratio of the dry bucket 3 of the first order, is convenient to strengthen the hot gas flow.
Second level thermal current pipe 6 is 1:10 with the diameter ratio of the dry bucket 7 in the second level, the hot gas flow is less than the thermal current in first order thermal current pipe 2, to prevent that granular material comparatively dry in the dry bucket 7 in the second level from, along 8 discharges of second level exhaust outlet, polluting and wasting.
Claims (5)
1. granular wet stock drying equipment, it is characterized in that: described granular wet stock drying equipment, comprise hopper (1), first order thermal current pipe (2), the dry bucket of the first order (3), first order exhaust outlet (4), first order material outlet (5), second level thermal current pipe (6), the dry bucket in the second level (7), second level exhaust outlet (8), second level material outlet (9);
Wherein: hopper (1) is connected with the top of the dry bucket of the first order (3) respectively with first order thermal current pipe (2), first order exhaust outlet (4) is arranged in the position of the dry bucket of the first order (3) top section of sidewall, with first order thermal current pipe (2) with respect to becoming 180 ° of layouts, first order material outlet (5) is arranged on the below of the dry bucket of the first order (3), is connected with the dry bucket in the second level (7); Second level thermal current pipe (6) is connected with the top of the dry bucket in the second level (7), second level exhaust outlet (8) is arranged on the top position of sidewall of the dry bucket in the second level (7), with second level thermal current pipe (6) with respect to becoming 180 ° of layouts, second level material outlet (9) be positioned at the dry bucket in the second level (7) under.
2. according to granular wet stock drying equipment claimed in claim 1, it is characterized in that: the air-flow incident direction of described first order thermal current pipe (2) becomes 60 ° of layouts with the axis direction of the dry bucket of the first order (3).
3. according to granular wet stock drying equipment claimed in claim 1, it is characterized in that: the air-flow incident direction of described second level thermal current pipe (6) becomes 60 ° of layouts with the axis direction of the dry bucket in the second level (7).
4. according to granular wet stock drying equipment claimed in claim 1, it is characterized in that: described first order thermal current pipe (2) is 1:7 with the diameter ratio of the dry bucket of the first order (3).
5. according to granular wet stock drying equipment claimed in claim 1, it is characterized in that: described second level thermal current pipe (6) is 1:10 with the diameter ratio of the dry bucket in the second level (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202181430U CN203310231U (en) | 2013-04-26 | 2013-04-26 | Drying equipment for granular wet materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202181430U CN203310231U (en) | 2013-04-26 | 2013-04-26 | Drying equipment for granular wet materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203310231U true CN203310231U (en) | 2013-11-27 |
Family
ID=49616435
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013202181430U Expired - Lifetime CN203310231U (en) | 2013-04-26 | 2013-04-26 | Drying equipment for granular wet materials |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203310231U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103217004A (en) * | 2013-04-26 | 2013-07-24 | 国家电网公司 | Granulous wet material drying device |
-
2013
- 2013-04-26 CN CN2013202181430U patent/CN203310231U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103217004A (en) * | 2013-04-26 | 2013-07-24 | 国家电网公司 | Granulous wet material drying device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202123798U (en) | High-pressure hot air curing and drying device | |
| CN204421551U (en) | Material drying machine | |
| CN203310231U (en) | Drying equipment for granular wet materials | |
| CN103217004B (en) | Granulous wet material drying device | |
| CN202941337U (en) | Grain drying tower capable of uniformly distributing hot gas | |
| CN203803345U (en) | Small-sized chlorine gas drying device | |
| CN202980039U (en) | Ventilation drying barn for grain storage | |
| CN204115443U (en) | A kind of Drying separator | |
| CN202376791U (en) | Dried exhaust discharging and precipitating device | |
| CN205152656U (en) | Quick dryer | |
| CN203799762U (en) | Cable drying cylinder | |
| CN204739858U (en) | Tealeaves stoving energy -saving equipment | |
| CN203731807U (en) | Energy-saving paper tube baking room | |
| CN204285980U (en) | A kind of three-pass rotary drum drying system for fermented bean dregs | |
| CN202032849U (en) | Powdery material dryer | |
| CN201917191U (en) | Device used for drying bamboo building template raw materials | |
| CN203162924U (en) | Device for recycling and reusing of hot steam in drying room | |
| CN207335380U (en) | Air knife structure | |
| CN207870217U (en) | A kind of segmented tea making tea drier | |
| CN203478857U (en) | Drying device for feed raw material | |
| CN205784491U (en) | A kind of sodium dithionite dry feed device of improvement | |
| CN203053198U (en) | Steam dehumidifying tower | |
| CN206645993U (en) | A kind of sludge dries hopper | |
| CN103407014A (en) | Vacuum drying machine | |
| CN202734456U (en) | Fertilizer drying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20131127 Effective date of abandoning: 20150114 |
|
| RGAV | Abandon patent right to avoid regrant |