CN105135823A - Drying system - Google Patents
Drying system Download PDFInfo
- Publication number
- CN105135823A CN105135823A CN201510664176.1A CN201510664176A CN105135823A CN 105135823 A CN105135823 A CN 105135823A CN 201510664176 A CN201510664176 A CN 201510664176A CN 105135823 A CN105135823 A CN 105135823A
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- dryer
- output
- output end
- conveyor
- drying
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Abstract
The invention provides a drying system. The drying system comprises a primary conveyor, a rotary cutter, a secondary conveyor, a dryer, a combustor, a gas generator, a discharge device, an induced draught system, a deduster, a tertiary conveyor, a crusher and a winnow, wherein the rotary cutter is connected with an output end of the primary conveyor; the secondary conveyor is connected with an output end of the rotary cutter; the dryer is connected with an output end of the secondary conveyor; the combustor is connected with one end of the dryer; the gas generator is connected with an input end of the combustor; the discharge device is connected with the other end of the dryer; the induced draught system is connected above an output end of the discharge device; the deduster is connected with an output end of the induced draught system; the tertiary conveyor is connected below the output end of the discharge device; the crusher is connected with an output end of the tertiary conveyor; the winnow is connected with an output end of the crusher; and the three conveyors are inclined belt conveyors. The drying system has high dryer processing capacity and is low in fuel consumption and drying cost.
Description
Technical field
The present invention relates to a kind of drying system, belong to drying technology field.
Background technology
Drying system is that material passes through rotate back and forth inside at oven dry machine barrel and make a kind of drying device of heating material.Dry wet stock delivers to hopper by belt conveyor or bucket elevator, and the charger then through hopper enters feed end by feeding tube.The gradient of feeding tube is greater than the angle of crater of material, so that material flows in drier smoothly.Material adds from higher one end, and thermophore is entered by low side, becomes counter current contacting with material, also has thermophore together with material and flows to into cylindrical shell.Rotation material gravitate along with cylinder runs to the one end end of compared with.Wet stock in cylindrical shell in movement forward, directly or indirectly obtain thermophore to heat, make wet stock be able to drying, then send through belt feeder or conveying worm at discharge end.Cylinder inboard wall is equipped with flight, and its effect material is taken up and spreads down, and the contact surface of material and air-flow is increased, to improve rate of drying and to promote that material advances.Thermophore is generally divided into hot-air, flue gas etc.After thermophore drying device, generally need cyclone dust collectors by gas be with material to trap.As needed to reduce tail gas dustiness further, also should put again after sack cleaner or hydrofilter.
Existing drying system drying machine disposal ability is little, and fuel consumption is many, and drying cost is high.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art part, a kind of drying system is provided.
Drying system of the present invention, comprise primary conveyor, the peeler be connected with primary conveyor output, the two-stage conveying machine be connected with peeler output, the dryer be connected with two-stage conveying machine output, the combustion chamber be connected with dryer one end, the gas generator be connected with combustion chamber input, the drawing mechanism be connected with the dryer other end, the induced draught system be connected with above drawing mechanism output, the deduster be connected with induced draught system output, the three grades of conveyers be connected with below drawing mechanism output, the disintegrating machine be connected with three grades of conveyer outputs, the Winnowing machine be connected with disintegrating machine output, three described conveyers are tilting belt conveyor.
Drying system drying machine disposal ability of the present invention is large, and fuel consumption is few, and drying cost is low.
Accompanying drawing explanation
Fig. 1 is the structural representation of drying system of the present invention.
Wherein, 1 is primary conveyor, and 2 is peeler, and 3 is two-stage conveying machine, and 4 is dryer, and 5 is combustion chamber, and 6 is gas generator, and 7 is drawing mechanism, and 8 is induced draught system, and 9 is deduster, and 10 is three grades of conveyers, and 11 is disintegrating machine, and 12 is Winnowing machine.
Detailed description of the invention
Drying system of the present invention, comprise primary conveyor 1, the peeler 2 be connected with primary conveyor 1 output, the two-stage conveying machine 3 be connected with peeler 2 output, the dryer 4 be connected with two-stage conveying machine 3 output, the combustion chamber 5 be connected with dryer 4 one end, the gas generator 6 be connected with combustion chamber 5 input, the drawing mechanism 7 be connected with dryer 4 other end, the induced draught system 8 be connected with above drawing mechanism 7 output, the deduster 9 be connected with induced draught system 8 output, the three grades of conveyers 10 be connected with below drawing mechanism 7 output, the disintegrating machine 11 be connected with three grades of conveyer 10 outputs, the Winnowing machine 12 be connected with disintegrating machine 11 output, three described conveyers are tilting belt conveyor.
The course of work of the present invention is as follows, wet feed is through primary conveyor 1, peeler 2, two-stage conveying machine 3, dryer 4, drawing mechanism 7, three grades of conveyers 10, disintegrating machine 11 and Winnowing machines 12, dry as finished product exports, wherein dust is discharged through induced draught system 8 and deduster 9.
Claims (1)
1. drying system, it is characterized in that, comprise primary conveyor, the peeler be connected with primary conveyor output, the two-stage conveying machine be connected with peeler output, the dryer be connected with two-stage conveying machine output, the combustion chamber be connected with dryer one end, the gas generator be connected with combustion chamber input, the drawing mechanism be connected with the dryer other end, the induced draught system be connected with above drawing mechanism output, the deduster be connected with induced draught system output, the three grades of conveyers be connected with below drawing mechanism output, the disintegrating machine be connected with three grades of conveyer outputs, the Winnowing machine be connected with disintegrating machine output, three described conveyers are tilting belt conveyor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510664176.1A CN105135823A (en) | 2015-10-13 | 2015-10-13 | Drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510664176.1A CN105135823A (en) | 2015-10-13 | 2015-10-13 | Drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105135823A true CN105135823A (en) | 2015-12-09 |
Family
ID=54721270
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510664176.1A Pending CN105135823A (en) | 2015-10-13 | 2015-10-13 | Drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105135823A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080201978A1 (en) * | 2005-01-13 | 2008-08-28 | Asbjorn Hammer | Device For Drying Material |
| CN201173666Y (en) * | 2008-02-03 | 2008-12-31 | 李国鹏 | Equipment for drying slag ball |
| WO2010084156A1 (en) * | 2009-01-21 | 2010-07-29 | Paul Wurth S.A. | Method for producing pulverized coal |
| CN201992959U (en) * | 2011-03-10 | 2011-09-28 | 郑州市鼎力干燥设备有限公司 | Coal slurry drying device |
| CN203177631U (en) * | 2013-03-28 | 2013-09-04 | 河南南洋环保机械有限公司 | Drying barrel with material carrying device and lignite drying machine with drying barrel |
| CN205048881U (en) * | 2015-10-13 | 2016-02-24 | 江苏天鹏机电制造有限公司 | Drying system |
-
2015
- 2015-10-13 CN CN201510664176.1A patent/CN105135823A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080201978A1 (en) * | 2005-01-13 | 2008-08-28 | Asbjorn Hammer | Device For Drying Material |
| CN201173666Y (en) * | 2008-02-03 | 2008-12-31 | 李国鹏 | Equipment for drying slag ball |
| WO2010084156A1 (en) * | 2009-01-21 | 2010-07-29 | Paul Wurth S.A. | Method for producing pulverized coal |
| CN201992959U (en) * | 2011-03-10 | 2011-09-28 | 郑州市鼎力干燥设备有限公司 | Coal slurry drying device |
| CN203177631U (en) * | 2013-03-28 | 2013-09-04 | 河南南洋环保机械有限公司 | Drying barrel with material carrying device and lignite drying machine with drying barrel |
| CN205048881U (en) * | 2015-10-13 | 2016-02-24 | 江苏天鹏机电制造有限公司 | Drying system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151209 |
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| RJ01 | Rejection of invention patent application after publication |