CN209623315U - A kind of pneumatic conveying dryer - Google Patents
A kind of pneumatic conveying dryer Download PDFInfo
- Publication number
- CN209623315U CN209623315U CN201822268618.2U CN201822268618U CN209623315U CN 209623315 U CN209623315 U CN 209623315U CN 201822268618 U CN201822268618 U CN 201822268618U CN 209623315 U CN209623315 U CN 209623315U
- Authority
- CN
- China
- Prior art keywords
- drying tube
- conveying mechanism
- drying
- pneumatic conveying
- feed inlet
- 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.)
- Active
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a kind of drying equipments, more particularly to a kind of pneumatic conveying dryer, including front conveying mechanism, the drying tube that is connected with conveying mechanism and the processing unit for being connected to drying tube rear portion, the output end of the conveying mechanism is connected at the feed inlet of drying tube, hot wind conveying mechanism is connected with below the drying tube feed inlet, the hot wind conveying mechanism includes sequentially connected air filter, air blower and vapor heat exchanger, compared with prior art, the beneficial effects of the utility model are: the environmental protection airing drying machine of the utility model, the air filter is located at the front end of air blower, vapor heat exchanger is located at the rear end of air blower, and it is directly connect with drying tube.By strong negative-pressure caused by air blower and subsequent air-introduced machine, so that material moment at feed opening enters drying tube.
Description
Technical field
The utility model relates to a kind of drying equipments, and in particular to a kind of pneumatic conveying dryer.
Background technique
Drying steps can be passed through in amino-acid chelate production process, hot air inlet pipe is entered with suitable spout velocity
Dry motor spindle enters material dispersion hothouse, generates that strong dispersion, blow floating rotary operation to material, then material by from
The heart, dispersion, collision, friction and by micronized, enhance mass-and heat-transfer.In the bottom of drying machine, larger wetter cluster of grains exists
Under the action of blender by mechanical blowing dissipate, moisture content it is lower, the lesser particle of granularity by swirling eddy carry secretly rise, rising
It is further dried in the process.Since gas-particle two-phase makees rotational flow, solid phase inertia is greater than gas phase, the alternate relative velocity of solid gas two
It is larger, strengthen two alternate heat and mass, so machine production intensity is high.
Its working method is usual are as follows: wet feed is added to upright pipe through feeder, and air is heated through the heater in air blower
After be blown into upright pipe, the wind speed in pipe is decided by the granular size and density of wet feed, the generally higher than sinking speed of particle, has done
Dry particle is taken out of by strong air-flow, is sent in two cyclone separators in parallel and separates, tail gas is set through bag type dust collection
It is standby to gather dust.But some substances for having peculiar smell volatile generated in process of production only use bag collection, cannot effectively go
Locate peculiar smell.Internal moisture discharges caused by being also possible to occur because of hot-spot after the material of heat drying is directly packaged bag
To surface, causes recrystallization to generate caking phenomenon, seriously affected the physical stability of product.
Therefore, a kind of new pneumatic conveying dryer is developed, not only there is urgent researching value, it may have good economic effect
Benefit and commercial application potentiality, this is exactly where the power that the utility model is accomplished and basis.
Utility model content
In order to overcome the defect of the prior art as indicated above, the utility model people has made intensive studies this, In
After having paid a large amount of creative works, so as to complete the utility model.
Specifically, the technical problem to be solved by the utility model is to provide a kind of pneumatic conveying dryer, it is existing to solve
The easy the technical issues of of influencing environment such as having machinery, energy consumption is high, and peculiar smell easily distributes.
To achieve the above object, the utility model provides the following technical solutions:
A kind of pneumatic conveying dryer including front conveying mechanism, the drying tube being connected with conveying mechanism and is connected to drying
The output end of the processing unit at pipe rear portion, the conveying mechanism is connected at the feed inlet of drying tube, the drying tube feed inlet
Lower section is connected with hot wind conveying mechanism, and the hot wind conveying mechanism includes sequentially connected air filter, air blower and steam
Heat exchanger, the air outlet of the vapor heat exchanger are communicated in the drying tube below feed inlet, and the processing unit includes successively
Primary cyclone, deduster, ozone generator, secondary cyclone and the rewinding blower of connection, the one cyclonic
The feed end of separator is connected with the discharge end of drying tube.
In the present invention, as an improvement, the internal diameter thickness checker of the drying tube, drying tube is interior to be installed
There is the spinning disk of helically type curve, around dry inside pipe wall setting, the spinning disk lateral wall is fixed on dry the spinning disk
On dry pipe.
In the present invention, as an improvement, the inverted u-shaped setting of drying tube, the spinning disk is mounted on dry
In the second half of dry pipe.
In the present invention, as an improvement, the primary cyclone is connected with cooled dehumidifier unit, described cold
The air outlet for freezing dehumidifier is connected at the blanking of primary cyclone feed inlet.
In the present invention, as an improvement, the deduster is water dust scrubber.
In the present invention, as an improvement, the ammonia redox in gas is made ammonia by the ozone generator
Gas is discharged after being converted into innocuous gas.
In the present invention, as an improvement, the front end of the air blower is equipped with anemobiagraph.
In the present invention, as an improvement, the conveying mechanism is conveying belt conveyor, the conveying mechanism
Front end is connected with weighing belt, and material is sent into the feed inlet of drying tube by weighing belt.
Compared with prior art, the utility model has the beneficial effects that
(1) the environmental protection airing drying machine of the utility model, the air filter are located at the front end of air blower, vapor heat exchanger
It is connect positioned at the rear end of air blower, and directly with drying tube.By strong negative-pressure caused by air blower and subsequent air-introduced machine,
So that material moment at feed opening enters drying tube.
(2) the environmental protection airing drying machine of the utility model, the vapor heat exchanger of drying tube front end provide stable heat source,
The wind speed for cooperating air blower powerful, so that the temperature that heat source provides is dispersed rapidly, so that being heated evenly for material, effectively keeps away
Exempt from the coking and discoloration of heat-sensitive substance.
(3) the environmental protection airing drying machine of the utility model, the second half of drying tube is equipped with spinning disk, tangential to blow, and mentions
High wind speed preferably obtains the material of low moisture and high fineness so that material is dry again at the middle part of drying process and hits.
Detailed description of the invention
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific embodiment or attached drawing needed to be used in the description of the prior art are briefly described.In all the appended drawings, similar
Element or part are generally identified by similar appended drawing reference.In attached drawing, each element or part might not be according to actual ratios
It draws.
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the structural upright schematic diagram of the utility model；
Fig. 3 is the structural schematic diagram of the utility model spinning disk；
Fig. 4 is the structural schematic diagram of the utility model conveying mechanism and drying tube；
Fig. 5 is the structural schematic diagram of the utility model processing unit；
In figure: 1, drying tube, 2, air filter, 3, air blower, 4, vapor heat exchanger, 5, primary cyclone, 6,
Deduster, 7, ozone generator, 8, secondary cyclone, 9, rewinding blower, 10, spinning disk, 11, anemobiagraph, 12, belt
Scale, 13, cooled dehumidifier unit, 14, air-introduced machine, 15, conveying belt conveyor.
Specific embodiment
It is described in detail below in conjunction with embodiment of the attached drawing to technical solutions of the utility model.Following embodiment is only
For clearly illustrating the technical solution of the utility model, therefore it is only used as example, and it is originally practical to cannot be used as a limitation limitation
Novel protection scope.
As Figure 1-Figure 5, a kind of pneumatic conveying dryer, including front conveying mechanism, the drying being connected with conveying mechanism
Pipe 1 and the processing unit for being connected to 1 rear portion of drying tube, the conveying mechanism, drying tube 1 and processing unit are mounted on rack
On, and be fixedly installed, the drying tube 1 is round tube, material is sent at the feed inlet of drying tube 1 by conveying mechanism, via
Drying tube 1 is entered in processing unit after conveying by the discharge port of drying tube 1, carries out subsequent processing step.
The output end of the conveying mechanism is connected at the feed inlet of drying tube 1, connection below 1 feed inlet of drying tube
There is hot wind conveying mechanism, the hot wind conveying mechanism is passed through hot wind into drying tube 1, and drives material in drying tube by hot wind
Walking in 1, the hot wind conveying mechanism includes sequentially connected air filter 2, air blower 3 and vapor heat exchanger 4, the steaming
The air outlet of vapour heat exchanger 4 is communicated in the drying tube 1 below feed inlet, and air blower 3 is drawn air into, and is passed through during inhalation
The filtering of air filter 2 is crossed, avoids impurity in hot wind more, the wind of blowout enters drying tube 1 after heating by vapor heat exchanger 4
It is interior, since the lower end of feed inlet is arranged in air inlet, material is blown upwards in material bottom into the hot wind in drying tube 1, is made
Material more disperses during transportation, and drying effect is more preferably.
The processing unit includes sequentially connected primary cyclone 5, deduster 6, ozone generator 7, second level rotation
The feed end of wind separator 8 and rewinding blower 9, the primary cyclone 5 is connected with the discharge end of drying tube 1, and described one
Grade cyclone separator 5 is connected with cooled dehumidifier unit 13, and the air outlet of the cooled dehumidifier unit 13 is connected to primary cyclone 5
At the blanking of feed inlet, the material after drying enters primary cyclone 5 via the discharge end of drying tube 1, and the freezing removes
Wet machine 13 is passed through cold wind to primary cyclone 5, into the rapid cool-down dehumidification of material of primary cyclone 5, after
Continuous processing step.
The internal diameter thickness checker of the drying tube 1 so that the wind speed of drying changes repeatedly, and then sufficiently makes material exist
It is dry in drying tube 1, the spinning disk 10 of helically type curve is installed, the spinning disk 10 is mounted on drying tube 1 in drying tube 1
The second half in, the spinning disk 10 is arranged around 1 inner wall of drying tube, and 10 lateral wall of spinning disk is fixed on drying tube 1,
So that after the drying the phase generate strong swirling eddy again, to the material on wall generate it is strong wash away the effect of taking out of, disappear
Except wall sticking phenomenon.
The inverted u-shaped setting of the drying tube 1 reduces occupied area and extends drying time of the material in drying tube 1.
Air-introduced machine 14 is equipped between the primary cyclone 5 and deduster 6, air-introduced machine 14 absorbs material, described to remove
Dirt device 6 is water dust scrubber.
Following reaction is occurred for the ammonia redox in gas by the ozone generator 7:
NH3+O3=N2+O2+H2O；It is discharged after so that ammonia is converted into innocuous gas.
The front end of the air blower is equipped with anemobiagraph 11, can carry out wind speed according to the different specific weight and property of different material
Adjusting.
The conveying mechanism is conveying belt conveyor 15, and the front end of the conveying mechanism is connected with weighing belt 12, and passes through
Material is sent into the feed inlet of drying tube 1 by weighing belt 12, and weighing belt 12 adjusts the transmission speed of belt, and then adjusts unit
Inlet amount in time is provided with current controller on air blower, to adjust air inlet size, so that temperature is controlled, it is described
Firsts and seconds cyclone separator be equipped with vibration motor, situations such as to prevent feed blocking, wall built-up.
Finally, it should be noted that the above various embodiments is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should
Understand: it is still possible to modify the technical solutions described in the foregoing embodiments, or to some or all of
Technical characteristic is equivalently replaced；And these are modified or replaceed, it does not separate the essence of the corresponding technical solution, and this is practical new
The range of each embodiment technical solution of type, should all cover in the claim of the utility model and the range of specification.
Claims (8)
1. a kind of pneumatic conveying dryer including front conveying mechanism, the drying tube being connected with conveying mechanism (1) and is connected to drying
Manage the processing unit at (1) rear portion, it is characterised in that: the output end of the conveying mechanism is connected at the feed inlet of drying tube (1),
It is connected with hot wind conveying mechanism below drying tube (1) feed inlet, the hot wind conveying mechanism includes sequentially connected air
Filter (2), air blower (3) and vapor heat exchanger (4), the air outlet of the vapor heat exchanger (4) are communicated to below feed inlet
Drying tube (1) in, the processing unit include sequentially connected primary cyclone (5), deduster (6), ozone occur
Device (7), secondary cyclone (8) and rewinding blower (9), feed end and drying tube (1) of the primary cyclone (5)
Discharge end be connected.
2. a kind of pneumatic conveying dryer according to claim 1, it is characterised in that: the internal diameter thickness of the drying tube (1)
Checker, the interior spinning disk (10) for being equipped with helically type curve of drying tube (1), the spinning disk (10) is around drying tube
(1) inner wall is arranged, and spinning disk (10) lateral wall is fixed on drying tube (1).
3. a kind of pneumatic conveying dryer according to claim 2, it is characterised in that: the drying tube (1) is inverted u-shaped to be set
It sets, the spinning disk (10) is mounted in the second half of drying tube (1).
4. a kind of pneumatic conveying dryer according to claim 2, it is characterised in that: the primary cyclone (5) with
Cooled dehumidifier unit (13) is connected, and the air outlet of the cooled dehumidifier unit (13) is connected to primary cyclone (5) feed inlet
At blanking.
5. a kind of pneumatic conveying dryer according to claim 4, it is characterised in that: the deduster (6) is water film dedusting
Device.
6. a kind of pneumatic conveying dryer according to claim 5, it is characterised in that: the ozone generator (7) is by gas
In ammonia redox, be discharged after so that ammonia is converted into innocuous gas.
7. a kind of pneumatic conveying dryer according to claim 1, it is characterised in that: the front end of the air blower is equipped with wind
Fast instrument (11).
8. a kind of pneumatic conveying dryer according to claim 1, it is characterised in that: the conveying mechanism is conveyer belt transmission
The front end of machine, the conveying mechanism is connected with weighing belt (12), and by weighing belt (12) by material be sent into drying tube (1) into
In material mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822268618.2U CN209623315U (en) | 2018-12-29 | 2018-12-29 | A kind of pneumatic conveying dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822268618.2U CN209623315U (en) | 2018-12-29 | 2018-12-29 | A kind of pneumatic conveying dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209623315U true CN209623315U (en) | 2019-11-12 |
Family
ID=68448410
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822268618.2U Active CN209623315U (en) | 2018-12-29 | 2018-12-29 | A kind of pneumatic conveying dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209623315U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112641117A (en) * | 2020-12-28 | 2021-04-13 | 齐鲁工业大学 | Continuous cyclone drying equipment for small berries |
-
2018
- 2018-12-29 CN CN201822268618.2U patent/CN209623315U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112641117A (en) * | 2020-12-28 | 2021-04-13 | 齐鲁工业大学 | Continuous cyclone drying equipment for small berries |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104722094B (en) | Recirculating fluidized bed spray drying device | |
| CN207214663U (en) | A kind of dry dust removal device of titanium dioxide | |
| CN203964589U (en) | Granule materials drying machine | |
| CN205403417U (en) | Calcium hypochlorite flash drying equipment | |
| CN104110941B (en) | The ciculation fluidized bed drying method of partial tail gas and equipment | |
| CN205175001U (en) | Air -flowing type for dry system | |
| CN205825587U (en) | A kind of Novel drying device | |
| CN208124832U (en) | A kind of plastic grain dryer for mesh pocket production | |
| CN104930832B (en) | Twin-roll crops drier | |
| CN107976054A (en) | A kind of hydroresorcinol closed cycle two-stage drying means and drying device | |
| CN209623315U (en) | A kind of pneumatic conveying dryer | |
| US3720253A (en) | Egg white spray drying apparatus and method | |
| CN104880029A (en) | Closed-cycle fluidized bed equipment and application method thereof | |
| CN104738158A (en) | Grain-drying dust collector | |
| CN203534103U (en) | Pneumatic drying device | |
| CN208254072U (en) | A kind of new polyester chip drying device | |
| CN204730608U (en) | A kind of drying and crushing classification integral type superfine powder treating apparatus | |
| CN206056225U (en) | A kind of flash dryer circulation of tail gas application system | |
| CN205425745U (en) | Rotatory flash distillation sack dust removal desiccator of pesticide | |
| CN107655311B (en) | The drying device and method of haloflex | |
| CN208282533U (en) | Powder dries subpackage apparatus | |
| CN103808108B (en) | The low temperature drying method of low-melting-point resin | |
| CN104880031A (en) | Closed-circulation fluidized-bed equipment with continuous discharge function and method for applying closed-circulation fluidized-bed equipment | |
| CN107816844A (en) | Internal heat type fluidized bed dryer | |
| CN208635532U (en) | Activated carbon raw material drying equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 421500 Xinyuan Road, Shuikoushan Economic Development Zone, Changning City, Hengyang City, Hunan Province Patentee after: Hunan Debang Biotechnology Co.,Ltd. Address before: 421000 68 Daqiao Road, Shuikoushan Town, Changning City, Hengyang City, Hunan Province Patentee before: CHANGNING DEBANG BIOTECHNOLOGY Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Airflow drying equipment Effective date of registration: 20220307 Granted publication date: 20191112 Pledgee: Hengyang Branch of China Everbright Bank Co.,Ltd. Pledgor: Hunan Debang Biotechnology Co.,Ltd. Registration number: Y2022430000016 |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 421500 Xinyuan Road, Shuikoushan Economic Development Zone, Changning City, Hengyang City, Hunan Province Patentee after: Hunan Debang Biotechnology Co.,Ltd. Address before: 421500 Xinyuan Road, Shuikoushan Economic Development Zone, Changning City, Hengyang City, Hunan Province Patentee before: Hunan Debang Biotechnology Co.,Ltd. |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230511 Granted publication date: 20191112 Pledgee: Hengyang Branch of China Everbright Bank Co.,Ltd. Pledgor: Hunan Debang Biotechnology Co.,Ltd. Registration number: Y2022430000016 |