CN205549624U - Novel spray drier - Google Patents

Novel spray drier Download PDF

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Publication number
CN205549624U
CN205549624U CN201620404704.XU CN201620404704U CN205549624U CN 205549624 U CN205549624 U CN 205549624U CN 201620404704 U CN201620404704 U CN 201620404704U CN 205549624 U CN205549624 U CN 205549624U
Authority
CN
China
Prior art keywords
wall
drying tower
pipe
return pipe
air
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
Application number
CN201620404704.XU
Other languages
Chinese (zh)
Inventor
李节良
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xiayi County Yu Hao Additives LLC
Original Assignee
Xiayi County Yu Hao Additives LLC
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xiayi County Yu Hao Additives LLC filed Critical Xiayi County Yu Hao Additives LLC
Priority to CN201620404704.XU priority Critical patent/CN205549624U/en
Application granted granted Critical
Publication of CN205549624U publication Critical patent/CN205549624U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model provides a novel spray drier has effectually solved the problem that the material glues the wall among the dry run, the utility model discloses a drying tower, a serial communication port, the drying tower top is equipped with the centrifugal atomizer, inlet pipe and air -supply line are connected to the centrifugal atomizer, the drying tower includes inner wall and outer wall, be equipped with ventilation layer between inner wall and the outer wall, the inner wall is mobilizable soft materials, the inboard drying chamber that is of inner wall, the drying chamber intercommunication has cyclone, the cyclone lower extreme is equipped with the discharge gate, loop in through other return pipe intercommunication in cyclone one side, install first check valve on the other return pipe, constitute the structure that other return pipe can only be looped in to a direction, cyclone's air outlet communicates ventilation layer through the ventilation pipe, install second check valve and force pump on the ventilation pipe, ventilation layer connects the dust remover, the utility model discloses simple structure, the cyclic utilization energy, and reduce the input of equipment, the emergence of can very big reduction gluing the wall for the drying of material more thoroughly, the effect is better.

Description

Novel atomizing drying machine
Technical field
This utility model relates to chemical industry technique with the apparatus field, particularly relates to a kind of novel atomizing drying machine.
Background technology
In the production process of auxiliary chemicals, finally need be dried by auxiliary agent and make granular structure, at this time need to use to process to spray dryer, and spray dryer is susceptible to the situation of viscous wall, drying tower wall is persistently blown by conventional processing mode for using air jet pipe, make material will not be bonded in Ta Bishang, but this mode needs an extra aerator, consume too much resource, and the drying regime in persistently air blowing influences whether drying tower, the crystallization to material has certain negative effect.
Utility model content
For above-mentioned situation, for overcoming the defect of prior art, the purpose of this utility model is just to provide a kind of novel atomizing drying machine, effectively solves the problem that in dry run, material glues wall.
Its technical scheme solved is, this utility model includes drying tower, it is characterized in that, drying tower top is provided with centrifugal atomizer, centrifugal atomizer connects feed pipe and blast pipe, drying tower includes inner and outer wall, ventilating layer it is provided with between inner and outer wall, inwall is mobilizable soft material, inner wall is hothouse, hothouse is communicated with cyclone separator, cyclone separator lower end is provided with discharging opening, cyclone separator side forms loop through other return pipe connection, on other return pipe, the first check valve is installed, constituting other return pipe can only be to the structure in formation loop, a direction, the air outlet of cyclone separator connects ventilating layer through ventilation duct, second check valve and compression pump are installed on ventilation duct, ventilating layer connects cleaner unit.
This utility model simple in construction, recycling energy, and reduce the input of equipment, the generation of viscous wall can be significantly reduced so that being dried of material is more thorough, better.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in further detail.
nullBe given by Fig. 1,This utility model includes drying tower,It is characterized in that,Drying tower top is provided with centrifugal atomizer 5,Centrifugal atomizer 5 connects feed pipe 7 and blast pipe 8,Drying tower includes inwall 2 and outer wall 1,Ventilating layer 3 it is provided with between inwall 2 and outer wall 1,Inwall 2 is mobilizable soft material,It it is hothouse 4 inside inwall 2,Hothouse 4 is communicated with cyclone separator 17,Cyclone separator 17 lower end is provided with discharging opening 20,Cyclone separator 17 side forms loop through other return pipe 18 connection,On other return pipe 18, first check valve 19 is installed,Constituting other return pipe 18 can only be to the structure in formation loop, a direction,The air outlet of cyclone separator 17 connects ventilating layer 3 through ventilation duct 14,Second check valve 16 and the first compression pump 15 is installed on ventilation duct 14,Ventilating layer 3 connects cleaner unit 21.
Filter 10 and the second compression pump 9 it is sequentially provided with on described feed pipe 7.
Air filter 13, aerator 12 and heater 11 it is sequentially provided with on described blast pipe 8.
Multiple shower nozzle 6 it is provided with below described centrifugal atomizer 5.
Described drying tower lower end is provided with discharge gate 23.
Air-introduced machine 22 it is provided with between described drying tower and cleaner unit 21.
This utility model in use,
nullFeed pipe 7 connects storage tank,Blast pipe 8 connects outside air,It is then turn on device power supply (DPS),Start working,The material of liquid enters in centrifugal atomizer 5 through filter 10 and the second compression pump 9,Effect through centrifugal atomizer 5,The material of liquid is formed fine spray be injected in hothouse 4,Outside air under the effect of aerator 12 through air filter 13 and the effect of heater 11,The gas forming high temperature and high speed moves downward in hothouse 4 with spraying,Owing to spraying increases the contact area with air,High temperature air is easy to evaporate totally the moisture in material,Dried material is discharged from discharge gate 23,Air with molecule material enters in cyclone separator 17 from the side of hothouse 4,In the separation through cyclone separator 17,Fine particle thing in air is separated from air,Discharge from discharging opening 20,Remaining air turns again in cyclone separator 17 from other return pipe 18,Through secondary separation,The material particles in air is made to be totally separated out,Air then enters ventilation duct 14,Under the effect of the first compression pump 15,Change air pressure,Enter in ventilating layer 3,Owing to hothouse 4 is different with the atmospheric pressure in ventilating layer 3,Inwall 2 can produce different shapes according to the difference of both sides pressure,The pressure of the first compression pump 15 is continually changing,The shape of inwall 2 the most constantly changes,So that inwall is continuously in motion,Material particles in hothouse 4 is difficult to be attached on inwall 2,Play the effect of antiseized wall.
Air in ventilating layer 3 enters in dust removal machine 21 under the effect of air-introduced machine 22, the dust in air and the material particles that cannot separate is separated with air, is discharged in air by clean air, does not results in the pollution of air.
This utility model is compared to traditional spray dryer, it is double-deck that hothouse is divided into inner and outer wall, ventilating layer is set between the inner walls and the outer, inwall takes soft mobilizable material, by changing the pressure differential between ventilating layer and hothouse, inwall is in constantly vibration, avoid the attachment of particulate matter, and in traditional drying tower, must be equipped with gas sweeping device, and gas sweeping device is set in drying tower and easily makes particulate matter be attached on gas sweeping device, and easily have influence on dry process, and this utility model is not added with any equipment in hothouse, dry run is the most at all affected, the effect of antiseized wall can be played again.
This utility model simple in construction, recycling energy, and reduce the input of equipment, the generation of viscous wall can be significantly reduced so that being dried of material is more thorough, better.

Claims (6)

  1. null1. a novel atomizing drying machine,Including drying tower,It is characterized in that,Drying tower top is provided with centrifugal atomizer (5),Centrifugal atomizer (5) connects feed pipe (7) and blast pipe (8),Drying tower includes inwall (2) and outer wall (1),Ventilating layer (3) it is provided with between inwall (2) and outer wall (1),Inwall (2) is mobilizable soft material,Inwall (2) inner side is hothouse (4),Hothouse (4) is communicated with cyclone separator (17),Cyclone separator (17) lower end is provided with discharging opening (20),Cyclone separator (17) side forms loop through other return pipe (18) connection,On other return pipe (18), the first check valve (19) is installed,Constituting other return pipe (18) can only be to the structure in formation loop, a direction,The air outlet of cyclone separator (17) is through ventilation duct (14) connection ventilating layer (3),Second check valve (16) and the first compression pump (15) are installed on ventilation duct (14),Ventilating layer (3) connects cleaner unit (21).
  2. Novel atomizing drying machine the most according to claim 1, it is characterised in that be sequentially provided with filter (10) and the second compression pump (9) on described feed pipe (7).
  3. Novel atomizing drying machine the most according to claim 1, it is characterised in that be sequentially provided with air filter (13), aerator (12) and heater (11) on described blast pipe (8).
  4. Novel atomizing drying machine the most according to claim 1, it is characterised in that described centrifugal atomizer (5) lower section is provided with multiple shower nozzle (6).
  5. Novel atomizing drying machine the most according to claim 1, it is characterised in that described drying tower lower end is provided with discharge gate (23).
  6. Novel atomizing drying machine the most according to claim 1, it is characterised in that be provided with air-introduced machine (22) between described drying tower and cleaner unit (21).
CN201620404704.XU 2016-05-08 2016-05-08 Novel spray drier Expired - Fee Related CN205549624U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620404704.XU CN205549624U (en) 2016-05-08 2016-05-08 Novel spray drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620404704.XU CN205549624U (en) 2016-05-08 2016-05-08 Novel spray drier

Publications (1)

Publication Number Publication Date
CN205549624U true CN205549624U (en) 2016-09-07

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620404704.XU Expired - Fee Related CN205549624U (en) 2016-05-08 2016-05-08 Novel spray drier

Country Status (1)

Country Link
CN (1) CN205549624U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111071643A (en) * 2019-12-28 2020-04-28 甘肃省敦煌种业果蔬制品有限公司 Tomato ketchup preheats storage jar
CN111841047A (en) * 2019-04-26 2020-10-30 宁德时代新能源科技股份有限公司 Negative electrode material production equipment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111841047A (en) * 2019-04-26 2020-10-30 宁德时代新能源科技股份有限公司 Negative electrode material production equipment
CN111841047B (en) * 2019-04-26 2023-07-14 宁德时代新能源科技股份有限公司 Negative electrode material production equipment
CN111071643A (en) * 2019-12-28 2020-04-28 甘肃省敦煌种业果蔬制品有限公司 Tomato ketchup preheats storage jar

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160907

Termination date: 20170508

CF01 Termination of patent right due to non-payment of annual fee