CN102993444B - Atomization tower - Google Patents

Atomization tower Download PDF

Info

Publication number
CN102993444B
CN102993444B CN201110265742.3A CN201110265742A CN102993444B CN 102993444 B CN102993444 B CN 102993444B CN 201110265742 A CN201110265742 A CN 201110265742A CN 102993444 B CN102993444 B CN 102993444B
Authority
CN
China
Prior art keywords
spray chamber
high pressure
auxiliary material
atomization
pipe
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
CN201110265742.3A
Other languages
Chinese (zh)
Other versions
CN102993444A (en
Inventor
刘明秋
张吉太
邹开良
周德胜
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.)
BEIJING ZHONGSHIHONG INSTALLATION ENGINEERING CO., LTD.
Original Assignee
JIANGSU GUOZHENG NEW MATERIAL TECHNOLOGY Co Ltd
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 JIANGSU GUOZHENG NEW MATERIAL TECHNOLOGY Co Ltd filed Critical JIANGSU GUOZHENG NEW MATERIAL TECHNOLOGY Co Ltd
Priority to CN201110265742.3A priority Critical patent/CN102993444B/en
Publication of CN102993444A publication Critical patent/CN102993444A/en
Application granted granted Critical
Publication of CN102993444B publication Critical patent/CN102993444B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Nozzles (AREA)

Abstract

The invention discloses an atomization tower comprising an atomization chamber (1). A hot wind inlet (2) and a discharging port (3) are respectively arranged on the top end and the bottom end of the atomization chamber (1). The hot wind inlet (2) is connected with a hot blast stove (5) through a pipe (4). A high-pressure nozzle (6) is arranged in the atomization chamber (1). An atomization baffle (7) is arranged on the spray side of the high-pressure nozzle (6). A feeding side of the high-pressure nozzle (6) is connected with a booster pump (9) on the outer side of the atomization chamber (1) through a feeing pipe (8). The booster pump (9) is sequentially connected with a static mixer (10) and a main material supply device (11) through the feeding pipe (8). An auxiliary material inlet (12) is arranged on the side wall on the lower part of the atomization chamber (1). The auxiliary material inlet (12) is connected with an auxiliary material supply device (13) through the feeding pipe (8). With the atomization tower provided by the invention, high-polymer substances can be gradually subjected to high-temperature poly-condensation, and a product satisfies the requirements of conductive materials. The product has adjustable volume and high uniformity. The atomization tower provided by the invention is suitable to be popularized.

Description

Atomisation tower
Technical field
The present invention relates to a kind of atomisation unit, especially fluent meterial is become to the atomisation tower of vaporific particulate.
Background technology
Existing atomisation unit adopts the mode of interior burning to carry out atomization to raw material substantially, the atomizing pressure of this atomisation unit is low, and the fluid viscosity of carrying is little, atomization product cut size is out larger, and raw material undergoes phase transition and makes the product obtaining can only be used for doing carbon black after high-temp combustion, do not reach the ingredient requirement of electro-conductive material, therefore can not be used as electro-conductive material.
Summary of the invention
The object of the invention is the defect for prior art, provide a kind of simple in structure, atomizing effect good and product can be used as the spraying gun of electro-conductive material.
The object of the invention is to solve by the following technical programs:
A kind of atomisation tower, comprise spray chamber, the top of described spray chamber and bottom are respectively equipped with hot blast import and discharge port, hot blast import is connected with hotblast stove by pipeline, in described spray chamber, be provided with high pressure spray nozzle, the ejection side of high pressure spray nozzle is provided with the baffle plate that hazes, and the feeding side of high pressure spray nozzle is connected with the topping-up pump in spray chamber outside by feed-pipe, and topping-up pump is connected with major ingredient loader with static mixer successively by feed-pipe; The lower sides of described spray chamber is provided with auxiliary material import, and auxiliary material import is connected with auxiliary material feeding device by feed-pipe.
In described spray chamber, be provided with the high pressure spray nozzle being oppositely arranged up and down.
The downside of the high pressure spray nozzle of described spray chamber internal upper part setting is provided with the baffle plate that hazes; The upside of the high pressure spray nozzle that in described spray chamber, bottom arranges is provided with the baffle plate that hazes.
Described major ingredient loader is high pressure loader.
Described auxiliary material feeding device is high pressure loader.
The bottom of described spray chamber is back taper.
Described auxiliary material import is positioned on the tapered sidewalls of spray chamber bottom.
Described discharge port is positioned on the vertex of a cone of spray chamber bottom.
The present invention has the following advantages compared to existing technology:
Atomisation tower of the present invention can make superpolymer high-temperature polycondensation progressively in atomisation tower, can form the curing dispersion homogeneous phase particle that meets electro-conductive material demand.
The present invention, by the fluent meterial of High Temperature High Pressure is squeezed into high pressure spray nozzle with increase pump, is then ejected into fluent meterial to haze on baffle plate, atomization produce granular size adjustable, uniformity coefficient is high, power consumption is low.
The present invention is simple in structure, esy to use, safe and reliable, and low cost of manufacture, and use range is wide, suitable promoting the use of.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present invention.
Wherein: 1-spray chamber; The import of 2-hot blast; 3-discharge port; 4-pipeline; 5-hotblast stove; 6-high pressure spray nozzle; 7-baffle plate hazes; 8-feed-pipe; 9-topping-up pump; 10-static mixer; 11-major ingredient loader; The import of 12-auxiliary material; 13-auxiliary material feeding device.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the present invention is further illustrated.
As shown in Figure 1: a kind of atomisation tower, comprise spray chamber 1, the bottom of spray chamber 1 is back taper, and is provided with auxiliary material import 12 on the tapered sidewalls of spray chamber 1 bottom, and auxiliary material import 12 is connected with auxiliary material feeding device 13 by feed-pipe 8; Top and bottom at spray chamber 1 are respectively equipped with hot blast import 2 and discharge port 3, and discharge port 3 is positioned on the vertex of a cone of spray chamber 1 bottom, and hot blast import 2 is connected with hotblast stove 5 by pipeline 4.In spray chamber 1, be provided with the high pressure spray nozzle 6 being oppositely arranged up and down, the ejection side of high pressure spray nozzle 6 is provided with the baffle plate 7 that hazes, and wherein the downside of the high pressure spray nozzle 6 of spray chamber 1 internal upper part setting is provided with the baffle plate 7 that hazes; The upside of the high pressure spray nozzle 6 that the interior bottom of spray chamber 1 arranges is provided with the baffle plate 7 that hazes.Feeding side at high pressure spray nozzle 6 is connected with the topping-up pump 9 in spray chamber 1 outside by feed-pipe 8, and topping-up pump 9 is connected with major ingredient loader 11 with static mixer 10 successively by feed-pipe 8.Major ingredient loader 11 and auxiliary material feeding device 13 all adopt high pressure loader in addition.
The present invention in use, the material of modulating through high temperature is from the full and uniform mixing of the major ingredient loader 11 process static mixers 10 of high pressure, under the effect by topping-up pump 9, being input to high pressure spray nozzle 6 by feed-pipe 8 sprays, the material that high pressure spray nozzle 6 sprays is ejected into and hazes on baffle plate 7, produces droplet of uniform size.In the time of needs inert gas environment or other auxiliary material, auxiliary material feeding device 13 arrives supplementary material spray in spray chamber 1, for the atomization of major ingredient provides condition through auxiliary material import 12.In addition under normal circumstances, in the time need to obtaining the larger atomizing particle of diameter, the high pressure spray nozzle 6 that material arranges from spray chamber 1 bottom ejects; In the time need to obtaining the less atomizing particle of diameter, the high pressure spray nozzle 6 that material arranges from spray chamber 1 top ejects.Atomisation tower of the present invention can make superpolymer high-temperature polycondensation progressively in atomisation tower, can form the curing dispersion homogeneous phase particle that meets electro-conductive material demand, and its size is adjustable, uniformity coefficient is high, power consumption is low, and there is feature simple in structure, easy to use, cost is low, its use range is wide, suitable promoting the use of.
The technology that the present invention does not relate to all can be realized by prior art.

Claims (8)

1. an atomisation tower, comprise spray chamber (1), the bottom that the top that it is characterized in that described spray chamber (1) is provided with hot blast import (2) and spray chamber (1) is provided with discharge port (3), hot blast import (2) is connected with hotblast stove (5) by pipeline (4), in described spray chamber (1), be provided with high pressure spray nozzle (6), the ejection side of high pressure spray nozzle (6) is provided with the baffle plate that hazes (7), the feeding side of high pressure spray nozzle (6) is connected with the topping-up pump (9) in spray chamber (1) outside by feed-pipe (8), topping-up pump (9) is connected with major ingredient loader (11) with static mixer (10) successively by feed-pipe (8), the lower sides of described spray chamber (1) is provided with auxiliary material import (12), and auxiliary material import (12) is connected with auxiliary material feeding device (13) by feed-pipe (8).
2. atomisation tower according to claim 1, is characterized in that being provided with the high pressure spray nozzle (6) being oppositely arranged up and down in described spray chamber (1).
3. atomisation tower according to claim 2, is characterized in that the downside of the high pressure spray nozzle (6) of described spray chamber (1) internal upper part setting is provided with the baffle plate that hazes (7); The upside of the high pressure spray nozzle (6) that the interior bottom of described spray chamber (1) arranges is provided with the baffle plate that hazes (7).
4. atomisation tower according to claim 1, is characterized in that described major ingredient loader (11) is high pressure loader.
5. atomisation tower according to claim 1, is characterized in that described auxiliary material feeding device (13) is high pressure loader.
6. atomisation tower according to claim 1, is characterized in that the bottom of described spray chamber (1) is back taper.
7. atomisation tower according to claim 6, is characterized in that described auxiliary material import (12) is positioned on the tapered sidewalls of spray chamber (1) bottom.
8. atomisation tower according to claim 6, is characterized in that described discharge port (3) is positioned on the vertex of a cone of spray chamber (1) bottom.
CN201110265742.3A 2011-09-08 2011-09-08 Atomization tower Expired - Fee Related CN102993444B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201110265742.3A CN102993444B (en) 2011-09-08 2011-09-08 Atomization tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201110265742.3A CN102993444B (en) 2011-09-08 2011-09-08 Atomization tower

Publications (2)

Publication Number Publication Date
CN102993444A CN102993444A (en) 2013-03-27
CN102993444B true CN102993444B (en) 2014-11-05

Family

ID=47922595

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201110265742.3A Expired - Fee Related CN102993444B (en) 2011-09-08 2011-09-08 Atomization tower

Country Status (1)

Country Link
CN (1) CN102993444B (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2602454B2 (en) * 1976-01-23 1980-12-11 Claudius Peters Ag, 2000 Hamburg Device for treating powdery or granular substances with a liquid

Also Published As

Publication number Publication date
CN102993444A (en) 2013-03-27

Similar Documents

Publication Publication Date Title
CN101979940B (en) Spray drying tower for preparing powder
CN203162943U (en) Efficient fuel oil atomization nozzle
CN205155947U (en) Fuel atomizing rifle of combustor
CN102993444B (en) Atomization tower
CN105126277B (en) A kind of big flow compressed-air foam mixing arrangement
CN201665639U (en) Sensitizer spraying injection device
CN202224121U (en) Atomizing tower
CN102865575A (en) Micro-explosion atomization oil gun
CN208010436U (en) A kind of carbamide granulation blowoff
CN201382416Y (en) Double-layered directional air atomizing oil gun
CN201676801U (en) High evenness oil spraying device
CN207722393U (en) A kind of latex powder spray drying tower
CN102311826B (en) Carbon baking furnace alternative fuel and equipment
CN101403499B (en) Double-Y shaped fuel treble atomizing method and atomizer
CN104611066B (en) Gasifier nozzle
CN104498533A (en) Method for preparing ethyl alcohol
CN202328229U (en) Fuel nozzle device for combustor
CN220169929U (en) Novel rotary kiln ignition fuel-saving device
CN207688123U (en) A kind of secondary air atomizing fuel nozzle
CN208205007U (en) A kind of gas-liquid combustible combustion device
CN206587942U (en) A kind of shower nozzle with good atomizing effect
CN202730025U (en) Compound fertilizer anti-blocking spray head
CN201684681U (en) High-pressure vortex nozzle
CN205042137U (en) A atomizer for spray drier
CN105484919B (en) A kind of micro-disturbance extends out the atomizer of type spray orifice

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: BEIJING ZHONGSHIHONG INSTALLATION ENGINEERING CO.,

Free format text: FORMER OWNER: JIANGSU GUOZHENG NEW MATERIAL TECHNOLOGY CO., LTD.

Effective date: 20141126

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20141126

Address after: Xinjiezhen Zhenxin West Road Yixing Jiangsu province 214204 city of Wuxi City, No. 6-8

Patentee after: BEIJING ZHONGSHIHONG INSTALLATION ENGINEERING CO., LTD.

Address before: Xinjiezhen Zhenxin West Road Yixing Jiangsu province 214204 city of Wuxi City, No. 6-8

Patentee before: Jiangsu Guozheng New Material Technology Co., Ltd.

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

Granted publication date: 20141105

Termination date: 20180908

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