CN105571302B - A kind of spray drying tower hot air distribution device - Google Patents

A kind of spray drying tower hot air distribution device Download PDF

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Publication number
CN105571302B
CN105571302B CN201610050398.9A CN201610050398A CN105571302B CN 105571302 B CN105571302 B CN 105571302B CN 201610050398 A CN201610050398 A CN 201610050398A CN 105571302 B CN105571302 B CN 105571302B
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CN
China
Prior art keywords
platform shape
taper platform
inversed taper
air
shape housing
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CN201610050398.9A
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Chinese (zh)
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CN105571302A (en
Inventor
贾绍广
马双忱
李智
张润盘
赵晓利
孟金波
江天亮
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China Electric Power Construction Group Hebei electric survey and Design Research Institute Co., Ltd.
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Hebei Electric Power Design and Research Institute
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Priority to CN201610050398.9A priority Critical patent/CN105571302B/en
Publication of CN105571302A publication Critical patent/CN105571302A/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/004Nozzle assemblies; Air knives; Air distributors; Blow boxes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The present invention relates to a kind of hot air distribution device, specifically a kind of spray drying tower hot air distribution device, belong to technical field of drying.The hot air distribution device includes three inversed taper platform shape housings being set with one heart, and three inversed taper platform shape housings are connected by top cover;Outside inversed taper platform shape housing upper is partitioned into air intake spiral case by cylinder, and some blast pipe connection air intake spiral cases and the air channel being made up of outside inversed taper platform shape housing and middle part inversed taper platform shape housing are uniformly arranged on cylinder;Deflector is uniformly arranged on the bottom of the outer wall of middle part inversed taper platform shape housing;It is mounted with that the inside inversed taper platform shape housing of centrifugal atomizer is located at middle part inversed taper platform shape enclosure interior;The air intake spiral case is connected with external air channel.It is more uniform that the present invention can be such that hot-air is distributed when entering drying tower, can control the distribution of droplet group, hot-air and the full and uniform combination drying of droplet, avoids the generation of glutinous wall, glutinous top phenomenon to greatest extent.

Description

A kind of spray drying tower hot air distribution device
Technical field
The present invention relates to a kind of hot air distribution device, specifically a kind of spray drying tower hot air distribution device, belong to dry Dry technical field.
Background technology
The application field of dry technology was more and more extensive in recent years, in addition to traditional food, medicine and other fields, environmental protection Also applied in field.With the aggravation of environmental pollution, environmental standard is strict all the more, and national requirements coal-burning power plant is to desulfurization wastewater Deng progress zero discharge treatment, there is scholar's research to set up the evaporation process that single drying tower carries out desulfurization wastewater.The method requirement The part heat smoke introduced before air preheater, fully contact being evaporated with desulfurization wastewater, evaporation product is trapped by electrostatic precipitator.
Generally, hot blast is needed after hot air distribution device is uniformly distributed, and could enter spray drying tower.Hot blast The effect of distributor is uniformly to provide the heat required for range drying, controls route that droplet and particle are passed through and quick Ground is removed by the moisture of evaporation from range of atomization.
In use, the problem of hot blast skewness, air outlet be present with hot air distribution device in existing drying tower Hot blast speed and direction are bad, cause material uniformly to be mixed with hot blast, the problems such as so as to cause to dry insufficient or viscous wall
The content of the invention
The technical problem to be solved in the invention is to provide a kind of spraying simple in construction, that hot blast can be made to be evenly distributed and done Dry tower hot air distribution device.
In order to solve the above technical problems, the technical solution adopted in the present invention is:
A kind of spray drying tower hot air distribution device, including three inversed taper platform shape housings being set with one heart, three inversed taper platforms Shape housing is connected by top cover;Outside inversed taper platform shape housing upper is partitioned into air intake spiral case by cylinder, is uniformly set on cylinder Put some blast pipe connection air intake spiral cases and the air channel being made up of outside inversed taper platform shape housing and middle part inversed taper platform shape housing;Water conservancy diversion Plate is uniformly arranged on the bottom of the outer wall of middle part inversed taper platform shape housing;The inside inversed taper platform shape housing of installation centrifugal atomizer is located at Middle part inversed taper platform shape enclosure interior;The air intake spiral case is connected with external air channel.
Further, the air inlet end of the blast pipe and air opening end are hypotenuse, the hypotenuse of air inlet end during installation Face hot wind flow direction, air outlet are inclined to the bottom in air channel.
Further, the air intake spiral case and external air channel are tangent in junction.
Further, the regulating gate of control intake is set in the middle part of the blast pipe.
Further, described deflector one end sets an auricle, and deflector is screwed on middle part by auricle and fallen On the outer wall of frustum shell, the adjustable angle of deflector and vertical direction.
Further, three inversed taper platform shape housing male cone (strobilus masculinus) tapers are identical.
By adopting the above-described technical solution, the technological progress that the present invention obtains is:
Hot blast is incorporated into air channel by some blast pipes in the present invention, passes through blast pipe and the tune of blast pipe upper lock gate Section so that air intake is uniformly and downward spiral flows.
Present invention improves over deflector structure, is improved to the deflector of adjustable angle, can control into hot blast and enter drying The angle of tower, so as to control the distribution characteristics of droplet group, prevent the generation of wall sticking phenomenon.
Air intake spiral case is changed to cross-sectional area equal air channel everywhere in the present invention, so can ensure air intake spiral case everywhere Blast is equal, and hot blast is more uniform when entering air channel by blast pipe.
External air channel and the tangent connection of air intake spiral case, can make hot blast tangentially enter air intake spiral case, so as to protect in the present invention Demonstrate,proving hot blast has higher wind speed and the unification of hot wind flow direction.
Brief description of the drawings
Fig. 1 is the schematic front view of the present invention;
Fig. 2 is deflector scheme of installation of the present invention;
Fig. 3 is blast pipe structural representation of the present invention;
Fig. 4 is deflector front view of the present invention;
Fig. 5 is deflector top view of the present invention;
Wherein, 1 be blast pipe, 2 be regulating gate, 3 be air intake spiral case, 4 be outside inversed taper platform shape housing, 5 be middle part fall Frustum shell, 6 be internal inversed taper platform shape housing, 7 be deflector, 8 be centrifugal atomizer, 9 be auricle, 10 be external air channel, 11 it is air channel, 12 be cylinder, 13 is top cover.
Embodiment
The present invention is described in further details with reference to embodiment:
As shown in figure 1, the present invention includes three inversed taper platform shape housings being set with one heart, three inversed taper platform shape housings are used Top cover 13 is connected;Air intake spiral case 3 is partitioned into by cylinder 12 on the outside top of inversed taper platform shape housing 4, and on cylinder 12 uniformly The blast pipe 1 of some adjusting air inlet amounts is installed, blast pipe 1 is connected air intake spiral case 3 and by outside inversed taper platform shape housing 4 with The air channel 11 that portion's inversed taper platform shape housing 5 forms;Deflector 7 is uniformly arranged on to the bottom of the outer wall of middle part inversed taper platform shape housing 4; The inside inversed taper platform shape housing 6 for being provided with centrifugal atomizer 8 is arranged in middle part inversed taper platform shape housing 5;External air channel 10 with Air intake spiral case 3 is connected, in order that outside hot blast can keep very fast wind speed even into the hot air distribution device, external air channel 10 is tangent in junction with air intake spiral case 3, and hot blast tangentially enters air intake spiral case 3, as shown in Figure 2.
The mode that hot blast is entered to hot air distribution device in the present invention is improved, some using being installed on cylinder 12 The mode of blast pipe 1, connection air intake spiral case 3 and air channel 11.The structure of blast pipe 1 is as shown in figure 3, air inlet end and air opening end Hypotenuse is processed into, makes the direction of the hypotenuse face hot wind flow of air intake when mounted, blast pipe 1 is in tilted layout and makes air outlet The bottom in air channel 11 is inclined to, is arranged so as to that hot blast can be made helically to flow downwards in air channel 11.In order to better control over into Air quantity has installed regulating gate 2 additional on blast pipe 1, and regulating gate 2 is controlled using long distance electricization.It can be controlled using above-mentioned design The air quantity of heating wind makes hot blast distribution more uniformly flow downward in the shape of a spiral.Air intake spiral case 3 in present invention cross section everywhere Product is identical, can ensure that air pressure is identical everywhere during use, hot blast is entered outside inversed taper platform shape housing 4 and middle part inversed taper platform shape shell It is more uniform and stable during the air channel 11 that body 5 surrounds.
The present invention is improved the structure and mounting means of deflector 7, and one is provided with one end of deflector 7 admittedly Surely the auricle 9 connected, concrete structure is as shown in Figure 4, Figure 5.Deflector 7 is screwed in middle part inversed taper platform by auricle 9 On the outer wall of shape housing 5 and angle is adjusted, the angle of deflector 7 and vertical direction can adjust as needed, so can be with Wind speed and rotation mist square size are suitable when the hot blast is entered drying tower by the bottom in air channel 11, it is ensured that droplet even drop down is simultaneously Fully dry.
The present invention is arranged on to the top of spray drying tower during use, external air channel 10 is connected with air intake spiral case 3, will Desulfurization wastewater introduces centrifugal atomizer 8, and drying tower is entered after atomizing.Hot blast is from external air channel 10 tangentially into hot blast point With device, by the distribution of hot air distribution device, hot blast can be made equably spirally to be entered by the bottom in air channel 11 downwards Drying tower, with needing dry droplet fully to be contacted, complete dry heat and mass transfer process.Hot blast is led through deflector 7 Stream uniformly moves downward at the appropriate speed in drying tower, can both ensure that droplet is fully dried, and to greatest extent Avoid the generation of glutinous wall, glutinous top phenomenon.

Claims (6)

  1. A kind of 1. spray drying tower hot air distribution device, it is characterised in that:Including three inversed taper platform shape being set with one heart housings, three Individual inversed taper platform shape housing passes through top cover(13)It is connected;Outside inversed taper platform shape housing(4)Top is by cylinder(12)It is partitioned into air intake Spiral case(3), in cylinder(12)On be uniformly arranged some blast pipes(1)Connect air intake spiral case(3)With by outside inversed taper platform shape housing (4)With middle part inversed taper platform shape housing(5)The air channel of composition(11);Deflector(7)Uniformly it is arranged on middle part inversed taper platform shape housing(5) Outer wall bottom;Centrifugal atomizer is installed(8)Inside inversed taper platform shape housing(6)Positioned at middle part inversed taper platform shape housing(5)It is interior Portion;The air intake spiral case(3)With external air channel(10)It is connected.
  2. A kind of 2. spray drying tower hot air distribution device according to claim 1, it is characterised in that:The blast pipe(1) Air inlet end and air opening end be hypotenuse, the hypotenuse face hot wind flow direction of air inlet end, air outlet deviation during installation Air channel(11)Bottom.
  3. A kind of 3. spray drying tower hot air distribution device according to claim 1, it is characterised in that:The air intake spiral case (3)With external air channel(10)It is tangent in junction, ensure that hot blast tangentially enters air intake spiral case(3).
  4. 4. according to a kind of spray drying tower hot air distribution device described in any one of claim 1 or 2, it is characterised in that:It is described Blast pipe(1)Middle part sets the regulating gate of control intake(2).
  5. A kind of 5. spray drying tower hot air distribution device according to claim 1, it is characterised in that:The deflector(7) One end sets auricle(9), deflector(7)Pass through auricle(9)It is screwed on middle part inversed taper platform shape housing(5)Outer wall on.
  6. A kind of 6. spray drying tower hot air distribution device according to claim 1, it is characterised in that:Three inversed taper platform shape shells External conical degree of conical surface is identical.
CN201610050398.9A 2016-01-26 2016-01-26 A kind of spray drying tower hot air distribution device Active CN105571302B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610050398.9A CN105571302B (en) 2016-01-26 2016-01-26 A kind of spray drying tower hot air distribution device

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Application Number Priority Date Filing Date Title
CN201610050398.9A CN105571302B (en) 2016-01-26 2016-01-26 A kind of spray drying tower hot air distribution device

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CN105571302B true CN105571302B (en) 2017-12-22

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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109589625B (en) * 2019-01-25 2023-08-15 山东祥桓环保工程有限公司 Spray drying system

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2383025Y (en) * 1999-08-20 2000-06-14 中国人民解放军第三四一九工厂 High efficiency hot air distributor
CN2442213Y (en) * 2000-09-19 2001-08-08 山东省科学院能源研究所 Hot air distributor of centrifugal spray dry tower
JP2006061761A (en) * 2004-08-24 2006-03-09 Tdk Corp Spray-drying apparatus
CN203329386U (en) * 2013-06-19 2013-12-11 常州市宇通干燥设备有限公司 Hot air distributor for spray tower
CN103776251A (en) * 2012-10-17 2014-05-07 中国石油化工股份有限公司 Hot wind distributor
CN203842327U (en) * 2014-04-23 2014-09-24 无锡市阳光干燥设备有限公司 Centrifugal hot air distributor of upper air discharge dryer
WO2015185060A1 (en) * 2014-06-04 2015-12-10 Gea Process Engineering A/S An air disperser for spray-drying, and a method for manufacturing an air disperser comprising metal forming

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2383025Y (en) * 1999-08-20 2000-06-14 中国人民解放军第三四一九工厂 High efficiency hot air distributor
CN2442213Y (en) * 2000-09-19 2001-08-08 山东省科学院能源研究所 Hot air distributor of centrifugal spray dry tower
JP2006061761A (en) * 2004-08-24 2006-03-09 Tdk Corp Spray-drying apparatus
CN103776251A (en) * 2012-10-17 2014-05-07 中国石油化工股份有限公司 Hot wind distributor
CN203329386U (en) * 2013-06-19 2013-12-11 常州市宇通干燥设备有限公司 Hot air distributor for spray tower
CN203842327U (en) * 2014-04-23 2014-09-24 无锡市阳光干燥设备有限公司 Centrifugal hot air distributor of upper air discharge dryer
WO2015185060A1 (en) * 2014-06-04 2015-12-10 Gea Process Engineering A/S An air disperser for spray-drying, and a method for manufacturing an air disperser comprising metal forming

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Address after: 050031 No. 6 Jianbei Street, Chang'an District, Shijiazhuang City, Hebei Province

Patentee after: China Electric Power Construction Group Hebei electric survey and Design Research Institute Co., Ltd.

Address before: 050031 No. 6 Jianbei Street, Chang'an District, Shijiazhuang City, Hebei Province

Patentee before: Hebei Province Power Surveying Design & Research Institute