CN109357477A - A kind of circular form suspension siding pressure spray drying tower - Google Patents
A kind of circular form suspension siding pressure spray drying tower Download PDFInfo
- Publication number
- CN109357477A CN109357477A CN201811167010.9A CN201811167010A CN109357477A CN 109357477 A CN109357477 A CN 109357477A CN 201811167010 A CN201811167010 A CN 201811167010A CN 109357477 A CN109357477 A CN 109357477A
- Authority
- CN
- China
- Prior art keywords
- siding
- drying tower
- tower
- plate
- wind
- 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.)
- Granted
Links
- 239000000725 suspension Substances 0.000 title claims abstract description 28
- 238000001694 spray drying Methods 0.000 title claims abstract description 13
- 238000001035 drying Methods 0.000 claims abstract description 58
- 239000000843 powder Substances 0.000 claims abstract description 31
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 19
- 239000010959 steel Substances 0.000 claims abstract description 19
- 239000007921 spray Substances 0.000 claims abstract description 14
- 239000003595 mist Substances 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 238000004140 cleaning Methods 0.000 claims description 12
- 239000011248 coating agent Substances 0.000 claims description 10
- 238000000576 coating method Methods 0.000 claims description 10
- 230000007246 mechanism Effects 0.000 claims description 10
- 238000009413 insulation Methods 0.000 claims description 9
- 230000005540 biological transmission Effects 0.000 claims description 8
- 238000010926 purge Methods 0.000 claims description 6
- 230000033001 locomotion Effects 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 4
- 210000002985 organ of corti Anatomy 0.000 claims description 4
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 3
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 3
- 238000005422 blasting Methods 0.000 claims description 3
- 239000003063 flame retardant Substances 0.000 claims description 3
- 230000002265 prevention Effects 0.000 claims description 3
- 229910052709 silver Inorganic materials 0.000 claims description 3
- 239000004332 silver Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 7
- 239000002699 waste material Substances 0.000 abstract description 6
- 238000004134 energy conservation Methods 0.000 abstract description 3
- 230000007774 longterm Effects 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 description 15
- 239000000243 solution Substances 0.000 description 9
- 238000009825 accumulation Methods 0.000 description 7
- 238000013461 design Methods 0.000 description 7
- 238000009434 installation Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 238000007789 sealing Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 210000003097 mucus Anatomy 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 210000003746 feather Anatomy 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/10—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it
- F26B3/12—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it in the form of a spray, i.e. sprayed or dispersed emulsions or suspensions
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/001—Heating arrangements using waste heat
- F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
- F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/008—Seals, locks, e.g. gas barriers or air curtains, for drying enclosures
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/06—Chambers, containers, or receptacles
- F26B25/08—Parts thereof
- F26B25/12—Walls or sides; Doors
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of circular forms to hang siding pressure spray drying tower, it includes hot air inlet, flusher, conveying device and recyclable device, and the hot air inlet is arranged at the top of drying tower, and lower part is equipped with flusher;The flusher includes the drying tower siding of hot wind wind distributing hole plate and liquid mist spray head lower part, and side is equipped with gate-type manhole;The conveying device includes active type suspension siding, and it includes circulating overhead chain conveyer and suspension type steel plate that active type, which hangs siding,;Lower part is equipped with recyclable device, and the whirlwind orifice plate of aperture obliquely upward is additionally provided on the inside of the annular air channel siding, and centre is equipped with gate-type manhole, and dry tower bottom is equipped with rotating disc type albumen powder collecting device;It is equipped with micro-positive pressure low temperature wind air outlet in the space of bottom plate and inclined rewinding turntable, top is equipped with return air inlet and heat exchanger channels.It solves the problems, such as wall built-up, greatly reduces the waste of material, guarantee product not by the pollution of wall built-up object, energy conservation causes the device to produce steadily in the long term.
Description
Technical field
The present invention relates to drying tower apparatus technical fields more particularly to a kind of circular form to hang siding pressure spray dryer
Tower.
Background technique
At present, main problem existing for spray dryer (especially pressure type drying tower) is not well solve reduction
Energy consumption and wall built-up problem is avoided, causes many resources to waste and production suspension induced losses to actual production.
Produce feather enzymolysis protein using pressure spray dryer, due to cannot completely eliminate the solid particle of slurry with not yet
The feather stem fiber of complete hydrolysis, therefore the blockage problem of drying tower nozzle is still remained in process of production, whitewashing is caused, out
Existing serious wall built-up, the albumen powder agglomeration being scorched are removed very difficult, it is sometimes desirable to which a large amount of clear water, which rinse, is up to a few hours, no
But production cost is increased, also causes very big burden to the sewage treatment of enterprise.
Main problem existing for drying process with atomizing technology is current line in the industry:
(1) thermal efficiency is low.The design for relying solely on drying tower, for cocurrent technique, effect is extremely limited in terms of energy conservation.
Currently, complete constant speed to develop two stages dry both at home and abroad using drying tower and dry, after liquid basically forms solid again into
Enter next stage drier, improves heat utilization rate.Since the matching of existing secondary drying equipment and drying tower is restricted, need
To be directed to eggWhite powderDedicated secondary drying device is further developed in drying.
(2) wall built-up is serious.The domestic wall built-up problem dry with pressure atomization is not well solved in the world, this problem
Have become the common fault of such equipment.In order to solve the problems, such as feed liquid wall built-up, usually increase drying tower diameter, centering skinny device is very
Effectively, but large scale equipment energy consumption is increased excessively, is run uneconomical.In recent years, both at home and abroad by improving airflow direction, reducing
Four approach such as tower wall temperature, installation gas sweeping device and improvement siding material solve the problems, such as wall built-up.Due to all equal offices of design
It is limited to make an issue of around siding, so while there are some effects, not
There is real solve the problems, such as.Product is polluted by wall built-up char particles, and need to stop production clear tower, to reduce having for equipment
Imitate utilization rate.
(3) it has a single function.It is commonly designed mostly by professional division, is respectively designed with drying tower, energy-saving appliance, whirlwind
Deduster, bag filter, the single devices such as deodorizing device, are then connected with pipeline, valve, pipeline complexity,
Consumptive material is more, and equipment volume is huge, needs tall and big workshop or place space.And since each independent equipment connects, increase
Many intermediate conversion links, structure is complicated for system, inconvenient to use.
(4) Drying Equipments pay attention to complete machine exploitation, lack the research of matching technology, there is a serious shortage of on-line checking instruments to set
Standby, the acquisition lag of various technological parameters, system feedback is imperfect, and existing drying equipment is really achieved not yet with optimised process
State is run, and there are also gaps compared with international advanced energy consumption index especially in terms of energy-saving effect.
Summary of the invention
Technical problem to be solved by the invention is to provide a kind of a kind of circular form suspensions suitable for solving the above problems
Siding pressure spray drying tower.
In order to solve the above technical problems, the technical solution used in the present invention is:
A kind of circular form hangs siding pressure spray drying tower, it is characterised in that including hot air inlet, flusher, defeated
Device and recyclable device are sent, the top of drying tower is arranged in the hot air inlet, and lower part is equipped with flusher;The sprinkling dress
The drying tower siding of the lower part including hot wind wind distributing hole plate and liquid mist spray head is set, side is equipped with gate-type manhole;The conveying device
Siding is hung including active type, and active type suspension siding includes circulating overhead chain conveyer and mutually overlapped suspension type steel
Plate forms an enclosed annular operating drying tower siding;Lower part is equipped with recyclable device, under the annular air channel siding
Side keeps the temperature and sets an annular passage in tower wall, and inside is additionally provided with the whirlwind orifice plate of aperture obliquely upward, and centre is equipped with gate-type people
Hole, dry tower bottom are equipped with rotating disc type albumen powder collecting device;It is low equipped with micro-positive pressure with the space of inclined rewinding turntable in bottom plate
Warm wind air outlet, top are equipped with return air inlet and heat exchanger channels.
Further technical solution is: the track of the cyclic conveyor is equipped with after one section of vertical downlink and rises again U-shaped
Bend, suspender are equipped with cross steering structure, can be carried out 90 ° of deflecting movement in U-shaped curved formula suspension road.
Further technical solution is: the tower wall opening position is formed equipped with the gas bypass from purge chamber side
The air curtain of micro-positive pressure plays the role of and purge chamber's seal isolation.
Further technical solution is: the tower wall and/or suspension type steel plate of the drying tower are that general steel plate is coated with resistance to height
The self-cleaning silver Gui dope layer of temperature;Suspension type steel plate carries out Shot Blasting, increases the surface area of surface relief injustice.
Further technical solution is: shape is toasted in the fire prevention diatom ooze coating bottoming of the outer wall of the high temperature section of the tower wall
At the polyurathamc coating of one layer of thermal insulation layer, then spray coated flame retardant, thickness is no less than 150mm.
Further technical solution is: the gate-type manhole, is equipped with integral heat insulation layer on the outside of door-plate, and be equipped with concealed step on
Plate and folding railing.
Further technical solution is: the return air inlet is annular, is pooled to main air hose, is equipped in the main air hose perpendicular
To wind-wind heat exchanger of comb, outdoor fresh air is sent into vertical comb by filter, and is sent hot wind after heat exchange by air blower
Enter burner.
Further technical solution is: the rotating disc type albumen powder collecting device, including a half-open shell, motor, transmission
Mechanism and inclination rewinding rotary disk, the hinged scraper plate of housing sidewall, the scraper plate is fixed on inclination rewinding rotary disk, described
It tilts rewinding rotary disk and is equipped with rotary shaft, by rotation axis connection transmission mechanism, the transmission mechanism is built-in with a motor, lower section
Discharging spiral organ is equipped with equipped with collecting tank, in the collecting tank.
The beneficial effects of adopting the technical scheme are that
The deficiency of the prior art is overcome, the wall built-up which not only can be well solved pressure atomization drying process is asked
Topic greatly reduces material waste caused by wall built-up, guarantees product not by the pollution of wall built-up object, energy conservation reduces the clear tower frequency that stops production
Rate causes the device to produce steadily in the long term, improves the dry thermal efficiency, improves production efficiency, guarantees product quality, easy to operate, greatly
Cost is reduced greatly.
(1) drying tower uses the automatically cleaning measure of the vertical plate barrel of suspension type of the outer stereo circulating of tower and strengthens spray system
The traditional idea that the drying tower over 30 years has been formed is breached completely, is solved long-standing material wall built-up in industry and is asked
Topic, started it is a kind of it is novel do not shut down efficient process material wall built-up system, caused by substantially increasing production efficiency and wall built-up
The waste of material, energy, first is that wall built-up slurry or powder can recycle in time;Second is that solving burned albumen powder to product matter
The influence of amount;Third is that blowing out cleaning is avoided to waste a large amount of time and flushing water (forming secondary pollution).It can reduce about
10% production cost.This will become a major transformation of pressure atomization drying tower.
(2) drying tower siding coating, air curtain and hot wind whirlpool comprehensive treatment technique, extension droplet drying time can be reduced
The straight section height of drying tower;The accumulation of surface drying powder caused by cone surface to reduce traditional drying tower bottom, changes biography
The design of the drying tower bottom of system further decreases dry tower height degree using the flat tower bottom structure with bridging plate, can be with
Reduce by 25% equipment manufacturing cost and loss burned after albumen powder accumulation.
(3) the wall built-up albumen powder reclaiming device for using suspension type siding, can reduce drying tower 6m or so, both reduce
Project cost, and convenient maintenance management;By the science organization of air return system, reduce the carrying amount of albumen powder;By whole
Body heat preservation technology, improves capacity usage ratio.
(4) it is dry to extend droplet for the self-cleaning coating of drying tower siding, anti-accumulation air curtain and hot wind whirlpool integrated treatment structure
Time overcomes drying tower and tower body height is relied on to meet dry shortcoming merely, and solves the problems, such as the anti-accumulation of surface drying powder.
(5) novel gate-type manhole technology is used, the maintenance management of production process is facilitated, especially advantageous production is just
Phase carries out every scientific research.
Detailed description of the invention
The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.
Fig. 1 is structural schematic diagram of the invention;
Fig. 2 is drawing in side sectional elevation of the invention;
Wherein: 1- hot wind inlet, 2- tower body and insulating layer, 3- hot wind wind distributing hole plate, 4- liquid mist spray head, the circulating suspension of 5-
Conveyer, 6- whirlwind orifice plate, 7- return air channel, 8- rotary disk, 9- scraper plate, 10- discharging spiral organ, 11- heat exchanger channels, 12- are returned
Air port, 13- gate-type manhole, 14- steel construction seal operation room, the driving of 15- stretched wire, 16- insulating layer.
Specific embodiment
With reference to the attached drawing in the embodiment of the present invention, technical solution in the embodiment of the present invention carries out clear, complete
Ground description, it is clear that described embodiment is only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
In the following description, numerous specific details are set forth in order to facilitate a full understanding of the present invention, but the present invention can be with
Implemented using other than the one described here other way, those skilled in the art can be without prejudice to intension of the present invention
In the case of do similar popularization, therefore the present invention is not limited by the specific embodiments disclosed below.
As shown in Figs. 1-2, a kind of circular form suspension siding press atomization is dry, it is characterised in that including hot air inlet 1, spray
Device, conveying device and recyclable device are spilt, the top of drying tower is arranged in the hot air inlet 1, and lower part is equipped with flusher;
The flusher includes the drying tower siding of the lower part of hot wind wind distributing hole plate 3 and liquid mist spray head 4, and side is equipped with gate-type manhole
13;The conveying device includes active type suspension siding, and the active type suspension siding includes circulating overhead chain conveyer 5 and phase
Mutually overlapped suspension type steel plate forms an enclosed annular operating drying tower siding;Lower part is equipped with recyclable device, in the ring
The lower section of shape air flue siding keeps the temperature in tower wall and sets an annular passage, and inside is additionally provided with the whirlwind orifice plate 6 of aperture obliquely upward,
Centre is equipped with gate-type manhole 13, and dry tower bottom is equipped with rotating disc type albumen powder collecting device;In bottom plate and inclined rewinding turntable
Space is equipped with micro-positive pressure low temperature wind air outlet, and top is equipped with return air inlet 12 and heat exchanger channels 11.
Further preferred is: the track of the circulating overhead chain conveyer 5 is equipped with again multiple after one section of vertical downlink rise
U-shaped bend, suspender is equipped with cross steering structure, can be carried out 90 ° of deflecting movement in U-shaped curved formula suspension road.
Further preferred is: the tower wall opening position, and equipped with the gas bypass from purge chamber side, formation is micro- just
The air curtain of pressure plays the role of and purge chamber's seal isolation.
Further preferred is: the tower wall and suspension type steel plate of the drying tower be general steel plate be coated with it is resistant to high temperature from
Clean property silver Gui dope layer;The suspension type steel plate carries out Shot Blasting, to increase surface area.
Further preferred is: the fire prevention diatom ooze coating bottoming of the outer wall of the high temperature section of the tower wall, baking are formed
One layer of thermal insulation layer, then the polyurathamc coating of spray coated flame retardant, thickness are no less than 150mm.
Further preferred is: the gate-type manhole 13, integral heat insulation layer is equipped on the outside of door-plate, and be equipped with concealed step on
Plate and folding railing.
Further preferred is: the return air inlet 12 is annular, is pooled to main air hose, is equipped in the main air hose perpendicular
To wind-wind heat exchanger of comb, outdoor fresh air is sent into vertical comb by filter, and is sent hot wind after heat exchange by air blower
Enter burner.
Further preferred is: the rotating disc type albumen powder collecting device, including a half-open shell, motor, driver
Structure and inclination rewinding rotary disk 8, the housing sidewall hinged one scrape 9, and the scraper plate 9 is fixed on inclination rewinding rotary disk 8, described
It tilts rewinding rotary disk 8 and is equipped with rotary shaft, by rotation axis connection transmission mechanism, the transmission mechanism is built-in with a motor, under
Side is equipped with collecting tank, and discharging spiral organ 10 is equipped in the collecting tank.
Easily is there is the tower wall in the region of wall built-up by the present invention in drying tower, carries out innovative design, the vertical hanging board upper end of bar shaped
It is hung on the suspension hook of overhead chain conveyer by the hinge with cross shift fork, overhead chain conveyer selects pushing-type chain structure, each
Chain link uses four bearings, smooth running, and operation can be pulled to run and deposit with pushing.This secondary design is exactly to utilize pushing-type chain
The characteristics of run down suspended chain, then return up again, suspended chain along three-dimensional curve run, according to the instruction of sensor
(medium sensor on high-pressure oil feed pipe pressure sensor, sealing plate) operates counterclockwise, and the hanging plate of outlet end is run with suspended chain
To the sealing room of drying tower side, in the horizontal segment for entering sealing room, the water mist equipped with high temperature, the length direction along hanging plate is equipped with
Water-bath spray head, using the protein of high-temperature water clean the surface, suspended chain specially devises descending branch, is conducive to cleaning.
Before decreasing, cross shift fork on hinge and suspended chain buting iron outstanding bump against hanging plate, by 90 ° of switch, hanging plate by
The originally state of a continuous line, by successively rotating as parastate, subsequently into running down section;Downlink section is close
Vertically, hanging plate is during decline gradually close to and generating friction.Due to the steel plate that hanging plate is 1.2mm, each hanging plate is nearly weighed
7kg or so, the phase mutual friction of plate face can destroy hardened protein char layer.At this time, suspended chain remains in operation under
The horizontal segment of layer, cross shift fork and the suspended chain other side buting iron outstanding also relied on hinge bump against, and are reversed switch
90 °, hanging plate is restored to the state of an original continuous line.High temperature (operating) water nozzle positioned inside rushes hanging plate inside
It washes, followed by 90 ° of switch enter the ascent stage.Ascent stage is still close to the phase mutual friction progress machine for vertically, utilizing plate face again
Tool cleaning.90 ° of states for being restored to a continuous line are inverted after running to horizontal segment, and are entered in drying tower.Exactly will
Continuous cleaning outside slurry or albumen powder the progress tower that tower wall is hung, avoids and accumulates for a long time, is burned, falling off, and influences
Product quality;The clear wall that also avoids stopping production causes the waste of production efficiency and resource.
The movement of hanging plate is to rely on suspended chain, needs to meet the smallest turn of suspended chain in the position of suspended chain disengaging drying tower
Curved radius, in the intersections of inlet and outlet, there are certain intervals;In order to guarantee the vacuum degree in tower, be additionally provided with one it is fixed close
Sealing plate;Above apparatus with the circular sealing interior of cricoid insulation belt and 3/4, return equipped with protein liquid by sealing room bottom
Closed tube road, top are equipped with manhole with into exhaust outlet, and centre is equipped with vertical ladder, can manually be periodically into inspection, dimension
Shield, cleaning.It seals room and maintains negative pressure, but pressure is slightly larger than drying tower, avoids the hot wind containing albumen powder from leaking, and suspended chain goes out
Mouth is equipped with small-sized air curtain, and the water mist containing albumen powder is avoided to enter in drying tower.
Albumen powder bulk density very little, it is easy to tower wall deposition occur and make somebody a mere figurehead, accelerate the mobility of albumen powder using vibrator;
This design uses flat-bottom structure to effectively reduce tower body height, and albumen powder passes through the seam of turntable and tower wall in order to prevent
Gap falls into bottom space, uses soft plastic seal between the two;By taking a shower and in Cryogenic air after operation, hanging steel
The temperature of plate is far below hot blast temperature close to 90 DEG C or so, not will cause albumen sintering;The disengaging of mechanical stretched wire and hanging steel plate
Mouth forms the air curtain of micro-positive pressure using gas bypass, that is, plays sealing function, and forms the airflow screen for stopping droplet to be scattered tower wall
It on barrier, is also possible to prevent under normal production conditions, tiny mist droplet deposition is on tower wall surface.
There are also 8 meters or so for tower body straight section, are still likely to occur wall built-up or albumen powder accumulation.Therefore, middle and lower part tower body carries out
Continue anti-wall built-up or albumen powder accumulation transformation.Firstly, hanging steel plate siding 9 meters of straight sections below use self-cleaning coating wall
Plate, and on the siding of the 4m high of this section, using the air flue of five annulars, form alternate 0.6m air outlet slit (slit width 5mm), structure
At the air curtain layer of adherent very thin downward cocurrent, it can effectively prevent do not had falling with drying hot wind for injection power
Mist cloud (1~3m/s);It is 3 meters following again, then it is provided with the microwell plate obliquely upward to aperture, utilizes tangential gentle breeze and downward master
The a tail wind of thermally conductive wind synthesizes the whirlpool slowly rotated, and changing vertical drop have passed through constant rate of drying droplet motion profile, opens
Beginning rotates along helix;Since whirlpool revolving speed is very low, centrifugal force does not overcome gravity, and droplet dries path simply by change
(3~5m/s) extends droplet drying time, and will not deposit on side wall because centrifugal force is excessive.Even if there is a small amount of egg
White powder is scattering on side wall, can also be immediately exposed to tangential gentle breeze effect, and is blown off.
Drying tower lower part is provided with the annular return air inlet of 450mm, the annular passage of external 1.2m × 1.2m, due to return air inlet
Developed area has 5m2As many as, so return air amount is maintained when being slightly above air output in drying tower under conditions of tiny structure, annular return air
The wind speed of mouth only has the half of wind speed in tower, due to the low albumen powder that will not take away many surface dryings of wind speed;By annular return air inlet
Outside is that section reaches 1.44m2Annular air -return duct, wind speed rapid drawdown, a suitable albumen powder can fall into annular air -return duct cone cell
Albumen powder collecting tank, by vibration feeder, albumen powder is fallen into again on the rewinding turntable of dry tower bottom.For balanced wind
Speed, the backwind tube being mounted on outside the side wall of air duct are connect by variable diameter air duct with main air duct.
In order to be collected in time in air duct because condensation effects appear in the albumen mucus on wind-vertical comb of wind heat exchanger,
The efficiency for guaranteeing heat exchange is set with the porous plate for studding with the inclination installation of rubber before vertical comb integral solder first
(being oriented to using casing), every comb correspondence penetrate a hole, and porous plate is pulled by two chains, be can move up and down, and is removed
The albumen powder and albumen mucus of vertical comb;Albumen powder is sent to revolution charging tray by the chute around drying tower annular return air inlet bottom
On;A small amount of albumen mucus by the porous plate of inclination installation by the collecting box of water conservancy diversion to main air duct bottom, by artificial regular
Recycling, while main air duct installs manhole, periodic cleaning.
Drying tower plate all using silver-colored Gui coating spraying, has heat-resistant quality, replaces stainless steel;Its self-cleaning property is reduced
Electrostatic Absorption causes the accumulation of albumen dust on siding, even if there is the dust adhered on a small quantity, by micro electromagnetic vibrator
It can be easy to fall off.
Normal drying tower is only equipped with manhole, and few installation doors;The overwhelming majority is designed in outer skin manhole again
On, in order to reduce heat loss, reduce manhole quantity to the greatest extent, and manhole is not easy to personnel's maintenance;This secondary design, by the big portion of manhole
Point it transform vertical hinged door as, and on the frame including being mounted directly, it is synchronous on the outside of door-plate to implement integral heat insulation, in order to open, first
Hole is opened by artificial pull-out 400mm horizontal outward using double leval jib blocking mechanism;Then the folding of blocking mechanism side is utilized
Page, is freely opened flat installation door;Last personnel's push-in is mounted on the aluminum alloy pedal being hidden in channel steel on chassis base, opens folding
Folded railing, personnel can enter safely operation in tower, and such installation door is installed one in each tower section of drying tower, is convenient for
Upkeep operation in tower;Individual manhole ways are identical as installation door, all done using what integral heat insulation, entirety were pulled out and then was opened flat
Method.
Claims (8)
1. a kind of circular form hangs siding pressure spray drying tower, it is characterised in that: including hot air inlet (1), flusher,
The top of drying tower is arranged in conveying device and recyclable device, the hot air inlet (1), and lower part is equipped with flusher;It is described
Flusher includes the drying tower siding of the lower part of hot wind wind distributing hole plate (3) and liquid mist spray head (4), and side is equipped with gate-type manhole
(13);The conveying device includes active type suspension siding, and the active type suspension siding includes circulating overhead chain conveyer (5)
And mutual overlapped suspension type steel plate, form an enclosed annular operating drying tower siding;Lower part is equipped with recyclable device, in institute
The lower section of annular air channel siding is stated, keeps the temperature in tower wall and sets an annular passage, inside is additionally provided with the whirlwind hole of aperture obliquely upward
Plate (6), centre are equipped with gate-type manhole (13), and dry tower bottom is equipped with rotating disc type albumen powder collecting device;It is received in bottom plate and inclined
Expect that the space of turntable is equipped with micro-positive pressure low temperature wind air outlet, top is equipped with return air inlet (12) and heat exchanger channels (11).
2. a kind of circular form according to claim 1 hangs siding pressure spray drying tower, it is characterised in that the circulation
The track of formula overhead chain conveyer (5) is equipped with the U-shaped bend risen again again after one section of vertical downlink, and suspender is equipped with cross and turns to knot
Structure can be carried out 90 ° of deflecting movement in U-shaped curved formula suspension road.
3. a kind of circular form according to claim 2 hangs siding pressure spray drying tower, it is characterised in that the tower wall
Opening position forms the air curtain of micro-positive pressure equipped with the gas bypass from purge chamber side, plays to seal off with purge chamber and make
With.
4. a kind of circular form according to claim 3 hangs siding pressure spray drying tower, it is characterised in that the drying
The tower wall and suspension type steel plate of tower are that general steel plate is coated with self-cleaning silver Gui dope layer resistant to high temperature;The suspension type steel plate carries out
Shot Blasting, to increase surface area.
5. a kind of circular form according to claim 4 hangs siding pressure spray drying tower, it is characterised in that the tower wall
High temperature section outer wall fire prevention diatom ooze coating bottoming, baking forms one layer of thermal insulation layer, then the polyurathamc of spray coated flame retardant
Coating, thickness are no less than 150mm.
6. a kind of circular form according to claim 5 hangs siding pressure spray drying tower, it is characterised in that the gate-type
Manhole (13), door-plate outside are equipped with integral heat insulation layer, and are equipped with concealed pedal and fold railing.
7. a kind of circular form according to claim 6 hangs siding pressure spray drying tower, it is characterised in that the return air
Mouth (12) is annular, is pooled to main air hose, and wind-wind heat exchanger of vertical comb is equipped in the main air hose, and outdoor fresh air is logical
It crosses filter and is sent into vertical comb, and hot wind after heat exchange is sent into burner by air blower.
8. a kind of circular form according to claim 7 hangs siding pressure spray drying tower, it is characterised in that the turntable
Formula albumen powder collecting device, including a half-open shell, motor, transmission mechanism and inclination rewinding rotary disk (8), the housing sidewall
Hinged one scrapes (9), and the scraper plate (9) is fixed on inclination rewinding rotary disk (8), and the inclination rewinding rotary disk (8) is equipped with rotation
Shaft, by rotation axis connection transmission mechanism, the transmission mechanism is built-in with a motor, and lower section is equipped with collecting tank, the collecting tank
In be equipped with discharging spiral organ (10).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811167010.9A CN109357477B (en) | 2018-10-08 | 2018-10-08 | Circulation type hangs wallboard pressure spray drying tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811167010.9A CN109357477B (en) | 2018-10-08 | 2018-10-08 | Circulation type hangs wallboard pressure spray drying tower |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109357477A true CN109357477A (en) | 2019-02-19 |
CN109357477B CN109357477B (en) | 2020-09-29 |
Family
ID=65348304
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811167010.9A Active CN109357477B (en) | 2018-10-08 | 2018-10-08 | Circulation type hangs wallboard pressure spray drying tower |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109357477B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112008830A (en) * | 2020-09-05 | 2020-12-01 | 曹凯悦 | Ceramic tile production process |
CN115256249A (en) * | 2022-09-29 | 2022-11-01 | 达州市全锦建材有限责任公司 | Shot blasting machine |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2733288Y (en) * | 2004-10-25 | 2005-10-12 | 山东天力干燥设备有限公司 | Pressure type spraying drier |
CN2765121Y (en) * | 2004-10-14 | 2006-03-15 | 沈善明 | Fluided bed continuous extractum granulation dryer |
CN2935045Y (en) * | 2006-05-27 | 2007-08-15 | 新疆屯河投资股份有限公司果蔬制品昌吉分公司 | Special drying device for tomato powder |
CN201476502U (en) * | 2009-09-01 | 2010-05-19 | 兆光生物工程(邹平)有限公司 | Pressure spray drying tower |
CN202041044U (en) * | 2011-04-27 | 2011-11-16 | 国家海洋局第三海洋研究所 | Spray drying waste heat recycling device |
CN202814041U (en) * | 2012-07-27 | 2013-03-20 | 德州瑞康食品有限公司 | Tower cleaning device for spray drying tower |
CN203100404U (en) * | 2012-12-19 | 2013-07-31 | 南通万通食品科技有限公司 | Modified pressure spray drying tower |
CN204177158U (en) * | 2014-09-28 | 2015-02-25 | 河南泰利杰生物科技有限公司 | Wall pressure spray drying tower is glued on antiseized top |
CN205561421U (en) * | 2016-01-29 | 2016-09-07 | 保定市华联化工有限责任公司 | But centrifugal spray drying tower of redispersibility latex powder |
CN107525396A (en) * | 2016-06-20 | 2017-12-29 | 宜昌西部化工有限公司 | A kind of spray drying tower dust-scraping device |
RU2656541C1 (en) * | 2017-06-29 | 2018-06-05 | Олег Савельевич Кочетов | Spray dryer |
-
2018
- 2018-10-08 CN CN201811167010.9A patent/CN109357477B/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2765121Y (en) * | 2004-10-14 | 2006-03-15 | 沈善明 | Fluided bed continuous extractum granulation dryer |
CN2733288Y (en) * | 2004-10-25 | 2005-10-12 | 山东天力干燥设备有限公司 | Pressure type spraying drier |
CN2935045Y (en) * | 2006-05-27 | 2007-08-15 | 新疆屯河投资股份有限公司果蔬制品昌吉分公司 | Special drying device for tomato powder |
CN201476502U (en) * | 2009-09-01 | 2010-05-19 | 兆光生物工程(邹平)有限公司 | Pressure spray drying tower |
CN202041044U (en) * | 2011-04-27 | 2011-11-16 | 国家海洋局第三海洋研究所 | Spray drying waste heat recycling device |
CN202814041U (en) * | 2012-07-27 | 2013-03-20 | 德州瑞康食品有限公司 | Tower cleaning device for spray drying tower |
CN203100404U (en) * | 2012-12-19 | 2013-07-31 | 南通万通食品科技有限公司 | Modified pressure spray drying tower |
CN204177158U (en) * | 2014-09-28 | 2015-02-25 | 河南泰利杰生物科技有限公司 | Wall pressure spray drying tower is glued on antiseized top |
CN205561421U (en) * | 2016-01-29 | 2016-09-07 | 保定市华联化工有限责任公司 | But centrifugal spray drying tower of redispersibility latex powder |
CN107525396A (en) * | 2016-06-20 | 2017-12-29 | 宜昌西部化工有限公司 | A kind of spray drying tower dust-scraping device |
RU2656541C1 (en) * | 2017-06-29 | 2018-06-05 | Олег Савельевич Кочетов | Spray dryer |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112008830A (en) * | 2020-09-05 | 2020-12-01 | 曹凯悦 | Ceramic tile production process |
CN112008830B (en) * | 2020-09-05 | 2021-06-11 | 清远市欧雅陶瓷有限公司 | Ceramic tile production process |
CN115256249A (en) * | 2022-09-29 | 2022-11-01 | 达州市全锦建材有限责任公司 | Shot blasting machine |
Also Published As
Publication number | Publication date |
---|---|
CN109357477B (en) | 2020-09-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109357477A (en) | A kind of circular form suspension siding pressure spray drying tower | |
CN107174899A (en) | A kind of spiral spray deduster | |
CN108532415A (en) | A kind of asphalt mixing plant and technique of high proportion addition reworked material | |
CN206310866U (en) | A kind of building sand drying unit | |
CN103604281B (en) | Rotary drum drying machine | |
CN102423128B (en) | Roller filling machine | |
CN101569887B (en) | Method for movably collecting, conveying, dedusting and desulfurizing dust of coke oven coke guide | |
CN104061772B (en) | A kind of band drier | |
CN2501005Y (en) | Drying equipment for mud material | |
CN102519234A (en) | Novel vertical drying equipment | |
CN207815897U (en) | A kind of energy-saving box-type drying unit | |
CN204426639U (en) | A kind of machine for drying melon seeds | |
CN206674928U (en) | A kind of tea drier | |
CN206637646U (en) | A kind of direct contact type flue gas condensing recovery of latent heat device | |
CN112146385A (en) | Rapid drying device for coal gangue bricks and using method thereof | |
CN207076275U (en) | A kind of spiral spray deduster | |
CN205100066U (en) | Horizontal energy -concerving and environment -protective type asphalt concrete regenerating device | |
CN212397600U (en) | Dust collecting pipeline cleaning structure of dust removing system | |
CN209065773U (en) | A kind of energy-saving natural gas perlite bloating plant | |
CN209508149U (en) | The anti-blocking gas operated device of automatically cleaning for pulverized coal pyrolysis rotary furnace | |
CN208734896U (en) | A kind of unloading valve and gas cleaning ash conveying device | |
CN207501762U (en) | A kind of anti-blocking blockage removal system of rotary regenerative air preheater | |
CN206887022U (en) | A kind of solid garbage as resource utilizes system | |
CN206279123U (en) | Semi-coke dry coke quenching auxiliary | |
CN206560816U (en) | A kind of lithium battery nanoscale microparticle high speed mixer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right |
Effective date of registration: 20231106 Address after: 5 / F, 277 Huqingping Road, Minhang District, Shanghai, 201100 Patentee after: JUNHE (Shanghai) Instrument Technology Co.,Ltd. Address before: 055650 North side of Shidai Road West Section, Xinhe County, Xingtai City, Hebei Province Patentee before: XINHE JINBO LYUTAI TECHNOLOGY CO.,LTD. |
|
TR01 | Transfer of patent right |