CN104397330B - A kind of pig blood reusing appts of mist projection granulating - Google Patents
A kind of pig blood reusing appts of mist projection granulating Download PDFInfo
- Publication number
- CN104397330B CN104397330B CN201410547867.9A CN201410547867A CN104397330B CN 104397330 B CN104397330 B CN 104397330B CN 201410547867 A CN201410547867 A CN 201410547867A CN 104397330 B CN104397330 B CN 104397330B
- Authority
- CN
- China
- Prior art keywords
- air
- pipe
- outlet
- drier
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention relates to the recycling processing unit of pig blood, the pig blood reusing appts of more particularly to a kind of mist projection granulating.It includes air cleaner, air cleaner connection drying device；Drying device connects sprayer unit；Air heater is connected between air cleaner and drying device；Air heater includes being provided between the parallel light calandria heat exchanger being alternately arranged, light calandria heat exchanger including checking the hollow every road of window；Sprayer unit includes granulation fluidization tower, air intake, gas outlet, sprayer and oblique reclaiming plate, and the charging aperture of sprayer unit is connected with disk centrifuge, is provided between drier and dust collector and shunted cribellum；Dust collector includes cyclone separator and dust arrester；Cyclone separator outlet is connected with heat exchanger；Dryer export is connected with storage tank, reservoir inlet and is provided with magnetic separator.Present invention granulation is uniform, clean separation effect is good, recyclability is good, abundant recovery waste heat.
Description
Technical field
The present invention relates to the recycling processing unit of pig blood, the pig blood reusing appts of more particularly to a kind of mist projection granulating.
Background technology
The protein content of red blood cell is up to 38% in pig blood, accounts for more than the 75% of whole blood Tot Prot, wherein 92%
Above is hemoglobin, therefore pig blood ball is a kind of excellent animal protein source, pig blood processor is directly made for a long time
Into the sale of blood cell powder.But due to containing ferroheme in blood cell powder so that blood cell powder is dark red, and with very heavy bloody
Taste, sense organ is bad to be difficult to receive, and its economic value added is not high.
Mist projection granulating, is exactly, by means of atomization and the effect of heat, to make the solvent in slurry droplet using spray dryer
The method that evaporation obtains dry powder.Spray-drying process is exactly that slurry makes the rapid drying of slurry drop become particle by atomizer
The process of powder.Spray drying is not only extensive in traditional ceramics, organic and inorganic chemical industry, powder metallurgy, food, medical industry
Using, and be used widely in various hyundai electronicses, function ceramics industry.Spray drying has turned into modern oxide
Ceramic prepared composition is uniform, dry-pressing blank density is uniform, and the important process that the original paper of acquisition consistency of performance number is essential is arranged
Apply.
Generally albumen powder is dried using spray drying tower at present, but still contained in the tail gas of spray drying tower
There is a certain amount of albumen powder, albumen powder is directly discharged into air with the tail gas of spray drying tower, pollution not only produced to environment,
And the waste of albumen powder is caused, it is unfavorable for making full use of for resource.
CN102067939 (2011-5-25) discloses a kind of process for preparing feed protein powder, specifically A, acidolysis;It is B, net
Change;C, drying;D, mixing.But its undisclosed specific preparation facilities of the patent, it is not the preparation dress for being exclusively used in Swine blood protein
Put, production process is not environmentally friendly enough, and production performance has much room for improvement.
The content of the invention
It is an object of the invention to provide a kind of clean separation effect is good, granulation is uniform, recyclability is good and can fully reclaim
The pig blood reusing appts of the mist projection granulating of waste heat.
The present invention above-mentioned technical purpose technical scheme is that：
A kind of pig blood reusing appts of mist projection granulating, including for providing the air cleaner of clean air, its described sky
Air filter is connected with the drying device entrance for drying Swine blood protein；The drying device entrance is also associated with being used to make
Sprayer unit of the porcine hemoglobin solution granulation as Swine blood protein；
It is connected with for heating air to provide the sky of hot-air between the air cleaner and the drying device
Hot-air heater；
The air heater includes setting between the parallel light calandria heat exchanger being alternately arranged, the smooth calandria heat exchanger
Have including checking the hollow every road of window, the smooth calandria heat exchanger both sides are provided with air inlet and connect going out for the sprayer unit
Air port；
The sprayer unit includes granulation fluidization tower, air intake and gas outlet, and is arranged on the granulation fluidization tower
Middle sprayer and the oblique reclaiming plate being arranged on below the sprayer, the angle of the reclaiming plate and horizontal plane
For 10 ° -35 °；High past lower is provided with the wind distributing hole that diameter gradually increases, the sprayer and charging aperture on the reclaiming plate
Communicate, the least significant end of the reclaiming plate and positioned at it is described granulation fluidization tower side wall be provided with discharging opening；
The air cleaner is connected with the air intake of the sprayer unit；
The charging aperture of the sprayer unit is connected with disk centrifuge, and the disk centrifuge includes body, the body
Inside it is provided with the top of rotary drum, the body and is provided with inlet and outlet device, the raw material that the inlet and outlet device includes parallel arrangement enters
Mouth pipe, heavy out pipe and light phase export pipe, the material inlet pipe, heavy out pipe and light phase export pipe and the rotary drum phase
Logical, the body side is provided with the deslagging portion communicated with the rotary drum and wastewater outlet, and the wastewater outlet is located at the row
The lower section in slag portion, the side of the body, which is provided with cleaning water inlet, the deslagging portion, is provided with PLC device；
The inlet and outlet device includes the material inlet pipe imported and exported seat and be fixed on the import and export seat, the original
Be provided with the upper centripetal discharge pump for separating heavy phase and the lower centripetal discharge pump for separating light phase on the side wall for expecting inlet tube, it is described on to
Heart pump is located at the top of the lower centripetal discharge pump, and the side of the material inlet pipe is connected with to be radially extended in the material inlet pipe
Heavy out pipe one end, the opposite side of the material inlet pipe is connected with the light phase radially extended in the material inlet pipe
One end of outlet；
The drying device bottom is provided with Swine blood protein collecting chamber；
The dust collector for collecting the tail gas containing part Swine blood protein is connected with the drying device；It is described
Dust collector include be used for separate the tail gas containing part Swine blood protein cyclone separator and with the cyclonic separation
The dust arrester that device is communicated；
The cyclone separator is connected with one-level collecting pipe, and the one-level collecting pipe is connected with two by the first isocon
Individual two grades of collecting pipes, two grades of collecting pipes are connected to two three-level collecting pipes by the second isocon, and the three-level is received
Collector is connected with dust arrester；
The cyclone separator outlet is connected with heat exchanger；
Heat conduction disk is provided with the heat exchanger, the heat conduction disk is circular metal disc, the heat conduction disk
Centre is provided with rotating shaft, and the rotating shaft is vertical with by the airflow direction of disk, and the two ends of the heat exchanger are respectively equipped with row
Cigarette channel and air intake passage, the side wall of the heat exchanger are provided with transducing hot-blast outlet, the discharge flue and the whirlwind
Separator is connected, and the transducing hot-blast outlet is communicated with the air scoop and/or the drying device of the sprayer unit；
It is provided between the drier and the dust collector and shunted cribellum；The cribellum that shunted includes shunting
Pipe and spin vibration sieve, the isocon are provided with equally distributed more than two branch pipes, the top of the drier with described point
Flow tube manifold inlet is communicated, and the isocon branch outlet is communicated with the spin vibration sieve；The connection powder at the top of the spin vibration sieve
Dirt collector；
The dryer export is connected with the magnetic separator being provided with storage tank, the reservoir inlet for removal of impurities.
Use programmable logic controller (PLC)（PLC）Device is arranged on the deslagging portion, situation about can be produced in continuous feed
Lower implementation periodically quantifies deslagging, can also carry out total discharge when stopping charging, so as to the dirt in automatic cleaning rotary drum, has
Automaticity height, the strong adaptability to technique adjustment, easy to adjust, good separating effect advantage；Pass through the material inlet
The arrangement of pipe, heavy out pipe and light phase export pipe, while coordinating the setting in rotary drum and deslagging portion, can make density relatively large
The centripetal pump chamber outflow under of heavy burder blood cell, make the centripetal pump chamber outflow under of the relatively small light material blood plasma of density, to pig blood
Blood plasma and the separating property height of blood cell separation, effect are good；Pass through the material inlet pipe and the upper centripetal discharge pump and lower centripetal discharge pump
Arrangement, while coordinating heavy out pipe, light phase export pipe and flow regulator, the heavy burder that density can be made relatively large
Blood cell is flowed out by lower centripetal discharge pump, and the light material blood plasma for making density relatively small flows out from lower centripetal discharge pump, to pig blood blood plasma and blood cell
The separating property of separation is high, effect is good；
Disk centrifuge is connected with sprayer unit charging aperture, the porcine hemoglobin that can isolate disk centrifuge
The blood cell of solution, is made for hyperglobulinemia polypeptide powder after being sprayed through sprayer unit, can fully remove its smell of blood, sensory properties
It is substantially improved；Hyperglobulinemia polypeptide powder content of ashes is low, and solubility is good, and protein content is high, is especially enriched in substantial amounts of small molecule many
Peptide, and improve the content of several amino acids.The feed nutrition of processing can improve sucking pig immunity, increase antibacterial and to virus
Inhibitory action.
During using above-mentioned technical proposal, normal temperature air is heated to be high-temperature gas through gas generating unit, high-temperature steam from
Heat pipe blows to cold pipe, enables more effectively to heat from the air that cryogenic piping flows into high-temperature pipe；
Porcine hemoglobin solution is sprayed into drying device through sprayer unit, and is contacted with high-temperature gas, in albumen powder
Moisture evaporation；Sprayer unit is set by reclaiming plate and the structure of wind distributing hole and position, the reclaiming plate is functioned simultaneously as cloth
The effect of aerofoil, simplifies structure setting；And the particle after final molding is slid along skewed reclaiming plate, can be with
Reduce energy consumption；It is bigger in the wind distributing hole closer to discharge outlet, the incomplete particle discharging of mist projection granulating is prevented, can be made
Crystal seed in granulation process is atomized uniform multilayer parcel, make the parcel number of plies of final particle with it is uniform in size；
Dry albumen powder is collected in dry tower bottom afterwards, and tail gas is further separated into cyclone separator, so
Tail gas sequentially enters dust collector and preheater afterwards, can fully collect the albumen powder in tail gas, and make full use of heat exchange
Device exchanges heat, recovery waste heat；
By the isocon set between drier discharge nozzle and spin vibration sieve, make dried material diversion, while making to do
The flow velocity when discharging flow of dry device is run with spin vibration sieve is matched, and is divided so as to uniform sieving, by the albumen powder of different-grain diameter
Level, good separating effect；
Heat transmission equipment overall volume is small, can make full use of cryopumping after heat energy, and the air intake of low temperature can be contacted fully
Heat-transfer surface, heat exchange property is high；The temperature of baking oven interior circulation hot blast can be improved, so as to improve the wet rate of appearance, evaporation rate is improved.
Preferably, the pipe ends between the drier and the dust collector are provided with air door.
Air door is being set in the end pipeline of the isocon, is making air flow method evenly, separating effect is more preferable；And
And can again be shunted after the protein powder in waste gas concentrates mixing a period of time, reduce operating cost.
Preferably, be connected between the air cleaner and the sprayer unit be easy to air flow into air blower or
Air pump.
Preferably, the air intake is located at the lower section of the reclaiming plate and is arranged on the bottom of the granulation fluidization tower
Portion；The gas outlet is located at the upper side of the granulation fluidization tower and outstanding.Blowing to for gas determines that crystal seed is wrapped
Wrap up in into the number of plies and the uniformity of particle；Discharging is easy in the setting of this air outlet structure.
Preferably, the reclaiming plate is network structure, the wind distributing hole on the reclaiming plate is shaped as circle.
Preferably, the upper surface of the wind distributing hole is provided with the calotte raised up.
The effect one of calotte is can to change air flow, particle is uniformly granulated in granulation tower；Two can be prevented from
Less particle directly leaks down from wind distributing hole.
Preferably, the dust arrester includes dust removing tube and the dust excluding hood being connected with the dust removing tube, the dust excluding hood
It is uniformly distributed on the dust arrester.
Preferably, the sectional area of the one-level collecting pipe is S1, the sectional area of two grades of collecting pipes is S2, wherein S1
=（1.05-1.3）S2.
Preferably, the sectional area of the three-level collecting pipe is S3, wherein S2=（1.05-1.3）S3.
The collecting pipes at different levels of the match of pipe diameter, energy consumption is lower when using dust collector of the present invention, more environmentally friendly.
In summary, the invention has the advantages that：Clean separation effect is good, granulates uniform, good separating effect, return
Receipts performance is good and can abundant recovery waste heat.
Brief description of the drawings
Fig. 1 is the schematic diagram of the pig blood reusing appts of mist projection granulating of the present invention；
Fig. 2 is the top view of disk centrifuge of the present invention；
Fig. 3 is the side view of disk centrifuge of the present invention；
Fig. 4 is the operating diagram of disk centrifuge of the present invention；
Fig. 5 is present heat exchanger sectional view；
Fig. 6 is the structural representation of reclaiming plate of the present invention.
Embodiment
The present invention is described in further detail below in conjunction with accompanying drawing.
As Figure 1-Figure 5, disk centrifuge 9 includes body, be provided with body at the top of rotary drum 91, body be provided with into
Outlet device 92, inlet and outlet device 92 includes material inlet pipe 922, heavy out pipe 925 and the light phase export pipe of parallel arrangement
926, material inlet pipe 922, heavy out pipe 925 and light phase export pipe 926 are communicated with rotary drum 91, and body side is provided with turning
Deslagging portion 93 and wastewater outlet 94 that drum 91 is communicated, wastewater outlet 94 are located at the lower section in deslagging portion 93, and the side of body is provided with
Clean in water inlet 95, deslagging portion 93 and be provided with PLC device；
Inlet and outlet device 92 includes importing and exporting seat and is fixed on the material inlet pipe 922 imported and exported on seat, material inlet
The upper centripetal discharge pump for separating heavy phase and the lower centripetal discharge pump for separating light phase, upper centripetal discharge pump position are provided with the side wall of pipe 922
In the top of lower centripetal discharge pump, the side of material inlet pipe 922 is connected with the heavy out pipe radially extended in material inlet pipe 922
925 one end, the opposite side of material inlet pipe 922 is connected with the light phase export pipe 926 radially extended in material inlet pipe 922
One end.
Air cleaner 1 is connected with the entrance of drying device 2 for drying Swine blood protein；The entrance of drying device 2 also connects
It is connected to for making sprayer unit of the porcine hemoglobin solution granulation as Swine blood protein；
It is connected with for heating air to provide the air heating of hot-air between air cleaner 1 and drying device 2
Device 4；
In order to improve heating effect, reduce air drag, air heater 4 includes the parallel light comb heat exchange being alternately arranged
It is provided between device 41, light calandria heat exchanger 41 including checking the hollow every road 43 of window 42, the both sides of light calandria heat exchanger 41 are set
There is the air outlet 45 of air inlet 44 and connection sprayer unit；Check that window can check the working condition and work of light calandria heat exchanger 41
Make efficiency；Flowed into for ease of air, air blower or air pump 10 are connected between air cleaner 1 and sprayer unit.
In order to improve mist projection granulating effect, sprayer unit includes granulation fluidization tower 31, air intake 33 and gas outlet 34, with
And be arranged on the sprayer 32 in the middle of granulation fluidization tower 31 and be arranged on the oblique reclaiming plate 35 of the lower section of sprayer 32, go out
The angle of flitch 35 and horizontal plane is 10 ° -35 °；High past lower is provided with the wind distributing hole that diameter gradually increases on reclaiming plate 35
351, sprayer 32 is communicated with charging aperture 36, the least significant end of reclaiming plate 35 and positioned at granulation fluidization tower 31 side wall be provided with discharging
Mouth 37；Air cleaner 1 is connected with the air intake 33 of sprayer unit；
Reclaiming plate 35 is that the wind distributing hole 351 on network structure, reclaiming plate 35 is shaped as circle.Air intake 33 is located at discharging
The lower section of plate 35 and the bottom for being arranged on granulation fluidization tower 31；Gas outlet 34 is located at the upper side of granulation fluidization tower 31 and outside
It is prominent.Sprayer unit charging aperture 36 connects disk centrifuge 9.Disk centrifuge is connected with sprayer unit charging aperture, can be made
The blood cell for the porcine hemoglobin solution that disk centrifuge is isolated, is made for hyperglobulinemia polypeptide after being sprayed through sprayer unit
Powder, can fully remove its smell of blood.
The bottom of drying device 2 is provided with Swine blood protein collecting chamber 21, larger by gravitational settling to collect particle
The Swine blood protein got off；
The dust collector 5 for collecting the tail gas containing part Swine blood protein is connected with drying device 2；Dust is received
Storage 5 include be used for separate the tail gas containing part Swine blood protein cyclone separator 54 and with the phase of cyclone separator 54
Logical dust arrester 55；
In order to uniform sieving, by albumen powder classification, good separating effect drier 2 and the dust collector of different-grain diameter
It is provided between 5 and shunted cribellum 7；Shunting cribellum 7 includes isocon 71 and spin vibration sieve 72, and isocon 71 is provided with uniform point
More than two branch pipes of cloth, the top of drier 2 is communicated with the manifold inlet of isocon 71, and the branch outlet of isocon 71 shakes with rotation
Sieve 72 is communicated；The top of spin vibration sieve 72 connection dust collector 5.
In order that air flow method is evenly, the pipe ends between drier 2 and dust collector 5 are provided with air door 8.
Cyclone separator 54 is connected with one-level collecting pipe 51, and one-level collecting pipe 51 is connected with two by the first isocon 56
Individual two grades of collecting pipes 52, two grades of collecting pipes 52 are connected to two three-level collecting pipes 53 by the second isocon 59, and three-level is received
Collector 53 is connected with dust arrester 55；Dust arrester 55 includes dust removing tube and the dust excluding hood that is connected with dust removing tube, dust excluding hood except
It is uniformly distributed on dirt device 55.
To improve shunting effect, the sectional area of one-level collecting pipe 51 is S1, and the sectional area of two grades of collecting pipes 52 is S2, wherein
S1=1.05-1.3S2.The sectional area of three-level collecting pipe 53 is S3, wherein S2=1.05-1.3S3.
In order to make full use of waste heat, the outlet of cyclone separator 54 is connected with heat exchanger 6；Heat exchanger 6 is exported and spray
The air intake of air intake 33 of mist device 3 is communicated；The either outlet of heat exchanger 6 is communicated with drying device 2.
Heat conduction disk 64 is provided with recuperation of heat and heat transfer effect, heat exchanger 6 to improve, heat conduction disk 64 is circular gold
Belong to and be provided with rotating shaft 641 in the middle of disc, heat conduction disk 64, rotating shaft 641 is vertical with the airflow direction by heat conduction disk 64, heat is handed over
The two ends of parallel operation 6 are respectively equipped with discharge flue 61 and air intake passage 62, and the side wall of heat exchanger 6 is provided with transducing hot-blast outlet
63, discharge flue 61 is connected with cyclone separator 54, the air intake 33 of transducing hot-blast outlet 63 and sprayer unit and/or dry
Dry device 2 is communicated；
Drier 2 outlet be connected with storage tank 11, the porch of storage tank 11 is provided with the magnetic separator 12 for removal of impurities, can preferentially by
The metal class impurity for dropping or being mingled with pre-treatment step is removed, and plays abundant cleaning effect.
This specific embodiment is only explanation of the invention, and it is not limitation of the present invention, people in the art
Member can make the modification without creative contribution to the present embodiment as needed after this specification is read, but as long as at this
All protected in the right of invention by Patent Law.
Claims (2)
1. a kind of pig blood reusing appts of mist projection granulating, including for providing the air cleaner of clean air（1）, its feature exists
In：The air cleaner（1）It is connected with the drier for drying Swine blood protein（2）Entrance；The drier（2）Entrance
It is also associated with for making sprayer unit of the porcine hemoglobin solution granulation as Swine blood protein；
The air cleaner（1）With the drier（2）Between be connected with for heating air to provide the sky of hot-air
Hot-air heater（4）；
The air heater（4）Including the parallel light calandria heat exchanger being alternately arranged（41）, the smooth calandria heat exchanger（41）
Between be provided with including check window（42）It is hollow every road（43）, the smooth calandria heat exchanger（41）Both sides are provided with air inlet
（44）With the air outlet for connecting the sprayer unit（45）；
The sprayer unit includes granulation fluidization tower（31）, air intake（33）And gas outlet（34）, and it is arranged on described make
Grain fluidization tower（31）Middle sprayer（32）Be arranged on the sprayer（32）The oblique reclaiming plate of lower section（35）,
The reclaiming plate（35）Angle with horizontal plane is 10 ° -35 °；The reclaiming plate（35）On from it is high toward lower be provided with diameter by
Cumulative big wind distributing hole（351）, the sprayer（32）With charging aperture（36）Communicate, the reclaiming plate（35）Least significant end and position
In the granulation fluidization tower（31）Side wall be provided with discharging opening（37）；
The air cleaner（1）With the air intake of the sprayer unit（33）It is connected；
The charging aperture of the sprayer unit（36）It is connected with disk centrifuge（9）, the disk centrifuge（9）Including body, institute
State and rotary drum is provided with body（91）, the body top is provided with inlet and outlet device（92）, the inlet and outlet device（92）Bag
Include the material inlet pipe of parallel arrangement（922）, heavy out pipe（925）With light phase export pipe（926）, the material inlet pipe
（922）, heavy out pipe（925）With light phase export pipe（926）With the rotary drum（91）Communicate, body side be provided with
The rotary drum（91）The deslagging portion communicated（93）And wastewater outlet（94）, the wastewater outlet（94）Positioned at the deslagging portion（93）
Lower section, the side of the body is provided with cleaning water inlet（95）, the deslagging portion（93）Inside it is provided with PLC device；
The inlet and outlet device（92）Including the material inlet pipe imported and exported seat and be fixed on the import and export seat（922）,
The material inlet pipe（922）Side wall on be provided with upper centripetal discharge pump for separating heavy phase and centripetal under light phase for separating
Pump, the upper centripetal discharge pump is located at the top of the lower centripetal discharge pump, the material inlet pipe（922）Side be connected with the original
Expect inlet tube（922）The heavy out pipe radially extended（925）One end, the material inlet pipe（922）Opposite side connection
Have in the material inlet pipe（922）The light phase export pipe radially extended（926）One end；
The drier（2）Bottom is provided with Swine blood protein collecting chamber（21）；
The drier（2）On be connected with dust collector for collecting the tail gas containing part Swine blood protein（5）；It is described
Dust collector（5）Including the cyclone separator for separating the tail gas containing part Swine blood protein（54）With with the rotation
Wind separator（54）The dust arrester communicated（55）；
The cyclone separator（54）It is connected with one-level collecting pipe（51）, the one-level collecting pipe（51）Pass through the first isocon
（56）It is connected with two two grades of collecting pipes（52）, two grades of collecting pipes（52）Pass through the second isocon（59）It is connected to two
Individual three-level collecting pipe（53）, the three-level collecting pipe（53）It is connected with dust arrester（55）；
The cyclone separator（54）Outlet is connected with heat exchanger（6）；
The heat exchanger（6）Inside it is provided with heat conduction disk（64）, the heat conduction disk（64）It is described to lead for circular metal disc
Hot disk（64）Centre is provided with rotating shaft（641）, the rotating shaft（641）With passing through heat conduction disk（64）Airflow direction it is vertical,
The heat exchanger（6）Two ends be respectively equipped with discharge flue（61）And air intake passage（62）, the heat exchanger（6）Side wall
It is provided with transducing hot-blast outlet（63）, the discharge flue（61）With the cyclone separator（54）It is connected, the transducing heat
Wind is exported（63）With the air intake of the sprayer unit（33）And/or the drier（2）Air intake is communicated；
The drier（2）With the dust collector（5）Between be provided with and shunted cribellum（7）；It is described to shunt cribellum（7）
Including isocon（71）And spin vibration sieve（72）, the isocon（71）Equally distributed more than two branch pipes are provided with, it is described
Drier（2）Top and the isocon（71）Manifold inlet is communicated, the isocon（71）Branch outlet shakes with the rotation
Sieve（72）Communicate；The spin vibration sieve（72）Top connects the dust collector（5）；
The drier（2）Outlet is connected with storage tank（11）, the storage tank（11）Porch is provided with the magnetic separator for removal of impurities
（12）；
The drier（2）With the dust collector（5）Between pipe ends be provided with air door（8）；
The air cleaner（1）The air blower for being easy to air to flow into or air pump are connected between the sprayer unit
（10）；The air inlet（44）Connect the air blower or air pump（10）Outlet；
The air intake（33）Positioned at the reclaiming plate（35）Lower section and be arranged on the granulation fluidization tower（31）Bottom；
The gas outlet（34）Positioned at the granulation fluidization tower（31）Upper side and outstanding；
The wind distributing hole（351）Upper surface be provided with the calotte raised up；
The dust arrester（55）The dust excluding hood being connected including dust removing tube and with the dust removing tube, the dust excluding hood is in the dedusting
It is uniformly distributed on device；
The one-level collecting pipe（51）Sectional area be S1, two grades of collecting pipes（52）Sectional area be S2, wherein S1=
（1.05-1.3）S2；
The three-level collecting pipe（53）Sectional area be S3, wherein S2=（1.05-1.3）S3.
2. a kind of pig blood reusing appts of mist projection granulating according to claim 1, it is characterised in that：The reclaiming plate（35）
For network structure, the reclaiming plate（35）On wind distributing hole（351）It is shaped as circle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410547867.9A CN104397330B (en) | 2014-10-16 | 2014-10-16 | A kind of pig blood reusing appts of mist projection granulating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410547867.9A CN104397330B (en) | 2014-10-16 | 2014-10-16 | A kind of pig blood reusing appts of mist projection granulating |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104397330A CN104397330A (en) | 2015-03-11 |
| CN104397330B true CN104397330B (en) | 2017-09-08 |
Family
ID=52635052
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410547867.9A Active CN104397330B (en) | 2014-10-16 | 2014-10-16 | A kind of pig blood reusing appts of mist projection granulating |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104397330B (en) |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63209570A (en) * | 1987-02-27 | 1988-08-31 | Dainippon Seito Kk | Sprinkling |
| CN2474232Y (en) * | 2001-04-29 | 2002-01-30 | 范炳喜 | High pressure spray drying machine |
| CN103418202A (en) * | 2012-05-20 | 2013-12-04 | 湖州展望药业有限公司 | Dust collector |
| CN203370515U (en) * | 2013-06-25 | 2014-01-01 | 浙江升华拜克生物股份有限公司 | Spray prilling tower |
| CN103471372A (en) * | 2013-09-18 | 2013-12-25 | 浙江索纳克生物科技有限公司 | High-performance heat exchanging equipment |
| CN103462189B (en) * | 2013-09-18 | 2015-07-08 | 浙江索纳克生物科技有限公司 | Environment-friendly and high-efficiency porcine blood protein powder preparation device |
-
2014
- 2014-10-16 CN CN201410547867.9A patent/CN104397330B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN104397330A (en) | 2015-03-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104764298B (en) | Circulating fluidised bed apparatus | |
| CN203687563U (en) | Pneumatic drying device for material breaking | |
| CN106267950B (en) | A kind of rotary flashing drying equipment and drying means | |
| CN107238256A (en) | Efficient spray drying device is used in a kind of milk powder processing | |
| CN103931868A (en) | High-efficiency albumen powder drying device | |
| CN206881161U (en) | A kind of rice protein powder production centrifugal spray drying tower | |
| CN108709406B (en) | High-efficient drying equipment of rice processing | |
| CN109589869A (en) | Continous way press atomization boiling granulating drying system | |
| CN108261844A (en) | A kind of closed circuit VC dedicated drying equipments of nitrogen and its method of work | |
| CN205965060U (en) | High -speed centrifugal spray drying equipment suitable for preparation dibazolum capsule | |
| CN104365998A (en) | Pig blood globulin powder preparation device | |
| CN209696840U (en) | Continous way press atomization boiling granulating drying system | |
| CN202186954U (en) | Spray drying device | |
| CN104397330B (en) | A kind of pig blood reusing appts of mist projection granulating | |
| CN205042132U (en) | Novel spray drier | |
| CN204104718U (en) | A kind of pig blood reusing appts of mist projection granulating | |
| CN204104793U (en) | A kind of clean proteinic powder of porcine preparation facilities | |
| CN204121789U (en) | A kind of Swine blood protein dried recovered device | |
| CN104399262B (en) | A kind of Swine blood protein dried recovered device | |
| CN207247724U (en) | Zinc sulfate drying device | |
| CN206746008U (en) | Milk drying device | |
| CN204104720U (en) | A kind of proteinic powder of porcine preparation facilities | |
| CN204104721U (en) | A kind of proteinic powder of porcine preparation facilities with air preheat function | |
| CN104397856B (en) | A kind of clean proteinic powder of porcine preparation facilities | |
| CN104258784B (en) | A kind of Swine blood protein separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A pig blood reusing device by spray granulation Effective date of registration: 20211015 Granted publication date: 20170908 Pledgee: Anji green sub branch of Hangzhou United Rural Commercial Bank Co.,Ltd. Pledgor: ZHEJIANG SONAC BIOLOGICAL SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: Y2021330001917 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |