CN204121789U - A kind of Swine blood protein dried recovered device - Google Patents

A kind of Swine blood protein dried recovered device Download PDF

Info

Publication number
CN204121789U
CN204121789U CN201420598082.XU CN201420598082U CN204121789U CN 204121789 U CN204121789 U CN 204121789U CN 201420598082 U CN201420598082 U CN 201420598082U CN 204121789 U CN204121789 U CN 204121789U
Authority
CN
China
Prior art keywords
pipe
air
chamber
blood protein
inlet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420598082.XU
Other languages
Chinese (zh)
Inventor
刘观洲
邓自伟
沙欢
李宁丰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZHEJIANG SONAC BIOTECHNOLOGY Co Ltd
Original Assignee
ZHEJIANG SONAC BIOTECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ZHEJIANG SONAC BIOTECHNOLOGY Co Ltd filed Critical ZHEJIANG SONAC BIOTECHNOLOGY Co Ltd
Priority to CN201420598082.XU priority Critical patent/CN204121789U/en
Application granted granted Critical
Publication of CN204121789U publication Critical patent/CN204121789U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The utility model relates to the recycling treating apparatus of pig blood, particularly a kind of Swine blood protein dried recovered device.It comprises air cleaner, and air cleaner connects drying device; Drying device connects sprayer unit; Air heater is connected between air cleaner with drying device; Air heater comprises chamber, top and chamber, the end; Chamber, top is the input cavity for inputting for air to be heated and the output cavity for heating air output by baffle for separating; Be communicated with cold pipe between input cavity and chamber, the end, between output cavity and chamber, the end, be communicated with heat pipe; Sprayer unit comprises fluidising chamber, air inlet, air outlet and spraying heat pipe and ventilation terminal, and the first feed space is connected with disk centrifuge, is provided with and shunted cribellum between drier and dust collection; Dust collection comprises cyclone separator and dust arrester; Cyclone separator outlet is connected with heat exchanger.The utility model granulation is even, good, the abundant recovery waste heat of good separating effect, recyclability.

Description

A kind of Swine blood protein dried recovered device
Technical field
The utility model relates to the recycling treating apparatus of pig blood, particularly a kind of Swine blood protein dried recovered device.
Background technology
In pig blood, erythrocytic protein content is up to 38%, accounts for more than 75% of whole blood Tot Prot, and wherein more than 92% is hemoglobin, and therefore pig blood cell is a kind of excellent animal protein source, and pig blood processor is directly made into the sale of blood cell powder for a long time.But owing to containing ferroheme in blood cell powder, make blood cell powder be dark red, and with the very heavy smell of blood, accept, and its economic value added is not high sense organ bad being difficult to.
Mist projection granulating, is exactly adopt spray dryer by means of atomization and the effect of heat, makes the solvent in slurry droplet evaporate the method obtaining dry powder.Spray-drying process is exactly that slurry makes slurry drip the process of drying rapidly and becoming particle powder through atomizer.Spraying dry is extensive use in traditional ceramics, organic and inorganic chemical industry, powder metallurgy, food, medical industry not only, and is used widely in various hyundai electronics, function ceramics industry.Spraying dry become modern oxide ceramics prepared composition evenly, dry-pressing blank density is even, obtains the requisite important process measure of original paper of consistency of performance number.
Usually spray drying tower is adopted to carry out drying to albumen powder at present, but still containing a certain amount of albumen powder in the tail gas of spray drying tower, albumen powder directly enters in air with the tail gas of spray drying tower, not only environment is produced and pollute, and cause the waste of albumen powder, be unfavorable for making full use of of resource.
CN102067939 (2011-5-25) discloses a kind of process for preparing feed protein powder, specifically A, acidolysis; B, purification; C, drying; D, mixing.But this patent its concrete preparation facilities unexposed, not the preparation facilities being exclusively used in Swine blood protein, the inadequate environmental protection of production process, and production performance has much room for improvement.
Utility model content
The purpose of this utility model is to provide a kind of good separating effect, granulation is even, recyclability good and the Swine blood protein dried recovered device of the abundant recovery waste heat of energy.
Above-mentioned technical purpose of the present utility model is achieved by the following technical programs:
A kind of Swine blood protein dried recovered device, comprise the air cleaner for providing clean air, air cleaner described in it is connected with the drying device entrance for dry Swine blood protein; Described drying device entrance is also connected with the sprayer unit for making the granulation of porcine hemoglobin solution become Swine blood protein;
Be connected with for adding hot-air thus providing the air heater of hot-air between described air cleaner and described drying device;
Described air heater comprises chamber, top and chamber, the end; Chamber, described top is the input cavity for inputting for air to be heated and the output cavity for heating air output by baffle for separating;
Be communicated with cold pipe between described input cavity and chamber, the described end, between described output cavity and chamber, the described end, be communicated with heat pipe;
Described sprayer unit comprises fluidising chamber, be positioned at the air inlet bottom described fluidising chamber and be positioned at the air outlet at described fluidising chamber top, and be arranged on the spraying heat pipe on described fluidising chamber top and the ventilation terminal be arranged on bottom described fluidising chamber, described spraying heat pipe, by being arranged on the first feed space charging of described fluidising chamber outside, described fluidising chamber lateral wall is also provided with the second feed space; Described ventilation terminal comprises cloth wind frame and the uniform intervals wind-distributing pipe in described cloth wind frame arranged in a crossed manner, and the netted gap that described wind-distributing pipe intersects to form is discharging opening, described wind-distributing pipe is provided with the first wind distributing hole, and described wind-distributing pipe is by described air inlet air intake; Be positioned at below described sprayer unit and be provided with anti-collision net above described reclaiming plate;
Described first feed space is connected with disk centrifuge, described disk centrifuge comprises body, rotary drum is provided with in described body, described body top is provided with inlet and outlet device, described inlet and outlet device comprises the material inlet pipe be arranged in parallel, heavy out pipe and light phase export pipe, described material inlet pipe, heavy out pipe and light phase export pipe communicate with described rotary drum, described body side is provided with the deslagging portion and wastewater outlet that communicate with described rotary drum, described wastewater outlet is positioned at the below in described deslagging portion, the side of described body is provided with rinse water import, PLC device is provided with in described deslagging portion,
Described inlet and outlet device comprises the material inlet pipe imported and exported seat and be fixed on described import and export seat, the sidewall of described material inlet pipe is provided with the upper centripetal discharge pump for separating of heavy phase and the lower centripetal discharge pump for separating of light phase, described upper centripetal discharge pump is positioned at the top of described lower centripetal discharge pump, the side of described material inlet pipe is connected with in described material inlet caliber one end to the heavy out pipe extended, and the opposite side of described material inlet pipe is connected with in described material inlet caliber one end to the light phase export pipe extended;
Swine blood protein collecting chamber is provided with bottom described drying device;
Described drying device is connected with the dust collection for collecting the tail gas containing part Swine blood protein; Described dust collection comprises for separating of the cyclone separator of the tail gas containing part Swine blood protein and the dust arrester that communicates with described cyclone separator;
Described cyclone separator is connected with one-level collecting pipe, described one-level collecting pipe is connected with two secondary collecting pipes by the first isocon, described secondary collecting pipe is connected to two three grades of collecting pipes by the second isocon, and described three grades of collecting pipes are connected with dust arrester;
Described cyclone separator outlet is connected with heat exchanger;
Heat conduction disk is provided with in described heat exchanger, described heat conduction disk is circular metal disc, rotating shaft is provided with in the middle of described heat conduction disk, described rotating shaft is vertical with the airflow direction by disk, the two ends of described heat exchanger are respectively equipped with discharge flue and air intake passage, the sidewall of described heat exchanger is provided with transducing hot-blast outlet, and described discharge flue is connected with described cyclone separator, and air inlet and/or the described drying device of described transducing hot-blast outlet and described sprayer unit communicate;
Be provided with between described drier and described dust collection and shunted cribellum; Described cribellum of shunting comprises isocon and spin vibration sieve, and described isocon is provided with equally distributed plural arm, and the top of described drier communicates with described isocon manifold inlet, and described isocon branch outlet communicates with described spin vibration sieve; Described spin vibration sieve top is communicated with described dust collection.
Described deslagging portion is arranged on programmable logic controller (PLC) (PLC) device, regularly quantitative deslagging can be carried out when continuous feed is produced, also total discharge can be carried out when stopping charging, so that the dirt automatically in cleaning rotary drum, have that automaticity is high, advantage to the strong adaptability of technique adjustment, easy to adjust, good separating effect; By the layout of described material inlet pipe, heavy out pipe and light phase export pipe, coordinate the setting in rotary drum and deslagging portion simultaneously, the heavy burder blood cell that density can be made relatively large is flowed out by lower centripetal pump chamber, the light material blood plasma making density relatively little flows out from lower centripetal pump chamber, and the separating property be separated with blood cell pig blood blood plasma is high, effective; By the layout of described material inlet pipe and described upper centripetal discharge pump and lower centripetal discharge pump, coordinate heavy out pipe, light phase export pipe and flow regulator simultaneously, the heavy burder blood cell that density can be made relatively large is flowed out by lower centripetal discharge pump, the light material blood plasma making density relatively little flows out from lower centripetal discharge pump, and the separating property be separated with blood cell pig blood blood plasma is high, effective;
Be connected with the first feed space by disk centrifuge, can make the blood cell of the isolated porcine hemoglobin solution of disk centrifuge, after sprayer unit spraying, be made for hyperglobulinemia polypeptide powder, can fully remove its smell of blood, sensory properties significantly promotes; Hyperglobulinemia polypeptide powder content of ashes is low, and solubility is good, and protein content is high, is especially rich in a large amount of micromolecule polypeptides, and improves the content of several amino acids.The feed nutrition of processing can improve sucking pig immunity, increases antibacterial and to virus inhibitory action.
When adopting technique scheme, normal temperature air is heated to be high-temperature gas through gas generating unit, and high-temperature steam blows to cold pipe from heat pipe, and the air flowing into high-temperature pipe from cryogenic piping is more effectively heated;
Porcine hemoglobin solution sprays in drying device through sprayer unit, and contacts with high-temperature gas, the moisture evaporation in albumen powder;
Sprayer unit adopts special ventilation terminal and does not adopt traditional air distribution plate, and particle is not easy to be deposited on fluidized-bed bottom, and ventilation terminal is leakiness material not; The hot-air that described ventilation terminal flow velocity is adjustable can prevent the parcel number of plies from causing grain density uneven not, does not need follow-up multistage sieve grain, prevents particle too small with regard to discharging; Particle weight must be greater than the just meeting discharging of hot blast blowing force upwards;
Spraying heat pipe sprays the first feed liquid droplet by the first feed space, described second feed space is used for the second material as the charging of granulation crystal seed, feed liquid droplet parcel is sprayed on above crystal seed, and roll in described fluidising chamber under the hot blast of described ventilation terminal blows, multistage and evenly parcel and granulation;
The netted gap that wind-distributing pipe in ventilation terminal the intersects to form matts that such as wind-distributing pipe right-angled intersection is formed serves as the discharging opening of this device simultaneously, simplifies device, reduces cost;
Albumen powder dry is afterwards collected bottom drying tower, tail gas enters cyclone separator and is separated further, and then tail gas enters dust collection and preheater successively, fully can collect the albumen powder in tail gas, and make full use of heat exchanger heat exchange, recovery waste heat;
By the isocon arranged between drier discharge nozzle and spin vibration sieve, make dried material diversion, flow velocity when simultaneously making the discharging flow of drier run with spin vibration sieve mates, thus can evenly sieve, by the albumen powder classification of different-grain diameter, good separating effect;
Heat transmission equipment overall volume is little, can make full use of cryopumping after heat energy, and the air intake of low temperature can abundant contact heat-exchanging face, and heat exchange property is high; The temperature of baking oven Inner eycle hot blast can be improved, thus improve the wet rate of appearance, improve evaporation rate.
As preferably, the pipe ends between described drier and described dust collection is provided with air door.
Near described isocon end pipeline in air door is set, make air flow method evenly, separating effect is better; And can concentrate after mixing a period of time until the protein powder in waste gas and shunt again, reduce operating cost.
As preferably, described fluidising chamber madial wall is symmetrically arranged with crosswind mouth.
Crosswind mouth sticks to fluidising chamber's sidewall for preventing particle, particle deposition can also be prevented in the corner of cloth wind frame simultaneously.
As preferably, described cloth wind frame circumference is provided with the second wind distributing hole; The diameter of described second wind distributing hole is greater than the diameter of described first wind distributing hole.
Hot blast in first wind distributing hole and the second wind distributing hole can pass through air inlet air intake jointly, and the second wind distributing hole contributes to preventing particle deposition further on described wind-distributing pipe.
As preferably, be connected with between described air cleaner and described sprayer unit and be convenient to air blast that air flows into or air pump.
As preferably, the bilateral symmetry of described spraying heat pipe is provided with forges a knife.
That forges a knife arranges the wet environment that can improve mist projection granulating region, prevents local caking, improves bed stability.
As preferably, the upper surface of described first wind distributing hole is provided with the calotte raised up.
The effect one of calotte to change air flow, makes particle even granulation in granulation tower; Two is to prevent less particle from directly leaking down from wind distributing hole.
As preferably, the dust excluding hood that described dust arrester comprises dust removing tube and is connected with described dust removing tube, described dust excluding hood is uniformly distributed on described dust arrester.
As preferably, the sectional area of described one-level collecting pipe is S1, and the sectional area of described secondary collecting pipe is S2, wherein S1=(1.05-1.3) S2.
As preferably, the sectional area of described three grades of collecting pipes is S3, wherein S2=(1.05-1.3) S3.
The collecting pipes at different levels of described match of pipe diameter, when the utility model dust collection is used, energy consumption is lower, more environmental protection.
In sum, the utility model has following beneficial effect: good separating effect, granulation are evenly, good separating effect, recyclability be good and can abundant recovery waste heat.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the utility model Swine blood protein dried recovered device;
Fig. 2 is the top view of the utility model disk centrifuge;
Fig. 3 is the side view of the utility model disk centrifuge;
Fig. 4 is the operating diagram of the utility model disk centrifuge;
Fig. 5 is the utility model heat exchanger sectional view;
Fig. 6 is the schematic diagram of the utility model ventilation terminal;
Fig. 7 is the utility model wind-distributing pipe top view.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Fig. 1-Fig. 7, disk centrifuge 9 comprises body, rotary drum 91 is provided with in body, body top is provided with inlet and outlet device 92, inlet and outlet device 92 comprises the material inlet pipe 922, heavy out pipe 925 and the light phase export pipe 926 that are arranged in parallel, material inlet pipe 922, heavy out pipe 925 and light phase export pipe 926 communicate with rotary drum 91, body side is provided with the deslagging portion 93 and wastewater outlet 94 that communicate with rotary drum 91, wastewater outlet 94 is positioned at the below in deslagging portion 93, the side of body is provided with rinse water import 95, is provided with PLC device in deslagging portion 93;
Inlet and outlet device 92 comprises to be imported and exported seat 921 and is fixed on the material inlet pipe 922 imported and exported on seat 921, the sidewall of material inlet pipe 922 is provided with the upper centripetal discharge pump 923 for separating of heavy phase and the lower centripetal discharge pump 924 for separating of light phase, upper centripetal discharge pump 923 is positioned at the top of lower centripetal discharge pump 924, the side of material inlet pipe 922 is connected with the one end of the heavy out pipe 925 extended in material inlet pipe 922 radial direction, and the opposite side of material inlet pipe 922 is connected with the one end of the light phase export pipe 926 extended in material inlet pipe 922 radial direction.
Air cleaner 1 is connected with drying device 2 entrance for dry Swine blood protein; Drying device 2 entrance is also connected with the sprayer unit 3 for making the granulation of porcine hemoglobin solution become Swine blood protein;
Be connected with for adding hot-air thus providing the air heater 4 of hot-air between air cleaner 1 and drying device 2;
Air heater 4 comprises chamber 41, top and chamber, the end 42; The output cavity 412 that chamber 41, top is divided into the input cavity 411 for inputting for air to be heated by dividing plate 410 and is exported for heating air; Be communicated with cold pipe 43 between input cavity 411 and chamber, the end 42, between output cavity 412 and chamber, the end 42, be communicated with heat pipe 44; High-temperature steam blows to cold pipe from heat pipe; The air flowing into high-temperature pipe from cryogenic piping is more effectively heated;
Sprayer unit 3 comprises fluidising chamber 31, be positioned at the air inlet 32 bottom fluidising chamber 31 and be positioned at the air outlet 33 at fluidising chamber 31 top, and be arranged on the spraying heat pipe 34 on fluidising chamber 31 top and the ventilation terminal 35 be arranged on bottom fluidising chamber 31, spraying heat pipe 34, by being arranged on the first feed space 36 charging of fluidising chamber 31 outside, fluidising chamber 31 lateral wall is also provided with the second feed space 37; Ventilation terminal 35 comprises cloth wind frame 352 and the uniform intervals wind-distributing pipe 351 in cloth wind frame 352 arranged in a crossed manner, the netted gap that wind-distributing pipe 351 intersects to form is discharging opening 312, wind-distributing pipe 351 is provided with the first wind distributing hole 3511, wind-distributing pipe 351 is by air inlet 32 air intake; Be positioned at below sprayer unit and be provided with anti-collision net 39 above reclaiming plate;
In order to obtain better spraying dry effect, crosswind mouth 38 can be symmetrical arranged on fluidising chamber 31 madial wall; Second wind distributing hole 3521 can also be set in cloth wind frame 352 circumference; And the calotte 3512 raised up is set on the upper surface of the first wind distributing hole 3511.The diameter of the second wind distributing hole 3521 is greater than the diameter of the first wind distributing hole 3511.Liquid caking during in order to prevent from spraying, can be provided with in the bilateral symmetry of spraying heat pipe 34 and forge a knife 310.
Air cleaner 1 communicates with air inlet 32; Flow into for ease of air, between air cleaner 1 with sprayer unit 3, be connected air blast or air pump 10.
First feed space 36 connects disk centrifuge 9.Disk centrifuge is connected with the first feed space 36, the blood cell of the isolated porcine hemoglobin solution of disk centrifuge can be made, after sprayer unit 3 is sprayed, be made for hyperglobulinemia polypeptide powder, can fully remove its smell of blood.
Swine blood protein collecting chamber 21 is provided with, in order to the Swine blood protein got off by gravitational settling that collecting granules is larger bottom drying device 2;
Drying device 2 is connected with the dust collection 5 for collecting the tail gas containing part Swine blood protein; Dust collection 5 comprises for separating of the cyclone separator 54 of the tail gas containing part Swine blood protein and the dust arrester 55 that communicates with cyclone separator 54;
In order to can evenly sieve, by the albumen powder classification of different-grain diameter, be provided with between good separating effect drier 2 and dust collection 5 and shunted cribellum 7; Shunted cribellum 7 and comprise isocon 71 and spin vibration sieve 72, isocon 71 is provided with equally distributed plural arm, and the top of drier 2 communicates with isocon 71 manifold inlet, and isocon 71 branch outlet communicates with spin vibration sieve 72; Spin vibration sieve 72 top is communicated with dust collection 5.
In order to make air flow method evenly, the pipe ends between drier 2 and dust collection 5 is provided with air door 8.
Cyclone separator 54 is connected with one-level collecting pipe 51, one-level collecting pipe 51 is connected with two secondary collecting pipes 52 by the first isocon 56, secondary collecting pipe 52 is connected to two three grades of collecting pipes, 53, three grades of collecting pipes 53 by the second isocon 59 and is connected with dust arrester 55; The dust excluding hood 552 that dust arrester 55 comprises dust removing tube 551 and is connected with dust removing tube 551, dust excluding hood 552 is uniformly distributed on dust arrester 55.
For improving shunting effect, the sectional area of one-level collecting pipe 51 is S1, and the sectional area of secondary collecting pipe 52 is S2, wherein S1=1.05-1.3S2.The sectional area of three grades of collecting pipes 53 is S3, wherein S2=1.05-1.3S3.
In order to make full use of waste heat, cyclone separator 54 outlet is connected with heat exchanger 6; Heat exchanger 6 outlet communicates with air inlet 32; Or heat exchanger 6 outlet communicates with drying device 2.
For improving recuperation of heat and heat transfer effect, heat conduction disk 64 is provided with in heat exchanger 6, heat conduction disk 64 is circular metal disc, rotating shaft 641 is provided with in the middle of heat conduction disk 64, rotating shaft 641 is vertical with the airflow direction by disk 64, the two ends of heat exchanger 6 are respectively equipped with discharge flue 61 and air intake passage 62, and the sidewall of heat exchanger 62 is provided with transducing hot-blast outlet 63, and discharge flue 61 is connected with cyclone separator 54.
This specific embodiment is only to explanation of the present utility model; it is not to restriction of the present utility model; those skilled in the art can make to the present embodiment the amendment not having creative contribution as required after reading this description, as long as but be all subject to the protection of Patent Law in right of the present utility model.

Claims (10)

1. a Swine blood protein dried recovered device, comprising the air cleaner (1) for providing clean air, it is characterized in that: described air cleaner (1) is connected with drier (2) entrance for dry Swine blood protein; Described drier (2) entrance is also connected with the sprayer unit (3) for making the granulation of porcine hemoglobin solution become Swine blood protein;
Be connected with for adding hot-air thus providing the air heater (4) of hot-air between described air cleaner (1) and described drier (2);
Described air heater (4) comprises chamber, top (41) and chamber, the end (42); The output cavity (412) that chamber, described top (41) is divided into the input cavity (411) for inputting for air to be heated by dividing plate (410) and is exported for heating air; Be communicated with cold pipe (43) between described input cavity (411) and chamber, the described end (42), between described output cavity (412) and chamber, the described end (42), be communicated with heat pipe (44);
Described sprayer unit (3) comprises fluidising chamber (31), is positioned at the air inlet (32) of described fluidising chamber (31) bottom and is positioned at the air outlet (33) at described fluidising chamber (31) top, and be arranged on the spraying heat pipe (34) on described fluidising chamber (31) top and be arranged on the ventilation terminal (35) of described fluidising chamber (31) bottom, described spraying heat pipe (34), by being arranged on outside the first feed space (36) charging of described fluidising chamber (31), described fluidising chamber (31) lateral wall is also provided with the second feed space (37); Described ventilation terminal (35) comprises cloth wind frame (352) and the uniform intervals wind-distributing pipe (351) in described cloth wind frame (352) arranged in a crossed manner, the netted gap that described wind-distributing pipe (351) intersects to form is discharging opening (312), described wind-distributing pipe (351) is provided with the first wind distributing hole (3511), described wind-distributing pipe (351) is by described air inlet (32) air intake; Be positioned at below described sprayer unit and be provided with anti-collision net (39) above described reclaiming plate;
Described first feed space (36) is connected with disk centrifuge (9), described disk centrifuge (9) comprises body, rotary drum (91) is provided with in described body, described body top is provided with inlet and outlet device (92), described inlet and outlet device (92) comprises the material inlet pipe (922) be arranged in parallel, heavy out pipe (925) and light phase export pipe (926), described material inlet pipe (922), heavy out pipe (925) and light phase export pipe (926) communicate with described rotary drum (91), described body side is provided with the deslagging portion (93) and wastewater outlet (94) that communicate with described rotary drum (91), described wastewater outlet (94) is positioned at the below of described deslagging portion (93), the side of described body is provided with rinse water import (95), PLC device is provided with in described deslagging portion (93),
Described inlet and outlet device (92) comprises the material inlet pipe (922) imported and exported seat (921) and be fixed on described import and export seat (921), the sidewall of described material inlet pipe (922) is provided with the upper centripetal discharge pump (923) for separating of heavy phase and the lower centripetal discharge pump (924) for separating of light phase, described upper centripetal discharge pump (923) is positioned at the top of described lower centripetal discharge pump (924), the side of described material inlet pipe (922) is connected with the one end of the heavy out pipe (925) extended in described material inlet pipe (922) radial direction, the opposite side of described material inlet pipe (922) is connected with the one end of the light phase export pipe (926) extended in described material inlet pipe (922) radial direction,
Described drier (2) bottom is provided with Swine blood protein collecting chamber (21);
Described drier (2) is connected with the dust collection (5) for collecting the tail gas containing part Swine blood protein; Described dust collection (5) comprises for separating of the cyclone separator (54) of the tail gas containing part Swine blood protein and the dust arrester (55) that communicates with described cyclone separator (54);
Described cyclone separator (54) is connected with one-level collecting pipe (51), described one-level collecting pipe (51) is connected with two secondary collecting pipes (52) by the first isocon (56), described secondary collecting pipe (52) is connected to two three grades collecting pipes (53) by the second isocon (59), and described three grades of collecting pipes (53) are connected with dust arrester (55);
Described cyclone separator (54) outlet is connected with heat exchanger (6);
Heat conduction disk (64) is provided with in described heat exchanger (6), described heat conduction disk (64) is circular metal disc, rotating shaft (641) is provided with in the middle of described heat conduction disk (64), described rotating shaft (641) is vertical with the airflow direction by disk (64), the two ends of described heat exchanger (6) are respectively equipped with discharge flue (61) and air intake passage (62), the sidewall of described heat exchanger (62) is provided with transducing hot-blast outlet (63), described discharge flue (61) is connected with described cyclone separator (54), air inlet (32) and/or described drier (2) air intake of described transducing hot-blast outlet (63) and described sprayer unit (3) communicate,
Be provided with between described drier (2) and described dust collection (5) and shunted cribellum (7); Described cribellum (7) of shunting comprises isocon (71) and spin vibration sieve (72), described isocon (71) is provided with equally distributed plural arm, the top of described drier (2) communicates with described isocon (71) manifold inlet, and described isocon (71) branch outlet communicates with described spin vibration sieve (72); Described spin vibration sieve (72) top is communicated with described dust collection (5).
2. a kind of Swine blood protein dried recovered device according to claim 1, is characterized in that: the pipe ends between described drier (2) and described dust collection (5) is provided with air door (8).
3. a kind of Swine blood protein dried recovered device according to claim 1, is characterized in that: described fluidising chamber (31) madial wall is symmetrically arranged with crosswind mouth (38).
4. a kind of Swine blood protein dried recovered device according to claim 1, is characterized in that: described cloth wind frame (352) circumference is provided with the second wind distributing hole (3521); The diameter of described second wind distributing hole (3521) is greater than the diameter of described first wind distributing hole (3511).
5. a kind of Swine blood protein dried recovered device according to claim 1, is characterized in that: be connected with between described air cleaner (1) and described sprayer unit (3) and be convenient to air blast that air flows into or air pump (10).
6. a kind of Swine blood protein dried recovered device according to any one of claim 1-5, is characterized in that: the bilateral symmetry of described spraying heat pipe (34) is provided with forge a knife (310).
7. a kind of Swine blood protein dried recovered device according to claim 6, is characterized in that: the upper surface of described first wind distributing hole (3511) is provided with the calotte (3512) raised up.
8. a kind of Swine blood protein dried recovered device according to claim 7, it is characterized in that: the dust excluding hood (552) that described dust arrester (55) comprises dust removing tube (551) and is connected with described dust removing tube (551), described dust excluding hood (552) is uniformly distributed on described dust arrester (55).
9. a kind of Swine blood protein dried recovered device according to claim 8, it is characterized in that: the sectional area of described one-level collecting pipe (51) is S1, the sectional area of described secondary collecting pipe (52) is S2, wherein S1=(1.05-1.3) S2.
10. a kind of Swine blood protein dried recovered device according to claim 9, is characterized in that: the sectional area of described three grades of collecting pipes (53) is S3, wherein S2=(1.05-1.3) S3.
CN201420598082.XU 2014-10-16 2014-10-16 A kind of Swine blood protein dried recovered device Expired - Fee Related CN204121789U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420598082.XU CN204121789U (en) 2014-10-16 2014-10-16 A kind of Swine blood protein dried recovered device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420598082.XU CN204121789U (en) 2014-10-16 2014-10-16 A kind of Swine blood protein dried recovered device

Publications (1)

Publication Number Publication Date
CN204121789U true CN204121789U (en) 2015-01-28

Family

ID=52378179

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420598082.XU Expired - Fee Related CN204121789U (en) 2014-10-16 2014-10-16 A kind of Swine blood protein dried recovered device

Country Status (1)

Country Link
CN (1) CN204121789U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104399262A (en) * 2014-10-16 2015-03-11 浙江索纳克生物科技有限公司 Porcine blood protein powder drying and recycling apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104399262A (en) * 2014-10-16 2015-03-11 浙江索纳克生物科技有限公司 Porcine blood protein powder drying and recycling apparatus

Similar Documents

Publication Publication Date Title
CN102091566A (en) One-step granulating and drying equipment with fluidized bed
CN211800650U (en) Pressure spray granulator
CN204121789U (en) A kind of Swine blood protein dried recovered device
CN104399262B (en) A kind of Swine blood protein dried recovered device
CN205042132U (en) Novel spray drier
CN204619401U (en) A kind of spray dryer
CN103920299A (en) Spray drying system for wall-attaching materials
CN104365998A (en) Pig blood globulin powder preparation device
CN204104721U (en) A kind of proteinic powder of porcine preparation facilities with air preheat function
CN203790303U (en) Fluid-bed granulator for drug preparation
CN204104720U (en) A kind of proteinic powder of porcine preparation facilities
CN207881352U (en) A kind of Chinese medicine preparation spouted bed drying device
CN204104793U (en) A kind of clean proteinic powder of porcine preparation facilities
CN204104718U (en) A kind of pig blood reusing appts of mist projection granulating
CN205965060U (en) High -speed centrifugal spray drying equipment suitable for preparation dibazolum capsule
CN206881161U (en) A kind of rice protein powder production centrifugal spray drying tower
CN206511932U (en) A kind of graininess anhydrous calcium chloride continuous production device
CN104397856B (en) A kind of clean proteinic powder of porcine preparation facilities
CN202186954U (en) Spray drying device
CN201940207U (en) Granulating and drying device of one-step fluidized bed
CN204193878U (en) A kind of Swine blood protein separator
CN204104717U (en) A kind of Swine blood protein reclaims heat-exchanger rig
CN104258784B (en) A kind of Swine blood protein separator
CN104397327A (en) Pig blood protein powder forming granulation apparatus
CN204104719U (en) A kind of Swine blood protein formed granulating device

Legal Events

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

Granted publication date: 20150128

Termination date: 20161016

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