CN204104793U - A kind of clean proteinic powder of porcine preparation facilities - Google Patents
A kind of clean proteinic powder of porcine preparation facilities Download PDFInfo
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- CN204104793U CN204104793U CN201420598380.9U CN201420598380U CN204104793U CN 204104793 U CN204104793 U CN 204104793U CN 201420598380 U CN201420598380 U CN 201420598380U CN 204104793 U CN204104793 U CN 204104793U
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Abstract
The utility model relates to the recycling treating apparatus of pig blood, particularly a kind of clean proteinic powder of porcine preparation facilities.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 the parallel light calandria heat exchanger alternately arranged, be provided with between light calandria heat exchanger comprise inspection hatch hollow every road, light calandria heat exchanger both sides are provided with air inlet and the air outlet being connected sprayer unit; Sprayer unit twin fluid atomization spray gun feed liquid port 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; Dryer export is connected with storage tank, and reservoir inlet place is provided with magnetic separator.The utility model granulation is even, clean separation is effective, good, the abundant recovery waste heat of recyclability.
Description
Technical field
The utility model relates to the recycling treating apparatus of pig blood, particularly a kind of clean proteinic powder of porcine preparation facilities.
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 that a kind of clean separation is effective, granulation is even, recyclability is good and can the clean proteinic powder of porcine preparation facilities of abundant recovery waste heat.
Above-mentioned technical purpose of the present utility model is achieved by the following technical programs:
A clean proteinic powder of porcine preparation facilities, comprises the air cleaner for providing clean air, and 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 the parallel light calandria heat exchanger alternately arranged, be provided with between described smooth calandria heat exchanger comprise inspection hatch hollow every road, described smooth calandria heat exchanger both sides are provided with air inlet and the air outlet being connected described sprayer unit; Described sprayer unit comprise granulating fluidized bed, be arranged on forging a knife of described granulating fluidized bed sidewall, described bilateral symmetry of forging a knife is provided with twin fluid atomization spray gun, air intake and feed liquid port is provided with in described twin fluid atomization spray gun, described granulating fluidized bed bottom is provided with ventilation terminal, is provided with discharge chamber below described ventilation terminal;
Described twin fluid atomization spray gun feed liquid port 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, described discharge flue is connected with described cyclone separator, and described transducing hot-blast outlet communicates with described twin fluid atomization spray gun air intake and/or described drying device;
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 dryer export is connected with storage tank, and described reservoir inlet place is provided with the magnetic separator for removal of impurities.
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;
Disk centrifuge is connected with twin fluid atomization spray gun feed liquid port, the blood cell of the isolated porcine hemoglobin solution of disk centrifuge can be made, after twin fluid atomization gun 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 forge a knife and twin fluid atomization spray gun the wet environment that can improve mist projection granulating region is set, prevent local caking, improve the uniformity of bed stability and granulation; Connect drying device outward at discharge chamber, premix delicious and crisp good palatability, uniform particles, size is even, and spray when can prevent the spraying in fluid bed from not yet participating in granulation dried, granular size differs;
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 air cleaner communicates with described twin fluid atomization spray gun air intake.
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, described twin fluid atomization spray gun is tilted to down, is 5 °-10 ° with the angle of horizontal plane.
The location arrangements of twin fluid atomization spray gun can make the auxiliary fluidization of forging a knife better.
As preferably, described ventilation terminal is provided with wind distributing hole, described wind distributing hole is circular or oval.
As preferably, the upper surface of described 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: clean separation is effective, granulation is even, good separating effect, recyclability are good and energy fully recovery waste heat.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the proteinic powder of porcine preparation facilities that the utility model cleans;
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.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in figure-Fig. 5, 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;
In order to improve heating effect, reduce air drag, air heater 4 comprises the parallel light calandria heat exchanger 41 alternately arranged, be provided with between light calandria heat exchanger 41 comprise inspection hatch 42 hollow every road 43, light calandria heat exchanger 41 both sides are provided with air inlet 44 and the air outlet 45 being connected sprayer unit 3; Inspection hatch can check duty and the operating efficiency of light calandria heat exchanger 41; Air cleaner 1 communicates with twin fluid atomization spray gun 31 air intake; Flow into for ease of air, between air cleaner 1 with sprayer unit 3, be connected air blast or air pump 10.
Sprayer unit 3 comprise granulating fluidized bed 37, be arranged on granulating fluidized bed 37 sidewalls forge a knife 32, forge a knife 32 bilateral symmetry be provided with twin fluid atomization spray gun 31, air intake and feed liquid port is provided with in twin fluid atomization spray gun 31, the bottom of granulating fluidized bed 37 is provided with ventilation terminal 33, is provided with discharge chamber 35 below ventilation terminal 33; Ventilation terminal 33 is provided with wind distributing hole, and it is circular or oval that wind distributing hole can be set to rectangle; For improving cloth wind effect, the upper surface of wind distributing hole is provided with the calotte 331 raised up.For mist projection granulating better effects if, twin fluid atomization spray gun 31 is tilted to down, is 5 °-10 ° with the angle of horizontal plane.
Twin fluid atomization spray gun 31 feed liquid port connects disk centrifuge 9.Disk centrifuge is connected with twin fluid atomization spray gun feed liquid port, the blood cell of the isolated porcine hemoglobin solution of disk centrifuge can be made, after twin fluid atomization gun spraying, 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 twin fluid atomization spray gun 31 air intake; 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, the sidewall of heat exchanger 62 is provided with transducing hot-blast outlet 63, discharge flue 61 is connected with cyclone separator 54, and transducing hot-blast outlet 63 communicates with twin fluid atomization spray gun 31 air intake and/or drying device 2;
Drier 2 outlet is connected with storage tank 11, and storage tank 11 porch is provided with the magnetic separator 12 for removal of impurities, and the metal species Impurity removal that can preferentially will drop in pre-treatment step or be mingled with, plays abundant cleaning effect.
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 clean proteinic powder of porcine preparation facilities, 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 the parallel light calandria heat exchanger (41) alternately arranged, be provided with between described smooth calandria heat exchanger (41) comprise inspection hatch (42) hollow every road (43), described smooth calandria heat exchanger (41) both sides are provided with air inlet (44) and the air outlet (45) being connected described sprayer unit (3);
Described sprayer unit (3) comprises granulating fluidized bed (37), is arranged on forge a knife (32) of described granulating fluidized bed (37) sidewall, described bilateral symmetry of forging a knife (32) is provided with twin fluid atomization spray gun (31), air intake and feed liquid port is provided with in described twin fluid atomization spray gun (31), the bottom of described granulating fluidized bed (37) is provided with ventilation terminal (33), and described ventilation terminal (33) below is provided with discharge chamber (35);
Described twin fluid atomization spray gun (31) feed liquid port 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), described transducing hot-blast outlet (63) communicates with described twin fluid atomization spray gun (31) and/or described drier (2) air intake,
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);
Described drier (2) outlet is connected with storage tank (11), and described storage tank (11) porch is provided with the magnetic separator (12) for removal of impurities.
2. a kind of clean proteinic powder of porcine preparation facilities 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 clean proteinic powder of porcine preparation facilities according to claim 1, is characterized in that: (33) are provided with wind distributing hole to described ventilation terminal, and described wind distributing hole is rectangle, circle or oval.
4. a kind of clean proteinic powder of porcine preparation facilities according to claim 1, is characterized in that: described air cleaner (1) communicates with described twin fluid atomization spray gun (31) air intake.
5. a kind of clean proteinic powder of porcine preparation facilities 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); Described air inlet (44) connects described air blast or air pump (10) outlet.
6. a kind of clean proteinic powder of porcine preparation facilities according to any one of claim 1-5, is characterized in that: described twin fluid atomization spray gun (31) is tilted to down, is 5 °-10 ° with the angle of horizontal plane.
7. a kind of clean proteinic powder of porcine preparation facilities according to claim 6, is characterized in that: the upper surface of described wind distributing hole is provided with the calotte (331) raised up.
8. a kind of clean proteinic powder of porcine preparation facilities 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 clean proteinic powder of porcine preparation facilities 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 clean proteinic powder of porcine preparation facilities 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201420598380.9U CN204104793U (en) | 2014-10-16 | 2014-10-16 | A kind of clean proteinic powder of porcine preparation facilities |
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| CN201420598380.9U CN204104793U (en) | 2014-10-16 | 2014-10-16 | A kind of clean proteinic powder of porcine preparation facilities |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104397856A (en) * | 2014-10-16 | 2015-03-11 | 浙江索纳克生物科技有限公司 | Preparation device for clean porcine blood cell protein powder |
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2014
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104397856A (en) * | 2014-10-16 | 2015-03-11 | 浙江索纳克生物科技有限公司 | Preparation device for clean porcine blood cell protein powder |
| CN104397856B (en) * | 2014-10-16 | 2016-04-13 | 浙江索纳克生物科技有限公司 | A kind of clean proteinic powder of porcine preparation facilities |
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Granted publication date: 20150121 Termination date: 20161016 |
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| CF01 | Termination of patent right due to non-payment of annual fee |