CN204104717U - A kind of Swine blood protein reclaims heat-exchanger rig - Google Patents
A kind of Swine blood protein reclaims heat-exchanger rig Download PDFInfo
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- CN204104717U CN204104717U CN201420598098.0U CN201420598098U CN204104717U CN 204104717 U CN204104717 U CN 204104717U CN 201420598098 U CN201420598098 U CN 201420598098U CN 204104717 U CN204104717 U CN 204104717U
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- blood protein
- swine blood
- air
- drying device
- exchanger rig
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Abstract
The utility model relates to the recycling treating apparatus of a boar blood, and particularly a kind of Swine blood protein reclaims heat-exchanger rig.It comprises the air cleaner for providing clean air, and its air cleaner connects drying device first entrance; Drying device second entrance connects sprayer unit; Air heater is connected between air cleaner with drying device; Sprayer unit comprise granulating fluidized bed, be arranged on forging a knife of granulating fluidized bed sidewall, the bilateral symmetry of forging a knife arranges twin fluid atomization spray gun, arrange air intake and feed liquid port in twin fluid atomization spray gun, granulating fluidized bed bottom is provided with ventilation terminal, is provided with discharge chamber below ventilation terminal; Swine blood protein collecting chamber is provided with bottom drying device; Drying device is connected with dust collection; The dust arrester that dust collection comprises cyclone separator and communicates with cyclone separator; Cyclone separator outlet is connected with heat exchanger.The utility model granulation is even, recyclability good, abundant recovery waste heat.
Description
Technical field
The utility model relates to the recycling treating apparatus of a boar blood, and particularly a kind of Swine blood protein reclaims heat-exchanger rig.
Background technology
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 granulation is even, recyclability good and the Swine blood protein of abundant recovery waste heat can reclaims heat-exchanger rig.
Above-mentioned technical purpose of the present utility model is achieved by the following technical programs:
A kind of Swine blood protein reclaims heat-exchanger rig, and comprise the air cleaner for providing clean air, air cleaner described in it is connected with drying device first entrance for dry Swine blood protein; Described drying device second entrance is 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 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;
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.
When adopting technique scheme, normal temperature air is heated to be high-temperature gas through gas generating unit, and 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.
As preferably, described heat exchanger outlet communicates with the described twin fluid atomization spray gun air intake that is connected.
As preferably, described heat exchanger outlet communicates with described drying device.
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; 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: granulation is even, recyclability good and energy fully recovery waste heat.
Accompanying drawing explanation
Fig. 1 is the schematic diagram that the utility model Swine blood protein reclaims heat-exchanger rig;
Fig. 2 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. 2, Swine blood protein recovery heat-exchanger rig comprises the air cleaner 1 for providing clean air, and air cleaner 1 is connected with drying device 2 first entrance for dry Swine blood protein; Drying device 2 second entrance is 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 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.
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;
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 is connected with twin fluid atomization spray gun 31 air intake or drying device 2;
Heat exchanger 6 exports and is connected twin fluid atomization spray gun 31 and/or drying device 2 air intake communicates.
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.
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. Swine blood protein reclaims a heat-exchanger rig, comprising the air cleaner (1) for providing clean air, it is characterized in that:
Described air cleaner (1) is connected with drying device (2) first entrance for dry Swine blood protein; Described drying device (2) second entrance is 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 drying device (2);
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 drying device (2) bottom is provided with Swine blood protein collecting chamber (21);
Described drying device (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).
2. a kind of Swine blood protein according to claim 1 reclaims heat-exchanger rig, it is characterized in that: described heat exchanger (6) outlet communicates with described twin fluid atomization spray gun (31) air intake that is connected.
3. a kind of Swine blood protein according to claim 1 reclaims heat-exchanger rig, it is characterized in that: described heat exchanger (6) outlet communicates with described drying device (2).
4. a kind of Swine blood protein according to claim 1 reclaims heat-exchanger rig, it is characterized in that: described air cleaner (1) communicates with described twin fluid atomization spray gun (31) air intake.
5. a kind of Swine blood protein according to claim 1 reclaims heat-exchanger rig, it 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 according to any one of claim 1-5 reclaims heat-exchanger rig, it 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 Swine blood protein according to claim 6 reclaims heat-exchanger rig, it is characterized in that: (33) are provided with wind distributing hole to described ventilation terminal, and described wind distributing hole is circular or oval; The upper surface of described wind distributing hole is provided with the calotte (331) raised up.
8. a kind of Swine blood protein according to claim 7 reclaims heat-exchanger rig, 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 according to claim 8 reclaims heat-exchanger rig, and 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 according to claim 9 reclaims heat-exchanger rig, it 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 |
|---|---|---|---|
| CN201420598098.0U CN204104717U (en) | 2014-10-16 | 2014-10-16 | A kind of Swine blood protein reclaims heat-exchanger rig |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420598098.0U CN204104717U (en) | 2014-10-16 | 2014-10-16 | A kind of Swine blood protein reclaims heat-exchanger rig |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204104717U true CN204104717U (en) | 2015-01-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420598098.0U Expired - Fee Related CN204104717U (en) | 2014-10-16 | 2014-10-16 | A kind of Swine blood protein reclaims heat-exchanger rig |
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| Country | Link |
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| CN (1) | CN204104717U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104397328A (en) * | 2014-10-16 | 2015-03-11 | 浙江索纳克生物科技有限公司 | Pig blood protein powder recovery heat-exchange apparatus |
-
2014
- 2014-10-16 CN CN201420598098.0U patent/CN204104717U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104397328A (en) * | 2014-10-16 | 2015-03-11 | 浙江索纳克生物科技有限公司 | Pig blood protein powder recovery heat-exchange apparatus |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150121 Termination date: 20161016 |
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| CF01 | Termination of patent right due to non-payment of annual fee |