CN109158170A - A kind of vegetable fat raw material breaking method - Google Patents
A kind of vegetable fat raw material breaking method Download PDFInfo
- Publication number
- CN109158170A CN109158170A CN201811013764.9A CN201811013764A CN109158170A CN 109158170 A CN109158170 A CN 109158170A CN 201811013764 A CN201811013764 A CN 201811013764A CN 109158170 A CN109158170 A CN 109158170A
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- China
- Prior art keywords
- cylinder
- pulverization cylinder
- vegetable fat
- raw material
- fat raw
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/067—Tub-grinders
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
- B02C18/18—Knives; Mountings thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
- B02C18/22—Feed or discharge means
- B02C18/2216—Discharge means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
- B02C18/22—Feed or discharge means
- B02C18/2225—Feed means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
- B02C18/24—Drives
Abstract
A kind of vegetable fat raw material breaking method belongs to oil plant crushing technology field.It is characterized by: pulverization cylinder (1) outer coaxial sleeve is equipped with outer cylinder (3), it often is provided with the feeding port (101) for being connected to feed cavity with pulverization cylinder (1) inner cavity on the pulverization cylinder (1) between two connected stationary knifes (8), is provided with striker plate (11) outside each feeding port (101)；Vegetable fat raw material and complexed surfactant 100:0.7 ~ 1.9 in mass ratio are added in pulverization cylinder (1) and are crushed together, complexed surfactant is eight polyglyceryl palmitate and the complexed surfactant that six polyglycereol monolaurates, 17 ~ 26:44 ~ 53 in mass ratio are combined.This breaking method can directly crush the biggish vegetable fat raw material of viscosity, and good crushing effect, and grease separation is simple and convenient after crushing, and oil yield is high.
Description
Technical field
A kind of vegetable fat raw material breaking method belongs to oil plant crushing technology field.
Background technique
Material is crushed before extraction, to improve the speed of effective component proposition and the extracting rate of effective component.
Existing material-pulverizing device largely crushes material by way of shearing, that is, passes through the cooperation pair of moving knife and stationary knife
Material is crushed, and this grinding mode effect when crushing to dry material is fine, but when to oiliness crushing material,
Due to that can be deposited in the gap between stationary knife after oiliness crushing material, moving knife during rotation can be with the object in stationary knife gap
Expect frictional heating, causes material and device temperature excessively high, that is, affect the crushing of material, and have certain damage to equipment.
Summary of the invention
The technical problem to be solved by the present invention is overcoming the deficiencies of the prior art and provide one kind avoids material accumulation, grease
Separate simply and easily vegetable fat raw material breaking method.
The technical solution adopted by the present invention to solve the technical problems is: the vegetable fat raw material breaking method, feature
Be: grinding device used includes vertically arranged pulverization cylinder and the turntable that is co-axially located in pulverization cylinder, around crushing
The inner wall of cylinder is arranged at intervals with multiple stationary knifes, is arranged at intervals with multiple moving knife around the side of turntable, turntable is connected with motor, institute
The outer coaxial sleeve of the pulverization cylinder stated is equipped with outer cylinder, and outer cylinder and pulverization cylinder interval are arranged to form discharging chamber, often two connected stationary knifes it
Between pulverization cylinder on be provided with feed cavity be provided with backgauge with the feeding port that be connected to of tube inner chamber, each feeding port is crushed outside
Plate, striker plate outside, which is provided with, pushes striker plate by the closed elastic module of feeding port, and discharging chamber downside is connected with discharging cylinder；
Crushing process are as follows: after starting motor, vegetable fat raw material and complexed surfactant 100:0.7 ~ 1.9 in mass ratio are added
Enter into pulverization cylinder, the complexed surfactant is that eight polyglyceryl palmitate and six polyglycereol monolaurates press quality
The complexed surfactant being combined than 17 ~ 26:44 ~ 53；Elastic module pushes striker plate to close feeding port, in pulverization cylinder
The mixed material of vegetable fat raw material and complexed surfactant crushes during the relative motion of stationary knife and moving knife, works as phase
When mixed material accumulation between adjacent stationary knife is excessive, moving knife pushes striker plate automatically to beat feeding port the pressure of mixed material
It opens, smashed mixed material enters in discharging cylinder；
After the every crushing 15min ~ 55min of mixed material, i.e., carried out to 0.2 ~ 1.5 times of the water that mixed material quality is added in pulverization cylinder
8s ~ 20s is rinsed, flushing water enters in discharging cylinder the wet pulp that crushing is mixed to get with smashed mixed material.
The present invention realizes the fast-crushing of this viscous material of vegetable fat raw material, outside the pulverization cylinder of grinding device used
It is provided with discharging chamber, elastic module pushes striker plate to close feeding port, when the material accumulation between adjacent stationary knife is excessive, moves
Knife pushes striker plate to open feeding port the pressure of material, and material enters in discharging cylinder, avoids that material viscosity is excessive to be led
It causes material to stay in the gap between stationary knife, so that the fever of equipment will not be caused, keeps this grinding device directly viscous to having
The material of property is crushed, and good crushing effect.In the crushing process of vegetable fat raw material, inventor is added using special
The surface for crushing broken oil plant is modified by the compound obtained complexed surfactant of long-chain and middle long-chain, not only can be greatly
Crushing rear material is reduced to the adhesion of pulverization cylinder, effectively prevents from gathering blocking；And make protein in broken oil plant at
Part is affine with pure water compared to being easier with oil plant, while being easy to be separated from water under external force again；And the present invention is in crushing process
In be rinsed with water, rinse cooling while obtain be crush wet pulp, can greatly simplify comminuting matter in subsequent step
Grease separated with oil plant slag.Due to the effect of the complexed surfactant of addition when subsequent grease separates, grease is from protein
Middle separation is quickly floated under the action of water, and the grease on upper layer can be contacted no longer with oil plant slag, so as to easily separate
Grease can be such that grease therein more completely leaches, and oil yield is greatly improved, while oil plant is gone out by water logging, guarantee
It is safe and nontoxic.The separation of grease and water is simpler, easy to operate.
The upper end of the pulverization cylinder and outer cylinder is all closed setting, is provided on the upside of outer cylinder and crushes what tube inner chamber was connected to
Feed pipe and inlet tube；The vegetable fat raw material by feed pipe be added pulverization cylinder in, the complexed surfactant and
Water is added in pulverization cylinder by inlet tube.Vegetable fat raw material and complexed surfactant are separately added into, and can better ensure that original
Expect smooth into pulverization cylinder.In the case where not needing in advance to mix the two, directly add in proportion respectively, it can be quick
Uniformly mixing.
It is the taper that diameter is gradually increased from the bottom to top on the upside of turntable, turntable is arranged in the feed pipe and inlet tube
Upside.Feed enhanced convenience.The upside of turntable is taper, can uniformly be delivered in pulverization cylinder material, material is avoided to exist
Pulverization cylinder is accumulated close to the side of feed pipe.
Further include the main shaft with pulverization cylinder coaxial arrangement, turntable is connected with main shaft and rotates synchronously with main shaft, motor it is defeated
Shaft is connected with main shaft.
Discharge barrel is provided on the downside of the pulverization cylinder, discharge barrel is arranged in discharging cylinder, and discharging cylinder inner wall and discharging
The setting of drum outer wall interval.
Crushing is added to after the vegetable fat raw material and complexed surfactant 100:1.1 in mass ratio ~ 1.4 mixing
In cylinder.The additional amount of preferred complexed surfactant can be better protected from material and be attached to pulverization cylinder barrel, stationary knife and move
On knife, and grease and Separation of Proteins are more thorough.
The complexed surfactant be eight polyglyceryl palmitate and six polyglycereol monolaurates in mass ratio 19 ~
The complexed surfactant that 22:48 ~ 51 are combined.The composition of preferred complexed surfactant can be better protected from material
It is attached on pulverization cylinder barrel, stationary knife and moving knife, and grease and Separation of Proteins are more thorough.
After the every crushing 28min ~ 35min of the mixed material, i.e., 1 ~ 1.2 times of mixed material quality is added to pulverization cylinder
Water be rinsed 8s ~ 10s.The preferred frequency and dosage of rinsing can be better protected from material and be attached to pulverization cylinder barrel, determine
While on knife and moving knife, the proportion of suitable material and water is obtained, is that subsequent grease separation is more simple and easy to do.
Preferably, the top of the discharging cylinder is the taper that from top to bottom diameter is gradually reduced, and the lower part of discharging cylinder is set
It is equipped with cylindric discharge gate, the upside of discharge barrel is connected with the downside of outer cylinder.
Preferably, be provided with the scraper plate being bonded with discharge barrel inner wall in the discharge barrel, scraper plate be connected with turntable and with
Turntable rotates synchronously.Scraper plate can be avoided material sticks on discharge barrel inner wall.
Preferably, the feeding port is the sector gradually to broaden from the inside to the outside, and striker plate is matched with feeding port
Fanning strip.Feeding port is the sector gradually to broaden from the inside to the outside, and striker plate is the fanning strip matched with feeding port, feeding port energy
It is enough that striker plate is limited.
Compared with prior art, beneficial effect possessed by a kind of vegetable fat raw material breaking method of the invention is: this
Discharging chamber is provided with outside the pulverization cylinder of viscous material grinding device, elastic module pushes striker plate to close feeding port, adjacent
When material accumulation between stationary knife is excessive, moving knife pushes striker plate to open feeding port the pressure of material, and material enters row
In barrel, avoid that material viscosity is excessive to cause material to stay in the gap between stationary knife, so that the fever of equipment will not be caused,
This grinding device is set directly to crush to sticking material, and good crushing effect.In the crushing process of glyceride stock
The viscosity of the components such as the boring middle protein of material and starch is larger, heats up under shearing force, stickiness further increases.And this hair
The complexed surfactant of bright addition can reduce the sticky ingredients such as protein and starch and stick to barrel, stationary knife and moving knife
Property.Not only it is conducive to the disengaging of oiliness material and machine, more preferably prevents grinding device from blocking, and is conducive to grease point when later period oil expression
From.
Detailed description of the invention
Fig. 1 is a kind of main view schematic cross-sectional view of grinding device used in the present invention.
Fig. 2 is a kind of vertical view schematic cross-sectional view of grinding device used in the present invention.
Fig. 3 is the partial enlarged view in Fig. 2 at A.
Fig. 4 is the connection schematic diagram of striker plate.
Fig. 5 is the main view schematic cross-sectional view of viscous material grinding device in grinding device 2.
Fig. 6 is the vertical view schematic cross-sectional view of viscous material grinding device in grinding device 2.
Fig. 7 is the partial enlarged view in Fig. 6 at B.
In figure: 1, pulverization cylinder 101, feeding port 2, turntable 3, outer cylinder 301, inlet tube 302, feed pipe 4,
Material guiding plate 5, discharge barrel 501, discharge port 6, scraper plate 7, support rod 8, stationary knife 9, moving knife 10, discharging cylinder
1001, discharge gate 11, striker plate 12, guide rod 13, spring.
Specific embodiment
Referring to attached drawing 1 ~ 7: a kind of grinding device used in the present invention including vertically arranged pulverization cylinder 1 and is coaxially set
The turntable 2 in pulverization cylinder 1 is set, the inner wall around pulverization cylinder 1 is arranged at intervals with multiple stationary knifes 8, around the side interval of turntable 2
Multiple moving knife 9 are provided with, turntable 2 is connected with motor, and the outer coaxial sleeve of pulverization cylinder 1 is equipped with outer cylinder 3, and outer cylinder 3 is set with the interval of pulverization cylinder 1
It sets to form discharging chamber, is often provided on the pulverization cylinder 1 between two connected stationary knifes 8 and is connected to feed cavity with 1 inner cavity of pulverization cylinder
Feeding port 101, be provided with striker plate 11 outside each feeding port 101, be provided on the outside of striker plate 11 and push striker plate 11 will
The closed elastic module of feeding port 101 is connected with discharge barrel 5 on the downside of pulverization cylinder 1, is connected with discharging cylinder 10 on the downside of discharging chamber.This
Discharging chamber is provided with outside the pulverization cylinder 1 of viscous material grinding device, elastic module pushes striker plate 11 to close feeding port 101,
When material accumulation between adjacent stationary knife 8 is excessive, moving knife 9 pushes striker plate 11 to open feeding port 101 pressure of material,
Material enters in discharging cylinder 10, avoid material viscosity it is excessive cause material to stay in the gap between stationary knife 8, thus will not
The fever for leading to equipment enables this grinding device directly to crush to sticking material, and good crushing effect.
Lower mask body is described further grinding device used in the present invention, however persons familiar with the art should
Solution, is to preferably explain here in connection with the detailed description that attached drawing provides, structure of the invention necessarily has exceeded limited
These embodiments, and for some equivalents or common approach, it is no longer described in detail herein, but still fall within the application
Protection scope.
Grinding device 1
As shown in Fig. 1 ~ 4: the viscous material grinding device further includes the main shaft being coaxially disposed with pulverization cylinder 1, and turntable 2 and main shaft are same
Axis is connected and keeps rotating synchronously.Driving pulley is installed, outer cylinder 3, and main shaft are stretched out in the upper end of main shaft on the output shaft of motor
Upper end be equipped with driven pulley, driving pulley and driven pulley by V band be connected.
The setting of the side interval of 1 inner wall of pulverization cylinder and turntable 2 has multiple stationary knifes 8 around 1 inner wall of pulverization cylinder uniformly at intervals,
There are multiple moving knife 9 uniformly at intervals around the side of turntable 2, moving knife 9 is rotated synchronously with turntable 2, to keep stationary knife 8 and moving knife 9 real
It now relatively rotates, and then realizes the crushing to material.
Turntable 2 be it is vertically arranged cylindric, the top surface of turntable 2 is the taper that diameter is gradually increased from the bottom to top.Outer cylinder 3
For vertically arranged cylinder, outer cylinder 3 and pulverization cylinder 1 are coaxially disposed, and the upper end of outer cylinder 3 is provided with inlet tube 301 and feed pipe
302, feed pipe 302 and inlet tube 301 are separately positioned on main shaft two sides, so as to keep the material entered in pulverization cylinder 1 equal
It is even to be distributed between stationary knife 8 and moving knife 9.Inlet tube 301 can not only be passed through liquid, but also can be used as blast pipe, can pass through liquid
Feeding is realized in the flowing of body and gas.
The downside of pulverization cylinder 1 is connected with discharge barrel 5, the top of discharge barrel 5 taper that from top to bottom diameter is gradually reduced, out
The lower part of barrel 5 is the cylindric discharge port 501 being coaxially disposed with main shaft.The upper end of discharge barrel 5 and the lower end of pulverization cylinder 1 are close
Envelope connection.
The top of discharge barrel 5 is provided with scraper plate 6, and the lower end of main shaft extends downwardly turntable 2, and scraper plate 6 passes through support rod 7 and master
The lower end of axis is connected, and rotates synchronously with main shaft, scraper plate 6 uniformly at intervals there are three, support rod 7 and scraper plate 6 correspond, scraper plate
6 can either avoid material sticks on 5 inner wall of discharge barrel, and can match with support rod 7 and be supported to the lower end of main shaft,
Guarantee that main axis is steady.The lower end of scraper plate 6 is tilted to the rear side of the direction of rotation of main shaft, can also be by object while scraper
Expect to convey to the downside of discharge barrel 5.
The downside of discharge barrel 5 is equipped with vibrating screen, and discharge port 501 is connected to the feed inlet of vibrating screen, and the fines of vibrating screen goes out
The mouth material up to standard for granularity after crushing is sent out, and the coarse fodder discharging of vibrating screen is connected with conveying auger, conveying auger connection
Feeding cylinder 302, so as to be crushed again to the undesirable material of granularity.
Pulverization cylinder 1 is vertically arranged cylinder, and outer cylinder 3 is identical as the height of pulverization cylinder 1, and outer cylinder 3 and pulverization cylinder 1 is upper
Side is closed by same disk, and the inner wall of outer cylinder 3 and the outer wall interval of pulverization cylinder 1 are arranged, and forms discharging chamber.The downside of outer cylinder 3
Be provided with discharging cylinder 10, discharging chamber is connected to discharging cylinder 10, and discharging cylinder 10 and discharge barrel 5 are coaxially disposed, 10 inner wall of discharging cylinder with
The setting of 5 outer wall interval of discharge barrel.The top of discharging cylinder 10 is the taper that from top to bottom diameter is gradually reduced, the lower part of discharging cylinder 10
For vertically arranged cylindric discharge gate 1001, discharge gate 1001 and discharge port 501 are coaxially disposed.Discharge gate 1001 also with vibration
The feed inlet connection of dynamic sieve.
Be provided with feeding port 101 on per 1 barrel of pulverization cylinder between two adjacent stationary knifes 8, feeding port 101 be by it is interior extremely
The taper that gradually broadens outside, is provided with a striker plate 11 outside each feeding port 101, and striker plate 11 is and 101 phase of feeding port
The fanning strip of cooperation, the inside of striker plate 11 are protruded into feeding port 101 and close feeding port 101.Feeding port 101 be by it is interior extremely
The sector gradually to broaden outside, striker plate 11 is the fanning strip matched with feeding port 101, and feeding port 101 can be to striker plate 11
It is limited.It is provided with radial guide rod 12 on 3 inner wall of outer cylinder, is provided on striker plate 11 and is led with what guide rod 12 matched
Xiang Kong, and be slidably located on guide rod 12 by pilot hole, it is arranged on the guide rod 12 between 3 inner wall of striker plate 11 and outer cylinder
There is spring 13, spring 13 pushes striker plate 11 to close feeding port 101.
Two pilot holes are arranged at intervals on each striker plate 11 along the vertical direction, pilot hole and guide rod 12 1 are a pair of
It answers, is arranged with spring 13 on each guide rod 12.When the material in adjacent 8 gap of stationary knife is excessive, under the pressure of moving knife 9
It will push striker plate 11 to open feedhole 101, the material for accumulating in 8 gap of stationary knife is entered in discharging chamber by feedhole 101,
And vibrating screen Inside sifter is entered through discharging cylinder 10.
The inner end of each guide rod 12 is the taper being gradually increased by end to mid diameter, thus avoid to material into
Enter and is counteracted into discharging chamber.Preferably, the outer end of each guide rod 12 is provided with screw thread, it is arranged on the barrel of outer cylinder 3
There is the through-hole matched with guide rod 12,12 outer end of guide rod passes through through-hole and stretches out, and each guide rod 12 is located at outside outer cylinder 3
One end is equipped with fastening nut, to facilitate the maintenance of striker plate 11.
Grinding device 2
As shown in Fig. 5 ~ 7: grinding device 2 and the difference of grinding device 1 are: pulverization cylinder 1 is that diameter is gradually reduced from the bottom to top
Taper, the side of turntable 2 is the taper that diameter is gradually reduced from the bottom to top, can slow down the speed of material whereabouts, continuation
The milling time of material, the material size after making grinding are thinner.
The upside of pulverization cylinder 1 is provided with material guiding plate 4, and material guiding plate 4 is coaxially connected with main shaft and rotates synchronously with main shaft, guide
The downside of disk 4 is connected with the upside of turntable 2, and the side of material guiding plate 4 and 3 inner wall interval of outer cylinder are arranged, the upside of pulverization cylinder 1 with lead
The downside of charging tray 4 is rotatablely connected.Material guiding plate 4 is disk, and the top of material guiding plate 4 is the cone that diameter is gradually reduced from the bottom to top
Shape.The upside of turntable 2 is horizontal and is connected with material guiding plate 4.
It is tightly connected between 1 outer wall of lower end and pulverization cylinder of outer cylinder 3, the inner wall of outer cylinder 3 is set with the outer wall interval of pulverization cylinder 1
It sets, to form feed cavity, the upper end closed of outer cylinder 3, the upper end of outer cylinder 3 and the upside interval of material guiding plate 4 are arranged, main shaft upper end
Across outer cylinder 3 upper end and with the upper end of outer cylinder 3 be rotatablely connected.In the present embodiment, striker plate is not provided at feeding port 101
11, material is sent in pulverization cylinder 1 by feed cavity by feeding port 101.
Grinding device 3
Grinding device 3 and the difference of grinding device 1 are: discharge barrel, 3 downside of outer cylinder and discharging cylinder are not provided on the downside of pulverization cylinder 1
10 are connected, and smashed material passes through discharging cylinder 10 with the material in discharging chamber and is discharged in pulverization cylinder 1.
The present invention will be further described combined with specific embodiments below, and wherein embodiment 1 is best implements.
Embodiment 1
Crushing process: after starting motor, add after vegetable fat raw material and complexed surfactant 100:1.2 in mass ratio are mixed
Enter into pulverization cylinder 1, vegetable fat raw material is added in pulverization cylinder 1 by feed pipe 302, the complexed surfactant and water by
Inlet tube 301 is added in pulverization cylinder 1；Complexed surfactant is that eight polyglyceryl palmitate and six polyglycereol monolaurates are pressed
The complexed surfactant that mass ratio 20:50 is combined；Elastic module pushes striker plate 11 to close feeding port 101, crushes
The mixed material of 1 implants glyceride stock of cylinder and complexed surfactant powder during the relative motion of stationary knife 8 and moving knife 9
Broken, when the mixed material accumulation between adjacent stationary knife 8 is excessive, moving knife 9 pushes striker plate 11 automatic the pressure of mixed material
Feeding port 101 is opened, smashed mixed material enters in discharging cylinder 10；After the every crushing 32min of mixed material, i.e., to powder
1.1 times of the water that mixed material quality is added in broken cylinder 1 is rinsed 8s, and flushing water enters in discharging cylinder 10 to be mixed with smashed
Material is mixed to get the wet pulp of crushing.Do not occur material in crushing process to stay in the gap between stationary knife, caused equipment hair
Heat, good crushing effect.
Embodiment 2
Crushing process: after starting motor, add after vegetable fat raw material and complexed surfactant 100:1.1 in mass ratio are mixed
Enter into pulverization cylinder 1, vegetable fat raw material is added in pulverization cylinder 1 by feed pipe 302, the complexed surfactant and water by
Inlet tube 301 is added in pulverization cylinder 1；Complexed surfactant is that eight polyglyceryl palmitate and six polyglycereol monolaurates are pressed
The complexed surfactant that mass ratio 19:51 is combined；Elastic module pushes striker plate 11 to close feeding port 101, crushes
The mixed material of 1 implants glyceride stock of cylinder and complexed surfactant powder during the relative motion of stationary knife 8 and moving knife 9
Broken, when the mixed material accumulation between adjacent stationary knife 8 is excessive, moving knife 9 pushes striker plate 11 automatic the pressure of mixed material
Feeding port 101 is opened, smashed mixed material enters in discharging cylinder 10；After the every crushing 35min of mixed material, i.e., to powder
1.2 times of the water that mixed material quality is added in broken cylinder 1 is rinsed 9s, and flushing water enters in discharging cylinder 10 to be mixed with smashed
Material is mixed to get the wet pulp of crushing.Do not occur material in crushing process to stay in the gap between stationary knife, caused equipment hair
Heat, good crushing effect.
Embodiment 3
Crushing process: after starting motor, add after vegetable fat raw material and complexed surfactant 100:1.4 in mass ratio are mixed
Enter into pulverization cylinder 1, vegetable fat raw material is added in pulverization cylinder 1 by feed pipe 302, the complexed surfactant and water by
Inlet tube 301 is added in pulverization cylinder 1；Complexed surfactant is that eight polyglyceryl palmitate and six polyglycereol monolaurates are pressed
The complexed surfactant that mass ratio 22:48 is combined；Elastic module pushes striker plate 11 to close feeding port 101, crushes
The mixed material of 1 implants glyceride stock of cylinder and complexed surfactant powder during the relative motion of stationary knife 8 and moving knife 9
Broken, when the mixed material accumulation between adjacent stationary knife 8 is excessive, moving knife 9 pushes striker plate 11 automatic the pressure of mixed material
Feeding port 101 is opened, smashed mixed material enters in discharging cylinder 10；After the every crushing 28min of mixed material, i.e., to powder
1 times of the water that mixed material quality is added in broken cylinder 1 is rinsed 10s, and flushing water enters in discharging cylinder 10 to be mixed with smashed
Material is mixed to get the wet pulp of crushing.Do not occur material in crushing process to stay in the gap between stationary knife, caused equipment hair
Heat, good crushing effect.
Embodiment 4
Crushing process: after starting motor, add after vegetable fat raw material and complexed surfactant 100:0.7 in mass ratio are mixed
Enter into pulverization cylinder 1, vegetable fat raw material is added in pulverization cylinder 1 by feed pipe 302, the complexed surfactant and water by
Inlet tube 301 is added in pulverization cylinder 1；Complexed surfactant is that eight polyglyceryl palmitate and six polyglycereol monolaurates are pressed
The complexed surfactant that mass ratio 26:44 is combined；Elastic module pushes striker plate 11 to close feeding port 101, crushes
The mixed material of 1 implants glyceride stock of cylinder and complexed surfactant powder during the relative motion of stationary knife 8 and moving knife 9
Broken, when the mixed material accumulation between adjacent stationary knife 8 is excessive, moving knife 9 pushes striker plate 11 automatic the pressure of mixed material
Feeding port 101 is opened, smashed mixed material enters in discharging cylinder 10；After the every crushing 15min of mixed material, i.e., to powder
0.2 times of the water that mixed material quality is added in broken cylinder 1 is rinsed 13s, and flushing water enters in discharging cylinder 10 to be mixed with smashed
Close the wet pulp that material is mixed to get crushing.Do not occur material in crushing process to stay in the gap between stationary knife, caused equipment
Fever, good crushing effect.
Embodiment 5
Crushing process: after starting motor, add after vegetable fat raw material and complexed surfactant 100:1.9 in mass ratio are mixed
Enter into pulverization cylinder 1, vegetable fat raw material is added in pulverization cylinder 1 by feed pipe 302, the complexed surfactant and water by
Inlet tube 301 is added in pulverization cylinder 1；Complexed surfactant is that eight polyglyceryl palmitate and six polyglycereol monolaurates are pressed
The complexed surfactant that mass ratio 17:53 is combined；Elastic module pushes striker plate 11 to close feeding port 101, crushes
The mixed material of 1 implants glyceride stock of cylinder and complexed surfactant powder during the relative motion of stationary knife 8 and moving knife 9
Broken, when the mixed material accumulation between adjacent stationary knife 8 is excessive, moving knife 9 pushes striker plate 11 automatic the pressure of mixed material
Feeding port 101 is opened, smashed mixed material enters in discharging cylinder 10；After the every crushing 55min of mixed material, i.e., to powder
1.5 times of the water that mixed material quality is added in broken cylinder 1 is rinsed 20s, and flushing water enters in discharging cylinder 10 to be mixed with smashed
Close the wet pulp that material is mixed to get crushing.Do not occur material in crushing process to stay in the gap between stationary knife, caused equipment
Fever, good crushing effect.
The above described is only a preferred embodiment of the present invention, being not that the invention has other forms of limitations, appoint
What those skilled in the art changed or be modified as possibly also with the technology contents of the disclosure above equivalent variations etc.
Imitate embodiment.But without departing from the technical solutions of the present invention, according to the technical essence of the invention to above embodiments institute
Any simple modification, equivalent variations and the remodeling made, still fall within the protection scope of technical solution of the present invention.
Claims (8)
1. a kind of vegetable fat raw material breaking method, it is characterised in that: grinding device used includes vertically arranged pulverization cylinder
(1) and the turntable (2) that is co-axially located in pulverization cylinder (1), the inner wall around pulverization cylinder (1) are arranged at intervals with multiple stationary knifes
(8), the side around turntable (2) is arranged at intervals with multiple moving knife (9), and turntable (2) is connected with motor, the pulverization cylinder (1)
Outer coaxial sleeve is equipped with outer cylinder (3), and outer cylinder (3) and the setting of pulverization cylinder (1) interval form discharging chamber, often two connected stationary knifes (8)
Between pulverization cylinder (1) on be provided with the feeding port (101) for being connected to feed cavity with pulverization cylinder (1) inner cavity, each feeding port
(101) it is provided with striker plate (11) outside, is provided on the outside of striker plate (11) and striker plate (11) is pushed to close feeding port (101)
Elastic module, be connected with discharging cylinder (10) on the downside of discharging chamber；
After starting motor, vegetable fat raw material and complexed surfactant 100:0.7 ~ 1.9 in mass ratio are added to pulverization cylinder
(1) in, the complexed surfactant be eight polyglyceryl palmitate and six polyglycereol monolaurates in mass ratio 17 ~
The complexed surfactant that 26:44 ~ 53 are combined；Elastic module pushes striker plate (11) to close feeding port (101), crushes
Mistake of the mixed material of cylinder (1) implants glyceride stock and complexed surfactant in the relative motion of stationary knife (8) and moving knife (9)
It is crushed in journey, when the mixed material accumulation between adjacent stationary knife (8) is excessive, moving knife (9) pushes gear to the pressure of mixed material
Flitch (11) automatically opens feeding port (101), and smashed mixed material enters in discharging cylinder (10)；
The every crushing 15min ~ 55min of mixed material, i.e., to pulverization cylinder (1) be added mixed material quality 0.2 ~ 1.5 times of water into
Row rinses 8s ~ 20s, and flushing water enters in discharging cylinder (10) wet pulp that crushing is mixed to get with smashed mixed material.
2. a kind of vegetable fat raw material breaking method according to claim 1, it is characterised in that: the pulverization cylinder (1)
It is all closed setting with the upper end of outer cylinder (3), the feed pipe (302) being connected to pulverization cylinder (1) inner cavity is provided on the upside of outer cylinder (3)
With inlet tube (301)；The vegetable fat raw material is added in pulverization cylinder (1) by feed pipe (302), and the composite surface is living
Property agent and water by inlet tube (301) be added pulverization cylinder (1) in.
3. a kind of vegetable fat raw material breaking method according to claim 2, it is characterised in that: serve as reasons on the upside of turntable (2)
Under the taper that is gradually increased of supreme diameter, the feed pipe (302) and inlet tube (301) setting turntable (2) upside.
4. a kind of vegetable fat raw material breaking method according to claim 1, it is characterised in that: further include and pulverization cylinder
(1) main shaft being coaxially disposed, turntable (2) are connected with main shaft and rotate synchronously with main shaft, and the output shaft of motor is connected with main shaft.
5. a kind of vegetable fat raw material breaking method according to claim 1, it is characterised in that: the pulverization cylinder (1)
Downside be provided with discharge barrel (5), discharge barrel (5) is arranged in discharging cylinder (10), and discharging cylinder (10) inner wall and discharge barrel (5) are outside
The setting of wall interval.
6. a kind of vegetable fat raw material breaking method according to claim 1, it is characterised in that: the vegetable fat is former
It is added in pulverization cylinder (1) after material and complexed surfactant 100:1.1 in mass ratio ~ 1.4 mixing.
7. a kind of vegetable fat raw material breaking method according to claim 1, it is characterised in that: the composite surface
It is compound that activating agent is that eight polyglyceryl palmitate and six polyglycereol monolaurates, 19 ~ 22:48 ~ 51 in mass ratio are combined
Surfactant.
8. a kind of vegetable fat raw material breaking method according to claim 1, it is characterised in that: the mixed material is every
28min ~ 35min is crushed, i.e., is rinsed 8s ~ 10s to 1 ~ 1.2 times of the water that mixed material quality is added in pulverization cylinder (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811013764.9A CN109158170B (en) | 2018-08-31 | 2018-08-31 | Method for crushing vegetable oil raw material |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811013764.9A CN109158170B (en) | 2018-08-31 | 2018-08-31 | Method for crushing vegetable oil raw material |
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| CN109158170A true CN109158170A (en) | 2019-01-08 |
| CN109158170B CN109158170B (en) | 2020-08-07 |
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ID=64893572
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| CN201811013764.9A Active CN109158170B (en) | 2018-08-31 | 2018-08-31 | Method for crushing vegetable oil raw material |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113426556A (en) * | 2021-08-26 | 2021-09-24 | 德哈哈压缩机江苏有限公司 | Purification and grinding equipment for waste and impurity discharge |
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| Publication number | Publication date |
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| CN109158170B (en) | 2020-08-07 |
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