CN106629145A - Pulp dispersing and conveying device - Google Patents
Pulp dispersing and conveying device Download PDFInfo
- Publication number
- CN106629145A CN106629145A CN201710061029.4A CN201710061029A CN106629145A CN 106629145 A CN106629145 A CN 106629145A CN 201710061029 A CN201710061029 A CN 201710061029A CN 106629145 A CN106629145 A CN 106629145A
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- China
- Prior art keywords
- bucket
- pulp
- level
- disperses
- conveying device
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G69/00—Auxiliary measures taken, or devices used, in connection with loading or unloading
- B65G69/04—Spreading out the materials conveyed over the whole surface to be loaded; Trimming heaps of loose materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G15/00—Conveyors having endless load-conveying surfaces, i.e. belts and like continuous members, to which tractive effort is transmitted by means other than endless driving elements of similar configuration
- B65G15/30—Belts or like endless load-carriers
- B65G15/54—Endless load-carriers made of interwoven ropes or wires
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G2201/00—Indexing codes relating to handling devices, e.g. conveyors, characterised by the type of product or load being conveyed or handled
- B65G2201/02—Articles
- B65G2201/0202—Agricultural and processed food products
- B65G2201/0211—Fruits and vegetables
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Paper (AREA)
Abstract
The invention provides a pulp dispersing and conveying device. The pulp dispersing and conveying device comprises a drainage chute, a conveying mesh band and multiple levels of dispersing hoppers. The multiple levels of dispersing hoppers receive mixed material flow input by the drainage chute, and pulp in the mixed material flow can be conveyed onto the conveying mesh band after dispersion. The multiple levels of dispersing hoppers at least comprise the first-level dispersing hopper and the second-level dispersing hopper. The first-level dispersing hopper is constructed in the way that the mixed material flow has a gradually-expanded material flow width in the first-level dispersing hopper and also has a first tilted posture relative to the horizontal plane, so that the mixed material flow in the first-level dispersing hopper and the mixed material flow in the drainage chute are opposite in flow direction. The second-level dispersing hopper is constructed in the way that the mixed material flow has a gradually-expanded material flow width in the second-level dispersing hopper and also has a second tilted posture relative to the horizontal plane, so that the mixed material flow in the second-level dispersing hopper and the mixed material flow in the first-level dispersing hopper are opposite in flow direction. By means of the pulp dispersing and conveying device, the pulp can be evenly distributed on the conveying mesh band, and therefore pulp selection and/or canning operations can be facilitated.
Description
Technical field
The present invention relates to a kind of tinned fruit process equipment；More particularly, it relates to a kind of for pulp is equal
The even pulp dispersion conveying device being distributed on foraminous conveyer.
Background technology
At present, tinned fruit processing enterprise is chosen using the pulp for including selecting guipure, rinsing device and draining guipure mostly
Select system；Wherein, undesirable pulp is picked out by hand on guipure is selected, using current to pulp in rinsing device
Cleaned and reached with current pulp dispersion purpose, the pulp after dispersion be transported on draining guipure tinning after draining (
It is equally possible during cleaning and draining to carry out complementary selecting operation).In this pulp selection system, rinsing device
Be formed with wider rinsing water stream channel, and rinse the direction of current be also it is unidirectional, thus can be because of the unstability of current
Cause pulp to be trapped in water stream channel, pulp disperses uneven problem on draining guipure, and substantial amounts of use can be expended
Water.
The pulp dispersion effect of this pulp selection system is shown in Fig. 5.As seen from Figure 5, pulp is substantially collected at
The centre position of draining guipure, causes to be not easy to find unqualified pulp or damage around it because selecting unqualified pulp by hand
Qualified pulp, select operation to the pulp on draining guipure and cause very big difficult and increase pulp loss.More seriously,
Because the output end in production process generally in draining guipure is arranged side by side multiple storage container with separation to receive pulp, to carry out pulp
Automatically tinning, due to pulp on draining guipure skewness, therefore connect in different storage container with separation within the identical time
The pulp weight difference of receipts is very big, and to the automatic tinning of pulp very big inconvenience is brought.
The content of the invention
For the deficiencies in the prior art, the main object of the present invention is to provide one kind and enables to pulp on foraminous conveyer
Equally distributed pulp disperses conveying device.
In order to realize above-mentioned main purpose, the invention provides a kind of pulp dispersion conveying device, including it is drainage trough, defeated
Send guipure and Multistage dispersion bucket；Wherein, Multistage dispersion bucket receives the mixture flow being input into by drainage trough, and by mixture flow
Pulp dispersion after export on foraminous conveyer；Wherein, Multistage dispersion bucket at least includes：
One-level dispersion bucket, receives the mixture flow being input into by drainage trough, and is constructed so that mixture flow in a fraction
Dissipate and there is the stock flow width gradually expanded in bucket；Wherein, one-level dispersion bucket with respect to the horizontal plane has the first lateral attitude, so that
Obtain one-level dispersion bucket and the mixture flow in drainage trough has contrary flow direction；
Secondary breakup bucket, receives and disperses the be input into mixture flow of bucket by one-level, and is constructed so that mixture flow two
There is the stock flow width gradually expanded in level dispersion bucket；Wherein, secondary breakup bucket with respect to the horizontal plane has the second lateral attitude,
So that the mixture flow in secondary breakup bucket and one-level dispersion bucket has contrary flow direction.
In the present invention, Multistage dispersion bucket may further include the more polydispersion buckets such as three-level dispersion bucket, level Four dispersion bucket, respectively
Individual dispersion bucket can have substantially the same structure, as long as the dispersion bucket positioned at downstream on the flow path of mixture flow is big
In the dispersion bucket positioned at upstream；Wherein, mixture flow flows through successively the compound in dispersion buckets at different levels, and adjacent dispersion bucket
Stream has contrary flow direction.
It should be noted that there is mixture flow contrary flow direction to be not necessarily referring to mixture flow on same material flow path reversely
Flowing, and refer to that mixture flow flows in the opposite direction while material flow path changes and (be for example changed into from flowing to the left
Flow to the right, or be changed into flowing to the left from flowing to the right).For example, it is assumed that mixture flow in drainage trough towards right side flow,
Then towards left side flowing in one-level dispersion bucket, now stream direction of the mixture flow in drainage trough and one-level dispersion bucket is contrary
, but the flow path in drainage trough and one-level dispersion bucket is different；Correspondingly, mixture flow court in secondary breakup bucket
Right side flow, now stream direction of the mixture flow in secondary breakup bucket and one-level dispersion bucket is contrary, but in two fractions
The flow path dissipated in bucket and one-level dispersion bucket is different.
In above-mentioned technical proposal, mixture flow is between drainage trough and one-level dispersion bucket and one-level dispersion struggles against and two fractions
Dissipate and reverse flow occurs between bucket, this reverse flow can play cushioning effect to mixture flow；Meanwhile, mixture flow is in one-level
There is the stock flow width gradually expanded, mixture flow can be expanded along stock flow width direction and drive in dispersion bucket and secondary breakup bucket
Pulp therein flows along stock flow width direction, causes the pulp in mixture flow to enter defeated with equally distributed state therefrom
Guipure is sent, consequently facilitating carry out selecting operation on foraminous conveyer and reduce pulp loss, or in the delivery end of foraminous conveyer
Carry out pulp tinning operation.In addition, above-mentioned technical proposal may also reach up the purpose for saving industrial water.
A kind of specific embodiment of the invention, the angle between one-level dispersion bucket and horizontal plane is more than or equal to 5
Degree, less than or equal to 60 degree, preferably greater than equal to 10 degree, less than or equal to 45 degree, more preferably higher than equal to 15 degree, be less than or equal to
30 degree.Wherein, by the control to angle between one-level dispersion bucket and horizontal plane, more preferably pulp dispersion effect can be reached.
Another specific embodiment of the invention, the angle between secondary breakup bucket and horizontal plane is more than or equal to 5
Degree, less than or equal to 60 degree, preferably greater than equal to 10 degree, less than or equal to 45 degree, more preferably higher than equal to 15 degree, be less than or equal to
30 degree.Similarly, by the control to angle between secondary breakup bucket and horizontal plane, more preferably pulp dispersion effect can be reached
Really.
In the present invention, the angle between angle and one-level dispersion bucket and horizontal plane between secondary breakup bucket and horizontal plane can
With identical or difference.Wherein, the angle between secondary breakup bucket and horizontal plane be preferably greater than one-level dispersion bucket with horizontal plane it
Between angle, further to improve pulp dispersion effect.For example, secondary breakup bucket disperses with the angle and one-level of horizontal plane
Difference between bucket and the angle of horizontal plane may be controlled to more than or equal to 2 degree, less than or equal to 10 degree, preferably about 5 degree.
In the present invention, one-level dispersion bucket can include that being located at one-level disperses the baffle wall of bucket small end, with respect to the horizontal plane inclines
Diapire, the first side wall and the second sidewall for tiltedly arranging；Wherein, the first side wall and second sidewall are arranged on the phase of one-level dispersion bucket
To both sides, and it is connected with diapire and baffle wall respectively；On stream direction in one-level disperses bucket, the first side wall and the second side
The distance between wall gradually increases.
In above-mentioned technical proposal, the baffle wall of one-level dispersion bucket, the first side wall and second sidewall can be formed as plane or
Cambered surface；Wherein, the first side wall and second sidewall are preferably arranged symmetrically, and diapire is preferably formed into plane, with further
Improve pulp dispersion effect.
Similarly, secondary breakup bucket can include being located at the baffle wall of secondary breakup bucket small end, be inclined relative to horizontal
The diapire of setting, the first side wall and second sidewall；Wherein, the first side wall and second sidewall are arranged on the relative of secondary breakup bucket
Both sides, and be connected with diapire and baffle wall respectively；On stream direction in secondary breakup bucket, the first side wall and second sidewall it
Between distance gradually increase.
In above-mentioned technical proposal, the baffle wall of secondary breakup bucket, the first side wall and second sidewall can be formed as plane or
Cambered surface；Wherein, the first side wall and second sidewall are preferably arranged symmetrically, and diapire is preferably formed into plane, with further
Improve pulp dispersion effect.
In the present invention, foraminous conveyer can select guipure or draining guipure.The pulp dispersion conveying device of this is fitted
For various pulp, the dispersion conveying of easily broken peeling tangerine piece is especially suitable for.
In order to more clearly illustrate the objects, technical solutions and advantages of the present invention, with reference to specific embodiment to this
Invention is described in further detail.
Description of the drawings
Fig. 1 is the overlooking the structure diagram that pulp of the present invention disperses conveying device embodiment；
Fig. 2 is the side structure schematic diagram that pulp of the present invention disperses conveying device embodiment；
Fig. 3 is the dimensional structure diagram of the first dispersion bucket in pulp dispersion conveying device embodiment of the present invention；
Fig. 4 is to represent that pulp of the present invention disperses the picture of conveying device embodiment pulp dispersion effect；
Fig. 5 is to represent that a kind of existing pulp disperses the picture of conveying device pulp dispersion effect.
Specific embodiment
Fig. 1 and 2 is the structural representation of the pulp dispersion conveying device as a kind of preferred embodiment of the invention.Such as Fig. 1
With shown in 2, the pulp dispersion conveying device of the present embodiment includes selecting guipure 1, draining guipure 2, is arranged on and selects guipure 1 and drip
The network of rivers is with the rinsing device 3 and Multistage dispersion bucket 4 between 2；Wherein, can carry out selecting operation by hand on guipure 1 is selected, with
Reject unqualified pulp.
Rinsing device 3 has potcher 31 and a drainage trough 32, it is selected on guipure 1 is selected after pulp be input to rinsing
In groove 31.As shown in figure 1, potcher 31 adds cofferdam type dividing plate 311 in the downstream of stream conveying direction, after making to select
Pulp is effectively rinsed in the clear water of enough depth, and the pulp after rinsing enters drainage trough after gathering by gathering mouth again
32。
Mixture flow after gathering enters drainage trough 32 and flows from left to right, and Multistage dispersion bucket 4 is received by drainage trough 32
The mixture flow being input into, and will export on draining guipure 2 after the pulp dispersion in mixture flow.Wherein, in rinsing device 3
Equally can carry out complementary selecting operation on neutralization draining guipure 2.
Multistage dispersion bucket 4 includes one-level dispersion bucket 41 and secondary breakup bucket 42, one-level dispersion bucket 41 and secondary breakup bucket 42
It is in up-small and down-big toed-out shape；Wherein, one-level dispersion bucket 41 receives the mixture flow being input into by drainage trough 32, and constructs
There is the stock flow width gradually expanded in one-level disperses bucket 41 to cause mixture flow；Also, one-level dispersion bucket 41 relative to
Horizontal plane has the first lateral attitude, so that one-level dispersion bucket 41 and the mixture flow in drainage trough 32 have contrary stream
To that is, mixture flow is entered and flowed from right to left after one-level dispersion bucket 41.In the present embodiment, one-level dispersion bucket 41 with horizontal plane it
Between (one-level dispersion bucket 41 diapire and horizontal plane between) angle be of about 20 degree.
Specifically, referring to Fig. 3, one-level dispersion bucket 41 include be located at one-level disperse bucket 41 small ends baffle wall 411, relative to
Horizontal plane arrange diapire 412, symmetrically be arranged on one-level dispersion bucket 41 opposite sides the and of the first side wall 413
Second sidewall 414；The first side wall 413 and second sidewall 414 are connected respectively with diapire 412 and baffle wall 411, to limit one
The one-level dispersion slot 410 gradually expanded on stream conveying direction in level dispersion bucket 41.Wherein, baffle wall 411, diapire 412,
Side wall 413 and second sidewall 414 are all formed as plane, on the stream direction in one-level disperses bucket 41, the first side wall 413
Gradually increase with the distance between second sidewall 414.
With continued reference to shown in Fig. 1 and 2, secondary breakup bucket 42 is received and disperses 41 mixture flows being input into that struggle against by one-level, and
It is constructed so that mixture flow has the stock flow width gradually expanded in secondary breakup bucket 42；Wherein, the phase of secondary breakup bucket 42
For horizontal plane has the second lateral attitude, so that the mixture flow in secondary breakup bucket 42 and one-level dispersion bucket 41 has phase
Anti- flow direction, i.e. mixture flow are entered and flowed from left to right after secondary breakup bucket 42.Secondary breakup bucket 42 has and one-level dispersion
Struggle against 41 substantially the same structures, and simply its size is more than one-level dispersion bucket 41；That is, secondary breakup bucket 42 can be considered as
After one-level dispersion bucket 41 is amplified by proper proportion.In the present embodiment, (two fractions between secondary breakup bucket 42 and horizontal plane
Dissipate bucket 42 diapire and horizontal plane between) angle be of about 25 degree.
Fig. 4 shows that the pulp of the present embodiment disperses the pulp dispersion effect of conveying device.Referring to Fig. 4, in drainage trough
Mixture flow is sequentially passed through after the two-stage dispersion of one-level dispersion bucket and secondary breakup bucket, and the pulp in mixture flow is fairly evenly
It is distributed on draining guipure.
In above-described embodiment, can be to arrange Multistage dispersion bucket 4 in the input for selecting guipure 1, by mixture flow
Pulp dispersion after be transported to and select on guipure 1 so that pulp is equally evenly distributed on guipure 1 is selected, consequently facilitating choosing
Carry out selecting operation on network selection band 1, it is more thorough not only to select effect, and can eliminate or reduce the fruit brought because selecting operation
Meat is lost.
Although depicting the present invention above by preferred embodiment, but it is to be understood that, those of ordinary skill in the art
In the invention scope without departing from the present invention, all equal improvement made according to the present invention should be protection scope of the present invention institute
Cover.
Claims (10)
1. a kind of pulp disperses conveying device, including drainage trough, foraminous conveyer and Multistage dispersion bucket；Wherein, the Multistage dispersion
Bucket receives the mixture flow being input into by the drainage trough, and by output after the pulp dispersion in mixture flow to the transmission net
Take；Wherein, the Multistage dispersion bucket at least includes：
One-level dispersion bucket, receives the mixture flow being input into by the drainage trough, and is constructed so that mixture flow described one
There is the stock flow width gradually expanded in level dispersion bucket；Wherein, the one-level dispersion bucket is with respect to the horizontal plane inclined with first
Attitude, so that one-level dispersion bucket and the mixture flow in the drainage trough have contrary flow direction；
Secondary breakup bucket, receives and disperses the be input into mixture flow of bucket by the one-level, and is constructed so that mixture flow in institute
State and there is the stock flow width gradually expanded in secondary breakup bucket；Wherein, the secondary breakup bucket with respect to the horizontal plane has second
Lateral attitude, so that the mixture flow in the secondary breakup bucket and one-level dispersion bucket has contrary flow direction.
2. pulp as claimed in claim 1 disperses conveying device, wherein, the angle between the one-level dispersion bucket and horizontal plane
It is more than or equal to 5 degree, less than or equal to 60 degree.
3. pulp as claimed in claim 2 disperses conveying device, wherein, the angle between the one-level dispersion bucket and horizontal plane
It is more than or equal to 10 degree, less than or equal to 45 degree.
4. pulp as claimed in claim 1 disperses conveying device, wherein, the angle between the secondary breakup bucket and horizontal plane
It is more than or equal to 5 degree, less than or equal to 60 degree.
5. pulp as claimed in claim 4 disperses conveying device, wherein, the angle between the secondary breakup bucket and horizontal plane
It is more than or equal to 10 degree, less than or equal to 45 degree.
6. pulp as claimed in claim 1 disperses conveying device, wherein, the angle between the secondary breakup bucket and horizontal plane
More than the angle that the one-level is disperseed between bucket and horizontal plane.
7. pulp as claimed in claim 1 disperses conveying device, wherein, the one-level dispersion bucket includes being located at a fraction
The baffle wall for dissipating bucket small end, the diapire, the first side wall and the second sidewall that are inclined relative to horizontal setting；Wherein, described first
Side wall and the second sidewall are arranged on the opposite sides of one-level dispersion bucket, and respectively with the diapire and the baffle wall
Connection；On stream direction in the one-level disperses bucket, the distance between the first side wall and the second sidewall are gradually
Increase.
8. pulp as claimed in claim 7 disperses conveying device, wherein, the first side wall and the second sidewall are mutually right
Ground is claimed to arrange, the diapire is formed as plane.
9. pulp as claimed in claim 1 disperses conveying device, wherein, the secondary breakup bucket includes being located at two fraction
The baffle wall for dissipating bucket small end, the diapire, the first side wall and the second sidewall that are inclined relative to horizontal setting；Wherein, described first
Side wall and the second sidewall are arranged on the opposite sides of the secondary breakup bucket, and respectively with the diapire and the baffle wall
Connection；On stream direction in the secondary breakup bucket, the distance between the first side wall and the second sidewall are gradually
Increase.
10. pulp as claimed in claim 9 disperses conveying device, wherein, the first side wall and the second sidewall are mutual
It is symmetrically arranged, the diapire is formed as plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710061029.4A CN106629145A (en) | 2017-01-25 | 2017-01-25 | Pulp dispersing and conveying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710061029.4A CN106629145A (en) | 2017-01-25 | 2017-01-25 | Pulp dispersing and conveying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106629145A true CN106629145A (en) | 2017-05-10 |
Family
ID=58841574
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710061029.4A Pending CN106629145A (en) | 2017-01-25 | 2017-01-25 | Pulp dispersing and conveying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106629145A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB303234A (en) * | 1927-10-25 | 1929-01-03 | Woodall Duckham 1920 Ltd | Improvements in devices for delivering material on to a floor or into a waggon or the like |
| GB1208929A (en) * | 1968-09-10 | 1970-10-14 | Coal Industry Patents Ltd | Conveying solid divided material by chute |
| EP0018196A1 (en) * | 1979-04-16 | 1980-10-29 | Cabot Corporation | Gravity feed stream splitter for splitting particulate material or for splitting and spreading particulate material, especially for use in particulate material separators |
| CA1101347A (en) * | 1979-05-24 | 1981-05-19 | John H. Baker | Apparatus and method for uniformly spreading a flowing stream of dry solids |
| CN201559951U (en) * | 2009-05-27 | 2010-08-25 | 无锡锡通工程机械有限公司 | High-position stone-feeding dispersing device |
| CN202860811U (en) * | 2012-10-10 | 2013-04-10 | 辣妹子食品股份有限公司 | Fruit grain selecting machine |
| CN206590615U (en) * | 2017-01-25 | 2017-10-27 | 湛江市欢乐家食品有限公司 | Pulp disperses conveying device |
-
2017
- 2017-01-25 CN CN201710061029.4A patent/CN106629145A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB303234A (en) * | 1927-10-25 | 1929-01-03 | Woodall Duckham 1920 Ltd | Improvements in devices for delivering material on to a floor or into a waggon or the like |
| GB1208929A (en) * | 1968-09-10 | 1970-10-14 | Coal Industry Patents Ltd | Conveying solid divided material by chute |
| EP0018196A1 (en) * | 1979-04-16 | 1980-10-29 | Cabot Corporation | Gravity feed stream splitter for splitting particulate material or for splitting and spreading particulate material, especially for use in particulate material separators |
| CA1101347A (en) * | 1979-05-24 | 1981-05-19 | John H. Baker | Apparatus and method for uniformly spreading a flowing stream of dry solids |
| CN201559951U (en) * | 2009-05-27 | 2010-08-25 | 无锡锡通工程机械有限公司 | High-position stone-feeding dispersing device |
| CN202860811U (en) * | 2012-10-10 | 2013-04-10 | 辣妹子食品股份有限公司 | Fruit grain selecting machine |
| CN206590615U (en) * | 2017-01-25 | 2017-10-27 | 湛江市欢乐家食品有限公司 | Pulp disperses conveying device |
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| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
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| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170510 |
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| WD01 | Invention patent application deemed withdrawn after publication |