CN215710217U

CN215710217U - Even powder unloading mechanism for sugar manufacturing

Info

Publication number: CN215710217U
Application number: CN202122137605.3U
Authority: CN
Inventors: 葛旭锋; 顾林峰
Original assignee: Ningbo Dean Tianhui Machinery Co ltd
Current assignee: Ningbo Dean Tianhui Machinery Co ltd
Priority date: 2021-09-06
Filing date: 2021-09-06
Publication date: 2022-02-01
Anticipated expiration: 2031-09-06

Abstract

The utility model discloses a flour homogenizing and blanking mechanism for sugar making, and belongs to the technical field of sugar making equipment. This sugaring is with even powder unloading mechanism, including the equipment rack, the side of equipment rack is provided with the feed portion, from last to installing screening portion, circulation drying part and lower powder ejection of compact portion down in proper order in the equipment rack, the feed portion with screening portion is connected, the feed portion includes first conveyer cylinder, first conveyer cylinder is equipped with a screw conveyer, the vertical setting of first conveyer cylinder. Such setting can be through the screening portion with caking or the thick powdered sugar screen out of granule process, and discharge equipment frame, only make the tiny powdered sugar that the particle size meets the requirements get into the below, ensure powdered sugar particle quality, rethread circulation stoving portion is dried powdered sugar, reduces moisture in the powdered sugar, avoids powdered sugar to agglomerate again, under the combined action of these two processes, makes the powdered sugar granule even, has improved the quality of powdered sugar, and then has guaranteed the processingquality of follow-up candy.

Description

Even powder unloading mechanism for sugar manufacturing

Technical Field

The utility model relates to the technical field of sugar making equipment, in particular to a flour homogenizing and blanking mechanism for making sugar.

Background

The candy industry, as one of the two traditional post snack industries in China, keeps growing rapidly, and the potential market share is expanding continuously. Meanwhile, the consumption level of people is improved, and on the basis of meeting the taste of the candy, the appearance of the candy is one of the conditions for consumers to choose, so that a new challenge is provided for the existing candy production industry.

At present, the candy molding mainly depends on the mode of impression pouring, and the impression mainly rubs out required shape on the powdered sugar through the mould, later pours into the syrup into the pit that forms in the powdered sugar in, and then makes the syrup shaping. The quality of the powdered sugar determines the quality of the candies to a great extent, but the existing production equipment can not ensure the quality of the powdered sugar, so that the powdered sugar with coarse particles or agglomerated powdered sugar can appear in the powdered sugar, and the production quality of the candies is further influenced, so that the condition that the powdered sugar is uniform and fine is the important factor in the production process.

SUMMERY OF THE UTILITY MODEL

Aiming at the defects in the prior art, the utility model aims to provide a flour homogenizing and blanking mechanism for sugar production.

In order to achieve the above purpose, the technical scheme adopted by the utility model is that the uniform powder blanking mechanism for sugar production comprises an equipment rack, wherein a feeding part is arranged on the side surface of the equipment rack, a sieving part, a circulating drying part and a lower powder discharging part are sequentially arranged in the equipment rack from top to bottom, the feeding part is connected with the sieving part, the feeding part comprises a first conveying cylinder, the first conveying cylinder is provided with a first spiral conveyor, and the first conveying cylinder is vertically arranged.

Further, the screening portion includes a second conveying cylinder, a screening cylinder and a coarse particle outlet, a second screw conveyor is arranged in the second conveying cylinder, one end of the second conveying cylinder is connected with the output end of the first conveying cylinder, the other end of the second conveying cylinder is connected with the screening cylinder, the screening cylinder is composed of a filter screen, the other end of the screening cylinder is a coarse particle discharge end, and the coarse particle outlet is located below the coarse particle discharge end.

Further, the screening drum is connected with the second spiral conveyor in the second conveying drum and rotates along with the second spiral conveyor.

Furthermore, the second conveying cylinders and the screening cylinders in the screening part are arranged into two groups and are respectively positioned on two sides of the first conveying cylinder.

Further, circulation stoving portion is including stoving ejection of compact section of thick bamboo, stoving feeding cylinder, drying equipment, stoving feeding cylinder with the same parallel arrangement of stoving ejection of compact, the feed end of stoving ejection of compact section of thick bamboo is located the top, stoving ejection of compact section of thick bamboo with still install the stock guide that the slope set up between the sieving section, the discharge end of stoving feeding cylinder is located the below, stoving ejection of compact section of thick bamboo, stoving feeding cylinder all extend to the outside of equipment rack is connected with drying equipment.

Furthermore, a spiral blade powder feeding mechanism which is distributed in the vertical direction is arranged between the lower part of the drying feeding cylinder and the lower powder discharging part.

Furthermore, a liquid level device used for sensing the sugar accumulation height on the blade is arranged on the equipment rack corresponding to the spiral blade powder feeding mechanism.

Further, powder discharge portion includes the discharge gate down, the discharge gate is "V" shape, powder baffle subassembly is still installed in the discharge gate outside, powder baffle subassembly rotates to be connected discharge gate department.

Furthermore, keep off powder board subassembly including keeping off the powder board, the both ends fixedly connected with fluted disc that keeps off the powder board, the fluted disc with the equipment frame rotates to be connected the side of equipment frame still is equipped with the rolling disc, be connected with the pivot on the rolling disc, fixedly connected with in the pivot with the gear that the fluted disc meshes mutually.

Furthermore, an observation window is further formed in the equipment rack and is formed above the screening part.

After the flour homogenizing and blanking mechanism for sugar production is adopted, compared with the prior art, the utility model has the advantages that: this system sugar is with even powder unloading mechanism sends into the equipment frame with powdered sugar through the feed portion, at first sieve the work through sieving the branch, make the tiny powdered sugar of granule fall down, and the coarse grain powdered sugar is got rid of after being screened, reduces the coarse grain in the powdered sugar, the tiny powdered sugar after the screening gets into in the circulation stoving portion of sieving the branch below, send out and dry back and get back to in the equipment frame again, make powdered sugar dry, reduce the problem of powdered sugar caking, powdered sugar discharge portion discharge and collection under again after the stoving, carry out subsequent processing work. Through such setting, can be on the one hand through the screening portion will be caked or the thick powdered sugar screen of granule is discharged the equipment frame, only make the tiny powdered sugar that the particle size meets the requirements get into the below, ensure powdered sugar particle quality, the rethread circulation stoving portion is dried powdered sugar, reduces moisture in the powdered sugar, avoids powdered sugar to agglomerate again, under the combined action of these two processes, makes the powdered sugar granule even, has improved the quality of powdered sugar, and then has guaranteed the processingquality of follow-up candy.

Drawings

FIG. 1 is a schematic perspective view of the front side of the flour homogenizing and blanking mechanism for sugar production according to the present invention;

FIG. 2 is a schematic perspective view of the back of the homogenizing and blanking mechanism for sugar production according to the present invention;

FIG. 3 is a schematic front view of a flour homogenizing and blanking mechanism for sugar production according to the present invention;

FIG. 4 is a schematic left side view of the refining and blanking mechanism for sugar production according to the present invention;

FIG. 5 is a schematic cross-sectional view taken along line A-A in FIG. 3;

FIG. 6 is a schematic cross-sectional view taken along line B-B in FIG. 4;

fig. 7 is a partially enlarged structural view of a region "C" in fig. 5.

In the figure: 10. an equipment rack; 11. an observation window; 12; an inspection window; 20. A first delivery cartridge; 30. screening; 31. a second delivery cartridge; 32. a screening drum; 33. a coarse particle outlet; 40. a circulating drying section; 41. drying the discharging barrel; 42. drying the feeding cylinder; 43. a material guide plate; 50. a powder discharging part; 51. a discharge port; 60. a powder baffle assembly; 61. a powder baffle plate; 62. a fluted disc; 63. rotating the disc; 64. a rotating shaft; 65. a gear; 70. a magnetic attraction device; 80. a liquid level device.

Detailed Description

The following description is only a preferred embodiment of the present invention, so that the present invention is more clearly and clearly understood, and the protection scope of the present invention is not limited thereby.

As shown in fig. 1 to 6, the present invention discloses a sugar refining and blanking mechanism, which comprises an apparatus frame 10, wherein a feeding portion is arranged on a side surface of the apparatus frame 10, a sieving portion 30, a circulating drying portion 40 and a lower powder discharging portion 50 are sequentially arranged in the apparatus frame 10 from top to bottom, the feeding portion is connected to the sieving portion 30, the feeding portion comprises a first conveying cylinder 20, the first conveying cylinder 20 is provided with a first screw conveyor, and the first conveying cylinder 20 is vertically arranged.

The sugar powder is conveyed to the upper part of an equipment rack 10 along a first conveying cylinder 20 through a vertically arranged first spiral conveyer in a feeding part of the powder homogenizing and blanking mechanism for sugar manufacturing, and enters a sieving part 30, the sieving work is carried out through the sieving part 30, so that the fine sugar powder with fine particles falls down, the coarse-particle sugar powder is filtered and discharged, coarse particles in the sugar powder are reduced, only the fine sugar powder after being sieved is conveyed into a circulating drying part 40 below the sieving part 30, the fine sugar powder in the circulating drying part 40 is conveyed out and dried and then returns to the equipment rack 10, the sugar powder is dried through the process, the moisture in the sugar powder is reduced, the problem of caking of the sugar powder is further reduced, and finally the dried sugar powder is discharged and collected through a powder discharging part 50 for subsequent processing work, so that the coarse-particle sugar powder and the caking sugar powder in the sugar powder are reduced, the powdered sugar is more exquisite, the moisture in the powdered sugar is reduced, the subsequent agglomeration of the powdered sugar is avoided, and the quality of the powdered sugar is improved.

Further, sifting portion 30 includes second conveyer cylinder 31, sifting cylinder 32, coarse grain export 33, be equipped with second screw conveyer in the second conveyer cylinder 31, the one end of second conveyer cylinder 31 with the output of first conveyer cylinder 20 is connected, the other end of second conveyer cylinder 31 with sifting cylinder 32 is connected, sifting cylinder 32 comprises the filter screen, the other end of sifting cylinder 32 is the coarse grain discharge end, coarse grain export 33 is located coarse grain discharge end below.

The first transport cylinder 20 of feeding portion is connected with the second transport cylinder 31, when powdered sugar moves to the upper end of first transport cylinder 20, just can get into in the second transport cylinder 31, receive second screw conveyer's effect simultaneously, move to the other end of second transport cylinder 31, and then get into screening section of thick bamboo 32, screening section of thick bamboo 32 passes through the filtering action of filter screen, tiny powdered sugar falls down naturally, and the powdered sugar of coarse grain and caking continues to the movement of the other end coarse grain discharge end of screening section of thick bamboo 32, the coarse grain after the filter screen filters at last passes through coarse grain export 33 discharge apparatus frame 10. Such transport and screening efficiency is high, and is stable moreover, ensures that equipment can stable operation for a long time.

Further, the screening drum 32 is connected to the second screw conveyor in the second conveying drum 31 and rotates together therewith.

The second screw conveyer in making screening section of thick bamboo 32 and the second conveying cylinder 31 rotates together and can make the continuous motion in screening section of thick bamboo 32 of powdered sugar, and then has improved the screening efficiency in screening section of thick bamboo 32, makes powdered sugar drop in the screening section of thick bamboo 32 of quick follow, avoids piling up of powdered sugar.

Furthermore, the second conveying cylinders 31 and the classifying cylinders 32 in the classifying section 30 are arranged in two groups, and are respectively located on two sides of the first conveying cylinder 20.

Set up respectively and can feed simultaneously and sieve at two sets of second transport cylinder 31 machine screening section of thick bamboo 32 of first transport cylinder 20 both sides, increased screening efficiency on the one hand, on the other hand when first screw conveyer carries the powdered sugar to the second transport cylinder 31 of the entering both sides that can be even when first transport cylinder 20 top, reduced the accumulational condition of powdered sugar, improve equipment operation's stability.

Further, the circulating drying part 40 includes a drying discharging cylinder 41, a drying feeding cylinder 42, and a drying device, the drying feeding cylinder 42 and the drying discharging cylinder are arranged in parallel, a feeding end of the drying discharging cylinder 41 is located above, a material guide plate 43 arranged in an inclined manner is further installed between the drying discharging cylinder 41 and the sieving part 30, a discharging end of the drying feeding cylinder 42 is located below, and both the drying discharging cylinder 41 and the drying feeding cylinder 42 extend to the outside of the device rack 10 and are connected to the drying device.

Under the guide effect of the guide plate 43 that drops through the filter screen screening in the screening portion 30, get into stoving ejection of compact section of thick bamboo 41 under the slope, powdered sugar is carried out from stoving ejection of compact section of thick bamboo 41 through third screw conveyer to in getting into drying equipment, powdered sugar after the stoving gets back to in the equipment frame 10 from stoving feed cylinder 42, carries out follow-up work, and wherein drying equipment can adopt current drying equipment, does not have detailed description in this embodiment.

Further, a spiral blade powder feeding mechanism which is distributed in the vertical direction is arranged between the lower part of the drying and feeding cylinder 42 and the lower powder discharging part 51.

The drying feeding cylinder 42 discharges materials to the lower powder discharging part 51 through the spiral blade powder feeding mechanism, so that dried sugar is scattered to fall into the lower powder discharging part 51, and the sugar is prevented from directly falling into the lower powder discharging part 51 to form block accumulation.

Further, a liquid level device 80 for sensing the sugar accumulation height on the blade is arranged on the equipment frame 10 corresponding to the spiral blade powder feeding mechanism.

Setting up through liquid level device 80 can highly monitoring the accumulational powdered sugar on helical blade powder feeding mechanism's the blade, the blade has almost no resistance when idle running, and when stoving feeding cylinder sent powder downwards, powdered sugar can drop on the blade, when liquid level device 80 sensed the bearing height of sugar on the blade and exceeded when predetermineeing, can accelerate helical blade powder feeding mechanism's rotation rate, accelerate the speed of sending powder downwards promptly, otherwise, when sensing the accumulation volume on the blade less gradually, helical blade powder feeding mechanism slew rate also descends gradually. Therefore, the powdered sugar is prevented from being blocked on the blades and finally being piled into blocks, and the quality and the discharging speed of the powdered sugar are prevented from being influenced.

Further, a magnetic attraction device 70 is further installed on the equipment rack 10, and the magnetic attraction device 70 is located below the drying feed cylinder 42.

At the in-process of screening sugaring, wearing and tearing production iron fillings can appear probably to equipment, and then make powdered sugar mix at last and have some iron fillings, and through the setting of magnetism device 70 of inhaling, separate the powdered sugar that falls down in the stoving feed cylinder 42, inhale the iron fillings that mix in the powdered sugar on magnetism device 70, ensured the purity of powdered sugar, improved the sugaring quality.

Further, lower powder discharge part 50 includes discharge gate 51, discharge gate 51 is "V" shape, powder baffle 61 subassembly 60 is still installed to the discharge gate 51 outside, powder baffle 61 subassembly 60 rotates to be connected discharge gate 51 department.

The discharge gate 51 of "V" shape can enough make the powdered sugar can be concentrated more get rid of from it, can also make the powdered sugar independently drop through the inclined plane of both sides for ejection of compact speed, and rotate and connect the baffle 61 subassembly 60 that is connected at discharge gate 51 and can make the size of discharge gate 51 change through rotating, and then the speed of adjustment ejection of compact.

Further, keep off powder board 61 subassembly 60 including keeping off powder board 61, the both ends fixedly connected with fluted disc 62 of keeping off powder board 61, fluted disc 62 with equipment rack 10 rotates to be connected the side of equipment rack 10 still is equipped with rolling disc 63, be connected with pivot 64 on the rolling disc 63, fixedly connected with on the pivot 64 with fluted disc 62 engaged with gear 65.

Through drive rolling disc 63, and then drive the gear 65 that is connected with pivot 64 and rotate, and then make the fluted disc 62 with gear 65 meshing drive fender powder board 61 and rotate, such drive mode has avoided the workman to use the hand direct with keep off powder board 61 contact, both clean health, is convenient for moreover to the regulation of fender powder board 61 angle that opens and shuts.

Furthermore, the equipment rack 10 is further provided with an observation window 11, and the observation window 11 is arranged above the sieving part 30.

Furthermore, an access window 12 is further formed in the equipment rack 10, and the access window is formed in the top of the equipment rack 10.

The observation window 11 can observe the powdered sugar state in screening portion 30, and the discovery filter screen that on the one hand can be timely is blockked up, masters powdered sugar screening condition, and the holistic operational aspect of equipment to the observation that the other party can be timely to in time take measures. Meanwhile, the arrangement of the access window 12 can facilitate the inspection or repair of the equipment so as to ensure that the equipment can work safely and smoothly.

While the utility model has been described with reference to a preferred embodiment and principles of technology applied thereto, it will be understood by those skilled in the art that the utility model is not limited to the particular embodiments described herein, but is capable of numerous obvious changes, rearrangements and substitutions without departing from the scope of the utility model.

Claims

1. The utility model provides a sugaring is with even powder unloading mechanism, a serial communication port, includes the equipment frame, the side of equipment frame is provided with feed portion, from last to installing screening portion, circulation drying part and lower powder ejection of compact portion down in proper order in the equipment frame, feed portion with screening portion is connected, feed portion includes first conveyer tube, first conveyer tube is equipped with first screw conveyer, the vertical setting of first conveyer tube.

2. The system of claim 1, wherein the sifting portion comprises a second conveying cylinder, a sifting cylinder and a coarse particle outlet, a second screw conveyor is arranged in the second conveying cylinder, one end of the second conveying cylinder is connected with the output end of the first conveying cylinder, the other end of the second conveying cylinder is connected with the sifting cylinder, the sifting cylinder is composed of a filter screen, the other end of the sifting cylinder is a coarse particle discharge end, and the coarse particle outlet is located below the coarse particle discharge end.

3. A refining, distributing and blanking mechanism for sugar manufacture as recited in claim 2, wherein said sifting cylinder is connected to and rotates with said second screw conveyor in said second conveyor cylinder.

4. A sugar refining homogenizing and blanking mechanism according to claim 2 or 3, wherein the second conveying cylinders and the sieving cylinders in the sieving part are arranged in two groups and are respectively positioned on two sides of the first conveying cylinder.

5. The uniform powder discharging mechanism for sugar production according to claim 1, wherein the circulating drying part comprises a drying material discharging cylinder, a drying material feeding cylinder and a drying device, the drying material feeding cylinder and the drying material discharging cylinder are arranged in parallel, the material feeding end of the drying material discharging cylinder is positioned above the material feeding cylinder, a material guide plate which is obliquely arranged is further installed between the drying material discharging cylinder and the sieving part, the material discharging end of the drying material feeding cylinder is positioned below the material feeding cylinder, and the drying material discharging cylinder and the drying material feeding cylinder both extend to the outer side of the device rack and are connected with the drying device.

6. A sugar refining homogenizing and blanking mechanism as claimed in claim 5 wherein a vertically distributed helical blade powder feeding mechanism is provided between the lower part of the drying and feeding cylinder and the lower powder discharging part.

7. A sugar refining homogenizing and blanking mechanism as claimed in claim 6 wherein the apparatus frame is provided with a level device corresponding to the helical blade feeding mechanism for sensing the height of sugar deposited on the blade.

8. The uniform powder discharging mechanism for sugar production according to claim 1, wherein the lower powder discharging part comprises a discharging port, the discharging port is V-shaped, a powder baffle assembly is further mounted on the outer side of the discharging port, and the powder baffle assembly is rotatably connected to the discharging port.

9. The mechanism as claimed in claim 8, wherein the powder baffle assembly comprises a powder baffle plate, two ends of the powder baffle plate are fixedly connected with fluted discs, the fluted discs are rotatably connected with the equipment rack, a rotating disc is further arranged on a side surface of the equipment rack, the rotating disc is connected with a rotating shaft, and a gear meshed with the fluted discs is fixedly connected with the rotating shaft.

10. The flour mixing and blanking mechanism for sugar production as claimed in claim 1, wherein an observation window is further formed on the equipment rack, and the observation window is formed above the screening part.