CN103920577A - Sugar granule crushing and separating device - Google Patents
Sugar granule crushing and separating device Download PDFInfo
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- CN103920577A CN103920577A CN201410173457.2A CN201410173457A CN103920577A CN 103920577 A CN103920577 A CN 103920577A CN 201410173457 A CN201410173457 A CN 201410173457A CN 103920577 A CN103920577 A CN 103920577A
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- sugar
- discharging opening
- distribution device
- air exhauster
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Abstract
The invention discloses a sugar granule crushing and separating device which comprises a crushing device, wherein a discharge opening of the crushing device is communicated with an air inlet of an exhaust fan; a feeding hopper is communicated on the top of the crushing device; a blanking tank is communicated between the discharge opening of the crushing device and the air inlet of the exhaust fan; a discharging device A is communicated with the bottom of the blanking tank; a discharge opening A is formed in the bottom of the discharging device A; an air outlet of the exhaust fan is communicated with a discharging device B; a discharge opening B is formed in the bottom of the discharging device B. According to the structure, the sugar granule crushing and separating device is simple in structure, sugar granules can be crushed, and the sugar powder can be respectively collected according to the granule size, so that the sugar powder of different granule sizes can be used for different processes or technologies, and the utilization rate of the sugar powder is improved.
Description
Technical field
The present invention relates to biscuit manufacture field, be specifically related to a kind of particulate sugar and pulverize feeding-distribution device.
Background technology
The primary raw material of biscuit is wheat flour, then adds the auxiliary materials such as carbohydrate, grease, egg product, dairy products.According to the difference of formula and production technology, rusk can be divided into tough biscuit and the large class of shortbread type biscuit two.The feature of tough biscuit is that die moulding mostly is recessed flower, and there is pinprick on surface.Product surface is smooth smooth, and section structure has levels, and has crisp sense during chewing, resistance to chewing, and crisp is its distinctive characteristic.The sugar of tough biscuit and the crisper property of the proportioning of grease cake are low.General with below 30% of sugar amount, by oil mass, be below 20%.The feature of shortbread type biscuit is that die moulding mostly is protruding flower, and decorative pattern is obvious, and structure is fine and closely woven, is 14% ~ 30% of flour amount.The particular product that some sweet taste is loose, grease amount can be up to 50% left and right.
Biscuit processing enterprise, in the manufacturing process of biscuit, in order to improve the taste of some biscuit, can sprinkle one deck Icing Sugar on the surface of biscuit at present.Because Icing Sugar is very easily combined with airborne water, cause Icing Sugar bonding, so generally biscuit processing enterprise does not directly buy Icing Sugar, but after buying particulate sugar, by reducing mechanism, pulverize.But the Icing Sugar after reducing mechanism is pulverized, cannot guarantee the in the same size of Icing Sugar particle, the thickness that causes Icing Sugar to be sprinkling upon biscuit surface cannot guarantee, the Icing Sugar particle that is sprinkling upon in addition biscuit surface varies, and affects attractive in appearance.
Summary of the invention
The object of the invention is to: overcome the deficiencies in the prior art, provide a kind of particulate sugar to pulverize feeding-distribution device, simple in structure, particulate sugar can be pulverized, and can distinguish rewinding according to the granular size of Icing Sugar, make the Icing Sugar of variable grain size for different operations or technique, improve the utilization rate of Icing Sugar.
The technical solution used in the present invention is:
Particulate sugar is pulverized feeding-distribution device, comprise reducing mechanism, the discharging opening of described reducing mechanism is communicated with the air inlet of air exhauster, the top of reducing mechanism is communicated with feed hopper, between the discharging opening of described reducing mechanism and the air inlet of air exhauster, be communicated with blanking tank, the bottom of described blanking tank is communicated with drawing mechanism A, and drawing mechanism A bottom is provided with discharging port A, the air outlet of described air exhauster is communicated with drawing mechanism B, and the bottom of described drawing mechanism B is provided with discharging opening B.
The further improvement project of the present invention is that the discharging opening of described reducing mechanism is communicated with the top of blanking tank by pipeline A.
The present invention further improvement project is, the air inlet of described air exhauster is communicated with the top of blanking tank by pipeline B, and the air outlet of air exhauster is communicated with drawing mechanism B by pipeline C.
The present invention further improvement project is that described discharging port A and discharging opening B are equipped with respectively rewinding bag A and rewinding bag B.
The present invention further improvement project is that described rewinding bag B is dustproof cloth bag.
The present invention further improvement project is that described discharging port A and discharging opening B are provided with a plurality of.
The present invention further improvement project is that a plurality of discharging port A are symmetric.
The present invention further improvement project is that a plurality of discharging opening B are arranged in a row.
Beneficial effect of the present invention is:
Particulate sugar of the present invention is pulverized feeding-distribution device, simple in structure, particulate sugar can be pulverized, and can distinguish rewinding according to the granular size of Icing Sugar, makes the Icing Sugar of variable grain size for different operations or technique, improves the utilization rate of Icing Sugar.
accompanying drawing explanation:
Fig. 1 is that the master of structure of the present invention looks schematic diagram.
the specific embodiment:
As shown in Figure 1, the present invention includes reducing mechanism 2, the discharging opening of described reducing mechanism 2 is communicated with the air inlet of air exhauster 6, the top of reducing mechanism 2 is communicated with feed hopper 1, between the air inlet of the discharging opening of described reducing mechanism 2 and air exhauster 6, be communicated with blanking tank 4, the bottom of described blanking tank 4 is communicated with drawing mechanism A7, and drawing mechanism A7 bottom is provided with discharging port A 8, the air outlet of described air exhauster 6 is communicated with drawing mechanism B10, and the bottom of described drawing mechanism B10 is provided with discharging opening B11; The discharging opening of described reducing mechanism 2 is communicated with the top of blanking tank 4 by pipeline A3; The air inlet of described air exhauster 6 is communicated with the top of blanking tank 4 by pipeline B5, and the air outlet of air exhauster 6 is communicated with drawing mechanism B10 by pipeline C9; Described discharging port A 8 and discharging opening B11 are equipped with respectively rewinding bag A12 and rewinding bag B13; Described rewinding bag B13 is dustproof cloth bag; Described discharging port A 8 and discharging opening B11 are provided with a plurality of (in the implementation case, discharging port A 8 is provided with 2, and discharging opening B11 is provided with 4); A plurality of discharging port A 8 are symmetric; A plurality of discharging opening B11 are arranged in a row.
When the present invention uses, particulate sugar is imported in feed hopper 1, open reducing mechanism 2, air exhauster 6 and drawing mechanism A7 simultaneously, particulate sugar forms Icing Sugar after reducing mechanism 2 pulverization process, Icing Sugar enters blanking tank 4 under the effect of air exhauster 6, and the larger Icing Sugar of particle, due to heavier, directly enters rewinding bag A12 from the discharging port A 8 of the blanking tank 4 set drawing mechanism A7 in bottom, after the rewinding bag A12 of one of them discharging port A 8 fills Icing Sugar, change another discharging port A 8 and proceed Icing Sugar rewinding; The less Icing Sugar of particle, under the effect of air exhauster 6, continues to be pumped and enters in drawing mechanism B10, and under the effect of air exhauster 6, Icing Sugar enters rewinding bag B13 by discharging opening B11 successively by particle order from big to small; The wind of air exhauster 6 also blows out from rewinding bag B13 simultaneously.
Claims (8)
1. particulate sugar is pulverized feeding-distribution device, comprise reducing mechanism (2), the discharging opening of described reducing mechanism (2) is communicated with the air inlet of air exhauster (6), the top of reducing mechanism (2) is communicated with feed hopper (1), it is characterized in that: between the discharging opening of described reducing mechanism (2) and the air inlet of air exhauster (6), be communicated with blanking tank (4), the bottom of described blanking tank (4) is communicated with drawing mechanism A(7), drawing mechanism A(7) bottom is provided with discharging port A (8), the air outlet of described air exhauster (6) is communicated with drawing mechanism B(10), described drawing mechanism B(10) bottom is provided with discharging opening B(11).
2. particulate sugar as claimed in claim 1 is pulverized feeding-distribution device, it is characterized in that: the discharging opening of described reducing mechanism (2) is by pipeline A(3) be communicated with the top of blanking tank (4).
3. particulate sugar as claimed in claim 1 is pulverized feeding-distribution device, it is characterized in that: the air inlet of described air exhauster (6) is by pipeline B(5) be communicated with the top of blanking tank (4), the air outlet of air exhauster (6) passes through pipeline C(9) with drawing mechanism B(10) be communicated with.
4. particulate sugar as claimed in claim 1 is pulverized feeding-distribution device, it is characterized in that: described discharging port A (8) and discharging opening B(11) be equipped with respectively rewinding bag A(12) and rewinding bag B(13).
5. particulate sugar as claimed in claim 4 is pulverized feeding-distribution device, it is characterized in that: be described rewinding bag B(13) dustproof cloth bag.
6. particulate sugar as claimed in claim 1 is pulverized feeding-distribution device, it is characterized in that: described discharging port A (8) and discharging opening B(11) be provided with a plurality of.
7. particulate sugar as claimed in claim 6 is pulverized feeding-distribution device, it is characterized in that: a plurality of discharging port A (8) are symmetric.
8. particulate sugar as claimed in claim 6 is pulverized feeding-distribution device, it is characterized in that: a plurality of discharging opening B(11) be arranged in a row.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201410173457.2A CN103920577B (en) | 2014-04-28 | 2014-04-28 | Particulate sugar is pulverized feeding-distribution device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201410173457.2A CN103920577B (en) | 2014-04-28 | 2014-04-28 | Particulate sugar is pulverized feeding-distribution device |
Publications (2)
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CN103920577A true CN103920577A (en) | 2014-07-16 |
CN103920577B CN103920577B (en) | 2016-05-25 |
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CN201410173457.2A Active CN103920577B (en) | 2014-04-28 | 2014-04-28 | Particulate sugar is pulverized feeding-distribution device |
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Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070108321A1 (en) * | 2005-11-16 | 2007-05-17 | Rodney Booth | Grinding mill with air recirculation |
KR100849626B1 (en) * | 2008-01-16 | 2008-07-31 | 김태영 | A crusher for food |
CN101537384A (en) * | 2009-04-30 | 2009-09-23 | 李喜福 | Crushing and restoring system of broken noodles |
CN102019221A (en) * | 2009-09-16 | 2011-04-20 | 王小钧 | High efficient machinery pulverizer |
CN102806131A (en) * | 2012-08-20 | 2012-12-05 | 闽西丰农食品有限公司 | Bamboo shoot full-pulverizer and production process of bamboo shoot powder |
CN202778664U (en) * | 2012-07-02 | 2013-03-13 | 四川新华康生物科技有限公司 | Citrus aurantium crushing device |
CN203184236U (en) * | 2013-04-24 | 2013-09-11 | 湘潭瑞通球团有限公司 | Material classification device |
CN203803602U (en) * | 2014-04-28 | 2014-09-03 | 宿迁市汇味食品有限公司 | Granule sugar crushing and separating device |
-
2014
- 2014-04-28 CN CN201410173457.2A patent/CN103920577B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070108321A1 (en) * | 2005-11-16 | 2007-05-17 | Rodney Booth | Grinding mill with air recirculation |
KR100849626B1 (en) * | 2008-01-16 | 2008-07-31 | 김태영 | A crusher for food |
CN101537384A (en) * | 2009-04-30 | 2009-09-23 | 李喜福 | Crushing and restoring system of broken noodles |
CN102019221A (en) * | 2009-09-16 | 2011-04-20 | 王小钧 | High efficient machinery pulverizer |
CN202778664U (en) * | 2012-07-02 | 2013-03-13 | 四川新华康生物科技有限公司 | Citrus aurantium crushing device |
CN102806131A (en) * | 2012-08-20 | 2012-12-05 | 闽西丰农食品有限公司 | Bamboo shoot full-pulverizer and production process of bamboo shoot powder |
CN203184236U (en) * | 2013-04-24 | 2013-09-11 | 湘潭瑞通球团有限公司 | Material classification device |
CN203803602U (en) * | 2014-04-28 | 2014-09-03 | 宿迁市汇味食品有限公司 | Granule sugar crushing and separating device |
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CN103920577B (en) | 2016-05-25 |
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