CN202626205U - Clearance sugar vaporizing device - Google Patents

Clearance sugar vaporizing device Download PDF

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Publication number
CN202626205U
CN202626205U CN 201220304434 CN201220304434U CN202626205U CN 202626205 U CN202626205 U CN 202626205U CN 201220304434 CN201220304434 CN 201220304434 CN 201220304434 U CN201220304434 U CN 201220304434U CN 202626205 U CN202626205 U CN 202626205U
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CN
China
Prior art keywords
circular clearance
clearance
urceolus
annular clearance
sugar
Prior art date
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.)
Expired - Lifetime
Application number
CN 201220304434
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Chinese (zh)
Inventor
罗明秀
王润华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DUJIANGYAN TIANWANG FOOD INDUSTRY CO LTD
Original Assignee
DUJIANGYAN TIANWANG FOOD INDUSTRY CO LTD
Priority date (The priority date 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 date listed.)
Filing date
Publication date
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Priority to CN 201220304434 priority Critical patent/CN202626205U/en
Application granted granted Critical
Publication of CN202626205U publication Critical patent/CN202626205U/en
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Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses a clearance sugar vaporizing device, and belongs to equipment used in the sugar boiling process. The device comprises an inner barrel and an outer barrel, wherein the inner barrel (1) is positioned in the outer barrel (2) to form a first annular clearance (3), a second annular clearance (4), a third annular clearance (5), a fourth annular clearance (6) and a fifth annular clearance (7). The device is characterized in that the sizes of the first annular clearance (3), the second annular clearance (4) and the third annular clearance (5) are sequentially reduced; the sizes of the fourth annular clearance (6) and the second annular clearance (4) are the same; the sizes of the fifth annular clearance (7) and the second annular clearance (4) are the same; and the size of the third annular clearance (5) is 1.4 to 1.6mm. Sugar is heated and vaporized in the clearances between the inner barrel and the outer barrel, so that the aim of dehydrating the sugar is fulfilled; and the device has the advantages that the sugar is uniformly and quickly heated and fully vaporized, and the device has a simple structure.

Description

Interval type sugar material vapourizing unit
Technical field
The utility model discloses a kind of gapped sugar material vapourizing unit, belong to industry or food-processing industry, especially to the equipment in the sugar material infusion process the spissated device of liquid sugar material.
Background technology
At present, the concentrated mode to the sugar material mostly adopts normal temperature to concentrate concentrating under reduced pressure; Thin film evaporation, modes such as rotary evaporation, these modes are carried out long-time repeated heating to the spissated liquid sugar material of needs; And the inequality of being heated; Not only power consumption is bigger, also causes the quality after the sugar material concentrates unstable, makes the quality of product descend.
Having occurred the patent No. subsequently is 200420105827.0, and the applying date is on December 30th, 2004, and open day is on February 1st, 2006, and denomination of invention is the patented technology scheme of rotary ultrathin membrane vacuum concentrating apparatus.The technical scheme of this patent is: adopt a rotation inner core that connects with driving unit shaft and one to be enclosed within the outside urceolus that cooperates with the inner core minim gap of inner core; Interior tube inner chamber is connected with steam-pipe respectively with the urceolus annular chamber; Gap between inner core and the urceolus is that annular chamber surrounding is the slip heating chamber, which is provided with opening for feed and extraction line.Adopt this technical scheme; Make slip extract discharge port out by negative pressure of vacuum from opening for feed, heating chamber, because heating chamber inside and outside both sides heating, and thinner thickness; Add the rotation that inner core does not stop; It is concentrated that the sugar material is heated with filminess fast, equably, farthest kept the effective constituent of liquid concentrator, and guaranteed the stability of quality product.Though above-mentioned patented technology scheme has solved the sugared material uneven problem of being heated largely, still exist: the uneven problem of sugar material heating solves fully; The sugar material is mobile bad in heat-processed, causes heating uneven; And above-mentioned patented technology scheme does not have further the spacing in gap is described, and makes the sugar material in vaporescence, can not fully vaporize, and then strengthen problem such as energy consumption.
Summary of the invention
For solving the problems of the technologies described above, the utility model provides a kind of and has been heated evenly, and heating is quick, the sugar material vapourizing unit that can make sugared material can fully vaporize at short notice, vaporize abundant and simple in structure.
For realizing above-mentioned technical purpose, the technical scheme of the utility model is:
Interval type sugar material vapourizing unit; Comprise that inner core 1, urceolus 2, inner core 1 are positioned at urceolus 2; Form first circular clearance 3, second circular clearance 4, the 3rd circular clearance 5; Shape gap, Fourth Ring 6 and shape gap, five rings 7 is characterized in that: the spacing of said first circular clearance 3, second circular clearance 4 and the 3rd circular clearance 5 reduces successively, and shape gap, Fourth Ring 6 is identical with the spacing of second circular clearance 4; Shape gap, five rings 7 is identical with the spacing of second circular clearance 4, and the spacing of said the 3rd circular clearance 4 is 1.4-1.6 millimeters.
The said urceolus 2 of the utility model is a bilayer structure, which is provided with steam inlet 8 and vapour outlet 9.
The said steam inlet 8 of the utility model is arranged on urceolus 2 tops, and vapour outlet 9 is arranged on the bottom of urceolus 2.
Because the utility model adopts technique scheme, therefore, with respect to prior art, has the following advantages:
At first: the spacing of first circular clearance, second circular clearance and the 3rd circular clearance reduces successively; The import of sugar material is arranged on the position, first circular clearance of urceolus bottom; The outlet of sugar material is arranged on the position, first circular clearance on urceolus top, so, makes sugared material can pass through first circular clearance, second circular clearance, the 3rd circular clearance (vaporization zone) of bottom rapidly; Arrive second gap, the third space on top then smoothly, arrive peripheral vacuum apparatus at last.Like this, the time that the sugar material is detained in entire equipment is very short, has not only reduced power consumption, and has shortened the process-cycle.And prior art has just explained between the inside and outside tube minim gap is arranged, and this can not let the sugar material in heat-processed, flow smoothly, is easy to cause sugar material trapping phenomena to occur, and then the inequality that causes being heated;
Secondly, the spacing of the 3rd circular clearance is 1.0-2.0 millimeters, has guaranteed that fully sugared material can accept inner core and urceolus heat energy, makes the sugar material vaporize rapidly;
On the chart (Fig. 2) of different clearance, the actual testing data arrangement of obtaining of flow, can see; (hard candy contains solid thing standard 96-98% in order to guarantee producing qualified candy; Soft sweets contain solid thing standard 92-96%); When flow (output) was maximum relatively simultaneously: 500Kg/h, the gap was 1.5mm (1.4-1.6mm).Can satisfy candy production line normal volume configuration (450-500Kg/h) this moment.
The 3rd, because urceolus is bilayer structure, steam inlet, outlet are set on urceolus, steam is collet chuck layer internal recycle outside, has guaranteed that sugared material can accept from inside and outside two-layer heating, is that sugared material can be heated rapidly, and vaporization;
The 4th, steam inlet is arranged on urceolus top, and vapour outlet is arranged on the urceolus bottom, and the mode that this employing steam is enterprising, go out has down remedied the sugared material uneven defective of in receiving thermal process, being heated.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is the testing data figure of the utility model.
Embodiment
Embodiment 1
Interval type sugar material vapourizing unit; Comprise that inner core 1, urceolus 2, inner core 1 are positioned at urceolus 2; Form first circular clearance 3, second circular clearance 4, the 3rd circular clearance 5; Shape gap, Fourth Ring 6 and shape gap, five rings 7 is characterized in that: the spacing of said first circular clearance 3, second circular clearance 4 and the 3rd circular clearance 5 reduces successively, and shape gap, Fourth Ring 6 is identical with the spacing of second circular clearance 4; Shape gap, five rings 7 is identical with the spacing of second circular clearance 4, and the spacing of said the 3rd circular clearance 4 is 1.4
Embodiment 2
Interval type sugar material vapourizing unit; Comprise that inner core 1, urceolus 2, inner core 1 are positioned at urceolus 2; Form first circular clearance 3, second circular clearance 4, the 3rd circular clearance 5; Shape gap, Fourth Ring 6 and shape gap, five rings 7 is characterized in that: the spacing of said first circular clearance 3, second circular clearance 4 and the 3rd circular clearance 5 reduces successively, and shape gap, Fourth Ring 6 is identical with the spacing of second circular clearance 4; Shape gap, five rings 7 is identical with the spacing of second circular clearance 4, and the spacing of said the 3rd circular clearance 4 is 1.6 millimeters.Said urceolus 2 is a bilayer structure, which is provided with steam inlet 8 and vapour outlet 9.
Embodiment 3
The preferred forms of the utility model:
Interval type sugar material vapourizing unit; Comprise that inner core 1, urceolus 2, inner core 1 are positioned at urceolus 2; Form first circular clearance 3, second circular clearance 4, the 3rd circular clearance 5; Shape gap, Fourth Ring 6 and shape gap, five rings 7 is characterized in that: the spacing of said first circular clearance 3, second circular clearance 4 and the 3rd circular clearance 5 reduces successively, and shape gap, Fourth Ring 6 is identical with the spacing of second circular clearance 4; Shape gap, five rings 7 is identical with the spacing of second circular clearance 4, and the spacing of said the 3rd circular clearance 4 is 1.5 millimeters.Said urceolus 2 is a bilayer structure, which is provided with steam inlet 8 and vapour outlet 9.Said steam inlet 8 is arranged on urceolus 2 tops, and vapour outlet 9 is arranged on the bottom of urceolus 2.

Claims (3)

1. interval type sugar is expected vapourizing unit; Comprise that inner core (1), urceolus (2), inner core (1) are positioned at urceolus (2); Form first circular clearance (3), second circular clearance (4), the 3rd circular clearance (5); Shape gap, Fourth Ring (6) and shape gap, five rings (7) is characterized in that: the spacing of said first circular clearance (3), second circular clearance (4) and the 3rd circular clearance (5) reduces successively, and shape gap, Fourth Ring (6) is identical with the spacing of second circular clearance (4); Shape gap, five rings (7) is identical with the spacing of second circular clearance (4), and the spacing of said the 3rd circular clearance (5) is 1.4-1.6 millimeters.
2. interval type sugar material vapourizing unit according to claim 1, it is characterized in that: said urceolus (2) is a bilayer structure, which is provided with steam inlet (8) and vapour outlet (9).
3. interval type sugar material vapourizing unit according to claim 2, it is characterized in that: said steam inlet (8) is arranged on urceolus (2) top, and vapour outlet (9) is arranged on the bottom of urceolus (2).
CN 201220304434 2012-06-27 2012-06-27 Clearance sugar vaporizing device Expired - Lifetime CN202626205U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220304434 CN202626205U (en) 2012-06-27 2012-06-27 Clearance sugar vaporizing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220304434 CN202626205U (en) 2012-06-27 2012-06-27 Clearance sugar vaporizing device

Publications (1)

Publication Number Publication Date
CN202626205U true CN202626205U (en) 2012-12-26

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220304434 Expired - Lifetime CN202626205U (en) 2012-06-27 2012-06-27 Clearance sugar vaporizing device

Country Status (1)

Country Link
CN (1) CN202626205U (en)

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Granted publication date: 20121226