CN2302662Y - Vacuum continuous sugar-cooker - Google Patents
Vacuum continuous sugar-cooker Download PDFInfo
- Publication number
- CN2302662Y CN2302662Y CN 97221154 CN97221154U CN2302662Y CN 2302662 Y CN2302662 Y CN 2302662Y CN 97221154 CN97221154 CN 97221154 CN 97221154 U CN97221154 U CN 97221154U CN 2302662 Y CN2302662 Y CN 2302662Y
- Authority
- CN
- China
- Prior art keywords
- sugar
- vacuum
- pump
- massecuite
- cooker
- 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 - Fee Related
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- Confectionery (AREA)
Abstract
The utility model belongs to a vacuum continuous sugar cooker applied in the confectionery manufacturing and processing enterprise, which is designed for solving the disadvantages of batch discharging, unstable massecuite quality and low production efficiency of the existing continuous vacuum sugar cooker. The sugar cooker adopts a fixed sugar cooking boiler, the lower part of which is added with an outlet duct, and the massecuite directly is conveyed from the outlet by a pump; a steam heat insulating pipe is additionally arranged outside the sugar cooking boiler, and simultaneously a hydraulic jet pump is used for replacing the water ring type vacuum pump, which largely increases the quality and the production efficiency of the massecuite, and improves the sanitary condition for cooking the sugar. The utility model can be widely used for the confectionery manufacturing and processing enterprise.
Description
The utility model belongs to the vacuum continuous pan boiling machine of candy production, processing enterprise's application.
At present, the domestic continous vacuum sugar-cooker that provides is the continuous relatively production technology that grows up on the basis of vacuum sugar boiling, and the sugar boiler of vacuum chamber bottom is that two sugar pots are alternately rotated the commentaries on classics pot of operation in this explained hereafter equipment.When promptly changeing pot work, two alternately material loading in batches, dischargings of one pot one pot of pot.Pot is changeed in conversion constantly aborning, causes the cyclically-varying of pot interior vacuum.Output and quality that candy is produced have directly been influenced.Worker's labour intensity and the contaminated chance of massecuite have also been increased simultaneously.
The utility model is a kind of output and the quality that can effectively improve the sugar cook product that designs at the deficiencies in the prior art, improves the vacuum continuous pan boiling machine of working condition and worker's labour intensity.
The utility model is realized by following measure.Vacuum continuous pan boiling machine mainly is made up of liquid glucose constant displacement pump, heating coil, vaporization chamber, vacuum chamber, sugar boiler, vacuum system and massecuite induction system etc.One end of heating coil links to each other with sugar dissolving kettle through the liquid glucose constant displacement pump, and the other end links to each other with vaporization chamber, is vacuum chamber and sugar boiler below the vaporization chamber, and the flow control valve of control liquid glucose flow is arranged between vaporization chamber and the vacuum chamber.Said sugar boiler is the fixedly sugar boiler that is tightly connected by gripping mechanism and vacuum chamber in the utility model, and one group of steam insulating tube is installed in the outside of this pot; There is a delivery channel to be connected with the massecuite delivery pump in the bottom of pot; Said vacuum system is made up of hydraulic jet pump, centrifugal water pump and cyclic water tank etc.
In vacuum continuous pan boiling machine when work,, lysed liquid glucose is pressed into coll(-tube) heater by constant displacement pump, and liquid glucose is the thread state and flows in pipe, and tube wall is subjected to the heating of steam and temperature rises, and heat is passed to liquid glucose in flowing.The liquid glucose temperature rises, the moisture content vaporization.Be full of liquid glucose and secondary steam in the exit of coiled pipe.Secondary steam is discharged by exhaust outlet, and liquid glucose directly enters vaporization chamber.The liquid glucose that enters vaporization chamber forms a good fluidized state and carries out vapor-liquid separation, and steam continues to discharge.After the liquid glucose inflow of vaporization chamber is a certain amount of, open flow control valve, liquid glucose is flowed in the sugar boiler of vacuum chamber bottom, carry out vacuum and concentrate.The inside of sugar boiler is vacuum state, and there is the steam heating pipe insulation outside, makes the liquid glucose temperature remain at optimum state.This moment, the liquid glucose under vacuum state continued boiling, and moisture content advances an evaporation, and liquid glucose is concentrated.The massecuite that boils is delivered directly to blender by the delivery channel and the delivery pump of sugar boiler bottom, carries out candy and gives forming processes.
The utility model has the advantages that, adopt hydraulic jet pump to replace water-ring vacuum pump, replace a pair of commentaries on classics pot with a sugar boiler, and steam insulating tube and delivery channel have been installed outside pot.Make sugar cook technology realize sealing, vacuum, continuously, whole production technology more rationally, reliable, provide reliable assurance to quality and the output that improves candy.Sanitary condition has also had very big improvement.
Accompanying drawing 1 is sugar boiler and a vaporization chamber structural representation partly in the utility model.(1) is steam vent among the figure; (2) be the liquid glucose import; (3) be vaporization chamber; (4) be flow control valve; (5) be vacuum chamber; (6) be gripping mechanism; (7) be the vavuum pump interface; (8) be sugar boiler; (9) be the steam insulating tube; (10) be delivery channel; (11) be gear pump; (12) be buncher.
Below in conjunction with a description of drawings embodiment of the present utility model.
Steam vent (1) is arranged above the vaporization chamber of the present utility model (3), and there is liquid glucose import (2) side, is vacuum chamber (5) below; Between vaporization chamber (3) and vacuum chamber (5), flow control valve (4) is arranged; Sugar boiler (8) is connected with vacuum chamber by gripping mechanism (6) below vacuum chamber (5); One delivery channel (10) is arranged at the bottom of sugar boiler (8), connects gear pump (11) below, and gear pump (11) is by buncher (12) drive work.Lysed liquid glucose enters vaporization chamber (3) by liquid glucose import (2) after the serpentine heating pipe heating, carry out sugar, vapour separation, and steam is discharged from steam vent (1).After the inflow of the liquid glucose in the vaporization chamber (3) is a certain amount of, open flow control valve (4), liquid glucose is flowed in the following sugar boiler (8) of vacuum chamber (5), carry out vacuum and concentrate.Hydraulic jet pump passes through vavuum pump interface (7) with vacuum chamber (5) and sugar boiler (8) vacuum pumping state.There is steam insulating tube (9) that it is carried out heat tracing below the sugar boiler.The massecuite that boils drives the gear pump (11) that is installed on the delivery channel (10) by buncher (12), is delivered to subsequent processing.
Claims (2)
1, a kind of vacuum continuous pan boiling machine, mainly form by liquid glucose constant displacement pump, heating coil, vaporization chamber, vacuum chamber, sugar boiler, vacuum system and massecuite induction system etc., it is characterized in that: said sugar boiler (8) is the fixedly sugar boiler that is tightly connected by gripping mechanism (6) and vacuum chamber (5), and one group of steam insulating tube (9) is installed in the outside of this pot; There is a delivery channel (10) to be connected with massecuite delivery pump (11) in the bottom of pot.
2, vacuum continuous pan boiling machine according to claim 1, it is characterized in that: said vacuum system is made up of hydraulic jet pump, centrifugal water pump and cyclic water tank etc.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97221154 CN2302662Y (en) | 1997-07-15 | 1997-07-15 | Vacuum continuous sugar-cooker |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 97221154 CN2302662Y (en) | 1997-07-15 | 1997-07-15 | Vacuum continuous sugar-cooker |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2302662Y true CN2302662Y (en) | 1999-01-06 |
Family
ID=33936619
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 97221154 Expired - Fee Related CN2302662Y (en) | 1997-07-15 | 1997-07-15 | Vacuum continuous sugar-cooker |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2302662Y (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100403916C (en) * | 2003-04-15 | 2008-07-23 | 上海冠生园食品有限公司 | Art for whitening cooked syrup |
CN102894161A (en) * | 2012-11-13 | 2013-01-30 | 如皋市包装食品机械有限公司 | Novel heating device of sugar decoction machine |
CN104273308A (en) * | 2014-10-24 | 2015-01-14 | 南通维尔斯机械科技有限公司 | Sugar cooking machine |
CN104726619A (en) * | 2015-03-06 | 2015-06-24 | 王连升 | Method and device for refining sugar |
-
1997
- 1997-07-15 CN CN 97221154 patent/CN2302662Y/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100403916C (en) * | 2003-04-15 | 2008-07-23 | 上海冠生园食品有限公司 | Art for whitening cooked syrup |
CN102894161A (en) * | 2012-11-13 | 2013-01-30 | 如皋市包装食品机械有限公司 | Novel heating device of sugar decoction machine |
CN104273308A (en) * | 2014-10-24 | 2015-01-14 | 南通维尔斯机械科技有限公司 | Sugar cooking machine |
CN104726619A (en) * | 2015-03-06 | 2015-06-24 | 王连升 | Method and device for refining sugar |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |