CN103652223B - Energy-saving type continuous sugar boiling machine - Google Patents
Energy-saving type continuous sugar boiling machine Download PDFInfo
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- CN103652223B CN103652223B CN201310742180.6A CN201310742180A CN103652223B CN 103652223 B CN103652223 B CN 103652223B CN 201310742180 A CN201310742180 A CN 201310742180A CN 103652223 B CN103652223 B CN 103652223B
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
The invention provides an energy-saving type continuous sugar boiling machine. The energy-saving type continuous sugar boiling machine comprises a syrup storage tank, a boiling and agitating combined tank, a vacuum tank, a vacuumizing device and a steam supplying device, wherein the boiling and agitating combined tank comprises an outer tank body, an inner tank body and an inner tank body rotation driving device; a first interlayer space is arranged on the tank wall of the outer tank body and the inner tank body is rotatably mounted in the outer tank body; a crack is formed between the inner tank body and the outer tank body; the boiling and agitating combined tank is provided with a combined tank feeding opening and a combined tank discharging opening which are communicated with the crack; a discharging opening of a material storage tank is communicated with the combined tank feeding opening; the combined tank discharging opening is communicated with a vacuum tank feeding opening; the first interlayer space, a cavity of the inner tank body and a second interlayer space above the vacuum tank are communicated with the steam supplying device; a cavity of the vacuum tank is communicated with the vacuumizing device. According to the boiling and agitating combined tank, a traditional thin film type sugar boiling tank and a thin film type agitating tank are ingeniously simplified and optimized and combined to form a whole body; the energy-saving type continuous sugar boiling machine is simple and compact in structure; a syrup conveying path is greatly shortened; the sugar boiling efficiency is high and the energy consumption is low.
Description
Technical field
The present invention relates to sugar cook equipment, be specifically related to a kind of energy-saving continuous sugar-cooker.
Background technology
Traditional sugar-cooker is constituted jointly by slurry can, preheater, sugar boiling pot (as diaphragm type sugar boiling pot), agitator tank (as diaphragm type agitator tank), vacuum tank, vacuum extractor, steam supply device and unloading pump etc., its huge structure is complicated, and the syrup in slurry can needs through preheater, sugar boiling pot, agitator tank and vacuum tank etc., syrup delivery Path too long, sugar cook efficiency is low, energy consumption is high, and the transparency of product, the uniformity are all subject to certain restrictions, be difficult to ensure that product keeps original flavor protoplasm.In addition; in agitator tank, adopt stainless steel stirring vane to rotate in copper cylinder barrel; carry out mechanical type friction stirring; due to the error in manufacture and the factor in material; in stirring, stainless steel stirring vane often scratches inner wall of cylinder; so that with copper powder in syrup, the improper product higher to hygienic requirements.In addition, traditional sugar-cooker all adopts the moisture in the form eliminating syrup once vacuumized, and is difficult to the requirement adapting to dissimilar product.
Summary of the invention
Technical problem to be solved by this invention be to provide a kind of simple and compact for structure, sugar cook efficiency is high and the energy-saving continuous sugar-cooker that energy consumption is low.The technical scheme adopted is as follows:
A kind of energy-saving continuous sugar-cooker, is characterized in that comprising slurry can, composite can, vacuum tank, vacuum extractor and steam supply device is stirred in infusion; Infusion is stirred composite can and is comprised outer tank body and interior tank body, the tank skin of outer tank body has the first mezzanine space, interior tank body is rotatably arranged in outer tank body, have crack between the outer wall of interior tank body and the inwall of outer tank body, infusion is stirred composite can and is also comprised the interior tank body device of rotation driving that interior tank body can be driven to rotate; Infusion is stirred composite can and is provided with composite can charging aperture and composite can discharging opening, and composite can charging aperture is all communicated with described crack with composite can discharging opening; Vacuum tank chuck is provided with outside the tank skin of vacuum tank, the second mezzanine space is formed between vacuum tank chuck and the tank skin of vacuum tank, vacuum tank is provided with vacuum tank charging aperture and vacuum tank discharging opening, and vacuum tank charging aperture is all communicated with the cavity of vacuum tank with vacuum tank discharging opening; The discharging opening of storage tank is communicated with composite can charging aperture by conveying pipeline, and composite can discharging opening is communicated with vacuum tank charging aperture by conveying pipeline; The cavity of the first mezzanine space, interior tank body is all communicated with steam supply device by steam pipeline with the second mezzanine space, and the cavity of vacuum tank is communicated with vacuum extractor.
Above-mentioned infusion is stirred in composite can, it is backward interior to the syrup heating in crack that the first mezzanine space in outer tank body passes into steam, the cavity of interior tank body passes into that steam is backward to be heated the syrup in crack outward, simultaneously, interior tank body rotates under the driving of interior tank body device of rotation driving, syrup in crack is stirred, like this, realize two film high speed infusion and stirring, infusion is quick, evenly, thus be one overall by traditional huge and the diaphragm type sugar boiling pot of complexity and diaphragm type agitator tank ingenious simplification optimum organization from theory and structure, realize functionally (infusion and stirring) and structural organic unity, structure is more simply compact, safe and reliable, and greatly shorten syrup delivery path, sugar cook efficiency is high, energy consumption is low, can the efficient high-quality syrup of output.
Above-mentioned slurry can treats the syrup of infusion for storing, slurry can stirs composite can conveying syrup (syrup enters in the crack between the outer wall of interior tank body and the inwall of outer tank body) by conveying pipeline to infusion.Opportunity and the flow that composite can is stirred in infusion is entered for the ease of controlling material, usually on the conveying pipeline between the discharging opening and composite can charging aperture of slurry can, be provided with constant displacement pump, the syrup in slurry can be extracted into infusion and stir in the crack of composite can by constant displacement pump; Stir composite can in order to prevent syrup from infusion and be back to slurry can, usually in the exit of constant displacement pump, check-valves is installed.
Above-mentioned interior tank body is connected with outer tank body by bearing usually, thus interior tank body can be moved in outer tank body transfer.Above-mentioned infusion is stirred in composite can, by arranging hermetically-sealed construction with lower end at its upper end, makes the connecting portion positiver sealing of interior tank body and outer tank body.
In preferred version, above-mentioned interior tank body top is installed with rotating shaft, and the rotating shaft of interior tank body is connected with outer tank body by bearing, and the rotating shaft of interior tank body and interior tank body device of rotation driving are in transmission connection.Above-mentioned interior tank body device of rotation driving can be arranged in outer tank body, also can be arranged in the frame beyond outer tank body.Usual above-mentioned interior tank body device of rotation driving comprises motor, and motor is arranged in outer tank body, and the rotating shaft of interior tank body is connected with the output shaft of motor by shaft coupling.Or above-mentioned interior tank body device of rotation driving comprises motor and transmission mechanism (as driving-belt, gear train etc.), motor is arranged in the frame in outer tank body or beyond outer tank body, and the power output shaft of motor is connected by the rotating shaft of transmission mechanism with interior tank body.By regulating the rotating speed of motor, the adjustment of interior tank body rotating speed can be realized.
When above-mentioned interior tank body rotates in tank body outside, can heat the syrup in crack and stir, syrup is heated more even, and improve firing rate.In order to strengthen mixing effect further, in preferred version, the lateral wall of above-mentioned interior tank body is provided with multiple stirring vane.More preferably, in scheme, above-mentioned stirring vane is fixed on the blade strip on the lateral wall of interior tank body, and blade strip is parallel with the axis direction of interior tank body.Above-mentioned stirring vane is uniformly distributed usually on the lateral wall of interior tank body.When interior tank body rotates, stirring vane rotates together with interior tank body, stirs more fully the syrup in crack.Above-mentioned stirring vane preferably adopts polytetrafluoroethylene (PTFE) (being commonly called as King) to make.
Usually, the tank skin of above-mentioned outer tank body is made up of outer cylinder and inner cylinder, and the space between outer cylinder and inner cylinder forms above-mentioned first mezzanine space.
In preferred version, combinations thereof tank charging aperture is located at infusion and is stirred bottom composite can, and composite can discharging opening is located at infusion and is stirred composite can top, and like this, the syrup in above-mentioned crack flows from bottom to top.
In preferred version, above-mentioned outer tank body top is provided with the first steam inlet be communicated with the first mezzanine space, the first condensation-water drain be communicated with the first mezzanine space is provided with bottom outer tank body, first steam inlet is communicated with steam supply device by steam pipeline, like this, the steam in the first mezzanine space flows from top to bottom.When from the first steam inlet in the first mezzanine space during delivering vapor, steam can to the syrup heating in outer tank body and crack, and syrup is heated up, and after steam heat radiation, the water of generation is discharged from the first condensation-water drain.
In preferred version, above-mentioned interior tank base is provided with two-way steam swivel joint, two-way steam swivel joint has steam access port and condensed water discharge outlet, steam access port and condensed water discharge outlet are all communicated with the cavity of interior tank body, wherein steam access port is communicated with steam supply device by steam pipeline, the water that condensed water discharge outlet produces after being used for exhaust steam heat radiation.
Above-mentioned vacuum tank chuck is provided with the second steam inlet and the second condensation-water drain that are communicated with the second mezzanine space, and wherein the second steam inlet is communicated with steam supply device by steam pipeline.When from the second steam inlet in the second mezzanine space during delivering vapor, steam can to the syrup heating in vacuum tank and vacuum tank, and syrup is heated up, and after steam heat radiation, the water of generation is discharged from the second condensation-water drain.
In preferred version, funnel-form partition member is provided with in above-mentioned vacuum tank, the cavity of vacuum tank is divided into upper vacuum chamber and lower vacuum chamber by funnel-form partition member, syrup flow export is provided with bottom funnel-form partition member, syrup flow export is by upper vacuum chamber and lower vacuum chamber, and vacuum tank is provided with the syrup flow export opening-closing controller for controlling the opening and closing of syrup flow export; Upper vacuum chamber is all communicated with vacuum extractor with lower vacuum chamber.Under the control of syrup flow export opening-closing controller, syrup flow export can open or close.When syrup flow export is opened, upper vacuum chamber communicates with lower vacuum chamber, and the syrup in upper vacuum chamber can flow in lower vacuum chamber; When syrup flow export is closed, upper vacuum chamber and lower vacuum chamber isolated, can respectively to upper vacuum chamber, lower vacuum chamber by vacuum extractor.Therefore, by controlling opening or closing of syrup flow export, according to the requirement of dissimilar product, can select once to vacuumize or secondary vacuum pumping, get rid of the moisture in syrup.
Above-mentioned syrup flow export opening-closing controller can adopt switch valve, switch valve comprises switch valve seat, switch valve core and the switch valve core position adjusting mechanism for by-pass cock spool position, wherein switch valve seat is arranged on syrup flow export, switch valve core is in the cavity of switch valve seat, and switch valve core position adjusting mechanism to be located on vacuum tank and to be connected with switch valve core.
Usually, above-mentioned vacuum tank charging aperture is located at vacuum tank top, and vacuum tank discharging opening is located at bottom vacuum tank.
Through outflow opportunity of the syrup of infusion and flow, be preferably provided with unloading pump in above-mentioned vacuum tank discharge outlet for the ease of controlling, the syrup in vacuum tank can be extracted out by unloading pump.
Above-mentioned unloading pump can adopt modularization one package structual, and a pair rotor included by unloading pump is set to independently rotor module.Unloading pump supportingly can have the multiple rotor module be made up of difform rotor, different rotor module is interchangeable, like this, according to the requirement of dissimilar product, do not changing other structure of unloading pump, and under not increasing or reduce the condition of other part of unloading pump, realize the exchange of difformity rotor.In supporting rotor module, rotor can be quincunx rotor, crescent rotor, flute profile rotor.
The grout outlet of above-mentioned unloading pump is connected with syrup efferent duct.In preferred version, be provided with syrup efferent duct chuck outside the tube wall of above-mentioned syrup efferent duct, form the 3rd mezzanine space between the tube wall of syrup efferent duct chuck and syrup efferent duct, the 3rd mezzanine space is communicated with steam supply device by steam pipeline.Pass into steam in 3rd mezzanine space, the syrup in syrup efferent duct is incubated.
More preferably in scheme, above-mentioned syrup efferent duct chuck rear end is provided with the 3rd steam inlet be communicated with the 3rd mezzanine space, syrup efferent duct chuck front end is provided with the 3rd condensation-water drain be communicated with the 3rd mezzanine space, 3rd steam inlet is communicated with steam supply device by steam pipeline, like this, steam in 3rd mezzanine space flows from back to front, contrary with the flow direction of syrup in syrup efferent duct, be more conducive to the steam in the 3rd mezzanine space and the syrup in syrup efferent duct fully carries out heat exchange.When from the 3rd steam inlet in the 3rd mezzanine space during delivering vapor, steam can to the syrup heating in syrup efferent duct and syrup efferent duct, and the water produced after steam heat radiation is discharged from the 3rd condensation-water drain.
Above-mentioned vacuum extractor can adopt vavuum pump.When the cavity of vacuum tank is divided into vacuum chamber and lower vacuum chamber, upper vacuum chamber, lower vacuum chamber connect the inlet end of total exhaust tube respectively by upper exhaust tube, lower pumping pipe, the outlet side of total exhaust tube connects vavuum pump, upper exhaust tube is provided with vacuum valve, and lower pumping pipe is provided with lower vacuum valve.Upper vacuum valve is for controlling conducting or the cut-off of upper exhaust tube, and lower vacuum valve is for controlling conducting or the cut-off of lower pumping pipe.
Above-mentioned steam supply device comprises steam reservoir, the place that the high-temperature steam be stored in wherein for storing the high-temperature steam produced by steam production plant (as steam boiler), and is flowed to the first mezzanine space by steam pipeline by steam reservoir, the cavity, the second mezzanine space, the 3rd mezzanine space etc. of interior tank body need steam.
The water of discharging from the first condensation-water drain, condensed water discharge outlet, the second condensation-water drain, the 3rd condensation-water drain is communicated to by water return pipeline cylinder barrel collection of catchmenting, recoverable.
Above-mentioned outer tank body, interior tank body, vacuum tank, conveying pipeline, syrup efferent duct etc. can adopt 304 stainless steels of hygienic environment-protecting or 316 stainless steels to make.
Infusion of the present invention is stirred in composite can, steam can be passed into by the cavity of tank body in rotating, and the first mezzanine space in outer tank body passes into steam, inside and outside simultaneously in crack syrup heating, quick infusion in the crack of syrup between outer tank body and interior tank body, and the interior tank body rotated stirs the syrup in crack, syrup advances as carried out again diaphragm type scrolling wave while diaphragm type infusion, thus be one overall by traditional huge and the diaphragm type sugar boiling pot of complexity and diaphragm type agitator tank ingenious simplification optimum organization from theory and structure, realize functionally (the infusion function of comprehensive sugar boiling pot and the agitating function of agitator tank) and structural organic unity, structure is more simply compact, safe and reliable, and greatly shorten syrup delivery path, sugar cook efficiency is high, energy consumption is low, environmental protection and energy-conservation on there is distinctive feature, and the infusion quality of syrup and mixing quality effectively improve, the efficient high-quality syrup of output of energy, the syrup endured out more can ensure original flavor and color, quality is high.Also reduce device fabrication cost simultaneously, assemble, adjust, keep in repair convenient.Energy-saving continuous sugar-cooker of the present invention is compared with traditional sugar-cooker, and its cost performance is more superior.
Accompanying drawing explanation
Fig. 1 is the structural representation of the preferred embodiment of the present invention;
Fig. 2 is the structural representation that in Fig. 1, composite can bottom is stirred in infusion;
Fig. 3 is the enlarged drawing of vacuum tank in Fig. 1;
Fig. 4 is the schematic diagram of the first rotor of unloading pump in Fig. 1;
Fig. 5 is the schematic diagram of the second rotor of unloading pump in Fig. 1;
Fig. 6 is the schematic diagram of the third rotor of unloading pump in Fig. 1.
Detailed description of the invention
As shown in Figure 1, this energy-saving continuous sugar-cooker comprises slurry can 1, composite can 2, vacuum tank 3, vacuum extractor and steam supply device are stirred in infusion; Infusion is stirred composite can 2 and is comprised outer tank body 21 and interior tank body 22, the tank skin of outer tank body 21 has the first mezzanine space 23, interior tank body 22 is rotatably arranged in outer tank body 21, have crack 24 between the outer wall of interior tank body 22 and the inwall of outer tank body 21, infusion is stirred composite can 2 and is also comprised the interior tank body device of rotation driving that interior tank body 22 can be driven to rotate; Infusion is stirred composite can 2 and is provided with composite can charging aperture 25 and composite can discharging opening 26, and composite can charging aperture 25 and composite can discharging opening 26 are all communicated with described crack 24; Vacuum tank chuck 31 is provided with outside the tank skin of vacuum tank 3, the second mezzanine space 32 is formed between the tank skin of vacuum tank chuck 31 and vacuum tank 3, vacuum tank 3 is provided with vacuum tank charging aperture 33 and vacuum tank discharging opening 34, and vacuum tank charging aperture 33 is all communicated with the cavity of vacuum tank 3 with vacuum tank discharging opening 34; The discharging opening of storage tank 1 is communicated with composite can charging aperture 25 by conveying pipeline 4, and composite can discharging opening 26 is communicated with vacuum tank charging aperture 33 by conveying pipeline 5; The cavity of the first mezzanine space 23, interior tank body 22 is all communicated with steam supply device by steam pipeline 6 with the second mezzanine space 32, and the cavity of vacuum tank 3 is communicated with vacuum extractor.
Slurry can 1 treats the syrup of infusion for storing, slurry can 1 stirs composite can 2 by conveying pipeline 4 to infusion and carries syrup (syrup enters in the crack 24 between the outer wall of interior tank body 22 and the inwall of outer tank body 21); Conveying pipeline 4 between the discharging opening and composite can charging aperture 25 of slurry can 1 is provided with constant displacement pump 7, and the syrup in slurry can 1 can be extracted into infusion and stir in the crack 24 of composite can 2 by constant displacement pump 7.In the exit of constant displacement pump 7, check-valves 71 is installed, stirs composite can 2 to prevent syrup from infusion and be back to slurry can 1.
In the present embodiment, interior tank body 22 top is installed with rotating shaft 27, and the rotating shaft 27 of interior tank body 22 is connected with outer tank body 21 by bearing, and the rotating shaft 27 of interior tank body 22 is in transmission connection with interior tank body device of rotation driving.Interior tank body device of rotation driving comprises motor 28 and transmission mechanism (being driving-belt 29 in the present embodiment), and motor 28 is arranged in the frame beyond outer tank body 21, and the power output shaft of motor 28 is connected by the rotating shaft 27 of driving-belt 29 with interior tank body 22.By regulating the rotating speed of motor 28, the adjustment of interior tank body 22 rotating speed can be realized.
With reference to figure 2, the lateral wall of interior tank body 22 is provided with multiple stirring vane 210, and this stirring vane 210 is fixed on the blade strip on the lateral wall of interior tank body 22, and blade strip is parallel with the axis direction of interior tank body 22.Above-mentioned stirring vane 210 is uniformly distributed on the lateral wall of interior tank body 22 (circumference namely along interior tank body 22 is uniform).When interior tank body 22 rotates, stirring vane 210 rotates together with interior tank body 22, stirs the syrup in crack 24.Above-mentioned stirring vane 22 adopts polytetrafluoroethylene (PTFE) (being commonly called as King) to make.
With reference to figure 2, the tank skin of outer tank body 21 forms 212 by outer cylinder 211 and inner cylinder, and the space between outer cylinder 211 and inner cylinder 212 forms above-mentioned first mezzanine space 23.Composite can charging aperture 25 is located at infusion and is stirred bottom composite can 2, and composite can discharging opening 26 is located at infusion and is stirred composite can 2 top, and like this, the syrup in above-mentioned crack 24 is from bottom to top in wavy rising flowing.Outer tank body 21 top is provided with the first steam inlet 213 be communicated with the first mezzanine space 23, the first condensation-water drain 214 be communicated with the first mezzanine space 23 is provided with bottom outer tank body 21, first steam inlet 213 is communicated with steam supply device by steam pipeline 6, like this, the steam in the first mezzanine space 23 flows from top to bottom.
With reference to figure 2, two-way steam swivel joint 215 is provided with bottom interior tank body 22, two-way steam swivel joint 215 has steam access port 216 and condensed water discharge outlet 217, steam access port 216 and condensed water discharge outlet 217 are all communicated with the cavity of interior tank body 22, wherein steam access port 216 is communicated with steam supply device by steam pipeline 6, the water of condensed water discharge outlet 217 for producing after exhaust steam heat radiation.In the present embodiment, the condensate output transistor 219 that two-way steam swivel joint 215 comprises steam input pipe 218 and is sheathed on outside steam input pipe 218, steam input pipe 218 upper end is in the cavity of inner canister body 22, lower end is communicated with steam supply device (lower end of steam input pipe 218 is steam access port 216) by steam pipeline 6, and condensate output transistor 218 upper end is communicated with the cavity of interior tank body 22, lower end is provided with described condensed water discharge outlet 217.
With reference to figure 3, vacuum tank chuck 31 is provided with the second steam inlet 35 and the second condensation-water drain 36 be communicated with the second mezzanine space 32, and wherein the second steam inlet 35 is communicated with steam supply device by steam pipeline 6.In the present embodiment, funnel-form partition member 37 is provided with in vacuum tank 3, the cavity of vacuum tank 3 is divided into upper vacuum chamber 38 and lower vacuum chamber 39 by funnel-form partition member 37, syrup flow export 310 is provided with bottom funnel-form partition member 37, upper vacuum chamber 38 is communicated with lower vacuum chamber 39 by syrup flow export 310, and vacuum tank 3 is provided with the syrup flow export opening-closing controller for controlling syrup flow export 310 opening and closing; Upper vacuum chamber 38 is all communicated with vacuum extractor with lower vacuum chamber 39.Above-mentioned syrup flow export opening-closing controller adopts switch valve, this switch valve comprises switch valve seat 311, switch valve core 312, and for the switch valve core position adjusting mechanism of by-pass cock spool 312 position, wherein switch valve seat 311 is arranged on syrup flow export 310, switch valve core 312 is in the cavity of switch valve seat 311, switch valve core position adjusting mechanism to be located on vacuum tank 3 and to be connected with switch valve core 312 (with reference to figure 1 and Fig. 3, switch valve core position adjusting mechanism comprises lifting arm 313 and action bars 314, be hinged in a frame in the middle part of action bars 314, lifting arm 313 lower end connecting valve spool 312, upper end and action bars 314 one end hinged, press or lifting action bars 314 other end time switch valve core 312 can be made to rise or decline, realize the position adjustments of switch valve core 312).Under the control of syrup flow export opening-closing controller, syrup flow export 310 can open or close.When syrup flow export 310 is opened, upper vacuum chamber 38 communicates with lower vacuum chamber 39, and the syrup in upper vacuum chamber 38 can flow in lower vacuum chamber 39; When syrup flow export 310 is closed, upper vacuum chamber 38 is isolated with lower vacuum chamber 39, can be vacuumized upper vacuum chamber 38, lower vacuum chamber 39 respectively by vacuum extractor.By controlling opening or closing of syrup flow export 310, according to the requirement of dissimilar product, can select once to vacuumize or secondary vacuum pumping, get rid of the moisture in syrup.
Vacuum tank charging aperture 33 is located at vacuum tank 3 top, and vacuum tank discharging opening 34 is located at bottom vacuum tank 3.
Vacuum tank discharging opening 34 place is provided with unloading pump 8, and the syrup in vacuum tank 3 can be extracted out by unloading pump 8.
Unloading pump 8 adopts modularization one package structual, and a pair rotor 81 included by unloading pump 8 is set to independently rotor module.In the present embodiment, unloading pump 8 is supporting three rotor module be made up of difform rotor 81, different rotor module is interchangeable, with reference to figure 4-Fig. 6, in three supporting rotor module, rotor 81 is respectively quincunx rotor (Fig. 4), crescent rotor (Fig. 5), flute profile rotor (Fig. 6).According to the requirement of dissimilar product, do not changing other structure of unloading pump 8, and under not increasing or reduce the condition of other part of unloading pump 8, realizing the exchange of difformity rotor 81.
The grout outlet of unloading pump 8 is connected with syrup efferent duct 9, syrup efferent duct chuck 91 is provided with outside the tube wall of syrup efferent duct 9, form the 3rd mezzanine space the 92, three mezzanine space 92 between syrup efferent duct chuck 91 and the tube wall of syrup efferent duct 9 to be communicated with steam supply device by steam pipeline 6.Syrup efferent duct chuck 91 rear end is provided with the 3rd steam inlet 93 be communicated with the 3rd mezzanine space 92, syrup efferent duct chuck 91 front end is provided with the 3rd condensation-water drain 94 be communicated with the 3rd mezzanine space 92,3rd steam inlet 93 is communicated with steam supply device by steam pipeline 6, like this, steam in 3rd mezzanine space 92 flows from back to front, contrary with the flow direction of syrup in syrup efferent duct 9, be conducive to the steam in the 3rd mezzanine space 92 and the syrup in syrup efferent duct 9 fully carries out heat exchange.
Above-mentioned vacuum extractor adopts vavuum pump 10.In the present embodiment, upper vacuum chamber 38, lower vacuum chamber 39 connect the inlet end of total exhaust tube 13 respectively by upper exhaust tube 11, lower pumping pipe 12, the outlet side of total exhaust tube 13 connects vavuum pump 10, and upper exhaust tube 11 is provided with vacuum valve 14, and lower pumping pipe 12 is provided with lower vacuum valve 15.Upper vacuum valve 14 is for controlling conducting or the cut-off of upper exhaust tube 11, and lower vacuum valve 15 is for controlling conducting or the cut-off of lower pumping pipe 12.Upper vacuum chamber 38 is connected with vacuum meter 16, and lower vacuum chamber 39 is connected with vacuum meter 17.
Above-mentioned steam supply device comprises steam reservoir 18, the place that the high-temperature steam be stored in wherein for storing the high-temperature steam produced by steam production plant (as steam boiler), and is flowed to the first mezzanine space 23 by steam pipeline 6 by steam reservoir 18, the cavity, the second mezzanine space 32, the 3rd mezzanine space 92, unloading pump 8 etc. of interior tank body 22 need steam.In the present embodiment, steam reservoir 18 is by the cavity delivering vapor of a steam pipeline 6 to the first mezzanine space 23, interior tank body 22, by another steam pipeline 6 to the second mezzanine space 32, the 3rd mezzanine space 92 delivering vapor, two steam pipelines 6 are equipped with stop valve 181, pressure-reducing valve 182, safety valve 183, Pressure gauge 184 and flow divider 185.
Outer tank body 21, interior tank body 22, vacuum tank 3, conveying pipeline 4, conveying pipeline 5, syrup efferent duct 9 etc. can adopt 304 stainless steels of hygienic environment-protecting or 316 stainless steels to make.
The operation principle of brief description once this energy-saving continuous sugar-cooker:
Deployed syrup is first stored in slurry can 1; Syrup in slurry can 1 is extracted into infusion through conveying pipeline 4 and stirs in the crack 24 of composite can 2 by constant displacement pump 7, carries out infusion, stirring; The syrup stirred after composite can 2 infusion, stirring through infusion enters in vacuum tank 3 through conveying pipeline 5, is extracted the moisture in syrup by vavuum pump 10; Syrup in vacuum tank 3 is extracted out by unloading pump 8, and flows out through syrup efferent duct 9, enters next procedure.
Stir in composite can 2 in infusion, it is backward interior to the syrup heating in crack 24 that the first mezzanine space 23 in outer tank body 21 passes into steam, the cavity of interior tank body 22 passes into that steam is backward to be heated the syrup in crack 24 outward, simultaneously, interior tank body 22 rotates under the driving of interior tank body device of rotation driving, syrup in crack 24 is stirred (syrup in crack 24 rotates from bottom to top in wavy rising feeding around interior tank body 22), like this, realizes two film high speed infusion and stirring.
When from the first steam inlet 213 in the first mezzanine space 23 during delivering vapor, steam is to the syrup heating in outer tank body 21 and crack 24, and the water produced after steam heat radiation is discharged from the first condensation-water drain 214.When in the cavity from the inside tank body 22 of steam input pipe 218 during delivering vapor, syrup heating in the internal tank body 22 of steam and crack 24, the water produced after steam heat radiation, through the gap between steam input pipe 218 outer wall and condensate output transistor 219 inwall, is discharged from condensed water discharge outlet 217.When from the second steam inlet 35 in the second mezzanine space 32 during delivering vapor, steam is to the syrup heating in vacuum tank 3 and vacuum tank 3, and the water produced after steam heat radiation is discharged from the second condensation-water drain 36.When from the 3rd steam inlet 93 in the 3rd mezzanine space 92 during delivering vapor, steam is to the syrup heating in syrup efferent duct 9 and syrup efferent duct 9, and the water produced after steam heat radiation is discharged from the 3rd condensation-water drain 94.
Be communicated to by water return pipeline 19, hydrophobic component 201 cylinder barrel 202 that catchments from the water of the first condensation-water drain 214, condensed water discharge outlet 217, second condensation-water drain 36, the 3rd condensation-water drain 94 discharge to collect, recoverable.
Claims (8)
1. an energy-saving continuous sugar-cooker, is characterized in that comprising slurry can, composite can, vacuum tank, vacuum extractor and steam supply device is stirred in infusion; Infusion is stirred composite can and is comprised outer tank body and interior tank body, the tank skin of outer tank body has the first mezzanine space, interior tank body is rotatably arranged in outer tank body, have crack between the outer wall of interior tank body and the inwall of outer tank body, infusion is stirred composite can and is also comprised the interior tank body device of rotation driving that interior tank body can be driven to rotate; Infusion is stirred composite can and is provided with composite can charging aperture and composite can discharging opening, and composite can charging aperture is all communicated with described crack with composite can discharging opening; Vacuum tank chuck is provided with outside the tank skin of vacuum tank, the second mezzanine space is formed between vacuum tank chuck and the tank skin of vacuum tank, vacuum tank is provided with vacuum tank charging aperture and vacuum tank discharging opening, and vacuum tank charging aperture is all communicated with the cavity of vacuum tank with vacuum tank discharging opening; The discharging opening of storage tank is communicated with composite can charging aperture by conveying pipeline, and composite can discharging opening is communicated with vacuum tank charging aperture by conveying pipeline; The cavity of the first mezzanine space, interior tank body is all communicated with steam supply device by steam pipeline with the second mezzanine space;
The lateral wall of described interior tank body is provided with multiple stirring vane;
Funnel-form partition member is provided with in described vacuum tank, the cavity of vacuum tank is divided into upper vacuum chamber and lower vacuum chamber by funnel-form partition member, syrup flow export is provided with bottom funnel-form partition member, syrup flow export is by upper vacuum chamber and lower vacuum chamber, and vacuum tank is provided with the syrup flow export opening-closing controller for controlling the opening and closing of syrup flow export; Upper vacuum chamber is all communicated with vacuum extractor with lower vacuum chamber.
2. energy-saving continuous sugar-cooker according to claim 1, is characterized in that: the conveying pipeline between the discharging opening of described slurry can and composite can charging aperture is provided with constant displacement pump.
3. energy-saving continuous sugar-cooker according to claim 1, is characterized in that: described interior tank body top is installed with rotating shaft, and the rotating shaft of interior tank body is connected with outer tank body by bearing, and the rotating shaft of interior tank body and interior tank body device of rotation driving are in transmission connection.
4. energy-saving continuous sugar-cooker according to claim 1, is characterized in that: described stirring vane is fixed on the blade strip on the lateral wall of interior tank body, and blade strip is parallel with the axis direction of interior tank body.
5. energy-saving continuous sugar-cooker according to claim 1, is characterized in that: described composite can charging aperture is located at infusion and is stirred bottom composite can, and composite can discharging opening is located at infusion and is stirred composite can top; Outer tank body top is provided with the first steam inlet be communicated with the first mezzanine space, and be provided with the first condensation-water drain be communicated with the first mezzanine space bottom outer tank body, the first steam inlet is communicated with steam supply device by steam pipeline.
6. energy-saving continuous sugar-cooker according to claim 1, it is characterized in that: described interior tank base is provided with two-way steam swivel joint, two-way steam swivel joint has steam access port and condensed water discharge outlet, steam access port and condensed water discharge outlet are all communicated with the cavity of interior tank body, and wherein steam access port is communicated with steam supply device by steam pipeline.
7. energy-saving continuous sugar-cooker according to claim 1, is characterized in that: described vacuum tank discharge outlet is provided with unloading pump, and the grout outlet of unloading pump is connected with syrup efferent duct; Be provided with syrup efferent duct chuck outside the tube wall of syrup efferent duct, form the 3rd mezzanine space between the tube wall of syrup efferent duct chuck and syrup efferent duct, the 3rd mezzanine space is communicated with steam supply device by steam pipeline.
8. energy-saving continuous sugar-cooker according to claim 7, it is characterized in that: a pair rotor included by described unloading pump is set to independently rotor module, unloading pump is supporting the multiple rotor module be made up of difform rotor, and different rotor module is interchangeable.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310742180.6A CN103652223B (en) | 2013-12-30 | 2013-12-30 | Energy-saving type continuous sugar boiling machine |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310742180.6A CN103652223B (en) | 2013-12-30 | 2013-12-30 | Energy-saving type continuous sugar boiling machine |
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| CN103652223A CN103652223A (en) | 2014-03-26 |
| CN103652223B true CN103652223B (en) | 2015-01-28 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105028851B (en) * | 2015-09-09 | 2018-06-15 | 广东好心情食品集团有限公司 | A kind of ultralow temperature healthy confectionery continuously boils equipment |
Citations (4)
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|---|---|---|---|---|
| CN101598950A (en) * | 2009-06-17 | 2009-12-09 | 东华大学 | Vacuum sugar boiling pot temperature intelligence controlling device and method |
| CN201976688U (en) * | 2011-03-03 | 2011-09-21 | 汕头市万盼食品有限公司 | Sugar boiling device |
| CN102397572A (en) * | 2010-09-17 | 2012-04-04 | 谷神生物科技集团有限公司 | Thermosensitive powder sterilization technology and equipment |
| CN202618189U (en) * | 2012-06-27 | 2012-12-26 | 都江堰天旺食品工业有限责任公司 | Full-automatic continuous vacuum sugar-cooking device |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101598950A (en) * | 2009-06-17 | 2009-12-09 | 东华大学 | Vacuum sugar boiling pot temperature intelligence controlling device and method |
| CN102397572A (en) * | 2010-09-17 | 2012-04-04 | 谷神生物科技集团有限公司 | Thermosensitive powder sterilization technology and equipment |
| CN201976688U (en) * | 2011-03-03 | 2011-09-21 | 汕头市万盼食品有限公司 | Sugar boiling device |
| CN202618189U (en) * | 2012-06-27 | 2012-12-26 | 都江堰天旺食品工业有限责任公司 | Full-automatic continuous vacuum sugar-cooking device |
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| CN103652223A (en) | 2014-03-26 |
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