CN105028851A - Continuous boiling equipment for ultralow temperature healthy candies - Google Patents
Continuous boiling equipment for ultralow temperature healthy candies Download PDFInfo
- Publication number
- CN105028851A CN105028851A CN201510431382.8A CN201510431382A CN105028851A CN 105028851 A CN105028851 A CN 105028851A CN 201510431382 A CN201510431382 A CN 201510431382A CN 105028851 A CN105028851 A CN 105028851A
- Authority
- CN
- China
- Prior art keywords
- syrup
- interlayer
- steam
- vacuum storehouse
- tank
- 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.)
- Granted
Links
Landscapes
- Confectionery (AREA)
Abstract
The invention discloses continuous boiling equipment for ultralow temperature healthy candies. A homogenization syrup boiling tank comprises an outer syrup tank, an outer heating interlayer, an inner steam tank, multiple blades, a rotating shaft and a motor, the outer heating interlayer is arranged on the outer wall of the outer syrup tank, the inner steam tank is installed inside an inner cavity of the outer syrup tank through the rotating shaft, the syrup conveying interlayer is formed by the outer wall of the inner steam tank and the inner wall of the outer syrup tank, and the multiple blades are divided into multiple blade ring groups and installed on the outer wall of the inner steam tank uniformly; the inlet end and the outlet end of the syrup conveying interlayer are connected with an inlet pump and a syrup moisture removing device respectively in a communicated mode; the outer heating interlayer and the inner steam tank are connected with a steam supply device in a communicated mode through a steam pipe. A syrup collecting bucket is arranged under a storage outlet of the syrup moisture removing device. The equipment is simple in structure and low in manufacturing cost, the syrup is heated at an ultralow temperature, the original color, taste and nutrition ingredients of candy products can be maintained, the elasticity is sufficient, the candies are not sticky to teeth even chewed over and over again, and the candies are more beneficial to human health.
Description
Technical field
The present invention relates to the sugared equipment of oneization, particularly relate to a kind of ultralow temperature healthy confectionery and boil equipment continuously.
Background technology
In candy production industry, the change sugar equipment being conventionally used to syrup is all simpler and cruder, generally include charging basket and agitator, syrup source, white granulated sugar, water are put in charging basket, heat while adopt agitator to be uniformly mixed, although be uniformly mixed mode structure this simple, its shortcoming is particularly evident, mainly there is the defect of following four aspects:
(1) owing to heating while stir, syrup water vapour directly overflows from the opening of charging basket, is full of whole workshop, causes serious environmental pollution, and the air conditioner refrigerating consuming more heating energy source and offset in workshop, causes energy waste;
(2) owing to there is the dead angle that cannot be stirred between agitator and the inwall of charging basket, syrup cannot be stirred, cause the candy each several part finally made uneven, be difficult to reach original flavor mouthfeel, tone is also uneven, affects the quality of candy;
(3) not to the step that the moisture in syrup evaporates, be difficult to reduce the moisture in syrup, the moisture in syrup is more, and causing the candy mouthfeel made poor, is also the key factor affecting candy quality;
(4) directly syrup is heated, easily burns situation, the syrup particularly located bottom charging basket, due to stir less than, more easily burn, cause waste, have a strong impact on the quality of candy.
For solving the problem, both at home and abroad the sugared equipment of change is made a big improvement, current change sugar equipment mainly comprises preheater, sugar boiling pot, vacuum tank, mixer, unloading pump etc., the sugared equipment of thisization can realize boiling continuously of syrup, and also to a certain extent moisture is evaporated, also improve the mouthfeel of candy to a certain extent.But, in order to the moisture in syrup is oozed out, need longer to boil path, therefore, cause device structure bulky complex, syrup flow path has more bending and path change, syrup flow path is also quite long, cause energy consumption large, reduced sugar and moisture content difficult parameters up to standard, product transparency, the uniformitys etc. are all subject to certain restrictions, ensure under implementation low-temperature energy-saving condition, just be difficult to realize keeping confectionary products color originally, original flavor mouthfeel, original nutrition, elastic foot, repeatedly chew and do not stick to one's teeth, this is the difficult problem that this professional equipment exists both at home and abroad always.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of ultralow temperature healthy confectionery and boils equipment continuously, this ultralow temperature healthy confectionery boils that device structure is simple, manufacturing cost is lower continuously, and syrup mixing is more even, transparency and the uniformity of confectionary products are increased substantially, and adopt ultralow temperature to add hot molass, confectionary products originally color, original flavor mouthfeel, original nutrition can be kept, elastic foot, repeatedly chew and do not stick to one's teeth, more be of value to health.The technical scheme adopted is as follows:
A kind of ultralow temperature healthy confectionery boils equipment continuously, comprise feed pump, steam supply device, syrup moisture removal device, syrup splicing bucket, steam pipe and syrup tube, it is characterized in that: also comprise homogenize infusion syrup can, homogenize infusion syrup can comprises syrup outer tank, external heat interlayer, steam inner canister, multiple blade, rotating shaft and motor; External heat interlayer is arranged on the lateral wall of syrup outer tank; The two ends of steam inner canister are rotatably arranged on by rotating shaft in the inner chamber of syrup outer tank, be provided with gap and form syrup delivery interlayer between the outer wall of steam inner canister and the inwall of syrup outer tank; Described multiple blade is divided into multiple blade ring group, each blade ring group is made up of multiple blade, each blade ring group is arranged on the outer wall of steam inner canister along the axis of steam inner canister equably, and each blade in each blade ring group is evenly arranged along the outer circumference of steam inner canister; Described feed pump is connected by the feed end of syrup tube and syrup delivery interlayer, and the discharge end of syrup delivery interlayer is connected by the charging aperture of syrup tube and described syrup moisture removal device; Steam inner canister, external heat interlayer are all connected by steam pipe and steam supply device; Described syrup splicing bucket is arranged on below the discharging opening of syrup moisture removal device.
The mounting means of above-mentioned blade is: one end of blade is connected with the outer wall of steam inner canister, has gap between the other end of blade and the inwall of syrup outer tank.
High-temperature steam is input in steam inner canister and external heat interlayer by steam supply device, the mode simultaneously heated inside and outside employing, and in steam, tank wall, external heat interlayer heat the syrup in syrup delivery interlayer simultaneously, syrup delivery is entered syrup delivery interlayer by syrup tube by feed pump, under the driving of motor, steam inner canister rotates in syrup outer tank, each blade ring group in steam on tank wall is along with rotation, from feed end toward discharge end, each blade ring group is pushed ahead the syrup in syrup delivery interlayer, in progradation, each blade stirs repeatedly to syrup, shear, finally heat, the syrup stirred outputs to syrup moisture removal device from the other end of syrup delivery interlayer, after the moisture in syrup moisture removal device removing syrup, output to syrup splicing bucket from the discharging opening of syrup moisture removal device.The present invention is by designing dexterously, preheater of the prior art, sugar boiling pot, vacuum tank, mixer are integrated into a homogenize infusion syrup can, it is simple for changing bulky complex, more concise in structure, simple, assembling, adjustment, easy to maintenance, dependable performance is practical, significantly reduces manufacturing cost, syrup delivery interlayer is formed by steam inner canister and syrup outer tank, syrup is carried in syrup delivery interlayer, and heated inside and outside being undertaken by steam inner canister, external heat interlayer simultaneously, from A-P by blade repeated stirring, shearing, there is not dead angle in heating, stirring, thus make the heating of syrup, mixing more even, increase substantially transparency and the uniformity of confectionary products, owing to syrup significantly being made thinner in syrup delivery interlayer, and by steam inner canister, external heat interlayer heats inside and outside carrying out simultaneously, particularly because the multiple blade ring groups on tank wall in steam stir syrup, shear, wave advances, syrup is evenly distributed in interlayer be fed forward, syrup repeatedly stirs in forward movement, shear, heating, thus the temperature considerably reduced needed for heating, realize adopting ultralow temperature to add hot molass, confectionary products color originally can be kept, original flavor mouthfeel, original nutrition, elastic foot, repeatedly chew and do not stick to one's teeth, more be of value to health.
As preferred version of the present invention, described blade comprises strip substrates, strip substrates has the side of two wider width and the narrower side of at least four width, at least one side offers guiding deep-slotted chip breaker to strip substrates, the length direction of guiding deep-slotted chip breaker is along the length direction of strip substrates, one side of strip substrates offers at least one homogenize deep-slotted chip breaker, the length direction of homogenize deep-slotted chip breaker is perpendicular to the length direction of strip substrates.Guiding deep-slotted chip breaker on blade and afterbody have guiding and progradation to syrup at the volley; Syrup is passing in the proal process of homogenize deep-slotted chip breaker, in previous moment, the flow direction of syrup is cut off by homogenize deep-slotted chip breaker, at subsequent time, blade stops the syrup in this flow direction, syrup is passed from the homogenize deep-slotted chip breaker of other blade, strengthens the shearing dynamics to syrup, realize the dislocation conveying of syrup, there is the effect of flexible homogenize syrup.
As the further preferred version of the present invention, the afterbody of described strip substrates is provided with inclined-plane.By arranging inclined-plane at strip substrates free end, guide functions is played to syrup.The inclination angle on preferred described inclined-plane is greater than 30 °.
As the further preferred version of the present invention, the radius r 1 > 3mm of described guiding deep-slotted chip breaker, the radius r 2 > 16mm of described homogenize deep-slotted chip breaker.
As the further preferred version of the present invention, described r2/r1 > 4.
As preferred version of the present invention, the syrup tube be connected between described syrup delivery interlayer and described syrup moisture removal device is horizontal duplex feed pipe for mortar.Syrup tube between syrup delivery interlayer and syrup moisture removal device is set to horizontal duplex feed pipe for mortar, boil on path at syrup, isolate the moisture in syrup in advance, enter syrup moisture removal device as a laminar flow, syrup is more prone to, more thoroughly with being separated of moisture.
As the further preferred version of the present invention, described horizontal duplex feed pipe for mortar comprises body and dividing plate, and the length of dividing plate is less than the length of body, and dividing plate is arranged in body and along the axis of body and extends, and dividing plate offers multiple through hole.Preferred described through hole is bar hole.Heating, stir after syrup export from syrup delivery interlayer, enter in horizontal duplex feed pipe for mortar, syrup flows to below dividing plate, and the steam in syrup then rises to above dividing plate through through hole, realizes being separated in advance of syrup and steam.
As preferred version of the present invention, described syrup moisture content removal device, comprises vacuum storehouse, lower vacuum storehouse, separatory funnel, barrel, upper vavuum pump, lower vavuum pump and control valve; Upper vacuum storehouse is arranged on above lower vacuum storehouse, separatory funnel is arranged between vacuum storehouse and lower vacuum storehouse, the upper end open of separatory funnel is tightly connected with the lower limb in upper vacuum storehouse, the top edge in lower vacuum storehouse respectively, control valve is arranged on the lower ending opening place of separatory funnel, the adjusting rod of control valve projects upwardly to outside vacuum storehouse, and the upper end of barrel is connected with the lower ending opening of separatory funnel; The bottom in lower vacuum storehouse is provided with discharging opening, and the top in upper vacuum storehouse is provided with charging aperture, and charging aperture is connected by syrup tube and described syrup delivery interlayer; Upper vavuum pump is connected by the top in tracheae and upper vacuum storehouse, and lower vavuum pump is connected by the top in tracheae and lower vacuum storehouse.By arranging upper vacuum storehouse, lower vacuum storehouse, upper vavuum pump, lower vavuum pump, upper vacuum storehouse, the upper and lower two-part vacuum draw steam discharge in lower vacuum storehouse are independent of each other.In upper vacuum storehouse, syrup spreads out by separatory funnel, and the moisture content contributed in syrup is dispersed out, and then by the suction of upper vavuum pump, more easily removes the moisture content in syrup, make the tone of candy, taste, mouthfeel better; By governor valve control flow, the syrup in vacuum storehouse is made to flow into lower vacuum storehouse in thread mode, the moisture content in syrup is made to come out further, and then by the suction of lower vavuum pump, moisture content in further removing syrup, make the tone of candy, taste, mouthfeel better, elastic foot, repeatedly chew and do not stick to one's teeth.
As the further preferred version of the present invention, the outer wall in described upper vacuum storehouse is provided with the first heat preservation sandwich layer, and the first heat preservation sandwich layer is connected by steam pipe and described steam supply device; The outer wall of described barrel is provided with the second heat preservation sandwich layer, and the second heat preservation sandwich layer is connected by steam pipe and described steam supply device.Namely be that outer insulation is set in upper vacuum storehouse, internal layer insulation be set in lower vacuum storehouse, syrup is directly incubated, guarantee that the syrup in lower vacuum storehouse carries out vacuum under the environment of insulation, be more conducive to the removal of syrup moisture.
As the further preferred version of the present invention, described syrup moisture content removal device also comprises water purification tank, and water purification tank is connected with upper vavuum pump, lower vavuum pump.By arranging water purification tank, the steam that upper vavuum pump, lower vavuum pump pump out being purified, avoids environmental pollution.
As preferred version of the present invention, described syrup splicing bucket is sandwich-type rotary unloading slurry bucket.The interlayer madial wall of sandwich-type rotary unloading slurry bucket adopts King F4, interlayer parcel the inside can be heatpiston, also can be vacuum, the interlayer lateral wall of sandwich-type rotary unloading slurry bucket adopts stainless steel or common metal container material to establish chromium coating, and the shape of sandwich-type rotary unloading slurry bucket is spherical or oval spherical.Syrup splicing bucket is set to sandwich-type rotary unloading slurry bucket, decrease the unloading pump on traditional syrup splicing bucket, shorten syrup and boil path, minimizing syrup boils the defect that operation after technological process often occurs, syrup fast cooling and mechanical friction is avoided to cause sand return phenomenon, keep confectionary products color, original flavor mouthfeel, original nutrition originally, make confectionary products more be of value to health.
Compared with prior art, tool has the following advantages in the present invention:
The present invention is by designing dexterously, preheater of the prior art, sugar boiling pot, vacuum tank, mixer are integrated into a homogenize infusion syrup can, it is simple for changing bulky complex, more concise in structure, simple, assembling, adjustment, easy to maintenance, dependable performance is practical, significantly reduces manufacturing cost, syrup delivery interlayer is formed by steam inner canister and syrup outer tank, syrup is carried in syrup delivery interlayer, and heated inside and outside being undertaken by steam inner canister, external heat interlayer simultaneously, from A-P by blade repeated stirring, shearing, there is not dead angle in heating, stirring, thus make the heating of syrup, mixing more even, increase substantially transparency and the uniformity of confectionary products, owing to syrup significantly being made thinner in syrup delivery interlayer, and by steam inner canister, external heat interlayer heats inside and outside carrying out simultaneously, particularly because the multiple blade ring groups on tank wall in steam stir syrup, shear, wave advances, syrup is evenly distributed in interlayer be fed forward, syrup repeatedly stirs in forward movement, shear, heating, thus the temperature considerably reduced needed for heating, realize adopting ultralow temperature to add hot molass, confectionary products color originally can be kept, original flavor mouthfeel, original nutrition, elastic foot, repeatedly chew and do not stick to one's teeth, more be of value to health.
Accompanying drawing explanation
Fig. 1 is the structural representation of the preferred embodiment for the present invention;
Fig. 2 is the structural representation of blade;
Fig. 3 is the sectional view of Fig. 2 along A-A;
Fig. 4 is the structural representation of horizontal duplex feed pipe for mortar;
Fig. 5 is the sectional view of Fig. 4 along B-B;
Fig. 6 is the structural representation of syrup moisture removal device.
Detailed description of the invention
Be described further below in conjunction with accompanying drawing and the preferred embodiment of the present invention.
As shown in Figure 1, this ultralow temperature healthy confectionery boils equipment continuously, comprises feed pump 1, steam supply device 2, syrup moisture removal device 3, sandwich-type rotary unloading slurry bucket 4, steam pipe 5, syrup tube 6 and homogenize infusion syrup can 7; Homogenize infusion syrup can 7 comprises syrup outer tank 701, external heat interlayer 702, steam inner canister 703, multiple blade 704, rotating shaft 705 and motor 706; External heat interlayer 702 is arranged on the lateral wall of syrup outer tank 701; The two ends of steam inner canister 703 are rotatably arranged on by rotating shaft 705 in the inner chamber of syrup outer tank 701, be provided with gap and form syrup delivery interlayer 707 between the outer wall of steam inner canister 703 and the inwall of syrup outer tank 701; Multiple blade 704 is divided into multiple blade ring group 708, each blade ring group 708 is made up of multiple blade 704, each blade ring group 708 is arranged on the outer wall of steam inner canister 703 along the axis of steam inner canister 703 equably, and each blade 704 in each blade ring group 708 is evenly arranged along the outer circumference of steam inner canister 703; Feed pump 1 is connected by the feed end of syrup tube 6 with syrup delivery interlayer 707, and the discharge end of syrup delivery interlayer 707 is connected by the charging aperture of syrup tube 6 with syrup moisture removal device 3; Steam inner canister 703, external heat interlayer 702 are all connected by steam pipe 5 and steam supply device 2; Sandwich-type rotary unloading slurry bucket 4 is arranged on below the discharging opening of syrup moisture removal device 3.
Above-mentioned rotating shaft 705 generally adopts hollow rotating shaft, and hollow rotating shaft extend in the inner chamber of steam inner canister 703, and steam supply device 2 is connected with the outer end of hollow rotating shaft by steam pipe 5, and steam enters into the inner chamber of steam inner canister 703 by hollow rotating shaft.
The mounting means of above-mentioned blade 704 is: one end of blade 704 is connected with the outer wall of steam inner canister 703, has gap between the other end of blade 704 and the inwall of syrup outer tank 701.
As shown in Figure 2 and Figure 3, above-mentioned blade 704 comprises strip substrates 7041, strip substrates 7041 has the side of two wider width and the narrower side of at least four width, one side of strip substrates 7041 offers guiding deep-slotted chip breaker 7042, the length direction of guiding deep-slotted chip breaker 7042 is along the length direction of strip substrates 7041, one side of strip substrates 7041 offers homogenize deep-slotted chip breaker 7043, the length direction of homogenize deep-slotted chip breaker 7043 is perpendicular to the length direction of strip substrates 7041, and the afterbody of strip substrates 7041 is provided with inclined-plane 7044.The inclination angle on preferred inclined-plane 7044 is greater than 30 °.The radius r 1 > 3mm of preferred guiding deep-slotted chip breaker 7042, the radius r 2 > 16mm of homogenize deep-slotted chip breaker 7043, further preferred r2/r1 > 4.
As shown in Figure 4 and Figure 5, the above-mentioned syrup tube 6 be connected between syrup delivery interlayer 707 and syrup moisture removal device 3 is horizontal duplex feed pipe for mortar 60, horizontal duplex feed pipe for mortar 60 comprises body 601 and dividing plate 602, the length of dividing plate 602 is less than the length of body 601, dividing plate 602 is arranged in body 601 and along the axis of body 601 and extends, and dividing plate 602 offers multiple bar hole 603.
As shown in figures 1 to 6, syrup moisture content removal device 3, comprises vacuum storehouse 301, lower vacuum storehouse 302, separatory funnel 303, barrel 304, upper vavuum pump 305, lower vavuum pump 306, control valve 307 and water purification tank 308; Upper vacuum storehouse 301 is arranged on above lower vacuum storehouse 302, separatory funnel 303 is arranged between vacuum storehouse 301 and lower vacuum storehouse 302, the upper end open of separatory funnel 303 is tightly connected with the lower limb in upper vacuum storehouse 301, the top edge in lower vacuum storehouse 302 respectively, control valve 307 is arranged on the lower ending opening place of separatory funnel 303, the adjusting rod of control valve 307 projects upwardly to outside vacuum storehouse 301, and the upper end of barrel 304 is connected with the lower ending opening of separatory funnel 303; The bottom in lower vacuum storehouse 302 is provided with discharging opening, and the top in upper vacuum storehouse 301 is provided with charging aperture, and charging aperture is connected by syrup tube 6 and syrup delivery interlayer 707; Upper vavuum pump 305 is connected by the top of tracheae 8 with upper vacuum storehouse 301, and lower vavuum pump 306 is connected by the top of tracheae 8 with lower vacuum storehouse 302; Water purification tank 308 is connected with upper vavuum pump 305, lower vavuum pump 306; The outer wall in upper vacuum storehouse 301 is provided with the first heat preservation sandwich layer 309, first heat preservation sandwich layer 309 and is connected by steam pipe 5 and steam supply device 2; The outer wall of barrel 304 is provided with the second heat preservation sandwich layer 310, second heat preservation sandwich layer 310 and is connected by steam pipe 5 and steam supply device 2.
Above-mentioned sandwich-type rotary unloading slurry bucket 4 generally comprises staving, bearing, gear shaft, gear drive group and electric rotating machine, the lower end of gear shaft is rotatably arranged on bearing, the bottom of staving is arranged on the upper end of gear shaft, and electric rotating machine is connected with gear spindle drive by gear drive group.Electric rotating machine is rotated by gear drive group driven gear axle, thus drives staving to rotate.The interlayer madial wall of the staving of above-mentioned sandwich-type rotary unloading slurry bucket 4 adopts King F4, interlayer parcel the inside can be heatpiston, also can be vacuum, the interlayer lateral wall of the staving of sandwich-type rotary unloading slurry bucket 4 adopts stainless steel or common metal container material to establish chromium coating, and the staving shape of sandwich-type rotary unloading slurry bucket 4 is spherical or oval spherical.
Below in conjunction with accompanying drawing, the course of work of equipment is boiled continuously to this ultralow temperature healthy confectionery and advantage is further described.
High-temperature steam is input in steam inner canister 703 and external heat interlayer 702 by steam supply device 2, the mode simultaneously heated inside and outside employing, and steam inner canister 703 outer wall, external heat interlayer 702 heat the syrup in syrup delivery interlayer 707 simultaneously, syrup delivery is entered syrup delivery interlayer 707 by syrup tube 6 by feed pump 1, under the driving of motor 706, steam inner canister 703 rotates in syrup outer tank 701, each blade ring group 708 on steam inner canister 703 outer wall is along with rotation, from feed end toward discharge end, syrup in each blade ring group 708 pairs of syrup delivery interlayers 707 is pushed ahead, in progradation, each blade 704 pairs of syrup stir repeatedly, shear, finally heat, the syrup stirred outputs to syrup moisture removal device 3 from the other end of syrup delivery interlayer 707, after syrup moisture removal device 3 removes the moisture in syrup, output to sandwich-type rotary unloading slurry bucket 4 from the discharging opening of syrup moisture removal device 3.The present invention is by designing dexterously, preheater of the prior art, sugar boiling pot, vacuum tank, mixer are integrated into a homogenize infusion syrup can 7, it is simple for changing bulky complex, more concise in structure, simple, assembling, adjustment, easy to maintenance, dependable performance is practical, significantly reduces manufacturing cost, syrup delivery interlayer 707 is formed by steam inner canister 703 and syrup outer tank 701, syrup is carried in syrup delivery interlayer 707, and heated inside and outside being undertaken by steam inner canister 703, external heat interlayer 702 simultaneously, from A-P by blade repeated stirring, shearing, there is not dead angle in heating, stirring, thus make the heating of syrup, mixing more even, increase substantially transparency and the uniformity of confectionary products, owing to syrup significantly being made thinner in syrup delivery interlayer 707, and by steam inner canister 703, heat inside and outside external heat interlayer 702 carries out simultaneously, particularly because the multiple blade ring groups 708 pairs of syrup on steam inner canister 703 outer wall stir, shear, wave advances, syrup is evenly distributed in syrup delivery interlayer 707 be fed forward, syrup repeatedly stirs in forward movement, shear, heating, thus the temperature considerably reduced needed for heating, realize adopting ultralow temperature to add hot molass, confectionary products color originally can be kept, original flavor mouthfeel, original nutrition, elastic foot, repeatedly chew and do not stick to one's teeth, more be of value to health.
In addition, the guiding deep-slotted chip breaker 7042 on blade 704 and afterbody have guiding and progradation to syrup at the volley; Syrup is passing in the proal process of homogenize deep-slotted chip breaker 7043, in previous moment, the flow direction of syrup is cut off by homogenize deep-slotted chip breaker 7043, at subsequent time, blade stops the syrup in this flow direction, syrup is passed from the homogenize deep-slotted chip breaker 7043 of other blade 704, strengthens the shearing dynamics to syrup, realize the dislocation conveying of syrup, there is the effect of flexible homogenize syrup.
In addition, syrup tube 6 between syrup delivery interlayer 707 and syrup moisture removal device 3 is set to horizontal duplex feed pipe for mortar 60, syrup after heating, stirring exports from syrup delivery interlayer 707, enter in horizontal duplex feed pipe for mortar, syrup flows to below dividing plate 602, steam in syrup then rises to above dividing plate 602 through bar hole 603, boil on path at syrup, isolate the moisture in syrup in advance, enter syrup moisture removal device 3 as a laminar flow, syrup is more prone to, more thoroughly with being separated of moisture.
In addition, by arranging upper vacuum storehouse 301, lower vacuum storehouse 302, upper vavuum pump 305, lower vavuum pump 306, upper vacuum storehouse 301, the two-part vacuum draw steam discharge in lower vacuum storehouse about 302 are independent of each other.In upper vacuum storehouse 301, syrup spreads out by separatory funnel 303, and the moisture content contributed in syrup is dispersed out, and then by the suction of upper vavuum pump 305, more easily removes the moisture content in syrup, make the tone of candy, taste, mouthfeel better; Flow is controlled by control valve 307, the syrup in vacuum storehouse 301 is made to flow into lower vacuum storehouse in thread mode, the moisture content in syrup is made to come out further, and then by the suction of lower vavuum pump 306, moisture content in further removing syrup, make the tone of candy, taste, mouthfeel better, elastic foot, repeatedly chew and do not stick to one's teeth.The outer wall of barrel 304 is provided with the second heat preservation sandwich layer 310, second heat preservation sandwich layer 310 is connected by steam pipe 5 and steam supply device 2, syrup is directly incubated, guarantees that the syrup in lower vacuum storehouse 302 carries out vacuum under the environment of insulation, be more conducive to the removal of syrup moisture.By arranging water purification tank 308, the steam that upper vavuum pump 305, lower vavuum pump 306 pump out being purified, avoids environmental pollution.
In addition, syrup splicing bucket is set to sandwich-type rotary unloading slurry bucket 4, decrease the unloading pump on traditional syrup splicing bucket, shorten syrup and boil path, minimizing syrup boils the defect that operation after technological process often occurs, avoid syrup fast cooling and mechanical friction to cause sand return phenomenon, keep confectionary products color, original flavor mouthfeel, original nutrition originally, make confectionary products more be of value to health.
In addition; it should be noted that, the specific embodiment described in this description, its each several part title etc. can be different; all equivalences of doing according to structure, feature and the principle described in inventional idea of the present invention or simple change, be included in the protection domain of patent of the present invention.Those skilled in the art can make various amendment or supplement or adopt similar mode to substitute to described specific embodiment; only otherwise depart from structure of the present invention or surmount this scope as defined in the claims, protection scope of the present invention all should be belonged to.
Claims (10)
1. a ultralow temperature healthy confectionery boils equipment continuously, comprise feed pump, steam supply device, syrup moisture removal device, syrup splicing bucket, steam pipe and syrup tube, it is characterized in that: also comprise homogenize infusion syrup can, homogenize infusion syrup can comprises syrup outer tank, external heat interlayer, steam inner canister, multiple blade, rotating shaft and motor; External heat interlayer is arranged on the lateral wall of syrup outer tank; The two ends of steam inner canister are rotatably arranged on by rotating shaft in the inner chamber of syrup outer tank, be provided with gap and form syrup delivery interlayer between the outer wall of steam inner canister and the inwall of syrup outer tank; Described multiple blade is divided into multiple blade ring group, each blade ring group is made up of multiple blade, each blade ring group is arranged on the outer wall of steam inner canister along the axis of steam inner canister equably, and each blade in each blade ring group is evenly arranged along the outer circumference of steam inner canister; Described feed pump is connected by the feed end of syrup tube and syrup delivery interlayer, and the discharge end of syrup delivery interlayer is connected by the charging aperture of syrup tube and described syrup moisture removal device; Steam inner canister, external heat interlayer are all connected by steam pipe and steam supply device; Described syrup splicing bucket is arranged on below the discharging opening of syrup moisture removal device.
2. ultralow temperature healthy confectionery as claimed in claim 1 boils equipment continuously, it is characterized in that: described blade comprises strip substrates, strip substrates has the side of two wider width and the narrower side of at least four width, at least one side offers guiding deep-slotted chip breaker to strip substrates, the length direction of guiding deep-slotted chip breaker is along the length direction of strip substrates, one side of strip substrates offers at least one homogenize deep-slotted chip breaker, the length direction of homogenize deep-slotted chip breaker is perpendicular to the length direction of strip substrates.
3. ultralow temperature healthy confectionery as claimed in claim 2 boils equipment continuously, it is characterized in that: the afterbody of described strip substrates is provided with inclined-plane.
4. ultralow temperature healthy confectionery as claimed in claim 2 boils equipment continuously, it is characterized in that: the radius r 1 > 3mm of described guiding deep-slotted chip breaker, the radius r 2 > 16mm of described homogenize deep-slotted chip breaker.
5. ultralow temperature healthy confectionery as claimed in claim 1 boils equipment continuously, it is characterized in that: the syrup tube be connected between described syrup delivery interlayer and described syrup moisture removal device is horizontal duplex feed pipe for mortar.
6. ultralow temperature healthy confectionery as claimed in claim 5 boils equipment continuously, it is characterized in that: described horizontal duplex feed pipe for mortar comprises body and dividing plate, the length of dividing plate is less than the length of body, and dividing plate is arranged in body and along the axis of body and extends, and dividing plate offers multiple through hole.
7. ultralow temperature healthy confectionery as claimed in claim 1 boils equipment continuously, it is characterized in that: described syrup moisture content removal device, comprises vacuum storehouse, lower vacuum storehouse, separatory funnel, barrel, upper vavuum pump, lower vavuum pump and control valve; Upper vacuum storehouse is arranged on above lower vacuum storehouse, separatory funnel is arranged between vacuum storehouse and lower vacuum storehouse, the upper end open of separatory funnel is tightly connected with the lower limb in upper vacuum storehouse, the top edge in lower vacuum storehouse respectively, control valve is arranged on the lower ending opening place of separatory funnel, the adjusting rod of control valve projects upwardly to outside vacuum storehouse, and the upper end of barrel is connected with the lower ending opening of separatory funnel; The bottom in lower vacuum storehouse is provided with discharging opening, and the top in upper vacuum storehouse is provided with charging aperture, and charging aperture is connected by syrup tube and described syrup delivery interlayer; Upper vavuum pump is connected by the top in tracheae and upper vacuum storehouse, and lower vavuum pump is connected by the top in tracheae and lower vacuum storehouse.
8. ultralow temperature healthy confectionery as claimed in claim 7 boils equipment continuously, and it is characterized in that: the outer wall in described upper vacuum storehouse is provided with the first heat preservation sandwich layer, the first heat preservation sandwich layer is connected by steam pipe and described steam supply device; The outer wall of described barrel is provided with the second heat preservation sandwich layer, and the second heat preservation sandwich layer is connected by steam pipe and described steam supply device.
9. ultralow temperature healthy confectionery as claimed in claim 7 boils equipment continuously, it is characterized in that: described syrup moisture content removal device also comprises water purification tank, and water purification tank is connected with upper vavuum pump, lower vavuum pump.
10. ultralow temperature healthy confectionery as claimed in claim 1 boils equipment continuously, it is characterized in that: described syrup splicing bucket is sandwich-type rotary unloading slurry bucket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510431382.8A CN105028851B (en) | 2015-09-09 | 2015-09-09 | A kind of ultralow temperature healthy confectionery continuously boils equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510431382.8A CN105028851B (en) | 2015-09-09 | 2015-09-09 | A kind of ultralow temperature healthy confectionery continuously boils equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105028851A true CN105028851A (en) | 2015-11-11 |
| CN105028851B CN105028851B (en) | 2018-06-15 |
Family
ID=54436321
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510431382.8A Active CN105028851B (en) | 2015-09-09 | 2015-09-09 | A kind of ultralow temperature healthy confectionery continuously boils equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105028851B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105496783A (en) * | 2015-12-15 | 2016-04-20 | 浙江健牌机械科技有限公司 | Automatic syrup preparation and conveying tank |
| CN108271908A (en) * | 2018-04-08 | 2018-07-13 | 张方富 | A kind of sweet potato pumpkin is the preparation method and its device of the soft sweets of major ingredient |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2688068Y (en) * | 2004-04-16 | 2005-03-30 | 华南理工大学 | Apparatus for manufacturing functional candies |
| CN202618188U (en) * | 2012-06-27 | 2012-12-26 | 都江堰天旺食品工业有限责任公司 | Air exhaust tank for continuous vacuum sugar-boiling equipment |
| CN203120892U (en) * | 2013-02-25 | 2013-08-14 | 广东好心情食品集团有限公司 | Environment-friendly energy-saving syrup stirring equipment |
| CN103652223A (en) * | 2013-12-30 | 2014-03-26 | 广东好心情食品集团有限公司 | Energy-saving type continuous sugar boiling machine |
| CN204120819U (en) * | 2014-07-30 | 2015-01-28 | 陈磊 | Automatic steam mashing off system |
| CN104805224A (en) * | 2015-04-02 | 2015-07-29 | 广西大学 | Originally ecological black sugar processing device |
| CN204969277U (en) * | 2015-09-09 | 2016-01-20 | 广东好心情食品集团有限公司 | System equipment is endured in succession to healthy candy of ultra -low temperature |
-
2015
- 2015-09-09 CN CN201510431382.8A patent/CN105028851B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2688068Y (en) * | 2004-04-16 | 2005-03-30 | 华南理工大学 | Apparatus for manufacturing functional candies |
| CN202618188U (en) * | 2012-06-27 | 2012-12-26 | 都江堰天旺食品工业有限责任公司 | Air exhaust tank for continuous vacuum sugar-boiling equipment |
| CN203120892U (en) * | 2013-02-25 | 2013-08-14 | 广东好心情食品集团有限公司 | Environment-friendly energy-saving syrup stirring equipment |
| CN103652223A (en) * | 2013-12-30 | 2014-03-26 | 广东好心情食品集团有限公司 | Energy-saving type continuous sugar boiling machine |
| CN204120819U (en) * | 2014-07-30 | 2015-01-28 | 陈磊 | Automatic steam mashing off system |
| CN104805224A (en) * | 2015-04-02 | 2015-07-29 | 广西大学 | Originally ecological black sugar processing device |
| CN204969277U (en) * | 2015-09-09 | 2016-01-20 | 广东好心情食品集团有限公司 | System equipment is endured in succession to healthy candy of ultra -low temperature |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105496783A (en) * | 2015-12-15 | 2016-04-20 | 浙江健牌机械科技有限公司 | Automatic syrup preparation and conveying tank |
| CN108271908A (en) * | 2018-04-08 | 2018-07-13 | 张方富 | A kind of sweet potato pumpkin is the preparation method and its device of the soft sweets of major ingredient |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105028851B (en) | 2018-06-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN211199162U (en) | Crude rice bran oil equipment of coming unstuck | |
| US9675945B2 (en) | Device for the continuous treatment of at least one raw material, treatment installation and use of such a device | |
| CN102178332A (en) | Equipment for preparing bean pulp solid-state fermentation substrate material and use method thereof | |
| CN102599473A (en) | Vertical cooling tank | |
| CN105028851A (en) | Continuous boiling equipment for ultralow temperature healthy candies | |
| CN204969277U (en) | System equipment is endured in succession to healthy candy of ultra -low temperature | |
| CN219308407U (en) | Honey low temperature system of processing | |
| CN219463104U (en) | Stirred tank is used in acidophilus milk preparation | |
| CN208755098U (en) | A kind of food steaming machine being heated evenly | |
| CN208275316U (en) | A kind ofization sugar bowl | |
| CN205266920U (en) | Biax differential fodder quenching and tempering ware | |
| CN216493398U (en) | Soft-shelled turtle fodder heating equipment that rolls | |
| CN211246151U (en) | High fine and smooth taste light fat drink dosing unit | |
| CN2704195Y (en) | Multifunctional seed wrapping apparatus | |
| CN207027921U (en) | A kind of sponge foaming agitating device | |
| KR101446764B1 (en) | Feed making apparatus with double screw | |
| CN206453137U (en) | A kind of constant temperature blanching device | |
| CN220835418U (en) | Ascorbyl palmitate mixing arrangement | |
| CN213428091U (en) | Evaporated concentration equipment of condensed milk | |
| CN219631107U (en) | Heat preservation agitating unit that chocolate production was used | |
| CN105536597B (en) | A kind of blender | |
| CN220779080U (en) | Even cooling crystallizer for D-sodium erythorbate | |
| CN220514070U (en) | Novel pickled vegetable agitator tank | |
| CN221244672U (en) | Compound honey product mixing equipment | |
| CN220634634U (en) | Pine mushroom thawing and pulping device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zheng Yiguang Inventor after: Wang Zhenfa Inventor after: Dai Jun Inventor after: Wang Shidan Inventor before: Zheng Yiguang Inventor before: Wang Zhenfa Inventor before: Wang Shidan |
|
| GR01 | Patent grant |