CN107841577A - A kind of production method and its process units of starch sugar particle - Google Patents

A kind of production method and its process units of starch sugar particle Download PDF

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Publication number
CN107841577A
CN107841577A CN201711355277.6A CN201711355277A CN107841577A CN 107841577 A CN107841577 A CN 107841577A CN 201711355277 A CN201711355277 A CN 201711355277A CN 107841577 A CN107841577 A CN 107841577A
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Prior art keywords
starch sugar
adhesive
starch
mesh
comminutor
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CN201711355277.6A
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刘伟杰
景栋
张圣军
赵长礼
秦玉国
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WEIFANG SHENGTAI MEDICINE CO Ltd
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WEIFANG SHENGTAI MEDICINE CO Ltd
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Priority to CN201711355277.6A priority Critical patent/CN107841577A/en
Publication of CN107841577A publication Critical patent/CN107841577A/en
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    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B50/00—Sugar products, e.g. powdered, lump or liquid sugar; Working-up of sugar
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
    • B01J2/04—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a gaseous medium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/16—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
    • C—CHEMISTRY; METALLURGY
    • C13—SUGAR INDUSTRY
    • C13K—SACCHARIDES OBTAINED FROM NATURAL SOURCES OR BY HYDROLYSIS OF NATURALLY OCCURRING DISACCHARIDES, OLIGOSACCHARIDES OR POLYSACCHARIDES
    • C13K1/00—Glucose; Glucose-containing syrups
    • C13K1/06—Glucose; Glucose-containing syrups obtained by saccharification of starch or raw materials containing starch

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biochemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Glanulating (AREA)

Abstract

The invention discloses a kind of production method and its process units of starch sugar particle, production method therein is preheated including being first passed through hot blast from the process units intracavity bottom of closing, and starch Icing Sugar and adhesive stream are added in the case where keeping ventilation state hybrid reaction is carried out in process units, generate bulky grain starch sugar.Also disclose the corresponding device using the method production starch sugar particle.Production method of the present invention and process units are simple, easy to use, can efficiently produce bulky grain starch sugar of the particle diameter in the mesh of 40 mesh~10, and good product quality.

Description

A kind of production method and its process units of starch sugar particle
Technical field
The invention belongs to starch sugar production technical field, and in particular to a kind of production method of starch sugar particle and its production Device.
Background technology
At present, starch sugar processing enterprise generally produces crystal diabetin, maltodextrin, Dextrose Monohydrate and DEXTROSE ANHYDROUS, Its particle diameter is typically in 100~40 mesh.In this production technology, the Icing Sugar of different-grain diameter is sieved by screening plant Choosing.But as current foreign customers are in the development of food field of deep, there is an urgent need to a kind of particle diameter between 40~10 mesh Sugared particle, it is commonly called as bulky grain sugar.A kind of process units and production method for being exclusively used in bulky grain starch sugar is currently there are no, therefore It can not meet customer need, there is an urgent need to a kind of mode of production that disclosure satisfy that this market.
The content of the invention
The technical problems to be solved by the invention one：A kind of production method of starch sugar particle is provided, this method is simple, right The equipment that forms a complete production network change is little, can produce the product of different-grain diameter size in the range of the mesh of 40 mesh~10 as needed.
The technical problems to be solved by the invention two：A kind of process units of starch sugar particle, apparatus structure letter are provided It is single, it is easy to use, it can efficiently produce bulky grain starch sugar of the particle diameter in the mesh of 40 mesh~10.
In order to solve the above technical problems, the technical scheme is that：
A kind of production method of starch sugar particle, comprises the following steps：
A. first it is passed through 45~55 DEG C of hot blast from the process units intracavity bottom of closing and preheats 10~15min；
B. in the case where keeping ventilation state, starch Icing Sugar and adhesive stream is added in process units inner chamber, are sufficiently mixed, is made Grain；
C. stop air intake after having reacted, obtain finished product.
Preferably, described adhesive is the aqueous solution of 0.2%~1.0%CMC carboxymethyl celluloses, 5.0%~25% One or more of mixtures in glucose syrup and 5.0%~25% malt syrup.
Preferably, the weight ratio of described starch Icing Sugar and adhesive is 10~14:5~7.
Preferably, described starch sugar is glucose.
A kind of process units of starch sugar particle, including raw material cabin, device for adding binder, comminutor, feeder, finished product Feed bin, air-intake device and exhaust apparatus, comminutor are provided with material inlet, adhesive import, material outlet, air inlet and air-out Mouthful, and it is connected respectively to raw material cabin, device for adding binder, feeder, air-intake device by these import or exports by pipeline And finished product materials are sent to finished product bin by exhaust apparatus, feeder by material conveying pipe；Comminutor includes hollow make Grain owner's body, comminutor main body are provided with micropowder gathering apparatus, fluidized granulating room and bottom cylinder, fluidized granulating room and bottom from top to bottom Tongue profiled orifice plate is provided between cylinder, if being provided with dry tongue type hole on tongue profiled orifice plate；If device for adding binder sprays including dry nebulization Head, atomizer are evenly distributed on chamber in fluidized granulating room.
Preferably, described micropowder gathering apparatus includes exhaust dust device with bag and rapping cylinder disposed thereon, pocket type remove Dirt device is arranged at the top of fluidized granulating room, top perisporium of the rapping cylinder through fluidized granulating room.
Preferably, described air inlet is arranged on the perisporium of bottom cylinder, and air inlet is provided with inlet air door control valve；Go out Air port is arranged on the perisporium on fluidized granulating room top, and air-out airdoor control valve is provided with air outlet；Material outlet is arranged on On the perisporium of fluidized granulating room bottom；Material inlet and adhesive import are arranged on the perisporium of fluidized granulating room.
Preferably, level-sensing device is additionally provided with the inside of described fluidized granulating room perisporium, is provided between raw material cabin and comminutor Material connecting pipe, Material control valve, level-sensing device, Material control valve, inlet air door control are provided with material connecting pipe Valve processed and air-out airdoor control valve are each coupled electrically to automatic control unit.
Preferably, described device for adding binder also includes binder materials storehouse, adhesive delivery pipe and measuring pump, meter Amount pump is each coupled electrically to automatic control unit with Material control valve.
Preferably, described air-intake device includes first medium effeciency filter, heater, high efficiency particulate air filter and wind-warm syndrome sensor, Heater and wind-warm syndrome sensor are electrically connected to automatic control unit.
Preferably, described exhaust apparatus includes air-out airdoor control valve, wind pipe and air-introduced machine.
Preferably, described atomizer is 4~8.
Preferably, some introscopes are additionally provided with described comminutor main body perisporium.
Preferably, described feeder is vacuum feeder.
By adopting the above-described technical solution, the beneficial effects of the invention are as follows：
1. binding agent usage amount of the present invention is few, when being produced in particular for dextran particles, pass through CMC carboxymethyl celluloses Element, glucose syrup and malt syrup are used in combination, and the addition for effectively reducing non-glucose composition can be reduced, so as to enter One step improves the quality of product；
2. dosage by controlling EAT and intake, additive etc., can be by the size controlling of finished product particle Within the specific limits, meet the needs of different clients, realize that product rises in value.
, can be with if being provided with dry tongue type hole on tongue profiled orifice plate 3. be provided with tongue profiled orifice plate between fluidized granulating room and bottom cylinder It is effective to ensure air inlet, fluidized granulating environment is formed, prevents starch sugar to be processed from blocking passage；
4. being provided with several atomizers in fluidized granulating room, each position of fluidized granulating room is distributed in, can be incited somebody to action Upper adhesive is uniformly sprayed on the starch sugar of each position in fluidized granulating room, ensure that moisture stabilization and the side of granulation product Just it is granulated；
5. being provided with rapping cylinder in micropowder gathering apparatus, the micro mist of trapping can be reclaimed automatically, be reduced artificial Labor intensity.
6. inlet air door control valve, air-out airdoor control valve, level-sensing device, Material control valve, heater and wind-warm syndrome sensing Device is each coupled electrically to automatic control unit, by the control of automatic control unit, the ratio between balance material that can be most preferably, Optimal working condition (temperature, wind-force size) etc. is provided, ensures production efficiency and product quality.
In a word, production method of the present invention and process units are simple, easy to use, can efficiently produce particle diameter in the mesh of 40 mesh~10 Bulky grain starch sugar, and good product quality.
Brief description of the drawings
Fig. 1 is positive structure diagram of the embodiment of the present invention；
Fig. 2 is side structure schematic view of the embodiment of the present invention；
Fig. 3 is tongue profiled orifice plate overlooking the structure diagram of the embodiment of the present invention；
Fig. 4 is tongue profiled orifice plate side elevational cross-section structural representation of the embodiment of the present invention；
In figure, 1- comminutors；101- fluidized granulatings room；102- bottoms cylinder；103- tongue profiled orifice plates；104- rapping cylinders；105- Exhaust dust device with bag；106- introscopes；107- air inlets；108- level-sensing devices；109- tongue type holes；2- raw material cabins；21- Material controls Valve；3- device for adding binder；301- binder materials storehouse；302- atomizers；303- measuring pumps；4- feeders；5- into Product feed bin；6- air-intake devices；The first medium effeciency filters of 601-；602- heaters；603- high efficiency particulate air filters；604- wind-warm syndrome sensors； 7- exhaust apparatus；701- air-out airdoor control valves；702- wind pipes；703- air-introduced machines.
Embodiment
With reference to the accompanying drawings and examples, the present invention is expanded on further.
Embodiment one：
As shown in Figures 1 to 4, a kind of starch sugar particle production apparatus, including raw material cabin 2, device for adding binder 3, make Grain machine 1, feeder 4, finished product bin 5, air-intake device 6 and exhaust apparatus 7, comminutor 1 is provided with material inlet, adhesive enters Mouth, material outlet, air inlet 107 and air outlet, and it is connected respectively to raw material cabin 2, viscous by these import or exports by pipeline Finished product materials are sent to finished product bin 5 by mixture adding set 3, feeder 4, air-intake device 6 and exhaust apparatus 7, feeder 4； Comminutor 1 includes hollow comminutor main body, and comminutor main body is provided with micropowder gathering apparatus, fluidized granulating room from top to bottom 101 and bottom cylinder 102, tongue profiled orifice plate 103 is provided between fluidized granulating room 101 and bottom cylinder 102, is provided with tongue profiled orifice plate 103 If dry tongue type hole 109；Device for adding binder 3 includes some atomizers 302, and atomizer 302 is evenly distributed on boiling and made The grain inner chamber of room 101.
Micropowder gathering apparatus includes exhaust dust device with bag 105 and rapping cylinder 104 disposed thereon, exhaust dust device with bag 105 are arranged at the top of fluidized granulating room 101, rapping cylinder 104 through fluidized granulating room 101 top perisporium,
Air inlet 107 is arranged on the perisporium of bottom cylinder 102, and inlet air door control valve is provided with air inlet 107；Air outlet It is arranged on the perisporium on the top of fluidized granulating room 101, air-out airdoor control valve 701 is provided with air outlet；Material outlet is set On the perisporium of the bottom of fluidized granulating room 101；Material inlet and adhesive import are arranged on the perisporium of fluidized granulating room.
Level-sensing device 108 is additionally provided with the inside of the perisporium of fluidized granulating room 101, material company is provided between raw material cabin 2 and comminutor 1 Adapter road, Material control valve 21, level-sensing device 108, Material control valve 21, inlet air door control are provided with material connecting pipe Valve processed and air-out airdoor control valve are each coupled electrically to automatic control unit.
Device for adding binder 3 also includes binder materials storehouse 301, adhesive delivery pipe and measuring pump 303, measuring pump 303 are each coupled electrically to automatic control unit with Material control valve 21.
Air-intake device 6 includes first medium effeciency filter 601, heater 602, high efficiency particulate air filter 603 and wind-warm syndrome sensor 604, Heater 602 and wind-warm syndrome sensor 604 are electrically connected to automatic control unit.
Exhaust apparatus 7 includes air-out airdoor control valve 701, wind pipe 702 and air-introduced machine 703.
Some introscopes 106 are additionally provided with comminutor main body perisporium.
During actual production：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：30%~ 70%, the leaving air temp of heater 602 is adjusted to 45~55 DEG C, preheats 10~15min.
2. powdered glucose is delivered in the fluidized granulating room 101 in comminutor 1 by raw material cabin 2, while open bonding Agent adding set 3 so that adhesive is entered in fluidized granulating room 101 by device for adding binder 3 by measuring pump 303, is glued Mixture is sprayed by atomizer 302 and uniformly mixed with powdered glucose, is granulated in boiling-like.In granulation process caused micro mist by Micropowder gathering apparatus reclaims.Wherein, the amount of the air quantity and wind-warm syndrome of air intake, glucose and adhesive is all entered by automatic control unit Row coordinates control, to ensure the yield of product and quality.
After 3. granulation terminates, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.
Embodiment two：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：30%~ 40%, the leaving air temp of heater 602 is adjusted to 45 DEG C, preheats 10min；
2. the powdered glucose of the mesh of 120 kg 60~80 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 0.6%CMC carboxymethyl celluloses by Adhesive adding device 3 is entered in granulation chamber 22 by measuring pump 15, addition 50L/h；Regulation inlet air door regulating valve makes The height that must seethe with excitement is maintained at 100~120cm, and adhesive adds shower nozzles 12 by 4 adhesives and sprays adhesive simultaneously, uniformly and Portugal Grape Icing Sugar mixes, and is granulated in boiling-like；
3. when material boiling time reaches 50min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 40 mesh~20 is 70Kg/h.
Embodiment three：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：50%~ 60%, the leaving air temp of heater 602 is adjusted to 55 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 80~100 is conveyed with the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 into comminutor 1, while open device for adding binder 3 so that 0.6%CMC carboxymethyl celluloses Entered by adhesive adding device 3 by measuring pump 15 in granulation chamber 22, addition 60L/h；Adjust inlet air door regulating valve So that boiling height is maintained at 100~120cm, adhesive adds shower nozzles 12 by 6 adhesives and sprays adhesive simultaneously, uniformly with Powdered glucose mixes, and is granulated in boiling-like；
3. when material boiling time reaches 70min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 60 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 40 mesh~20 is 105Kg/h.
Example IV：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：40%~ 50%, the leaving air temp of heater 602 is adjusted to 50 DEG C, preheats 10min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 0.2%CMC carboxymethyl celluloses by Adhesive adding device 3 is entered in granulation chamber 22 by measuring pump 15, addition 60L/h；Regulation inlet air door regulating valve makes The height that must seethe with excitement is maintained at 100~120cm, and adhesive adds shower nozzles 12 by 8 adhesives and sprays adhesive simultaneously, uniformly and Portugal Grape Icing Sugar mixes, and is granulated in boiling-like；
3. when material boiling time reaches 60min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 20 mesh~10 is 48Kg/h.
Embodiment five：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：60%~ 70%, the leaving air temp of heater 602 is adjusted to 45 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 0.8%CMC carboxymethyl celluloses by Adhesive adding device 3 is entered in granulation chamber 22 by measuring pump 15, addition 60L/h；Regulation inlet air door regulating valve makes The height that must seethe with excitement is maintained at 100~120cm, and adhesive adds shower nozzles 12 by 5 adhesives and sprays adhesive simultaneously, uniformly and Portugal Grape Icing Sugar mixes, and is granulated in boiling-like；
3. when material boiling time reaches 70min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 20 mesh~10 is 56Kg/h.
Embodiment six：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：30%~ 40%, the leaving air temp of heater 602 is adjusted to 50 DEG C, preheats 10min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 5.0% malt syrup is by adhesive Adding device 3 is entered in granulation chamber 22 by measuring pump 15, addition 60L/h；Regulation inlet air door regulating valve to seethe with excitement Highly it is maintained at 100~120cm, adhesive adds shower nozzles 12 by 7 adhesives and sprays adhesive simultaneously, uniformly and powdered glucose Mixing, is granulated in boiling-like；
3. when material boiling time reaches 70min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 60 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 20 mesh~10 is 26Kg/h.
Embodiment seven：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：40%~ 50%, the leaving air temp of heater 602 is adjusted to 55 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 15% malt syrup is added by adhesive Unit 3 is added to enter by measuring pump 15 in granulation chamber 22, addition 60L/h；Regulation inlet air door regulating valve make it that boiling is high Degree is maintained at 100~120cm, and adhesive adds shower nozzle 12 by 7 adhesives and sprays adhesive simultaneously, uniformly mixed with powdered glucose Close, be granulated in boiling-like；
3. when material boiling time reaches 60min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 60 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 20 mesh~10 is 38Kg/h.
Embodiment eight：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：60%~ 70%, the leaving air temp of heater 602 is adjusted to 50 DEG C, preheats 10min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 25% malt syrup is added by adhesive Unit 3 is added to enter by measuring pump 15 in granulation chamber 22, addition 50L/h；Regulation inlet air door regulating valve make it that boiling is high Degree is maintained at 100~120cm, and adhesive adds shower nozzle 12 by 7 adhesives and sprays adhesive simultaneously, uniformly mixed with powdered glucose Close, be granulated in boiling-like；
3. when material boiling time reaches 70min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 60 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 40 mesh~20 is 32Kg/h.
Embodiment nine：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：40%~ 50%, the leaving air temp of heater 602 is adjusted to 55 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 5.0% grape slurry is added by adhesive Unit 3 is added to enter by measuring pump 15 in granulation chamber 22, addition 60L/h；Regulation inlet air door regulating valve make it that boiling is high Degree is maintained at 100~120cm, and adhesive adds shower nozzle 12 by 7 adhesives and sprays adhesive simultaneously, uniformly mixed with powdered glucose Close, be granulated in boiling-like；
3. when material boiling time reaches 60min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 60 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 20 mesh~10 is 33Kg/h.
Embodiment ten：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：30%~ 40%, the leaving air temp of heater 602 is adjusted to 45 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 15% grape slurry is added by adhesive Unit 3 is entered in granulation chamber 22 by measuring pump 15, addition 50L/h；Regulation inlet air door regulating valve causes boiling height 100~120cm is maintained at, adhesive adds shower nozzle 12 by 7 adhesives and sprays adhesive simultaneously, uniformly mixed with powdered glucose Close, be granulated in boiling-like；
3. when material boiling time reaches 70min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 40 mesh~20 is 39Kg/h.
Embodiment 11：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：50%~ 60%, the leaving air temp of heater 602 is adjusted to 50 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that 25% grape slurry is added by adhesive Unit 3 is entered in granulation chamber 22 by measuring pump 15, addition 60L/h；Regulation inlet air door regulating valve causes boiling height 100~120cm is maintained at, adhesive adds shower nozzle 12 by 7 adhesives and sprays adhesive simultaneously, uniformly mixed with powdered glucose Close, be granulated in boiling-like；
3. when material boiling time reaches 70min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 20 mesh~10 is 37Kg/h.
Embodiment 12：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：50%~ 60%, the leaving air temp of heater 602 is adjusted to 50 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that binding agent (0.6%CMC carboxymethyls Cellulose and 15% grape slurry are with volume ratio 1:1 mixes) granulation chamber 22 is entered by measuring pump 15 by adhesive adding device 3 It is interior, addition 70L/h；Regulation inlet air door regulating valve causes boiling height to be maintained at 100~120cm, and adhesive is viscous by 7 Mixture addition shower nozzle 12 sprays adhesive simultaneously, uniformly mixes with powdered glucose, is granulated in boiling-like；
3. when material boiling time reaches 60min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 40 mesh~20 is 108Kg/h.
Embodiment 13：
1. opening air-intake device 6, hot blast is passed through to comminutor 1, wherein inlet air door control valve opening is：50%~ 60%, the leaving air temp of heater 602 is adjusted to 50 DEG C, preheats 15min；
2. the powdered glucose of the mesh of 120 kg 40~60 is delivered to the stream dosage of 120 kg per hour by raw material cabin 2 In fluidized granulating room 101 in comminutor 1, while open device for adding binder 3 so that binding agent (0.6%CMC carboxymethyls Cellulose, 15% grape slurry and 15% malt syrup are with volume ratio 2:1:1 mixes) measuring pump is passed through by adhesive adding device 3 15 enter in granulation chamber 22, addition 60L/h；Regulation inlet air door regulating valve cause boiling height be maintained at 100~ 120cm, adhesive add shower nozzle 12 by 7 adhesives and spray adhesive simultaneously, uniformly mix with powdered glucose, made in boiling-like Grain；
3. when material boiling time reaches 60min, boiling height to 100~120cm, reaction temperature liter in fluidized granulating room For 55 DEG C, start negative pressure discharging, the dextran particles for preparing completion are delivered in finished product bin 5 through feeder 4.Finished product Icing Sugar Grain mesh number is that the yield of the mesh of 40 mesh~20 is 106Kg/h.
It should be understood that these embodiments are only illustrative of the invention and is not intended to limit the scope of the invention.In addition, it is to be understood that After the content of the invention lectured has been read, those skilled in the art can make various changes or modifications to the present invention, these The equivalent form of value equally falls within the application appended claims limited range.

Claims (9)

  1. A kind of 1. production method of starch sugar particle, it is characterised in that：Comprise the following steps：
    A. first it is passed through 45~55 DEG C of hot blast from the process units intracavity bottom of closing and preheats 10~15min；
    B. in the case where keeping ventilation state, starch Icing Sugar and adhesive stream is added in process units inner chamber, are sufficiently mixed, be granulated；
    C. stop air intake after having reacted, obtain finished product.
  2. 2. the production method of starch sugar particle as claimed in claim 1, it is characterised in that：Described adhesive be 0.2%~ One kind in the aqueous solution of 1.0%CMC carboxymethyl celluloses, 5.0%~25% glucose syrup and 5.0%~25% malt syrup Or several mixture.
  3. 3. the production method of starch sugar particle as claimed in claim 1, it is characterised in that：The starch Icing Sugar and adhesive Weight ratio is 10~14:5~7.
  4. 4. the production method of starch sugar particle as claimed in claim 1, it is characterised in that：The starch sugar is glucose.
  5. A kind of 5. process units of starch sugar particle, it is characterised in that：Including raw material cabin, device for adding binder, comminutor, on Material machine, finished product bin, air-intake device and exhaust apparatus；The comminutor includes hollow comminutor main body, the granulation owner Body is provided with micropowder gathering apparatus, fluidized granulating room and bottom cylinder from top to bottom, is set between the fluidized granulating room and the bottom cylinder Tongue profiled orifice plate is equipped with, if being provided with dry tongue type hole on the tongue profiled orifice plate；If described adhesive adding set sprays including dry nebulization Head, the atomizer are evenly distributed on chamber in fluidized granulating room.
  6. 6. starch sugar particle production apparatus as claimed in claim 5, it is characterised in that：The micropowder gathering apparatus includes pocket type Dust arrester and rapping cylinder disposed thereon.
  7. 7. starch sugar particle production apparatus as claimed in claim 5, it is characterised in that：Described adhesive adding set also includes Binder materials storehouse, adhesive delivery pipe and measuring pump.
  8. 8. starch sugar particle production apparatus as claimed in claim 5, it is characterised in that：The atomizer is 4~8.
  9. 9. starch sugar particle production apparatus as claimed in claim 5, it is characterised in that：On the inside of the perisporium of the fluidized granulating room also It is provided with level-sensing device.
CN201711355277.6A 2017-12-16 2017-12-16 A kind of production method and its process units of starch sugar particle Pending CN107841577A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110679715A (en) * 2019-09-12 2020-01-14 天津尖峰弗兰德医药科技发展有限公司 Miniature candy and preparation method thereof
CN114522617A (en) * 2022-01-07 2022-05-24 上海康识食品科技有限公司 Flavor particle and granulation method thereof

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JP2002045675A (en) * 2000-08-08 2002-02-12 Ajinomoto Co Inc Novel spray drying pelletizing device and manufacturing method of granular food product
CN1974779A (en) * 2006-11-28 2007-06-06 江门量子高科生物工程有限公司 Process of preparing granular oligofructose
CN106179114A (en) * 2016-08-04 2016-12-07 浙江华康药业股份有限公司 A kind of continuous boiling granulator of vertical type full automatic and sugar alcohol prilling process
CN205980566U (en) * 2016-03-23 2017-02-22 浦城正大生化有限公司 Chloroteracycline drying system

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Publication number Priority date Publication date Assignee Title
JP2002045675A (en) * 2000-08-08 2002-02-12 Ajinomoto Co Inc Novel spray drying pelletizing device and manufacturing method of granular food product
CN1974779A (en) * 2006-11-28 2007-06-06 江门量子高科生物工程有限公司 Process of preparing granular oligofructose
CN205980566U (en) * 2016-03-23 2017-02-22 浦城正大生化有限公司 Chloroteracycline drying system
CN106179114A (en) * 2016-08-04 2016-12-07 浙江华康药业股份有限公司 A kind of continuous boiling granulator of vertical type full automatic and sugar alcohol prilling process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110679715A (en) * 2019-09-12 2020-01-14 天津尖峰弗兰德医药科技发展有限公司 Miniature candy and preparation method thereof
CN114522617A (en) * 2022-01-07 2022-05-24 上海康识食品科技有限公司 Flavor particle and granulation method thereof

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Application publication date: 20180327