CN110339930A - A kind of homogenate separator and plant beverage are homogenized separation method - Google Patents
A kind of homogenate separator and plant beverage are homogenized separation method Download PDFInfo
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- 238000000926 separation method Methods 0.000 title claims abstract description 24
- 239000000463 material Substances 0.000 claims abstract description 176
- 238000000227 grinding Methods 0.000 claims abstract description 67
- 239000002994 raw material Substances 0.000 claims abstract description 49
- 239000000084 colloidal system Substances 0.000 claims abstract description 31
- 230000001599 osteoclastic effect Effects 0.000 claims abstract description 26
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- 238000000034 method Methods 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 235000011837 pasties Nutrition 0.000 claims description 19
- 238000003756 stirring Methods 0.000 claims description 13
- 238000010008 shearing Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 abstract description 15
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- 238000004519 manufacturing process Methods 0.000 description 20
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- ADRVNXBAWSRFAJ-UHFFFAOYSA-N catechin Natural products OC1Cc2cc(O)cc(O)c2OC1c3ccc(O)c(O)c3 ADRVNXBAWSRFAJ-UHFFFAOYSA-N 0.000 description 7
- 235000005487 catechin Nutrition 0.000 description 7
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- 241000233866 Fungi Species 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B13/00—Control arrangements specially designed for centrifuges; Programme control of centrifuges
Abstract
The invention belongs to technical field of beverage preparation more particularly to a kind of homogenate separator and plant beverage to be homogenized separation method.Homogenate separator provided by the invention includes the raw material elevator 2 being sequentially connected in series, osteoclastic pulverizer 3, colloid mill 4, homogeneous tank 5, multistage grinding pump 6, the temporary agitator tank 7 of material and horizontal centrifugal seperator 9.Homogenate separator of the invention can make material reach higher fineness (more than 50 mesh), so as to sufficiently extract water-soluble substances in shorter time or lower temperature, the present invention does not need large granular materials or high temperature extracts, the heat-sensitive active material that can utmostly retain in raw material is not destroyed, while preferable natural flavor, fragrance and the soup look for keeping plant beverage.
Description
Technical field
The present invention relates to technical field of beverage preparation more particularly to the homogenate separation of a kind of homogenate separator and plant beverage
Method.
Background technique
Currently, the extracting method of beverage includes being extracted using hot water in extractor or being extracted using adverse current.However, extracting
In tank extracting method, filter screen is installed in the bottom of extractor, due to the limited area of filter screen, if extracted material is too
Carefully, it is easy blocking filter screen and is difficult to out liquid, need that the bigger material of granularity is selected to extract；And granularity is big, needs
Longer extraction time or higher Extracting temperature just can guarantee extraction completely, but be easy to cause some heat in material in this way
Quick property substance is destroyed, and soup look deepens, and natural fragrance weakens.In addition, countercurrent extraction method, which is also required to material, has certain
Granularity is just able to achieve adverse current between material and water, there is a problem of so as to cause it identical as said extracted tank extracting method.
Therefore, the extracting method of existing beverage finally can all lead to heat-sensitive active material loss, natural fragrance and flavor
Decline, soup look deepen.
Summary of the invention
The purpose of the present invention is to provide a kind of homogenate separators and plant beverage to be homogenized separation method, homogenate separation
Device can sufficiently extract the water-soluble substances in material in shorter time or lower temperature, utmostly remain work
Property substance be not destroyed, while preferable natural flavor, fragrance and the soup look for keeping plant beverage.
In order to achieve the above-mentioned object of the invention, the present invention the following technical schemes are provided:
The present invention provides a kind of homogenate separators, including raw material elevator 2, the osteoclastic pulverizer 3, glue being sequentially connected in series
Body mill 4, homogeneous tank 5, multistage grinding pump 6, material keep in agitator tank 7 and horizontal centrifugal seperator 9.
Preferably, further include screw pump 8, the screw pump 8 be set to the material keep in agitator tank 7 and it is described it is horizontal from
Between centrifugal separator 9.
The present invention provides the homogenate separation that plant beverage is carried out using homogenate separator described in above-mentioned technical proposal
Method, comprising the following steps:
Plant material is delivered to osteoclastic pulverizer 3 by raw material elevator 2, is crushed, obtains comminuting matter；
The comminuting matter is sent into colloid mill 4, is ground, grinding material is obtained；
The grinding material is transferred to homogeneous tank 5, homogeneous is carried out, obtains homogenous mass；
The homogenous mass is sent to multistage grinding pump 6, multistage grinding is carried out, obtains refinement material；
The refinement material is sent to material and keeps in agitator tank 7, is stirred, obtains pasty material；
The pasty material is pumped into horizontal centrifugal seperator 9, is centrifuged, obtains feed liquid.
Preferably, when carrying out the crushing, the plant material is mixed with water, material-water ratio is 1:0~15.
Preferably, the power of the grinding is 18.5kW, and the time of grinding is 2~5min, and the yield of the colloid mill is 2
~7T/h.
Preferably, the shearing rotating speed of the homogeneous is 4500r/min.
Preferably, when carrying out the multistage grinding, the power of the multistage grinding pump is 11kW, revolving speed 2950r/min,
Treating capacity is 3~7T/h.
Preferably, the time of the multistage grinding is 2~3min.
Preferably, the revolving speed of the stirring is 60~100r/min.
Preferably, the separation revolving speed of the centrifuge separation is 2500~3500r/min, and deslagging revolving speed is 1000~2400r/
min。
The present invention provides a kind of homogenate separators and plant beverage to be homogenized separation method, and homogenate of the invention separates dress
Setting can make material reach higher fineness (more than 50 mesh), so as to sufficiently extract in shorter time or lower temperature
Water-soluble substances, the present invention does not need large granular materials or high temperature extracts, and the thermal sensitivity that can utmostly retain in raw material is living
Property substance be not destroyed, while preferable natural flavor, fragrance and the soup look for keeping plant beverage.
Homogenate separator of the invention uses horizontal centrifugal seperator, can realize that feed liquid separates well, reach preferable
Extraction effect, the recovery rate of water-soluble substances is up to 95% or more.
Detailed description of the invention
Fig. 1 is present invention homogenate separator schematic diagram, wherein 1- feeding port, 2- raw material elevator, the osteoclastic crushing of 3-
Machine, 4- colloid mill, 5- homogeneous tank, 6- multistage grinding pump, 7- material keep in agitator tank, 8- screw pump, 9- horizontal centrifuge, 10-
Material residue outlet, 11- material liquid outlet.
Specific embodiment
The present invention provides a kind of homogenate separators, including raw material elevator 2, the osteoclastic pulverizer 3, glue being sequentially connected in series
Body mill 4, homogeneous tank 5, multistage grinding pump 6, material keep in agitator tank 7 and horizontal centrifugal seperator 9.
Homogenate separator provided by the invention includes raw material elevator 2, and the raw material elevator 2 is provided with feeding port 1,
The adjustable section of the feeding port 1.In the present invention, the raw material elevator 2 is preferably bucket elevator.In the present invention
In, the raw material elevator is used for feedstock transportation to the feed inlet of osteoclastic pulverizer.
Homogenate separator provided by the invention includes osteoclastic pulverizer 3, and the osteoclastic pulverizer 3 is preferably provided with charging
Mouthful, the feed inlet is used for raw material of the access from raw material elevator.In the present invention, the model of the osteoclastic pulverizer 3 is excellent
It is selected as PGJ-100.In the present invention, the sieve that aperture is 3~8mm is provided in the osteoclastic pulverizer, the sieve is used for
Material is filtered to the feed inlet of colloid mill after will be broken.In the present invention, the osteoclastic pulverizer primarily serves the work of comminuting matter
With the cutter that raw material can be operated when entering in osteoclastic pulverizer is broken into thin.
Homogenate separator provided by the invention includes colloid mill 4, and the colloid mill 4 is preferably provided with feed inlet, described
Feed inlet is preferably shaped to taper, and the feed inlet is used for the undersize material of access sieve in osteoclastic pulverizer.At this
In invention, the model of the colloid mill 4 is preferably JMF-180.In the present invention, the outlet of the colloid mill 4 is preferably provided with
Triple valve, the triple valve are used to adjust the direction of material, material can be turned to feed inlet or homogeneous tank.The present invention utilizes colloid
Mill further grinds material.
Homogenate separator provided by the invention includes homogeneous tank 5, and the homogeneous tank 5 preferably includes HSM-120 type height and cuts
Homogenizer is cut, the present invention further refines the granularity of material using homogeneous tank.
Homogenate separator provided by the invention includes multistage grinding pump 6, and the model of the multistage grinding pump 6 is preferably
AYJ-40-3.In the present invention, the multistage grinding pump is for conveying feed liquid and grinding to material.
Homogenate separator provided by the invention includes that material keeps in agitator tank 7, and the material is kept in agitator tank 7 and preferably set
It is equipped with agitating paddle and collet, using the stirring paddle stirring, material residue and liquid in material is enabled to keep pulpous state suspended state,
The water-soluble substances in material are precipitated sufficiently；The collet is for being heated or being cooled down to material, to ensure plant original
The freshness and material color of material are constant.
Homogenate separator provided by the invention includes horizontal centrifuge 9, and the horizontal centrifugal seperator 9 is preferably provided with
Main rotary drum is preferably provided with spiral deslagging rotary drum in the main rotary drum.In the present invention, the model of the horizontal centrifuge 9 is excellent
It is selected as LW450ND.In the present invention, the horizontal centrifugal seperator 9 is preferably provided with material residue outlet 10 and material liquid outlet 11.?
In the present invention, the main rotary drum is separated for feed liquid, and the spiral deslagging rotary drum is for being discharged the separating obtained material residue of feed liquid.
As an embodiment of the present invention, the homogenate separator further includes screw pump 8, and the screw pump 8 is distinguished
Agitator tank 7 is kept in material and horizontal centrifugal seperator 9 is connected；The screw rod 8 pumps the material for material to be kept in agitator tank 7
It is pumped into horizontal centrifugal seperator 9.
The present invention provides the homogenate separation that plant beverage is carried out using homogenate separator described in above-mentioned technical proposal
Method, comprising the following steps:
Plant material is delivered to osteoclastic pulverizer 3 by raw material elevator 2, is crushed, obtains comminuting matter；
The comminuting matter is sent into colloid mill 4, is ground, grinding material is obtained；
The grinding material is transferred to homogeneous tank 5, homogeneous is carried out, obtains homogenous mass；
The homogenous mass is sent to multistage grinding pump 6, multistage grinding is carried out, obtains refinement material；
The refinement material is sent to material and keeps in agitator tank 7, is stirred, obtains pasty material；
The pasty material is pumped into horizontal centrifugal seperator 9, is centrifuged, obtains feed liquid.
In the present invention, if without specified otherwise, required raw material is commercial goods well known to those skilled in the art.
Plant material is delivered to osteoclastic pulverizer 3 by raw material elevator 2 by the present invention, is crushed, obtains crushed material
Material.In the present invention, the plant material preferably includes water fruits and vegetables, tea, mushroom, dendrobium nobile, rhizoma polygonati or Chinese yam.The present invention is excellent
Choosing adjusts the feeding port size of raw material elevator according to (such as form, size) the characteristics of plant material, to control inlet amount.
In the present invention, the rate of feeding of the plant material is preferably 15~20kg/min.
In the present invention, when carrying out the crushing, the present invention preferably mixes the plant material with water, and material-water ratio is preferred
For 1:0~15, more preferably 1:10~15,1:0~1 or 1:2~5.The present invention preferably determines material-water ratio according to combustion.Tool
Body, such as dry state raw material: teas (green tea, black tea, dark green tea, white tea, yellow tea, green tea), mushroom (mushroom, needle mushroom, ox
Liver bacterium, tremella, black fungus, Agricus blazei etc.), integration of drinking and medicinal herbs class (rhizoma polygonati, Siraitia grosvenorii, Chinese yam, dendrobium nobile, ginkgo nut etc.) raw material, material
Water is than being preferably 1:10~15；For fresh water fruit material (strawberry, blueberry, fructus lycii, cucumber, dragon fruit, jujube, peach etc.),
The water content of its raw material itself is big, and material-water ratio is preferably 1:0~1, more preferably 1:0.5~1；It is swollen for being easy to produce after homogenate
The raw material (such as: rose, honeysuckle, Jasmine) of swollen phenomenon, material-water ratio is preferably 1:2~5.The present invention by plant material with
Water mixing forms the pasty material of flowing, after osteoclastic pulverizer and colloid mill homogenate convenient for multistage grinding pump and subsequent work
The circulation and normal operation of skill, it is therefore an objective to allow the water-soluble substances in raw material to be sufficiently dissolved out, improve extraction efficiency.
After obtaining comminuting matter, the present invention send the comminuting matter into colloid mill 4, is ground, and obtains abrasive material
Material.In the present invention, the comminuting matter preferably falls into the taper feed inlet of colloid mill by the sieve of osteoclastic pulverizer 3.?
In the present invention, the power of the grinding is preferably 18.5kW, and the time of grinding is preferably 2~5min, more preferably 3~4min,
The yield of the colloid mill 4 is preferably 2~7T/h, more preferably 3~5T/h.During the grinding process, colloid mill is specifically opened
The triple valve of exit setting, makes material flow back into colloid mill feed inlet, grinds Matter Transfer, then by ground material
(particle diameter fineness reaches 800 μm or less) turns to homogeneous tank by triple valve.After completing the grinding, the fineness of gained grinding material
Preferably 2~300 μm.
After obtaining grinding material, the grinding material is transferred to homogeneous tank 5 by the present invention, is carried out homogeneous, is obtained homogenous mass.
In the present invention, the process of the homogeneous is specially the high-shear homogenizing machine opened in homogeneous tank 5, and high-shear homogenizing machine is persistently transported
Row is until this batch materials is all pumped into multistage grinding pump 6.In the present invention, this batch materials refers to a collection of raw material from into tank
Subject to feed liquid production terminates, process continuous service does not stop.The high-speed revolution shearing that the present invention passes through high-shear homogenizing machine
Further increase fineness of materials.In the present invention, the shearing rotating speed of the homogeneous is preferably 4500r/min, the homogeneous
Time is until this batch materials has all been run.In the present invention, 5~6h of the high-shear homogenizing machine continuous operation need to shut down into
Row cleaning is further continued for running.
After obtaining homogenous mass, the present invention send the homogenous mass to multistage grinding pump 6, carries out multistage grinding, obtains
Refine material.In the present invention, the multistage grinding is specifically and opens multistage when homogenous mass reaches half tank of homogeneous tank and grind
Mill pump 6, is further ground.In the present invention, when carrying out the multistage grinding, the power of the multistage grinding pump 6 is preferred
For 11kW, revolving speed is preferably 2950r/min, and treating capacity is preferably 3~7T/h；The circulation time of the multistage grinding pump 6 is preferred
For 2~3min.In the present invention, the fineness of the refinement material is preferably 10~200 μm.
After obtaining refinement material, the refinement material is sent to material and keeps in agitator tank 7 by the present invention, is stirred, is obtained
Pasty material.In the present invention, when the liquid level that the refinement material delivers into the temporary agitator tank tank 7 of material reaches blade
When, it opens agitating paddle and carries out continuing stirring operation, until all production terminates to stop this batch materials.In the present invention, the stirring
Revolving speed be 60~100r/min, the process continuous service of the stirring is until the production process of this batch materials runs and completes.This
Invention makes material residue and liquid in material keep pulpous state suspended state (preventing material residue from precipitating) by persistently stirring, makes the water in material
Soluble substance is sufficiently precipitated.The present invention preferably heats or cools down to material according to the actual conditions of material；Specifically, right
In dry tea, dry mushroom raw material, the collet being arranged in agitator tank is kept in material and is passed through hot water or steam heating, is made on temperature of charge
Rise to 30 DEG C~80 DEG C so that the water soluble ingredient in material be more quickly dissolved into it is in the water being added in crushing process or fresh
The fruit juice that fruit is squeezed out；And it is complete come the dissolution for determining water soluble ingredient in material using the content of concentration tester detection solid content
Whole degree.For fresh water fruit material, it can not heat or chilled water can be passed through by collet, material is made to be cooled to 20
DEG C hereinafter, to ensure that fruit freshness and material color are constant.
After obtaining pasty material, the pasty material is pumped into horizontal centrifugal seperator 9 by the present invention, is centrifuged,
Obtain plant beverage.The present invention preferably passes through screw pump 8 and the pasty material is pumped into horizontal centrifugal seperator 9.In this hair
In bright, the revolving speed (main revolving speed) of the main rotary drum is preferably 2500~3500r/min, more preferably 2800~3200r/min；Institute
The revolving speed (deslagging revolving speed) for stating spiral deslagging rotary drum is preferably 1000~2400r/min, more preferably 1500~2000r/min；
The process continuous service of the centrifuge separation is completed up to the production process of this batch materials is run, in an embodiment of the present invention,
The time of the centrifuge separation is preferably 5~6h.In centrifugal separation processes, the pasty material is expected under the influence of centrifugal force
Liquid separation, material residue drain into material residue by inside spin deslagging rotary drum and export, and feed liquid is flowed out from the material liquid outlet of horizontal centrifugal seperator, is obtained
To plant beverage.
Fig. 1 is present invention homogenate separator schematic diagram, wherein 1- feeding port, 2- raw material elevator, the osteoclastic crushing of 3-
Machine, 4- colloid mill, 5- homogeneous tank, 6- multistage grinding pump, 7- material keep in agitator tank, 8- screw pump, 9- horizontal centrifuge, 10-
Material residue outlet, 11- material liquid outlet；As seen from the figure, raw material elevator, osteoclastic pulverizer, colloid mill, homogeneous tank, multistage grinding pump,
Material is kept in agitator tank, screw pump and horizontal centrifugal seperator and is sequentially connected in series, and plant material is delivered to by raw material elevator
Osteoclastic pulverizer is crushed, and gained comminuting matter enters colloid mill and ground, and gained grinding material enters the progress of homogeneous tank
Homogeneous, gained homogenous mass enter multistage grinding pump and carry out multistage grinding, and gained refinement material enters material and keeps in agitator tank,
Pasty material is formed under stirring operation, the pasty material is pumped to horizontal centrifugal seperator by screw rod, is centrifuged,
Material residue separation is carried out, feed liquid is obtained.
Homogenate separator provided by the invention and plant beverage homogenate separation method are carried out below with reference to embodiment detailed
Thin explanation, but they cannot be interpreted as limiting the scope of the present invention.
Embodiment 1
The feeding port that raw material elevator is poured into after dry green tea 1000kg is cleaned, by the rate of feeding of 15kg/min by raw material
Elevator, which is promoted, invests osteoclastic pulverizer, while the material-water ratio of 1:15 in mass ratio adds water, is crushed, gained comminuting matter warp
It crosses the sieve that aperture is 5mm and grinds 3min toward downstream to colloid mill, carrying out flowing back in colloid mill, gained grinding material is transferred to
Homogeneous tank, high-shear homogenizing machine is with the speed continuous shear stress of 4500r/min, when gained homogenous mass reaches half tank of homogeneous tank
When, multistage grinding pump is opened, the feed liquid that multistage grinding pump comes out first squeezes into homogeneous tank, after the Matter Transfer 2min of homogeneous tank,
Material is pumped into when fineness reaches 300 μm or less again and keeps in agitator tank, keeps in agitator tank when the refinement material delivers into material
When liquid level in tank reaches blade, agitating paddle is opened, Stirring is carried out with the speed of 60r/min, until this batch of production
Terminate, obtains pasty material；Screw pump is opened, according to the speed of 3000kg/h, the pasty material is pumped into horizontal centrifugal point
It disembarks, it is 3500r/min that main rotary drum revolving speed, which is arranged, while it is 2400r/min that spiral deslagging rotary drum revolving speed, which is arranged, in centrifugal force
Effect is lower to carry out feed liquid separation, and material residue is pushed out to material residue by spiral deslagging rotary drum and exports, and feed liquid flows from centrifuge material liquid outlet
Out, all raw materials of 290min and production procedure are fully completed, and the recovery rate of water-soluble substances is 95%, and millet paste solid content is
2.3% clarification feed liquid, i.e. green tea feed liquid (14500kg).
Comparative example 1
According to traditional extraction technique, green tea feed liquid is prepared using extractor, using material-water ratio example same as Example 1,
It in extractor, is extracted under the conditions of 80 DEG C, obtains green tea feed liquid.
Using high-efficiency liquid chromatography method for detecting, the green tea feed liquid prepared to embodiment 1 and comparative example 1 carries out ingredient point
Analysis, concrete outcome are shown in Table 1.
The ingredient of green tea feed liquid prepared by 1 embodiment 1 of table and comparative example 1
Table 1 shows the catechin component variation for the green tea beverage that embodiment 1 and comparative example 1 make, as shown in Table 1, real
Apply example 1 production green tea beverage in major catechin EGC EGCG EC ECG content it is greener than traditional handicraft (comparative example 1)
Tea material liquid is high, and in the green tea feed liquid of traditional handicraft (comparative example 1) production, the content of simple catechin C and secondary catechin GCG
Higher, this illustrates that traditional handicraft causes major catechin oxidation to reduce due to by high temperature, and secondary catechin increases, and secondary
The antioxidant effect of catechin is not so good as major catechin.Therefore, technique of the invention can guarantee that effective active composition is not broken
It is bad.
Embodiment 2
Strawberry juice is produced by raw material of strawberry fresh fruit:
The feeding port of raw material elevator is poured into after fresh strawberry 1000kg is cleaned, 15~20kg/min's by weight feeds intake
Speed promotes the osteoclastic pulverizer of trend of purchasing by raw material elevator and is crushed, and gained comminuting matter is past by the sieve that aperture is 5mm
Downstream to colloid mill, reflux grinding 3min is carried out in colloid mill, gained grinding material is transferred to homogeneous tank, the high shear in tank
Homogenizer persistently shears homogeneous with the speed of 4500r/min, until all production terminates this batch materials.When the homogeneous in tank
When material reaches half tank of homogeneous tank, multistage grinding pump is opened, the material that grinding pump comes out briefly returns to homogeneous tank circulation 2min, so
It is pumped into material again afterwards and keeps in agitator tank, when the liquid level that the refinement material delivers into the temporary agitator tank tank of material reaches blade
When, agitating paddle is opened, Stirring is carried out with the speed of 80r/min and obtains slurry until this batch of production terminates
Material；Screw pump is opened the pasty material is pumped into horizontal centrifugal seperator, main rotary drum is arranged according to the speed of 1500kg/h
Revolving speed is 3500r/min, while it is 1900r/min that spiral deslagging rotary drum revolving speed, which is arranged, carries out feed liquid under the influence of centrifugal force
Separation, material residue are pushed out to material residue by spiral deslagging rotary drum and export, and feed liquid flows out from centrifuge material liquid outlet, all originals of 60min
Material and production procedure are fully completed；Obtain strawberry juice (960kg)；The recovery rate of water-soluble substances is 96%, obtains solid content and contains
The clarification feed liquid of amount 4.8%.
Embodiment 3
The production of dendrobium candidum beverage:
The dendrobium nobile section of 1~2cm is cut into after fresh dendrobium candidum branch 1000kg is cleaned using medicine cutter；By the dendrobium nobile
Section pours into the feeding port of raw material elevator, is promoted by the rate of feeding of 15kg/min by raw material elevator and invests osteoclastic pulverizer,
Water is added with the ratio of material-water ratio 1:5 in mass ratio simultaneously, is crushed, gained comminuting matter is past by the sieve that aperture is 5mm
Downstream to colloid mill, reflux grinding 3min is carried out in colloid mill, gained grinding material is transferred to homogeneous tank, the high shear in tank
Homogenizer persistently shears homogeneous with the speed of 4500r/min, until all production terminates this batch materials；When the homogeneous in tank
When material reaches half tank of homogeneous tank, multistage grinding pump is opened, the material that grinding pump comes out briefly returns to homogeneous tank circulation 2min, so
It is pumped into material again afterwards and keeps in agitator tank, when the liquid level that the refinement material delivers into the temporary agitator tank tank of material reaches blade
When, agitating paddle is opened, Stirring is carried out with the speed of 60r/min and obtains slurry until this batch of production terminates
Material；Screw pump is opened, the pasty material is pumped into horizontal centrifugal seperator, it is 3500r/min that main rotary drum revolving speed, which is arranged, simultaneously
Setting spiral deslagging rotary drum revolving speed is 2400r/min, carries out feed liquid separation, material residue and dendrobium fiber quilt under the influence of centrifugal force
Spiral deslagging rotary drum is pushed out to material residue outlet, and feed liquid flows out from centrifuge material liquid outlet, all raw materials of 70min and production procedure
It is fully completed, the recovery rate of water-soluble substances is 96%, obtains the clarification feed liquid of solid content 1.5%, obtains dendrobium nobile feed liquid
(5762kg)。
The dendrobium nobile feed liquid is subjected to aseptic canning using conventional method, can be used as the primary raw material of dendrobium stem beverage production,
Dendrobium nobile solid beverage is used as after freeze drier or spray dryer can also be used dry.
Embodiment 4
The production of mushroom soup:
It is thin that the dry bolete 500kg of raw material, dried thin mushroom raw material 300kg and dry Agricus blazei 200kg are crushed to 1~3mm respectively
Then gained raw material is all uniformly mixed by degree, by the rate of feeding of 20kg/min by the raw material mixed from raw material elevator
Feeding port, which is promoted, invests osteoclastic pulverizer, while the material-water ratio of 1:15 in mass ratio, and hot water and material that temperature is 80 DEG C is added
Mixing, is crushed, and gained comminuting matter is past downstream to colloid mill by the sieve that aperture is 5mm, is returned in colloid mill
Stream grinding 2min, is transferred to homogeneous tank for gained grinding material, gained grinding material is transferred to homogeneous tank, the high shear homogeneous in tank
Machine even persistently shears homogeneous with the speed of 4500r/min, until all production terminates this batch materials；When the homogeneous object in tank
When material reaches half tank of homogeneous tank, multistage grinding pump is opened, the material that grinding pump comes out briefly returns to homogeneous tank circulation 2min, then
It is pumped into material again and keeps in agitator tank, when the liquid level that the refinement material delivers into the temporary agitator tank tank of material reaches blade
When, agitating paddle is opened, Stirring is carried out with the speed of 100r/min and obtains pulpous state until this batch of production terminates
Material；Screw pump is opened, the pasty material is pumped into horizontal centrifugal seperator, it is 3500r/min that main rotary drum revolving speed, which is arranged, together
When setting spiral deslagging rotary drum revolving speed be 2800r/min, under the influence of centrifugal force carry out feed liquid separation, material residue is by spiral deslagging
Rotary drum is pushed out to material residue outlet, and feed liquid flows out from centrifuge material liquid outlet, and all raw materials of 50min and production procedure are all complete
At the recovery rate of water-soluble substances is 95%, obtains the clarification feed liquid of solid content 2.2%, obtains mushroom feed liquid
(14200kg)。
The mushroom feed liquid is subjected to aseptic canning using conventional method, can be used as the master of mushroom soup or mushroom chafing dish bottom flavorings
Raw material is wanted, freeze drier or spray dryer can also be used, be used as mushroom solid beverage or mushroom flavouring after dry
Raw material.
As seen from the above embodiment, the present invention provides a kind of homogenate separators and plant beverage to be homogenized separation method,
Homogenate separator of the invention can make material reach higher fineness (more than 50 mesh), so as to shorter time or compared with
Low temperature sufficiently extracts water-soluble substances, and the present invention does not need large granular materials or high temperature extracts, and can utmostly protect
The heat-sensitive active material in raw material is stayed not to be destroyed, while preferable natural flavor, fragrance and the soup look for keeping plant beverage.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (10)
1. a kind of homogenate separator, which is characterized in that including be sequentially connected in series raw material elevator (2), osteoclastic pulverizer (3),
Colloid mill (4), homogeneous tank (5), multistage grinding pump (6), material keep in agitator tank (7) and horizontal centrifugal seperator (9).
2. homogenate separator according to claim 1, which is characterized in that further include screw pump (8), the screw pump
(8) material is set to keep between agitator tank (7) and the horizontal centrifugal seperator (9).
3. a kind of method that the homogenate for carrying out plant beverage using the as claimed in claim 1 or 22 homogenate separators is isolated, feature
It is, comprising the following steps:
Plant material is delivered to osteoclastic pulverizer (3) by raw material elevator (2), is crushed, obtains comminuting matter；
The comminuting matter is sent into colloid mill (4), is ground, obtains grinding material；
The grinding material is transferred to homogeneous tank (5), homogeneous is carried out, obtains homogenous mass；
The homogenous mass is sent to multistage grinding pump (6), multistage grinding is carried out, obtains refinement material；
The refinement material is sent to material and keeps in agitator tank (7), is stirred, obtains pasty material；
The pasty material is pumped into horizontal centrifugal seperator (9), is centrifuged, obtains feed liquid.
4. according to the method described in claim 3, it is characterized in that, the plant material is mixed with water when carrying out the crushing
It closes, material-water ratio is 1:0~15.
5. according to the method described in claim 3, the time of grinding is 2 it is characterized in that, the power of the grinding is 18.5kW
~5min, the yield of the colloid mill are 2~7T/h.
6. according to the method described in claim 3, it is characterized in that, the shearing rotating speed of the homogeneous is 4500r/min.
7. according to the method described in claim 3, it is characterized in that, when carrying out the multistage grinding, the multistage grinding pump
Power is 11kW, and revolving speed 2950r/min, treating capacity is 3~7T/h.
8. the method according to the description of claim 7 is characterized in that the time of the multistage grinding is 2~3min.
9. according to the method described in claim 3, it is characterized in that, the revolving speed of the stirring is 60~100r/min.
10. according to the method described in claim 3, it is characterized in that, the separation revolving speed of the centrifuge separation be 2500~
3500r/min, deslagging revolving speed are 1000~2400r/min.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113634336A (en) * | 2021-08-18 | 2021-11-12 | 优杨格股份有限公司 | Extraction element of asparagus powder plant chitosan and Beta glucan |
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| JPH02241555A (en) * | 1989-03-14 | 1990-09-26 | Satake Eng Co Ltd | Milling method and apparatus |
| CN2576336Y (en) * | 2002-09-11 | 2003-10-01 | 东北林业大学 | Beating extraction apparatus |
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