CN210753126U

CN210753126U - Homogenate separation device

Info

Publication number: CN210753126U
Application number: CN201921295892.7U
Authority: CN
Inventors: 章志强; 蔡亚; 靳锁; 陈克; 揭国良; 杨金花; 吴学进; 葛亮; 齐登峰; 王林林
Original assignee: Huangshan Greenxtracts Co ltd
Current assignee: Huangshan Greenxtracts Co ltd
Priority date: 2019-08-09
Filing date: 2019-08-09
Publication date: 2020-06-16
Anticipated expiration: 2029-08-09

Abstract

The utility model belongs to the technical field of the beverage preparation, especially, relate to a homogenate separation device. The utility model provides a homogenate separation device is including raw materials lifting machine 2, broken bone rubbing crusher 3, colloid mill 4, homogeneity jar 5, multistage grinding pump 6, the material agitator tank 7 and the horizontal centrifuge 9 of establishing ties in proper order. The utility model discloses a homogenate separator can make the material reach higher fineness (more than 50 meshes) to can not need large granule material or high temperature to draw at short time or lower temperature abundant extraction play water-soluble material, can remain the heat sensitivity active material in the raw materials by the at utmost and not destroyed, the natural flavor, fragrance and the hot water color of keeping plant beverage simultaneously better.

Description

Homogenate separation device

Technical Field

The utility model relates to a beverage preparation technical field especially relates to a homogenate separation device.

Background

Currently, the extraction methods of beverages include extraction in an extraction tank using hot water or counter-current extraction. However, in the extraction method of the extraction tank, the bottom of the extraction tank is provided with the filter screen, and because the area of the filter screen is limited, if the extracted material is too thin, the filter screen is easy to block and difficult to discharge, and the material with larger granularity needs to be selected for extraction; the particle size is large, long extraction time or high extraction temperature is needed to ensure complete extraction, but some heat-sensitive substances in the materials are easily damaged, the soup color becomes dark, and the natural aroma is weakened.

Therefore, the existing beverage extraction device finally causes the loss of heat-sensitive active substances, the reduction of natural aroma and flavor, and the deepening of soup color.

Disclosure of Invention

An object of the utility model is to provide a homogenate separation device, this homogenate separation device can be in short time or the lower temperature fully extract out the water-soluble material in the material, and the at utmost has remain active material and has not destroyed, the natural flavor, fragrance and the hot water color of better keeping plant beverage simultaneously.

In order to achieve the above object, the present invention provides the following technical solutions:

the utility model provides a homogenate separation device, including raw materials lifting machine 2, broken bone rubbing crusher 3, colloid mill 4, homogeneity jar 5, multistage grinding pump 6, the material agitator tank 7 and the horizontal centrifuge 9 of establishing ties in proper order.

Preferably, the device further comprises a screw pump 8, wherein the screw pump 8 is arranged between the material temporary storage stirring tank 7 and the horizontal centrifugal separator 9.

Preferably, the raw material elevator 2 is provided with a feeding port 1.

Preferably, the osteoclast crusher 3 is PGJ-100.

Preferably, the homogenizing tank 5 comprises a high shear homogenizer, which is of the type HSM-120.

Preferably, the multistage grinding pump 6 is model number AYJ-40-3.

Preferably, the horizontal centrifuge 9 is model LW450 ND.

Preferably, the horizontal centrifugal separator 9 is provided with a material residue outlet 10 and a material liquid outlet 11.

The utility model provides a homogenate separation device and plant beverage homogenate separation method, the utility model discloses a homogenate separation device can make the material reach higher fineness (more than 50 meshes) to can be in short time or lower temperature fully extract out water-soluble material, the utility model discloses do not need large granule material or high temperature to extract, can remain the heat sensitivity active material in the raw materials by the at utmost not destroyed, better natural flavor, fragrance and the hot water color of keeping plant beverage simultaneously.

The utility model discloses a homogenate separation device adopts horizontal centrifuge, and the separation of realization feed liquid that can be fine reaches better extraction effect, and the extraction rate of water-soluble material can reach more than 95%.

Drawings

FIG. 1 is a schematic diagram of the homogenate separation device of the utility model, wherein, 1-a feed port, 2-a raw material elevator, 3-a bone crusher, 4-a colloid mill, 5-a homogenizing tank, 6-a multistage grinding pump, 7-a material temporary storage stirring tank, 8-a screw pump, 9-a horizontal centrifuge, 10-a material slag outlet and 11-a material liquid outlet.

Detailed Description

The utility model provides a homogenate separator includes raw materials lifting machine 2, raw materials lifting machine 2 is provided with dog-house 1, the size of dog-house 1 is adjustable. In the present invention, the raw material elevator 2 is preferably a bucket elevator. The utility model discloses in, the raw materials lifting machine is used for carrying osteoclast rubbing crusher's feed inlet with the raw materials.

The utility model provides a homogenate separation device includes osteoclast rubbing crusher 3, osteoclast rubbing crusher 3 prefers to be provided with the feed inlet, the feed inlet is used for connecing the raw materials that come from the raw materials lifting machine greatly. In the present invention, the model of the osteoclast crusher 3 is preferably PGJ-100. The utility model discloses in, osteoclast crusher is built-in to be provided with the screen cloth that the aperture is 3 ~ 8mm, the screen cloth is used for straining the material after the breakage to colloid mill's feed inlet. The utility model discloses in, osteoclast rubbing crusher mainly plays the effect of smashing the material, and the raw materials can be broken into the fine particle by moving cutter when getting into osteoclast rubbing crusher.

The utility model provides a homogenate separation device includes colloid mill 4, colloid mill 4 preferred is provided with the feed inlet, the preferred toper of shape of feed inlet, the feed inlet is arranged in connecing greatly and comes from the undersize material of broken bone rubbing crusher well screen cloth. In the present invention, the colloid mill is preferably of the type JMF-180. The utility model discloses in, colloid mill 4's export is preferred to be provided with the three-way valve, the three-way valve is used for adjusting the direction of material, can turn to feed inlet or homogeneity jar with the material. The utility model discloses utilize the colloid mill to further grind the material.

The utility model provides a homogenate separator includes homogeneity jar 5, homogeneity jar 5 is preferred to include HSM-120 type high shear homogenizer, the utility model discloses utilize the homogeneity jar further to refine the granularity of material.

The utility model provides a homogenate separation device includes multistage grinding pump 6, the model of multistage grinding pump 6 is preferred AYJ-40-3. The utility model discloses in, multistage grinding pump is used for carrying the feed liquid and grinding the material.

The homogenate separation device provided by the utility model comprises a material temporary storage stirring tank 7, the material temporary storage stirring tank 7 is preferably provided with a stirring paddle and a jacket, and the stirring paddle is utilized for stirring, so that the material slag and liquid in the material can be kept in a slurry suspension state, and the water-soluble substances in the material can be fully separated out; the jacket is used for heating or cooling the materials so as to ensure that the freshness of the plant raw materials and the color of the materials are unchanged.

The utility model provides a homogenate separation device includes horizontal centrifuge 9, horizontal centrifuge 9 is preferred to be provided with main rotary drum, preferably be provided with the spiral in the main rotary drum and arrange the sediment rotary drum. In the present invention, the model of the horizontal centrifuge 9 is preferably LW450 ND. In the present invention, the horizontal centrifugal separator 9 is preferably provided with a material residue outlet 10 and a material liquid outlet 11. The utility model discloses in, the main rotary drum is used for the feed liquid separation, the spiral is arranged sediment rotary drum and is used for discharging the gained material sediment of feed liquid separation.

As an embodiment of the utility model, the homogenate separation device further comprises a screw pump 8, and the screw pump 8 is respectively connected with the material temporary storage stirring tank 7 and the horizontal centrifugal separator 9; the screw 8 pump is used for pumping the materials in the material temporary storage stirring tank 7 into the horizontal centrifugal separator 9.

The utility model provides an utilize above-mentioned technical scheme homogenate separator carries out plant beverage's homogenate separation's method, including following step:

conveying the plant raw materials to an osteoclast crusher 3 through a raw material elevator 2, and crushing to obtain crushed materials;

sending the crushed material to a colloid mill 4 for grinding to obtain a ground material;

transferring the ground material into a homogenizing tank 5, and homogenizing to obtain a homogenized material;

feeding the homogeneous material to a multistage grinding pump 6 for multistage grinding to obtain refined material;

sending the refined materials to a material temporary storage stirring tank 7, and stirring to obtain slurry materials;

and pumping the slurry material into a horizontal centrifugal separator 9 for centrifugal separation to obtain feed liquid.

In the present invention, the required raw materials are commercially available products known to those skilled in the art unless otherwise specified.

The utility model discloses carry plant material to osteoclast rubbing crusher 3 through raw materials lifting machine 2, smash, obtain crushing material. In the present invention, the plant material preferably includes fruits, vegetables, tea, mushrooms, dendrobe, polygonatum or yams. The utility model discloses the dog-house size of preferred characteristic (for example form, size) according to the plant material adjusts raw materials lifting machine to control the feeding volume. In the utility model discloses, the preferred material feeding speed of plant material is 15 ~ 20 kg/min.

In the utility model, when the smashing is carried out, the utility model discloses preferred will plant material mixes with water, and the material water ratio is preferred 1:0 ~ 15, more preferred 1:10 ~ 15, 1:0 ~ 1 or 1:2 ~ 5. The utility model discloses it is preferred to confirm the material water ratio according to the material property. Specifically, for dry raw materials such as: tea (green tea, black tea, dark tea, white tea, yellow tea and green tea), mushroom (mushroom, needle mushroom, bolete, tremella, black fungus, agaricus blazei murill and the like), medicinal and edible homologous raw materials (sealwort, momordica grosvenori, Chinese yam, dendrobium, ginkgo nuts and the like), and the ratio of materials to water is preferably 1: 10-15; for fresh fruit materials (such as strawberries, blueberries, medlar, cucumbers, dragon fruits, red dates, peaches and the like), the water content of the raw materials is large, and the ratio of the materials to the water is preferably 1: 0-1, and more preferably 1: 0.5-1; for raw materials (such as rose, honeysuckle, jasmine and the like) which are easy to swell after homogenization, the ratio of the raw materials to the water is preferably 1:2 to 5. The utility model discloses mix plant material and water, form mobile pulpiness material after osteoclast rubbing crusher and colloid mill homogenate, the circulation and the normal operating of the multistage grinding pump of being convenient for and follow-up technology, the purpose lets the water-soluble material in the raw materials fully dissolve out, improves extraction efficiency.

After obtaining the crushed material, the utility model discloses will the crushed material is sent to colloid mill 4 in, grinds, obtains the milling material. The utility model discloses in, the screen cloth of smashing the material preferred through osteoclast rubbing crusher 3 falls into colloid mill's toper feed inlet. The utility model discloses in, the power of grinding is preferred to be 18.5kW, and the time of grinding is preferred to be 2 ~ 5min, and more preferred is 3 ~ 4min, colloid mill 4's output is preferred to be 2 ~ 7T/h, and more preferred is 3 ~ 5T/h. In the grinding process, a three-way valve arranged at the outlet of the colloid mill is opened to enable the materials to flow back to the inlet of the colloid mill, the materials are circularly ground, and then the ground materials (the particle size fineness is less than 800 mu m) are turned to a homogenizing tank through the three-way valve. After the grinding is finished, the fineness of the obtained ground material is preferably 2-300 mu m.

After obtaining the grinding material, the utility model discloses will the grinding material changes over to homogeneity jar 5 over to, carries out the homogeneity, obtains the homogeneity material. The utility model discloses in, the process of homogeneity specifically is the high shear homogenizer who opens in the homogeneity jar 5, and high shear homogenizer continuously runs until this batch of material all pumps into multistage grinding pump 6. The utility model discloses in, this batch of material indicates that a batch of raw materials is accurate from advancing jar until feed liquid production finishes, and the process continuously moves and does not stop. The utility model discloses a high-speed rotatory shearing of high shear homogenizer makes the material fineness further improve. In the utility model discloses, homogeneous shearing rotational speed is preferred 4500r/min, homogeneous time is with this batch material complete operation. The utility model discloses in, high shear homogenizer continuous operation 5 ~ 6h need be shut down and wash the operation of resuming again.

After obtaining the homogeneity material, the utility model discloses will the homogeneity material is sent to multistage grinding pump 6, carries out multistage grinding, obtains refining the material. The utility model discloses in, multistage grinding specifically is when the homogeneity material reaches the half jar of homogeneity jar, opens multistage grinding pump 6, carries out further grinding. In the utility model, when the multistage grinding is carried out, the power of the multistage grinding pump 6 is preferably 11kW, the rotating speed is preferably 2950r/min, and the treatment capacity is preferably 3-7T/h; the circulation time of the multistage grinding pump 6 is preferably 2-3 min. In the utility model discloses, the fineness of refining the material is preferred 10 ~ 200 mu m.

Obtain refine the material after, the utility model discloses will refine the material and send to material agitator tank 7 of keeping in, stir, obtain the pulpiness material. The utility model discloses in, work as when refining the liquid level that the material was carried and is got into in the material agitator tank 7 of keeping in reachs the paddle, open the stirring rake and carry out the continuous stirring operation, end until this whole production of batch material. The utility model discloses in, the rotational speed of stirring is 60 ~ 100r/min, the process of stirring is continuously operated and is accomplished until the production process operation of this batch of material. The utility model discloses a material sediment and the liquid that continuously stir in making the material keep pulpiness suspended state (prevent that the material sediment from deposiing), make the water-soluble material in the material fully appear. The utility model preferably heats or cools the materials according to the actual conditions of the materials; specifically, for dry tea and dry fungus raw materials, hot water or steam is introduced into a jacket arranged in a material temporary storage stirring tank for heating, so that the temperature of the materials is raised to 30-80 ℃, and water-soluble components in the materials are more quickly dissolved into water added in the crushing process or juice extracted from fresh fruits; and a concentration tester is adopted to detect the content of the solid matters so as to judge the complete dissolution degree of the water-soluble components in the material. For fresh fruit materials, the temperature of the materials can be reduced to below 20 ℃ without heating or by introducing chilled water through a jacket, so that the freshness of the fruits and the color of the materials are not changed.

After obtaining the pulpiness material, the utility model discloses will horizontal centrifuge 9 is gone into to pulpiness material pump, carries out centrifugal separation, obtains the plant beverage. The utility model discloses it will preferably through screw pump 8 the pulpiness material pump is gone into horizontal centrifuge 9. In the utility model, the rotating speed (main rotating speed) of the main rotating drum is preferably 2500-3500 r/min, and more preferably 2800-3200 r/min; the rotating speed (deslagging rotating speed) of the spiral deslagging rotary drum is preferably 1000-2400 r/min, and more preferably 1500-2000 r/min; the process of centrifugal separation is continuously operated until the production process of this batch of material is operated and is accomplished the embodiment of the utility model provides an, centrifugal separation's time preferred is 5 ~ 6 h. In the centrifugal separation process, the slurry material is subjected to liquid-liquid separation under the action of centrifugal force, the material slag is discharged to a material slag outlet by the internal spiral deslagging rotary drum, and the material liquid flows out from a material liquid outlet of the horizontal centrifugal separator to obtain the plant beverage.

FIG. 1 is a schematic diagram of the homogenate separation device of the utility model, wherein, 1-a feed port, 2-a raw material elevator, 3-a osteoclast crusher, 4-a colloid mill, 5-a homogenizing tank, 6-a multi-stage grinding pump, 7-a material temporary storage stirring tank, 8-a screw pump, 9-a horizontal centrifuge, 10-a material slag outlet and 11-a material liquid outlet; according to the drawing, a raw material lifting machine, a broken bone pulverizer, a colloid mill, a homogenizing tank, a multi-stage grinding pump, a temporary material storage stirring tank, a screw pump and a horizontal centrifugal separator are sequentially connected in series, plant raw materials are conveyed to the broken bone pulverizer by the raw material lifting machine to be pulverized, obtained pulverized materials enter the colloid mill to be ground, obtained ground materials enter the homogenizing tank to be homogenized, obtained homogenized materials enter the multi-stage grinding pump to be multi-stage ground, obtained refined materials enter the temporary material storage stirring tank, slurry materials are formed under stirring operation, the slurry materials are conveyed to the horizontal centrifugal separator through the screw pump to be centrifugally separated, and material and slag separation is carried out to obtain material liquid.

The homogenate separation device provided in the present invention will be described in detail with reference to the following examples, but they should not be construed as limiting the scope of the present invention.

Example 1

Cleaning 1000kg of dry green tea, pouring the cleaned dry green tea into a feeding port of a raw material lifting machine, lifting the dried green tea by the raw material lifting machine at a feeding speed of 15kg/min, feeding the dried green tea into a osteoclast crusher, adding water at a material-water ratio of 1:15, crushing the dried green tea, enabling the obtained crushed green tea to flow downwards to a colloid mill through a screen with the aperture of 5mm, performing backflow grinding in the colloid mill for 3min, transferring the obtained ground green tea into a homogenizing tank, continuously shearing the ground green tea by a high-shear homogenizer at a speed of 4500r/min, starting a multi-stage grinding pump when the obtained ground green tea reaches a half tank of the homogenizing tank, pumping feed liquid from the multi-stage grinding pump into the homogenizing tank, circulating the feed liquid with the material in the homogenizing tank for 2min until the fineness reaches below 300 mu m, pumping the feed liquid into a material temporary storage stirring tank, starting a stirring paddle when the liquid level of the refined feed liquid conveyed into the material temporary stirring tank, obtaining a slurry material until the production of the batch of products is finished; starting a screw pump, pumping the slurry material into a horizontal centrifugal separator at a speed of 3000kg/h, setting the rotating speed of a main rotary drum to be 3500r/min and the rotating speed of a spiral deslagging rotary drum to be 2400r/min, separating the material liquid under the action of centrifugal force, pushing material slag out to a material slag outlet by the spiral deslagging rotary drum, allowing the material liquid to flow out of the material liquid outlet of the centrifugal separator, completing all raw materials and production processes in 290min, and obtaining a clarified material liquid (14500kg) with the water-soluble substance extraction rate of 95% and the tea soup solid content of 2.3%.

Comparative example 1

According to the traditional extraction process, an extraction tank is adopted to prepare the green tea feed liquid, the same feed-water ratio as that of the embodiment 1 is adopted, and extraction is carried out in the extraction tank at the temperature of 80 ℃ to obtain the green tea feed liquid.

The green tea liquid prepared in example 1 and comparative example 1 was subjected to component analysis by hplc method, and the specific results are shown in table 1.

Table 1 ingredients of green tea liquor prepared in example 1 and comparative example 1

Unit μ g/mL	Example 1	Comparative example 1
			Epigallocatechin EGC	2191.93	1736.96
Catechin C	85.59	88.79
			Epicatechin EC	524.25	369.63
Epigallocatechin gallate EGCG	3104.44	2363.88
			Gallocatechin gallate GCG	175.28	424.19
Epicatechin gallate ECG	566.77	482.77

Table 1 shows the change of the catechin composition of the green tea beverages prepared in example 1 and comparative example 1, and it can be seen from table 1 that the content of primary catechins EGC \ EGCG \ EC \ ECG in the green tea beverage prepared in example 1 is higher than that of the green tea feed liquid prepared in the conventional process (comparative example 1), while the content of simple catechins C and secondary catechins GCG in the green tea feed liquid prepared in the conventional process (comparative example 1) is higher, which indicates that the oxidation of the primary catechins is reduced and the oxidation of the secondary catechins is increased due to the high temperature damage in the conventional process, and the oxidation resistance effect of the secondary catechins is not as good as that of the primary catechins. Therefore, the process of the utility model can ensure that the effective active ingredients are not damaged.

Example 2

The fresh strawberry is used as a raw material to produce strawberry juice:

1000kg of fresh strawberries are cleaned and poured into a feeding port of a raw material lifting machine, the raw material lifting machine lifts the strawberries to a osteoclast crusher to crush the strawberries at a feeding speed of 15-20 kg/min, the obtained crushed materials flow downwards to a colloid mill through a screen with the aperture of 5mm, the colloid mill is subjected to reflux grinding for 3min, the obtained ground materials are transferred to a homogenizing tank, and a high-shear homogenizer in the homogenizing tank continuously performs shearing homogenization at a speed of 4500r/min until the batch of materials are completely produced. When the homogeneous materials in the tank reach a half tank of the homogenizing tank, starting a multi-stage grinding pump, returning the materials out of the grinding pump to the homogenizing tank for circulation for 2min, then pumping the materials into a material temporary storage stirring tank, when the liquid level of the refined materials conveyed into the material temporary storage stirring tank reaches a paddle, starting a stirring paddle, and carrying out rotary stirring at the speed of 80r/min until the production of the batch of products is finished to obtain slurry materials; starting a screw pump, pumping the slurry material into a horizontal centrifugal separator at a speed of 1500kg/h, setting the rotating speed of a main rotary drum to be 3500r/min and the rotating speed of a spiral deslagging rotary drum to be 1900r/min, separating the material liquid under the action of centrifugal force, pushing the material slag out to a material slag outlet by the spiral deslagging rotary drum, and allowing the material liquid to flow out of the material liquid outlet of the centrifugal separator, wherein all raw materials and production processes are completely finished within 60 min; obtaining strawberry juice (960 kg); the extraction rate of the water-soluble substances is 96 percent, and clear feed liquid with the solid content of 4.8 percent is obtained.

Example 3

Preparing the dendrobium officinale beverage:

cleaning 1000kg of fresh dendrobium officinale branches, and cutting into 1-2 cm dendrobium sections by using a medicine cutting machine; pouring the dendrobe segments into a feeding port of a raw material lifting machine, lifting the dendrobe segments by the raw material lifting machine at a feeding speed of 15kg/min and feeding the dendrobe segments into a osteoclast crusher, adding water at a material-water ratio of 1:5 according to a mass ratio, crushing, allowing the obtained crushed materials to flow downwards to a colloid mill through a screen with the aperture of 5mm, performing reflux grinding in the colloid mill for 3min, transferring the obtained ground materials into a homogenizing tank, and continuously shearing and homogenizing by a high-shear homogenizing machine in the tank at a speed of 4500r/min until the whole batch of materials are completely produced; when the homogeneous materials in the tank reach a half tank of the homogenizing tank, starting a multi-stage grinding pump, returning the materials out of the grinding pump to the homogenizing tank for circulation for 2min, then pumping the materials into a material temporary storage stirring tank, when the liquid level of the refined materials conveyed into the material temporary storage stirring tank reaches a paddle, starting a stirring paddle, and carrying out rotary stirring at the speed of 60r/min until the production of the batch of products is finished to obtain slurry materials; and (3) starting a screw pump, pumping the slurry material into a horizontal centrifugal separator, setting the rotating speed of a main rotary drum to be 3500r/min and the rotating speed of a spiral deslagging rotary drum to be 2400r/min, separating the material liquid under the action of centrifugal force, pushing the material slag and the dendrobium fiber to a material slag outlet by the spiral deslagging rotary drum, allowing the material liquid to flow out of the material liquid outlet of the centrifugal separator, completing all raw materials and production processes in 70min, and obtaining clear material liquid with the solid content of 1.5% and obtaining the dendrobium material liquid (5762kg), wherein the extraction rate of water-soluble substances is 96%.

The dendrobium feed liquid is aseptically canned by adopting a conventional method, can be used as a main raw material for preparing the dendrobium beverage, and can also be dried by adopting a freeze dryer or a spray dryer to be used as the dendrobium solid beverage.

Example 4

Preparing mushroom soup:

respectively crushing 500kg of raw materials of dry bolete, 300kg of dry mushroom raw material and 200kg of dry agaricus blazei murill into 1-3 mm of fineness, then uniformly mixing all the obtained raw materials, lifting the mixed raw materials from a feeding port of a raw material lifting machine at a feeding speed of 20kg/min, feeding the mixed raw materials into an osteoclast crusher, simultaneously adding hot water with the temperature of 80 ℃ to mix the hot water with the materials according to the material-water ratio of 1:15 by mass ratio, crushing, downwards flowing the obtained crushed materials into a colloid mill through a screen with the aperture of 5mm, carrying out reflux grinding in the colloid mill for 2min, transferring the obtained ground materials into a homogenizing tank, transferring the obtained ground materials into the homogenizing tank, continuously shearing and homogenizing by a high-shear homogenizer in the homogenizing tank at the speed of 4500r/min until all the batch of materials are completely produced; when the homogeneous materials in the tank reach a half tank of the homogenizing tank, starting a multi-stage grinding pump, returning the materials out of the grinding pump to the homogenizing tank for circulation for 2min, then pumping the materials into a material temporary storage stirring tank, when the liquid level of the refined materials conveyed into the material temporary storage stirring tank reaches a paddle, starting a stirring paddle, and carrying out rotary stirring at the speed of 100r/min until the production of the batch of products is finished to obtain slurry materials; and (3) starting a screw pump, pumping the slurry material into a horizontal centrifugal separator, setting the rotating speed of a main rotary drum to be 3500r/min and the rotating speed of a spiral deslagging rotary drum to be 2800r/min, separating the material liquid under the action of centrifugal force, pushing the material slag out to a material slag outlet by the spiral deslagging rotary drum, allowing the material liquid to flow out of the material liquid outlet of the centrifugal separator, completing all raw materials and production processes in 50min, obtaining a clarified material liquid with the solid content of 2.2% and obtaining a mushroom material liquid (14200kg), wherein the extraction rate of water-soluble substances is 95%.

The mushroom liquid is aseptically canned by adopting a conventional method, can be used as a main raw material of mushroom soup or mushroom hotpot condiment, and can also be dried by adopting a freeze dryer or a spray dryer to be used as a mushroom solid beverage or mushroom seasoning raw material.

According to the above embodiment, the utility model provides a homogenate separation device, the utility model discloses a homogenate separation device can make the material reach higher fineness (more than 50 meshes) to can be in short time or lower temperature fully extract out water-soluble material, do not need large granule material or high temperature to extract, can remain the heat sensitivity active material in the raw materials by the at utmost and not destroyed, the better natural flavor, fragrance and the hot water color that keeps vegetable beverage simultaneously.

The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications and decorations can be made without departing from the principle of the present invention, and these modifications and decorations should also be regarded as the protection scope of the present invention.

Claims

1. The utility model provides a homogenate separation device, its characterized in that includes raw materials lifting machine (2), osteoclast rubbing crusher (3), colloid mill (4), homogeneity jar (5), multistage grinding pump (6), the agitator tank (7) and horizontal centrifuge (9) of keeping in of establishing ties in proper order.

2. The homogenate separation device according to claim 1, characterized by further comprising a screw pump (8), the screw pump (8) being arranged between the material temporary holding tank (7) and the horizontal centrifuge (9).

3. The homogenate separation device according to claim 1, characterized in that the raw material elevator (2) is provided with a feed opening (1).

4. The homogenate separation device according to claim 1, characterized in that the osteoclast crusher (3) has the model PGJ-100.

5. The homogenate separation device according to claim 1, characterized in that the homogenizing tank (5) comprises a high shear homogenizer, the model of which is HSM-120.

6. The homogenate separation device according to claim 1, characterized in that the multistage grinding pump (6) has the model number AYJ-40-3.

7. The refining separation device according to claim 1, characterized in that the horizontal centrifuge (9) is of the type LW450 ND.

8. Homogenate separation device according to claim 1, characterized in that the horizontal centrifuge (9) is provided with a reject outlet (10) and a feed liquid outlet (11).