CN105918757B - A kind of preparation method of alfalfa solid beverage - Google Patents

A kind of preparation method of alfalfa solid beverage Download PDF

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CN105918757B
CN105918757B CN201610256161.6A CN201610256161A CN105918757B CN 105918757 B CN105918757 B CN 105918757B CN 201610256161 A CN201610256161 A CN 201610256161A CN 105918757 B CN105918757 B CN 105918757B
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alfalfa
solid beverage
concentrated slurry
preparation
concentrated
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CN105918757A (en
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玉永雄
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385Concentrates of non-alcoholic beverages
    • A23L2/39Dry compositions
    • A23L2/395Dry compositions in a particular shape or form
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52Adding ingredients
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A23L2/72Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by filtration
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

Abstract

The present invention provides a kind of preparation method of alfalfa solid beverage, comprising the following steps: after alfalfa fresh grass cleaning treatment, is successively beaten, is filtered, and obtains concentrated slurry after being concentrated;Auxiliary material is added into concentrated slurry, mixes, obtains molding feed liquid;The auxiliary material includes cyclodextrin;Molding feed liquid is used into mist projection granulating, obtains granular alfalfa solid beverage.In the present invention, water-removing processing is not carried out to alfalfa, be directly beaten, the content of the obtained nutritional ingredient in concentrated slurry significantly improves, especially the content of alfalfa saponin and flavones;The recovery rate of alfalfa is improved.Molding is dried for feed liquid is formed using Spray granulation method, forming temperature is low, advantageously ensures that effective nutritional ingredient in alfalfa is not lost.And moisture content is easy to control, and can guarantee the mass percentage of the moisture of alfalfa solid beverage of the invention below 5% well.

Description

A kind of preparation method of alfalfa solid beverage
Technical field
The present invention relates to alfalfa technical field of beverage more particularly to a kind of preparation sides of alfalfa solid beverage Method.
Background technique
Alfalfa is universally acknowledged high-quality legume forage, is known as " King of Pasture ", " father of food ".Alfalfa Rich in multiple nutritional components such as protein, microelement, vitamin, amino acid, but also contain unknown somatomedin.It is pale reddish brown Lysine content is 5.7 times higher than corn in alfalfa hay, the abundantest with the content of carrotene in vitamin, in microelement It is higher with the content of iron, manganese, zinc.Under same planting conditions, alfalfa is than the digestible protein that graminous pasture is harvested High 2.5 times of matter or so, high 6 times of minerals or so, high 2 times of digestible nutrient or so, in addition there are also significant UGF (unknown growth-promotings The long factor) effect.
It has been reported that at present and directly makes liquid beverage using after the mashing of alfalfa fresh grass, but need before mashing to fresh Grass is finished (drift soup), due to generally using high temperature when water-removing, when high temperature destroys cell membrane system and protein denaturation The solable matters such as saponin and flavones are encased and can not be exosmosed, and can also result in soluble protein and be denaturalized insoluble, reduction The nutritional ingredient of alfalfa.
Summary of the invention
In view of the above drawbacks of the prior art and problem, the object of the present invention is to provide a kind of alfalfa solid beverages Preparation method.During solving existing alfalfa processing and utilization, the technology of the component damages such as saponin, flavones and protein is asked Topic.
In order to achieve the above object, the invention provides the following technical scheme:
The preparation method of alfalfa solid beverage of the invention, comprising the following steps:
Step 1: being successively beaten after alfalfa fresh grass cleaning treatment, filter, and obtains thickened pulp after being concentrated Liquid;
Step 2: auxiliary material is added into concentrated slurry, mix, obtains molding feed liquid;The auxiliary material includes cyclodextrin;
Step 3: the molding feed liquid that step 2 is obtained carries out mist projection granulating, granular alfalfa solid drink is obtained Material;Wherein, during mist projection granulating, edible fine grained solid support is added.
In the present invention, in step 1, the density of the concentrated slurry obtained after control concentration is 1.1-1.5g/cm3.It is preferred that Ground, the density of concentrated slurry are 1.1-1.2g/cm3.Concentration is carried out using low-temperature reduced-pressure thickener, and temperature is controlled at 55 DEG C Below.
Preferably, in step 2, the mass ratio for controlling cyclodextrin and concentrated slurry is 1 ﹕ 30-45.More preferably, control ring is pasted The mass ratio of essence and concentrated slurry is 1 ﹕ 35-40.Optimally, the mass ratio for controlling cyclodextrin and concentrated slurry is 1 ﹕ 36.It is more smart The ratio of the two really is controlled, guarantees preferably embedding effect and low cost.
Further, in step 3, during mist projection granulating, control parameter is as follows: hot blast temperature is 60-70 DEG C, mist Changing chamber temperature is 40-60 DEG C.Preferably, hot blast temperature is 60-65 DEG C, and atomization chamber temperature is 45-55 DEG C.Optimally, hot wind temperature Degree is 60-65 DEG C, and atomization chamber temperature is 45-50 DEG C.
Further, in step 3, the partial size of the fine grained solid support is not less than 80 mesh.Preferably, the fine grained solid support Partial size is -120 mesh of 80 mesh.More preferably, the partial size of the fine grained solid support is -110 mesh of 100 mesh.
Further, in step 3, the weight ratio for controlling fine grained solid support and concentrated slurry is 1 ﹕ 3-6.Preferably, control is thin The weight ratio of grain carrier and concentrated slurry is 1 ﹕ 4.
Further, the fine grained solid support uses white sugar or/and maltodextrin;When for the mixture of white sugar and maltodextrin When, the mass ratio for controlling white sugar and maltodextrin is 3-5 ﹕ 1.Preferably, the mass ratio of control white sugar and maltodextrin is 4 ﹕ 1.
Further preferred technical solution is in step 1, after alfalfa fresh grass cleaning treatment, successively to be beaten Slurry, is obtained by filtration slurries, before slurries are concentrated, increases the step of heating to slurries, then by the slurries mistake after heating Filter, the leaf protein and filtered solution being precipitated, then filtered solution is concentrated, obtain concentrated slurry.Leaf protein is precipitated.At this point, It in concentration process, is carried out using low-temperature reduced-pressure thickener, temperature is controlled at 60-80 DEG C.
Further, in the heating stepses, slurries are heated up, control highest warming temperature is 80 DEG C, then keeps the temperature 3- Then 6min is filtered, obtain filtered solution.
Specifically, in the heating stepses, slurries is warming up to 60 DEG C -80 DEG C, 3-6min is kept the temperature, then filters, must filter Cross liquid.
Further, in the heating stepses, using staged heating method, 60 DEG C -72 DEG C is first warming up to, keeps the temperature 2- 5min, filtering, obtains green protein and filtered solution;Then filtered solution is again heated to 75 DEG C -80 DEG C, keeps the temperature 1-2min, refilters, Obtain white protein and filtered solution.
The preparation method of alfalfa solid beverage of the invention has following advantage:
(1) firstly, not finishing to alfalfa in the preparation process of the concentrated slurry of the alfalfa of step 1 Processing, is directly beaten, filters and be concentrated to get concentrated slurry.It is dense with the water-removing that is beaten, filters and is concentrated to get again after finishing Contracting slurries are compared, and the content for the nutritional ingredient in concentrated slurry that step 1 of the present invention obtains significantly improves, especially clover soap The content of glucoside and flavones;The recovery rate of alfalfa is improved;Be conducive to the alfalfa solid beverage that the present invention obtains to produce The raising of the yield and quality of product.Concentration process is carried out using low-temperature reduced-pressure thickener, and temperature is controlled at 55 DEG C or less.
(2) secondly, in step 2, concentrated slurry is carried out by the way that the auxiliary material comprising cyclodextrin is added into concentrated slurry Allotment, the careless fishy smell in concentrated slurry is embedded.And the mass ratio of cyclodextrin and concentrated slurry is furthermore presented, it protects Card preferably embeds effect and reduces cost.
(3) in addition, in step 3, using Spray granulation method, it is additionally added edible particulate in granulation process and carries Body.Using fine grained solid support as core, molding feed liquid is adhered on fine grained solid support, obtains the consistent granular solids of granular size, shape Beverage, nutrition is more and proportion is reasonable and easy to dissolve, is easily absorbed by the body, 5% or less water content.And it is spraying Forming temperature is low in prilling process, advantageously ensures that the effective component in alfalfa is not lost.And moisture content is easy control System, can guarantee well the content of the moisture of alfalfa solid beverage of the invention 5% (wt.) below.And in conventional dry In drying method (box-type drying method), concentrated slurry needs are spread out very one layer thin, and efficiency is very low;And concentrated slurry is at 70 DEG C or less When dry, moisture content be difficult it is up to standard, i.e., 5% hereinafter, but drying temperature at 70 DEG C or more be then easy to coking;It is difficult to control, It is not suitable for the molding feed liquid of step 2 of the present invention.
(4) simultaneously, in step 3, by the procedure parameter of comprehensively control mist projection granulating, and for the dense of mist projection granulating The parameters such as the density and concentrated slurry of contracting slurries and the ratio of fine grained solid support realize preferably control mist projection granulating molding.
(5) in preferred technical solution, before slurries are concentrated, the long-chained protein in slurries is precipitated by heating, is obtained To leaf protein and filtered solution, eliminate the long-chained protein for being not easy to be absorbed by the body in filtered solution, remain short catenin abundant, Small peptide, amino acid etc. easily absorb ingredient, so that active constituent content is high in finally obtained solid beverage, it is more reasonable to match, and And instant capacity is more preferable, is easier to be absorbed by the body.Obtained leaf protein, which is precipitated, can process to obtain leaf protein product, e.g., leaf protein Piece, leaf protein capsule etc..In the concentration process of the preferred technical solution, carried out using low-temperature reduced-pressure thickener, temperature control System is at 60-80 DEG C.
By further preferred gradient-heated mode, green protein and white protein is precipitated respectively, thus easily Different post-processings is carried out to green protein and white protein, obtains different protein products.
(6) the alfalfa solid beverage that preparation method of the invention obtains is granular size, the consistent graininess of shape Solid beverage, it is easy to dissolve, it is easily absorbed by the body, 5% or less water content.Wherein contain higher alfalfa saponin and flavones, With good quality.Preferably to obtained solid beverage after slurries heat treatment, long-chained protein is removed by the present invention, nutrition at Distribution ratio is more reasonable, while instant capacity is more preferable, it is easier to be absorbed by the body.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this Some embodiments of invention without any creative labor, may be used also for those of ordinary skill in the art To obtain other drawings based on these drawings.
Fig. 1 is the flow diagram of the preparation method of the alfalfa solid beverage of the embodiment of the present invention 1;
Fig. 2 is the flow diagram of the preparation method of the alfalfa solid beverage of the embodiment of the present invention 4.
Specific embodiment
Below in conjunction with the embodiment of the present invention, technical solution of the present invention is clearly and completely described, it is clear that Described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Based on the implementation in the present invention Example, every other embodiment obtained by those of ordinary skill in the art without making creative efforts belong to The scope of protection of the invention.
Embodiment 1
As shown in connection with fig. 1, illustrate the preparation method of the alfalfa solid beverage of the embodiment of the present invention 1, including following step It is rapid:
Step 1: being successively beaten after the removal of impurities of alfalfa fresh grass, cleaning treatment, filtering (e.g., filters pressing), obtain Slurries;Concentrated slurry is obtained after slurries are concentrated again;Concentration is carried out using low-temperature reduced-pressure thickener, and temperature is controlled 45 ℃-50℃。
Step 2: auxiliary material is added into concentrated slurry, mix, obtains molding feed liquid;The auxiliary material includes cyclodextrin;It utilizes The careless fishy smell of cyclodextrin embedding concentrated slurry.
Step 3: the molding feed liquid that step 2 is obtained carries out mist projection granulating, granular alfalfa solid drink is obtained Material;Wherein, during mist projection granulating, edible fine grained solid support is added.
In the present invention, using Spray granulation method, using fine grained solid support as core, molding feed liquid is adhered on fine grained solid support, is obtained To granular size, the consistent granular solids beverage of shape, 5% or less water content.And during mist projection granulating, molding temperature It spends low, advantageously ensures that the effective component in alfalfa is not lost.And moisture content is easy to control, and can guarantee this well The moisture content of the alfalfa solid beverage of invention 5% (wt.) below.
In step one of the invention, filter pulp is crossed to what is obtained after being directly beaten, filtering by alfalfa fresh grass in step 1 The dried object (i.e. extract) of liquid is measured, alfalfa saponins measurement using ultraviolet spectrophotometry (Wang Songbai, 2005, in State's academy of agricultural sciences's Master's thesis);Clover Determination of Total Flavonoids uses spectrophotometry (Gui Jingsong, 2009, Heilungkiang medical science).It surveys It is fixed that the results are shown in Table 1.
The extraction yield that 1 fresh grass of table is directly beaten and alfalfa saponin and flavones content in extract
*: what the dry rate 15.1% that hay weight is measured from large sample calculated.
Three parallel measurements are carried out after *: three sample extraction object mixing.
As a comparison, in the present invention to by after the water-removing of alfalfa fresh grass, then obtained water-removing after being beaten, being filtered The dried object (i.e. extract) of filter pulp liquid is measured, alfalfa saponins measurement using ultraviolet spectrophotometry (Wang Songbai, 2005, the Chinese Academy of Agricultural Sciences's Master's thesis);(Gui Jingsong, 2009, Heilungkiang is medical using spectrophotometry for clover Determination of Total Flavonoids Science).Measurement result is as shown in table 2.
The extraction yield being beaten after the water-removing of 2 fresh grass of table and alfalfa saponin and flavones content in extract
*: what the dry rate 15.1% that hay weight is measured from large sample calculated.
Three parallel measurements are carried out after *: three sample extraction object mixing.
As it can be seen that compared with the slurries being beaten again after water-removing, the present invention using do not finish directly be beaten by the way of obtain Slurries in the content of effective component significantly improve, the especially content of alfalfa saponin and flavones;Extraction to alfalfa Rate improves;Be conducive to the raising of the yield and quality for the alfalfa solid beverage product that the present invention obtains.
In the step of embodiment of the present invention 1 one, alfalfa fresh grass is directly beaten filtered slurries and is concentrated Processing is handled to certain specific gravity, to adapt to subsequent atomizing granulating technology.It is preferred that the concentrated slurry obtained after control concentration Density is 1.1-1.5g/cm3.The density of the concentrated slurry more preferably obtained after control concentration is 1.1-1.2g/cm3
In step 2, the auxiliary material comprising cyclodextrin is added, the careless fishy smell in concentrated slurry can be embedded.According to pale reddish brown The characteristic of alfalfa, the preferably mass ratio of control cyclodextrin and concentrated slurry are 1 ﹕ 30-45.Precisely control the ratio of the two Example guarantees preferably embedding effect and reduces cost.
It certainly, can also include other some auxiliary material raw materials, such as in the auxiliary material being added in step 2 into concentrated slurry The auxiliary materials such as D-sorbite or citric acid, can also add some functional components, so that final alfalfa solid is drunk Material has corresponding function.
It during the mist projection granulating of step 3, needs to control hot blast temperature and atomization chamber temperature, is granulated effect to guarantee to be atomized Fruit guarantees grain forming, and the water content for preferably controlling alfalfa solid beverage is lower than 5%.Therefore, for alfalfa Molding feed liquid the high characteristic of viscosity, during mist projection granulating, preferably control parameter is as follows: hot blast temperature is 60-70 DEG C, mist Changing chamber temperature is 40-60 DEG C.It is highly preferred that hot blast temperature is 60-65 DEG C, atomization chamber temperature is 45-55 DEG C.
In step 3, the partial size of the fine grained solid support is not less than 80 mesh.
The ratio of the fine grained solid support and concentrated slurry has shadow to grain forming rate, taste and the mouthfeel of solid beverage It rings.It is therefore preferred that the weight ratio of control fine grained solid support and concentrated slurry is 1 ﹕ 3-6.
Specifically, the fine grained solid support uses edible particulate, it is preferred to use white sugar or/and maltodextrin;When being white When the mixture of sugar and maltodextrin, the mass ratio for controlling white sugar and maltodextrin is 3-5 ﹕ 1.
In the embodiment of the present invention 1, the specific mist projection granulating that step 3 is completed using PLG spray-drying pelleting machine, concentrate Body enters atomization chamber by spray gun, and fine grained solid support is first put in atomization chamber bottom before by spraying.
Embodiment 2
The preparation method of the alfalfa solid beverage of the embodiment of the present invention 2, comprising the following steps:
Step 1: being successively beaten after the removal of impurities of alfalfa fresh grass, cleaning treatment, filtering (e.g., filters pressing), obtain Slurries;Concentrated slurry is obtained after slurries are concentrated again;The density for controlling concentrated slurry is 1.1-1.2g/cm3.Concentration uses Low-temperature reduced-pressure thickener carries out, and temperature is controlled at 45 DEG C -50 DEG C.
Step 2: auxiliary material is added into concentrated slurry, blending and mixing obtains molding feed liquid;The auxiliary material includes cyclodextrin; The mass ratio for controlling cyclodextrin and concentrated slurry is 1 ﹕ 36.
Step 3: the molding feed liquid that step 2 is obtained carries out mist projection granulating, granular alfalfa solid drink is obtained Material;Wherein, during mist projection granulating, edible fine grained solid support is added;The fine grained solid support uses white sugar and maltodextrin Mixture, the mass ratio of white sugar and maltodextrin is 4 ﹕ 1.The partial size of white sugar and maltodextrin is 100 in the fine grained solid support Mesh;The weight ratio for controlling fine grained solid support and concentrated slurry is 1 ﹕ 4.
And during mist projection granulating, control parameter is as follows: hot blast temperature is 60-65 DEG C, and atomization chamber temperature is 45-50 ℃。
In the embodiment of the present invention 2, density is 1.1-1.2g/cm in the fine grained solid support and step 1 of 100 mesh partial sizes3Concentration Slurries have better matching degree, so that ratio of briquetting is higher.
Embodiment 3
The preparation method of the alfalfa solid beverage of the embodiment of the present invention 3, comprising the following steps:
Step 1: being successively beaten after alfalfa fresh grass cleaning treatment, filters (e.g., filters pressing), obtain slurries; Concentrated slurry is obtained after slurries are concentrated again;The density for controlling concentrated slurry is 1.5g/cm3.Concentration uses low-temperature reduced-pressure Thickener carries out, and temperature is controlled at 45 DEG C -50 DEG C.
Step 2: auxiliary material is added into concentrated slurry, blending and mixing obtains molding feed liquid;The auxiliary material includes cyclodextrin; The mass ratio for controlling cyclodextrin and concentrated slurry is 1 ﹕ 35-40.
Step 3: the molding feed liquid that step 2 is obtained carries out mist projection granulating, granular alfalfa solid drink is obtained Material;Wherein, during mist projection granulating, edible fine grained solid support is added;The fine grained solid support uses white sugar and maltodextrin Mixture, the mass ratio of white sugar and maltodextrin is 3-5 ﹕ 1.The partial size of white sugar and maltodextrin is 80 in the fine grained solid support Mesh;The weight ratio for controlling fine grained solid support and concentrated slurry is 1 ﹕ 3-6.
And during mist projection granulating, control parameter is as follows: hot blast temperature is 60-65 DEG C, and atomization chamber temperature is 45-55 ℃。
Embodiment 4
Improvement on the basis of above-described embodiment 1 to embodiment 3, to step 1 progress.Specifically, as shown in Fig. 2, step In rapid one, after alfalfa fresh grass cleaning treatment, successively it is beaten, slurries is obtained by filtration, before slurries are concentrated, Increase the step of heating to slurries, heating temperature is up to 80 DEG C, is then filtered the slurries after heating, the leaf egg being precipitated White and filtered solution, then filtered solution is concentrated, obtain concentrated slurry.At this point, being concentrated in concentration process using low-temperature reduced-pressure Machine carries out, and temperature is controlled at 60-80 DEG C.
Specifically, in heating stepses, slurries is warming up to 60 DEG C -80 DEG C, 3-6min is kept the temperature, then filters, must filter Liquid.
Long-chained protein in slurries is not easy to be absorbed by the body, and will affect the water solubility of alfalfa solid beverage, because This, preferably by heating by slurries long-chained protein be precipitated, obtain leaf protein and filtered solution, eliminated in filtered solution be not easy by The long-chained protein of absorption of human body remains short catenin abundant, small peptide, amino acid etc. and easily absorbs ingredient, so that finally obtaining Solid beverage in active constituent content it is high, and nutritional ingredient proportion is rationally, is easier to be absorbed by the body;While instant capacity is more It is good.
Obtained leaf protein, which is precipitated, can process to obtain leaf protein product, e.g., leaf protein piece, leaf protein capsule etc..
There are green proteins and white protein in long-chained protein in slurries, are by whole in above-mentioned heating method Green protein and part long-chain white protein be precipitated simultaneously, to it is subsequent to albumen carry out deep processing when make troubles, therefore, Preferred technical solution is in the embodiment of the present invention 4, using staged heating method, by green protein and long-chain white protein into Row is precipitated respectively, and specific staged heating method is as follows: being first warming up to 60 DEG C -72 DEG C, keeps the temperature 2-5min, filtering obtains green Albumen and filtered solution;Then filtered solution is again heated to 75 DEG C -80 DEG C, keeps the temperature 1-2min, refilters, obtain white protein and filtration Liquid.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any Those familiar with the art in the technical scope disclosed by the present invention, can easily think of the change or the replacement, and should all contain Lid is within protection scope of the present invention.Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.

Claims (7)

1. a kind of preparation method of alfalfa solid beverage, which comprises the following steps:
Step 1: being successively beaten after alfalfa fresh grass cleaning treatment, filter, and obtains concentrated slurry after being concentrated;
Step 2: auxiliary material is added into concentrated slurry, mix, obtains molding feed liquid;The auxiliary material includes cyclodextrin;
Step 3: the molding feed liquid that step 2 is obtained carries out mist projection granulating, granular alfalfa solid beverage is obtained;Its In, during mist projection granulating, edible fine grained solid support is added;
In step 1, after alfalfa fresh grass cleaning treatment, successively it is beaten, slurries is obtained by filtration, carried out to slurries Before concentration, increase the step of heating to slurries, then filter the slurries after heating, the leaf protein and filtered solution being precipitated, Filtered solution is concentrated again, obtains concentrated slurry;
In the heating stepses, using staged heating method, 60 DEG C -72 DEG C are first warming up to, keeps the temperature 2-5min, filtering;Then 75 DEG C -80 DEG C are again heated to, 1-2min is kept the temperature, refilters, obtain filtered solution.
2. a kind of preparation method of alfalfa solid beverage according to claim 1, which is characterized in that in step 1, The density of the concentrated slurry obtained after control concentration is 1.1-1.5g/cm3.
3. a kind of preparation method of alfalfa solid beverage according to claim 1 or 2, which is characterized in that control The mass ratio of cyclodextrin and concentrated slurry is 1 ﹕ 30-45.
4. a kind of preparation method of alfalfa solid beverage according to claim 1 or 2, which is characterized in that spraying In granulation process, control parameter is as follows: hot blast temperature is 60-70 DEG C, and atomization chamber temperature is 40-60 DEG C.
5. a kind of preparation method of alfalfa solid beverage according to claim 1 or 2, which is characterized in that step In three, the partial size of the fine grained solid support is not less than 80 mesh.
6. a kind of preparation method of alfalfa solid beverage according to claim 1 or 2, which is characterized in that step In three, the weight ratio for controlling fine grained solid support and concentrated slurry is 1 ﹕ 3-6.
7. a kind of preparation method of alfalfa solid beverage according to claim 1 or 2, which is characterized in that step In three, the fine grained solid support uses white sugar or/and maltodextrin;When the fine grained solid support uses the mixing of white sugar and maltodextrin When object, the mass ratio for controlling white sugar and maltodextrin is 3-5 ﹕ 1.
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