阅读说明：本技术 一种山楂清汁及其生产工艺 (Hawthorn clear juice and production process thereof ) 是由 刘位刚 王泽祥 张松健 于 2020-12-22 设计创作，主要内容包括：本申请涉及饮料的领域,具体公开了一种山楂清汁及其生产工艺。一种山楂清汁由包含以下重量份的原料制成,鲜山楂：2～4份,纯水：6～8份,冰糖溶液：1～3份,鲜山楂与纯水混合并经浸提、过滤制得山楂浸出液,所述山楂浸出液包括一次浸提液和二次浸提液；其生产工艺为：一次浸提,过滤输送,二次浸提过滤输送,溶糖,调配定容,再次过滤,杀菌。本申请的山楂清汁通过将果肉过滤,其具有提高引用口感优点；另外,本申请的生产工艺具有降低山楂清汁内果肉含量优点。(The application relates to the field of beverages, and particularly discloses a hawthorn clear juice and a production process thereof. A hawthorn clear juice is prepared from the following raw materials in parts by weight: 2-4 parts of pure water: 6-8 parts of a rock sugar solution: 1-3 parts of fresh hawthorn and pure water, and leaching and filtering to obtain hawthorn leaching liquid, wherein the hawthorn leaching liquid comprises a primary leaching liquid and a secondary leaching liquid; the production process comprises the following steps: leaching for the first time, filtering and conveying, leaching for the second time, filtering and conveying, dissolving sugar, blending to a constant volume, filtering again and sterilizing. The hawthorn clear juice has the advantage of improving taste by filtering the pulp; in addition, the production process has the advantage of reducing the content of the pulp in the hawthorn clear juice.)

1. The hawthorn clear juice is characterized by being prepared from the following raw materials in parts by weight: 2-4 parts of pure water: 6-8 parts of a rock sugar solution: 1-3 parts of fresh hawthorn and pure water, and leaching and filtering to obtain hawthorn leachate, wherein the hawthorn leachate comprises a primary leaching solution and a secondary leaching solution.

2. The hawthorn juice according to claim 1, wherein the crystal sugar is a single crystal sugar, and the weight ratio of the fresh hawthorn, the pure water and the single crystal sugar is 2:6: 3.

3. The process for producing the hawthorn juice as claimed in any one of claims 1 to 2, which comprises the following steps:

s1, primary leaching: putting fresh hawthorn into an extraction pot extraction cage, adding pure water which accounts for half of the weight of the pure water into the extraction pot, wherein the temperature of the pure water is 85 ℃, heating the pure water to 90-100 ℃, and extracting for 50-70 min;

s2, filtration and transportation: obtaining a primary leaching solution after leaching, filtering the primary leaching solution in an extraction pot, pumping the filtered primary leaching solution into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s3, secondary leaching, filtering and conveying: adding the residual pure water into the extraction pot after the conveying is finished, circularly lifting the extraction cage in the extraction pot, wherein the lifting is carried out for 5-9 times, so as to obtain a secondary extract, filtering the secondary extract, pumping the filtered secondary extract into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s4, sugar dissolving: putting the single crystal sugar into a sugar dissolving tank while stirring the hawthorn leaching solution, wherein the stirring speed is 40r/min, and stirring for 15min to prepare a mixed solution;

s5, blending and fixing the volume: pumping the mixed solution into a blending cylinder for stirring at the stirring speed of 40r/min for 10 min;

s6, filtering again: filtering the mixed solution prepared in the step S5, wherein the filtering mesh number is 300 meshes;

s7, sterilization: and (4) carrying out ultra-high temperature sterilization on the mixed solution filtered by the S6, wherein the sterilization temperature is 105-125 ℃, and the sterilization time is 8-12S, so as to obtain the hawthorn clear juice.

4. The production process of the hawthorn juice as claimed in claim 3, further comprising a centrifugal precipitation, wherein the centrifugal precipitation is located between the primary leaching and the filtration and transportation processes, and the centrifugal precipitation is as follows: centrifuging the primary leaching solution, discarding the precipitate, and pumping the supernatant to a filtering process.

5. The production process of the hawthorn clear juice according to claim 3 or 4, characterized in that the sugar dissolving tank comprises a tank body (1) for containing the mixed solution, the side wall of the tank body (1) is detachably connected with a conveying mechanism (2) for conveying the mixed solution, the conveying mechanism (2) comprises a conveying pipe (21) detachably connected with the tank body (1), the liquid inlet end of the conveying pipe (21) is detachably connected with the lower end of the side wall of the tank body (1) and is communicated with the interior of the tank body (1), the liquid outlet end of the conveying pipe (21) is detachably connected with a conveying pump (22), the conveying pipe (21) is connected with a switch valve (212), the conveying pipe (21) is detachably connected with a filtering mechanism (3), and the filtering mechanism (3) filters the mixed solution.

6. The production process of the hawthorn juice as claimed in claim 5, wherein the conveying pipe (21) comprises a first pipe body (211) detachably connected with the cylinder body (1), the switch valve (212) is connected to the first pipe body (211), one end of the first pipe body (211) far away from the cylinder body (1) is detachably connected with a second pipe body (213), the second pipe body (213) is vertically arranged, the lower end of the second pipe body (213) is detachably connected with the first pipe body (211), one end of the second pipe body (213) far away from the first pipe body (211) is horizontally detachably connected with a third pipe body (214), one end of the third pipe body (214) far away from the second pipe body (213) is vertically detachably connected with a fourth pipe body (215), the upper end of the fourth pipe body (215) is detachably connected with the third pipe body (214), and the lower end of the fourth pipe body (215) is detachably connected with the liquid inlet end of the conveying pump (22), the filtering mechanism (3) is detachably connected in the second pipe body (213).

7. The production process of the hawthorn juice as claimed in claim 6, wherein the filtering mechanism (3) comprises a cylindrical filtering tube (31) coaxially arranged in the second tube body (213), the outer diameter of the filtering tube (31) is smaller than the inner diameter of the second tube body (213), a plurality of through holes (32) are formed in the side wall of the filtering tube (31), a sealing plate (33) for sealing one end of the filtering tube (31) is fixedly connected to one end of the filtering tube (31) facing the third tube body (214), and a connecting component (35) for detachably connecting the filtering tube (31) in the second tube body (213) is arranged on the side wall of the filtering tube (31).

8. The production process of the hawthorn juice as claimed in claim 7, wherein one end of the first pipe body (211) far away from the cylinder body (1) is obliquely arranged towards the direction far away from the ground.

9. The production process of hawthorn juice according to claim 7, wherein the connecting assembly (35) comprises a first connecting ring (351) fixedly connected to the inner wall of the second tube body (213), and a second connecting ring (352) is coaxially and fixedly connected to one end of the filtering tube (31) far away from the sealing plate (33), and the second connecting ring (352) is screwed into the first connecting ring (351).

10. The production process of the hawthorn juice as claimed in claim 7, wherein the sealing plate (33) is in threaded connection with an electric heating rod (341) for heating the mixed solution, the electric heating rod (341) is coaxially arranged in the filtering tube (31), the diameter of the electric heating rod (341) is smaller than the inner diameter of the filtering tube (31), and the electric heating rod (341) is electrically connected with a power supply.

Technical Field

The application relates to the field of beverages, in particular to a hawthorn clear juice and a production process thereof.

Background

The hawthorn is stone fruit, hard stone, thin pulp and slightly sour and astringent taste. The fruit can be eaten raw or used as a preserved fruit cake, can be used as a medicine after being dried, is a tree species which is a special Chinese medicine and fruit, has the effects of reducing blood fat, blood pressure, strengthening heart, resisting arrhythmia and the like, is also a good medicine for strengthening spleen, stimulating appetite, promoting digestion, removing food stagnation, promoting blood circulation and reducing phlegm, and has good curative effects on chest, diaphragm and spleen fullness, hernia, blood stasis, amenorrhea and other symptoms. The vitexin is a flavonoid compound in hawthorn, is a drug with strong anticancer effect, and the extract of the vitexin has certain effects on inhibiting the growth, proliferation and infiltration and metastasis of cancer cells in vivo.

The Chinese patent application with the publication number of CN110089643A discloses a hawthorn fruit granule beverage and a preparation process thereof, and the hawthorn fruit granule beverage comprises 10-20 wt% of hawthorn fruit granules, 77-89 wt% of hawthorn juice and 1-3 wt% of food additives, and is prepared by the processes of screening, cleaning, softening, pulping, leaching, coarse juice, granulating, refined juice, blending, homogenizing, filling, capping, inverted bottle sterilization, lamp inspection, constant-temperature sterilization and packaging.

In view of the above-mentioned related art, the inventors consider that a hawthorn beverage containing hawthorn fruit particles has poor mouthfeel upon drinking.

Disclosure of Invention

In order to improve the drinking taste of the hawthorn beverage, the application provides the hawthorn clear juice and a production process thereof.

In a first aspect, the application provides a hawthorn juice, which adopts the following technical scheme:

a hawthorn clear juice is prepared from the following raw materials in parts by weight: 2-4 parts of pure water: 6-8 parts of a rock sugar solution: 1-3 parts of fresh hawthorn and pure water, and leaching and filtering to obtain hawthorn leachate, wherein the hawthorn leachate comprises a primary leaching solution and a secondary leaching solution.

By adopting the technical scheme, the hawthorn extract and the rock candy are used as raw materials, and the hawthorn extract is only prepared from hawthorn and pure water, so that the prepared hawthorn clear juice is not added with any additive, and is healthier for human bodies; after the hawthorn extract is filtered, the pulp in the hawthorn extract can be effectively filtered, so that the taste of the hawthorn clear juice is further improved.

Preferably, the crystal sugar is single crystal sugar, and the weight ratio of the fresh hawthorn, the pure water and the single crystal sugar is 2:6: 3.

By adopting the technical scheme, the single crystal rock sugar is purer, so that the prepared hawthorn clear juice has fewer impurities, and the quality and the taste of the hawthorn clear juice are improved.

In a second aspect, the application provides a production process of hawthorn clear juice, which adopts the following technical scheme:

a production process of hawthorn clear juice comprises the following steps:

s1, primary leaching: putting fresh hawthorn into an extraction pot extraction cage, adding pure water which accounts for half of the weight of the pure water into the extraction pot, wherein the temperature of the pure water is 85 ℃, heating the pure water to 90-100 ℃, and extracting for 50-70 min;

s2, filtration and transportation: obtaining a primary leaching solution after leaching, filtering the primary leaching solution in an extraction pot, pumping the filtered primary leaching solution into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s3, secondary leaching, filtering and conveying: adding the residual pure water into the extraction pot after the conveying is finished, circularly lifting the extraction cage in the extraction pot, wherein the lifting is carried out for 5-9 times, so as to obtain a secondary extract, filtering the secondary extract, pumping the filtered secondary extract into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s4, sugar dissolving: putting the single crystal sugar into a sugar dissolving tank while stirring the hawthorn leaching solution, wherein the stirring speed is 40r/min, and stirring for 15min to prepare a mixed solution;

s5, blending and fixing the volume: pumping the mixed solution into a blending cylinder for stirring at the stirring speed of 40r/min for 10 min;

s6, filtering again: filtering the mixed solution prepared in the step S5, wherein the filtering mesh number is 300 meshes;

s7, sterilization: and (4) carrying out ultra-high temperature sterilization on the mixed solution filtered by the S6 at the sterilization temperature of 115 ℃ for 10S to obtain the hawthorn clear juice.

By adopting the technical scheme, the fresh hawthorn is soaked in hot water and then is heated and extracted, so that nutrient substances in the fresh hawthorn pass through the outer skin of the fresh hawthorn and enter pure water, the nutrient substances in the fresh hawthorn are further transferred into the pure water through secondary extraction, and pulp and impurities are removed while the acidity of the mixed solution is adjusted through a filtering, sugar dissolving and filtering mode, so that the taste of the clear hawthorn juice is improved.

Preferably, the method further comprises centrifugal precipitation, wherein the centrifugal precipitation is located between the primary leaching and the filtration conveying, and the centrifugal precipitation is as follows: centrifuging the primary leaching solution, discarding the precipitate, and pumping the supernatant to a filtering process.

By adopting the technical scheme, the pulp and the impurities are separated from the primary leaching liquor through centrifugal precipitation, and only the supernatant rich in the hawthorn nutrient substances is reserved, so that the precipitates in the primary leaching liquor are reduced, the difficulty of subsequent filtration is reduced, and the mouthfeel of the hawthorn clear juice is effectively improved.

Preferably, the sugar dissolving tank comprises a tank body for containing mixed solution, the side wall of the tank body can be disassembled and connected with a conveying mechanism for conveying the mixed solution, the conveying mechanism comprises a conveying pipe which can be disassembled and connected with the tank body, the liquid inlet end of the conveying pipe can be disassembled and connected with the lower end of the side wall of the tank body and communicated with the inside of the tank body, the liquid outlet end of the conveying pipe can be disassembled and connected with a conveying pump, the conveying pipe is connected with a switch valve, the conveying pipe is internally disassembled and connected with a filtering mechanism, and the filtering mechanism filters the.

Through adopting above-mentioned technical scheme, the mixed solution in the delivery pump will be cylinder body carries to next process through the conveyer pipe, and the in-process that mixed solution carried in the conveyer pipe does not dissolve the crystal sugar and separates with mixed solution in filter equipment department to the crystal sugar that reduces to get into in the delivery pump reduces the damage to the delivery pump, extension delivery pump life.

Preferably, the conveyer pipe includes can dismantle the first body of being connected with the cylinder body, the ooff valve is connected on first body, first body is kept away from cylinder body one end and can be dismantled and be connected with the second body, the vertical setting of second body, second body lower extreme can be dismantled with first body and be connected, the second body is kept away from first body one end level and can be dismantled and be connected with the third body, the third body is kept away from that second body one end is vertical to be dismantled and is connected with the fourth body, fourth body upper end can be dismantled with the third body and be connected, fourth body lower extreme can be dismantled with the delivery pump inlet end and be connected, filtering mechanism can dismantle and connect in the second body.

Through adopting above-mentioned technical scheme, adopt between each part of conveyer pipe and between conveyer pipe and the delivery pump to dismantle the mode of being connected to the convenience is overhauld conveyer pipe and delivery pump.

Preferably, the filtering mechanism comprises a cylindrical filtering pipe coaxially arranged in the second pipe body, the outer diameter of the filtering pipe is smaller than the inner diameter of the second pipe body, a plurality of through holes are formed in the side wall of the filtering pipe, the filtering pipe is fixedly connected with a sealing plate for sealing one end of the filtering pipe towards one end of the third pipe body, and a connecting assembly for detachably connecting the filtering pipe in the second pipe body is arranged on the side wall of the filtering pipe.

Through adopting above-mentioned technical scheme, under the delivery pump effect, not dissolve the crystal sugar and arrive filter mechanism department along with mixed solution, the filter tube will be mixed solution and not dissolve the crystal sugar separation to reduce the crystal sugar that gets into in the delivery pump, reduce the damage to the delivery pump, extension delivery pump life.

Preferably, one end of the first pipe body, which is far away from the cylinder body, is obliquely arranged towards the direction far away from the ground.

Through adopting above-mentioned technical scheme, the crystal sugar that does not dissolve is kept somewhere in filter tube department by the filter tube, carries the back that stops, and the crystal sugar that does not dissolve under the action of gravity slides in the cylinder body through second body and first body to continue dissolving, improve crystal sugar recycle rate.

Preferably, the connecting assembly comprises a first connecting ring fixedly connected to the inner wall of the second pipe body, one end of the filter pipe, which is far away from the sealing plate, is coaxially and fixedly connected with a second connecting ring, and the second connecting ring is in threaded connection with the first connecting ring.

Through adopting above-mentioned technical scheme, twist and move the filter tube and can follow the second internal taking off of body, conveniently change the filter tube.

Preferably, threaded connection has the electrical heating stick that heats the mixed solution on the sealing plate, the electrical heating stick is coaxial to be set up in the filter tube, the electrical heating stick diameter is less than the filter tube internal diameter, the electrical heating stick passes through the electricity with the power and is connected.

Through adopting above-mentioned technical scheme, the rock candy adhesion that does not dissolve is behind the filter tube inner wall, and the electrical heating stick heats mixed solution to make the rock candy dissolve in mixed solution, reduce the rock candy that gets into the delivery pump, reduce the damage to the delivery pump, extension delivery pump life.

In summary, the present application has the following beneficial effects:

1. because the hawthorn juice is prepared from fresh hawthorn, pure water and monocrystal rock sugar, and other additives are not added, the prepared hawthorn juice is healthier for human bodies.

2. Preferably adopt bright hawthorn to leach among this application, reduce the pulp of scattering in the solution among the leaching process to make pulp and impurity in the mixed solution reduce, reduce the degree of difficulty of follow-up filtration process, greatly improved the taste moreover.

3. According to the method, the fresh hawthorn is soaked by using hot pure water and then extracted, so that the condition that pulp is scattered in a mixed solution due to steaming and cracking of hawthorn skin in the temperature rise process can be effectively reduced, the pulp precipitated in the hawthorn clear juice is reduced, and the taste is improved.

4. According to the method, the nutrient substances on the surfaces of the hawthorn subjected to primary leaching are flushed into the secondary leaching liquid through the rise and fall of circulation in the secondary leaching, so that the nutrient substances in the hawthorn clear juice are further increased.

5. According to the method, the filtration is carried out after blending and constant volume, and the colloidal substances generated in the process of dissolving sugar in the hawthorn are filtered, so that the mouthfeel of the hawthorn clear juice is improved.

6. The sugar dissolving cylinder in the method filters impurities in the single crystal sugar, simultaneously filters the impurities in the pulp, and heats and dissolves the incompletely dissolved single crystal sugar, thereby reducing the waste of raw materials.

Drawings

FIG. 1 is a schematic view of the entire structure of a sugar dissolving tank in example 10 of the present application;

FIG. 2 is a partial structural schematic view of an embodiment 10 of the present application, which is mainly used for showing a delivery pipe;

FIG. 3 is a schematic sectional view of a part of the structure of embodiment 10 of the present application, which is mainly used for illustrating the connection relationship between the second pipe and the filtering mechanism;

fig. 4 is a schematic sectional view of a part of the structure of the embodiment 10 of the application, which is mainly used for a filtering mechanism.

Description of reference numerals: 1. a cylinder body; 2. a conveying mechanism; 21. a delivery pipe; 211. a first pipe body; 212. an on-off valve; 213. a second tube body; 214. a third tube; 215. a fourth tube body; 22. a delivery pump; 3. a filtering mechanism; 31. a filter tube; 32. a through hole; 33. a sealing plate; 34. a heating assembly; 341. an electrical heating rod; 342. an electric wire; 35. a connecting assembly; 351. a first connecting ring; 352. a second connecting ring.

Detailed Description

In the examples, fresh fructus crataegi is purchased from Chengde city of Hebei province, and the average weight of fructus crataegi is 7.95 g.

Single crystal sugar was purchased from chenchen tai morally food products limited,

the pure water is prepared by the ion exchange resin desalination technology in the factory, and the physical and chemical indexes of the pure water are

1. Sensory: no odor, no visible to the naked eye; 2. pH: 5.00 to 7.50; 3. total hardness: alkalinity (calculated as CaCO3, mg/L) is less than or equal to 45; 4. free residual chlorine (mg/L) is less than or equal to 0.1; 5. the conductivity is less than or equal to 100 mu s/cm; 6. the turbidity is less than or equal to 1 NTU.

The present application will be described in further detail with reference to the following drawings and examples.

Examples

Example 1

S1, primary leaching: putting 200kg of fresh hawthorn into an extraction pot extraction cage, adding 300L of pure water into the extraction pot, wherein the temperature of the pure water is 85 ℃, heating the pure water to 90 ℃, and extracting for 50 min;

s2, filtration and transportation: obtaining a primary leaching solution after leaching, filtering the primary leaching solution in an extraction pot, pumping the filtered primary leaching solution into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s3, secondary leaching, filtering and conveying: adding 300L of pure water into the extraction pot after the conveying is finished, circularly lifting the extraction cage in the extraction pot, wherein the lifting is carried out once after one cage falls, and the lifting is carried out for 5 times, so as to obtain a secondary extract, filtering the secondary extract, pumping the filtered secondary extract into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s4, sugar dissolving: putting 100kg of single crystal rock sugar into a sugar dissolving cylinder while stirring the hawthorn leaching solution, wherein the stirring speed is 40r/min, and stirring for 15min to prepare a mixed solution;

s5, blending and fixing the volume: pumping the mixed solution into a blending cylinder for stirring at the stirring speed of 40r/min for 10 min;

s6, filtering again: filtering the mixed solution prepared in the step S5, wherein the filtering mesh number is 300 meshes;

s7, sterilization: and (4) carrying out ultra-high temperature sterilization on the mixed solution filtered by the S6 at the sterilization temperature of 115 ℃ for 10S to obtain the hawthorn clear juice.

Example 2

The difference from the embodiment 1 is that: pure water in S1 was heated to 95 ℃.

Example 3

S1, primary leaching: putting 200kg of fresh hawthorn into an extraction pot extraction cage, adding 300L of pure water into the extraction pot, wherein the temperature of the pure water is 85 ℃, heating the pure water to 95 ℃, and extracting for 60 min;

s2, centrifugal precipitation: centrifuging the primary leaching solution in three batches at equal amount, wherein the centrifugation speed is 5000r/min, the centrifugation time of each batch is 15min, discarding the precipitate, and pumping the supernatant to the filtration process;

filtering and conveying: obtaining a primary leaching solution after leaching, filtering the primary leaching solution in an extraction pot, pumping the filtered primary leaching solution into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the primary filtering is 100 meshes, and the mesh number of the secondary filtering is 300 meshes;

s3, secondary leaching, filtering and conveying: adding 300L of pure water into the extraction pot after the conveying is finished, circularly lifting the extraction cage in the extraction pot, wherein the lifting is carried out for 7 times, so as to obtain a secondary leaching solution, filtering the secondary leaching solution, pumping the filtered secondary leaching solution into a sugar dissolving tank, wherein the filtering in the process is secondary filtering, the mesh number of the first filtering is 100 meshes, and the mesh number of the second filtering is 300 meshes;

s4, sugar dissolving: putting 300kg of single crystal rock sugar into a sugar dissolving cylinder while stirring the hawthorn leaching solution, wherein the stirring speed is 40r/min, and stirring for 15min to prepare a mixed solution;

s5, blending and fixing the volume: pumping the mixed solution into a blending cylinder for stirring at the stirring speed of 40r/min for 10 min;

s6, filtering again: filtering the mixed solution prepared in the step S5, wherein the filtering mesh number is 300 meshes;

s7, sterilization: and (4) carrying out ultra-high temperature sterilization on the mixed solution filtered by the S6 at the sterilization temperature of 115 ℃ for 10S to obtain the hawthorn clear juice.

Example 4

The difference from the embodiment 1 is that: s1, adding 200kg of fresh hawthorn and 300L of pure water, heating the pure water to 95 ℃, and leaching for 60 min; s3, adding 300L of pure water, and circularly rising and falling for 7 times; and 300kg of single crystal rock sugar is added into S4.

Example 5

The difference from the example 4 lies in: s1, adding 300kg of fresh hawthorn and 350L of pure water; 350L of pure water is added into S3, and 200kg of single crystal rock candy is added into S4.

Example 6

The difference from the example 5 is that: and 5 times of cycle rise and fall in S3.

Example 7

The difference from the embodiment 1 is that: s1, adding 400kg of fresh hawthorn and 400L of pure water, and heating the pure water to 100 ℃; and S3, adding 400L of pure water, and circulating and rising and falling for 9 times.

Example 8

The difference from example 7 is that: and 300kg of single crystal rock sugar is added into S4.

Example 9

The difference from example 8 is that: and leaching for 70min in S1.

The mixture ratio and the step parameters of the embodiment 1-9 are as follows:

TABLE 1 examples 1-9 ratios and procedure parameters

Comparative example

Comparative example 1

The difference from the example 4 lies in: the pure water used in S1 was extracted at 25 ℃ for 60min by heating to 95 ℃.

Comparative example 2

The difference from comparative example 1 is that: pure water was heated to 60 ℃ in S1.

Comparative example 3

The difference from the example 4 lies in: and 3 times of cycle rise and fall in S3.

Comparative example 4

The difference from the example 4 lies in: and in S3, the cycle is lifted and fallen for 11 times.

Comparative example 5

The difference from the example 4 lies in: the leaching time in S1 was 90 min.

Comparative example 6

The difference from the example 4 lies in: there is no filtering operation in S2 and no filtering operation in S3.

Comparative example 7

The difference from comparative example 6 is that: there is no filtering operation in S6.

Performance test

Detecting soluble solid and amino nitrogen according to GB/T12143 and 2008 'general analysis method for beverage';

detecting total acid according to GB/T12456-;

the method for detecting the pulp content in the hawthorn clear juice comprises the following steps:

after shaking the hawthorn clear juice evenly, transferring two samples of 50mL each of which are taken from each group of hawthorn clear juice in parallel, and transferring the samples into a graduated centrifuge tube.

The graduated centrifuge tubes were placed in a centrifuge and centrifuged for 10min at a rotational frequency which produced a centrifugal acceleration of 400 g.

And recording the scale values corresponding to the highest part and the lowest part of the pulp slurry in the centrifugal tube.

The test data are shown in the table

TABLE 2 clear haw juice testing data sheet

By combining the embodiment 4 and the comparative example 6 and combining the table 2, it can be seen that the pulp contained in the hawthorn clear juice can be greatly reduced through the filtration after the primary extraction, the filtration after the secondary extraction and the filtration after the blending and the volume fixing, thereby improving the mouthfeel of the hawthorn clear juice.

As can be seen by combining examples 3 and 4 with Table 2, the pulp content of the hawthorn juice can be further reduced by centrifugation.

As can be seen by combining example 4 and comparative example 1 with Table 2, the clear hawthorn juice of comparative example 1 is significantly increased over that of example 4, probably because the peel of fresh hawthorn, which has not been soaked in advance with hot water, is damaged by cooking during the heating process of extraction, resulting in scattering of pulp in pure water.

As can be seen by combining example 4 and comparative example 3, and by combining table 2, the increased number of cycle lifts results in the fresh hawthorns colliding and squeezing during the lift, thereby causing the pulp to fall out, thereby resulting in an increased pulp content in the hawthorn juice.

As can be seen from the combination of example 4 and comparative example 4 and table 2, the skin of the fresh hawthorn is damaged due to too long extraction time, and the pulp in the fresh hawthorn is scattered in the pure water.

As can be seen by combining comparative example 5 and comparative example 6 with table 2, the content of the pulp in comparative example 6 is increased relative to the pulp in comparative example 5, because during the blending and volume fixing process, the jelly is generated by the hawthorn pulp and the single crystal sugar during the stirring process, and the jelly is removed by filtering again in S6, so that the mouthfeel of the hawthorn clear juice is improved.

Production data

6 sets of replicates were prepared according to the formulation and preparation method of example 3, and designated as first, second, third, fourth, fifth and sixth sets, respectively, and the final product volume (L) was measured and the average data for the six sets was calculated, as detailed in the table below.

TABLE 3 Final product volume Table

Calculated according to the average value, the total amount of the added fresh hawthorns is 200kg, the average weight of the fresh hawthorns is 0.00795kg, and the total amount of the fresh hawthorns is 25157. The prepared hawthorn juice was poured into a beverage can with a volume of 310mL, and a total of 1590 cans were filled. The final calculation is carried out, and the average hawthorn clear juice in each jar is extracted from 15.8 fresh hawthorn.

Example 10

Referring to fig. 1, a sugar dissolving tank comprises a tank body 1, wherein a conveying mechanism 2 is arranged on the side wall of the tank body 1, the conveying mechanism 2 is communicated with the interior of the tank body 1, and a filtering mechanism 3 for filtering mixed solution is arranged in the conveying mechanism 2.

When the mixed solution is conveyed to the next procedure through the conveying mechanism 2, the filtering mechanism 3 filters the mixed solution, so that undissolved crystal sugar in the mixed solution is filtered.

Referring to fig. 1, the conveying mechanism 2 comprises a conveying pipe 21 detachably connected to the lower end of the side wall of the cylinder body 1, the liquid inlet end of the conveying pipe 21 is communicated with the cylinder body 1, and the liquid outlet end of the conveying pipe 21 is detachably connected with a conveying pump 22.

Referring to fig. 1 and 2, the conveying pipe 21 includes a first pipe 211 connected to a side wall of the cylinder block 1 by a flange, a liquid inlet end of the first pipe 211 is communicated with the side wall of the cylinder block 1, a liquid outlet end of the first pipe 211 is inclined to a direction away from the ground, a switch valve 212 is connected to the first pipe 211, and the switch valve 212 is a ball valve. The liquid outlet end of the first pipe body 211 is connected with a second pipe body 213 in a flange mode, the axis of the second pipe body 213 is vertically arranged, and the lower end of the second pipe body 213 is connected with the liquid outlet end of the first pipe body 211 in a flange mode. The horizontal flange of second body 213 upper end has third body 214, and the vertical flange of the third body 214 one end of keeping away from second body 213 has fourth body 215, and fourth body 215 upper end and third body 214 flange joint, fourth body 215 lower extreme and delivery pump 22 inlet flange joint.

Referring to fig. 3, the filtering mechanism 3 includes a cylindrical filtering pipe 31 coaxially disposed in the second pipe 213, a plurality of through holes 32 for the mixed solution to pass through are formed in a sidewall of the filtering pipe 31, a sealing plate 33 is fixedly connected to one end of the filtering pipe 31 facing the third pipe 214, and one end of the filtering pipe 31 close to the third pipe 214 is sealed by the sealing plate 33. A heating unit 34 for heating the mixed solution is detachably connected to the sealing plate 33. The filter pipe 31 is detachably connected to the second pipe 213 through the connection assembly 35.

When the undissolved rock sugar is conveyed to the filter pipe 31 along with the mixed solution, the undissolved rock sugar is remained at the filter pipe 31 when the mixed solution flows out from the through hole 32. After the transportation is stopped, the undissolved rock sugar slides into the cylinder body 1 along the length direction of the second pipe body 213 and the length direction of the first pipe body 211 under the action of gravity to be continuously dissolved. The undissolved crystal sugar adhered to the inner wall of the filtering pipe 31 is dissolved in the mixed solution by heating.

Referring to fig. 3, the heating unit 34 includes an electric heating rod 341 screwed to the sealing plate 33, the electric heating rod 341 is coaxially disposed with the filter tube 31, the electric heating rod 341 has a diameter smaller than the inner diameter of the filter tube 31, the electric heating rod 341 is electrically connected to a power source through an electric wire 342, and the electric wire 342 is hermetically connected to the third tube 214.

Referring to fig. 4, a second connection ring 352 is coaxially and fixedly connected to an end of the sidewall of the filter tube 31 remote from the sealing plate 33, a first connection ring 351 is coaxially and fixedly connected to the inside of the second tube body 213, and the second connection ring 352 is threadedly connected to the inside of the first connection ring 351.

The implementation principle of the sugar dissolving tank used in the examples 1-9 and the comparative examples 1-6 of the application is as follows: when the mixed solution needs to be transferred to the next process, the on-off valve 212 is opened, and the mixed solution enters the next process through the first pipe 211, the second pipe 213, the third pipe 214, the fourth pipe 215 and the transfer pump 22 by the transfer pump 22.

When the undissolved rock candy reaches the filter pipe 31 along with the mixed solution, the mixed solution flows out from the through holes 32 on the filter pipe 31, and the undissolved rock candy is left at the filter pipe 31. When the undissolved rock candy is piled up at the filtering pipe 31 to block the through-hole 32, the electric heating rod 341 heats the mixed solution, thereby promoting the dissolution of the undissolved rock candy in the mixed solution.

The present embodiment is only for explaining the present application, and it is not limited to the present application, and those skilled in the art can make modifications of the present embodiment without inventive contribution as needed after reading the present specification, but all of them are protected by patent law within the scope of the claims of the present application.