CN201244452Y - Device for mixing mixed granule type material and liquid material - Google Patents
Device for mixing mixed granule type material and liquid material Download PDFInfo
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- CN201244452Y CN201244452Y CNU2008201300766U CN200820130076U CN201244452Y CN 201244452 Y CN201244452 Y CN 201244452Y CN U2008201300766 U CNU2008201300766 U CN U2008201300766U CN 200820130076 U CN200820130076 U CN 200820130076U CN 201244452 Y CN201244452 Y CN 201244452Y
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Abstract
The utility model provides a mixing device for mixing particle material and liquid material, comprising a container body. A feed pipe is arranged in the container body, and a liquid material accommodating room is formed in the container body and outside the pipe wall of the feed pipe; the container body is provided with a liquid material inlet which leads the liquid material into the liquid material accommodating room; the feed pipe is arranged to form a 0-45 degrees included angle with the vertical direction; the upper end opening of the feed pipe is a particle material inlet and the lower end opening of the feed pipe is in sealed contact with the bottom of the container body; the pipe wall of the feed pipe is provided with an opening hole for the liquid material to enter the feed pipe; the underside of the container body, which is corresponding to the lower end surface, of the feed pipe is provided with a mixture material outlet. By utilizing the device, the particle material and the liquid material can be mixed evenly on line.
Description
Technical field
The utility model is the mixing arrangement that is used for hybrid particles type material and liquid material about a kind of.
Background technology
In modernization industry is produced, often granulate material need be mixed with liquid material, for example, contain in the liquid beverage or liquid newborn process that the particle (as cereal-granules, fruit-vegetable granules etc.) of chewing mouthfeel can be provided in production, or in the process of producing pulp jelly, generally be with the granulate material of dosage be filled in the unit packaging again after liquid material mixes.Wherein, the degree of mixing of granulate material and liquid material will directly influence the uniformity of each unit packaging endoparticle content.
In the present production technology, the operation of hybrid particles type material and liquid material is normally carried out in a mixing arrangement such as material-compound tank (pill tank), as shown in Figure 1, the liquid material of particle to be added is placed a material-compound tank 2 that is provided with agitating device 1, add granulate material, open and stir, make the mixing of granulate material and liquid material, the mixed material outlet 3 that mixed material is provided with through the material-compound tank bottom is again drawn the material-compound tank conveying and is gone bulking system to be filled to (or can again after sterilization) in the unit packaging.Utilize above-mentioned mixing arrangement that granulate material and liquid material are mixed, under production status, agitating device 1 needs to open all the time, so that particle is distributed in the whole batching system by means of the effect of stirring, make every effort to evenness of discharge, thus the uniformity of granule content in guarantor unit's packaging product.Influence the factor of particle dispersing uniformity in the material system in material-compound tank, except the design of agitating devices 1 in the material-compound tank 2 and selecting for use, mainly also comprise the size of material-compound tank 2 and the characteristic of particle itself.In the actual production since product in granule content less than liquid material, and the dosage in large-scale production in the material-compound tank 2 generally can reach 10～30 tons, can there be the mixing non-uniform phenomenon by agitating device 1 hybrid particles, or need than long mixing time and bigger intensity, need to consider the influence of agitating device simultaneously to the particle integrity degree, and carrying out stirring state and also will become complicated along with discharging; In addition, because different particle rerum natura difference, even adopt identical mixing plant and technological parameter, the dispersion effect of particle in feed liquid also may be different, especially for some density variations bigger particle and liquid material, be difficult to realize that the suspension of particle in liquid material is to reach even mixing.In a word, above-mentioned mixing arrangement narrow application range, and be difficult to make granulate material and liquid material to reach even to mix, and influencing the granule content uniformity in the unit packaging product, the quality of production is not very stable.
Therefore, need a kind of new mixing arrangement of research and development, so that granulate material is more even with mixing of liquid material, thus the uniformity of assurance can unit packaging endoparticle content.
The utility model content
Main purpose of the present utility model is to provide a kind of mixing arrangement, so that granulate material is more even with mixing of liquid material, thereby is that the uniformity that realizes unit packaging endoparticle content is given security.
For reaching above-mentioned purpose, the utility model provides a kind of mixing arrangement that is used for hybrid particles type material and liquid material, and this mixing arrangement mainly comprises:
Vessel is provided with a feed pipe in this vessel, form the liquid material accommodation space in vessel, outside the feed pipe tube wall; Described vessel is provided with the liquid material import of liquid material being introduced described liquid material accommodation space; Described feed pipe and vertical direction are 0～45 ° of angle setting, the upper port of feed pipe is the granulate material import, the bottom surface sealing of lower port and vessel contacts, and the feed pipe tube wall is provided with liquid material in the feed flow attitude material accommodation space and enters perforate in the feed pipe; And the bottom surface of the pairing vessel in lower surface of feed pipe is provided with the mixed material outlet.
When utilizing mixing arrangement of the present utility model that granulate material and liquid material are mixed, after can making the liquid material of particle to be added enter the liquid material accommodation space of vessel from the liquid material import, the perforate that is provided with from described feed pipe tube wall enters in the feed pipe, and in feed pipe, realize mixing with the granulate material that enters from the feed pipe upper port, formation contains the mixed material of particle, realizes that the mixed material outlet that the mixed mixed material that this contains particle can be provided with from the bottom surface of the pairing vessel in lower surface of feed pipe drawn feed pipe.
Utilize mixing arrangement of the present utility model, can continuously, uniformly and stably add in the liquid material of continuous-flow in the formula for a product ratio granulate material, by this dynamic on-line mixing process, can reach the good homogeneous mixed effect, thereby the can uniformity that can be follow-up can step realization unit packaging endoparticle content is given security.
According to specific embodiments of the present utility model, described vessel can be structure of container such as basic groove, jar, cylinder, bucket and (can directly utilize in the production line as the compensating groove equipment before sterilization machine, the bottle placer, install described feed pipe additional, and form mixing arrangement of the present utility model).Vessel upper end can be openend, with as the liquid material import; Preferably described liquid material import is arranged on the bottom (comprising the bottom) of vessel in concrete the production.
Mixing arrangement of the present utility model also can comprise: the product pump of mixed material being drawn feed pipe, the mixed material outlet that is provided with on the bottom surface of this product pump and described vessel links to each other, contain the mixed material of particle in order to conveying, and the on-line mixing in feed pipe provides part power for particle and liquid material.Described product pump specifically can be displacement pump, is preferably screw pump or impeller pump, helps the integrality of protection particle when conveying contains the mixed material of particle.
According to preferred embodiment of the present utility model, described mixed material outlet is arranged on the center of vessel bottom surface, that is, the lower surface of described feed pipe is arranged on the centre of described vessel bottom surface basically and contacts with the bottom surface sealing of vessel.
According to preferred embodiment of the present utility model, described feed pipe and vertical direction are 0～15 ° of angle setting, most preferably are to be 0 ° of angle setting.
According to specific embodiments of the present utility model, the height and position in 20 centimetres below the liquid material minimum liquid level in vessel on the described feed pipe tube wall is provided with described perforate.Perforate on the described feed pipe tube wall can comprise one or more groups, preferably, every group of perforate is symmetrical arranged (perforate of same level height setting is called one group on the feed pipe tube wall, and symmetrically arranged every group of perforate comprises two above perforates) in the horizontal direction on the feed pipe tube wall.The perforate gross area on the described feed pipe tube wall is preferably 0.9～1.5 times of mixed material discharge area on the vessel bottom surface, more preferably 1～1.3 times, can make inlet amount and load in the feed pipe reach balance, liquid level and the intrinsic liquid level of feed pipe outer container in the feed pipe in the continuous mixed process are remained basically stable, the rarefied phenomenon of liquid material in the feed pipe can not appear, interior certain flow or the flow velocity of feed pipe be can guarantee simultaneously again, the continuous-flow of material in the feed pipe and evenly mixing guaranteed.
Mixing arrangement of the present utility model is suitable for mixing of various granulate materials and liquid material.Described granulate material can be pure solid-state particulate matter, as cereal-granules etc., and also can be for a large amount of solid granulates are suspended in material in small volume of solution or the colloidal sol, if flesh fruit sauce etc.; But described liquid material is the liquid phase of continuous-flow, and for example solution or emulsion can be suspended with certain granule (the granule particle diameter should be less than the tube wall of feed pipe described in the utility model perforate aperture, to avoid stop up).
During concrete enforcement, flow that the concrete diameter of described feed pipe can be taken away according to material in it and the granular size in institute's hybrid particles type material and specifically determine are to reach the good effect that makes granulate material and liquid feed liquid realization on-line mixing.For example, when production contained the liquid beverage of chewing particle or liquid breast or pulp jelly, the size of common required hybrid particles was 1～30mm, and feed tube diameter can be made as 40～200mm usually in the mixing arrangement of the present utility model, preferred 60～120mm; Can control simultaneously flow 〉=1 that mixed material taken away ton/hour from feed pipe, in large industrialized is produced, can control that the flow of mixed material is 1～10 ton/hour in the feed pipe, preferred 4～8 tons/hour, for granulate material with even mixing of liquid material provide power and guarantee.The thickness that is appreciated that tube wall does not exert an influence substantially to mixed effect, and diameter described in the utility model is an internal diameter; And the size of the liquid material accommodation space in the vessel, outside the feed pipe tube wall is also inessential to the mixed effect influence, can decide according to concrete dosage or flow; In addition, the granulate material import of feed pipe should be higher than the liquid material liquid level position, and the mixed material outlet should be greater than grain diameter.
In sum as can be seen, mixing arrangement of the present utility model has following beneficial effect: can make granulate material and liquid material realize on-line mixing according to required ratio in the space of feed pipe, owing to be dynamic mixed process, can reach the good homogeneous mixed effect, thereby give security for producing the unit packaging product endoparticle content uniformity that obtains; The mixture homogeneity of granulate material and liquid material is not influenced by combined amount size and vessel size, and the characteristic of granulate material itself is little, applied widely to the mixture homogeneity influence; Can avoid the influence of traditional mixing stirring device, reduce the fragmentation of mixed process particle to the particle integrity degree; And the utility model apparatus structure advantages of simple can adapt to the large-scale industrial production requirement.
Description of drawings
Fig. 1 is for showing the structural representation of traditional mixing arrangement that is used for hybrid particles type material and liquid material.
Fig. 2 is the schematic diagram of the basic structure that shows the mixing arrangement that is used for hybrid particles type material and liquid material of the present utility model.
Fig. 3 is for showing the schematic diagram of the production process of utilizing mixing arrangement hybrid particles type material of the present utility model and liquid material.
The specific embodiment
Below describe apparatus features of the present utility model in detail by specific embodiment, the beneficial effect that is intended to help the reader to understand technical spirit of the present utility model better and brought can not be interpreted as any qualification to the utility model practical range.
See also shown in Figure 2ly, mixing arrangement of the present utility model mainly comprises:
The mixing arrangement of present embodiment also comprises displacement pump (screw pump or impeller pump) 30 (seeing also shown in Figure 3), this displacement pump 30 links to each other with mixed material outlet 102, the mixed material that contains particle in order to conveying, it is drawn feed pipe 20 backs continuously to the defeated material of subsequent production pipeline, and the on-line mixing that also can be particle and liquid phase simultaneously provides power.
When utilizing the mixing arrangement hybrid particles type material of present embodiment and liquid material, please refer to shown in Figure 3, can utilize feed liquid delivery pump 40 that liquid material is drawn from storage tank 50, liquid material import 101 by mixing arrangement of the present utility model is transported in the vessel 10, and enter in the feed pipe 20 by the perforate 202 on feed pipe 20 walls, when arriving certain liquid level, start displacement pump (screw pump or impeller pump) 30, and utilize granulate material conveyer 60 that granulate material is quantitatively added to the feed pipe 20 from granulate material import 201, mix in feed pipe 20 with liquid material and form the mixed material that contains particle, the material of taking out along with displacement pump 30, the mixed material of feed pipe 20 inclusion granules is extracted out continuously, send into follow-up can step (or first sterilization can again), realize online even mixing of granulate material and liquid material.
In the actual production, well mix and adapt to the liquid level that changes within the specific limits in the vessel in producing for what guarantee particle and liquid material, can be provided with perforate 202 in following 20 centimetres at vessel minimum level height and position, the liquid level of feed liquid changes in 30 centimetres in the controlled container made body simultaneously.If liquid level is too high in the production process, granulate material may occurs and in feed pipe, can not in time be taken away; If liquid level is lower than the highest one group or several groups of perforates, the perforate that exceeds liquid level is ineffective, the interior feed liquid of feed pipe might take place taken away, and feed liquid can not in time add in the feed pipe in the vessel, causes the interior feed liquid of feed pipe to be evacuated.In addition, preferred control is immersed in following perforate 202 gross areas of feed liquid liquid level in the vessel and equals mixed material and export 0.9～1.5 times of 102 cross-sectional areas, more preferably 1～1.3 times, the inlet amount of feed pipe 20 and load can reach balance like this, make in the feed pipe 20 with vessel 10 in, the outer liquid level of feed pipe 20 remains basically stable in the course of the work, charging liquid in pipe vaccuum phenomenon can not occur.
Application example 1
Utilize the mixing arrangement of embodiment 1 to produce a kind of seasoning breast that contains the polished rice particle, the composition of raw materials of described seasoning breast following (in 1000kg):
| The batching title | Basic consumption (kg) |
| Fresh milk | 800 |
| White granulated sugar | 28 |
| Stabilizing agent | 3.2 |
| Malt extract | 7 |
| Composite nutrient | 0.15 |
| Essence | 1.1 |
| Cereal-granules (the polished rice particle of slaking) | 100 |
| The batching water | Surplus |
Please in conjunction with referring to shown in Figure 3, it is mainly as follows to utilize the mixing arrangement of embodiment 1 to produce the technology of the above-mentioned seasoning breast that contains the polished rice particle:
1, prepare the milk liquid base material of cereal-granules to be added: other batchings in will filling a prescription according to conventional seasoning breast production technology except that cereal-granules are configured to the liquid base material of suckling, and place storage tank 50 temporary;
2, mixing of milk liquid base material and cereal-granules:
Utilize pump 40 liquid base material of will suckling from storage tank 50, to pump in the vessel 10; In this production technology, can utilize sterilization machine compensating groove (be arranged on the sterilization leading portion, be mainly used in temporary and bascule), install a feed pipe 20 additional and form mixing arrangement of the present utility model as vessel 10 to the feed liquid of sterilization machine pipeline feed;
Utilize granulate material conveyer 60 that cereal-granules is added in the feed pipe 20 by formula ratio, and unlatching displacement pump 30, the material of taking out along with displacement pump 30, milk liquid base material in the vessel 10 enters in the feed pipe 20 by perforate 202, realizes mixing in feed pipe 20 with the milk liquid base material from the cereal-granules that feed pipe 20 upper port add;
In this example, described feed pipe 20 (immersing the subsurface part of feed liquid) internal diameter 80mm, totally 28 of perforates 202 on the tube wall, every group of 4 perforates, the same level height of every group of perforate on the charging tube wall is symmetrically distributed, the highest group of perforate is in vessel (compensating groove) about 5 centimeters below the minimum liquid level, and the about 5cm of the height distance of adjacent set perforate, perforate 202 gross areas on the charging tube wall equal the area that the vessel bottom surface contains the mixed material outlet 102 of particle substantially.In the production process, the flow that control milk liquid base material enters vessel 10 is 5.4 tons/hour substantially, and the speed that cereal-granules enters feed pipe 20 is 10kg/ minute substantially, and liquid level changes in 30mm in the control vessel;
3, sterilization can:
After realizing that in feed pipe 20 the mixed material that contains particle is extracted out feed pipe 20 continuously by displacement pump 30, be transported to sterilization machine continuously and carried out 137 ℃～139 ℃/4S sterilization, be cooled to subsequently≤25 ℃ of sterile fillings, obtain containing the seasoning milk product of cereal-granules.Wherein be to make the mixed material that contains particle, realize serialization production, can avoid the mixed sedimentation that contains material particle in process of caching of particle no longer through process of caching but be filled to continuously in the unit packaging.
Comparative Examples 1
Utilize traditional production method that contains the particle drink and mixing arrangement to produce a kind of seasoning breast that contains cereal-granules, with the Comparative Examples as above-mentioned application example 1, the composition of raw materials of the seasoning breast of this Comparative Examples is identical with example 1.Its technological process of production detailed process comprises:
1, identical among proportioning process and the embodiment 1 of milk liquid base material, the milk liquid base material that obtains preparing places a material-compound tank (5 tons of dosages);
2, mixing of milk liquid base material and cereal-granules: according to formula ratio the particle of handling well is added above-mentioned steps 1 and be equipped with in the material-compound tank of the liquid base material of suckling, be provided with agitating device in the material-compound tank, adopt mixing effect side alr mode preferably, mixing speed is 960 rev/mins, mixing time is uniformly dispersed in feed liquid to make particle as far as possible more than 20 minutes;
3, UHTS and can: operation is substantially with example 1, specifically: the mixed material that contains particle is carried out 137～139 ℃/4S sterilization with about 6 tons/hour flow volume delivery (agitating device of the material-compound tank of the ccontaining material that contains particle is opened in course of conveying) always to sterilization machine by displacement pump in the above-mentioned steps 2, be cooled to afterwards≤25 ℃ of sterile fillings, obtain the seasoning milk product that contains cereal-granules of this Comparative Examples.
Unit packaging endoparticle content detection
On the production line of application example 1, got a packaged products as sample every 5 minutes, on the production line of Comparative Examples 1, got a packaged products as sample (in the Comparative Examples 1 every about 1 minute, for granulate material and milk liquid base material are mixed, dosage is less, production time is short continuously), every production line got the 50 product samples of contracting for fixed output quotas, the granule content in the test sample unit packaging.
The granule content detection method: the per unit packaged products is crossed 50 order bolters successively, and draining weighs up the particle weight that is leached after 2 minutes, the granule content of product in the unit of account packing, outcome record is in following table:
| Sample number into spectrum | Application example 1 granule content (%) | Comparative Examples 1 granule content (%) |
| 1 | 8.9 | 30.4 |
| 2 | 9.6 | 26.0 |
| 3 | 8.8 | 23.0 |
| 4 | 9.0 | 21.0 |
| 5 | 10.5 | 20.8 |
| 6 | 10.1 | 19.7 |
| 7 | 11.1 | 18.2 |
| 8 | 10.2 | 17.7 |
| 9 | 9.9 | 17.0 |
| 10 | 9.7 | 16.3 |
| 11 | 9.6 | 15.5 |
| 12 | 10.5 | 15.5 |
| 13 | 10.6 | 14.7 |
| 14 | 11.2 | 14.2 |
| 15 | 10.8 | 13.1 |
| 16 | 10.7 | 13.8 |
| 17 | 8.9 | 12.6 |
| 18 | 8.5 | 12.5 |
| 19 | 8.9 | 12.3 |
| 20 | 10.0 | 11.8 |
| 21 | 9.4 | 11.5 |
| 22 | 10.6 | 10.6 |
| 23 | 9.6 | 9.4 |
| 24 | 10.8 | 9.3 |
| 25 | 10.7 | 9.2 |
| 26 | 9.7 | 8.9 |
| 27 | 10.3 | 8.5 |
| 28 | 11.3 | 8.2 |
| 29 | 8.7 | 7.8 |
| 30 | 9.9 | 7.3 |
| 31 | 10.5 | 6.6 |
| 32 | 11.6 | 6.5 |
| 33 | 11.8 | 5.8 |
| 34 | 10.5 | 5.7 |
| 35 | 10.2 | 5.6 |
| 36 | 9.6 | 5.2 |
| 37 | 11.1 | 4.7 |
| 38 | 8.7 | 4.3 |
| 39 | 8.9 | 3.1 |
| 40 | 10.6 | 3.2 |
| 41 | 10.0 | 3.0 |
| 42 | 9.7 | 2.3 |
| 43 | 10.4 | 2.1 |
| 44 | 9.5 | 1.5 |
| 45 | 10.4 | 1.2 |
| 46 | 11.0 | 0.9 |
| 47 | 10.9 | 0.5 |
| 48 | 9.8 | 0.2 |
| 49 | 9.2 | 0 |
| 50 | 10.3 | 0 |
From last table result as can be seen: adopt the conventional hybrid device that granulate material and liquid material are mixed the Comparative Examples 1, exist between particle and the feed liquid mix inhomogeneous, particle deviation average in the products obtained therefrom unit packaging can reach 204%, and there is the sample particle content more than 80% all to exceed mean value 20% scope up and down in institute's test sample product, unstable product quality, and detect the particle integrity degree and only have an appointment 70%; And adopt mixing arrangement of the present utility model that granulate material and liquid material are mixed, the bias ratio of particle deviation average maximum is 18% in the application example 1, the granule content data are all in this scope in other test sample, granule content is relatively stable in the product, and the particle integrity degree is more than 90%.
Claims (10)
1, a kind of mixing arrangement that is used for hybrid particles type material and liquid material is characterized in that, this mixing arrangement comprises:
Vessel is provided with a feed pipe in this vessel, form the liquid material accommodation space in vessel, outside the feed pipe tube wall; Described vessel is provided with the liquid material import of liquid material being introduced described liquid material accommodation space; Described feed pipe and vertical direction are 0～45 ° of angle setting, the upper port of feed pipe is the granulate material import, the bottom surface sealing of lower port and vessel contacts, and the feed pipe tube wall is provided with liquid material in the feed flow attitude material accommodation space and enters perforate in the feed pipe; And the bottom surface of the pairing vessel in lower surface of feed pipe is provided with the mixed material outlet.
2, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, described liquid material import is arranged on the bottom of vessel.
3, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, this mixing arrangement also comprises:
Mixed material is drawn the product pump of feed pipe, and the mixed material outlet that is provided with on the bottom surface of this product pump and described vessel links to each other.
4, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 3 is characterized in that, described product pump is screw pump or impeller pump.
5, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, described mixed material outlet is arranged on the center of vessel bottom surface.
6, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, described feed pipe and vertical direction are 0～15 ° of angle setting.
7, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, the height and position in 20 centimetres below the liquid material minimum liquid level in vessel on the described feed pipe tube wall is provided with described perforate.
8, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, the perforate on the described feed pipe tube wall comprises one or more groups, and the horizontal direction of every group of perforate on the feed pipe tube wall is symmetrical arranged.
9, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, the perforate gross area on the described feed pipe tube wall is 0.9～1.5 times of mixed material discharge area on the vessel bottom surface.
10, the mixing arrangement that is used for hybrid particles type material and liquid material according to claim 1 is characterized in that, the diameter of described feed pipe is 40～200 millimeters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201300766U CN201244452Y (en) | 2008-08-11 | 2008-08-11 | Device for mixing mixed granule type material and liquid material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201300766U CN201244452Y (en) | 2008-08-11 | 2008-08-11 | Device for mixing mixed granule type material and liquid material |
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| Publication Number | Publication Date |
|---|---|
| CN201244452Y true CN201244452Y (en) | 2009-05-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201300766U Expired - Lifetime CN201244452Y (en) | 2008-08-11 | 2008-08-11 | Device for mixing mixed granule type material and liquid material |
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| Country | Link |
|---|---|
| CN (1) | CN201244452Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105767182A (en) * | 2014-12-15 | 2016-07-20 | 基伊埃工程技术（中国）有限公司 | Continuous production process and devices of milk drink containing cereal grains |
| TWI656066B (en) * | 2018-03-01 | 2019-04-11 | 統一企業股份有限公司 | Filling device for preventing particles from being absorbed |
-
2008
- 2008-08-11 CN CNU2008201300766U patent/CN201244452Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105767182A (en) * | 2014-12-15 | 2016-07-20 | 基伊埃工程技术（中国）有限公司 | Continuous production process and devices of milk drink containing cereal grains |
| TWI656066B (en) * | 2018-03-01 | 2019-04-11 | 統一企業股份有限公司 | Filling device for preventing particles from being absorbed |
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| GR01 | Patent grant | ||
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| CX01 | Expiry of patent term |
Granted publication date: 20090527 |