CN103445260B - A kind of instant cream method of height of plant beverage - Google Patents
A kind of instant cream method of height of plant beverage Download PDFInfo
- Publication number
- CN103445260B CN103445260B CN201310383144.5A CN201310383144A CN103445260B CN 103445260 B CN103445260 B CN 103445260B CN 201310383144 A CN201310383144 A CN 201310383144A CN 103445260 B CN103445260 B CN 103445260B
- Authority
- CN
- China
- Prior art keywords
- ointment
- hot water
- dissolving tank
- temperature
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Medicines Containing Plant Substances (AREA)
- Cosmetics (AREA)
Abstract
<b> the invention discloses a kind of instant cream method of height of plant beverage, and it comprises the following steps: 1) add hot water and ointment: first in the dissolving tank of high efficient mixer, inject hot water; After the ointment inlet being positioned at bottom dissolving tank when hot water is dipped, start membrane pump, extract the ointment in extract container by membrane pump, make ointment enter into dissolving tank bottom dissolving tank; After having extracted ointment, controlled the addition of hot water by mass flowmenter; 2) start high efficient mixer, carry out shear agitation in the bottom of dissolving tank; Be incubated while stirring; 3) after insulating process completes, successively concoction extracted, filter, cool and store.The present invention accurately can control the mass values of ointment and the hot water added, and guarantees that ointment fully dissolves, reduces ointment loss; Flavor taste and the quality of product can be ensured in the course of dissolution of ointment simultaneously.</b>
Description
Technical field
The present invention relates to a kind of raw material dissolving method of plant beverage, especially relate to a kind of instant cream method of height of plant beverage.Belong to technical field of food beverage.
Background technology
Plant beverage is the third generation drink after soda, beverage made of fruits or vegetables, compares common beverages, because it innately has the quality of " natural, green, nutrition, health ", meets beverage market trend and trend, liking more and more by consumer.At present, in the preparation technology of traditional plant beverage, mostly adopt the raw material (ointment) of method manually to plant beverage quantitatively to dissolve, particular by weighing appropriate medicinal extract manually, then, on a molten cream platform, manually ointment is poured into dissolving tank from top and dissolve.There is following shortcoming in the dissolving method of this ointment: 1, adopts manual cream of throwing to operate, accurately cannot control the mass values of ointment amount and the hot water added, cannot guarantee that ointment fully dissolves, make ointment loss large.2, mounting platform, easily operate miss is needed.3, owing to being pour in dissolving tank on the top of tank, operation is loaded down with trivial details, greatly reduces production efficiency.4, because the delivery of ointment is carried out in atmosphere, and cannot precise control of temperature, flavor taste and the quality of product can not be ensured.5, owing to being manual operation, also exist energy consumption large compared with the working strength of high, personnel, expend time in longer, poor stability, steady some property are poor, the shortcoming that is unfavorable for consecutive production in enormous quantities.
Summary of the invention
For the deficiencies in the prior art, object of the present invention aims to provide a kind of instant cream method of height of plant beverage, and it accurately can control the mass values of ointment amount and the hot water added, and guarantees that ointment fully dissolves, reduces ointment loss; Flavor taste and the quality of product can be ensured simultaneously in the course of dissolution of ointment, have that production efficiency is high, energy consumption is lower, the working strength of personnel effect, expend time in short, security good, steady some property is good and can realize the feature of consecutive production in enormous quantities.
For achieving the above object, the present invention adopts following technical scheme:
The instant cream method of height of plant beverage, is characterized in that comprising the following steps:
1) add hot water and ointment: first in the dissolving tank of high efficient mixer, inject hot water, and pass through the flow of mass flow meter measurement hot water, wherein, hot water temperature is 80 ∽ 90 DEG C; After the ointment inlet being positioned at bottom dissolving tank when hot water is dipped, start membrane pump, extract the ointment in extract container by membrane pump, make ointment enter into dissolving tank from the ointment inlet bottom dissolving tank; After having extracted ointment, controlled the addition of hot water by mass flowmenter, when the mass ratio between hot water and ointment is greater than 19 times, stop injecting hot water;
2) start high efficient mixer, carry out shear agitation in the bottom of dissolving tank, control mixing speed at 600 ∽ 1100r/min; Be incubated while stirring, temperature retention time is 8 ∽ 30 minutes, and holding temperature is 80 ∽ 95 DEG C;
3) after insulating process completes, successively concoction extracted, filter, cool and store.
Realize object of the present invention to reach by taking following technical scheme:
Realizing one embodiment of the present invention is: in step 1), after having extracted ointment, injects hot water and clean in extract container, and by membrane pump, the solution of mixing is injected into dissolving tank, and hot water temperature is 30 ∽ 60 DEG C.The object of rinsing guarantees accurately to add ointment, ensures that local flavor is normal.
Realizing one embodiment of the present invention is: at completing steps 3) operation after, again the operation of water liftout is carried out to pipeline: namely according to the water yield that the volume settings of pipeline is enough, and measured by mass flowmenter, the water yield of setting is injected in dissolving tank, extracted by centrifugal pump again, until the water in dissolving tank is all transported in holding vessel; Finally carry out quantitative work by formula again, the water of setting formula ratio is in dissolving tank, and be all drawn in holding vessel by the water in dissolving tank by centrifugal pump equally, be finally uniformly mixed in holding vessel, mixing time is 5 ∽ 10 minutes.
The object done like this is that guarantee consistent with formula consumption, the operation of water liftout is in order to more thorough recycling pipeline residual quantity in order to ensure the final percentage of ointment amount and water in 7 ∽ 50% scopes.
Realizing one embodiment of the present invention is: in step 3), by frequency conversion centrifugal pump, concoction is extracted, filter again through closed filters, and then carries out cooling, making temperature drop to less than 30 DEG C through plate heat exchanger, finally stores in double-layer heat insulation storage barrel; Wherein, the aperture of the stainless steel filtering net of filter is 100 ∽ 300 orders.
Extraction process traditional Chinese medicinal ointment is filtered through 100-300 order stainless steel filtering nets, ensure that final products clear, then makes ointment by High-temperature cooling to lower than 30 DEG C by heat exchange, ensure that ointment stored under refrigeration, reach preservation.
Realizing one embodiment of the present invention is: in step 1), and the interpolation weight of described ointment is 10 ∽ 100kg.
Realizing one embodiment of the present invention is: in step 1), by the temperature of temperature controller monitoring hot water, controls the fluctuation range of temperature at ± 2 DEG C.
Beneficial effect of the present invention is:
1, hot water addition of the present invention is controlled by the mass flowmenter of checking, very accurate, hot water temperature is between 80 ∽ 90 DEG C, the mass values > 19 times between hot water and ointment can be guaranteed, guarantee that ointment fully dissolves, ointment local flavor is effectively reduced, make product special flavour better; The mass flowmenter quality maximal accuracy used is 0.2%, safely, effectively, stablizes.
2, the present invention adopts membrane pump to carry out taking out cream, replaces tradition allotment and manually throws cream operation, improve the operating efficiency of operating personnel, reduce the manual labor of operating personnel.Meanwhile, because ointment enters into dissolving tank from the ointment inlet bottom dissolving tank, minimizing ointment contacts further with air and causes oxidation, guarantees ointment local flavor.Extract ointment, added quantitative hot water and carry out clean container, guaranteed accurately to add ointment, ensured that local flavor is normal.
3, the present invention also carries out the operation of water liftout to pipeline, more thoroughly recycles pipeline residual quantity, guarantees that the final percentage of ointment amount and water is in 7 ∽ 50% scopes, guarantees consistent with formula consumption.
4, high efficient mixer of the present invention has good heat preservation sandwich layer, can ensure that the reducing amount of temperature reaches minimum, by the scope control of cooling in 1 ∽ 3 DEG C, can ensure product special flavour mouthfeel and quality in 1 hour.
5, ointment amount of the present invention add accurately, transfer fully, can be fresh-keeping in spool, product special flavour mouthfeel and quality can be ensured, have that production efficiency is high, energy consumption is lower, the working strength of personnel effect, expend time in short advantage; The present invention can also adopt human-computer interface control panel to provide data about production routine, and the convenience that ensure that safety and produce, can realize consecutive production in enormous quantities.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Detailed description of the invention
Specific embodiment 1:
Below, the present invention is described further:
The instant cream method of height of plant beverage, it comprises the following steps:
1) hot water and ointment is added:
1-1) first in the dissolving tank of high efficient mixer, inject hot water, and pass through the flow of mass flow meter measurement hot water, wherein, hot water temperature is 85 DEG C; After the ointment inlet being positioned at bottom dissolving tank when hot water is dipped, start membrane pump, extract the ointment in extract container by membrane pump, make ointment enter into dissolving tank from the ointment inlet bottom dissolving tank; After having extracted ointment, controlled the addition of hot water by mass flowmenter, when the mass ratio between hot water and ointment is greater than 19 times, stop injecting hot water; The interpolation weight of described ointment is 50kg, and the addition of hot water is 951kg;
1-2) after having extracted ointment, inject hot water and clean in extract container, and by membrane pump, the solution of mixing is injected into dissolving tank, hot water temperature is 50 DEG C.The object of rinsing guarantees accurately to add ointment, ensures that local flavor is normal.
By temperature controller monitoring step 1-1) and step 1-2) in the temperature of hot water, the fluctuation range of temperature is controlled at ± 2 DEG C.
2) start high efficient mixer, carry out shear agitation in the bottom of dissolving tank, control mixing speed at 1000r/min; Be incubated while stirring, temperature retention time is 20 minutes, and holding temperature is 85 DEG C;
3) after insulating process completes, by frequency conversion centrifugal pump, concoction is extracted, then filter through the filter of closed, then carry out cooling, making temperature drop to less than 30 DEG C through plate heat exchanger, finally store in double-layer heat insulation storage barrel; Wherein, the aperture of the stainless steel filtering net of filter is 200 orders.
Specific embodiment 2:
The feature of the present embodiment is: at completing steps 3) operation after, again the operation of water liftout is carried out to pipeline: namely according to the water yield that the volume settings of pipeline is enough, and measured by mass flowmenter, precision reaches +/-0.2 and is injected in dissolving tank by the water yield of setting, extracted by centrifugal pump again, until the water in dissolving tank is all transported in holding vessel; Finally carry out quantitative work by formula again, the water of setting formula ratio is in dissolving tank, and be all drawn in holding vessel by the water in dissolving tank by centrifugal pump equally, be finally uniformly mixed in holding vessel, mixing time is 8 minutes.Other are identical with specific embodiment 1.
Water liftout operation refer to: when concoction by Pipeline transport to holding vessel time, concoction can fill to pipeline the water that instead of in pipeline, need to add again water to enter tank inherence and extract, the concoction in pipeline is replaced to water, the concoction in final pipeline is recovered in holding vessel.
Specific embodiment 3:
The feature of the present embodiment is: in step 1-1) in, the interpolation weight of described ointment is 10kg, and the addition of hot water is 1000kg.Other are identical with specific embodiment 1 or 2.
Specific embodiment 4:
The feature of the present embodiment is: in step 1-1) in, the interpolation weight of described ointment is 100kg, and the addition of hot water is 3000kg.Other are identical with specific embodiment 1 or 2.
Specific embodiment 5:
The feature of the present embodiment is:
In step 1-1) in, the temperature of described hot water is 80 DEG C; In step 1-2) in, the temperature of described hot water is 30 DEG C, and other are identical with specific embodiment 1 or 2.
Specific embodiment 6:
In step 1-1) in, the temperature of described hot water is 95 DEG C; In step 1-2) in, the temperature of described hot water is 60 DEG C, and other are identical with specific embodiment 1 or 2.
Specific embodiment 7:
The feature of the present embodiment is: in step 2) in, control mixing speed at 600r/min; Be incubated while stirring, temperature retention time is 8 minutes, and holding temperature is 80 DEG C; In step 3), the aperture of the stainless steel filtering net of filter is 100 orders.Other are identical with specific embodiment 1 or 2.
Specific embodiment 8:
The feature of the present embodiment is: in step 2) in, control mixing speed at 1100r/min; Be incubated while stirring, temperature retention time is 8 minutes, and holding temperature is 95 DEG C; In step 3), the aperture of the stainless steel filtering net of filter is 300 orders.Other are identical with specific embodiment 1 or 2.
With reference to Fig. 1: Hi-mixer 1 (or being homogenizer) of the present invention comprises dissolving tank 11, and the stator circulator 12 for stirring material be arranged on bottom dissolving tank, stator circulator 12 is by motor 13 driven rotary, described motor is also connected with a frequency converter 14, is controlled the rotating speed of stator circulator 12 by frequency converter 14.Dissolving tank 11 is also provided with liquid level sensor 15.Stator circulator 12 forms eddy current in constantly rotating, and eddy current particularly can both reach extremely strong effect of rinsing dissolving in bottom to each position of dissolving tank, and air seldom can be mixed in feed liquid.The air capacity that is mixed into adopting stator circulator to stir is 30 (Index), and the air capacity that is mixed into adopting paddle wheel agitator is 100 (Index); Meanwhile, barrier film mixed dissolution technology, can greatly reduce the bubble produced in draw dissolved process.Solve in the process of mixed dissolution therefore, it is possible to perfect, air be mixed into, lump, the problem such as deposition.
The bottom of described dissolving tank 11 is provided with ointment inlet, and ointment inlet is connected with membrane pump 3 (also can be barrier film draw-off pump) by the ointment conveyance conduit 2 with butterfly valve 10, and the liquid feeding end of membrane pump 3 is connected with extract container 5 by liquid suction pipe 4.
Described dissolving tank 11 is also provided with hot water inlet, and hot water inlet is connected with delivery pipeline 6, is provided with butterfly valve 10 and mass flowmenter 7 at delivery pipeline 6.An input of delivery pipeline 6 is connected with extract container 5 by a butterfly valve 10.
Described dissolving tank 11 is also connected with pipe blow-through 8, and pipe blow-through 8 is provided with butterfly valve 10, and pipe blow-through 8 is connected with cleaning fluid storage device by material-pumping tube cover 9.
With reference to table 1, the present invention utilizes membrane pump to extract medicinal extract, verifies that it extracts effect.Method is as the criterion the material liquid of the amount of preparing enough: medicinal extract liquid, counter-infiltration (RO) water, normally produces according to formula.By membrane pump, medicinal extract is extracted, extract completely once, finally observe the effect of extraction.
Table 1 membrane pump extracts the Contrast on effect table fed intake with tradition
| Project | Tradition feeds intake | Barrier film extracts | Effect comparison |
| Charging time (min) | 15 | 7 | Save 8min |
| Medicinal extract waste (g) | 3 | Nothing | Save 3g |
| Foam generation | On a small quantity | Denier | Non-foam |
Can obtain from above, in the medicinal extract interpolation time, traditional charging time is 15 minutes, and barrier film draw-off pump is 7 minutes, can save and take out cream time 8min, and charging time can save about 53%; Medicinal extract is in the process of transfer, and tradition is thrown the secondary loss of cream 1 and is about 3g medicinal extract, and barrier film extraction there is no loss medicinal extract; On the generation of foam, tradition feeds intake and has the generation of a small amount of foam, and barrier film extracts can not produce foam substantially.
Research proves, the utilization of barrier film extraction technique greatly can reduce the time extracting medicinal extract, and production efficiency can improve 53%.In addition, by barrier film draw-off pump, raw medicinal material medicinal extract is carried out mixed dissolution from the lower side bit extraction of tank to dissolving tank, the loss that medicinal extract occurs in input process can be efficiently avoid, and foamless generation substantially.
For a person skilled in the art, according to technical scheme described above and design, other various corresponding change and distortion can be made, and all these change and distortion all should belong within the protection domain of the claims in the present invention.
Claims (4)
1.
the instant cream method of height of plant beverage, is characterized in that comprising the following steps:
1) add hot water and ointment: first in the dissolving tank of high efficient mixer, inject hot water, and pass through the flow of mass flow meter measurement hot water, wherein, hot water temperature is 80 ∽ 90 DEG C; After the ointment inlet being positioned at bottom dissolving tank when hot water is dipped, start membrane pump, extract the ointment in extract container by membrane pump, make ointment enter into dissolving tank from the ointment inlet bottom dissolving tank; After having extracted ointment, controlled the addition of hot water by mass flowmenter, when the mass ratio between hot water and ointment is greater than 19 times, stop injecting hot water; In step 1), after having extracted ointment, injected hot water and clean in extract container, and by membrane pump, the solution of mixing has been injected into dissolving tank, hot water temperature is 30 ∽ 60 DEG C;
2) start high efficient mixer, carry out shear agitation in the bottom of dissolving tank, control mixing speed at 600 ∽ 1100r/min; Be incubated while stirring, temperature retention time is 8 ∽ 30 minutes, and holding temperature is 80 ∽ 95 DEG C;
3) after insulating process completes, successively concoction extracted, filter, cool and store; By frequency conversion centrifugal pump, concoction is extracted, then filter through the filter of closed, then carry out cooling, making temperature drop to less than 30 DEG C through plate heat exchanger, finally store in double-layer heat insulation storage barrel; Wherein, the aperture of the stainless steel filtering net of filter is 100 ∽ 300 orders.
2.
the instant cream method of height of a kind of plant beverage as claimed in claim 1, it is characterized in that: at completing steps 3) operation after, again the operation of water liftout is carried out to pipeline: namely according to the water yield that the volume settings of pipeline is enough, and measured by mass flowmenter, the water yield of setting is injected in dissolving tank, extracted by centrifugal pump again, until the water in dissolving tank is all transported in holding vessel; Finally carry out quantitative work by formula again, the water of setting formula ratio is in dissolving tank, and be all drawn in holding vessel by the water in dissolving tank by centrifugal pump equally, be finally uniformly mixed in holding vessel, mixing time is 5 ∽ 10 minutes.
3.
the instant cream method of height of a kind of plant beverage as claimed in claim 1, is characterized in that: in step 1), and the interpolation weight of described ointment is 10 ∽ 100kg.
4.
the instant cream method of height of a kind of plant beverage as claimed in claim 1, is characterized in that: in step 1), by the temperature of temperature controller monitoring hot water, controls the fluctuation range of temperature at ± 2 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310383144.5A CN103445260B (en) | 2012-08-29 | 2013-08-28 | A kind of instant cream method of height of plant beverage |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210311899XA CN102823911A (en) | 2012-08-29 | 2012-08-29 | High speed ointment dissolving method for vegetable drink |
| CN201210311899.X | 2012-08-29 | ||
| CN201310383144.5A CN103445260B (en) | 2012-08-29 | 2013-08-28 | A kind of instant cream method of height of plant beverage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103445260A CN103445260A (en) | 2013-12-18 |
| CN103445260B true CN103445260B (en) | 2015-10-28 |
Family
ID=47327381
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210311899XA Pending CN102823911A (en) | 2012-08-29 | 2012-08-29 | High speed ointment dissolving method for vegetable drink |
| CN201310383144.5A Active CN103445260B (en) | 2012-08-29 | 2013-08-28 | A kind of instant cream method of height of plant beverage |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210311899XA Pending CN102823911A (en) | 2012-08-29 | 2012-08-29 | High speed ointment dissolving method for vegetable drink |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN102823911A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190275A (en) * | 2014-08-08 | 2014-12-10 | 上海紫泉饮料工业有限公司 | Sugar dissolving method in beverage preparation |
| CN105935091A (en) * | 2015-08-26 | 2016-09-14 | 张志德 | Liquid self-flowing device system capable of blending and converting different proportions |
| CN112890050A (en) * | 2021-01-13 | 2021-06-04 | 统一企业(中国)投资有限公司 | Full-automatic dissolving system applied to beverage production line and processing method thereof |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1125887A2 (en) * | 2000-02-16 | 2001-08-22 | GBG- Ali S.p.A. | Syrup measuring device for machines for the extemporary preparation of drinks |
| JP2001328699A (en) * | 2000-05-23 | 2001-11-27 | Sanyo Electric Co Ltd | Beverage supplying equipment |
| CN1582990A (en) * | 2004-06-08 | 2005-02-23 | 千南成 | Beverage with Chinese medicines for relieving alcoholism |
| CN201427025Y (en) * | 2009-04-01 | 2010-03-24 | 湖北五瑞生物工程有限公司 | Dissolving tank |
| CN201735368U (en) * | 2010-06-24 | 2011-02-09 | 成都泓奇实业股份有限公司 | Continuous on-line automatic material mixing device |
| CN202172801U (en) * | 2011-06-24 | 2012-03-28 | 徐春根 | Grapefruit juice production line |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85102945A (en) * | 1985-04-16 | 1986-10-15 | 徐庭中 | Lime paste solubilized apparatus by self-energizing |
| CN1037741C (en) * | 1991-05-13 | 1998-03-18 | 海南省地方国营海口罐头厂 | Production method of natural pure coconut-apricot juice |
| US20020122866A1 (en) * | 2001-03-01 | 2002-09-05 | Sevugan Palaniappan | Process apparatus, and composition for calcium fortification of beverages |
| CN100435643C (en) * | 2006-06-30 | 2008-11-26 | 内蒙古蒙牛乳业（集团）股份有限公司 | Method for preparing milk beverage |
| CN102524469A (en) * | 2010-12-16 | 2012-07-04 | 苏州工业园区尚融科技有限公司 | Method for preparing sugar-free cold tea drink |
| CN202368800U (en) * | 2011-12-26 | 2012-08-08 | 江门市生和堂食品有限公司 | High efficiency liquid health food filling equipment |
-
2012
- 2012-08-29 CN CN201210311899XA patent/CN102823911A/en active Pending
-
2013
- 2013-08-28 CN CN201310383144.5A patent/CN103445260B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1125887A2 (en) * | 2000-02-16 | 2001-08-22 | GBG- Ali S.p.A. | Syrup measuring device for machines for the extemporary preparation of drinks |
| JP2001328699A (en) * | 2000-05-23 | 2001-11-27 | Sanyo Electric Co Ltd | Beverage supplying equipment |
| CN1582990A (en) * | 2004-06-08 | 2005-02-23 | 千南成 | Beverage with Chinese medicines for relieving alcoholism |
| CN201427025Y (en) * | 2009-04-01 | 2010-03-24 | 湖北五瑞生物工程有限公司 | Dissolving tank |
| CN201735368U (en) * | 2010-06-24 | 2011-02-09 | 成都泓奇实业股份有限公司 | Continuous on-line automatic material mixing device |
| CN202172801U (en) * | 2011-06-24 | 2012-03-28 | 徐春根 | Grapefruit juice production line |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103445260A (en) | 2013-12-18 |
| CN102823911A (en) | 2012-12-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103445260B (en) | A kind of instant cream method of height of plant beverage | |
| CN102388960B (en) | Quick-refrigerating type milk-storing cool storage tank | |
| CN102671556B (en) | Full automatic continuous sugar dissolving system and preparation method thereof | |
| CN203676041U (en) | Spice decoction device for stewing machine | |
| CN202191848U (en) | Equipment for rapidly dissolving sugar | |
| CN106190678B (en) | Intelligent beer machine capable of circularly discharging sugar | |
| CN202822849U (en) | Semi-automatic constant-temperature percolate extraction integrated system | |
| CN204275560U (en) | A kind of tea juice freezing concentrating device | |
| CN204412108U (en) | A kind of for preserved beancurd juice produce dissolve equipment | |
| CN205409517U (en) | Fermenting installation is pickled to hot pepper | |
| CN206333829U (en) | A kind of home-use portable rice noodle roll producing device | |
| CN211612572U (en) | Energy-concerving and environment-protective safe agitator | |
| CN208228878U (en) | It is a kind of for lifting the preparation facilities of rice soda hair cream | |
| CN110179333B (en) | Automatic change aquatic products boiling device | |
| CN206396166U (en) | Combined type Craft Beer factory | |
| CN109224930A (en) | A kind of fire foam process units | |
| CN207933406U (en) | A kind of fully-automatic production system of refined cooking wine | |
| CN207828236U (en) | A kind of sweet wine installation for fermenting convenient for temperature control | |
| CN207929098U (en) | A kind of processing unit (plant) for coating stirring | |
| CN202262372U (en) | Fast refrigeration type milk storage cold storage tank | |
| CN213266440U (en) | Freezing jar of preparation buckwheat flavor type base liquor | |
| CN206901041U (en) | Soya-bean milk holding vessel | |
| CN105418414A (en) | Production method for glycerol monostearate and glycerol distearate | |
| CN220845493U (en) | Full-automatic batching system | |
| CN204816267U (en) | A mixed heat preservation device of material for cake production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |