CN209711374U - A kind of Walnut protein powder preparation system - Google Patents
A kind of Walnut protein powder preparation system Download PDFInfo
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- CN209711374U CN209711374U CN201920133597.5U CN201920133597U CN209711374U CN 209711374 U CN209711374 U CN 209711374U CN 201920133597 U CN201920133597 U CN 201920133597U CN 209711374 U CN209711374 U CN 209711374U
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Abstract
The utility model relates to a kind of Walnut protein powder preparation systems, belong to Machine Design manufacturing technology field.The system includes extractor, serum pot, decanter centrifuge, neutralizing tank, inspissator, homogenizer and spray dryer, and extractor includes tank body, colloid mill and circulating line；Top of the tank is equipped with feed well and lye pond；It is equipped with the first valve between feed well and tank body, the second valve is equipped between feed well and lye pond；Tank body discharge port is connected by pipeline with the feed inlet of colloid mill；The discharge port of colloid mill is connected with discharge nozzle, circulating line respectively, and is equipped with triple valve in junction；The other end of discharge nozzle is connected with the top of tank body；This system apparatus structure is simple, simplifies protein extracting process, reduces equipment investment, solves the problems such as protein extraction rate is low in traditional walnut cake protein extracting process.The utility model can improve the attached value of walnut grouts, it is made to turn waste into wealth, and implementing process is easy and economical, be suitble to scale industrial production.
Description
Technical field
The utility model belongs to Machine Design manufacturing technology field, and in particular to a kind of extraction production system, in particular to
A kind of Walnut protein powder preparation system.
Background technique
China's walnut cultivated area and yield rank first in the world, as walnut planting scale and its yield expand year by year,
Domestic walnut oil expression manufacturer is more and more, generates a large amount of squeezing grouts therewith.Currently, walnut grouts are often by as feeding
Material and fertilizer or discarding, attached value are lower.Protein content is up to 45% in walnut grouts, is a kind of good protein resource.
In walnut grouts powder in terms of extracting protein matter, the extraction equipment being commonly used is big multi-form fairly simple,
In process of production, alkali soluble extractor, acid heavy tank, water washing tank, neutralizing tank etc. are configured, is related to various function tank bodies, increases enterprise
Factory area and cost of investment.Still further aspect, in process of production, there is also series of technical, such as walnut dregs
Powder is swum in above solution when entering extractor, is dissolved slower.And walnut grouts powder is in aqueous slkali, due to its grouts powder
Grain is larger, along with cell wall etc. strongly limits the dissolution of protein.Albumen extraction is generally improved using enzymatic shell-broken at present
Rate is taken, production cost is higher.The Walnut protein powder instant capacity of conventional method preparation is bad.It is therefore desirable to be subject to the prior art
It improves.
Utility model content
To solve the prior art, there are drawbacks described above, provide a kind of Walnut protein powder preparation system, this system device knot
Structure design rationally, realizes protein Fast Stripping in walnut grouts, especially dissolves out protein simultaneously in defibrination, have efficiently extraction
Take performance.
To achieve the above object, the technical solution adopted in the utility model is as follows:
A kind of Walnut protein powder preparation system, including extractor, serum pot, decanter centrifuge, neutralizing tank, inspissator,
Matter machine and spray dryer, the extractor include tank body, colloid mill and circulating line；Top of the tank is equipped with feed well and alkali
Liquid pool；
It is equipped with the first valve between feed well and tank body, the second valve is equipped between feed well and lye pond；
Tank body discharge port is connected by pipeline with the feed inlet of colloid mill；
The discharge port of colloid mill is connected with discharge nozzle, circulating line respectively, and is equipped with triple valve in junction；Discharge nozzle
The other end is connected with the top of tank body；
The outlet end of discharge nozzle is set to the surface of serum pot, and the discharge port of serum pot passes through with slurries tank valve, pump
Pipeline be connected with the feed inlet of decanter centrifuge side；The bottom of decanter centrifuge is equipped with solid phase outlet；Decanter centrifuge
The liquid outlet of the other side is connected with the top of neutralizing tank by pipeline, the bottom discharge port of neutralizing tank and the charging at the top of inspissator
Mouth is connected by pipeline；The discharge port of thickener underflow is connected with the feed inlet of homogenizer by pipeline；The discharge port of homogenizer
It is connected with the feed inlet of spray dryer by pipeline.
It is further preferred that colloid mill is set to the lower section of tank body.
It is further preferred that can outer surface is enclosed with hollow insulation layer.
It is further preferred that bottom is equipped with temp probe in tank body, and it is connected by conducting wire with display.
It is further preferred that bottom is popped one's head in equipped with pH measurement in tank body, and it is connected by conducting wire with display.
It is further preferred that being connected with level gauging pipe on tank body.
It is further preferred that level gauging pipe is connected with display.
It is further preferred that neutralizing tank is located at the top of inspissator.
The setting of the first valve of the utility model facilitates control inlet amount, and the setting of the second valve facilitates control lye amount.
The utility model temp probe, the setting of pH measurement probe and the setting of level gauging pipe, can be square
Just grasp and control temperature, pH value, feed liquid when amount of solvent in tank.
The utility model compared with prior art, it has the advantage that:
(1) by adopting the above technical scheme, top sets lye pond and feed well in extractor, is conducive to material and enters tank
It is interior, facilitate and adjusts pH value of solution, temperature and solution additive amount in tank.
(2) tank peripheral hardware circulator is extracted, not only makes protein extracting material in tank and solution fast by colloid mill
Fast defibrination mixes, and can also accelerate protein dissolution efficiency, substantially reduce the protein extracting time.Egg is extracted while defibrination
It is white, dissolved rate of protein >=90%；Protein content >=85% of the Walnut protein powder of spray-dried acquisition, instant capacity is good, can
It is widely used in beverage and instant product exploitation.
(3) this system apparatus structure is simple, simplifies protein extracting process, reduces equipment investment, solves traditional walnut
The problems such as protein extraction rate is low in cake protein extracting process.The utility model can improve the attached value of walnut grouts, make its change
Waste be changed into values, and implementing process is easy and economical, is suitble to scale industrial production.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of 1 walnut grouts defibrination of the utility model embodiment and protein extraction tank；
Fig. 2 is the structural schematic diagram of 1 walnut grouts defibrination of the utility model embodiment and protein extraction tank；
Fig. 3 is the structural schematic diagram of 1 walnut grouts defibrination of the utility model embodiment and protein extraction tank；
Fig. 4 is the structural schematic diagram of 1 walnut grouts defibrination of the utility model embodiment and protein extraction tank；
Fig. 5 is the structural schematic diagram of 1 walnut grouts defibrination of the utility model embodiment and protein extraction tank；
Wherein, the first valve of 1-, 2- feed well, 3- display, 4- level gauging pipe, 5- temp probe, 6- soda acid
Spend measuring probe, 7- level gauging pipe switch, 8- tank body, 9- hollow insulation layer, 10- colloid mill, 11- discharge nozzle, 12- tri-
Port valve, 13- circulating line, 14- lye pond, the second valve of 15-, 16- serum pot, 17- slurries tank valve, 18- pump, 19- crouch spiral shell
Centrifuge, 20- solid phase outlet, 21- neutralizing tank, 22- inspissator, 23- homogenizer, 24- spray dryer.
Specific embodiment
The utility model is described in further detail below with reference to embodiment.
It will be understood to those of skill in the art that the following example is merely to illustrate the utility model, and should not be regarded as limiting
The scope of the utility model.Particular technique, connection relationship or condition person are not specified in embodiment, according to the literature in the art institute
The technology of description, connection relationship, condition are carried out according to product description.Production is not specified in material therefor, instrument or equipment
Manufacturer person is the conventional products that can be obtained by purchase.
Those skilled in the art of the present technique are appreciated that unless expressly stated, singular " one " used herein, " one
It is a ", " described " and "the" may also comprise plural form.It is to be further understood that being used in the specification of the utility model
Wording " comprising " refer to that there are the feature, integer, step, operation, element and/or component, but it is not excluded that in the presence of or
Add other one or more features, integer, step, operation, element, component and/or their group.It should be understood that working as us
Element is claimed to be " connected " or when " coupled " to another element, it can be directly connected or coupled to other elements, or can also be with
There are intermediary elements.In addition, " connection " used herein or " coupling " may include being wirelessly connected or coupling.
In the description of the present invention, unless otherwise indicated, the meaning of " plurality " is two or more.Term
The orientation or state relation of the instructions such as "inner", "upper", "lower" are orientation based on the figure or state relation, merely to just
In description the utility model and simplify description, rather than the device or element of indication or suggestion meaning there must be specific side
Position is constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connection ", " being equipped with " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, be also possible to be electrically connected；It can be directly connected, it can also be indirectly connected through an intermediary.
For the ordinary skill in the art, understand as the case may be above-mentioned term in the present invention specifically contain
Justice.
Those skilled in the art of the present technique are appreciated that unless otherwise defined, all terms used herein (including technology art
Language and scientific term) there is meaning identical with the general understanding of those of ordinary skill in the utility model fields.Also
It should be understood that those terms such as defined in the general dictionary should be understood that have in the context of the prior art
The consistent meaning of meaning will not be explained in an idealized or overly formal meaning and unless defined as here.
The utility model for the first valve 1, the second valve 15 specific structure there is no limit.
Embodiment 1
As shown in Figure 1, a kind of Walnut protein powder preparation system, including extractor, serum pot 16, decanter centrifuge 19, in
With tank 21, inspissator 22, homogenizer 23 and spray dryer 24, the extractor includes tank body 8, colloid mill 10 and circulation pipe
Road 13；Feed well 2 and lye pond 14 are equipped at the top of tank body 8；
It is equipped with the first valve 1 between feed well 2 and tank body 8, the second valve 15 is equipped between feed well 2 and lye pond 14；
8 discharge port of tank body is connected by pipeline with the feed inlet of colloid mill 10；
The discharge port of colloid mill 10 is connected with discharge nozzle 11, circulating line 13 respectively, and is equipped with triple valve 12 in junction；
The other end of discharge nozzle 11 is connected with the top of tank body 8；
The outlet end of discharge nozzle 11 is set to the surface of serum pot 16, and the discharge port of serum pot 16 is by having slurries pot valve
Door 17, pump 18 pipeline be connected with the feed inlet of 19 side of decanter centrifuge；The bottom of decanter centrifuge 19 is discharged equipped with solid phase
Mouth 20；The liquid outlet of 19 other side of decanter centrifuge is connected with the top of neutralizing tank 21 by pipeline, and the bottom of neutralizing tank 21 goes out
Material mouth is connected with the feed inlet at 22 top of inspissator by pipeline；The discharge port of 22 lower part of inspissator and the feed inlet of homogenizer 23
It is connected by pipeline；The discharge port of homogenizer 23 is connected with the feed inlet of spray dryer 24 by pipeline.
Embodiment 2
As shown in Fig. 2, a kind of Walnut protein powder preparation system, including extractor, serum pot 16, decanter centrifuge 19, in
With tank 21, inspissator 22, homogenizer 23 and spray dryer 24, the extractor includes tank body 8, colloid mill 10 and circulation pipe
Road 13；Feed well 2 and lye pond 14 are equipped at the top of tank body 8；
It is equipped with the first valve 1 between feed well 2 and tank body 8, the second valve 15 is equipped between feed well 2 and lye pond 14；
8 discharge port of tank body is connected by pipeline with the feed inlet of colloid mill 10；
The discharge port of colloid mill 10 is connected with discharge nozzle 11, circulating line 13 respectively, and is equipped with triple valve 12 in junction；
The other end of discharge nozzle 11 is connected with the top of tank body 8；
The outlet end of discharge nozzle 11 is set to the surface of serum pot 16, and the discharge port of serum pot 16 is by having slurries pot valve
Door 17, pump 18 pipeline be connected with the feed inlet of 19 side of decanter centrifuge；The bottom of decanter centrifuge 19 is discharged equipped with solid phase
Mouth 20；The liquid outlet of 19 other side of decanter centrifuge is connected with the top of neutralizing tank 21 by pipeline, and the bottom of neutralizing tank 21 goes out
Material mouth is connected with the feed inlet at 22 top of inspissator by pipeline；The discharge port of 22 lower part of inspissator and the feed inlet of homogenizer 23
It is connected by pipeline；The discharge port of homogenizer 23 is connected with the feed inlet of spray dryer 24 by pipeline.
Colloid mill 10 is set to the lower section of tank body 8.
8 outer surface of tank body is enclosed with hollow insulation layer 9.
Embodiment 3
As shown in figure 3, a kind of Walnut protein powder preparation system, including extractor, serum pot 16, decanter centrifuge 19, in
With tank 21, inspissator 22, homogenizer 23 and spray dryer 24, the extractor includes tank body 8, colloid mill 10 and circulation pipe
Road 13；Feed well 2 and lye pond 14 are equipped at the top of tank body 8；
It is equipped with the first valve 1 between feed well 2 and tank body 8, the second valve 15 is equipped between feed well 2 and lye pond 14；
8 discharge port of tank body is connected by pipeline with the feed inlet of colloid mill 10；
The discharge port of colloid mill 10 is connected with discharge nozzle 11, circulating line 13 respectively, and is equipped with triple valve 12 in junction；
The other end of discharge nozzle 11 is connected with the top of tank body 8；
The outlet end of discharge nozzle 11 is set to the surface of serum pot 16, and the discharge port of serum pot 16 is by having slurries pot valve
Door 17, pump 18 pipeline be connected with the feed inlet of 19 side of decanter centrifuge；The bottom of decanter centrifuge 19 is discharged equipped with solid phase
Mouth 20；The liquid outlet of 19 other side of decanter centrifuge is connected with the top of neutralizing tank 21 by pipeline, and the bottom of neutralizing tank 21 goes out
Material mouth is connected with the feed inlet at 22 top of inspissator by pipeline；The discharge port of 22 lower part of inspissator and the feed inlet of homogenizer 23
It is connected by pipeline；The discharge port of homogenizer 23 is connected with the feed inlet of spray dryer 24 by pipeline.
Colloid mill 10 is set to the lower section of tank body 8.
8 outer surface of tank body is enclosed with hollow insulation layer 9.
Bottom is equipped with temp probe 5 and pH measurement probe 6 in tank body 8, and is connected by conducting wire with display 3.
Embodiment 4
As shown in figure 4, a kind of Walnut protein powder preparation system, including extractor, serum pot 16, decanter centrifuge 19, in
With tank 21, inspissator 22, homogenizer 23 and spray dryer 24, the extractor includes tank body 8, colloid mill 10 and circulation pipe
Road 13；Feed well 2 and lye pond 14 are equipped at the top of tank body 8；
It is equipped with the first valve 1 between feed well 2 and tank body 8, the second valve 15 is equipped between feed well 2 and lye pond 14；
8 discharge port of tank body is connected by pipeline with the feed inlet of colloid mill 10；
The discharge port of colloid mill 10 is connected with discharge nozzle 11, circulating line 13 respectively, and is equipped with triple valve 12 in junction；
The other end of discharge nozzle 11 is connected with the top of tank body 8；
The outlet end of discharge nozzle 11 is set to the surface of serum pot 16, and the discharge port of serum pot 16 is by having slurries pot valve
Door 17, pump 18 pipeline be connected with the feed inlet of 19 side of decanter centrifuge；The bottom of decanter centrifuge 19 is discharged equipped with solid phase
Mouth 20；The liquid outlet of 19 other side of decanter centrifuge is connected with the top of neutralizing tank 21 by pipeline, and the bottom of neutralizing tank 21 goes out
Material mouth is connected with the feed inlet at 22 top of inspissator by pipeline；The discharge port of 22 lower part of inspissator and the feed inlet of homogenizer 23
It is connected by pipeline；The discharge port of homogenizer 23 is connected with the feed inlet of spray dryer 24 by pipeline.
Colloid mill 10 is set to the lower section of tank body 8.
8 outer surface of tank body is enclosed with hollow insulation layer 9.
Bottom is equipped with temp probe 5 and pH measurement probe 6 in tank body 8, and is connected by conducting wire with display 3.
Level gauging pipe 4 is connected on tank body 8.
Embodiment 5
As shown in figure 5, a kind of Walnut protein powder preparation system, including extractor, serum pot 16, decanter centrifuge 19, in
With tank 21, inspissator 22, homogenizer 23 and spray dryer 24, the extractor includes tank body 8, colloid mill 10 and circulation pipe
Road 13；Feed well 2 and lye pond 14 are equipped at the top of tank body 8；
It is equipped with the first valve 1 between feed well 2 and tank body 8, the second valve 15 is equipped between feed well 2 and lye pond 14；
8 discharge port of tank body is connected by pipeline with the feed inlet of colloid mill 10；
The discharge port of colloid mill 10 is connected with discharge nozzle 11, circulating line 13 respectively, and is equipped with triple valve 12 in junction；
The other end of discharge nozzle 11 is connected with the top of tank body 8；
The outlet end of discharge nozzle 11 is set to the surface of serum pot 16, and the discharge port of serum pot 16 is by having slurries pot valve
Door 17, pump 18 pipeline be connected with the feed inlet of 19 side of decanter centrifuge；The bottom of decanter centrifuge 19 is discharged equipped with solid phase
Mouth 20；The liquid outlet of 19 other side of decanter centrifuge is connected with the top of neutralizing tank 21 by pipeline, and the bottom of neutralizing tank 21 goes out
Material mouth is connected with the feed inlet at 22 top of inspissator by pipeline；The discharge port of 22 lower part of inspissator and the feed inlet of homogenizer 23
It is connected by pipeline；The discharge port of homogenizer 23 is connected with the feed inlet of spray dryer 24 by pipeline.
Colloid mill 10 is set to the lower section of tank body 8.
8 outer surface of tank body is enclosed with hollow insulation layer 9.
Bottom is equipped with temp probe 5 and pH measurement probe 6 in tank body 8, and is connected by conducting wire with display 3.
Level gauging pipe 4 is connected on tank body 8, and level gauging pipe 4 is connected with display 3.Wherein, tank body
8 can be connected by level gauging pipe switch 7 with level gauging pipe 4 is connected with, but not limited to this.
Neutralizing tank 21 is located at the top of inspissator 22.
The effect of the utility model display 3 is for displays temperature 5 collected temperature of probe, pH measurement probe 6
PH value of solution in collected tank is also used to show the collected liquid level of level gauging pipe 4.The utility model is for aobvious
Show that there is no limit as long as be able to achieve its function for the internal structure of device 3.
Application method:
The utility model is heated and is kept the temperature by entering steam into hollow insulation layer 9 in extraction process；
Grouts powder of the walnut after squeezer liquefaction opens the first valve 1, by certain feed liquid mass ratio after pulverizing and sieving
It first passes through feed well 2 and softened water is added in tank body 8, close the first valve 1；
It by 14 fabricated food grade NaOH solution of lye pond, allows NaOH solution to enter in tank body 8 by the second valve 15, adjusts
The optimal pH of softened water pH to extracting protein matter is saved, the second valve 15 is closed；
Pass through feed well 2 again and opens the walnut grouts powder that certain mass is added in the first valve 1；
Triple valve 12 is opened, so that the discharge port of colloid mill 10 is only connected with circulating line 13, opens colloid mill later
10, it grinds walnut grouts liquid in tank body 8 by colloid mill 10, is recycled returning to flow into tank body 8, this not only makes object in tank body
Material is combined rapidly mixing with solution, can also accelerate proteolytic efficiency；
Situation, circular grinding certain time are dissolved out according to grouts degree of grinding and albumen；
After each feed cycle grinding, regulating three-way valve 12, so that the discharge port of colloid mill 10 and discharge nozzle 11
It is connected, walnut slurries is allowed to flow out by discharge nozzle 11, into serum pot 16, slurries tank valve 17, pump 18 is opened, so that slurry
Material, which enters in decanter centrifuge 19, to be centrifuged, and solid content is discharged from solid phase outlet 20, and supernatant flows into neutralizing tank 21,
PH is adjusted to neutrality, obtains protein solution；
The concentrated device 22 of protein solution enters 23 homogeneous of homogenizer after being concentrated, and finally flows into spray drying tower 24 and carries out
It dusts, obtains Walnut protein powder.
By temp probe 5, pH measurement probe 6 and the collected data of level gauging pipe 4, display can be passed through
Controller observation, can be convenient for users to grasping and control temperature in tank, pH value, feed liquid when amount of solvent.
Basic principles, main features, and advantages of the present invention has been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model is also
It will have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.The utility model
Claimed range is defined by the appending claims and its equivalent thereof.
Claims (8)
1. a kind of Walnut protein powder preparation system, which is characterized in that including extractor, serum pot (16), decanter centrifuge (19),
Neutralizing tank (21), inspissator (22), homogenizer (23) and spray dryer (24), the extractor includes tank body (8), colloid
Grind (10) and circulating line (13)；Feed well (2) and lye pond (14) are equipped at the top of tank body (8)；
It is equipped with the first valve (1) between feed well (2) and tank body (8), the second valve is equipped between feed well (2) and lye pond (14)
Door (15)；
Tank body (8) discharge port is connected by pipeline with the feed inlet of colloid mill (10)；
The discharge port of colloid mill (10) is connected with discharge nozzle (11), circulating line (13) respectively, and is equipped with triple valve in junction
(12)；The other end of discharge nozzle (11) is connected with the top of tank body (8)；
The outlet end of discharge nozzle (11) is set to the surface of serum pot (16), and the discharge port of serum pot (16) is by having serum pot
Valve (17), the pipeline for pumping (18) are connected with the feed inlet of decanter centrifuge (19) side；The bottom of decanter centrifuge (19) is set
There are solid phase outlet (20)；The liquid outlet of decanter centrifuge (19) other side is connected with the top of neutralizing tank (21) by pipeline,
The bottom discharge port of neutralizing tank (21) is connected with the feed inlet at the top of inspissator (22) by pipeline；Inspissator (22) lower part goes out
Material mouth is connected with the feed inlet of homogenizer (23) by pipeline；The discharge port of homogenizer (23) and the charging of spray dryer (24)
Mouth is connected by pipeline.
2. Walnut protein powder preparation system according to claim 1, which is characterized in that colloid mill (10) is set to tank body (8)
Lower section.
3. Walnut protein powder preparation system according to claim 1, which is characterized in that during tank body (8) outer surface is enclosed with
Empty insulating layer (9).
4. Walnut protein powder preparation system according to claim 1, which is characterized in that tank body (8) interior bottom is equipped with temperature
It pops one's head in (5), and is connected by conducting wire with display (3).
5. Walnut protein powder preparation system according to claim 1, which is characterized in that tank body (8) interior bottom is equipped with soda acid
It spends measuring probe (6), and is connected by conducting wire with display (3).
6. Walnut protein powder preparation system according to claim 1, which is characterized in that tank body is connected with liquid level height on (8)
It spends measurement pipe (4).
7. Walnut protein powder preparation system according to claim 1, which is characterized in that level gauging pipe (4) and aobvious
Show that device (3) are connected.
8. Walnut protein powder preparation system according to claim 1, which is characterized in that neutralizing tank (21) is located at inspissator
(22) top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920133597.5U CN209711374U (en) | 2019-01-25 | 2019-01-25 | A kind of Walnut protein powder preparation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920133597.5U CN209711374U (en) | 2019-01-25 | 2019-01-25 | A kind of Walnut protein powder preparation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209711374U true CN209711374U (en) | 2019-12-03 |
Family
ID=68681357
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920133597.5U Expired - Fee Related CN209711374U (en) | 2019-01-25 | 2019-01-25 | A kind of Walnut protein powder preparation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209711374U (en) |
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2019
- 2019-01-25 CN CN201920133597.5U patent/CN209711374U/en not_active Expired - Fee Related
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191203 Termination date: 20220125 |
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| CF01 | Termination of patent right due to non-payment of annual fee |