CN207202789U - A kind of food processor - Google Patents

A kind of food processor Download PDF

Info

Publication number
CN207202789U
CN207202789U CN201720324256.7U CN201720324256U CN207202789U CN 207202789 U CN207202789 U CN 207202789U CN 201720324256 U CN201720324256 U CN 201720324256U CN 207202789 U CN207202789 U CN 207202789U
Authority
CN
China
Prior art keywords
pulp
thick liquid
discharge
discharge pipe
plasma discharge
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
Application number
CN201720324256.7U
Other languages
Chinese (zh)
Inventor
王旭宁
郭红伟
刘超
余旦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hangzhou Jiuchuang Home Appliances Co ltd
Original Assignee
Joyoung Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Joyoung Co Ltd filed Critical Joyoung Co Ltd
Priority to CN201720324256.7U priority Critical patent/CN207202789U/en
Application granted granted Critical
Publication of CN207202789U publication Critical patent/CN207202789U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of food processor, belong to food processing apparatus field, solve the problems, such as that plasma discharge is blocked or splashed, the technical scheme for solving the problem mainly includes body and the water supply component located at body, shredder assemblies and plasma discharge component, shredder assemblies include crushing chamber, water supply component supplies water to crushing chamber, the bottom of crushing chamber is provided with thick liquid discharge mouth, plasma discharge component includes pulp-expelling valve and discharge pipe, pulp-expelling valve is provided with plasma discharge passage, the entrance of plasma discharge passage connects with thick liquid discharge mouth, the outlet of plasma discharge passage connects with discharge pipe, the circulation area of thick liquid discharge mouth is S1, S1=50mm2~260 mm2.The utility model is mainly used in realizing orderly, smooth plasma discharge.

Description

A kind of food processor
Technical field
Food processing apparatus is the utility model is related to, particularly a kind of food processor.
Background technology
A kind of existing food processor, including the body and water supply component located at body, shredder assemblies and plasma discharge component, Shredder assemblies include crushing chamber, and water supply component supplies water to crushing chamber, and the bottom of crushing chamber is provided with thick liquid discharge mouth, and plasma discharge component includes row Slurry valve and discharge pipe, pulp-expelling valve are provided with plasma discharge passage, and the entrance of plasma discharge passage connects with thick liquid discharge mouth, the outlet of plasma discharge passage and row Pipe connection is starched, if thick liquid discharge mouth is too small, easily occurs situation about blocking in plasma discharge, if thick liquid discharge mouth is excessive, holds in plasma discharge Easily there are slurries to gush the situation of splashing.
The content of the invention
The utility model purpose to be reached just is to provide a kind of food processor, realizes orderly, smooth plasma discharge.
In order to achieve the above object, the utility model adopts the following technical scheme that:A kind of food processor, including body and Located at the water supply component of body, shredder assemblies and plasma discharge component, shredder assemblies include crushing chamber, and water supply component supplies to crushing chamber Water, the bottom of crushing chamber are provided with thick liquid discharge mouth, and plasma discharge component includes pulp-expelling valve and discharge pipe, and pulp-expelling valve is provided with plasma discharge passage, plasma discharge The entrance of passage connects with thick liquid discharge mouth, and the outlet of plasma discharge passage connects with discharge pipe, and the circulation area of thick liquid discharge mouth is S1, and S1= 50mm2~260 mm2
Further, the S1=75mm2~200mm2
Further, the circulation area of the plasma discharge passage is S2, S2 >=S1.
Further, the angle between the plasma discharge direction of the discharge pipe and the center line of thick liquid discharge mouth is α, 0≤α≤70 °.
Further, the center line of the discharge pipe overlaps with the center line of thick liquid discharge mouth, α=0.
Further, the discharge pipe is connected including changeover portion, extension and pulp section, changeover portion with pulp-expelling valve, is extended Section be connected between changeover portion and pulp section, extension is extended with respect to the centerline dip of thick liquid discharge mouth, pulp section along put down Row is extended in the direction of the center line of thick liquid discharge mouth, α=0.
Further, the discharge pipe is connected including changeover portion, extension and pulp section, changeover portion with pulp-expelling valve, is extended Section is connected between changeover portion and pulp section, and extension is extended with respect to the centerline dip of thick liquid discharge mouth, the center of pulp section Line overlaps with the center line of extension, 0 < α≤70 °.
Further, center line of the pulp end face of the discharge pipe perpendicular to thick liquid discharge mouth.
Further, the pulp end face of the discharge pipe tilts with respect to the plasma discharge direction of discharge pipe.
Further, the circulation area of the discharge pipe is S3, S3 >=S2.
After adopting the above technical scheme, the utility model has the following advantages that:If S1 is too small, if slurries are denser When, slurries are poor in the mobility of thick liquid discharge mouth, easily block, and plasma discharge speed is slower, cause mixing time long, shadow Ring the usage experience of user;If S1 is excessive, the slurries velocity of discharge is too fast, and slurries can gush from discharge pipe, and slurries leave Easily splashed during discharge pipe, not only cause slurries to waste, and increase cleaning amount, also resulted under Consumer's Experience Drop, simultaneously because the slurries in crushing chamber are discharged into connect slurry cup in a short time, it is not easy to which passage time controls plasma discharge amount, is carrying out When slurries are blent, slurries easily produce lamination, cause mouthfeel to decline.
Brief description of the drawings
The utility model is described in further detail below in conjunction with the accompanying drawings:
Fig. 1 is a kind of schematic diagram of food processor of the utility model;
Fig. 2 is the enlarged drawing at I in Fig. 1;
Fig. 3 is the upward view of the pulp end face of discharge pipe in Fig. 2;
Fig. 4 is the structural representation of the utility model embodiment two;
Fig. 5 is the structural representation of the utility model embodiment three;
Fig. 6 is the structural representation of the utility model embodiment four.
Embodiment
As shown in figure 1, the utility model provides a kind of food processor, including body 1 and the water supply group located at body 1 Part, shredder assemblies and plasma discharge component, shredder assemblies include crushing chamber 300, crush motor 31 and Disintegrating knife 32, water supply component to Crushing chamber 300 supplies water, and water supply component generally comprises water tank 2 and water pump, and water tank 2, water pump and crushing chamber 300 pass sequentially through water inlet pipe Connection, pump working is by the water pump of water tank 2 to crushing chamber 300, in some types, can also water pump and crushing chamber 300 it Between setting be hot device, to water inlet heat, by hot water input crushing chamber 300, seen with reference to Fig. 2, the bottom of crushing chamber 300 is provided with Thick liquid discharge mouth 301, plasma discharge component include pulp-expelling valve 4 and discharge pipe 5, and pulp-expelling valve 4 is provided with plasma discharge passage 401, and plasma discharge passage 401 enters Mouth connects with thick liquid discharge mouth 301, and the outlet of plasma discharge passage 401 connects with discharge pipe 5, and discharge pipe 5 arranges slurries to slurry cup 6 is connect, and is The orderly plasma discharge of realization, avoids slurry plugs or splashing of gushing, and the circulation area of thick liquid discharge mouth 301 is S1, S1=50mm2~260 mm2
In the utility model, circulation area refers to intersect shape with oral area or passage perpendicular to the section of slurries flow direction Into the area that is surrounded of closed curve.If S1 is too small, if slurries are denser, mobility of the slurries in thick liquid discharge mouth 301 It is poor, easily block, and plasma discharge speed is slower, causes mixing time long, influences the usage experience of user;If S1 mistakes When big, the slurries velocity of discharge is too fast, and slurries can gush from discharge pipe 5, and slurries easily splash when leaving discharge pipe 5, Not only cause slurries to waste, and increase cleaning amount, Consumer's Experience decline is also resulted in, simultaneously because in crushing chamber 300 Slurries be discharged into connect slurry cup 6 in a short time, it is not easy to passage time controls plasma discharge amount, and when carrying out slurries and blending, slurries hold Lamination is also easy to produce, causes mouthfeel to decline.Therefore S1 can typically take 50mm2、60mm2、70mm2、80mm2、90mm2、 100mm2、110mm2、120mm2、130mm2、140mm2、150mm2、160mm2、170mm2、180mm2、190mm2、200mm2、 210mm2、220mm2、230mm2、240mm2、250mm2Or 260 mm2Etc..
Because slurries are the mixtures that are formed with water after crushing material, the density for the slurries that different materials is formed is not Together, while different slurrying flows also results in the slurries to form different densities, and as relatively good embodiment, S1= 75mm2~200mm2, S1 within this range, is adapted to the slurries density of relative broad range, it is ensured that slurries can be normally orderly It is discharged into and connects slurry cup 6.
In existing product, thick liquid discharge mouth 301 is traditionally arranged to be circle, can make slurries by when circulate smooth, material is not Easily residual, therefore according to S1 scope, as shown in Fig. 2 the diameter D1 of thick liquid discharge mouth 301 requirement can be changed into, the mm of D1=8~ 18.2mm, such as D1=8mm, 9mm, 10mm, 11mm, 12mm, 13mm, 14mm, 15mm, 16mm, 17mm or 18.2mm etc..
And plasma discharge passage 401 is connected to the downstream of thick liquid discharge mouth 301, i.e. slurries are led to by being put into plasma discharge after thick liquid discharge mouth 301 Road 401, because plasma discharge passage 401 needs to control opening/closing, therefore plasma discharge passage 401 will ensure the effective of opening/closing operation Property, to allow slurries to circulate more smooth, therefore the circulation area of plasma discharge passage 401 is S2, S2 >=S1.It is certainly contemplated that the row of arriving The size relationship of valve 4 is starched, S2 also will not be excessive, in general, S2=1.17S1 in S2=S1~1.44S1, such as the present embodiment, row Slurry passage 401 is also mostly circular, and S2 and S1 relation can be converted into diameter D2 and D1 relation, that is, have D2=1.08D1.See figure 2, plasma discharge passage 401 includes upper hole 4011, valve block hole 4012 and lower opening 4013, and upper hole 4011 and lower opening 4013 are located at pulp-expelling valve 4 Valve body 41 on, upper hole 4011 is always maintained at connecting with thick liquid discharge mouth 301, and lower opening 4013 is then always maintained at connecting with discharge pipe 5, valve Film perforation 4012 is located on the valve block 42 of pulp-expelling valve 4, and valve block turns to the position for making valve block hole 4012 be alignd with upper hole 4011 just It is the open mode of pulp-expelling valve 4, the upper hole 4011 of the connection of valve block hole 4012, lower opening 4013, valve block hole 4012 is staggered with upper hole 4011 Afterwards, it is exactly the closed mode of pulp-expelling valve 4, valve block separates upper hole 4011, lower opening 4013.In the opening procedure of pulp-expelling valve 4, valve Piece needs the regular hour to rotate the position to the position alignd with upper hole 4011 for allowing valve block hole 4012 to stagger from relatively upper hole 4011 Put, therefore the circulation area in valve block hole 4012 is limited with S2, it is ensured that slurries circulate smooth in valve block hole 4012, avoid material It is deposited in valve block hole 4012 and influences the mobility of slurries.
For slurries by that will enter discharge pipe 5 after pulp-expelling valve 4, in order to ensure slurries, flowing is smooth in discharge pipe 5, considers To the position relationship for connecing slurry cup 6 and pulp-expelling valve 4, the angle between the plasma discharge direction of discharge pipe 5 and the center line of thick liquid discharge mouth 301 is α, 0≤α≤70 ° can be required, such as the plasma discharge direction of discharge pipe 5 can be along the center line L of thick liquid discharge mouth 301, i.e. α=0; The plasma discharge direction of discharge pipe 5 can be allowed to be tilted with respect to the center line L of thick liquid discharge mouth 301, i.e. 0 < α≤70 °.The plasma discharge side of discharge pipe 5 To the flow direction that can be understood as slurries and leave the moment of discharge pipe 5, generally along the center of the pulp end of discharge pipe 5 Line, can be respectively with reference to the arrow in figure 2, Fig. 4, Fig. 5 and Fig. 6 for different embodiments.In addition, the circulation area of discharge pipe 5 For S3, S3 >=S2, D3 and D2 relation, usually D3=D2~1.2D2 are converted into.As D1=D2=D3, the slurries row of flowing through successively Mouth 301, plasma discharge passage 401 and discharge pipe 5 are starched, circulation area keeps constant, so slurry flow rate is stable, is not likely to produce turbulent flow, Discharge pipe 5 can be flowed out in order, avoided adverse current or splashed;And during D3 > D2 > D1, slurries flow through thick liquid discharge mouth 301, plasma discharge successively Passage 401 and discharge pipe 5, circulation area increases successively, due to not again being that the continuous change of taper type is big to D3 from D1 to D2, but Stepped segmentation becomes big, so the pressure of slurries continuously will not ceaselessly decline in flow process, but gradually reduces, no Turbulent flow is also easy to produce, slurries can flow out discharge pipe 5 in order, avoid adverse current or splash.
There can be various ways specific to the setting of discharge pipe 5, illustrate with reference to embodiment.
Embodiment one:
In some types, because space limits, the position of slurry cup 6 is connect not in the underface of pulp-expelling valve 4, it is therefore desirable to arrange Slurry pipe 5 is obliquely installed.Fig. 2 is returned to, in the present embodiment, discharge pipe 5 includes changeover portion 51, extension 52 and pulp section 53, mistake Cross section 51 to be connected with pulp-expelling valve 4, changeover portion 51 uses smooth curve transition, such as arc transition, extension 52 to be connected to transition Between section 51 and pulp section 53, extension 52 tilts with respect to the center line L of thick liquid discharge mouth 301 and is extended, the center of pulp section 53 Line overlaps with the center line of extension 52,0 < α≤70 °.α can according to connect slurry cup 6 with respect to thick liquid discharge mouth 301 position relationship come Selection, such as α=49 ° in the present embodiment.Because slurries plasma discharge is realized by the gravity of slurries, so α is unsuitable excessive, α is big In 70 °, then when can cause the slurries to pass through discharge pipe 5, the influence of the gravity convection speed of slurries itself reduces, and causes slurries outflow row Speed declines when starching pipe 5, because slurries have some tension, therefore outer surface adverse current of the slurries along discharge pipe 5 easily occurs, Cause slurries not to be discharged into normally and connect slurry cup 6, can also flow to other positions of body 1, increase cleaning amount.In addition, flow velocity Decline, blocking also would tend to occur.
Because the center line L of thick liquid discharge mouth 301 is substantially on gravity direction, in the present embodiment, discharge pipe 5 Pulp end face 501 perpendicular to thick liquid discharge mouth 301 center line L, be easy to eliminate slurries tension force influence so that slurries be easier with Discharge pipe 5 separates, and avoids outer surface adverse current of the slurries along discharge pipe 5.
In the present embodiment, the pulp end face 501 of discharge pipe 5 tilts with respect to the plasma discharge direction of discharge pipe 5, therefore expands simultaneously The area that the pulp end face 501 of big discharge pipe 5 is surrounded, as shown in figure 3, the shape that the pulp end face 501 of discharge pipe 5 is surrounded Shape is ellipse, compared to the circular cross-section of discharge pipe 5(Shown in dotted line)Circulation area it is big, it is easier to overcome slurries in pulp Tension force, be easy to slurries to be separated with discharge pipe 5 rapider, thoroughly.
Embodiment two:
As shown in figure 4, as preferable embodiment, the center line of discharge pipe 5 overlaps with the center line L of thick liquid discharge mouth 301, α= 0.Center line L of the pulp end face 501 of discharge pipe 5 perpendicular to thick liquid discharge mouth 301.
Other contents not described may be referred to embodiment one.
Embodiment three:
As shown in figure 5, on the basis of embodiment two, the plasma discharge side of the relative discharge pipe 5 in pulp end face 501 of discharge pipe 5 To inclination.
Other contents not described may be referred to embodiment one.
Example IV:
As shown in fig. 6, in the present embodiment, discharge pipe 5 includes changeover portion 51, extension 52 and pulp section 53, changeover portion 51 are connected with pulp-expelling valve 4, and extension 52 is connected between changeover portion 51 and pulp section 53, and extension 52 is with respect to thick liquid discharge mouth 301 Center line L, which is tilted, to be extended, and direction of the pulp section 53 along the center line L parallel to thick liquid discharge mouth 301 is extended, α=0.Prolong Stretch and should also be as being transition connection between section 52 and pulp section 53.The pulp end face 501 of discharge pipe 5 is in thick liquid discharge mouth 301 Heart line L.
It should be understood that in the present embodiment, can also be by plasma discharge of the pulp end face 501 of discharge pipe 5 with respect to discharge pipe 5 Direction tilts.
Other contents not described may be referred to embodiment one.
In addition to above preferred embodiment, the utility model also has other embodiments, and those skilled in the art can root It is variously modified and deforms according to the utility model, without departing from spirit of the present utility model, the utility model all should be belonged to Scope defined in appended claims.

Claims (10)

1. a kind of food processor, including the body and water supply component located at body, shredder assemblies and plasma discharge component, shredder assemblies Including crushing chamber, water supply component supplies water to crushing chamber, and the bottom of crushing chamber is provided with thick liquid discharge mouth, and plasma discharge component includes pulp-expelling valve and row Slurry pipe, pulp-expelling valve are provided with plasma discharge passage, and the entrance of plasma discharge passage connects with thick liquid discharge mouth, and outlet and the discharge pipe of plasma discharge passage connect It is logical, it is characterised in that the circulation area of the thick liquid discharge mouth is S1, S1=50mm2~260 mm2
2. food processor according to claim 1, it is characterised in that the S1=75mm2~200mm2
3. food processor according to claim 1 or 2, it is characterised in that the circulation area of the plasma discharge passage is S2, S2≥S1。
4. food processor according to claim 1, it is characterised in that the plasma discharge direction of the discharge pipe and thick liquid discharge mouth Angle between center line is α, 0≤α≤70 °.
5. food processor according to claim 4, it is characterised in that in the center line and thick liquid discharge mouth of the discharge pipe Heart line overlaps, α=0.
6. food processor according to claim 4, it is characterised in that the discharge pipe include changeover portion, extension and Pulp section, changeover portion are connected with pulp-expelling valve, and extension is connected between changeover portion and pulp section, and extension is with respect in thick liquid discharge mouth Heart line, which tilts, to be extended, and direction of the pulp section along the center line parallel to thick liquid discharge mouth is extended, α=0.
7. food processor according to claim 4, it is characterised in that the discharge pipe include changeover portion, extension and Pulp section, changeover portion are connected with pulp-expelling valve, and extension is connected between changeover portion and pulp section, and extension is with respect in thick liquid discharge mouth Heart line, which tilts, to be extended, and the center line of pulp section overlaps with the center line of extension, 0 < α≤70 °.
8. according to the food processor described in claim 4 or 5 or 6 or 7, it is characterised in that the pulp end face of the discharge pipe Perpendicular to the center line of thick liquid discharge mouth.
9. according to the food processor described in claim 4 or 5 or 6 or 7, it is characterised in that the pulp end face of the discharge pipe Plasma discharge direction with respect to discharge pipe tilts.
10. according to the food processor described in claim 4 or 5 or 6 or 7, it is characterised in that the circulation area of the discharge pipe For S3, S3 >=S2.
CN201720324256.7U 2017-03-30 2017-03-30 A kind of food processor Active CN207202789U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720324256.7U CN207202789U (en) 2017-03-30 2017-03-30 A kind of food processor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720324256.7U CN207202789U (en) 2017-03-30 2017-03-30 A kind of food processor

Publications (1)

Publication Number Publication Date
CN207202789U true CN207202789U (en) 2018-04-10

Family

ID=61809390

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720324256.7U Active CN207202789U (en) 2017-03-30 2017-03-30 A kind of food processor

Country Status (1)

Country Link
CN (1) CN207202789U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113925364A (en) * 2020-06-29 2022-01-14 杭州九阳小家电有限公司 Cleaning control method of food processor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113925364A (en) * 2020-06-29 2022-01-14 杭州九阳小家电有限公司 Cleaning control method of food processor

Similar Documents

Publication Publication Date Title
JP5450670B2 (en) Apparatus for producing a coffee extract having a fine bubble foam layer using an impact rough surface
CN107995879A (en) Atomizer
CN207202789U (en) A kind of food processor
CN106999964A (en) Rotatable tank cleaning nozzle head including self-cleaning spray nozzle
CN105283408A (en) Mixing nozzle
CN207341635U (en) A kind of good capsule beverage machine of pulp effect
CN207839338U (en) A kind of coating machine pulp feeder device
US9962022B2 (en) Collapsible, flow-restricted, controlled-pour pitcher for brewing coffee
JP4850729B2 (en) Method and apparatus for mixing powder and liquid
CN210171713U (en) Spiral-flow type liquid separation device
CN207349528U (en) A kind of resistance to compression anticracking tap
CN205413366U (en) Centrifuge subassembly to cartridge regulator solution layer depth degree
JP2004530600A (en) Filling port for umbrella-shaped ejection
CN207940693U (en) A kind of soy bean milk making machine
CN104998774B (en) Shower nozzle
CN205838550U (en) A kind of milk product fill terminal structure
JP5261253B2 (en) Beverage supply nozzle
CN207076570U (en) A kind of shower water structure
TW201417869A (en) Mixing device
CN209647568U (en) It is a kind of to prevent into the interstitital texture for pouring two sides construction materials contract volume gas
JP6166109B2 (en) Filling head tank and method for processing beverage
CN201816746U (en) Product barrel in food filling machine
CN207769589U (en) A kind of kneading machine
CN106185761A (en) A kind of antibacterial type milk product bulking system discharging structure
CN208909590U (en) Water jug

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20230529

Address after: Building 2, No. 52, 22nd Street, Baiyang Street, Qiantang New District, Hangzhou City, Zhejiang Province, 310000

Patentee after: Hangzhou Jiuchuang Home Appliances Co.,Ltd.

Address before: No. 999, Mei Li Road, Huaiyin District, Ji'nan, Shandong

Patentee before: JOYOUNG Co.,Ltd.

TR01 Transfer of patent right