CN207341635U - A kind of good capsule beverage machine of pulp effect - Google Patents

Abstract

The utility model provides a kind of pulp effect good capsule beverage machine, including engine base, brew head, for water assembly, the cup for infusing and steeping and control unit of accommodating capsule, the brew head, it is arranged at for water assembly and control unit on engine base, it is described to provide water to brew head for water assembly, it is described to be electrically connected for water assembly with control unit, the lower part of the brew head is equipped with slurry outlet nozzle, the slurry outlet nozzle includes the pulp passage surrounded by annular sidewall, stock inlet positioned at pulp passage upper end and the grout outlet positioned at pulp passage lower end, wherein, splitter cavity is equipped with pulp passage, splitter cavity upper port is opened wide, lower port stretches out the grout outlet of pulp passage, shunting cavity outer wall and annular sidewall connect and are equipped with gap between shunting cavity outer wall and annular sidewall.The utility model can realize pulp even concentration, and slurries can flow down vertically along slurry outlet nozzle and continuity is good.

Description

A kind of good capsule beverage machine of pulp effect

Technical field

It the utility model is related to field of beverage preparation, more particularly to a kind of capsule beverage machine.

Background technology

The patent of Application No. CN201520943579.5 discloses a kind of antispray beverage machine, including engine base, injection head, For water assembly and control unit, the injection head, be arranged on engine base for water assembly and control unit, described to be carried for water assembly Supply water to injection head, described to be electrically connected for water assembly with control unit, what the beverage machine included reconstituting capsule reconstitutes Chamber, the beverage machine further include out sizing device, it is described go out sizing device include slurry outlet nozzle, the slurry outlet nozzle be equipped with annular sidewall and Bottom wall, bottom wall are equipped with grout outlet, and the cavity that the annular sidewall and bottom wall of the slurry outlet nozzle surround is pulp passage, the annular The opening that sidewall upper is formed is stock inlet, and the slurry outlet nozzle is additionally provided with exhausting-gas hole, and the exhausting-gas hole connects with the pulp passage Logical, the slurries reconstituted pass through pulp passage, are discharged from grout outlet, and set exhausting-gas hole to make in pulp passage in slurry outlet nozzle Mixed gas is discharged by exhausting-gas hole in original gas and slurries so that slurries it is gentle by grout outlet, prevent slurries Splash.Flow-disturbing platform is equipped with the pulp passage, the flow-disturbing platform is located at the top of grout outlet, corresponding with the grout outlet to set Put, flow-disturbing platform hinders stock inlet to slow down slurry flow rate to the direct flow path between grout outlet, prevent slurries splash.

But the concentration of slurry flowed out through the grout outlet is not uniform enough, liquid stream is undesirable by the continuity of grout outlet.

Utility model content

The purpose of this utility model is to provide a kind of good capsule beverage machine of pulp effect.

In order to solve the above-mentioned technical problem, the utility model adopts the following technical solution：

A kind of good capsule beverage machine of pulp effect, including engine base, brew head, for water assembly, the cup for infusing and steeping of accommodating capsule And control unit, the brew head, be arranged on engine base for water assembly and control unit, described to provide water to punching for water assembly Steep head, described to be electrically connected with control unit for water assembly, the lower part of the brew head is equipped with slurry outlet nozzle, the slurry outlet nozzle including by Pulp passage, the stock inlet positioned at pulp passage upper end and the grout outlet positioned at pulp passage lower end that annular sidewall surrounds, Wherein, splitter cavity is equipped with pulp passage, splitter cavity upper port is opened wide, and lower port stretches out the grout outlet of pulp passage, splitter cavity Outer wall and annular sidewall connect and are equipped with gap between shunting cavity outer wall and annular sidewall.

Preferably, the splitter cavity includes bucket-shaped portion and positioned at the bucket-shaped subordinate portion and the tube that is attached thereto.

Preferably, the bucket-shaped portion is hemispherical or cone.

Preferably, the tube is pipe.

Preferably, at least 2 ribs are equipped between the annular sidewall of the shunting cavity outer wall and pulp passage.

Preferably, the rib is distributed in the annular sidewall of pulp passage and the annular gap of shunting cavity outer wall formation.

Preferably, the rib from the upper port of splitter cavity and under extend to the lower port of splitter cavity.

Preferably, rib surrounds flow-guiding channel with shunting cavity outer wall, annular sidewall.

Preferably, the pipe length is L, wherein 1mm≤L≤8mm.

Preferably, a diameter of D of splitter cavity lower port, wherein 1 mm≤D≤4 mm.

Compared with prior art, the beneficial effects of the utility model are：

1. the utility model, by setting splitter cavity in pulp passage, splitter cavity upper port is opened wide, and lower port stretches out The grout outlet of passage is starched, cavity outer wall and annular sidewall connection is shunted and is equipped with gap between shunting cavity outer wall and annular sidewall, point Stream chamber upper port is opened wide, and the slurries in pulp passage can be entered in splitter cavity by upper port, and splitter cavity can be to the slurry of inflow Liquid is temporarily stored, and during storage, slurries can further mix in splitter cavity so that the slurries for flowing out splitter cavity are molten Degree is more uniform, mouthfeel is more preferable, and splitter cavity hinders stock inlet to slow down slurries to the direct flow path between grout outlet Flowing velocity, can at the uniform velocity flow continually out, pulp effect while mixing into the slurries in splitter cavity through splitter cavity lower port Ideal, avoids and flows into slurries in pulp passage in short-term and excessively cause the instantaneous slurry-outlet velocity of grout outlet too fast so that slurries flow into Cause to splash in goblet below slurry outlet nozzle, cause scald or stained desktop；Slurry-outlet quantity is more in short-term or splitter cavity lower port During blocking, another grout outlet can be used as by shunting the gap between cavity outer wall and annular sidewall, and the slurries that gap is overflowed can To be flowed downward out along shunting cavity outer wall；In addition, the gap also has the function that to carry out air circulation with the external world, slurry outlet nozzle with it is outer Boundary's air circulation can reduce negative pressure, reduce the generation of bubble in slurries, and slurries are flowing through shunting cavity outer wall and annular side Between wall during gap, mixed gas can be discharged from gap in slurries, can be also squeezed and broken when air pocket passes through gap, so as to Bubbles volume in slurries is flowed out to reduce, gas is reduced in slurries, and flowing more steady and smooth, foam volume, which is reduced, can also lift drink Material mouth sense.

2. by being set to include bucket-shaped portion and positioned at bucket-shaped subordinate portion and the tube that is attached thereto by the splitter cavity, The bucket-shaped portion of upper end can temporarily store the slurries flowed out along pulp passage, and the slurries in pulp passage can be risen To buffering drainage, slurries enter again uniformly continuous from bucket-shaped portion and are flowed out from splitter cavity lower tubular portion, avoid making without buffering There is the difficult plasma discharge phenomenon of closure in the grout outlet that the too fast liquid stream of used time flow velocity is diminished by internal diameter, in addition, splitter cavity temporarily stores During slurries, slurries are mixed in bucket-shaped portion so that the slurries solubility flowed out from the tube of lower end more uniformly, mouthfeel More preferably, and enter upper end bucket-shaped portion slurries mixing while can the tube through lower end at the uniform velocity flow continually out, keep away Exempt from direct flowing of the slurries directly between stock inlet to grout outlet, slow down flow stream velocity, slurries flow into will not in goblet Cause to splash, pulp effect is preferable, and works as slurries in splitter cavity and be overfilled with, and slurries can also be along the outside surface current in bucket-shaped portion Go out, converge to tube and flowed into along tube outer surface below slurry outlet nozzle in goblet.

3. by the inner wall mistake that the bucket-shaped portion is arranged to hemispherical or cone, hemispherical or the bucket-shaped portion of cone Cross round and smooth, without dead angle, residual slurry will not be produced, clean hygiene, and hemispherical or circle are easier to ensure that inside bucket-shaped portion The bucket-shaped portion's inner wall of splitter cavity of taper is arc surface or inclined-plane, and arc surface or inclined-plane have buffering liquid stream effect, can slow down slurry Flow velocity, prevents splash, and hemispherical or the upper port in the bucket-shaped portion of cone are opened wide, and bucket-shaped portion's opening is big compared with tube, right Liquid stream has drainage effect in pulp passage, and bucket-shaped portion causes liquid stream along splitter cavity with the tube smooth connection positioned at lower part Inner wall flowing is gentler smooth.

4. by the way that the tube is arranged to pipe, the internal wall transitions of pipe are round and smooth, without dead angle, will not produce residual Slurries are stayed, and pipe is located at the lower end of slurry outlet nozzle, and circular grout outlet is acted on more preferably confluence, flowed out via pipe Slurries pulp effect it is more preferable, be not susceptible to bifurcated or deflection.

5. by setting at least 2 ribs, the muscle between the shunting cavity outer wall and the annular sidewall of pulp passage Bar can be used for the connection for shunting cavity outer wall and annular sidewall, at least 2 ribs cause the fixation of splitter cavity more firmly, stress It is more balanced, and the rib is tilted along shunting cavity outer wall and is uniformly arranged, between shunting between cavity outer wall and annular sidewall The slurries that clearance flow goes out along splitter cavity outside wall surface and the rib confluence and under, each stock flow quantity size is identical, along outside splitter cavity Wall and the liquid stream momentum of the rib oblique flow are cancelled out each other so that liquid stream confluence along splitter cavity lower port to flow down It is dynamic, it in addition, rib has barrier effect to slurries, on the one hand can slow down liquid flowing speed, part on the other hand can be caused to pass through The slurries that rib stops enter in splitter cavity to be mixed again, and concentration of slurry is evenly；When rib quantity is less than 2, slurries edge Easily there is the deflection of liquid stream in rib flowing, and the effect for the pulp that converges is bad, and the fixed effect of splitter cavity is also undesirable.

6. the annular gap that the annular sidewall by the way that the rib to be distributed on to pulp passage is formed with shunting cavity outer wall It is interior, on the one hand, the rib is uniformly arranged so that slurries are identical from the slurries amount flowed out between two adjacent ribs, along shunting The momentum of the oblique flow of cavity outer wall face and rib outflow slurries can be balanced mutually, and the confluence effect of liquid stream is good；It is another Aspect, the rib are located in annular gap, and annular gap is carried out to be divided into multiple arcs slurry outlet groove, the sky of single slurry outlet groove Between reduce, can stop and smash the bubble passed through.

7. by setting the rib to extend to from the upper port of splitter cavity the lower port of splitter cavity, the rib and under Guide functions can be produced to the slurries that gap is flowed out between annular sidewall and shunting cavity outer wall so that slurries are outside splitter cavity Wall converges with uniformly distributed rib is tilted to the lower port of splitter cavity, and the slurries flowed downward out are more concentrated, and liquid stream bifurcated is reduced, Pulp effect is more preferable.

8. surround flow-guiding channel by rib and shunting cavity outer wall, annular sidewall, when slurry-outlet quantity in short-term is more or splitter cavity When lower port blocks, flow-guiding channel can be used as another grout outlet, and slurries both can be along after flow-guiding channel flows out Splitter cavity outside wall surface between adjacent two ribs is converged diagonally downward, can also be converged downwards in itself along rib.

9. by the way that the pipe length L is set to 1mm-8mm, pipe can be to the slurries that are flowed out out of splitter cavity pipe Guide functions straight down are produced, while converge by the pipe can also and under for the slurries flowed out along splitter cavity outside wall surface Preferably confluence effect is produced, liquid stream is avoided and is flowed directly out through grout outlet and glance off.As L ＞ 8mm, pipe length is spent Long, liquid stream, by needing the longer time, influences pulp efficiency in cylinder；Work as L<During 1mm, pipe length is too short, cylinder pair It is undesirable to flow through the vertical water conservancy diversion effect of liquid stream, the easy bifurcated of slurries or deflection.

10. by the way that the splitter cavity lower port diameter D is set to 1 mm-4 mm, it can prevent splitter cavity lower port from occurring Block, and can guarantee that the confluence effect that the efficiency of pulp and liquid stream flow downward out.As D 4 mm of ＞, liquid stream passes through under splitter cavity The improved efficiency of port, but effect of converging is poor, bifurcated easily occurs from the slurries of lower port outflow, and lower port diameter is excessive So that instantaneous delivery is too big, slurries are also easy to produce splashing；Work as D<During 1 mm, lower port diameter is small, and liquid stream is low by efficiency, and slurries In be mixed into powder particles and easily block lower port.

Brief description of the drawings

Fig. 1 is the overall structure figure of capsule beverage machine described in the utility model；

Fig. 2 is the longitudinal sectional view of one slurry outlet nozzle of the utility model embodiment；

Fig. 3 is the transverse sectional view of one slurry outlet nozzle of the utility model embodiment；

Fig. 4 is the bottom view of one slurry outlet nozzle of the utility model embodiment；

Fig. 5 is the longitudinal sectional view of another slurry outlet nozzle of the utility model embodiment one；

Fig. 6 is the longitudinal sectional view of two slurry outlet nozzle of the utility model embodiment；

Fig. 7 is the bottom view of two slurry outlet nozzle of the utility model embodiment；

Fig. 8 is the longitudinal sectional view of three slurry outlet nozzle of the utility model embodiment；

It is as follows that the names of the parts is marked in figure：

1. engine base；2. water tank；3. water receiver；4. slurry outlet nozzle；41. annular sidewall；42. pulp passage；421. epimere pulps Passage；422. hypomere pulp passages；43. stock inlet；44. grout outlet；5. splitter cavity；51. bucket-shaped portion；52. tube； 53. splitter cavity upper port；54. splitter cavity lower port；55. splitter cavity grout outlet；6. overflow launder；7. flow-guiding channel；8. muscle Bar；81. the first rib；82. the second rib；83. the 3rd rib；84. the 4th rib；85. the 5th rib；86. the 6th rib； 9. step；10. through hole.

Embodiment

Below in conjunction with drawings and the specific embodiments, the utility model is described in further detail.

Embodiment one：

As shown in Figs 1-4, the good capsule beverage machine of a kind of pulp effect described in the utility model, the capsule beverage machine For horizontal capsule beverage machine, including engine base 1, brew head, for water assembly, the cup for infusing and steeping and control unit of accommodating capsule, the punching Steep head, be arranged at for water assembly and control unit on engine base 1, it is described to provide water to brew head, the brew head for water assembly It is internally provided with into water pricker and draws pricker, draw pricker below water inlet pricker, water inlet pricker and extraction pricker can be equal Arranged on the bottom wall side of brew head, cup for infusing and steeping can be with respect to brew head transverse shifting（It can be laterally horizontal or level of approximation Form）.Water inlet pricker is used to introduce the water into soaking beverage in capsule, draws pricker and is used to brewed slurries drawing capsule, The lower part of the brew head is equipped with slurry outlet nozzle 4, and the lower section of slurry outlet nozzle 4 is equipped with water receiver 3, and the water receiver 3 can be used for putting Goblet and storage waste liquid are put, it is described to include water tank 2 and water pump for water assembly, it is described to be electrically connected for water assembly with control unit, Control unit control completes brewing for capsule for water assembly quantitative water supply, and the slurry outlet nozzle 4 includes what is surrounded by annular sidewall 41 Pulp passage 42, the stock inlet 43 positioned at 42 upper end of pulp passage and the grout outlet 44 positioned at 42 lower end of pulp passage, it is described Pulp passage 42 is cylindrical shape.

In the present embodiment, splitter cavity 5 is equipped with pulp passage 42, splitter cavity upper port 53 is opened wide, splitter cavity lower port 54 The grout outlet 44 of pulp passage 42 is stretched out, 5 outer wall of splitter cavity is connected with annular sidewall 41 and 5 outer wall of splitter cavity and annular sidewall 41 Between be equipped with gap.The advantages of this arrangement are as follows splitter cavity 5 can carry out temporarily the slurries flowed out along pulp passage 42 Storage, slurries can further mix in splitter cavity 5 so that the slurries solubility of outflow splitter cavity 5 more uniformly, mouthfeel more Well, it can at the uniform velocity be flowed out through splitter cavity grout outlet 55 while and mixing into the slurries in splitter cavity 5, avoid and flow in short-term Slurries excessively cause 55 instantaneous slurry-outlet velocity of splitter cavity grout outlet too fast in into pulp passage 42 so that slurries are flowed into goblet Cause to splash, cause scald or stained desktop；Slurry-outlet quantity is more in short-term or splitter cavity grout outlet 55 is blocked when being unable to pulp, shunting Gap between 5 outer wall of chamber and annular sidewall 41 can be used as another grout outlet, and the slurries that gap is overflowed can be along shunting 5 outer wall of chamber flows downward out；In addition, the gap also has the function that to carry out air circulation, slurry outlet nozzle 4 and outside air with the external world Circulation can reduce negative pressure, reduce the generation of bubble in slurries, and slurries flow through 5 outer wall of splitter cavity and annular sidewall 41 it Between gap when, air pocket can be squeezed and broken, it is possible to reduce outflow slurries in bubbles volume, liquid stream outflow uniformly continuous, bubbles volume reduce Beverage mouthfeel can be lifted.

In the present embodiment, the splitter cavity 5 includes bucket-shaped portion 51 and positioned at bucket-shaped 51 lower part of portion and the tubulose being attached thereto Portion 52, the bucket-shaped portion 51 are located in pulp passage 42, and the tube 52 stretches out the grout outlet 44 of pulp passage 42, upper end Bucket-shaped portion 51 can temporarily store the slurries flowed out along pulp passage 42, and the slurries in pulp passage 42 can be risen To buffering drainage, slurries enter again uniformly continuous from bucket-shaped portion 51 and are flowed out from splitter cavity lower tubular portion 52, avoided without slow There is the difficult plasma discharge phenomenon of closure in the grout outlet that the too fast liquid stream of flow velocity is diminished by internal diameter when punching acts on, and slurries can be in bucket-shaped portion Mixed in 51 so that flow out the slurries solubility of the tube 52 of lower end more uniformly, mouthfeel it is more preferable, and enter upper end The slurries in bucket-shaped portion 51 can at the uniform velocity flow out while mixing through the tube 52 of lower end, avoid upper end stock inlet 43 with End grout outlet 44 directly circulates, and outflow slurries are excessive in short-term, slurry-outlet velocity is too fast, and slurries flow into cup body and will not cause to splash, Pulp effect is preferable, and works as slurries in splitter cavity and be overfilled with, and slurries can also be flowed out along the lateral surface in bucket-shaped portion 51, convergence Flowed into tube 52 and along 52 outer surface of tube in 4 lower section goblet of slurry outlet nozzle.

In the present embodiment, the bucket-shaped portion 51 is hemispherical, and the internal wall transitions in the bucket-shaped portion 51 of hemispherical are round and smooth, without dead Angle, will not produce residual slurry, and clean hygiene, and the liquid storage cylinder of hemispherical or cone are easier to ensure that inside bucket-shaped portion 51 Inner wall is arc surface, and arc surface has buffering liquid stream effect, can slow down slurry flow rate, prevent splash, and hemispherical is bucket-shaped The upper port in portion is opened wide, and bucket-shaped portion's opening is big compared with tube, has drainage effect, bucket-shaped portion and position to liquid stream in pulp passage 42 Tube in lower part is in smoothing junction so that liquid stream is gentler smooth along the flowing of shunting cavity wall.

In the present embodiment, the tube 52 is pipe, and the internal wall transitions of pipe are round and smooth, without dead angle, will not be produced residual Slurries are stayed, and pipe is located at the lower end of slurry outlet nozzle 4, and circular grout outlet is acted on more preferably confluence, via Pipe Flow The slurries pulp effect gone out is more preferable.The pipe length is L, wherein 1mm≤L≤8mm, and pipe can be to from 5 pipe of splitter cavity The slurries of interior outflow produce guide functions straight down, while the slurries flowed out along 5 outside wall surface of splitter cavity pass through the pipe Confluence and it is lower can also produce effect of preferably converging, avoid liquid stream and flowed directly out through grout outlet 44 and glance off, this implementation Example is 4mm, the advantages of this arrangement are as follows, it can both ensure preferable water conservancy diversion effect, product cost can also be controlled.Described point Flow 55 a diameter of D of chamber grout outlet, wherein 1 mm≤D≤4 mm, can prevent splitter cavity grout outlet 55 block and The confluence effect that the efficiency and liquid stream of pulp flow downward out, the present embodiment 2mm, the advantages of this arrangement are as follows, both it can guarantee that Preferable pulp effect, and product cost can be controlled.

In the present embodiment, at least 2 ribs are equipped between the annular sidewall 41 of 5 outer wall of splitter cavity and pulp passage 42 8, the present embodiment is 6, and the rib 8 can be used for the connection of 5 outer wall of splitter cavity and annular sidewall 41, and at least 2 ribs 8 make Splitter cavity 5 fixation more firmly, stress it is more balanced, and the rib 8 along 5 outer wall of splitter cavity tilt be uniformly arranged, The slurries flowed out through the gap between 5 outer wall of splitter cavity and annular sidewall 41 converge along 5 outside wall surface of splitter cavity and the rib 8 Under and, each stock flow quantity size is identical, cancels out each other along the liquid stream momentum of 8 oblique flow of 5 outside wall surface of splitter cavity and the rib, So that liquid stream confluence flows downward along splitter cavity lower port 54, in addition, rib 8 has barrier effect to slurries, on the one hand may be used To slow down liquid flowing speed, it on the other hand can cause slurries of the part through the stop of rib 8 enter in splitter cavity 5 to mix again, starch Liquid concentration is evenly.The rib 8 is distributed on the annular gap that the annular sidewall 41 of pulp passage 42 is formed with 5 outer wall of splitter cavity It is interior, on the one hand, the rib 8 is uniformly arranged so that slurries are identical from the slurries amount flowed out between two adjacent ribs 8, and edge is divided The momentum for the oblique flow that stream 5 outside wall surface of chamber and the rib 8 flow out slurries can be balanced mutually, and the confluence effect of liquid stream is good； On the other hand, the rib 8 is located in annular gap, and annular gap is carried out to be divided into multiple arcs slurry outlet groove, single pulp The space of groove reduces, and can stop and smash the bubble passed through.

In the present embodiment, the rib 8 from splitter cavity upper port 53 and under extend to splitter cavity lower port 54, the rib 8 upper ends are concordant with splitter cavity upper port 53, and the rib 8 is connected with annular sidewall 41, and the rib 8 is to annular sidewall The slurries that gap is flowed out between 41 and 5 outer wall of splitter cavity produce guide functions so that slurries are along 5 outside wall surface of splitter cavity and inclination Uniformly distributed rib 8 converges to 5 lower port 54 of splitter cavity, and the slurries flowed downward out are more concentrated, and liquid stream bifurcated is reduced, pulp effect More preferably.Adjacent two ribs 8 and 5 outer wall of splitter cavity, the annular sidewall 41 of pulp passage 42 surround flow-guiding channel 7, rib 8 with 41 integrated injection molding of annular sidewall of 5 outer wall of splitter cavity, pulp passage 42, when slurry-outlet quantity in short-term is more or splitter cavity grout outlet During 55 blocking, flow-guiding channel 7 can be used as another pulp passage 42.The rib 8 is extended downwardly along splitter cavity lower port 54 And along the radial setting of bucket-shaped 51 outside wall surface of portion, the muscle of the radial setting of bucket-shaped 51 outside wall surface of portion centered on tube 52 Bar connects one to one with bucket-shaped 51 top rib of portion, and slurries both can be along adjacent two ribs 8 after the outflow of flow-guiding channel 7 Between 5 outside wall surface of splitter cavity converge diagonally downward, can also converge along the rib of radial setting to tube 52.

In the present embodiment, annular gap is overflow launder 6 between 5 outer wall of annular sidewall 41 and splitter cavity of pulp passage 42, 6 width of overflow launder is A, wherein 0.5 mm≤A≤4 mm, the overflow launder 6 at the top of liquid storage cylinder with 42 side of pulp passage Gap between wall, on the one hand so setting can ensure that overflow launder 6 can realize the function of discharge opeing and ventilation, on the other hand may be used To ensure that liquid storage cylinder has enough liquid storage spaces, realize and the caching of slurries in pulp passage 42 is acted on so that liquid stream can be with Uniformly, continuously flowed out from grout outlet, the present embodiment 2mm, can both ensure drainage and the shunting function of splitter cavity 5, also may be used To control the relative size size of pulp passage 42 and splitter cavity 5.

It should be understood that in the internal face of splitter cavity 5, and block reinforcement, the gear are equipped with the position opposite with flow-guiding channel 7 Muscle can form certain barrier effect to the liquid stream for entering splitter cavity 5 so that more liquid streams can be flowed from flow-guiding channel 7 Go out, reduce the flow quantity in splitter cavity 5, slurries outflow is more efficient, can keep temperature and the nutrition of slurries, the beverage of preparation Mouthfeel is more preferably.

It should be understood that water inlet pricker can be arranged on the bottom wall of brew head, the side wall that pricker is arranged on brew head is drawn.

It should be understood that the bucket-shaped portion 51 is cone, there are preferable drainage and slurries to delay in conical bucket-shaped portion Rush effect.

It should be understood that the capsule beverage machine is vertical capsule beverage machine, the brew head is internally provided with into water pricker, It is equipped with the cup for infusing and steeping and draws pricker, the central axis of capsule is vertically arranged, i.e. the vertical placement of capsule, coordinates different capsules to make With extraction pricker can not also be set in the cup for infusing and steeping, the pulp passage 42 that brewed slurries are directly set from capsule bottom Slurry outlet nozzle 4 is exited into, since the structure of above-mentioned capsule beverage machine has been existing structure, is just no longer repeated one by one here.

It should be understood that can equipped with 8 quantity of rib between 5 outer wall of splitter cavity and the annular sidewall 41 of pulp passage 42 To be 2,3,4,5,7,8 etc..

It should be understood that the 6 width A of overflow launder can be 0.5 mm, 1mm, 1.5mm, 2.5mm, 3mm, 3.5mm, 4 Mm etc..

It should be understood that as shown in figure 5, the rib upwardly extends along bucket-shaped portion's outer wall and is higher by the bottom of pulp passage Wall, the part that the rib is higher by bucket-shaped portion's upper port are connected with annular sidewall 41, are higher by the rib of bucket-shaped portion's upper port part The slurries flowed through in the slurries or pulp passage that can be overflowed to splitter cavity produce drainage so that what slurries can be smooth is logical The flow-guiding channel 7 crossed between splitter cavity and annular sidewall flows out.

Embodiment two：

The difference between this embodiment and the first embodiment lies in part rib 8 is not connected with the annular sidewall 41 of pulp passage 42.

As shown in Figure 6 and Figure 7, rib 8 includes 6 ribs, wherein the first rib 81, the 3rd rib 83 and the 5th rib 85 Connected with 42 annular sidewall 41 of pulp passage, the second rib 82, the 4th rib 84 and the 6th rib 86 and pulp passage 42 Gap is equipped between annular sidewall 41.Connected by setting a part of rib 8 with 42 side wall of pulp passage, it is another The part rib 8 is set gap between 42 side wall of pulp passage, so sets the gap that can have both increased overflow launder 6 empty Between so that slurries outflow is more efficient, it is also ensured that through overflowing the slurries of groove outflow along liquid storage cavity outer wall and rib 8 to pulp The confluence effect of mouth direction flowing.The unaccounted structure of other in the present embodiment and effect are identical with embodiment one, herein no longer Repeat.

Embodiment three：

The difference between the present embodiment and the second embodiment lies in that the structure of pulp passage 42 is different.

As shown in figure 8, the pulp passage 42 includes two sections, epimere pulp passage 421 is cylindrical, hypomere pulp The diameter of passage 422 is big compared with epimere pulp passage 421, and upper end is cylindrical shape, and lower end is hemispherical, hypomere pulp passage 422 Lower port to central reduction formed necking, the bucket-shaped portion 51 of splitter cavity is located at the necking, and bucket-shaped portion upper end is located at Starch in passage 3, bucket-shaped subordinate end and tube 52 stretch out pulp passage 3, and the inside of hypomere pulp passage 422 can be right for infundibulate The slurries that splitter cavity is overflowed have conflux and memory action, and the upper-lower section junction of pulp passage 3 is because of internal diameter formation of different sizes Step 9, is equipped with through hole 10 at step 9, and slurry outlet nozzle 4 is equipped with opening in many places diverse location, and the structure of pulp and ventilation is more, goes out Starching mouth 4 has more preferably pulp effect, even if ororrhea goes out inside splitter cavity, between 5 outer wall of annular sidewall 41 and splitter cavity Through hole 10 can also realize the purpose of plasma discharge and ventilation at overflow launder 6 and step 9.The pipe length L is 2mm, because bucket-shaped Subordinate end and tube 52 stretch out pulp passage 3, and the bucket-shaped portion 51 of splitter cavity 5 itself can produce certain water conservancy diversion to slurries and make With, thus pipe length need not set it is long.The 55 diameter D of splitter cavity grout outlet is 3mm, big because of the splitter cavity 5 Part-structure stretches out pulp passage 3, and the size that the size of splitter cavity grout outlet 55 needs to reach certain just can guarantee that splitter cavity 5 Drainage effect.Rib 8 along splitter cavity outside wall surface set, the rib 8 from splitter cavity upper port 53 and under extend to splitter cavity Lower port 54,8 upper end of rib is concordant with splitter cavity upper port 53, and the lower end of the rib 8 and hypomere pulp passage 422 Necking connects, and the rib 8 had both had drainage and confluence effect, and the structure that can also strengthen the bucket-shaped portion 51 of splitter cavity is strong Degree.The complete machine of capsule beverage machine and other unaccounted structures and effect of slurry outlet nozzle are identical with embodiment two in the present embodiment, this Place repeats no more.

It should be understood that the rib 8 from splitter cavity upper port 53 and under extend to the grout outlet of hypomere pulp passage 422 Place, the rib 8 is used for the connection of splitter cavity 5 and annular sidewall 41, and has and draw the slurries overflowed in splitter cavity 5 downwards The effect gone out.

As described above, is only the preferred embodiment of the utility model, is not used for limiting the reality of the utility model Apply scope, i.e., all equivalent changes and modifications made according to the utility model, are all that the utility model claims scope is covered, Here no longer illustrate one by one.

Claims (10)

1. a kind of good capsule beverage machine of pulp effect, including engine base, brew head, for water assembly, accommodating capsule cup for infusing and steeping and Control unit, the brew head, be arranged on engine base for water assembly and control unit, and described provided water to for water assembly brews Head, described to be electrically connected for water assembly with control unit, the lower part of the brew head is equipped with slurry outlet nozzle, and the slurry outlet nozzle is included by ring Pulp passage, the stock inlet positioned at pulp passage upper end and the grout outlet positioned at pulp passage lower end that shape side wall surrounds, its It is characterized in that：Splitter cavity is equipped with pulp passage, splitter cavity upper port is opened wide, and lower port stretches out the grout outlet of pulp passage, point Stream cavity outer wall and annular sidewall connect and are equipped with gap between shunting cavity outer wall and annular sidewall.

A kind of 2. good capsule beverage machine of pulp effect according to claim 1, it is characterised in that：The splitter cavity includes bucket Shape portion and positioned at the bucket-shaped subordinate portion and the tube that is attached thereto.

A kind of 3. good capsule beverage machine of pulp effect according to claim 2, it is characterised in that：The bucket-shaped portion is hemisphere Shape or cone.

A kind of 4. good capsule beverage machine of pulp effect according to claim 2, it is characterised in that：The tube is circle Pipe.

A kind of 5. good capsule beverage machine of pulp effect according to claim 1, it is characterised in that：It is described shunting cavity outer wall with At least 2 ribs are equipped between the annular sidewall of pulp passage.

A kind of 6. good capsule beverage machine of pulp effect according to claim 5, it is characterised in that：The rib is distributed on out Starch in the annular sidewall of passage and the annular gap of shunting cavity outer wall formation.

A kind of 7. good capsule beverage machine of pulp effect according to claim 5, it is characterised in that：The rib is from splitter cavity Upper port and under extend to the lower port of splitter cavity.

A kind of 8. good capsule beverage machine of pulp effect according to claim 7, it is characterised in that：Outside rib and splitter cavity Wall, annular sidewall surround flow-guiding channel.

A kind of 9. good capsule beverage machine of pulp effect according to claim 4, it is characterised in that：The pipe length is L, Wherein 1mm≤L≤8mm.

A kind of 10. good capsule beverage machine of pulp effect according to claim 4, it is characterised in that：The splitter cavity lower end Mouthful a diameter of D, wherein 1 mm≤D≤4 mm.