CN207535138U - A kind of multigroup part of mixing arrangement - Google Patents
A kind of multigroup part of mixing arrangement Download PDFInfo
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- CN207535138U CN207535138U CN201721288590.8U CN201721288590U CN207535138U CN 207535138 U CN207535138 U CN 207535138U CN 201721288590 U CN201721288590 U CN 201721288590U CN 207535138 U CN207535138 U CN 207535138U
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- 238000010992 reflux Methods 0.000 claims description 55
- 230000003014 reinforcing effect Effects 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 13
- 238000007789 sealing Methods 0.000 claims description 12
- 239000002994 raw material Substances 0.000 abstract description 63
- 238000000034 method Methods 0.000 abstract description 13
- 239000000203 mixture Substances 0.000 description 10
- 238000010586 diagram Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
Abstract
The utility model is related to multigroup part of mixing arrangements, including level-one mixing arrangement and two level mixing arrangement, at least two feed inlets of the level-one mixing arrangement are connect with the mixing discharge port of the level-one mixing arrangement, and the mixing discharge port of the level-one mixing arrangement is connect with the feed inlet of the two level mixing arrangement.Multigroup part of mixing arrangement provided by the utility model makes the process that raw material is sprayed after start to mixing very fast.
Description
Technical field
The utility model is related to a kind of real-time mixing arrangements of large scale for being used for multigroup part.Specifically, the utility model
Subject matter be a kind of device of at least two liquid components in Mixture of multiple components wet application system.
Background technology
In the industrial production, often multigroup part of large scale difference raw material is mixed, since large scale difference raw material directly mixes
Well-mixed requirement is extremely difficult to, therefore traditional hybrid mode is is then transferred to another appearance after being pre-mixed in a vessel
The mode being thoroughly mixed in device, this mode is more using container, and mixed process is more complicated, makes raw material from starting mixing
After the process that sprays it is slower.
Utility model content
Therefore, the utility model provides a kind of multigroup part of mixing arrangement, to solve the above problems.The multigroup part of response type
Raw material can be following raw material：Resin, waterproof, anti-corrosion, thermal insulation material etc..
The technical solution of the utility model is：Including level-one mixing arrangement and two level mixing arrangement, the level-one mixing dress
At least two feed inlets put are connect with the mixing discharge port of the level-one mixing arrangement, and the level-one mixing arrangement blends
Material mouth is connect with the feed inlet of the two level mixing arrangement.
Optionally, the level-one mixing arrangement is provided at least two feed inlets and the mixing connected with feed inlet discharging
Mouthful；The mixing discharge port that the two level mixing arrangement is provided at least two feed inlets and is connected with feed inlet；The level-one is mixed
The mixing discharge port put is attached together to connect with the feed inlet of the two level mixing arrangement.
Optionally, the level-one mixing arrangement is additionally provided with the refluxing opening coordinated respectively with feed inlet, the refluxing opening with
Piston is provided between the feed inlet, the piston is connected with driving device；The two level mixing arrangement is additionally provided with difference
With the refluxing opening of feed inlet cooperation, piston is provided between the refluxing opening and the feed inlet, the piston is connected with driving
Device.
Optionally, auxiliary mixing device is installed between the level-one mixing arrangement and the two level mixing arrangement；It is described
The mixing discharge port of two level mixing arrangement is connected with auxiliary mixing device；
Pressure regulator is installed on the feed inlet of the level-one mixing arrangement；
Pressure regulator is installed on the feed inlet of the two level mixing arrangement.
Optionally, three-level mixing device is further included, the three-level mixing device is provided at least two feed inlets, with feeding
The mixing discharge port of mouth connection and the respectively refluxing opening with feed inlet cooperation, are provided between the refluxing opening and the feed inlet
Piston, the piston are connected with driving device；The mixing discharge port of the two level mixing arrangement and the three-level mixing device
Feed inlet connects.
Optionally, plug is installed on the refluxing opening of the two level mixing arrangement；The refluxing opening of the three-level mixing device
On plug is installed.
Optionally, plug is installed on the refluxing opening of the two level mixing arrangement；The refluxing opening of the three-level mixing device
On plug is installed；The quantity of the level-one mixing arrangement is identical with the quantity of the feed inlet of the two level mixing arrangement, described
Feed inlet of the discharge port of level-one mixing arrangement respectively with the two level mixing arrangement is connect.
Optionally, pressure regulator is installed on the feed inlet of the level-one mixing arrangement；The two level mixing arrangement
Pressure regulator is installed on feed inlet.
Optionally, be longitudinally provided with reinforcing prop between the feed inlet and the discharge port, on the reinforcing prop by up to
Under multiple semi-spiral pieces are installed, the top of the semi-spiral piece is located at the side of the feed inlet, the bottom of the semi-spiral piece
End is located at the side of mixing discharge port.
Optionally, channel is formed between the feed inlet and the discharge port, the top setting of the channel is fluted；Institute
It is inclined that groove, which is stated, close to the side of the discharge port, and the distance L1 of bottom end to discharge port is less than top to the distance of discharge port
L2；Elastic diaphragm is installed, the elastic diaphragm is inclined, and the height of the bottom end of the elastic diaphragm is less than in the groove
The height on the top of the elastic diaphragm.
Optionally, piston channel is provided in the level-one mixing arrangement, the piston channel longitudinally runs through the level-one
Mixing arrangement；The piston is connect by piston rod with driving device, has spacing between the piston rod and the piston channel；
Sealing piston is additionally provided on the piston rod, the sealing piston is located at the top of the refluxing opening；The two level mixing dress
It puts and is provided with piston channel, the piston channel longitudinally runs through the two level mixing arrangement；The piston by piston rod with
Driving device connects, and has spacing between the piston rod and the piston channel；Sealing piston is additionally provided on the piston rod,
The sealing piston is located at the top of the refluxing opening.
Using Fig. 1 and Fig. 2 as row, which is：By the raw material A of large scale be divided into suitable two parts A1 and
A2, A1 and the raw material B of small scale are transported to the feed inlet of level-one mixing arrangement by high-pressure pump, and two kinds of raw materials are in the state of high pressure
Lower head-on collision mixing, is mixed into raw material A 1+B, is then supplied to the feed inlet of two level mixing arrangement, A2 is equally defeated by high-pressure pump
Another feed inlet of two level mixing arrangement is sent to, mixing of clashing under high pressure conditions is realized, ensure that mixing uniformity, continue to fill
Divide and be mixed into raw material A 1+A2+B, be then supplied to working end.It is the working condition of two-component two level mixing arrangement as shown in Figure 1；
Control level-one mixing arrangement piston downwards operation be stopped end work when, refluxing opening is connected with feed inlet, one
Grade mixing arrangement stops the mixing of raw material A 1 and B, and the two starts to flow back according to respective path, is simultaneously stopped to two level and mixes dress
Put supply mixture A1+B；The piston of similary control two level mixing arrangement is run downwards, and A2 starts also according to the path of oneself
Reflux, to block, the mixture of level-one mixing arrangement is rested in pipeline to be continued to supply another refluxing opening when waiting for work next time
Material.It is illustrated in figure 2 the stop working state of two-component two level mixing arrangement.
Multigroup part of mixing arrangement provided by the utility model can be completed raw material using a device and mix, eliminate and turn
The process of container is changed, mixed process is relatively easy, makes the process that raw material is sprayed after start to mixing very fast.It is in addition, logical
Cross setting refluxing opening, can stop in the case where not closing high-pressure pump mixing, without it is every mixing will once open and
Closing high-pressure pump is primary, is particularly suitable for needing frequently the interim situation for stopping mixing.
Description of the drawings
Fig. 1 is a kind of two-component two level mixing arrangement working state schematic representation provided by the utility model；
Fig. 2 is a kind of two-component two level mixing arrangement stop working state schematic diagram provided by the utility model；
Fig. 3 is a kind of two-component three-level mixing device structure diagram provided by the utility model；
Fig. 4 is a kind of three components three-level mixing device structure diagram provided by the utility model；
Fig. 5 is the mounting structure schematic diagram of the reinforcing prop of the utility model；
Fig. 6 is the mounting structure schematic diagram of the elastic diaphragm of the utility model；
Fig. 7 is the mounting structure schematic diagram of the piston of the utility model.
Specific embodiment
The technical solution of the utility model is described in detail below in conjunction with the accompanying drawings.
Embodiment 1, the utility model provide a kind of two-component two level mixing arrangement, referring to Fig. 1-Fig. 2, are mixed including level-one
It attaches together to put and two level mixing arrangement, the level-one mixing arrangement is provided with feed inlet 11, feed inlet 12 and feed inlet 11 and charging
The mixing discharge ports 13 of 12 connection of mouth and the refluxing opening 14 and refluxing opening 15 coordinated respectively with feed inlet 11, feed inlet 12, institute
It states and piston 16 is provided between refluxing opening 14 and refluxing opening 15 and the feed inlet 11 and feed inlet 12, the piston is connected with drive
Dynamic device 1611, driving device can use existing driving device, such as linear motor, hydraulic stem etc., be typically secured to one
On grade mixing arrangement；The structure of two level mixing arrangement is identical with the structure of level-one mixing arrangement, referring to Fig. 1 and Fig. 2, the two level
Mixing arrangement be provided with feed inlet 112, feed inlet 122, the mixing discharge port 132 that is connected with feed inlet 112 and feed inlet 122 with
And the refluxing opening 142 and refluxing opening 152 with feed inlet cooperation respectively, the refluxing opening 142 and 152 and the feed inlet 112 and
Piston 162 is provided between feed inlet 122, the piston is connected with driving device 1612；The mixing of the level-one mixing arrangement
Discharge port 13 is connect with the feed inlet 122 of the two level mixing arrangement, is equipped on the refluxing opening 152 of the two level mixing arrangement
Plug.
The device operation principle is：The raw material A of large scale is divided into suitable two parts A1 and the original of A2, A1 and small scale
Material B is transported to the feed inlet 11 of level-one mixing arrangement and feed inlet 12 by high-pressure pump, and two kinds of raw materials are right in the state of high pressure
Mixing is hit, is mixed into raw material A 1+B, is then supplied to the feed inlet 122 of two level mixing arrangement, A2 is equally defeated by high-pressure pump
Another feed inlet 112 of two level mixing arrangement is sent to, mixing of clashing under high pressure conditions is realized, ensure that mixing uniformity, after
It is continuous to be sufficiently mixed into raw material A 1+A2+B, it is then supplied to working end 21.It is the work of two-component two level mixing arrangement as shown in Figure 1
Make state；
Control level-one mixing arrangement the operation downwards of piston 16 be stopped 21 work of end when, refluxing opening 14 and refluxing opening 15
It is connected with feed inlet 11 and feed inlet 12, level-one mixing arrangement stops the mixing of raw material A 1 and B, and the two is opened according to respective path
Begin to flow back, raw material is made to return to original place, be simultaneously stopped to two level mixing arrangement supply mixture A1+B；Similary control two level mixing dress
The piston 162 put is run downwards, and A2 starts to flow back also according to the path of oneself, another refluxing opening 152 be closure, level-one
The mixture of mixing arrangement is rested in pipeline to be continued to be fed when waiting for work next time.It is illustrated in figure 2 the mixing of two-component two level
The stop working state of device.Certainly, another refluxing opening 152 can also connect collection device with spare.
In order to improve mixing efficiency and uniformly mixed degree, the level-one mixing arrangement and the two level mixing arrangement it
Between auxiliary mixing device 19 is installed, general auxiliary mixing device 19 is installed on the mixing discharge port 13 of level-one mixing arrangement
On, auxiliary mixing device can be connect by pipeline 20 with the feed inlet 122 of the two level mixing arrangement；The two level mixing dress
The mixing discharge port 132 put is connected with auxiliary mixing device 192.In the application, feed rate is adjusted for convenience, is mixed in level-one
It attaches together the feed inlet 11 put and is also equipped with pressure regulator 17 and pressure regulator 18 on feed inlet 12；Place two level is mixed
It attaches together the feed inlet 112 put and pressure regulator 172 and pressure regulator 182 is installed on feed inlet 122, pressure regulator can
To use existing pressure regulator.It is preferable to use static mixer formula power blenders for above-mentioned auxiliary mixing device.
As a preferred mode, referring to Fig. 7, piston channel 26, the work are provided in the level-one mixing arrangement
It fills in channel and longitudinally runs through the level-one mixing arrangement；The piston 16 is connect by piston rod 27 with driving device 1611, described
There is spacing between piston rod and the piston channel；Sealing piston 28, the sealing piston position are additionally provided on the piston rod
In the top of the refluxing opening 14,15 to prevent raw material from revealing；The structure of two level mixing arrangement and the structure of level-one mixing arrangement
It is identical, i.e., piston channel is provided on described two level mixing arrangement, the piston channel longitudinally runs through the two level mixing arrangement；
The piston 162 is connect by piston rod with driving device 1612, has spacing between the piston rod and the piston channel；Institute
It states and sealing piston is additionally provided on piston rod, the sealing piston is located at the top of the refluxing opening 142,152.
As a kind of deformation, the feed inlet of above-mentioned level-one mixing arrangement and two level mixing arrangement can also be arranged to more
It is a.
Embodiment 2, embodiment 2 is identical with the principle of embodiment 1, and only increasing three-level on the basis of embodiment 1 mixes
It attaches together and puts, referring to Fig. 3, the structure of three-level mixing device is identical with level-one mixing arrangement, that is, the three-level mixing device is provided with
Feed inlet 113 and feed inlet 123, the mixing discharge port 133 connected with feed inlet 113 and feed inlet 123 and respectively with charging
The refluxing opening 143 and refluxing opening 153, the refluxing opening 143 and refluxing opening 153 and the charging that mouth 113 and feed inlet 123 coordinate
Piston 163 is provided between mouth 113 and feed inlet 123, the piston is connected with driving device 1613；
The mixing discharge port 132 of the two level mixing arrangement is connect with the feed inlet 123 of the three-level mixing device, described
Plug is installed on the refluxing opening 153 of three-level mixing device.
The device operation principle is：The raw material A of large scale is divided into suitable three parts A1, A2 and A3, first by A1 and
The raw material B of small scale is transported to the feed inlet 11 of level-one mixing arrangement and feed inlet 12 by high-pressure pump, and two kinds of raw materials are in high pressure
In the state of clash mixing, be mixed into raw material A 1+B, be then supplied to the feed inlet 122 of two level mixing arrangement, A2 is similary
Another feed inlet 112 of two level mixing arrangement is transported to by high-pressure pump, continues to be sufficiently mixed into raw material A 1+ in the same way
A2+B, then mixed raw material A1+A2+B is supplied to same series system the feed inlet 123 of three-level mixing device, A3 is similary
Another feed inlet 113 of three-level mixing device is transported to by high-pressure pump, realizes to clash under high pressure conditions in the same way and mix
Close, continue to be sufficiently mixed into raw material A 1+A2+A3+B, be then supplied to working end 21, be achieved the raw material A of large scale with
The raw material B of small scale is in due course, is sufficiently mixed.It is illustrated in figure 3 the working condition of two-component three-level mixing device；Stopped process
Identical with the principle of two-component two level mixing arrangement, details are not described herein again.Certainly, another refluxing opening 153 can also connect receipts
Acquisition means are with spare.
Similarly, in order to improve mixing efficiency and uniformly mixed degree, the two level mixing arrangement and the three-level mix
Auxiliary mixing device 192 is installed, general auxiliary mixing device is installed on the mixing discharging of two level mixing arrangement between device
On mouth 13, auxiliary mixing device can be connect by pipeline 20 with the feed inlet 123 of the three-level mixing device；The three-level is mixed
It attaches together the mixing discharge port 132 put and is connected with auxiliary mixing device 193.In the application, feed rate is adjusted for convenience, two
Pressure regulator 172 and pressure regulator 182 are also equipped on the grade feed inlet 112 of mixing arrangement and feed inlet 122；Institute
Pressure regulator 173 and pressure regulator 183, pressure are installed on the feed inlet 113 of three-level mixing device and feed inlet 123
Adjuster can use existing pressure regulator.
Embodiment 3, embodiment 3 is that level-one mixing arrangement is increased on the basis of embodiment 2, referring to Fig. 4, the two level
Plug is installed on the refluxing opening 142 of mixing arrangement and refluxing opening 152；It is installed on the refluxing opening 153 of the three-level mixing device
There is plug；The quantity of the level-one mixing arrangement is identical with the quantity of the feed inlet of the two level mixing arrangement, and level-one is mixed herein
It is two to attach together the quantity put, the discharge ports 13 of two level-one mixing arrangements respectively with two two level mixing arrangements
Feed inlet 112 and feed inlet 122 connect.
The operation principle of the device is：The raw material A of large scale is divided into suitable three parts A1, A2 and A3, first by A1
With the raw material B of small scale the feed inlet 11 of a level-one mixing arrangement and feed inlet 12, two kinds of raw materials are transported to by high-pressure pump
It clashes and mixes in the state of high pressure, be mixed into raw material A 1+B, be then supplied to the feed inlet 122 of two level mixing arrangement；
The A2 and raw material C of small scale is transported to the feed inlet 11 and feed inlet of another level-one mixing arrangement by high-pressure pump simultaneously
12, two kinds of raw materials clash mixing in the state of high pressure, are mixed into raw material A 2+C, are then supplied to two level mixing arrangement
Feed inlet 112；A1+B and A2+C continuation is sufficiently mixed into raw material A 1+A2+B+C in the same way in two level mixing arrangement,
It is then supplied to the feed inlet 123 of three-level mixing device；A3 is equally transported to the another of three-level mixing device by high-pressure pump at this time
A feed inlet 113 continues to be sufficiently mixed into raw material A 1+A2+A3+B+C in the same way, is then supplied to working end 21, this
Sample realize large scale raw material A and small scale raw material B and C in due course, be sufficiently mixed.It is illustrated in figure 4 three component three-levels
The working condition of mixing arrangement.
In the application, applicant has also done following design, referring to Fig. 5, the feed inlet 11 and feed inlet 12 with it is described go out
Reinforcing prop 22 is longitudinally provided between material mouth 13, multiple semi-spiral pieces are from top to bottom installed on the reinforcing prop, it is described herein
Semi-spiral piece, that is, flight half, that is, reinforcing prop longitudinally has half to be equipped with flight in figure, it can be understood as
Reinforcing prop removes the flight of side after installing flight, and the top of the semi-spiral piece on one of reinforcing prop is located at institute
The side of feed inlet 11 is stated, positioned at the side of mixing discharge port 13, the top of the semi-spiral piece on another reinforcing prop is located at institute
The side of feed inlet 12 is stated, bottom end is located at the side of mixing discharge port 13, and this structure is passed through in the A1 and raw material B of small scale
After high-pressure pump is transported to the feed inlet 11 of level-one mixing arrangement and feed inlet 12, when the two flows separately through reinforcing prop, it is reinforced column
And bump against after the dispersion of semi-spiral piece, so as to be more advantageous to mixing, in addition, the semi-spiral piece on two reinforcing props will flow the original passed through
Material water conservancy diversion is all interpenetrated into during the shock of both semi-spiral shapes and after hitting in rotation status, has agitaion to other side,
The mixing of the two is more advantageous to, further, since the top of the semi-spiral piece on one of reinforcing prop is located at the feed inlet 11
Side, bottom end is located at the side of mixing discharge port 13, and the top of the semi-spiral piece on another reinforcing prop is located at the charging
Mouthfuls 12 side, bottom end are located at the side of mixing discharge port 13, in this way can by the raw material flowed through semi-spiral water conservancy diversion from top to bottom,
Be conducive to improve the flow velocity of raw material, shorten the stroke of small part raw material.
In the application, applicant has also done following design, referring to Fig. 6, the feed inlet 11 and feed inlet 12 with it is described go out
Channel 231, the top setting fluted 24 of the channel are formed between material mouth 13；The groove is close to the side of the discharge port
To be inclined, angle of inclination generally may be configured as 30-60 degree, the distance L1 of bottom end to discharge port be less than top to discharge port away from
From L2；Elastic diaphragm 25 is installed, elastic diaphragm can be with the diaphragm of the materials such as rubber, silica gel making, institute in the groove
It is inclined to state elastic diaphragm, and angle of inclination generally may be configured as 30-60 degree, and the height of the bottom end of the elastic diaphragm is less than institute
State the height on the top of elastic diaphragm.This structure is conducive to protect high-pressure pump, specifically, in work when stopping raw material mixing
During plug moves downward, certain obstruction can be formed to channel 231, at this point, the raw material of high-pressure pump conveying can the elasticity of compression
Diaphragm makes it be deformed to inside grooves, alleviates the pressure of high-pressure pump to a certain extent, is conducive to protect high-pressure pump, in addition,
During raw material mixes, there is the mistake of of short duration extraction external feed after pressurizeing due to high-pressure pump (especially piston pump)
Journey is not to compress raw material always, and in the process, elastic diaphragm has very of short duration compression and becomes larger the process of diminution, and then
It constantly vibrates, pushes and pulls raw material, so as to make that fluctuation is generated in material flow, be more advantageous to the mixing of raw material；When pushing and pulling raw material
Coordinate the agitation of semi-spiral piece again, be more advantageous to the mixing of raw material.
Multigroup part of mixing arrangement provided by the utility model can be completed raw material using a device and mix, eliminate and turn
The process of container is changed, mixed process is relatively easy, makes the process that raw material is sprayed after start to mixing very fast, in addition, logical
Cross setting refluxing opening, can stop in the case where not closing high-pressure pump mixing, without it is every mixing will once open and
Closing high-pressure pump is primary, is particularly suitable for needing frequently the interim situation for stopping mixing.
It should be noted that according to production needs, the three-level mixing device can also be continued to connect in the form of connecting
The feed inlet 12N for being connected to N grades of mixing arrangements forms N grades of mixing arrangements, N=4,5,6 ....
When mixing arrangements at different levels are in working condition, piston is upper；It is living when mixing arrangements at different levels are in off state
Plug is bottom, and piston can be driven by the cylinder.When the feed inlet of mixing arrangements at different levels is by high-pressure pump transferring raw material, path pair
The refluxing opening guarantee answered is unimpeded, and when being stopped so as to working end, raw material can be flowed back into feeding device；It avoids causing to waste.
In addition, when the feed inlet of mixing arrangements at different levels is connected by the auxiliary mixing device and connecting tube of upper level mixing arrangement, the charging
The corresponding refluxing opening in path of mouth is blocks.In mixing arrangements at different levels, the effect of pressure regulator be adjustable feed inlet by
The flow of high-pressure pump transferring raw material is more advantageous to the adjusting of material rate in this way.
Multigroup part of mixing arrangement provided by the utility model, has the following advantages：
1st, the present apparatus ensure that mixing quality, improved raw material mixing velocity using classification head-on collision mixing；
2nd, the present apparatus does not need to artificial dispensing, and material rate can be adjusted；
3rd, the present apparatus does not need to, using a large amount of cleaning solution cleaning equipments, save largely manually, and reduce to environment
Pollution；
4th, the present apparatus carries reflux, and raw material mixing process can stop at any time, cannot be used up, cause after avoiding raw material mixing
Waste.
Large scale raw material A material is divided into A1, A2, A3 by the present apparatus according to actual needs simultaneously ..., and An divides N grades and small scale
Raw material B is mixed step by step, can also realize multigroup part of multistage mixing according to actual needs.
Above-described embodiment is the illustration of utility model, should not be described to limit with the exemplary embodiments of specification and attached drawing
The protection domain of patent right processed.
The utility model preferred embodiment and embodiment are explained in detail above in conjunction with attached drawing, but this
Utility model is not limited to the above-described embodiment and examples, in the knowledge having in those skilled in the art, may be used also
With various changes can be made without departing from the concept of the premise utility.It in the claims, should not will be between bracket
Any reference mark as limitations on claims.Word "comprising" does not exclude the presence of element not listed in the claims
Or step.
Claims (10)
1. a kind of multigroup part of mixing arrangement, which is characterized in that including level-one mixing arrangement and two level mixing arrangement, the level-one is mixed
It attaches together at least two feed inlets put to connect with the mixing discharge port of the level-one mixing arrangement, the level-one mixing arrangement mixes
Discharge port is closed to connect with the feed inlet of the two level mixing arrangement.
2. multigroup part of mixing arrangement according to claim 1, which is characterized in that the level-one mixing arrangement is provided at least
Two feed inlets (11,12) and the mixing discharge port (13) connected with feed inlet (11,12)；
The two level mixing arrangement is provided at least two feed inlets (112,122) and is connected with feed inlet (112,122) mixed
Close discharge port (132)；
The mixing discharge port (13) of the level-one mixing arrangement is connect with the feed inlet (122) of the two level mixing arrangement.
3. multigroup part of mixing arrangement according to claim 2, which is characterized in that the level-one mixing arrangement is additionally provided with point
The refluxing opening (14,15) not coordinated with feed inlet (11,12), between the refluxing opening (14,15) and the feed inlet (11,12)
Piston (16) is provided with, the piston is connected with driving device (1611)；
The two level mixing arrangement is additionally provided with the refluxing opening (142,152) coordinated respectively with feed inlet, the refluxing opening (142,
152) piston (162) is provided between the feed inlet (112,122), the piston is connected with driving device (1612).
4. multigroup part of mixing arrangement according to claim 3, which is characterized in that the level-one mixing arrangement and the two level
Auxiliary mixing device (19) is installed between mixing arrangement；
The mixing discharge port (132) of the two level mixing arrangement is connected with auxiliary mixing device (192)；
Pressure regulator (17,18) is installed on the feed inlet (11,12) of the level-one mixing arrangement；
Pressure regulator (172,182) is installed on the feed inlet (112,122) of the two level mixing arrangement.
5. multigroup part of mixing arrangement according to claim 4, which is characterized in that further include three-level mixing device, described three
Grade mixing arrangement is provided at least two feed inlets (113,123), the mixing discharge port connected with feed inlet (113,123)
(133) and respectively with the refluxing opening (143,153) of feed inlet (113,123) cooperation, the refluxing opening (143,153) with it is described into
Piston (163) is provided between material mouth (113,123), the piston is connected with driving device (1613)；
The mixing discharge port (132) of the two level mixing arrangement is connect with the feed inlet (123) of the three-level mixing device.
6. multigroup part of mixing arrangement according to claim 5, which is characterized in that the refluxing opening of the two level mixing arrangement
(152) plug is installed on；
Plug is installed on the refluxing opening (153) of the three-level mixing device.
7. multigroup part of mixing arrangement according to claim 5, which is characterized in that the refluxing opening of the two level mixing arrangement
Plug is installed on (142,152)；
Plug is installed on the refluxing opening (153) of the three-level mixing device；
The quantity of the level-one mixing arrangement is identical with the quantity of the feed inlet of the two level mixing arrangement, the level-one mixing dress
Feed inlet of the discharge port put respectively with the two level mixing arrangement is connect.
8. multigroup part of mixing arrangement according to claim 3, which is characterized in that the feed inlet (11,12) with it is described go out
Reinforcing prop (22) is longitudinally provided between material mouth (13), multiple semi-spiral pieces 23, institute are from top to bottom installed on the reinforcing prop
The top for stating semi-spiral piece is located at the side of the feed inlet (11,12), and the bottom end of the semi-spiral piece is located at mixing discharge port
(13) side.
9. the multigroup part of mixing arrangement according to claim 3 or 8, which is characterized in that the feed inlet (11,12) with it is described
Channel (231) is formed between discharge port (13), the top of the channel sets fluted (24)；
The groove is inclined close to the side of the discharge port, and the distance L1 of bottom end to discharge port is less than top to discharge port
Distance L2；
Elastic diaphragm (25) is installed, the elastic diaphragm is inclined, the height of the bottom end of the elastic diaphragm in the groove
Degree is less than the height on the top of the elastic diaphragm.
10. multigroup part of mixing arrangement according to claim 3, which is characterized in that be provided in the level-one mixing arrangement
Piston channel (26), the piston channel longitudinally run through the level-one mixing arrangement；
The piston (16) is connect by piston rod (27) with driving device (1611), the piston rod and the piston channel it
Between have spacing；
Sealing piston (28) is additionally provided on the piston rod, the sealing piston is located at the top of the refluxing opening (14,15)；
Piston channel is provided on the two level mixing arrangement, the piston channel longitudinally runs through the two level mixing arrangement；
The piston (162) is connect by piston rod with driving device (1612), between the piston rod and the piston channel
There is spacing；
Sealing piston is additionally provided on the piston rod, the sealing piston is located at the top of the refluxing opening (142,152).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721288590.8U CN207535138U (en) | 2017-09-30 | 2017-09-30 | A kind of multigroup part of mixing arrangement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721288590.8U CN207535138U (en) | 2017-09-30 | 2017-09-30 | A kind of multigroup part of mixing arrangement |
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| Publication Number | Publication Date |
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| CN207535138U true CN207535138U (en) | 2018-06-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721288590.8U Withdrawn - After Issue CN207535138U (en) | 2017-09-30 | 2017-09-30 | A kind of multigroup part of mixing arrangement |
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| CN (1) | CN207535138U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107520987A (en) * | 2017-09-30 | 2017-12-29 | 京华派克邯郸机械科技有限公司 | A kind of more component mixing arrangements |
| CN107520987B (en) * | 2017-09-30 | 2024-06-28 | 京华派克邯郸机械科技有限公司 | Multicomponent mixing arrangement |
-
2017
- 2017-09-30 CN CN201721288590.8U patent/CN207535138U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107520987A (en) * | 2017-09-30 | 2017-12-29 | 京华派克邯郸机械科技有限公司 | A kind of more component mixing arrangements |
| CN107520987B (en) * | 2017-09-30 | 2024-06-28 | 京华派克邯郸机械科技有限公司 | Multicomponent mixing arrangement |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20180626 Effective date of abandoning: 20240628 |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20180626 Effective date of abandoning: 20240628 |