CN203565466U - Distilling kettle - Google Patents
Distilling kettle Download PDFInfo
- Publication number
- CN203565466U CN203565466U CN201320739011.2U CN201320739011U CN203565466U CN 203565466 U CN203565466 U CN 203565466U CN 201320739011 U CN201320739011 U CN 201320739011U CN 203565466 U CN203565466 U CN 203565466U
- Authority
- CN
- China
- Prior art keywords
- kettle
- shaft
- distilling
- wall
- baffle plate
- 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.)
- Expired - Lifetime
Links
- 238000007599 discharging Methods 0.000 claims abstract description 10
- 238000005452 bending Methods 0.000 claims description 19
- 230000005540 biological transmission Effects 0.000 claims description 12
- 230000008878 coupling Effects 0.000 claims description 8
- 238000010168 coupling process Methods 0.000 claims description 8
- 238000005859 coupling reaction Methods 0.000 claims description 8
- 230000007246 mechanism Effects 0.000 claims description 7
- 238000010030 laminating Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 40
- 238000003756 stirring Methods 0.000 abstract description 20
- 239000000725 suspension Substances 0.000 abstract description 7
- 230000008021 deposition Effects 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- 230000000903 blocking effect Effects 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 239000010794 food waste Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 6
- 238000004062 sedimentation Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000006194 liquid suspension Substances 0.000 description 3
- 235000012054 meals Nutrition 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010237 hybrid technique Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000008093 supporting effect Effects 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a distilling kettle. The distilling kettle comprises a kettle body (10), a stirring shaft (4), a first stirrer (5) and a wall baffle (6), wherein the first stirrer (5) is arranged on the stirring shaft; the stirring shaft of the kettle body is vertically arranged in an inner cavity of a cylinder; the wall baffle is inserted between the first stirrer in the inner cavity and the kettle wall of the kettle body along the height direction. The wall baffle is additionally arranged in the distilling kettle; when circumferential stirring flow hits against the wall baffle, axial turbulent flow can be generated, so that a heavy-phase substance is prevented from being centrifugally settled. A second stirrer (9) can be arranged in a conical bottom cavity in the bottom of the kettle body, materials are further stirred and are overturned upwards, and a uniformly-stirred suspension can be formed. A cyclone connecting pipe (8) can be arranged on the kettle wall of the conical bottom cavity and is used for injecting water flow or steam flow for full mixing and cyclone stirring, so that deposition of a heavy-phase material at the bottom of the kettle and blocking of a discharging hole (11) are avoided.
Description
Technical field
The utility model relates to a kind of vertical mixing system, in particular for processing the distilling kettle of changing food waste.
Background technology
In changing food waste, the proportion of each component differs greatly, percentage of impurity is high, poor fluidity.For this mixing changing food waste that is pulp-like, heavy phase thing free settling and there is viscosity higher, require to adopt rational rabbling mechanism with suitable stir speed (S.S.), changing food waste material fully to be stirred, form uniform suspension, avoid heavy phase material deposition wherein, so that cause that the discharging opening of kettle stops up.
Be current a kind of distilling kettle for the treatment of changing food waste as depicted in figs. 1 and 2.In the kettle 10 of this distilling kettle, only in its straight tube chamber, be provided with the paddle agitator that a multistage paddle agitator 5(adopts multilayer) to stir material, thereby reach, force material suspended technological requirement.Wherein, external motor drives shaft 4 around its rotation OO ' rotation by power transmission shaft 1, shaft coupling 3, drives 5 pairs of materials of agitator to stir, and the material after uniform stirring can be from discharging opening 11 dischargings.Wherein power transmission shaft 1 is arranged on distilling kettle by block bearing 2 supportings, and shaft 4 stretches out downwards and suspends.
Yet, in this distilling kettle, multistage paddle agitator 5 simple in structure, be applicable to more rotating speed extremely low, in the hybrid technique of the less demanding low viscosity material of mixing effect, in changing food waste processing procedure, have the following disadvantages:
1), in order fully to stir to form uniform suspension, need to increase the stirring intensity of agitator, thereby mixing arm adopts the long and wide blade that twists into arcuation mostly.This blade processing and manufacturing difficulty is high, and easily occurs and accumulated deformation, and even bending damages, and causes service life low;
2), via the stirring of multistage paddle agitator 5, material easily forms fixedly flow pattern---form around the peripheral flow of multistage paddle agitator 5, as shown in the arrow in Fig. 2, along the peripheral flow of direction of rotation w.So not only be difficult to reach and make material suspended technological requirement, even easily cause heavy phase material to form centrifugal sedimentation;
3), the heavy phase material of centrifugal sedimentation is easily accumulated in the conical bottom chamber (being kettle reducer) in kettle 10, the still wall in this region of wearing and tearing, easily causes the discharging opening 11 at the bottom of still to stop up;
4), shaft 4 end that stretches into kettle 10 bottoms do not supported, this shaft 4 is cantilever beam structures, causes the rigidity of shaft 4 low, deflection increases, axial movement value increases, thereby reduces service life of equipment, has a strong impact on mixing effect.
Utility model content
The purpose of this utility model is to provide a kind of distilling kettle, and this distilling kettle is particularly suited for processing changing food waste, changing food waste material fully can be stirred into uniform suspension.
For achieving the above object, the utility model provides a kind of distilling kettle, this distilling kettle comprises vertical kettle, shaft and is arranged on the first agitator on this shaft, described shaft extend into downwards the inner chamber of this kettle from the top of described kettle, wherein, this distilling kettle also comprises wall baffle plate, and this wall baffle plate is inserted between described the first agitator and the still wall of described kettle in described inner chamber along short transverse.
Preferably, described wall baffle plate is polylith, and this polylith wall baffle plate is arranged along interval on the circumferencial direction of the rotation around described shaft.
Preferably, the bending plate of described wall baffle plate for being formed by the bending of individual plates broad ways, on the cross section of this bending plate, the bending drift angle of described bending plate is arranged towards the rotation of described shaft.
Preferably, in the footpath of described kettle upwards, 1/12～1/10 of the internal diameter that the width that described wall baffle plate makes progress along described footpath is described kettle, and the internal diameter that is described kettle of the spacing between the still wall of described wall baffle plate and described kettle 1/50～1/20.
Preferably, described wall baffle plate is dull and stereotyped, and the still wall interval of this flat board and described kettle arranges or laminating is installed on described still wall.
Preferably, this distilling kettle also comprises driving mechanism, power transmission shaft, block bearing and shaft coupling, described block bearing is installed on described distilling kettle, described power transmission shaft is rotatably supported on described block bearing and drives rotation by described driving mechanism, and described power transmission shaft connects by described shaft coupling and drives described shaft.
Preferably, the inner chamber of above-mentioned kettle comprises the conical bottom chamber of straight tube chamber and bottom, this straight tube chamber, this conical bottom chamber has discharging opening, described the first agitator is arranged in described straight tube chamber, described shaft stretches in described conical bottom chamber, and described distilling kettle also comprises the second agitator, this second agitator is installed on described shaft and is arranged in described conical bottom chamber.
Preferably, described the second agitator is gate stirrer.
Preferably, this distilling kettle also comprises the positioning support being arranged in described conical bottom chamber, and the bottom of this positioning support is supported on the still wall in described conical bottom chamber, top for grip be inserted into described conical bottom chamber described shaft to locate this shaft.
Preferably, this distilling kettle also comprises the eddy flow adapter on the still wall that is arranged on described conical bottom chamber, and the outlet that this eddy flow is taken over arranges obliquely.
According to technique scheme, in distilling kettle of the present utility model, set up along short transverse and be inserted in the wall baffle plate in the inner chamber of kettle and between the still wall of the first agitator and kettle, the peripheral flow forming due to the stirring of agitator is after impact walls baffle plate, can produce the axial turbulence that is conducive to solid-liquid suspension, thereby prevent that heavy phase material from forming centrifugal sedimentation.
Other feature and advantage of the present utility model partly in detail are described the specific embodiment subsequently.
Accompanying drawing explanation
Accompanying drawing is to be used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, but does not form restriction of the present utility model with the specific embodiment one below.In the accompanying drawings:
Fig. 1 is the structural representation of a kind of distilling kettle of the prior art;
Fig. 2 is that distilling kettle in Fig. 1 is along the view of A view directions;
Fig. 3 is according to the structural representation of the distilling kettle of preferred embodiment of the present utility model;
Fig. 4 be distilling kettle in Fig. 3 along the view of B view directions, wherein for clarity sake, only shown the first agitator, wall baffle plate and kettle, and omitted other all parts such as connecting plate between the second agitator, wall baffle plate and still inwall.
description of reference numerals
The specific embodiment
Below in conjunction with accompanying drawing, the specific embodiment of the present utility model is elaborated.Should be understood that, the specific embodiment described herein only, for description and interpretation the utility model, is not limited to the utility model.
In the utility model, in the situation that not doing contrary explanation, the noun of locality of use as " upper and lower, top, the end " normally for direction shown in the drawings or for each parts mutual alignment relationship description word vertically, on vertical or gravity direction.
As shown in Figure 3, the utility model provides a kind of distilling kettle at this, this distilling kettle comprises vertical kettle 10, shaft 4 and is removably mounted on the first agitator 5 on this shaft 4, and shaft 4 extend into downwards the inner chamber of this kettle 10 from the top of kettle 10; Wherein, this distilling kettle also comprises wall baffle plate 6, and this wall baffle plate 6 is inserted between the first agitator 5 and the still wall of kettle 10 in inner chamber along short transverse (above-below direction in figure).In the utility model, taken into full account the liquid flow pattern in kettle, by wall baffle plate 6 being set to strengthen axial turbulence intensity, avoid the material being stirred to form fixing circumferential revolution, prevent that heavy phase material from forming centrifugal sedimentation, and produced the axial flow that is conducive to solid-liquid suspension, more can meet the technological requirement that material is evenly suspended.
Preferably, this wall baffle plate 6 is polylith, and this polylith wall baffle plate 6 is arranged along interval on the circumferencial direction of the rotation OO ' around shaft 4.As shown in Figure 4,4 wall baffle plates 6 in kettle 10, have along the circumferential direction equally spaced been arranged.Wherein, the rotation OO ' of shaft 4 preferably overlaps with the center line of kettle 10.As shown in Figure 4, wall baffle plate 6 is preferably the bending plate being formed along the width bending of this plate by individual plates, the cross section of this bending plate as shown in Figure 4, arrange towards the rotation OO ' of shaft 4, bends the rear opening forming towards the still wall of kettle 10 by the bending drift angle of bending plate.The wall baffle plate 6 of this shape and position can strengthen axial turbulence intensity, reduces stirring material along the stopping of the circumferential flow of direction of rotation w simultaneously as far as possible, thereby reduces the power consumption of the first agitator 5.On the basis of design and Multi simulation running simulation, pin is especially to meal kitchen material, for making can reach as the wall baffle plate 6 that Fig. 4 arranges the effect of better enhancing axial turbulence, footpath at kettle 10 makes progress, the width design that wall baffle plate 6 is radially gone up be kettle 10 internal diameter 1/12～1/10, and the spacing between wall baffle plate 6 and the still wall of kettle 10 be preferably kettle 10 internal diameter 1/50～1/20.Herein, as shown in Figure 4, the radial alignment that the width that wall baffle plate 6 is radially gone up refers to through the bending summit of bending plate arrives the width between bending plate opposite side opening.This wall baffle plate 6 can be fixedly mounted on the roof of kettle 10 or sidewall to fix, and in a kind of mounting means of the wall baffle plate 6 showing in Fig. 3, wall baffle plate 6 is welded on still inwall by a plurality of connecting plates 61.In addition for unclassified stores or for the not high occasion of the Functional Requirement of wall baffle plate 6, wall baffle plate 6 can be also dull and stereotyped other shapes that wait, and flat board can arrange with the still wall interval of kettle 10 or directly fit and be installed on still wall.
As shown in Figure 3, distilling kettle of the present utility model also comprises driving mechanism (not shown), power transmission shaft 1, block bearing 2 and shaft coupling 3, block bearing 2 is preferably and keeps at a certain distance away mounted in pairs on distilling kettle, as two fulcrums, power transmission shaft 1 is rotatably supported on block bearing 2 and by driving rotations such as driving mechanism such as motors, power transmission shaft 1 connects by shaft coupling 3 and drives shaft 4, drives meal kitchen material to do gyration.
In addition, the inner chamber of kettle 10 comprises the conical bottom chamber (being kettle reducer) of straight tube chamber (being kettle direct tube section) and bottom, this straight tube chamber, this conical bottom chamber has discharging opening 11, the first agitator 5 is arranged in straight tube chamber, shaft 4 stretches in conical bottom chamber and (in Fig. 3, adopts shaft coupling 3 to plug into one section of shaft 4 of downward-extension), and distilling kettle also comprises the second agitator 9, this second agitator 9 is installed on shaft 4 and is arranged in conical bottom chamber.The second agitator 9 herein arranging, for material is upwards turned over and sent, forms suspension.Make the heavy phase material of sedimentation upwards to turn over and to send as the direction of arrow in figure, strengthen material in straight tube chamber and the mobility between the material in conical bottom chamber, each material can be fully uniformly mixed and form suspension.And increased the stirring intensity of bed material, alleviated wearing and tearing and the obstruction of underflow opening.Wherein, the second agitator 9 is preferably the gate stirrer shown in Fig. 3, and not only mixing power is large for this gate stirrer, stirring intensity is high, and shape design meets the shape and structure in conical bottom chamber.The general paddle agitator that adopts of the first agitator 5, as shown in Figure 3, in short transverse, interval is provided with three layers of slurry formula stirring vane, and intermediate blade arranges with levels blade is vertical.Certainly, also can adopt other existing agitators, such as gate stirrer or anchor agitator etc.
In the present embodiment, as shown in Figure 3, this distilling kettle also preferably includes the positioning support 7 being arranged in conical bottom chamber, the bottom of this positioning support 7 is supported on the still wall in conical bottom chamber, the top of positioning support 7 for grip be inserted into conical bottom chamber shaft 4 to locate this shaft 4.Prevent shaft 4 when rotating because vibration produces excessive device for elimination of axial-and radial-play amount, strengthen the rigidity of the stirring shaft part in conical bottom chamber, improve service life.
In addition, this distilling kettle also can comprise the eddy flow adapter 8 on the still wall that is arranged on conical bottom chamber, and this eddy flow takes over 8 for injection water or vapor stream, to lock meal kitchen material, fully mixes and cyclone mixing, at the bottom of avoiding heavy phase material to be deposited on still, stop up discharging opening 11.Wherein, this eddy flow is taken over 8 outlet and is preferably obliquely and arranges, and to contribute to upwards to turn over, send material, avoids heavy phase thing sedimentation at the bottom of still in material, deposits, hardens.
Distilling kettle of the present utility model is compared with the distilling kettle of current processing changing food waste, processing that this constituent is complicated, percentage of impurity is high, poor fluidity, while thering is the mixing changing food waste of viscosity higher, have the following advantages:
1), can process the material of viscosity, mu < 20Pas, be applicable to process the wide material of this range of viscosities of changing food waste;
2), can to process density contrast large, the material that in mixture, solid-to-liquid ratio heavily differs greatly;
3), can, under the process conditions of speed of agitator n=20～100r/min, blade end of blade linear velocity v=1～5m, material evenly be suspended;
4), wall baffle plate is set, strengthened axial turbulence intensity, avoided material to form fixing circumferential revolution, and produced the axial flow be conducive to solid-liquid suspension;
5), at the bottom of still, set up gate stirrer, increased the turbulent disturbance of underflow, alleviated wearing and tearing and the obstruction of discharging opening, be conducive to the discharge of highly enriched material;
6), at the bottom of still, suspension free settling section is provided with waterpower (current or vapor stream) eddy flow and takes over, hydraulic cyclone buoyancy will slow down heavy phase thing sinking speed, increase the turbulent disturbance of underflow, avoid material deposition, harden.
When processing the material of this composition of changing food waste and physical property complexity, compare with common agitating device, according to distilling kettle of the present utility model, more can meet the technological requirement that material is evenly suspended, and can regulate the stirring capacity of distilling kettle by controlling the intensity of rotating speed of transmission shaft and waterpower (current or vapor stream) eddy flow, thereby production control ability.And it should be noted that, the wall baffle plate adopting in the utility model is not only applicable in distilling kettle, more can expand in other agitating device or vertical mixing system stirring to needs, such as the cyclone desander for changing food waste is removed sand etc.
Below describe by reference to the accompanying drawings preferred embodiment of the present utility model in detail; but; the utility model is not limited to the detail in above-mentioned embodiment; within the scope of technical conceive of the present utility model; can carry out multiple simple variant to the technical solution of the utility model, these simple variant all belong to protection domain of the present utility model.
It should be noted that in addition, each concrete technical characterictic described in the above-mentioned specific embodiment, in reconcilable situation, can combine by any suitable mode, for fear of unnecessary repetition, the utility model is to the explanation no longer separately of various possible combinations.
In addition, between various embodiment of the present utility model, also can be combined, as long as it is without prejudice to thought of the present utility model, it should be considered as content disclosed in the utility model equally.
Claims (10)
1. a distilling kettle, this distilling kettle comprises kettle (10), shaft (4) and is arranged on the first agitator (5) on this shaft (4), described shaft (4) extend into downwards the inner chamber of this kettle (10) from the top of described kettle (10), it is characterized in that, this distilling kettle also comprises wall baffle plate (6), and this wall baffle plate (6) is inserted in the inner chamber of described kettle (10) and is arranged between described the first agitator (5) and the still wall of described kettle (10) along short transverse.
2. distilling kettle according to claim 1, is characterized in that, described wall baffle plate (6) is polylith, and this polylith wall baffle plate (6) is arranged along interval on the circumferencial direction of the rotation around described shaft (4) (OO ').
3. distilling kettle according to claim 1, it is characterized in that, the bending plate of described wall baffle plate (6) for being formed by individual plates broad ways bending, on the cross section of this bending plate, the bending drift angle of described bending plate is arranged towards the rotation of described shaft (4) (OO ').
4. distilling kettle according to claim 3, it is characterized in that, footpath at described kettle (10) makes progress, the width that described wall baffle plate (6) makes progress along described footpath be described kettle (10) internal diameter 1/12～1/10, and the spacing between described wall baffle plate (6) and the still wall of described kettle (10) be described kettle (10) internal diameter 1/50～1/20.
5. distilling kettle according to claim 1, is characterized in that, described wall baffle plate (6) is dull and stereotyped, and the still wall interval of this flat board and described kettle (10) arranges or laminating is installed on described still wall.
6. distilling kettle according to claim 1, it is characterized in that, this distilling kettle also comprises driving mechanism, power transmission shaft (1), block bearing (2) and shaft coupling (3), described block bearing (2) is installed on described distilling kettle, it is upper and drive rotation by described driving mechanism that described power transmission shaft (1) is rotatably supported in described block bearing (2), and described power transmission shaft (1) connects by described shaft coupling (3) and drives described shaft (4).
7. according to the distilling kettle described in any one in claim 1-6, it is characterized in that, the inner chamber of described kettle (10) comprises the conical bottom chamber of straight tube chamber and bottom, this straight tube chamber, this conical bottom chamber has discharging opening (11), described the first agitator (5) is arranged in described straight tube chamber, described shaft (4) stretches in described conical bottom chamber, and described distilling kettle also comprises the second agitator (9), this second agitator (9) is installed on described shaft (4) and goes up and be arranged in described conical bottom chamber.
8. distilling kettle according to claim 7, is characterized in that, described the second agitator (9) is gate stirrer.
9. distilling kettle according to claim 7, it is characterized in that, this distilling kettle also comprises the positioning support (7) being arranged in described conical bottom chamber, the bottom of this positioning support (7) is supported on the still wall in described conical bottom chamber, top for grip be inserted into described conical bottom chamber described shaft (4) to locate this shaft (4).
10. distilling kettle according to claim 7, is characterized in that, this distilling kettle also comprises the eddy flow adapter (8) on the still wall that is arranged on described conical bottom chamber, and the outlet that this eddy flow is taken over (8) arranges obliquely.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320739011.2U CN203565466U (en) | 2013-11-20 | 2013-11-20 | Distilling kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320739011.2U CN203565466U (en) | 2013-11-20 | 2013-11-20 | Distilling kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203565466U true CN203565466U (en) | 2014-04-30 |
Family
ID=50533225
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320739011.2U Expired - Lifetime CN203565466U (en) | 2013-11-20 | 2013-11-20 | Distilling kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203565466U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110252206A (en) * | 2019-06-28 | 2019-09-20 | 广西金秀松源林产有限公司 | A kind of rosin dissolver and method |
| CN111760871A (en) * | 2020-05-14 | 2020-10-13 | 浙江青草地环境科技有限公司 | On-site treatment method of kitchen waste |
| CN112191657A (en) * | 2020-09-21 | 2021-01-08 | 吉林省佳园再生科技有限公司 | Steaming and boiling drying device |
-
2013
- 2013-11-20 CN CN201320739011.2U patent/CN203565466U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110252206A (en) * | 2019-06-28 | 2019-09-20 | 广西金秀松源林产有限公司 | A kind of rosin dissolver and method |
| CN111760871A (en) * | 2020-05-14 | 2020-10-13 | 浙江青草地环境科技有限公司 | On-site treatment method of kitchen waste |
| CN112191657A (en) * | 2020-09-21 | 2021-01-08 | 吉林省佳园再生科技有限公司 | Steaming and boiling drying device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203999081U (en) | Stirring coagulation device for sewage disposal | |
| CN107281965A (en) | A kind of impacting type chemical raw material mixing stirring device | |
| CN203565466U (en) | Distilling kettle | |
| CN205730485U (en) | A kind of efficient equipment for separating liquid from solid | |
| CN203790950U (en) | Reaction kettle | |
| CN205672618U (en) | A kind of high-efficiency concentrator with self-cleaning pressure-preventing rake function | |
| CN204622317U (en) | A kind of concrete central mix plant | |
| CN202826052U (en) | Mixing device for solid concrete admixture | |
| CN105904589B (en) | A kind of agitating device and its stirring system | |
| CN205710031U (en) | A kind of efficient cracking flossing machine of two-chamber | |
| CN202022781U (en) | Flocculation reactor | |
| CN101658737A (en) | Rotational-flow gravity settling and separating method and device thereof | |
| CN105771337B (en) | A kind of efficient equipment for separating liquid from solid and its application | |
| CN204973743U (en) | A particle feedstock agitating unit for water treatment agent production | |
| CN204894214U (en) | Evaporate and press aerated concrete complete sets pouring mixer | |
| CN204265755U (en) | For combining the CSTR reactor possessed except scum silica frost ability of anaerobism | |
| CN203513459U (en) | Sludge conditioner | |
| CN205668325U (en) | A kind of agitating device and stirring system thereof | |
| CN103482847A (en) | Sludge conditioner and sludge conditioning method thereof | |
| CN204107495U (en) | A kind of retaining device about stirred tank | |
| CN102728258A (en) | Colter type mixer | |
| CN203061092U (en) | Multi-cavity continuous-fluid high-speed mixer | |
| CN207871968U (en) | Solid-liquid mixing machine | |
| CN207189955U (en) | Construction concrete circulation stirring blending tank | |
| CN207091081U (en) | A kind of modified mudpan |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP03 | Change of name, title or address |
Address after: 410000 Hunan province Changsha hi tech Development Zone, Lin Yulu No. 288 Co-patentee after: ZOOMLION HEAVY INDUSTRY SCIENCE AND TECHNOLOGY Co.,Ltd. Patentee after: ZOOMLION ENVIRONMENTAL INDUSTRY Co.,Ltd. Address before: 410013 Changsha province high tech Development Zone, No. 307 South Road, silver basin Co-patentee before: ZOOMLION HEAVY INDUSTRY SCIENCE AND TECHNOLOGY Co.,Ltd. Patentee before: Changsha Zoomlion Environmental Industry Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170613 Address after: 410000 Hunan province Changsha hi tech Development Zone, Lin Yulu No. 288 Patentee after: ZOOMLION ENVIRONMENTAL INDUSTRY Co.,Ltd. Address before: 410000 Hunan province Changsha hi tech Development Zone, Lin Yulu No. 288 Co-patentee before: ZOOMLION HEAVY INDUSTRY SCIENCE AND TECHNOLOGY Co.,Ltd. Patentee before: ZOOMLION ENVIRONMENTAL INDUSTRY Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140430 |