CN103433151A - Horizontal spiral discharge sedimentary centrifuge - Google Patents
Horizontal spiral discharge sedimentary centrifuge Download PDFInfo
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- CN103433151A CN103433151A CN2013103482232A CN201310348223A CN103433151A CN 103433151 A CN103433151 A CN 103433151A CN 2013103482232 A CN2013103482232 A CN 2013103482232A CN 201310348223 A CN201310348223 A CN 201310348223A CN 103433151 A CN103433151 A CN 103433151A
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- mandrel
- cloth
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
- B04B2001/2033—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl with feed accelerator inside the conveying screw
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Abstract
The invention discloses a horizontal spiral discharge sedimentary centrifuge, which comprises a chassis, a rotary drum, and a spiral pushing device, wherein the rotary drum is driven to rotate by a rotary drum power device, and is provided with a liquid outlet and a solid outlet; the spiral pushing device comprises a hollow core shaft; spiral pushing blades are arranged on an outer wall of the core shaft; a material distribution accelerator is arranged in an inner cavity of the core shaft, is connected with an outer space of a screw rod through material distribution holes, and comprises a connecting body arranged in a middle section of the core shaft; a material distribution cavity is arranged in the connecting body; a material inlet is arranged on a front end of the material distribution cavity; at least two material distribution holes communicated with the material distribution cavity are formed in a side wall of the connecting body; a hole edge of each material distribution hole, at the rotary downstream side, is extended in an arc shape towards the rotary downstream side from inside to outside. According to the centrifuge, the material discharging manner of the material distribution accelerator is optimized, a material discharging direction is changed, the impact force of materials discharged from the material distribution holes on a sedimented solid phase of an inner wall of the rotary drum is reduced, and the sedimentary centrifuge effect is improved.
Description
Technical field
The present invention relates to a kind of centrifuge, refer to especially a kind of horizontal spiral discharge sedimentation centrifuge.
Background technology
Horizontal spiral discharge sedimentation centrifuge utilizes in mixed liquor has different densities and immiscible light, heavy-fluid and solid phase, obtains the principle of different sinking speed in centrifugal force field, reaches the purpose of separating layering or making solid particles sediment in liquid.This type energy automatic continuous operation, be widely used in the industrial departments such as chemical industry, light industry, food, ore dressing, in environment-friendly engineering, is also desirable equipment.After solid phase particles deposits in rotary drum, be under the promotion of screw rod, discharge with the outlet of rotary drum small end solid phase.Current centrifuge comprises casing, rotates the rotary drum be installed in casing, rotation is installed on the spiral pusher device in rotary drum, this rotary drum drives rotation by the rotary drum power set, this rotary drum comprises interconnective cylindrical tube and frustum of a cone cylindrical shell, the end of cylindrical tube is provided with leakage fluid dram, and the end of frustum of a cone cylindrical shell is provided with Pai Gukou; This spiral pusher device comprises the mandrel of hollow, this mandrel coaxial rotation is installed in rotary drum and is driven by mandrel power mechanism, the outer wall of this mandrel is provided with spiral helicine pusher blade, this pusher blade comprises cylindrical section and frustum of a cone section, this cylindrical section is corresponding with cylindrical tube and frustum of a cone cylindrical shell respectively with frustum of a cone section, cloth accelerator in the inner chamber of mandrel, this cloth accelerator is communicated with the screw rod space outerpace by the cloth hole, is placed with the feed pipe extended in the cloth accelerator in mandrel.The following problem of this centrifuge ubiquity: 1. the structure in current cloth hole is strip or rectangle cloth hole, and larger to the impulsive force of drum inner wall while due to the shape in cloth hole, causing material to be discharged from the cloth hole, so just may cause the solid phase that has been deposited in drum inner wall originally again broken up and, by forming suspension, so just reduced centrifugal efficiency and the effect of sedimentation.2. the solid phase water content that the spiral pusher device of current centrifuge is discharged is larger, can't meet like this solid phase that water content is low and discharge requirement; 3. the height of the leakage fluid dram of rotary drum is non-adjustable, can't adapt to the centrifugal demand of various materials; 4. centrifuge is in detachable maintaining inconvenience, because rotary drum and the mandrel of centrifuge is all to install by bearing block, bearing block generally adopts conventional structure, the bearing block body that it comprises the end cap that is positioned at the left and right sides and is positioned at middle part, for rotary drum and mandrel are split out, whole bearing block need to be shifted out just and can take out from two ends, demolition and maintenance are very constant.
Summary of the invention
Technical problem to be solved by this invention is: a kind of horizontal spiral discharge sedimentation centrifuge is provided, this centrifuge is optimized the discharge method of cloth accelerator, change its discharging direction, the impulsive force of the material that reduction is discharged from the cloth hole to the solid phase of drum inner wall sedimentation, improve the centrifugal effect of sedimentation.
Another technical problem to be solved by this invention is: provide a kind of dehydrating effect better horizontal spiral discharge sedimentation centrifuge.
For solving the problems of the technologies described above, technical scheme of the present invention is: horizontal spiral discharge sedimentation centrifuge, comprise casing, rotate the rotary drum be installed in casing, rotation is installed on the spiral pusher device in rotary drum, this rotary drum drives rotation by the rotary drum power set, this rotary drum comprises interconnective cylindrical tube and frustum of a cone cylindrical shell, and the end of cylindrical tube is provided with leakage fluid dram, and the end of frustum of a cone cylindrical shell is provided with Pai Gukou, this spiral pusher device comprises the mandrel of hollow, this mandrel coaxial rotation is installed in rotary drum and is driven by mandrel power mechanism, the outer wall of this mandrel is provided with spiral helicine pusher blade, this pusher blade comprises cylindrical section and frustum of a cone section, this cylindrical section is corresponding with cylindrical tube and frustum of a cone cylindrical shell respectively with frustum of a cone section, cloth accelerator in the inner chamber of mandrel, this cloth accelerator is communicated with the screw rod space outerpace by the cloth hole, be placed with the feed pipe extended in the cloth accelerator in mandrel, this cloth accelerator comprises the connector that is arranged at the mandrel stage casing, be provided with distribution cavity in this connector, the front end of this distribution cavity is provided with charging aperture, the sidewall of described connector is provided with at least two cloth holes that are communicated with distribution cavity, the hole in each rotation downstream, cloth hole is along extending towards rotation downstream arc from inside to outside.
As a kind of preferred scheme, the arc on the edge, hole in each rotation downstream, cloth hole extends to circular arc and extends.
As a kind of preferred scheme, the number in described cloth hole is two and arranges with respect to the axis Central Symmetry of mandrel.
As a kind of preferred scheme, be installed with striker plate on the outer wall of described mandrel, this striker plate is positioned at the cylindrical section of pusher blade and the junction of frustum of a cone section, there is the pusher gap between the outer rim of this striker plate and drum inner wall, this pusher gap is greater than the gap between pusher blade outer rim and drum inner wall, also be provided with opening on this striker plate, form the material flow channel between this opening and drum inner wall.
As a kind of preferred scheme, described striker plate is the fan annular.
As a kind of preferred scheme, described leakage fluid dram place is equipped with the fluid arrangement for adjusting height.
As a kind of preferred scheme, described fluid arrangement for adjusting height comprises and blocks liquid fixed head and one group of DOCK LEVELER, described blocking on the liquid fixed head is provided with bolt hole, the described liquid fixed head that blocks is provided with fluid hole, described one group of DOCK LEVELER is provided with the installing hole corresponding with the bolt hole position, but this group of DOCK LEVELER is the partial occlusion fluid hole all, and the area of the fluid hole that blocks of each DOCK LEVELER is all not identical; Described block the liquid fixed head by the bolt through bolt hole and installing hole wherein a tile height adjustable plate be fixed on the leakage fluid dram place of rotary drum.
As a kind of preferred scheme, described rotary drum and mandrel are realized rotating by bearing block and are installed, and bearing block comprises upper cover and the lower cover cooperatively interacted, and has the bearing installing space between upper cover and lower cover, between upper cover and lower cover, by bolt, detachably installs.
After having adopted technique scheme, effect of the present invention is: because this cloth accelerator comprises the connector that is arranged at the mandrel stage casing, be provided with distribution cavity in this connector, the front end of this distribution cavity is provided with charging aperture, the sidewall of described connector is provided with at least two cloth holes that are communicated with distribution cavity, the hole in each rotation downstream, cloth hole is along extending towards rotation downstream arc from inside to outside, therefore, the material flown out not is that direct projection is on the inwall of rotary drum, flying route with material in currently available technology compares, material of the present invention to fly route rounder and more smooth, impulsive force to drum inner wall is less, like this, just to the solid phase be deposited on drum inner wall, upset less, can improve separative efficiency and the separating effect of centrifuge.
Be installed with striker plate on outer wall due to described mandrel again, this striker plate is positioned at the cylindrical section of pusher blade and the junction of frustum of a cone section, there is the pusher gap between the outer rim of this striker plate and drum inner wall, this pusher gap is greater than the gap between pusher blade outer rim and drum inner wall, also be provided with opening on this striker plate, form the material flow channel between this opening and drum inner wall, therefore, when solid phase is promoted by pusher blade, when the junction through cylindrical section and frustum of a cone section, sectional area diminishes, thereby can producing, solid phase piles up extruding, now, again because of the existence of striker plate, make solid phase further push, realized the secondary extrusion dehydration of solid phase, the solid phase water content that row Gu Kou discharges like this is lower.
Because comprising, described fluid arrangement for adjusting height blocks liquid fixed head and one group of DOCK LEVELER again, described blocking on the liquid fixed head is provided with bolt hole, the described liquid fixed head that blocks is provided with fluid hole, described one group of DOCK LEVELER is provided with the installing hole corresponding with the bolt hole position, but this group of DOCK LEVELER is the partial occlusion fluid hole all, and the area of the fluid hole that blocks of each DOCK LEVELER is all not identical; Described block the liquid fixed head by the bolt through bolt hole and installing hole wherein a tile height adjustable plate be fixed on the leakage fluid dram place of rotary drum.By changing the DOCK LEVELER of different size, realized that the height of leakage fluid dram is regulated.
Realize rotating by bearing block due to described rotary drum and mandrel again and install, bearing block comprises upper cover and the lower cover cooperatively interacted, and has the bearing installing space between upper cover and lower cover, between upper cover and lower cover, by bolt, detachably installs.Lower cover can fix on the ground like this, and only dismantle the upper cover casing and complete splitting out of rotary drum and mandrel, not only easy maintenance and installation, and can guarantee the flatness between lower cover, and guarantee the installation accuracy of centrifuge, avoid rocking and shaking.
The accompanying drawing explanation
Below in conjunction with drawings and Examples, the present invention is further described.
Fig. 1 is the structure cutaway view of the embodiment of the present invention;
Fig. 2 is the structure cutaway view of the spiral pusher device of the embodiment of the present invention;
Fig. 3 is the structure cutaway view of the cloth accelerator of the embodiment of the present invention;
Fig. 4 is the enlarged diagram of Fig. 1 at the I place;
Fig. 5 is the cutaway view that blocks the liquid fixed head;
Fig. 6 is the front schematic view of blocking the liquid fixed head;
Fig. 7 is the structural representation of DOCK LEVELER;
Fig. 8 is the enlarged diagram of Fig. 1 at the II place;
Fig. 9 is the structural representation of bearing block;
In accompanying drawing: 1. casing; 11. liquid outlet; 12. go out Gu Kou; 2. rotary drum; 21. leakage fluid dram; 3. spiral pusher device; 31. cylindrical section; 32. cloth accelerator; 321. distribution cavity; 322. charging aperture; 323. cloth hole; 3231. the edge, hole in rotation downstream; 3232. the edge, hole of rotation upstream side; 33. frustum of a cone section; 34. helical blade; 35. striker plate; 4. bearing block; 41. upper cover; 42. lower cover; 43. bolt; 5. mandrel power mechanism; 6. rotary drum power set; 7. block the liquid fixed head; 71. lip ring section; 72. fixing ring portion; 73. bolt hole; 74. fluid hole; 741. straightway; 742. major arc section; 8. DOCK LEVELER; 81. major arc section; 82. installing hole; 83. minor segment.
The specific embodiment
Below by specific embodiment, the present invention is described in further detail.
As shown in Figure 1, a kind of horizontal spiral discharge sedimentation centrifuge, comprise casing 1, rotate the rotary drum 2 be installed in casing 1, rotation is installed on the spiral pusher device 3 in rotary drum 2, rotary drum 2 and spiral pusher device 3 are all covered by casing 1, one end of casing 1 arranges liquid outlet 11, and the other end sets out solid mouthful 12; This rotary drum 2 drives rotation by rotary drum power set 6, and this rotary drum 2 comprises interconnective cylindrical tube and frustum of a cone cylindrical shell, and the end of cylindrical tube is provided with leakage fluid dram 21, and the end of frustum of a cone cylindrical shell is provided with Pai Gukou; Leakage fluid dram 21 and liquid outlet 11 correspondences, row Gu Kou is with to go out solid mouth 12 positions corresponding.
As Fig. 2, 3, 4 these spiral pusher devices 3 comprise the mandrel of hollow, this mandrel coaxial rotation is installed in rotary drum 2 and by mandrel power mechanism 5 and drives, the outer wall of this mandrel is provided with spiral helicine pusher blade, this pusher blade comprises cylindrical section 31 and frustum of a cone section 33, this cylindrical section 31 is corresponding with cylindrical tube and frustum of a cone cylindrical shell respectively with frustum of a cone section 33, cloth accelerator 32 in the inner chamber of mandrel, this cloth accelerator 32 is communicated with the screw rod space outerpace by the cloth hole, be placed with the feed pipe extended in cloth accelerator 32 in mandrel, this cloth accelerator 32 comprises the connector that is arranged at the mandrel stage casing, this connector arranges the part of the middle part of cylindrical section 31 as mandrel, be provided with distribution cavity 321 in this connector, the front end of this distribution cavity 321 is provided with charging aperture 322, the sidewall of described connector is provided with at least two cloth holes 323 that are communicated with distribution cavity 321, extend towards rotation downstream arc from inside to outside along 3231 in the hole in each 323 rotation downstream, cloth hole.
The hole in preferred each 323 rotation downstream, cloth hole extends to the circular arc extension along 3231 arc.The number in described cloth hole 323 is two and arranges with respect to the axis Central Symmetry of mandrel.The hole in the rotation downstream in any cloth hole 323 along 3231 and the hole of the rotation upstream side in another cloth hole 323 along equal arc-shaped transition between 3232, like this, material is when from the cloth hole, 323 rotations are derived, can along 3231 shapes, fly out in 323 holes that rotate downstreams along the cloth hole, dwindle so as much as possible the angle that material flies out between direction and rotary drum 2 inwalls, thereby to the disturbance of the solid phase of sedimentation, improve centrifugal mass while reducing cloth.
As shown in Figure 4, be installed with striker plate 35 on the outer wall of described mandrel, this striker plate 35 is positioned at the cylindrical section 31 of pusher blade and the junction of frustum of a cone section 33, there is the pusher gap between the outer rim of this striker plate 35 and rotary drum 2 inwalls, this pusher gap is greater than the gap between pusher blade outer rim and rotary drum 2 inwalls, also be provided with opening on this striker plate 35, form the material flow channel between this opening and rotary drum 2 inwalls.Described striker plate 35 is the fan annular.So, the interior annulus of striker plate 35 is fixed on the outer wall of mandrel, and it is fanned between annular opening and mandrel and rotary drum 2 inwalls and forms the material flow channel.The existence of striker plate 35, make reducing by space of solid phase, and mandrel is in rotation process, and solid phase is promoted to frustum of a cone section 33 by cylindrical section 31, and after the further backgauge of striker plate 35, solid phase can secondary extrusion be dewatered, and can further fall low-soild water content.
As Fig. 5,6,7,8, in order to adapt to the separation requirement of different material, described leakage fluid dram 21 places are equipped with the fluid arrangement for adjusting height in addition.This fluid arrangement for adjusting height comprises and blocks liquid fixed head 7 and one group of DOCK LEVELER 8, described blocking on liquid fixed head 7 is provided with bolt hole 73, the described liquid fixed head 7 that blocks is provided with fluid hole 74, described one group of DOCK LEVELER 8 is provided with the installing hole 82 corresponding with bolt hole 73 positions, but the equal partial occlusion fluid hole 74 of this one group of DOCK LEVELER 8, and the area of the fluid hole 74 that blocks of each DOCK LEVELER 8 is all not identical; Described block liquid fixed head 7 by the bolt through bolt hole 73 and installing hole 82 wherein a tile height adjustable plate 8 be fixed on leakage fluid dram 21 places of rotary drum 2.
Wherein, blocking liquid fixed head 7 comprises the fixedly ring portion 72 of an annular and is covered in the lip ring section 71 on fixing ring portion 72, this lip ring section 71 is fluid hole 74 partial occlusions of ring portion 72 fixedly, described bolt hole 73 is arranged on the position that fixedly ring portion 72 is not blocked, and the cross sectional shape that by lip ring, is not blocked fluid hole 74 is that major arc section 742 surrounds shape with the sealing of straightway 741.
And described one group of DOCK LEVELER 8 is the closure plate that a major arc section 81 and minor segment 83 surround, the indent direction of this minor segment 83 and major arc section 81 is identical, and the area surrounded between the minor segment 83 of each DOCK LEVELER 8 and the straightway 741 of fluid hole 74 is all not identical.Like this, change different DOCK LEVELER 8 and just can change the area between minor segment 83 and straightway 741, thereby changed the fluid height of leakage fluid dram 21.
As shown in Figure 9, and described rotary drum 2 and mandrel realize rotating installation by bearing block 4, the number of bearing block 4 is two, for convenience of description, be referred to as clutch shaft bearing seat and the second bearing block, clutch shaft bearing seat and the second bearing block are arranged at respectively the two ends of rotary drum 2, one end of rotary drum 2 rotates and is installed on the clutch shaft bearing seat, other end turning set is contained on mandrel, and an end rotation of mandrel is installed on the second bearing block, the other end rotates and is arranged in rotary drum 2, like this, and the mutual rotary support of rotary drum 2 and mandrel.Rotary drum 2 and mandrel drive by its corresponding power set, and it realizes the difference of rotating speed by a differential mechanism.And clutch shaft bearing seat and the second bearing block all adopt the structure of two-piece unit formula, comprise the upper cover 41 and the lower cover 42 that cooperatively interact, there is the bearing installing space between upper cover 41 and lower cover 42, between upper cover 41 and lower cover 42, by bolt 43, detachably install.During actual installation, lower cover 42 is that relative ground is fixing, levelness between the lower cover 42 of the lower cover 42 of clutch shaft bearing seat 4 and the second bearing block 4 is proofreaded when mounted so, when needs dismounting spiral pusher device 3 or rotary drum 2, only upper cover 41 casings 1 need be taken off, spiral pusher device 3 or rotary drum 2 taking-ups will be unloaded, while so again installing, without the levelness between two bearing blocks 4 of calibration, the demolition and maintenance maintenance is time saving and energy saving.
Claims (8)
1. horizontal spiral discharge sedimentation centrifuge, comprise casing, rotate the rotary drum be installed in casing, rotation is installed on the spiral pusher device in rotary drum, this rotary drum drives rotation by the rotary drum power set, this rotary drum comprises interconnective cylindrical tube and frustum of a cone cylindrical shell, the end of cylindrical tube is provided with leakage fluid dram, and the end of frustum of a cone cylindrical shell is provided with Pai Gukou, this spiral pusher device comprises the mandrel of hollow, this mandrel coaxial rotation is installed in rotary drum and is driven by mandrel power mechanism, the outer wall of this mandrel is provided with spiral helicine pusher blade, this pusher blade comprises cylindrical section and frustum of a cone section, this cylindrical section is corresponding with cylindrical tube and frustum of a cone cylindrical shell respectively with frustum of a cone section, cloth accelerator in the inner chamber of mandrel, this cloth accelerator is communicated with the screw rod space outerpace by the cloth hole, be placed with the feed pipe extended in the cloth accelerator in mandrel, it is characterized in that: this cloth accelerator comprises the connector that is arranged at the mandrel stage casing, be provided with distribution cavity in this connector, the front end of this distribution cavity is provided with charging aperture, the sidewall of described connector is provided with at least two cloth holes that are communicated with distribution cavity, the hole in each rotation downstream, cloth hole is along extending towards rotation downstream arc from inside to outside.
2. horizontal spiral discharge sedimentation centrifuge as claimed in claim 1 is characterized in that: the arc on the edge, hole in each rotation downstream, cloth hole extends to circular arc and extends.
3. horizontal spiral discharge sedimentation centrifuge as claimed in claim 2 is characterized in that: the number in described cloth hole is two and arranges with respect to the axis Central Symmetry of mandrel.
4. horizontal spiral discharge sedimentation centrifuge as described as the claims 1 to 3 any one, it is characterized in that: on the outer wall of described mandrel, be installed with striker plate, this striker plate is positioned at the cylindrical section of pusher blade and the junction of frustum of a cone section, there is the pusher gap between the outer rim of this striker plate and drum inner wall, this pusher gap is greater than the gap between pusher blade outer rim and drum inner wall, also be provided with opening on this striker plate, form the material flow channel between this opening and drum inner wall.
5. horizontal spiral discharge sedimentation centrifuge as claimed in claim 4 is characterized in that: described striker plate is the fan annular.
6. horizontal spiral discharge sedimentation centrifuge as claimed in claim 5, it is characterized in that: described leakage fluid dram place is equipped with the fluid arrangement for adjusting height.
7. horizontal spiral discharge sedimentation centrifuge as claimed in claim 6, it is characterized in that: described fluid arrangement for adjusting height comprises and blocks liquid fixed head and one group of DOCK LEVELER, described blocking on the liquid fixed head is provided with bolt hole, the described liquid fixed head that blocks is provided with fluid hole, described one group of DOCK LEVELER is provided with the installing hole corresponding with the bolt hole position, but this group of DOCK LEVELER is the partial occlusion fluid hole all, and the area of the fluid hole that blocks of each DOCK LEVELER is all not identical; Described block the liquid fixed head by the bolt through bolt hole and installing hole wherein a tile height adjustable plate be fixed on the leakage fluid dram place of rotary drum.
8. horizontal spiral discharge sedimentation centrifuge as claimed in claim 7, it is characterized in that: described rotary drum and mandrel are realized rotating by bearing block and are installed, bearing block comprises upper cover and the lower cover cooperatively interacted, there is the bearing installing space between upper cover and lower cover, detachably install by bolt between upper cover and lower cover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013103482232A CN103433151A (en) | 2013-08-12 | 2013-08-12 | Horizontal spiral discharge sedimentary centrifuge |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2013103482232A CN103433151A (en) | 2013-08-12 | 2013-08-12 | Horizontal spiral discharge sedimentary centrifuge |
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| CN103433151A true CN103433151A (en) | 2013-12-11 |
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| CN2013103482232A Pending CN103433151A (en) | 2013-08-12 | 2013-08-12 | Horizontal spiral discharge sedimentary centrifuge |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104741250A (en) * | 2015-03-30 | 2015-07-01 | 绿水分离设备股份有限公司 | Horizontal spiral discharge sedimentary centrifuge and feeding pipe barrel thereof |
| CN104959240A (en) * | 2015-05-23 | 2015-10-07 | 安徽普源分离机械制造有限公司 | Horizontal spiral discharging sedimentation centrifuge for energy-efficient proteins |
| CN104998765A (en) * | 2015-07-02 | 2015-10-28 | 蚌埠市兴利离心机制造有限公司 | Material pushing device of horizontal sedimenting centrifuge |
| CN106622686A (en) * | 2015-08-26 | 2017-05-10 | 苏州瑞威离心分离技术有限公司 | Horizontal spiral centrifugal machine |
| CN108043596A (en) * | 2017-12-20 | 2018-05-18 | 上海亭博分离技术有限公司 | A kind of drunk fish centrifuge |
| CN109092571A (en) * | 2018-07-25 | 2018-12-28 | 泸州市江阳区红岩机械有限公司 | A kind of Horizontal double cone screw settling centrifuge |
| CN109590117A (en) * | 2019-02-13 | 2019-04-09 | 成都西部石油装备股份有限公司 | A kind of auger stripper with material acceleration function |
| CN111545358A (en) * | 2020-05-20 | 2020-08-18 | 上海离创环保机电有限公司 | Slag hole scraping device of horizontal spiral sedimentation centrifuge |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104741250A (en) * | 2015-03-30 | 2015-07-01 | 绿水分离设备股份有限公司 | Horizontal spiral discharge sedimentary centrifuge and feeding pipe barrel thereof |
| CN104741250B (en) * | 2015-03-30 | 2017-06-27 | 绿水股份有限公司 | Horizontal spiral discharge sedimentation centrifuge and its charging tube cylinder |
| CN104959240A (en) * | 2015-05-23 | 2015-10-07 | 安徽普源分离机械制造有限公司 | Horizontal spiral discharging sedimentation centrifuge for energy-efficient proteins |
| CN104959240B (en) * | 2015-05-23 | 2018-08-31 | 安徽普源分离机械制造有限公司 | A kind of energy-efficient albumen special horizontal spiral discharge sedimentation centrifuge |
| CN104998765A (en) * | 2015-07-02 | 2015-10-28 | 蚌埠市兴利离心机制造有限公司 | Material pushing device of horizontal sedimenting centrifuge |
| CN106622686A (en) * | 2015-08-26 | 2017-05-10 | 苏州瑞威离心分离技术有限公司 | Horizontal spiral centrifugal machine |
| CN108043596A (en) * | 2017-12-20 | 2018-05-18 | 上海亭博分离技术有限公司 | A kind of drunk fish centrifuge |
| CN109092571A (en) * | 2018-07-25 | 2018-12-28 | 泸州市江阳区红岩机械有限公司 | A kind of Horizontal double cone screw settling centrifuge |
| CN109590117A (en) * | 2019-02-13 | 2019-04-09 | 成都西部石油装备股份有限公司 | A kind of auger stripper with material acceleration function |
| CN111545358A (en) * | 2020-05-20 | 2020-08-18 | 上海离创环保机电有限公司 | Slag hole scraping device of horizontal spiral sedimentation centrifuge |
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Application publication date: 20131211 |