CN101327466A - Helical-conveyer centrifugal - Google Patents
Helical-conveyer centrifugal Download PDFInfo
- Publication number
- CN101327466A CN101327466A CNA2008100227132A CN200810022713A CN101327466A CN 101327466 A CN101327466 A CN 101327466A CN A2008100227132 A CNA2008100227132 A CN A2008100227132A CN 200810022713 A CN200810022713 A CN 200810022713A CN 101327466 A CN101327466 A CN 101327466A
- Authority
- CN
- China
- Prior art keywords
- rotary drum
- inner core
- pusher
- transmission mechanism
- inner cylinder
- 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.)
- Pending
Links
- 239000000463 material Substances 0.000 claims abstract description 18
- 230000005540 biological transmission Effects 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 230000001050 lubricating effect Effects 0.000 claims abstract description 5
- 238000009434 installation Methods 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 6
- 241000239290 Araneae Species 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 4
- 239000002002 slurry Substances 0.000 abstract description 13
- 239000007787 solid Substances 0.000 abstract description 10
- 238000000926 separation method Methods 0.000 abstract description 3
- 239000006228 supernatant Substances 0.000 abstract 2
- 239000000706 filtrate Substances 0.000 description 6
- 238000004062 sedimentation Methods 0.000 description 6
- 239000007790 solid phase Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000005622 photoelectricity Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Centrifugal Separators (AREA)
Abstract
The present invention discloses a spiral discharge centrifuge of slurry with less than 25 percent of separable solid content. The spiral discharge centrifuge comprises a machine base and a machine body and a casing arranged on the machine base. A transmission mechanism, a lubricating mechanism which is matched with the transmission mechanism and a rotary drum and a material pusher which are driven by the transmission mechanism at differential speed are arranged in the machine body. The rotary drum comprises a rotary drum bottom and a rotary drum barrel which is arranged on the rotary drum bottom. The rotary drum is arranged in the casing. The material pusher comprises an inner cylinder and an inner cylinder bottom which are arranged together. The external wall of the inner cylinder is provided with a spiral material pushing leaf. A trumpet-shaped feeding opening is arranged in the inner cylinder. The feeding opening is communicated with a feeding pipe of a feeding device. At least a pair of material passing holes is arranged at the inner cylinder near the inner cylinder bottom. A filter screen is arranged at the rotary drum barrel near a discharge opening. The rotary drum bottom is provided with four overflow ports. Each overflow port is communicated with a supernatant liquid outlet through the rotary drum and a supernatant liquid cavity between the casings. The spiral discharge centrifuge is mainly used for the solid-liquid separation of the slurry with less than 25 percent of the solid content.
Description
Technical field
The present invention relates to centrifuge, refer more particularly to helical-conveyer centrifugal.
Background technology
As everyone knows, centrifuge is that the centrifugal inertial force that utilizes drum rotating to produce is realized the separation of suspension, emulsion and other heterogeneous material or concentrated machine.Helical-conveyer centrifugal is the at present domestic and international the most frequently used a kind of related centrifuge that the continuous operation of screw unloading function is arranged, and its structure mainly is made of rotary drum, screw feeder, differential mechanism, feed arrangement, wash mill, lubricating system, transmission system, motor, casing, support and vibration damping base.Its operation principle is: motor is by two groups of belt pulley transferring power, drive rotary drum and screw feeder respectively with the rotation at a high speed in the same way of certain speed discrepancy, material is introduced the screw feeder inner core continuously by feed pipe, enter rotary drum after the acceleration, under the effect of centrifugal force field, liquid phase is discharged rotary drum by filter medium (screen cloth also claims filter screen), and through mother liquor pipe outflow centrifuge, solid phase is trapped within and forms filter residue in the rotary drum, filter residue is under the acting in conjunction of centrifugal component and defeated material spiral, continuously move to big end and throw away by the small end of rotary drum, and through the blowpit discharge centrifuge, screw unloading filter centrifugal machine can continuous feed under the full-speed operation state, separate and discharging, have compact conformation, volume is little, continued operation, running steadily, characteristics such as the big and filter residue water capacity for the treatment of capacity is low.But, screw unloading filter centrifugal machine be applicable to the solid phase particles granularity greater than 0.10 millimeter, solid concentration greater than 25% the coarse crystallization and the Separation of Solid and Liquid of short fiber material.Because the filter medium of this centrifuge is a metal lath, be to process by methods such as punching on metal book plate, photoelectricity burn into laser perforations, for guaranteeing the intensity of net, the percent opening of net is all about 5%, so it requires more than 25% the material solid concentration, after solid concentration has lacked, can cause the filter residue humidity, separate consequence such as unclear, output minimizing.A lot of materials also just can't reach instructions for use because be subjected to the restriction of technology can't reach solid concentration requirement 25% or more, and this has greatly limited the application of this centrifuge on a lot of materials.In addition, the rotary drum of present helical-conveyer centrifugal is bearing between the pair of bearings, and the dismounting of rotary drum extremely bothers, the bearing of one side must be pulled down earlier, rotary drum could be pulled down then, clean and regular maintenance, bring inconvenience so just for the regular maintenances such as cleaning of bowl.
Summary of the invention
A technical problem to be solved by this invention is: the helical-conveyer centrifugal of a kind of separable solid concentration at the slurry below 25% is provided.
For solving the problems of the technologies described above, the technical solution used in the present invention is: helical-conveyer centrifugal, comprise: support and the fuselage and the casing that are arranged on the support, the lubricating structure that is provided with transmission mechanism in the fuselage and matches with transmission mechanism, and the rotary drum and the pusher that drive by the transmission mechanism differential, rotary drum comprise at the bottom of the rotary drum and be arranged on rotary drum at the bottom of on rotary drum, rotary drum is arranged in the casing, described pusher comprises at the bottom of the inner core and inner core that is set together, the outer wall of inner core is provided with the spiral pusher leaf, be provided with trumpet-shaped charge door in the inner core, this charge door is connected with the charge pipe of feeding device, inner core is offering at least one pair of material path near the inner core bottom, described rotary drum is being provided with filter screen near the discharging opening place, be provided with at least one overfall at the bottom of the rotary drum, all overfalls communicate with heavy purified liquor outlet with heavy clear liquid chamber between the casing by rotary drum.
Be provided with four overfalls at the bottom of the described rotary drum, the concrete set-up mode of each overfall is: be provided with the circular arc installation base at the bottom of the rotary drum, the overflow plate that is positioned at the overfall outside is made of inside and outside baffle plate, the outer of interior side shield is provided with the circular arc that matches with installation base groove is installed, also offer a pair of locking screw pit and the locking hole that matches with clamping screw on the inside and outside baffle plate respectively, inside and outside baffle plate is locked on the installation base by clamping screw.
Another technical problem to be solved by this invention is: a kind of dismounting rotary drum helical-conveyer centrifugal very easily is provided.
For solving another above-mentioned technical problem, the technical solution used in the present invention is: described transmission mechanism comprises: be bearing in the differential mechanism in the fuselage and rotary drum axle that links to each other with differential mechanism and pusher axle by pair of bearings, described rotary drum and pusher be positioned at this to side of bearing and rotary drum at the bottom of with the inner core of pusher at the bottom of link to each other with the pusher axle with the rotary drum axle respectively, this opposite side to bearing is provided with driven spider gear and the driven drive that links to each other with differential mechanism; Described rotary drum is made of big straight tube, little straight tube and the conically shaped that connects large and small straight tube, is detachable minute body structure between big straight tube and the conically shaped.
Described inner core offers several washing holes in the outside of its charge door, is equipped with sluicing pipe in the described feed pipe, offers on the sluicing pipe and several fluid holes that matches with washing hole.
The invention has the beneficial effects as follows: the pusher among the present invention is provided with inner core, the charge pipe of feeding device links to each other with charge door in the inner core, slurry quickens the back and enters rotary drum from material path in inner core, because stopping of spiral pusher leaf, slurry in rotary drum owing to obtain sedimentation and enrichment, the slurry of enrichment discharging opening to rotary drum under the promotion of spiral pusher leaf moves, and filtrate throws away from the filter screen on the little straight tube, and solid-phase material is pushed into out feed bin.Owing to increased the sedimentation concentrating function, the present invention just can be used for separating solid concentration at the slurry below 25%.Can also regulate the size of overfall by the relative position of adjusting inside and outside baffle plate and installation base according to actual needs, thereby reach the purpose of improving the sedimentation concentrated effect.In addition, the present invention is also by being arranged on rotary drum one side of pair of bearings, and rotary drum is arranged to split-type structural, makes the dismounting of rotary drum become very convenient, so just greatly facilitates the line services such as cleaning of rotary drum.Also have, this centrifuge is also offering washing hole, is being provided with sluicing pipe in charge pipe on the inner core, make slurry clean earlier before strainer filtering, can improve the purity of filter residue so greatly, thereby improves the quality of finished product.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is a structure for amplifying schematic diagram local among Fig. 1;
Fig. 3 is the structure for amplifying schematic diagram of Internal baffle among Fig. 1;
Fig. 4 is the structure for amplifying schematic diagram of outer baffle among Fig. 1;
Among Fig. 1 to Fig. 4: 1, support, 11, fuselage, 12, casing, 13, damper, 2, fore bearing, 3, rear bearing, 4, differential mechanism, 5, rotary drum, 50, the rotary drum axle, 51, big straight tube, 52, taper is little, 53, little straight tube, 54, overfall, 55, installation base, 56, Internal baffle, 57, outer baffle, 58, groove is installed, 6, pusher, 60, the pusher axle, 61, the pusher leaf, 62, charge door, 63, material path, 64, washing hole, 7, charge pipe, 8, sluicing pipe, 9, driven spider gear, 10, driven drive, 20, heavy clear liquid chamber, 21, heavy purified liquor outlet, 22, filtrate channel, 23, filtrate (liquid, 24, go out feed bin.
The specific embodiment
Below in conjunction with accompanying drawing, describe specific embodiments of the present invention in detail.
As Fig. 1, shown in Figure 2, helical-conveyer centrifugal of the present invention, comprise: support 1 and the fuselage 11 and the casing 12 that are arranged on the support 1, the lubricating structure that is provided with transmission mechanism in the fuselage 11 and matches with transmission mechanism, and the rotary drum 5 and the pusher 6 that drive by the transmission mechanism differential, described rotary drum 5 comprise at the bottom of the rotary drum and be arranged on rotary drum at the bottom of on rotary drum, rotary drum 5 is arranged in the casing 12, described pusher 6 comprises at the bottom of the inner core and inner core that is set together, the outer wall of inner core is provided with spiral pusher leaf 61, be provided with trumpet-shaped charge door 62 in the inner core, charge door 62 is connected with the charge pipe 7 of feeding device, inner core is offering at least one pair of material path 63 near the inner core bottom, described rotary drum is by big straight tube 51, little straight tube 53 and connection are big, the conically shaped 52 of little straight tube 51 and 53 constitutes, wherein: between big straight tube 51 and the conically shaped 52 is detachable branch body structure, rotary drum is that little straight tube 53 is provided with filter screen near the discharging opening place, be provided with four overfalls 54 at the bottom of the rotary drum, the concrete set-up mode of each overfall is: be provided with circular arc installation base 55 at the bottom of the rotary drum, as shown in Figure 3, the overflow plate that is positioned at overfall 54 outsides by, outer baffle 56 and 57 constitutes, the outer of Internal baffle 56 is provided with the circular arc that matches with installation base 55 groove 58 is installed, offer three locking screw pits that match with clamping screw on the Internal baffle 56, offer three locking holes that match with the locking screw pit on the outer baffle 57, in, outer baffle 56 and 57 is locked on the installation base 55 by clamping screw---and installation base 55 is arranged in the installation groove 58 of Internal baffle 56; Overfall 54 communicates with heavy purified liquor outlet 21 with heavy clear liquid chamber 20 between the casing 12 by rotary drum 5.In the present embodiment, described transmission mechanism comprises: be arranged on differential mechanism 4 and rotary drum axle 50 that links to each other with differential mechanism 4 and pusher axle 60 in the fuselage 11 by forward and backward bearing 2 and 3, described rotary drum 5 and pusher 6 link to each other with pusher axle 60 with rotary drum axle 50 respectively at the bottom of being positioned at the bottom of the rotary drum of forward and backward bearing 2 and 3 side and rotary drum 5 inner core with pusher 6, and forward and backward bearing 2 is provided with driven spider gear 9 and the driven drive 10 that links to each other with differential mechanism 4 with 3 opposite side; The inner core of described pusher 6 offers several washing holes 64 in the outside of its charge door 62, be equipped with sluicing pipe 8 in the described feed pipe 7, offers on the sluicing pipe 8 and several fluid holes that matches with washing hole 64.
Claims (4)
1. helical-conveyer centrifugal, comprise: support and the fuselage and the casing that are arranged on the support, the lubricating structure that is provided with transmission mechanism in the fuselage and matches with transmission mechanism, and the rotary drum and the pusher that drive by the transmission mechanism differential, rotary drum comprises: at the bottom of the rotary drum and the rotary drum on being arranged at the bottom of the rotary drum, rotary drum is arranged in the casing, it is characterized in that: described pusher comprises: at the bottom of the inner core and inner core that is set together, the outer wall of inner core is provided with the spiral pusher leaf, be provided with trumpet-shaped charge door in the inner core, this charge door is connected with the charge pipe of feeding device, inner core is offering at least one pair of material path near the inner core bottom, described rotary drum is being provided with filter screen near the discharging opening place, be provided with at least one overfall at the bottom of the rotary drum, all overfalls communicate with heavy purified liquor outlet with heavy clear liquid chamber between the casing by rotary drum.
2. helical-conveyer centrifugal as claimed in claim 1, it is characterized in that: be provided with four overfalls at the bottom of the described rotary drum, the concrete set-up mode of each overfall is: be provided with the circular arc installation base at the bottom of the rotary drum, the overflow plate that is positioned at the overfall outside is made of inside and outside baffle plate, the outer of interior side shield is provided with the circular arc that matches with installation base groove is installed, also offer a pair of locking screw pit and the locking hole that matches with clamping screw on the inside and outside baffle plate respectively, inside and outside baffle plate is locked on the installation base by clamping screw.
3. helical-conveyer centrifugal as claimed in claim 1 or 2, it is characterized in that: described transmission mechanism comprises: be bearing in the differential mechanism in the fuselage and rotary drum axle that links to each other with differential mechanism and pusher axle by pair of bearings, described rotary drum and pusher be positioned at this to side of bearing and rotary drum at the bottom of with the inner core of pusher at the bottom of link to each other with the pusher axle with the rotary drum axle respectively, this opposite side to bearing is provided with driven spider gear and the driven drive that links to each other with differential mechanism; Described rotary drum is made of big straight tube, little straight tube and the conically shaped that connects large and small straight tube, is detachable minute body structure between big straight tube and the conically shaped.
4. helical-conveyer centrifugal as claimed in claim 1 or 2, it is characterized in that: described inner core offers several washing holes in the outside of its charge door, be equipped with sluicing pipe in the described feed pipe, offer on the sluicing pipe and several fluid holes that matches with washing hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100227132A CN101327466A (en) | 2008-07-08 | 2008-07-08 | Helical-conveyer centrifugal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100227132A CN101327466A (en) | 2008-07-08 | 2008-07-08 | Helical-conveyer centrifugal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101327466A true CN101327466A (en) | 2008-12-24 |
Family
ID=40203608
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2008100227132A Pending CN101327466A (en) | 2008-07-08 | 2008-07-08 | Helical-conveyer centrifugal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101327466A (en) |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102698881A (en) * | 2012-05-18 | 2012-10-03 | 江苏赛德力制药机械制造有限公司 | Cantilevered spiral discharging settling centrifuge |
| CN102974473A (en) * | 2012-12-04 | 2013-03-20 | 江苏牡丹离心机制造有限公司 | Material concentration pre-increased spiral discharging and filtering centrifuge |
| CN103285649A (en) * | 2013-06-04 | 2013-09-11 | 江西桃苑农牧科技有限公司 | Organic matter solid-liquid separator |
| CN104084318A (en) * | 2014-07-17 | 2014-10-08 | 赵来宁 | Rotating cage and spiral solid-liquid separator |
| CN104525391A (en) * | 2014-12-31 | 2015-04-22 | 江苏华大离心机股份有限公司 | Horizontal centrifuge preventing feed from flowing backwards |
| CN104624395A (en) * | 2014-12-31 | 2015-05-20 | 江苏华大离心机股份有限公司 | Horizontal centrifugal machine with scraper device |
| CN104896287A (en) * | 2015-05-23 | 2015-09-09 | 安徽普源分离机械制造有限公司 | High-speed horizontal type spiral discharging decanting centrifuge bearing lubricating system |
| CN104907187A (en) * | 2015-05-29 | 2015-09-16 | 上海铠镝贸易有限公司 | Multi-stage type helical screen continuous centrifuge |
| CN106495269A (en) * | 2016-11-08 | 2017-03-15 | 东莞市天合机电开发有限公司 | A kind of centrifugal solid-liquid separator |
| CN108187918A (en) * | 2017-06-09 | 2018-06-22 | 上海亭博分离技术有限公司 | Alpha type high-strength gypsum centrifuge |
| CN110694750A (en) * | 2019-10-22 | 2020-01-17 | 上海琥崧智能科技股份有限公司 | Spiral discharging horizontal sand mill and spiral discharging method |
| CN111185308A (en) * | 2020-03-09 | 2020-05-22 | 上海亭博分离技术有限公司 | Centrifugal machine for separating chemical wastewater |
| CN112604820A (en) * | 2020-12-04 | 2021-04-06 | 成都高分离心机有限公司 | Horizontal screw centrifuge and separation washing process |
| CN112626791A (en) * | 2020-12-22 | 2021-04-09 | 李贤富 | Uniform material distribution washing device of centrifugal machine |
| CN112973974A (en) * | 2019-12-18 | 2021-06-18 | 江苏兴科制药设备制造有限公司 | Sedimentation and filtration two-in-one centrifugal machine |
| CN115228625A (en) * | 2022-07-18 | 2022-10-25 | 江苏同泽过滤科技有限公司 | Installation structure of sedimentation and filtering mechanism in sedimentation filtering centrifuge |
| CN118142720A (en) * | 2024-05-13 | 2024-06-07 | 江苏同泽过滤科技有限公司 | Sedimentation filtering, cleaning and drying centrifugal machine |
| CN118577398A (en) * | 2024-08-02 | 2024-09-03 | 山东华盛创新纺织科技有限公司 | A centrifugal processing device for yarn raw materials |
-
2008
- 2008-07-08 CN CNA2008100227132A patent/CN101327466A/en active Pending
Cited By (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102698881A (en) * | 2012-05-18 | 2012-10-03 | 江苏赛德力制药机械制造有限公司 | Cantilevered spiral discharging settling centrifuge |
| CN102974473A (en) * | 2012-12-04 | 2013-03-20 | 江苏牡丹离心机制造有限公司 | Material concentration pre-increased spiral discharging and filtering centrifuge |
| CN103285649A (en) * | 2013-06-04 | 2013-09-11 | 江西桃苑农牧科技有限公司 | Organic matter solid-liquid separator |
| CN104084318A (en) * | 2014-07-17 | 2014-10-08 | 赵来宁 | Rotating cage and spiral solid-liquid separator |
| CN104525391A (en) * | 2014-12-31 | 2015-04-22 | 江苏华大离心机股份有限公司 | Horizontal centrifuge preventing feed from flowing backwards |
| CN104624395A (en) * | 2014-12-31 | 2015-05-20 | 江苏华大离心机股份有限公司 | Horizontal centrifugal machine with scraper device |
| CN104624395B (en) * | 2014-12-31 | 2016-10-12 | 江苏华大离心机制造有限公司 | Horizontal centrifuge with doctor blade device |
| CN104896287A (en) * | 2015-05-23 | 2015-09-09 | 安徽普源分离机械制造有限公司 | High-speed horizontal type spiral discharging decanting centrifuge bearing lubricating system |
| CN104907187B (en) * | 2015-05-29 | 2019-05-03 | 上海铠镝贸易有限公司 | A kind of multisection type helical screens continuous centrifuge |
| CN104907187A (en) * | 2015-05-29 | 2015-09-16 | 上海铠镝贸易有限公司 | Multi-stage type helical screen continuous centrifuge |
| CN106495269B (en) * | 2016-11-08 | 2019-07-02 | 广东创美达环保科技有限公司 | A kind of centrifugal solid-liquid separator |
| CN106495269A (en) * | 2016-11-08 | 2017-03-15 | 东莞市天合机电开发有限公司 | A kind of centrifugal solid-liquid separator |
| CN108187918A (en) * | 2017-06-09 | 2018-06-22 | 上海亭博分离技术有限公司 | Alpha type high-strength gypsum centrifuge |
| CN110694750A (en) * | 2019-10-22 | 2020-01-17 | 上海琥崧智能科技股份有限公司 | Spiral discharging horizontal sand mill and spiral discharging method |
| CN112973974A (en) * | 2019-12-18 | 2021-06-18 | 江苏兴科制药设备制造有限公司 | Sedimentation and filtration two-in-one centrifugal machine |
| CN111185308A (en) * | 2020-03-09 | 2020-05-22 | 上海亭博分离技术有限公司 | Centrifugal machine for separating chemical wastewater |
| CN112604820A (en) * | 2020-12-04 | 2021-04-06 | 成都高分离心机有限公司 | Horizontal screw centrifuge and separation washing process |
| CN112626791A (en) * | 2020-12-22 | 2021-04-09 | 李贤富 | Uniform material distribution washing device of centrifugal machine |
| CN112626791B (en) * | 2020-12-22 | 2023-05-09 | 湘潭离心机有限公司 | Uniform material distribution washing device of centrifugal machine |
| CN115228625A (en) * | 2022-07-18 | 2022-10-25 | 江苏同泽过滤科技有限公司 | Installation structure of sedimentation and filtering mechanism in sedimentation filtering centrifuge |
| CN115228625B (en) * | 2022-07-18 | 2023-11-14 | 江苏同泽过滤科技有限公司 | Installation structure of sedimentation and filtration mechanism in sedimentation and filtration centrifuge |
| CN118142720A (en) * | 2024-05-13 | 2024-06-07 | 江苏同泽过滤科技有限公司 | Sedimentation filtering, cleaning and drying centrifugal machine |
| CN118142720B (en) * | 2024-05-13 | 2024-07-02 | 江苏同泽过滤科技有限公司 | Sedimentation filtering, cleaning and drying centrifugal machine |
| CN118577398A (en) * | 2024-08-02 | 2024-09-03 | 山东华盛创新纺织科技有限公司 | A centrifugal processing device for yarn raw materials |
| CN118577398B (en) * | 2024-08-02 | 2024-11-05 | 山东华盛创新纺织科技有限公司 | A centrifugal processing device for yarn raw materials |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101327466A (en) | Helical-conveyer centrifugal | |
| RU2223151C2 (en) | Centrifugal with additional section of rotor | |
| CN103415348A (en) | Centrifugal dehydration method and centrifugal dehydration device | |
| CN101806530A (en) | Vertical centrifugal hydroextractor | |
| CN201257404Y (en) | Helical conveyer centrifugal | |
| CN105921290B (en) | A kind of pre-separation type vertical centrifugal machine | |
| CN213315618U (en) | Horizontal spiral filtering centrifuge | |
| CN111185308A (en) | Centrifugal machine for separating chemical wastewater | |
| CN103212487A (en) | Forced-discharging and self-cleaning type centrifugal throwing machine | |
| CN111495612A (en) | Horizontal spiral filtering centrifuge | |
| CN102974473A (en) | Material concentration pre-increased spiral discharging and filtering centrifuge | |
| CN112387427B (en) | Decanter centrifuge | |
| CN106694241B (en) | Horizontal spiral discharge sedimentation centrifuge | |
| CN117065454A (en) | Sedimentation and filtration composite centrifuge | |
| CN203853184U (en) | Composite filter cloth frame type drum device for double-stage centrifugal discharge centrifuges | |
| CN111729762B (en) | Multi-cone sedimentation filter centrifuge | |
| CN212328620U (en) | Centrifugal machine for separating chemical wastewater | |
| CN213727168U (en) | Horizontal screw centrifugal machine | |
| CN213051091U (en) | Multi-cone sedimentation filter centrifuge | |
| CN2780337Y (en) | Upper overflow type settling centrifugal | |
| CN222019771U (en) | A symmetrical double siphon centrifuge | |
| CN115259615A (en) | Horizontal screw sedimentation centrifugal dehydrator for slurry screening and dewatering | |
| CN209333977U (en) | A kind of horizontal spiral discharge sedimentation centrifuge | |
| CN111495616A (en) | Rotary drum device for horizontal spiral filtering centrifuge | |
| JP4163050B2 (en) | Upper solids reflux type screw conveyor centrifugal dehydrator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20081224 |