CN104043270A - Continuous subsider - Google Patents
Continuous subsider Download PDFInfo
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- CN104043270A CN104043270A CN201410278140.5A CN201410278140A CN104043270A CN 104043270 A CN104043270 A CN 104043270A CN 201410278140 A CN201410278140 A CN 201410278140A CN 104043270 A CN104043270 A CN 104043270A
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- subsider
- cell body
- drive
- overfall
- blades
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Abstract
The invention discloses a continuous subsider, wherein the subsider is a cylindrical groove body; the middle part of the groove body is provided with a cylindrical material well structure; the side part of the groove body is provided with an overflow opening; the bottom of a drive shaft is provided with two drive blades; the top ends of the drive blades are connected to the upper part of the drive shaft by connecting ropes; a plurality of swing blades are uniformly distributed below the drive blades; the swing blades are movably connected below the drive blades by rotary shafts. According to the invention, the structures of a material well, the overflow opening and the drive blades are matched with the drive blades under the gravity effect to form centrifugal force, the subsiding effect in the subsider is improved integrally in the process of stirring at a low speed; meanwhile, a charging pipeline for charging continuously and the overflow opening for discharging continuously are matched, so that the subsider meets the requirement of continuous industrial production.
Description
Technical field
The present invention relates to chemical separating apparatus field, relate in particular to a kind of highly effective continuous subsider that is applicable to suspension.
Background technology
Subsider is by means of Action of Gravity Field, utilizes the density contrast between decentralized photo and continuous phase, makes both produce relative motion, thereby realizes separated between particle and fluid.Because need to utilizing gravitational settling effect, subsider completes separated between particle and fluid, therefore the standing suspension liquid of general employing is to reach the object of Separation of Solid and Liquid, but standing reaction system is difficult to carry out successive reaction, be not suitable for the demand that modernization industry is produced.
Also there is on the market centrifugal subsider simultaneously, by centrifugal force, completing sedimentation operates, but this kind of subsider need to be accompanied by centrifugal mixer in infall process always, in continuous flow procedure, be difficult to discharge the clear liquid on upper strata, therefore common centrifugation apparatus is difficult to meet the continuous sedimentation requirement in consecutive production process.
Summary of the invention
For the problem of above-mentioned existence, it is a kind of simple to operate that the object of the invention is to provide, the industrial continous way subsider of applicable serialization of convenience and high-efficiency.
In order to achieve the above object, the technical solution used in the present invention is as follows: a kind of continous way subsider, described subsider is columniform cell body, the bottom surface of described cell body is taper bottom surface, described cell body middle part is provided with turning cylinder, described turning cylinder is by drive and driving belt connection for transmission motor, described cell body middle part is provided with columniform material well construction, the side of described cell body is provided with overfall, the bottom of described power transmission shaft is provided with two drive blades, the top of described drive blade is connected to the top of power transmission shaft by connection cord, the below of described drive blade is evenly distributed with a plurality of oscillating vanes, described oscillating vane is movably connected in drive blade below by rotating shaft.
The aboveground side of material of the present invention is provided with feed pipe, and the middle part of described taper bottom surface is provided with thick slurry mouthful; By the suspension raw material of expecting that aboveground side's feed pipe passes into, facilitate suspension to be blended into rapidly in tank liquor, convenient separated rapidly, the thick of bottom starched mouth for discharging because the solid particle under centrifugal force and Action of Gravity Field, the bottom surface structure that coordinates taper, the discharge of thick slurry is effective.
Cell body of the present invention top is provided with covering plate structure, and the setting height(from bottom) of described overfall is lower than the setting height(from bottom) 5-10cm of cover plate, and described overfall is provided with vertically arranged filter screen structure; By the sealing effectiveness of covering plate structure assurance device, and be used for discharging supernatant liquor lower than the overfall of cover plate, prevent that liquid-liquid from overflowing, be applicable to continuous process and produce.
The setting height(from bottom) of the bottom of material well of the present invention is lower than the setting height(from bottom) 20-30cm of overfall; By being arranged on square stock well under overfall, suspension directly can be joined to the liquid level below in trough body structure; Prevent liquid splash, can guarantee that suspension is under the effect of centrifugal force, be scattered in rapidly in groove, improve the effect of settling of device simultaneously.
The invention has the advantages that: the present invention is by being arranged on the material well at cell body middle part, overfall and drive blade structure, the centrifugal force forming while coordinating drive blade to rotate under Action of Gravity Field, rotation by oscillating vane along with drive blade, improved the contact area of the tank liquor of drive blade, in the process of stirring at low speed, improve the effect of centrifugal mixer, and then improved the effect of settling in bulk settling groove, the overfall that simultaneously coordinates feed intake pipeline and the continuous discharge of continuous feed, thick slurry mouthful, make subsider meet the industrial needs of serialization, simple to operation, good practical effect.
Accompanying drawing explanation
Fig. 1 is structure diagram of the present invention;
Fig. 2 is oscillating vane mounting structure sketch of the present invention;
Wherein, 1 cell body, 2 turning cylinders, 3 taper bottom surfaces, 4 overfalls, 5 filter screen structures, 6 material well constructions, 7 feed pipes, 8 covering plate structures, 9 drive blades, 10 connection cords, 11 oscillating vanes, 12 thick slurries mouthful, 13 rotating shafts.
The specific embodiment
Below in conjunction with accompanying drawing explanation and the specific embodiment, the present invention is described in further detail.
embodiment 1:a kind of continous way subsider as illustrated in fig. 1 and 2, described subsider is columniform cell body 1, the bottom surface of described cell body 1 is taper bottom surface 3, described cell body 1 middle part is provided with turning cylinder 2, described turning cylinder 2 is by drive and driving belt connection for transmission motor, described cell body 1 middle part is provided with columniform material well construction 6, the side of described cell body 1 is provided with overfall 4, the bottom of described power transmission shaft 6 is provided with two drive blades 9, the top of described drive blade 9 is connected to the top of power transmission shaft 2 by connection cord 10, the below of described drive blade 9 is evenly distributed with a plurality of oscillating vanes 11, described oscillating vane 11 is movably connected in the below of drive blade 9 by rotating shaft 13.
embodiment 2:as shown in Figure 1, described material well 6 tops are provided with feed pipe 7, and the middle part of described taper bottom surface 3 is provided with thick slurry mouth 12; By the suspension raw material of expecting that the feed pipe 7 of well 6 tops passes into, facilitate suspension to be blended into rapidly in tank liquor, convenient separated rapidly, the thick of bottom starched mouth 12 for discharging because the solid particle under centrifugal force and Action of Gravity Field, the bottom surface structure 3 that coordinates taper, the discharge of thick slurry is effective.
embodiment 3:as shown in Figure 1, described cell body 1 top is provided with covering plate structure 8, and the setting height(from bottom) of described overfall 4 is lower than the setting height(from bottom) 5-10cm of cover plate 8, and described overfall 4 is provided with vertically arranged filter screen structure 5; By covering plate structure, protect the sealing effectiveness of 8 card devices, and lower than the overfall 4 of cover plate 8 for discharging supernatant liquor, prevent that liquid-liquid from overflowing, be applicable to continuous process and produce.
embodiment 4:as shown in Figure 1, the setting height(from bottom) of the bottom of described material well 6 is lower than the setting height(from bottom) 20-30cm of overfall 4; By being arranged on 4 times square stock wells 6 of overfall, suspension directly can be joined to the liquid level below in trough body structure; Prevent liquid splash, can guarantee that suspension is under the effect of centrifugal force, be scattered in rapidly in groove, improve the effect of settling of device simultaneously.
It should be noted that, above-mentioned is only preferred embodiment of the present invention, is not used for limiting protection scope of the present invention, and the equivalents of having done on the basis of above-described embodiment all belongs to protection scope of the present invention.
Claims (4)
1. a continous way subsider, described subsider is columniform cell body, the bottom surface of described cell body is taper bottom surface, described cell body middle part is provided with turning cylinder, described turning cylinder is by drive and driving belt connection for transmission motor, it is characterized in that, described cell body middle part is provided with columniform material well construction, the side of described cell body is provided with overfall, the bottom of described power transmission shaft is provided with two drive blades, the top of described drive blade is connected to the top of power transmission shaft by connection cord, the below of described drive blade is evenly distributed with a plurality of oscillating vanes, described oscillating vane is movably connected in drive blade below by rotating shaft.
2. continous way subsider according to claim 1, is characterized in that, the aboveground side of described material is provided with feed pipe, and the middle part of described taper bottom surface is provided with thick slurry mouthful.
3. continous way subsider according to claim 1, it is characterized in that, described cell body top is provided with covering plate structure, and the setting height(from bottom) of described overfall is lower than the setting height(from bottom) 5-10cm of cover plate, and described overfall is provided with vertically arranged filter screen structure.
4. continous way subsider according to claim 1, is characterized in that, the setting height(from bottom) of the bottom of described material well is lower than the setting height(from bottom) 20-30cm of overfall.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410278140.5A CN104043270A (en) | 2014-06-20 | 2014-06-20 | Continuous subsider |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410278140.5A CN104043270A (en) | 2014-06-20 | 2014-06-20 | Continuous subsider |
Publications (1)
Publication Number | Publication Date |
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CN104043270A true CN104043270A (en) | 2014-09-17 |
Family
ID=51496970
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201410278140.5A Pending CN104043270A (en) | 2014-06-20 | 2014-06-20 | Continuous subsider |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106621487A (en) * | 2016-11-30 | 2017-05-10 | 尹国祥 | Slurry draining bottom plate for continuous settling tank |
CN106621486A (en) * | 2016-11-30 | 2017-05-10 | 尹国祥 | A continuous settling tank |
CN113601886A (en) * | 2021-08-03 | 2021-11-05 | 李华飞 | Filtrate separation equipment for soil remediation system and separation method thereof |
CN114307345A (en) * | 2022-01-05 | 2022-04-12 | 薛黎明 | Sewage treatment equipment suitable for urban sewage treatment |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1504255A (en) * | 2002-11-28 | 2004-06-16 | 天津渤海化工有限责任公司天津化工厂 | High-efficient thickener apparatus |
CN201052427Y (en) * | 2007-04-06 | 2008-04-30 | 李全德 | Vertical continuous centrifugal dewaterer |
US20090173701A1 (en) * | 2005-11-23 | 2009-07-09 | Kadant Black Clawson Inc. | Centrifugal Flow Distribution Clarifier Feedwell and Method of Feeding Influent to a Clarifier Thereby |
-
2014
- 2014-06-20 CN CN201410278140.5A patent/CN104043270A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1504255A (en) * | 2002-11-28 | 2004-06-16 | 天津渤海化工有限责任公司天津化工厂 | High-efficient thickener apparatus |
US20090173701A1 (en) * | 2005-11-23 | 2009-07-09 | Kadant Black Clawson Inc. | Centrifugal Flow Distribution Clarifier Feedwell and Method of Feeding Influent to a Clarifier Thereby |
CN201052427Y (en) * | 2007-04-06 | 2008-04-30 | 李全德 | Vertical continuous centrifugal dewaterer |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106621487A (en) * | 2016-11-30 | 2017-05-10 | 尹国祥 | Slurry draining bottom plate for continuous settling tank |
CN106621486A (en) * | 2016-11-30 | 2017-05-10 | 尹国祥 | A continuous settling tank |
CN106621487B (en) * | 2016-11-30 | 2019-02-12 | 尹国祥 | A kind of continuous subsider |
CN106621486B (en) * | 2016-11-30 | 2019-02-12 | 尹国祥 | A kind of continuous subsider |
CN113601886A (en) * | 2021-08-03 | 2021-11-05 | 李华飞 | Filtrate separation equipment for soil remediation system and separation method thereof |
CN113601886B (en) * | 2021-08-03 | 2023-10-13 | 李华飞 | Filtrate separation equipment for soil remediation system and separation method thereof |
CN114307345A (en) * | 2022-01-05 | 2022-04-12 | 薛黎明 | Sewage treatment equipment suitable for urban sewage treatment |
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Application publication date: 20140917 |