CN102512853B - Nano powder slurry settling tank - Google Patents
Nano powder slurry settling tank Download PDFInfo
- Publication number
- CN102512853B CN102512853B CN201110383495.7A CN201110383495A CN102512853B CN 102512853 B CN102512853 B CN 102512853B CN 201110383495 A CN201110383495 A CN 201110383495A CN 102512853 B CN102512853 B CN 102512853B
- Authority
- CN
- China
- Prior art keywords
- feed bin
- plate
- swash plate
- overflow
- sedimentation
- 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 - Fee Related
Links
Images
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The invention relates to a nano powder slurry settling tank, which belongs to the technical field of liquid-solid separation of nano powder slurry, and comprises a trough, a stock bin and an upper sloping plate, wherein the trough comprises a left side plate, a right side plate, a front side plate, a rear side plate and a base plate; the stock bin comprises a feeding bin, a settling bin, a baffling bin, an overflowing bin, a discharging bin and a nano powder collecting bin; the upper sloping plate comprises a settling bin upper short sloping plate, a baffling bin upper short sloping plate, a settling bin upper long sloping plate, a baffling bin upper long sloping plate, a feeding bin short clapboard, a feeding bin overflow plate, an overflowing bin overflow plate, a lower large sloping plate, a lower small sloping plate, a support rib plate and slurry channels (A, B, C, D and E); and discharge valves are respectively arranged on two sides of the lower part of the right side plate. When in use, the settling tank can carry out continuous feed and continuous discharge. The nano powder slurry settling tank has the beneficial effects that: the settling speed of the nano powder slurry is fast, and the yield is high; the structural design is reasonable, and nano powder can be completely collected on the bottom part of equipment; the equipment has a small size and is easy to maintain; and the settling tank meets environmental protection requirement without generating any pollution.
Description
Technical field
The present invention is a kind of powder slurries subsider, and particularly a kind of nano powder slurry settling tank belongs to the technical field of the liquid-solid separation of nanometer powder slurry.
background technology
The production process of nanometer powder is, before this burden process: medium additive is reacted with plurality of raw materials, get rid of multiple useless molecule (impurity), control content, concentration, acid-base value well, make to generate satisfactory heavy metal nanometer powder slurry; Next is liquid-solid separation circuit: in the situation that concentration, proportion and slurry pattern that needs are controlled are sent heavy metal nanometer powder slurry into centrifuge and carried out Separation of Solid and Liquid; Be finally sedimentation operation: the nanometer powder slurry that the machine of being centrifuged is separated enters sedimentation operation, finally heavy metal nanometer powder solia particle separated completely from liquid nano powder slurries.In above-mentioned operation, burden process and liquid-solid separation circuit are maturation process, and key is last nanometer powder slurry sedimentation operation, on the yield of sinking speed and nanometer powder, does not reach desirable effect.
Existing sedimentation operation referenced device has circular and two kinds of equipment of square sedimentation, and circular precipitation apparatus is because volume is limited, and the rate of settling is fallen slowly, and multiplex reaction equation sedimentation increases effect.As shown in Figure 1, existing square precipitation apparatus is very general to not reacting deadweight sedimentation process, but internal structure arranges unreasonable, subregion not between decanting zone, swash plate design is improper, the rate of settling cannot design, do not have flow control, tomography is obvious, and sedimentation vortex is obvious, the formation that is unfavorable for settling bin, user can better not utilize subsider internal production to accelerate quality and the speed of sedimentation; Existing square precipitation apparatus bottom does not arrange declined board, and structure stress supports unreasonable, easily distortion; Without nanometer powder collection structure, nanometer powder is collected not thorough, cell body material is polluted, and does not meet environmental requirement.
summary of the invention
The object of the invention is in above-mentioned prior art, the rate of settling of nanometer powder is slow, yield is low, and the defect of not environmental protection of infall process, provides a kind of nano powder slurry settling tank, can reach that the nanometer powder slurry rate of settling is fast, yield is high, infall process meets the object of environmental protection.
The technical scheme that the present invention takes is to achieve these goals: a kind of nano powder slurry settling tank, comprise hopper, feed bin and inclined board, described hopper comprises a left side, right, before, back side panel and base plate, described right plate is provided with outlet valve, described feed bin comprises charging feed bin, sedimentation feed bin, baffling feed bin, overflow feed bin, discharging feed bin and nanometer powder are collected feed bin, described inclined board comprises short swash plate on sedimentation feed bin, short swash plate on baffling feed bin, long swash plate on long swash plate and baffling feed bin on sedimentation feed bin, also comprise charging feed bin breviseptum, charging feed bin overflow plate, overflow feed bin overflow plate, lower large swash plate, lower little swash plate, bearing rib and slurry passage A, B, C, D, E,
Long swash plate, the setting in turn from left to right of overflow feed bin overflow plate on short swash plate, baffling feed bin on long swash plate, baffling feed bin on short swash plate, sedimentation feed bin in feed bin between described left and right side plate, on charging feed bin overflow plate, sedimentation feed bin, and the both sides of above-mentioned plate are fixedly connected with the forward and backward side plate of hopper;
Described charging feed bin breviseptum in charging feed bin, top, arrange vertical with left plate, charging feed bin breviseptum two ends are fixedly connected with left plate, charging feed bin overflow plate respectively, in order to increase hopper intensity; Described charging feed bin overflow plate and overflow feed bin overflow plate and baseplate vertical direction setting, the oblique setting of long swash plate right-to-left on short swash plate and baffling feed bin on long swash plate, baffling feed bin on short swash plate, sedimentation feed bin on sedimentation feed bin; Described bearing rib, on hopper base plate, along the parallel direction of front and back side plate, arranges with hopper base plate is vertical; Described lower large swash plate is in hopper bottom oblique setting from back to front, the rear side of lower large swash plate is fixedly connected with back side panel, the lower front side of large swash plate and the upper end of bearing rib are fixedly connected with, and the both sides of lower large swash plate are tight fit with charging feed bin overflow plate and overflow feed bin overflow plate respectively; Described lower little swash plate is in hopper bottom oblique setting from front to back, and the front side of lower little swash plate is fixedly connected with front side board, and the both sides of lower little swash plate are fixedly connected with overflow feed bin overflow plate with charging feed bin overflow plate respectively;
Described charging feed bin is between left plate and charging feed bin overflow plate, described sedimentation feed bin is on charging feed bin overflow plate and sedimentation feed bin between long swash plate, described baffling feed bin is on sedimentation feed bin on long swash plate and baffling feed bin between long swash plate, described overflow feed bin is on baffling feed bin between long swash plate and overflow feed bin overflow plate, described discharging feed bin is between overflow feed bin overflow plate and right plate, and described nanometer powder is collected feed bin in lower little swash plate bottom;
Described slurry passage A is arranged on charging feed bin overflow plate top, lower position in charging feed bin overflow plate upper end, charging feed bin and sedimentation feed bin interlink by slurry passage A, charging feed bin overflow plate plate face is from edge, groove top to bottom land, add vis in situ, the in the situation that of 3 cubes per hour of feed rate, guarantee containing the abundant overflow of nanometer powder oar material, so open this passage, not opening whole strip and circle is because feed liquid is insufficient evenly;
Described slurry channel B is arranged on long swash plate top on sedimentation feed bin, the lower position of long swash plate upper end on sedimentation feed bin, sedimentation feed bin and baffling feed bin interlink by slurry channel B, and slurry channel B guarantees the good liquid communication of part sedimentation, liquid part sedimentation herein;
Described slurry channel C is arranged on overflow feed bin overflow plate upper end, and overflow feed bin and discharging feed bin interlink by slurry channel C, and the height of slurry channel C setting has determined the effect of sedimentation, and in discharging feed bin, liquid is quite limpid, further fully sedimentation.Under circulation status, liquid level surface velocity is large, so the content of beary metal in this storehouse is quite few, can be considered heavy metal free completely, and slurry channel C feed liquid out represents that sedimentation is complete;
Described slurry passage D is arranged between lower large swash plate bottom and lower little swash plate lower end, and the bottom of sedimentation feed bin, baffling feed bin and overflow feed bin and nanometer powder are collected between feed bin, and by slurry passage, D interlinks; Slurry passage D is designed to so low, is further to carry out sedimentation.High words sedimentation meeting tomography, before the nanometer powder slurry of sedimentation feed bin and baffling feed bin can enter overflow storehouse from bottom, be unfavorable for like this sedimentation route and principle.The design of slurry passage D, makes nanometer powder slurry carry out sedimentation thoroughly, also can guarantee that sedimentation route is not changed;
Described slurry passage E is arranged on lower large swash plate bottom, overflow feed bin overflow plate bottom is provided with through hole, slurry passage E and discharging feed bin interlink by through hole, slurry passage E does not need outlet, it is excessive in order to prevent the gravitational pressure on the lower large swash plate of slurry passage E top allowing slurry passage E the inside be full of liquid level, can be out of shape, and keep pressure balance; Discharging bin space is too small in addition, and discharging bin and slurry passage E UNICOM make full use of the space of slurry passage E exactly.
Described outlet valve has 2, is separately positioned on both sides, right plate bottom.
Described slurry passage A is more than 2 oblong channel symmetrical on charging feed bin overflow plate top; Described slurry channel B is more than 2 small circular passage that long swash plate top is arranged side by side on sedimentation feed bin; Described slurry channel C is more than 2 the odontoid passage of serrate slot arranging in overflow feed bin overflow plate upper end; Described slurry passage D is that following large swash plate lower end and lower little swash plate lower end are the long and narrow gap on 2 long limits, and the width in gap is 40-60MM.
Described slurry passage A has 2 oblong channel; Described slurry channel B has 17 small circular passages; Described slurry channel C has 8 serrate slots, and slurry channel C is designed to lower triangle, is conducive to liquid flow, is conducive to stability of flow; The width in the gap of described slurry passage D is 50MM.
Described slurry passage D comprises slurry passage D front portion, D middle part and D rear portion, sedimentation feed bin is collected between feed bin and is communicated with by slurry passage D is anterior with nanometer powder, baffling feed bin is collected between feed bin and is communicated with by slurry passage D middle part with nanometer powder, and overflow feed bin is collected between feed bin and is communicated with by slurry passage D rear portion with nanometer powder; Between baffling feed bin and overflow feed bin, by slurry passage D middle part, nanometer powder, collect feed bin and slurry passage D rear portion is connected.
On described sedimentation feed bin on short swash plate, sedimentation feed bin on long swash plate, baffling feed bin on short swash plate and baffling feed bin the angle of long swash plate and vertical direction be α 15-20 °; The angle of lower large swash plate and vertical direction is β 75-85 °; The angle of lower little swash plate and vertical direction is γ 40-50 °.
On described sedimentation feed bin on short swash plate, sedimentation feed bin on long swash plate, baffling feed bin on short swash plate and baffling feed bin the gradient of long swash plate and vertical direction be 16 ° of α; The angle of lower large swash plate and vertical direction is that 81 ° of β are 44 ° of γ with the angle of lower little swash plate and vertical direction.
On described sedimentation feed bin, on short swash plate and baffling feed bin, the degree of depth of short swash plate is the 3/10-1/2 of the hopper degree of depth.
On described sedimentation feed bin, on short swash plate and baffling feed bin, the degree of depth of short swash plate is 2/5 of the hopper degree of depth.
Described nanometer powder is collected in feed bin and is also provided with nanometer powder collecting pipe, reducing connector, gripper shoe and cleaning eye; Described nanometer powder collecting pipe is elongated shape pipe, is arranged on nanometer powder and collects feed bin middle part, parallels with hopper bottom; Nanometer powder collecting pipe bottom interval is provided with more than 2 groups small circular through holes, and every group has 1 above small circular through hole; Described reducing connector is arranged on the nanometer powder collecting pipe left side port of export, and reducing connector outside is connected with delivery pump A again; Described gripper shoe is arranged between hopper bottom and nanometer powder collecting pipe, and gripper shoe and hopper bottom vertical arrange, and its lower end is fixedly connected with hopper bottom, and its upper end is fixedly connected with nanometer powder collecting pipe bottom; Described cleaning eye has 2, is separately positioned on lower little swash plate and the lower large swash plate below of hopper two side bottoms; Described right plate top is provided with overflow valve, liquid level valve A, and right plate bottom is also provided with liquid level valve B, blowoff valve, and described blowoff valve is at right plate foot, and described outlet valve is connected with the delivery pump B of outside again.
Nanometer powder collecting pipe bottom interval is provided with 12 groups of small circular through holes, and every group has 3 little shape round tube holes.
The infall process of nanometer powder in nano powder slurry settling tank: see Fig. 3, the nanometer powder slurry that the machine of being centrifuged is separated directly pours into charging feed bin; Slurry passage A from charging feed bin through feeding warehouse overflow plate top enters sedimentation feed bin, by sedimentation feed bin infall process, by the nanometer powder of sedimentation, through slurry passage D front portion, entered nanometer powder and collect feed bin, remaining nanometer powder slurry is from sedimentation feed bin after on sedimentation feed bin, turn back in short swash plate bottom, then the slurry channel B on long swash plate top enters baffling feed bin on sedimentation feed bin; At baffling feed bin, pass through baffling feed bin infall process, by the nanometer powder of sedimentation, through slurry passage D middle part, entered nanometer powder and collect feed bin, remaining nanometer powder slurry is first after on baffling feed bin, turn back in short swash plate bottom, on baffling feed bin, the slurry passage D of long swash plate bottom middle part enters nanometer powder and collects feed bin again, then through slurry passage D rear portion, enters overflow feed bin by nanometer powder collection feed bin; At overflow feed bin, through overflow feed bin infall process, entered nanometer powder collect feed bin by the nanometer powder of sedimentation through slurry passage D rear portion, remaining nanometer powder slurry enters discharging feed bin through the slurry channel C on overflow plate top; Finally at discharging feed bin, nanometer powder slurry, after last infall process, becomes the liquid that meets discharge standard, through the outlet valve of right plate, to delivery pump B output, send sewage disposal device to process.The nanometer powder that nanometer powder is collected feed bin reclaims by nanometer powder collecting pipe.
Nanometer powder infall process mechanism: in Fig. 3, nanometer powder slurry enters charging feed bin, until fill charging feed bin, start the overflow through slurry passage A, overflow is to sedimentation feed bin, after whole jetsam feed bin is filled, the liquid level of sedimentation feed bin is higher than the height of charging feed bin overflow plate spreading mass passage A, so when liquid enters sedimentation feed bin from charging feed bin, that extruding enters sedimentation feed bin, to guarantee the smoothness of sedimentation feed bin liquid; Sedimentation liquid, from the entering at the middle and upper levels sedimentation feed bin of charging feed bin liquid layer, is more conducive to the sedimentation of nanometer powder like this, less to the impact of sedimentation feed bin sedimentation.Same reason, nanometer powder slurry, after the overflow of slurry channel B, has also played the smoothness that guarantees baffling feed bin liquid, also less to the impact of baffling feed bin sedimentation.When charging feed bin liquid level fill with to spout hole be slurry passage A, overflow is to sedimentation feed bin, sedimentation feed bin liquid level increases thereupon, surpasses feeding warehouse spout hole; When sedimentation feed bin liquid level fill with to spout hole be slurry channel B, overflow is to baffling feed bin, baffling feed bin liquid level increases thereupon, surpass charging feed bin and sedimentation feed bin spout hole, again through overflow feed bin, discharging feed bin, overflow feed bin, discharging feed bin liquid level are increased thereupon, surpass charging feed bin and sedimentation feed bin spout hole, sedimentation forms.The liquid that enters so again charging feed bin will start sedimentation work, how much liquid of having come in, overflow feed bin will how much liquid of overflow to discharging feed bin.
Compared with prior art, the invention has the beneficial effects as follows:
(1) nanometer powder slurry sinking speed of the present invention is fast, yield is high: at centrifuge, carry out continuously under the state of Separation of Solid and Liquid, what produce contains useful nanometer powder liquid material from centrifuge flows out continuously, can reclaim fast and efficiently and process, its design has continuity and high efficiency, realized two-forty and high effect, can useful nanometer powder reclaimed quite thoroughly.
(2) reasonable in design, occupies little space, and equipment is small: the design of declined board and nanometer powder collecting pipe has solved the difficult problem that nanometer powder difficulty is received in square precipitation apparatus bottom; In continuity infall process, the flow velocity of 3 cubes per hour, the equipment profile that the unpowered design without auxiliary material of tradition need to be made is quite large; The in the situation that of limited space, the present invention has reduced and has taken up room, and practicality is high, and equipment is easily transformed and safeguarded.
(3) meet environmental requirement: without any power facility, cell body material is pollution-free, settling efficiency is high, be simple and easy to maintainability has become environmental protection main points of the present invention; Useful heavy metal nanometer powder in heavy metal slurry is recycled to country and below row internal standard value, and meets continuity work, without any power and supplementary product onsumption, do not produce any pollution;
Accompanying drawing explanation:
Fig. 1 is: former square precipitation apparatus structure chart;
Fig. 2 is: plan structure figure of the present invention;
Fig. 3 is: the A-A cutaway view of Fig. 2;
Fig. 4 is: the B-B cutaway view of Fig. 3;
Fig. 5 is: the C-C cutaway view of Fig. 3;
Fig. 6 is: the D-D cutaway view of Fig. 3;
Fig. 7 is: left plate structure chart of the present invention;
Fig. 8 is: charging feed bin overflow plate structure chart of the present invention;
Fig. 9 is: long swash plate structure chart on sedimentation feed bin of the present invention;
Figure 10 is: overflow feed bin overflow plate structure chart of the present invention;
Figure 11 is: right plate structure chart of the present invention;
Figure 12 is: front side board structure chart of the present invention;
Description of reference numerals: 1 hopper, 11 left plates, 12 right plates, 121 outlet valves, 122 overflow valves, 123 liquid level valve A, 124 liquid level valve B, 125 blowoff valves, 13 front side boards, 14 back side panels, 15 base plates, 2 feed bins, 21 charging feed bins, 22 sedimentation feed bins, 23 baffling feed bins, 24 overflow feed bins, 25 discharging feed bins, 26 nanometer powders are collected feed bin, 261 nanometer powder collecting pipes, 262 reducing connectors, 263 gripper shoes, 264 cleaning eyes, 265 small circular through holes, 3 inclined boards, short swash plate on 31 sedimentation feed bins, short swash plate on 32 baffling feed bins, long swash plate on 33 sedimentation feed bins, 331 small circular passages, long swash plate on 34 baffling feed bins, 4 charging feed bin breviseptums, 51 charging feed bin overflow plates, 52 overflow feed bin overflow plates, 521 through holes, 61 times large swash plates, 62 times little swash plates, 7 bearing ribs, 81 slurry passage A, 82 slurry channel B, 83 slurry channel C, 84 slurry passage D, 841 slurry passage D are anterior, 842 slurry passage D middle parts, 843 slurry passage D rear portions, 85 slurry passage E.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the invention will be further described, but not as a limitation of the invention.
As shown in Fig. 2-12, the present invention is directed to the take up room problem of the aspects such as build of equipment of speed by sedimentation quality and sedimentation and sedimentation, by following scheme, solve.A kind of nano powder slurry settling tank, comprise hopper 1, feed bin 2 and inclined board 3, described feed bin 2 is the inner chamber of hopper 1, described hopper 1 comprises left plate 11, right plate 12, front side board 13, back side panel 14 and base plate 15, described right plate 12 bottoms are provided with outlet valve 121, described feed bin comprises charging feed bin 21, sedimentation feed bin 22, baffling feed bin 23, overflow feed bin 24, discharging feed bin 25 and nanometer powder are collected feed bin 26, described inclined board 3 comprises short swash plate 31 on sedimentation feed bin, short swash plate 32 on baffling feed bin, long swash plate 34 on long swash plate 33 and baffling feed bin on sedimentation feed bin, also comprise charging feed bin breviseptum 4, charging feed bin overflow plate 51, overflow feed bin overflow plate 52, lower large swash plate 61, lower little swash plate 62, bearing rib 7 and slurry passage A81, B82, C83, D84, E85,
Long swash plate 34, overflow feed bin overflow plate 52 setting in turn from left to right on short swash plate 32, baffling feed bin on long swash plate 33, baffling feed bin on short swash plate 31, sedimentation feed bin in feed bin between described left and right side plate 11,12, on charging feed bin overflow plate 51, sedimentation feed bin, and the both sides of above-mentioned plate are fixedly connected with the forward and backward side plate 13,14 of hopper 1;
Described charging feed bin breviseptum 4 in charging feed bin 21, top, setting vertical with left plate 11, described charging feed bin overflow plate 51 and overflow feed bin overflow plate 52 and base plate 15 vertical direction settings, the oblique setting of long swash plate 34 right-to-left on short swash plate 32 and baffling feed bin on long swash plate 33, baffling feed bin on short swash plate 31, sedimentation feed bin on sedimentation feed bin; Described bearing rib 7 on hopper base plate 15, along the parallel direction of forward and backward side plate 13,14, setting vertical with hopper base plate 15; Described lower large swash plate 61 is in the oblique setting from back to front of hopper 1 bottom, the rear side of lower large swash plate 61 is fixedly connected with back side panel 14, the front side of lower large swash plate 61 is fixedly connected with the upper end of bearing rib 7, and the both sides of lower large swash plate 61 are tight fit with charging feed bin overflow plate 51 and overflow feed bin overflow plate 52 respectively; Described lower little swash plate 62 is in the oblique setting from front to back of hopper 1 bottom, and the front side of lower little swash plate 62 is fixedly connected with front side board 13, and the both sides of lower little swash plate 62 are fixedly connected with overflow feed bin overflow plate 52 with charging feed bin overflow plate 51 respectively;
Described charging feed bin 21 is between left plate 11 and charging feed bin overflow plate 51, described sedimentation feed bin 22 is on charging feed bin overflow plate 51 and sedimentation feed bin between long swash plate 33, described baffling feed bin 23 is on sedimentation feed bin on long swash plate 33 and baffling feed bin between long swash plate 34, described overflow feed bin 24 is on baffling feed bin between long swash plate 34 and overflow feed bin overflow plate 52, described discharging feed bin 25 is between overflow feed bin overflow plate 52 and right plate 12, and described nanometer powder is collected feed bin 26 in lower little swash plate 62 bottoms;
Described slurry passage A81 is arranged on charging feed bin overflow plate 51 tops, the lower position in charging feed bin overflow plate 51 upper ends, and charging feed bin 21 interlinks by slurry passage A81 with sedimentation feed bin 22; Described slurry channel B 82 is arranged on long swash plate 33 tops on sedimentation feed bin, the lower position of long swash plate 33 upper ends on sedimentation feed bin, and sedimentation feed bin and baffling feed bin 23 interlink by slurry channel B 82; Described slurry channel C 83 is arranged on overflow feed bin overflow plate 52 upper ends, and overflow feed bin 24 interlinks by slurry channel C 83 with discharging feed bin 25; Described slurry passage D84 is arranged between lower large swash plate 61 bottoms and lower little swash plate 62 lower ends, and the bottom of sedimentation feed bin 22, baffling feed bin 23 and overflow feed bin 24 and nanometer powder are collected between feed bin 26, and by slurry passage, D84 interlinks; Described slurry passage E85 is arranged on lower large swash plate 61 bottoms, and overflow feed bin overflow plate 52 bottoms are provided with through hole 521, and slurry passage E85 and discharging feed bin 25 interlink by through hole 521.
Described outlet valve 121 has 2, is separately positioned on right plate 12 both sides, bottom.
Described slurry passage A81 is in 2 symmetrical oblong channel of charging feed bin overflow plate 51 tops; Described slurry channel B 82 is 17 small circular passages 331 that long swash plate 33 tops are arranged side by side on sedimentation feed bin; Described slurry channel C 83 is the odontoid passage at 8 serrate slots of overflow feed bin overflow plate 52 upper ends settings; Described slurry passage D84 is that following large swash plate 61 lower ends and lower little swash plate 62 lower ends are the long and narrow gap on 2 long limits, and the width in gap is 50MM.
Described slurry passage D84 comprises slurry passage D front portion 841, D middle part 842 and D rear portion 843, sedimentation feed bin 22 is collected between feed bin 26 and is communicated with by slurry passage D anterior 841 with nanometer powder, baffling feed bin 23 and nanometer powder are collected between feed bin 26 and are communicated with by slurry passage D middle part 842, and overflow feed bin 24 and nanometer powder are collected between feed bin 26 by 83 connections of slurry passage D rear portion: between baffling feed bin 23 and overflow feed bin 24 by the middle part of slurry passage D 842, nanometer powder collection feed bin 26 and slurry passage D rear portion 843 be connected.
On described sedimentation feed bin on short swash plate 31, sedimentation feed bin on long swash plate 33, baffling feed bin on short swash plate 32 and baffling feed bin long swash plate 34 be 16 ° with the angle [alpha] of vertical direction; Lower large swash plate 61 is 81 ° with the angle beta of vertical direction; Lower little swash plate 62 is 44 ° with the angle γ of vertical direction.
On described sedimentation feed bin, on short swash plate 31 and baffling feed bin, the degree of depth of short swash plate 32 is 2/5 of hopper 1 degree of depth.
Described nanometer powder is collected in feed bin 26 and is also provided with nanometer powder collecting pipe 261, reducing connector 262, gripper shoe 263 and cleaning eye 264; Described nanometer powder collecting pipe 261 is elongated shape pipe, is arranged on nanometer powder and collects feed bin 26 middle parts, parallels with hopper 1 bottom; Nanometer powder collecting pipe 261 bottom intervals are provided with 12 groups of small circular through holes 265, and every group has 3 roundlet through holes 265; Described reducing connector 262 is arranged on the nanometer powder collecting pipe 26 left side ports of export, and reducing connector 262 outsides are connected with delivery pump A (not shown) again; Described gripper shoe 263 is arranged between hopper 1 bottom and nanometer powder collecting pipe 261, gripper shoe 263 and hopper 1 bottom vertical setting, and its lower end is fixedly connected with hopper 1 bottom, and its upper end is fixedly connected with nanometer powder collecting pipe 261 bottoms; Described cleaning eye 264 has 2, is separately positioned on lower little swash plate 62 and lower large swash plate 61 belows of 1 liang of side bottom of hopper; Described right plate 12 tops are provided with overflow valve 122, liquid level valve A123, and described overflow valve 122 is in outlet valve 121 or go out the situation that material conveying pump breaks down, and settlement prevention groove is that hopper 1 has little time to process, and at once carries out overflow.Right plate 12 bottoms are also provided with liquid level valve B124, blowoff valve 125; Described outlet valve 121 is connected with the delivery pump B (not shown) of outside again, carries the liquid that meets discharge standard by delivery pump B.Liquid level valve A123 and the liquid level valve B124 of described right plate 12 upper and lower parts are used for demonstrating material liquid surface lifting.Described blowoff valve 125 is at right plate 12 foots, and when sedimentation is broken down, in discharging feed bin 25, liquid exceeds standard containing nanometer powder amount, i.e. also further sedimentation in discharging feed bin, then drains through blowoff valve 125.The above reducing connector 262, overflow valve 122, liquid level valve A123, liquid level valve B124, outlet valve 121, blowoff valve 125 are standard component.
Collecting opportunity of nanometer powder: discharging feed bin 25 regularly samples, while finding that in discharging feed bin 25, liquid exceeds standard containing nanometer powder amount, should reclaim the nanometer powder of sedimentation at once.Charging feed bin 21 regularly samples, and calculates in feed liquid and contains nanometer powder amount, calculates the time of the nanometer powder that need to reclaim sedimentation slag.Irregularly reclaim at random the nanometer powder of sedimentation, more keep the circulation of sedimentation.
The collection methods of nanometer powder: open delivery pump A, the nanometer powder of nanometer powder collecting pipe 261 peripheries and nanometer powder collecting pipe 261 inside and liquid material are just inhaled into delivery pump A and deliver to accumulator tank (not shown).Nanometer powder collecting pipe 261 above nanometer powder is sucked away, and nanometer powder collecting pipe 261 nanometer powder below is partly or entirely sucked away, and inhales the nanometer powder of not walking and just sinks to there, opens cleaning eye 264 cleanings next time.
The regular operation of cleaning eye 264 is used: the nanometer powder content that reclaims when nanometer powder collecting pipe 261 is high or when too low, at once nanometer powder collecting pipe 261 is cleared up.Open the nanometer powder collecting pipe cleaning eye 264 under lower little swash plate 62, can check that nanometer powder collecting pipe 261 roundlet through hole B265 above has or not to be plugged.Open the cleaning eye 264 under lower large swash plate 61, can check that lower large swash plate 61 has or not distortion or seepage, cleaning immediately, ensures that discharging feed bin overflowing liquid meets discharge standard.
Sedimentation hopper 1 continuous feed in use, continuous discharge, does not need groove clearly.
Above-described embodiment, the present invention specific embodiment a kind of more preferably just, the common variation that those skilled in the art carries out within the scope of technical solution of the present invention and replacing all should be included in protection scope of the present invention.
Claims (10)
1. a nano powder slurry settling tank, comprise hopper, feed bin and inclined board, described hopper comprises a left side, right, before, back side panel and base plate, described right plate is provided with outlet valve, it is characterized in that: described feed bin comprises charging feed bin, sedimentation feed bin, baffling feed bin, overflow feed bin, discharging feed bin and nanometer powder are collected feed bin, described inclined board comprises short swash plate on sedimentation feed bin, short swash plate on baffling feed bin, long swash plate on long swash plate and baffling feed bin on sedimentation feed bin, also comprise charging feed bin breviseptum, charging feed bin overflow plate, overflow feed bin overflow plate, lower large swash plate, lower little swash plate, bearing rib and slurry passage A, B, C, D, E,
In feed bin between described left and right side plate, long swash plate, overflow feed bin overflow plate setting in turn from left to right on short swash plate, baffling feed bin on long swash plate, baffling feed bin on short swash plate, sedimentation feed bin on charging feed bin overflow plate, sedimentation feed bin, and the both sides of above-mentioned plate are fixedly connected with the forward and backward side plate of hopper;
Described charging feed bin breviseptum in charging feed bin, top, arrange vertical with left plate, described charging feed bin overflow plate and overflow feed bin overflow plate and baseplate vertical direction setting, the oblique setting of long swash plate right-to-left on short swash plate and baffling feed bin on long swash plate, baffling feed bin on short swash plate, sedimentation feed bin on sedimentation feed bin; Described bearing rib, on hopper base plate, along the parallel direction of front and back side plate, arranges with hopper base plate is vertical; Described lower large swash plate is in hopper bottom oblique setting from back to front, the rear side of lower large swash plate is fixedly connected with back side panel, the lower front side of large swash plate and the upper end of bearing rib are fixedly connected with, and the both sides of lower large swash plate are tight fit with charging feed bin overflow plate and overflow feed bin overflow plate respectively; Described lower little swash plate is in hopper bottom oblique setting from front to back, and the front side of lower little swash plate is fixedly connected with front side board, and the both sides of lower little swash plate are fixedly connected with overflow feed bin overflow plate with charging feed bin overflow plate respectively;
Described charging feed bin is between left plate and charging feed bin overflow plate, described sedimentation feed bin is on charging feed bin overflow plate and sedimentation feed bin between long swash plate, described baffling feed bin is on sedimentation feed bin on long swash plate and baffling feed bin between long swash plate, described overflow feed bin is on baffling feed bin between long swash plate and overflow feed bin overflow plate, described discharging feed bin is between overflow feed bin overflow plate and right plate, and described nanometer powder is collected feed bin in lower little swash plate bottom;
Described slurry passage A is arranged on charging feed bin overflow plate top, the lower position in charging feed bin overflow plate upper end, and charging feed bin and sedimentation feed bin interlink by slurry passage A; Described slurry channel B is arranged on long swash plate top on sedimentation feed bin, the lower position of long swash plate upper end on sedimentation feed bin, and sedimentation feed bin and baffling feed bin interlink by slurry channel B; Described slurry channel C is arranged on overflow feed bin overflow plate upper end, and overflow feed bin and discharging feed bin interlink by slurry channel C; Described slurry passage D is arranged between lower large swash plate bottom and lower little swash plate lower end, and the bottom of sedimentation feed bin, baffling feed bin and overflow feed bin and nanometer powder are collected between feed bin, and by slurry passage, D interlinks; Described slurry passage E is arranged on lower large swash plate bottom, and overflow feed bin overflow plate bottom is provided with through hole, and slurry passage E and discharging feed bin interlink by through hole;
Described outlet valve has 2, is separately positioned on both sides, right plate bottom.
2. a kind of nano powder slurry settling tank according to claim 1, is characterized in that: described slurry passage A is more than 2 oblong channel symmetrical on charging feed bin overflow plate top; Described slurry channel B is more than 2 small circular passage that long swash plate top is arranged side by side on sedimentation feed bin; Described slurry channel C is more than 2 the odontoid passage of serrate slot arranging in overflow feed bin overflow plate upper end; Described slurry passage D is that following large swash plate lower end and lower little swash plate lower end are the long and narrow gap on 2 long limits, and the width in gap is 40-60MM.
3. a kind of nano powder slurry settling tank according to claim 2, is characterized in that: described slurry passage A has 2 oblong channel; Described slurry channel B has 17 small circular passages; Described slurry channel C has 8 serrate slots; The width in the gap of described slurry passage D is 50MM.
4. according to a kind of nano powder slurry settling tank described in claim 1,2 or 3, it is characterized in that: described slurry passage D comprises slurry passage D front portion, D middle part and D rear portion, sedimentation feed bin is collected between feed bin and is communicated with by slurry passage D is anterior with nanometer powder, baffling feed bin is collected between feed bin and is communicated with by slurry passage D middle part with nanometer powder, and overflow feed bin is collected between feed bin and is communicated with by slurry passage D rear portion with nanometer powder; Between baffling feed bin and overflow feed bin, by slurry passage D middle part, nanometer powder, collect feed bin and slurry passage D rear portion is connected.
5. a kind of nano powder slurry settling tank according to claim 1, is characterized in that: on described sedimentation feed bin on short swash plate, sedimentation feed bin on long swash plate, baffling feed bin on short swash plate and baffling feed bin the angle of long swash plate and vertical direction be α 15-20 °; The angle of lower large swash plate and vertical direction is β 75-85 °; The angle of lower little swash plate and vertical direction is γ 40-50 °.
6. a kind of nano powder slurry settling tank according to claim 5, is characterized in that: on described sedimentation feed bin on short swash plate, sedimentation feed bin on long swash plate, baffling feed bin on short swash plate and baffling feed bin the gradient of long swash plate and vertical direction be 16 ° of α; The angle of lower large swash plate and vertical direction is that 81 ° of β are 44 ° of γ with the angle of lower little swash plate and vertical direction.
7. a kind of nano powder slurry settling tank according to claim 1, is characterized in that: on described sedimentation feed bin, on short swash plate and baffling feed bin, the degree of depth of short swash plate is the 3/10-1/2 of the hopper degree of depth.
8. a kind of nano powder slurry settling tank according to claim 1, is characterized in that: on described sedimentation feed bin, on short swash plate and baffling feed bin, the degree of depth of short swash plate is 2/5 of the hopper degree of depth.
9. a kind of nano powder slurry settling tank according to claim 1, is characterized in that: described nanometer powder is collected in feed bin and is also provided with nanometer powder collecting pipe, reducing connector, gripper shoe and cleaning eye; Described nanometer powder collecting pipe is elongated shape pipe, is arranged on nanometer powder and collects feed bin middle part, parallels with hopper bottom; Nanometer powder collecting pipe bottom interval is provided with more than 2 groups small circular through holes, and every group has 1 above small circular through hole; Described reducing connector is arranged on the nanometer powder collecting pipe left side port of export, and reducing connector outside is connected with delivery pump A again; Described gripper shoe is arranged between hopper bottom and nanometer powder collecting pipe, and gripper shoe and hopper bottom vertical arrange, and its lower end is fixedly connected with hopper bottom, and its upper end is fixedly connected with nanometer powder collecting pipe bottom; Described cleaning eye has 2, is separately positioned on lower little swash plate and the lower large swash plate below of hopper two side bottoms; Described right plate top is provided with overflow valve, liquid level valve A, and right plate bottom arranges also has liquid level valve B, blowoff valve, and described blowoff valve is at right plate foot, and described outlet valve is connected with the delivery pump B of outside again.
10. a kind of nano powder slurry settling tank according to claim 9, is characterized in that: nanometer powder collecting pipe bottom interval is provided with 12 groups of small circular through holes, and every group has 3 small circular through holes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110383495.7A CN102512853B (en) | 2011-11-28 | 2011-11-28 | Nano powder slurry settling tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110383495.7A CN102512853B (en) | 2011-11-28 | 2011-11-28 | Nano powder slurry settling tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102512853A CN102512853A (en) | 2012-06-27 |
| CN102512853B true CN102512853B (en) | 2014-04-09 |
Family
ID=46284076
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110383495.7A Expired - Fee Related CN102512853B (en) | 2011-11-28 | 2011-11-28 | Nano powder slurry settling tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102512853B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111097205A (en) * | 2019-12-20 | 2020-05-05 | 仇爽 | Movable system sand system |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103432776A (en) * | 2013-08-30 | 2013-12-11 | 南京协和助剂有限公司 | Gradient adjustable liquid settling tank for PVC (Poly Vinyl Chloride) processing |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2198960Y (en) * | 1994-06-14 | 1995-05-31 | 化学工业部上海化工研究院 | S-shaped groove continous filtering concentrator |
| CN201128742Y (en) * | 2007-01-31 | 2008-10-08 | 黄桂忠 | Static fast settling vessel |
| CN201470169U (en) * | 2009-09-08 | 2010-05-19 | 沈阳铝镁设计研究院 | Discharging structure of settling tank |
| CN202355873U (en) * | 2011-11-28 | 2012-08-01 | 新时代集团浙江新能源材料有限公司 | Nano powder slurry setting tank |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20110019687A (en) * | 2009-08-20 | 2011-02-28 | (주)휠탑 | Exhausted apparatus of precipitated sludge |
-
2011
- 2011-11-28 CN CN201110383495.7A patent/CN102512853B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2198960Y (en) * | 1994-06-14 | 1995-05-31 | 化学工业部上海化工研究院 | S-shaped groove continous filtering concentrator |
| CN201128742Y (en) * | 2007-01-31 | 2008-10-08 | 黄桂忠 | Static fast settling vessel |
| CN201470169U (en) * | 2009-09-08 | 2010-05-19 | 沈阳铝镁设计研究院 | Discharging structure of settling tank |
| CN202355873U (en) * | 2011-11-28 | 2012-08-01 | 新时代集团浙江新能源材料有限公司 | Nano powder slurry setting tank |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111097205A (en) * | 2019-12-20 | 2020-05-05 | 仇爽 | Movable system sand system |
| CN111097205B (en) * | 2019-12-20 | 2021-06-15 | 仇爽 | Movable system sand system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102512853A (en) | 2012-06-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110025988B (en) | Coal slime water concentration treatment system of three-section underflow discharge | |
| US20210008467A1 (en) | Reverse flow type multi-stage sedimentation rake-free thickening device | |
| CN102512853B (en) | Nano powder slurry settling tank | |
| CN202238273U (en) | Silt separation bucket | |
| CN104478114A (en) | Rotational flow air flotation separation device of tar ammonia water | |
| CN202355873U (en) | Nano powder slurry setting tank | |
| CN109731670B (en) | Pulse type heavy medium shallow slot sorting device and method | |
| CN110025989B (en) | Rake-free thickener with three-section discharge outlets | |
| CN206045484U (en) | Liquid separating appts with ball float level meters | |
| CN202315444U (en) | Multilayer precipitator | |
| CN103657162A (en) | Efficient and energy-saving solid-liquid separator | |
| CN102698880B (en) | Foam controlling and removing method for floatation | |
| CN203648145U (en) | Efficient energy-saving solid-liquid separating machine | |
| CN206881214U (en) | A kind of low-grade salt lake lithium carbonate extraction settling tank | |
| CN205949042U (en) | Shaking table is with dividing ore deposit ware | |
| CN206262174U (en) | A kind of atlapulgite slurry multifeed clarifier | |
| CN104436854A (en) | Slime water serial treatment system and slime water serial treatment process | |
| CN204841052U (en) | High -efficient hierarchical concentrated machine of tailing pulp material | |
| CN203877934U (en) | Flat stereoscopic composite trash rack/press dehydration integrated device | |
| CN104998441B (en) | Mine tailing slurry efficient graded concentrating machine | |
| CN203634958U (en) | Flotation tailing processing equipment group of copper smelting slag | |
| CN211070067U (en) | Calcium chloride solid powder production facility | |
| CN210787725U (en) | Coarse slime sorting equipment | |
| CN102776062A (en) | Treatment method of silicon wafer cutting liquid waste | |
| CN204644200U (en) | A kind of potash humate production equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140409 Termination date: 20171128 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |