CN2040398U - Rotary internal-filtering radiation type continuous filter - Google Patents

Rotary internal-filtering radiation type continuous filter Download PDF

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Publication number
CN2040398U
CN2040398U CN 88207094 CN88207094U CN2040398U CN 2040398 U CN2040398 U CN 2040398U CN 88207094 CN88207094 CN 88207094 CN 88207094 U CN88207094 U CN 88207094U CN 2040398 U CN2040398 U CN 2040398U
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filter
rotary drum
drum
filtering
saddle
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程慧雄
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Abstract

The utility model discloses a rotary drum internal-filtering radiation type vacuum continuous filter which is provided with a saddle filtering plate at the inner part, and the limited space filtering area and productive capacity are increased ten times. The height of a filtering slurry is capable of being adjusted to generate position difference and driving force of slurry filtering, and filter cake is formed to be washed. After the filter cake is self-discharging, a filter cloth is capable of being washed by clean water. Vacuum pumping proceeds among walls of filtering plates in slurry, so power consumption is reduced, and intensity of pumping is enhanced. The utility model is capable of separating suspension liquid and adhesive slurry, and especially to the suspension liquid which has higher require of filtering temperature is capable of being separated by the utility model. A heating apparatus and a heat preserving apparatus are arranged in the filter, and filtering and dewatering separation of solid phase and liquid phase are capable of proceeding at 98 DEG C.

Description

Rotary internal-filtering radiation type continuous filter
The utility model relates to separator, particularly the filtration machinery of the hydraulic vacuum of liquid/solid suspension or some high-viscosity material suction.
Filtering machinery tool in industrial department such as chemical industry, metallurgy, ore dressing, oil, food, sugaring, system wine, papermaking, chemical fibre and three industrial wastes are handled plays a very important role.
In the prior art, to separating of suspension and high-viscosity material, often need select the filter that adapts for use, for example the medium dehydration to high-viscosity material separates, need to use pressure filtration equipment: plate and frame filter, pressure leaf filter, pressurization vacuum disk filter, pressurization vacuum-type drum filter and domestic Cheng are faithful and upright, and the Chinese patent that proposes is announced No. 87102662, inscribes one's name to be " mechanical extruding type continuous filter press ".Then will adopt horizontal vacuum belt filter, disk vacuum filter and rotary drum vacuum filter to general suspension medium slurry dewatering separation.
Generally speaking these filters are mainly by frame or housing, rotary drum, filter, seal, compositions such as central dispense head and transmission device.Filter is covered with flat board or arc form cylinder inboard wall or the outside periphery around rotary drum usually, so after in case the size of rotary drum is determined, the filter area coverage, promptly filter area is also determined basically.Therefore, if increase filter area, just need the size of corresponding expansion rotary drum, improve auxiliary equipment power such as transmission and vaccum pump motor, make filter do very hugely, cause investment big, use the material expense, floor space is many.For instance, the just basic filter area of making, both at home and abroad all below 30M, " except that the special user needs " domestic production GN-20 cartridge type inner leaching vacuum filtering machine, roller diameter 4M, appearance and size 4M * 4M * 4M, and filter area has only 20M, vaccum pump motor that vacuum draw uses is 75 kilowatts.The LKGA-10 rotary drum vacuum filter, rotary drum interior diameter 2.6M, appearance and size 4.7M * 4M * 3.56M, and filter area has only 10M, and vaccum pump motor that vacuum draw uses is 30 kilowatts, sale price is 120,000 yuan.Another kind of GGX-27 filter, filter area is 27M, appearance and size 6.8M * 5.24M * 3.2M, sale price is 300,000 yuan.It is 60M that a kind of filter area is arranged again, appearance and size 20M * 5.5M * 3.3M, sale price is about 600,000 yuan, huge monster is installed etc. also for transportation and is all brought and is difficult to imagination difficulty like this, if increase the unit filter area again, under current conditions, carry out with regard to more being difficult to.And the appearance and size 4M of the utility model filter * 5.4M * 5.4M filter area just has between 150~200M.
Existing another ubiquity problem of filter, be to filter slip to pour in the rotary drum or rotor cover, all at the rotary drum center line with the bottom, immerse slip liquid inner filtration plate and only account for total filter about 1/4, so just be difficult for forming slurries pressure, on the contrary in vacuum draw, because easily be full of cracks of filter cake suction, a large amount of vacuum leaks had so both influenced vacuum draw intensity, had wasted power consumption simultaneously again in vain.
In addition, above-mentioned filter is because volume is big, so the used material of filter is generally all selected cast iron lining rubber for use, owing to be difficult to anticorrosion, not anti-higher temperature relation has limited filter for the popularity of handling slip.In addition, general vacuum filter, unloading filter cake is to add blowback air by scraper, makes that filter cloth surface pore is sticking smears obstruction, filter cloth uses filter effect relatively poor continuously, uses longly more, glues and smears obstruction, and is more obvious.
The purpose of this utility model is to overcome the shortcoming that exists in the above-mentioned filter, thereby provide the radial pattern filter plate is installed on a kind of drum inner wall, goes back the hydraulic vacuum continuous filter that suit one increases the hydraulic pressure drum in it.This filter is strong to filtering slip adaptability, and volume has only 1/8 of the former polytype vacuum continuous filter, when equal volume, " being roller diameter and length product " down filter area and production capacity be the former 10 times, power consumption has only 20% of the former filter, saves electric power greatly.And vacuum draw is carried out between the wooden partition of filter in slurries basically, the suction intensity large increase of getting back.And cost is only calculated the former 1/4~1/2 with every square of filter area.The trial production filter area is 60M at present, appearance and size 3M * 3M * 3M, and the scientific and technical research budget sale price is within 250,000 yuan.
Another purpose of the utility model is that filter material that all contact filtration media use is whole stainless steels and polytetrafluoroethylene (PTFE) etc.
The another purpose of the utility model is in the filter heater to be installed, and makes like this and can quicken separating and dehydrating to suspension, can separate having the high viscosity slip again.So this practical invention filter has compact conformation, rationally, floor space is little, and is in light weight, and cost is low, and is power-saving, and performance is good, also can adapt to separating of the floating suspension of various industry and some high-viscous media.
Filter of the present utility model has 6 above filters mainly by pair of frame in the rotary drum of one cylinder, one increases hydraulic pressure drum assembly, a dispensing head, compositions such as a pair of wheel holding mechanism, a pair of travelling gear and motor deceleration device.Rotary drum comprises the fixedly rotary drum stack shell of gear wheel of an outer end band convex shoulder and the other end, and one is positioned at the mainshaft gland in rotary drum stack shell left side, and one is positioned at the right aling cap on right side.Filter is actinomorphic shape of a saddle, and it axially is installed in and makes limited roller diameter space inner filtration area increase about 10 times on the inwall of rotary drum stack shell.Pair of frame comprises the rotary drum bearing bracket stand and regulates fixed support.Two wheel holding mechanisms are placed on rotary drum ground, below or the frame.The mainshaft gland of said rotary drum rolls with two wheel holding mechanisms with the rotary drum bearing block separately with rotary drum stack shell convex shoulder and is connected.A rotary drum gear wheel of one end fixed in position " geared sleeve ", said gear be contained in reduction gearbox output shaft upper transfer gear engaged transmission so that rotary drum rotates.
One increases hydraulic pressure drum assembly is installed in the inner chamber of rotary drum, this assembly comprises an outer lattice inner bag that is subjected to hydraulic pressure, the spacious seam of certain distance is arranged at its top, one is positioned at the center stiffening ring of nozzle one side, what one cross section was shallow U-shaped unloads the filter cake bucket, this pan tilts to be placed in the spacious seam, make under blowback air blowback effect, to unload naturally to fall and unload in the filter cake bucket at the filter cake that forms on the shape of a saddle filter, this bucket inclined plane of process glides outside the discharge machine automatically, regulating fixed support for one is located on the wall limit of lattice inner bag and center stiffening ring, other one of the lattice inner bag is installed in the mainshaft gland and is connected with the mainshaft gland sealed rolling, make and increase the hydraulic pressure drum and remain inactive state, one is located at the liquid baffle board that spacious seam two sides and two short slabs are located at two ends and are inclined upwardly or are connected with each other and constitute perpendicular to ground level by two block length plates, washing filter cloth aggregation slot also is housed in the liquid barrier outside, it makes the filter filter cloth obtain the clear water washing, enter filtration zone after the regeneration again, this makes when filtering the slurry dewatering separation, the filter cloth pore is difficult for stopping up, accelerate filtering rate, between lattice inner bag and center stiffening ring, pulp-inlet pipe is housed, slip can from outside be input in the rotary drum by pulp-inlet pipe.The dispensing head of filter is installed on the axial end of mainshaft gland, and the right aling cap of said rotary drum is that dynamic seal (packing) is connected with the center stiffening ring that increases the hydraulic pressure drum.
On the every shape of a saddle filter, be provided with drain pipe and air inlet pipe and unload the filter cake air slot.Drain pipe and air inlet pipe are also inserted on the rotary drum mainshaft gland, and use fixed by nut separately, use polytetrafluoroethylene (PTFE) fluid flexible pipe and air induction hose mutually and connect.Drain pipe inner filtration clear liquid is summarized in the dispensing head housing, outside discharging tube discharge machine.Air inlet pipe on the filter, when this shape of a saddle filter on the rotary drum entered dispensing head blowback air inlet pipe hole position, blowback air entered or connects filter by air induction hose, carried out blowback to having formed filter cake on the filter, and filter cake unloads voluntarily.Filter cake unloads, because spacing between the shape of a saddle filter and filter cake are in the effect of drum inner wall absorption affinity, filter cake still has part to be bonded on filter and the drum inner wall, in order thoroughly to unload remaining filter cake, in the shape of a saddle filters in the blowback air blowback, small amount of compression gas is arranged by the dyanainic friction sheet at dispensing head, enter out the valve pore, the valve of automatic inflatable valve is opened, the a large amount of compressed gas instantaneous times of 6kg/cm spray between filter surface and drum inner wall and dash, and dash through such spray, and filter cake unloads that to fall be thoroughly fully, make in this way, rely on blowback air and scraper to unload filter cake more than the rotary-drum vacuum continuous filter and want much superior.
The utility model increases considerably except top said filter area, and is of fine quality and cost is low, and it is strong to filter slip adaptability, outside the volume small footprint size waits less, also have easy to maintenance, simple to operate and good seal performance.This filter continuously-running, stable and reliable for performance.Unload filter cake and directly unload, also make the filter cloth pore unimpeded, so suitable long-term continuous use of filter cloth can be improved the filter effect of filter again by the blowback air effect.The utility model sealing property is reliable, the dehydration of volatile, noxious material or radioactive substance is separated can adopt closed structure, has created condition to realizing far distance controlled and automation control, can save the labour and can reduce labor intensity again.It is several hundred million to tens billion of direct wealth that this invention creates for Chinese society doctrine economic construction meeting, give national ten hundreds of industrial enterprise solved the insoluble three wastes handle in the Separation of Solid and Liquid problem, also can impel in the industrial production and the disposal of three wastes Separation of Solid and Liquid to obtain essence and solve.
Below with reference to accompanying drawing the utility model filter is described in detail:
Fig. 1 is a filtering machine structure schematic diagram of the present utility model;
Fig. 2 is a filter fundamental diagram of the present utility model;
Fig. 3 is the dispensing head cutaway view;
Fig. 4 is the view cross-sectional view of Fig. 5
Fig. 5 is a dispensing head dyanainic friction sheet schematic diagram;
Fig. 6 is a dispensing head static friction sheet schematic diagram;
Fig. 7 is the cutaway view of rotary drum;
Fig. 8 is the schematic diagram of shape of a saddle filter;
Fig. 9 is the view cross sections figure of Fig. 8;
Figure 10 is the cutaway view that increases hydraulic pressure drum, and wherein office cuts open part and represents the water back position,
Figure 11 is the view side view of Figure 10;
Among the figure 1, travelling gear, 2, gear, 3, bearing block 4, sealing ring, 5, centre bearing, 6, dispensing head, 7, the automatic inflatable valve, 8, base bearing, 9, the fluid flexible pipe, 10, air induction hose, 11, rotary drum, 12, the rotary drum stiffening ring, 13, shape of a saddle filter, 14, seal ring pressing plate, 15, sealing ring, 16, increase the hydraulic pressure drum, 17, regulate fixed support, 18, the rotary drum rolling supporting wheel, 19, discharging tube, 20, central shaft, 21, bearing, 22, the static friction sheet, 23, movable friction plate, 24, open the valve air admission hole, 25, lifting bolt, 26, vacuum meter, 27, the blowback air inlet pipe, 28, capping, 29, nut, 30, the compression spring, 31, spring base, 32, housing, 33, the vacuum drawing liquid portals, 34, enter the filter plate blowback air, 35, enter out the valve pore, 36, enter automatic inflatable valve pore, 37, the blowback air admission hole, 38, the import of nature gas, 39, air guide is poor, 40, the filtrate aggregation slot, 41, right aling cap, 42,5 rotary drum stack shells, 43, filter mesh division board, 44, mainshaft gland 45, filter cloth, 46, filter screen, 47, drain pipe, 48, the net supporting plate, 49, it is poor to unload filter cake gas, 50, air inlet pipe, 51, the center stiffening ring, 52, regulate slurries height discharge pipe, 53, unload the filter cake bucket, 54, the inner bag principal rod, 55, pulp-inlet pipe, 56, the lattice inner bag, 57, liquid barrier, 58, the centralized positioning axle, 59, washing filter cake shower, 60, overflow pipe, 61, the outlet of chuck steam heated, 62, lattice rubber, 63, washing filter cloth shower, 64, the washing filter cloth gathers poor, 65, the washings outlet, 66, the import of chuck steam heated, 67, direct heating steam pipe.
Referring to Fig. 1,2 and 7 radiation-type vacuum continuous filter using internal filtering in rotating drum of the present utility model comprise a pair of gear 1,2, dispensing head 6, rotary drum 11, radial pattern shape of a saddle filter 13, increase hydraulic pressure drum assembly 16, bearing block 3, adjusting fixed support 17 and a pair of support roller 18 etc.
Rotary drum 11 is by rotary drum stack shell 42, mainshaft gland 44, right aling cap 41 compositions such as grade.One end outer edge of said stack shell 42 has ring-type convex shoulder rotary drum stiffening ring 12, the fluid hole and the air inlet through hole that are provided with circumference uniform distribution and equate with emanant shape of a saddle filter quantity on the round plate near the mainshaft gland 44 at stack shell 42 inwall places.These two kinds of through holes of respective numbers circumference uniform distribution also are set at the necked part of mainshaft gland 44.Go out between the fluid through-hole and the air inlet through hole between respectively by fluid flexible pipe 9 and air induction hose 10, use fixed by nut each other, use teflon hose mutually and be communicated with.The inboard of mainshaft gland 44 has centre bore increases hydraulic pressure drum 16 with installation centralized positioning axle 58.
Said radial pattern shape of a saddle filter is axially uniform along the inwall of rotary drum stack shell 42, sees Fig. 8,9.Usually can establish 20-120 according to the structural requirement filter, the many more filter areas of quantity are big more.The cross sectional shape of radial pattern filter can be the shape of a saddle, trapezoidal, trapezoidal, rectangle U-shaped, V-arrangement etc., and is best with the shape of a saddle wherein.
The illustrated shape of a saddle filter 13 that all adopts in the utility model, shape of a saddle filter 13 structures comprise that a seal base, a cross section are semicircle saddle-shaped surface top, and this curved surface is wideer than the end of curved surface near the width of seal base portion.The curved surface of shape of a saddle filter 13 sets up or covers stainless (steel) wire supporting plate 48 from inside to outside, unloads filter cake air drain 49 on the net supporting plate, stainless steel prismatic filter screen 46 and filter cloth 45, and end cover is respectively established in the curved surface both sides, is provided with air inlet pipe 50 and drain pipe 47 on one of end cap.Described filter is installed in the inner edge wall of rotary drum stack shell 42 by seal base with screw, and air inlet pipe 50 and drain pipe 47 are connected with the fluid flexible pipe with air induction hose separately by two through holes on the rotary drum.Above-mentioned filter screen 46 and net holder 48 structures can make the filter cloth cladding filter cloth pore unimpeded on the net built on stilts.So under hydraulic pressure and two kinds of filtered driving force effects of vacuum draw, not only make slurry filtration speed fast, effective but also rate of cake moisture content that filter cloth surface is formed is lower than the filter cake of other vacuum continuous filter formation.
Increase hydraulic pressure drum 16, by center stiffening ring 51, regulate slurries height discharge pipe 52, unload filter cake bucket 53, inner bag principal rod 54, pulp-inlet pipe 55, lattice inner bag 56, liquid barrier 57, centralized positioning axle 58, washing filter cake shower 59, jacket steam heating tube and compositions such as direct heating steam pipe 67 and washing filter cloth aggregation slot.Inner bag principal rod 54 is used bolting with adjusting fixed support 17.Other end centralized positioning axle 58 is equipped with centre bearing 5, inserts in mainshaft gland 44 centre bores closely to be connected, and constitutes so-called sealed rolling and connects.And increase hydraulic pressure drum 16, be relative transfixion.The said filter cake bucket 53 that unloads is to take back increasing hydraulic pressure drum 16 centers, the diagonal angle, top passes described spacious seam obliquely and is extended to outside the center stiffening ring 51, the width and the slope that unload filter cake bucket 53 are enough to satisfy the filter of rotary drum when blowback district III, see Fig. 2, filter residue that blows off or filter cake slide into outside the machine for 53 times along unloading the filter cake bucket, liquid barrier 57 is provided with around the spacious seam of lattice inner bag 56, and its top is higher than lattice inner bag 56.Washing filter cloth aggregation slot 64 is just near unloading filter cake bucket 53, and the right side is unloaded filter cake bucket 53 and separate by lattice rubber 62 in the middle of gathering poor 64 with the washing filter cloth above lattice inner bag 56, washes filter cloth and gathers and be pickled with grains or in wine in 64 by the filter cloth shower 63 of washing and washings outlet 65 are arranged.Washing filter cake shower 59 is equipped with in the left side of lattice inner bag 56, regulates slurries height discharge pipe 52, can regulate the slip elevation of water of 56 of rotary drum 11 and lattice inner bags, this can make slip in rotary drum the natural pressure reduction of the hydraulic pressure that produces, together with vacuum draw.Make to produce two kinds of motive forces in the filter process, potential difference is big more, hydraulic coupling is big more.Because various slip character are different with the filtering content requirement, regulate height and will see the slip object.Will wash as filter cake, slip advances the slurry height will be lower than washing filter cake shower 59.It is lower to produce nature hydraulic pressure like this, does not need washing as filter cake, and slip can account for about 80% at the rotary drum inner height so, and the solid-liquid dehydration that certainly will help slip separates.Increase being tightly connected of right aling cap 41 of the center stiffening ring 51 of hydraulic pressure drum 16 and rotary drum 11, comprise and be placed on center stiffening ring 51, O-ring seal 4 between the concave ring part of external peripheral surface and right aling cap 41 and being fixed on the right aling cap 41, and the seal ring pressing plate 14 of compression seal circle 4, this being sealed into makes slip reach the liquid level certain altitude in rotary drum 11, do not leak out and can and not increase between the hydraulic pressure drum from rotary drum.
The liner of the rotary drum stack shell 42 of filter can be with stainless steel or rubber in the utility model, plastics, as polytetrafluoroethylene (PTFE) and coating epoxy, increase hydraulic pressure drum 16 usefulness stainless steels or resistant material manufacturing like that and make filter have better corrosion-resistant and heat resistance, applicable to various Acidity of Aikalinity slips.One jacket steam heater and direct heating steam pipe 67 also are housed on the outer wall of the lattice inner bag 56 that increases hydraulic pressure drum 16, and the latter can install according to the character and the permission of slip, and they are made by the stainless steel disc pipe.The import and export 66,61 of jacket steam heater and the import of direct heating steam pipe 67 all are positioned at the nozzle that increases hydraulic pressure drum 16, and the slip that solid-liquid phase filtering means dehydration is separated is heated to 98 ℃.This will help the dehydration of some resisting medium is separated accelerated filtration speed greatly.On the contrary, this is difficult to adopt on other kind vacuum filter, even will adopt also because of the filter volume is big, structure benzene is heavy, and most of heat is consumed by the heat absorption of the huge space of equipment and parts itself, really pass to the heat that filters on the slip just seldom.
In order to make rotary drum 11 stability of rotation, flexible, said wheel holding mechanism comprise two support roller assemblies that are separately fixed on the framework platform and are positioned at rotary drum 11 vertical planes that axial line is done two sides, install symmetrically, each assembly comprises two bearing bracket, two bearings, one and one rotary drum rolling supporting wheel 18 that is fixed on a last band connected in star, and the rolling of the convex shoulder on said wheel holding mechanism and the rotary drum is connected the apparent surface who comprises interactional convex shoulder and support roller 12.
Be installed in the central dispense 6 of the mainshaft gland axle head of rotary drum, see Fig. 3, be used for the filter gas-liquid that automaticallyes switch, the structure of this dispensing head 6 is seen Fig. 3, on parts are settled, dyanainic friction sheet 28 is arranged in housing 32, this part hexagon socket head cap screw is fixed on mainshaft gland 44 end faces, there is the vacuum drawing liquid to portal 33 on the dyanainic friction sheet 28, enters (stretching into) filter plate blowback air 34, enter (stretching into) and open 35, three different-diameter circumference uniform distributions of valve pore duct.Wherein enter filter plate blowback air 34 main conductance roads and enter (stretching into) shape of a saddle filter 13, partly gas is opened valve pore 35 by interior air flue backspace through entering (stretching into), opens automatic inflatable valve 7 and is shown in an open position 6kg/cm compression gas blowout and breaks through residual filter cake between filter plate and rotary drum barrel.With movable friction plate is corresponding static friction sheet 22 arranged, this sheet is fixed on the housing 32 interior disks by hexagon socket head cap screw, filtrate aggregation slot 40 is arranged on the static friction sheet 22, air slot 39, nature gas import 38, nature gas input can have been regulated natural gas, and filter pressure reduction in vacuum draw is increased, and makes cleaner liquid accelerate suction by outside the discharging tube 19 discharge machines.And when blowback unloaded filter cake, fluid flexible pipe 9 remaining raffinates seldom ran off.This design is present various continuous filter initiative.This sheet also has a difference position blowback pore 37 and enters automatic inflatable valve 36, and these two holes are synchronously formation filter cake on the filter plate to be unloaded inside and outside carrying out.Blowback air inlet pipe 27 is installed in the top of housing 22 center lines, make filter more reasonable when switching gas-liquid, all the other are equipped with central shaft 20 in the housing, plain thrust bearing 21, nut 29, compression spring 30, spring base 31, and housing capping 28, lifting bolt 25, vacuum meter 26.
Operation principle of the present utility model is that slip is by pump or liquid level nature pressure reduction, through pulp-inlet pipe, be that the feed slurry height is higher than in the rotary drum inner chamber and regulates slurries height discharge pipe 52, the inner chamber liquid level can be regulated according to slip character, the rotary drum running is under the driving of transmission, rotate along clockwise direction, see Fig. 2.The position I is a filtration zone among Fig. 2, accounts for 50-60%, and slip dewaters under hydraulic pressure own and vacuum draw effect and separates.The position II is clear water washing leaching cake zone among Fig. 2, account for 20%, do not need the clear water washing as filter cake, I, II two positions are filtration zone entirely so, enter slip liquid level in the rotary drum like this, can transfer to above more than the rotary drum center line, the slurry filtration clear liquid is by filter cloth pore on the shape of a saddle filter, the prismatic stainless steel filtering net and the net supporting plate of built on stilts filter cloth are extracted into drain pipe, gather dispensing head, under the vavuum pump suction, with filtered fluid outside discharging tube discharge machine.It is to filter under the promotion at two kinds that the filter cloth surface forms filter cake, promptly under potential difference hydraulic pressure and the vacuum draw effect, along with the rotation of rotary drum clockwise direction, progressive additive.After shape of a saddle filter left the liquid horizontal line, the part moisture content on filter cake surface on the filter continued to be fallen by vacuum draw.This machine filter process in slurries, carries out between the wooden partition of filter basically, and the vacuum force loss is minimum, and vacuum draw intensity is improved, and under higher atmospheric pressure differential, is sucked liquid part " moisture content ", thereby forms the lower filter cake of moisture percentage.Enter III thereupon, unloading the filter cake zone accounts for about 6%, at this regional filter cake is in filter, unload under the outer blowback air effect, fall in unloading the filter cake bucket outside the discharge machine, meanwhile, the pore of filter cloth keeps unimpeded under the blowback air effect, unload filter cake after, enter washing filter cloth zone V, account for about 4%, filter cloth is through the clear water regenerated from washing, and the clear water of clear water washing filter cloth can be controlled in the limited range this to long-term circulating filtration, its filter cloth filtering rate can remain unchanged lastingly, makes its filter cloth aging unless filter slip medium factor.Filter cloth enters in the diagrammatic sketch 2 after washing, the position of IV, and promptly the intermediate filtered zone accounts for about 10%, is no work done position, and this no work done loss is littler than any inside and outside formula rotary drum vacuum filter loss.Enter diagram I position afterwards again, shape of a saddle filter is like this periodically from charging, filtration, washing leaching cake in the rotary drum, and row unloads filter cake, clear water washing filter cloth moves continuously.

Claims (12)

1, a kind of radiation-type vacuum continuous filter using internal filtering in rotating drum, comprise frame or housing, rotary drum, filter, central dispense head and transmission device, it is characterized in that: said rotary drum comprises the rotary drum stack shell of an outer end band shape convex shoulder, one is positioned at the mainshaft gland in rotary drum stack shell left side, one is positioned at the right aling cap on right side, the rotary drum stack shell in addition end be installed with a gear and be contained in the engagement of reduction box power shaft upper transfer gear, filter is that radial pattern is saddle-shaped, have more than 6, each filter one side has a drain pipe and air inlet pipe and axially is installed on the inwall of rotary drum stack shell, frame is rotary drum bearing mounting and regulates two wheel holding mechanisms of fixed support and be installed under the rotary drum on the methods, rack, the mainshaft gland of described rotary drum rolls with two wheel holding mechanisms with the rotary drum bearing block separately with rotary drum stack shell convex shoulder and is connected, the present invention also has one to increase hydraulic pressure drum assembly and be installed in the inner chamber of rotary drum, this assembly comprises the outer hydraulic pressure lattice inner bag that is subjected to, the open of certain distance is arranged at its top, one is positioned at the center stiffening ring of nozzle one side, what one cross section was shallow " U " shape unloads the filter cake bucket, and this pan tilts to be installed in the spacious seam.One centralized positioning axle, the termination of this central shaft is installed in the mainshaft gland and with the mainshaft gland sealed rolling and is connected, the other end is fixed on to be regulated on the fixed support, increase the relative transfixion of hydraulic pressure drum, the lattice inner bag, one is connected with each other by two long slabs that are located at spacious seam two sides and two short slabs that are located at spacious seam two ends constitutes liquid barrier, and one is installed in the outside, the liquid barrier right side is equipped with the water washing filter cloth and gathers poorly, and inner bag center line left side is equipped with the spray flushing and is washed the filter cake device.Said dispensing head is installed on the axial end of mainshaft gland.The right aling cap of said rotary drum is tightly connected with the center stiffening ring that increases the hydraulic pressure drum, said filter drain pipe and air inlet pipe are inserted corresponding fluid flexible pipe and air induction hose on the rotary drum mainshaft gland separately, this fluid flexible pipe gathers the dispensing head housing, and air induction hose is then connected filter when this filter enters dispensing head blowback air admission hole position.In lattice inner bag center line left side the spray flushing is housed and washs the filter cake device.
2, filter according to claim 1, the round plate that it is characterized in that mainshaft gland be provided with circumference uniform distribution and equate with radial pattern shape of a saddle filter quantity go out fluid through-hole and air inlet through hole, necked part at mainshaft gland also is provided with these two kinds of through holes of respective numbers circumference uniform distribution, use fixed by nut respectively between two fluid holes and between the two air inlet through holes, be connected with each other logical by fluid flexible pipe and air induction hose again.
3, filter according to claim 1 and 2 is characterized in that general radial pattern shape of a saddle filter can establish 20~120, and the filter cross sectional shape can be the shape of a saddle, trapezoidal, rectangle, and trapezoidal, U-shaped, V-arrangement etc. wherein are preferably the shape of a saddle.
4, filter according to claim 3, it is characterized in that said shape of a saddle filter comprises a seal base, one cross section is the top of semicircle saddle-shaped surface, curved surface sets up from inside to outside or covers and unloads filter cake air drain, stainless steel prismatic filter screen and screen cloth on stainless (steel) wire supporting plate, the supporting plate, curved surface two sides are respectively established end cover, one of end cap is provided with air inlet pipe and drain pipe, and filter is installed on the inner edge wall of rotary drum stack shell with screw by seal base.
5, filter according to claim 4, it is characterized in that said centralized positioning axle is connected with the mainshaft gland sealed rolling, it comprises that the centre bore of the bearing placed in the shaft shoulder and annular groove on the centralized positioning axle, sealing ring and mainshaft gland is tight and contacts and be connected.
6, filter according to claim 5 is characterized in that being tightly connected of right aling cap of said center stiffening ring that increases hydraulic pressure drum and rotary drum comprises the O-ring seal between the concave ring part that is placed on center stiffening ring outer surface and right aling cap and be fixed on seal ring pressing plate on the right aling cap.
7,, it is characterized in that saidly being fixed on that the discharge pipe of outside overflow pipe and adjusting slurries height all is connected with soft rubber tube between lattice inner bag and center stiffening ring according to claim 1,2,4,5 or 6 described filters.
8, filter according to claim 7 is characterized in that on the outer outer wall that is subjected to hydraulic pressure lattice inner bag that increases hydraulic pressure drum a jacket steam heater and/or a direct heating tube being housed also, and they are made by stainless steel tube.
9, filter according to claim 8, the liner that it is characterized in that rotary drum stack shell 42 is that stainless steel is made with stainless steel or rubber, plastics and coating epoxy lining and increase the hydraulic pressure drum.
10, according to claim 1 or 9 described filters, it is characterized in that described dispensing head the automatic switchover gas-liquid the dynamic friction method with slide the static friction method mutually involutory with the dynamic friction method, having the vacuum extraction on the said rubbing manipulation portals and enters the filter plate blowback air and enter out three uniform ducts of different-diameter circumference of valve pore, the total groove of filtrate should be arranged respectively on the described static friction sheet relatively, the natural gas import that air slot, natural inflow amount can be regulated.
11, according to claim 7 or 10 described filters, when it is characterized in that the automatic inflatable valve carries out blowback and unloads filter cake in blowback air advances filter plate, part gas is opened earlier in the valve, and a large amount of blowback gas blowouts are broken through between filter plate surface and drum inner wall and pressure is about 6kg/cm.
12, according to claim 1 or 2 or 11 described filters, washing filter cake shower is equipped with in the left side that it is characterized in that the lattice inner bag, in water elder generation filter cloth aggregation slot by washing filter cloth shower is arranged.
CN 88207094 1988-06-11 1988-06-11 Rotary internal-filtering radiation type continuous filter Expired - Lifetime CN2040398U (en)

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CN 88207094 CN2040398U (en) 1988-06-11 1988-06-11 Rotary internal-filtering radiation type continuous filter

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CN 88207094 CN2040398U (en) 1988-06-11 1988-06-11 Rotary internal-filtering radiation type continuous filter

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CN2040398U true CN2040398U (en) 1989-07-05

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101987265A (en) * 2010-11-19 2011-03-23 成都天保重型装备股份有限公司 Novel liquid blocking device of rotary drum vacuum filter
CN101827767B (en) * 2007-10-12 2013-08-21 威特曼塑料仪器有限责任公司 Material separator for delivery systems
CN104307240A (en) * 2014-10-20 2015-01-28 湖南蓝天阳工程投资管理有限公司 Vacuum belt conveyor
CN106964189A (en) * 2017-05-16 2017-07-21 程慧骅 A kind of inner-drum radiation-type vacuum continuous filter

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101827767B (en) * 2007-10-12 2013-08-21 威特曼塑料仪器有限责任公司 Material separator for delivery systems
CN101987265A (en) * 2010-11-19 2011-03-23 成都天保重型装备股份有限公司 Novel liquid blocking device of rotary drum vacuum filter
CN101987265B (en) * 2010-11-19 2014-03-12 成都天保重型装备股份有限公司 Liquid blocking device of rotary drum vacuum filter
CN104307240A (en) * 2014-10-20 2015-01-28 湖南蓝天阳工程投资管理有限公司 Vacuum belt conveyor
CN104307240B (en) * 2014-10-20 2016-08-24 湖南昌迅科技环保股份有限公司 A kind of vacuum belt machine
CN106964189A (en) * 2017-05-16 2017-07-21 程慧骅 A kind of inner-drum radiation-type vacuum continuous filter

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