CN112354241A - Self-impurity-removing cylindrical filter device with backwashing net - Google Patents
Self-impurity-removing cylindrical filter device with backwashing net Download PDFInfo
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- CN112354241A CN112354241A CN202011535239.0A CN202011535239A CN112354241A CN 112354241 A CN112354241 A CN 112354241A CN 202011535239 A CN202011535239 A CN 202011535239A CN 112354241 A CN112354241 A CN 112354241A
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- 238000011001 backwashing Methods 0.000 title claims abstract description 158
- 239000012535 impurity Substances 0.000 claims abstract description 91
- 239000000463 material Substances 0.000 claims abstract description 89
- 238000007599 discharging Methods 0.000 claims abstract description 52
- 238000001914 filtration Methods 0.000 claims abstract description 43
- 238000011045 prefiltration Methods 0.000 claims description 7
- 230000000149 penetrating effect Effects 0.000 claims description 4
- 230000003068 static effect Effects 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 description 11
- 239000010813 municipal solid waste Substances 0.000 description 10
- 239000000203 mixture Substances 0.000 description 8
- 229920000433 Lyocell Polymers 0.000 description 6
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- 238000011084 recovery Methods 0.000 description 3
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- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/69—Filters or screens for the moulding material
- B29C48/694—Cylindrical or conical filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/66—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D29/68—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/94—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging the filter cake, e.g. chutes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Filtration Of Liquid (AREA)
Abstract
A self-impurity-removing cylindrical filter device with a backwashing net comprises a filter main body, an impurity-removing main body and an oil cylinder; the filter main body comprises a cylinder type main body shell, a cylinder type perforated plate, a cylinder type filter screen, a cylinder type backwashing support screen, an outlet plate and a main body cover plate, wherein the cylinder type perforated plate, the cylinder type filter screen and the cylinder type backwashing support screen are sleeved in the inner cavity of the cylinder type main body shell; a plurality of axial pre-filtering material channels are processed on the movable backwashing impurity discharging piston body around the central axis, and an annular backwashing flow channel and a meter-shaped backwashing flow channel which is communicated with the annular backwashing flow channel and the axial backwashing flow channel processed on the movable backwashing rod are arranged on the outer circular surface of the movable backwashing impurity discharging piston; the impurity discharging main body is connected with the right end of the movable backwashing rod, and the right end of the impurity discharging shell is connected with the oil cylinder.
Description
Technical Field
The invention relates to the recovery of various polymers, the production of plastic products, and the filtration of cellulose fiber stock solution in the textile industry, in particular to a cylindrical filtering device with an ultra-large filtering area and a backwashing net self-impurity-removing function.
Background
In the processes of polymer recovery, plastic product production and Lyocell fiber (Lyocell) cellulose stock solution filtration, a screen changer or a filter is required, some processes are recycling filtration, and some processes are filtration in product production, and Lyocell fiber (Lyocell) cellulose is special and requires filtration in the stock solution state before forming the fiber. The main purpose is to filter out impurities. The various screen changers or filters used at present have the problems, which are particularly shown in the following aspects:
(1) the common candle core type filter has large filtering area, solves the problem of frequent net replacement, but has overlarge cavity, large dead angle of a flow channel, serious material stagnation (retention), difficult replacement within a few hours, high use cost and application only in polyester spinning, and the filter screen is blocked and can not be backwashed on line without halt.
(2) Although the filter area of the multi-disc type filter is large, the problem of frequent screen replacement is solved, the filter screen is blocked and cannot be backwashed online without halt, and the use cost is high. Although the domestic multi-disc filter of imported Ribanum Mileen Mika company is also a material feeding mode in the center and has the impurity removing function of the self-flowing on-line non-stop backwashing filter screen, a backwashing flow control system is not provided, the influence on production during backwashing is large, the use cost of a special disc filter screen is high, and the purchase and maintenance cost of the filter is also high.
(3) The common plate-type or column-type screen changer or filter has small filtering area or can not backwash the filter screen to discharge impurities.
(4) In the common double-column back-flushing screen changer, when the filter screen is blocked, the filter screen is back-flushed on line by using external hydraulic power, but the filter unit needs to be separated from the filtering work, the flow rate of the process is greatly changed, and the production influence is large. Although the backwashing speed is high, the flow ratio of materials in the cavity is greatly different, a short circuit phenomenon is easily formed when the whole filter screen is backwashed, only local impurities are reversely discharged, and the backwashing efficiency is extremely low. Needs the outside to provide power for backwashing, can not utilize self material pressure to carry out gravity flow type backwashing filter screen, and the limited filter area of structure is not big.
(5) The filter is a meshless filter, which does not use a common filter screen but a special filter disc, and the filter disc is provided with small holes with dense and hemp meshes for materials to pass through. The scraper is tightly attached to the surface of the filter disc and continuously rotates at a low speed to scrape impurities, the filter does not need to replace a filter screen, the impurities can be automatically and centrifugally discharged, and the impurity discharge flow is controllable. But the filter disc has low filtering precision and cannot meet the requirement of fine filtering; the scraper continuously rotates on the surface of the filter disc, impurities are easily clamped into small holes of the mesh disc under the action of the scraper, and the impurities and the small holes are damaged very quickly; external force is needed to assist in removing impurities; the filter disc has poor corrosion resistance and is easy to damage.
Disclosure of Invention
The invention aims to provide the backwashing net self-impurity-removing cylindrical filtering device with a more scientific and reasonable structure aiming at the defects in the prior art.
The aim of the invention can be achieved by the following technical measures:
the self-impurity-removing cylindrical filter device with the backwashing net comprises a filter main body, an impurity-removing main body and an oil cylinder; the filter main body comprises a cylinder type main body shell, a cylinder type perforated plate, a cylinder type filter screen and a cylinder type backwashing support net which are sequentially sleeved in an inner cavity of the cylinder type main body shell in a coaxial line mode, a main body cover plate which is packaged on a body at the right end of the cylinder type main body shell and is provided with a material inlet communicated with the cylinder type pre-filter cavity, an outlet plate packaged at the left end of the cylinder type main body shell, a movable backwashing rod which is processed through the main body cover plate and is arranged in the cylinder type pre-filter cavity in a penetrating mode through a central shaft hole, a movable backwashing impurity-removing piston arranged at the left end of the movable backwashing rod and a cylinder type backwashing support matched with the movable; a plurality of axial pre-filtering material channels are processed on the movable backwashing impurity discharging piston body around the central axis, and an annular backwashing flow channel and a meter-shaped backwashing flow channel for communicating the annular backwashing flow channel with the axial backwashing flow channel processed on the movable backwashing rod are arranged on the outer circular surface of the movable backwashing impurity discharging piston; the impurity discharging main body consists of an impurity discharging shell connected with the right end of the movable backwashing rod, an impurity discharging screw rod and an impurity discharging screw sleeve which are arranged in the impurity discharging shell and provided with a self-impurity discharging gear, and the inner cavity of the impurity discharging shell is communicated with the axial backwashing flow channel of the movable backwashing rod; the right end of the impurity discharging shell is connected with the oil cylinder.
Furthermore, the material inlet on the main body cover plate is composed of three branch channels; the impurity removing main body is combined with the supporting rod slideway in a sliding fit mode through the guide rail bracket.
The cylindrical backwashing support is of a hollow structure, a backwashing support annular flow channel is formed in the circumferential direction of the cylindrical backwashing support, and the axial shape of the backwashing support annular flow channel is conical so as to increase the contact area with the cylindrical backwashing support net and further increase the filtering area and the backwashing area; the circular grooves for installing the cylindrical backwashing supporting net and the cylindrical filter screen are processed on the outer surface of the surrounding cylindrical backwashing support, the inner wall of the cylindrical backwashing support is in sliding fit with the movable backwashing impurity-removing piston, and the cylindrical perforated plate sleeved on the outer circular surface of the cylindrical filter screen is combined with the cylindrical backwashing support in a static fit mode.
The cylindrical perforated plate plays a role in supporting the filter screen, is matched with the cylindrical backwashing support and then clamped at two ends of the cavity of the filtering device, and is fixed in the cavity through bolts; the annular cavity between the outer surface of the cylindrical perforated plate and the inner wall of the cylindrical main body shell is used as a filtered material flow channel, because a material outlet after passing through the net is positioned at the left end of the filtering device, in order to prevent material stagnation, the distance between the outer surface of the cylindrical perforated plate and the inner wall of the cylindrical main body shell is gradually increased from small to large according to the material flow direction, the distance at the left end is twice as large as the distance at the right end, and a plurality of arc-shaped material channels which axially penetrate through the circumference of the left end surface of the perforated plate and face the outlet end arc-shaped material channel are arranged at the bottom of the annular cavity at the left end and are used as material; the material discharge channel is designed to be flat in structure for reducing material stagnation.
The invention has the following beneficial effects:
technical point of view, it is described what problems are solved and what advantages are brought about by the invention
1. The device has the advantages of super large filtering area, high material flow, no material detention, use of a common filter screen, online backwashing of the screen without shutdown, reduction of screen replacement times and low use cost.
2. This device adopts the mode of center feeding, fine solution the filter screen backwash problem, takes each mode of breaking through portable backwash piston to whole filter screen, progressively takes reverse net of washing to each part of filter screen, and the net area is little, the dynamics is big, the pressure fluctuation is little, no short circuit phenomenon to washing at every turn, and is efficient, effectual, does not shut down.
3. The filter device runs on line in a full-automatic mode, impurities are discharged through backwashing, the melt and the residual pressure of the impurities are used for pushing the impurity discharging device, the impurity discharging speed and flow are controllable, and the influence on the pressure of a main channel is extremely small during impurity discharging, so that stable-pressure continuous production is realized.
Drawings
Fig. 1 is a front view of the present invention (normal operation when backwashing is not performed).
Fig. 2 is a sectional view a-a of fig. 1.
Fig. 3 is a sectional view B-B of fig. 1.
Fig. 4 is a cross-sectional view C-C of fig. 1.
Fig. 5 is a cross-sectional view D-D of fig. 1.
Fig. 6 is a cross-sectional view E-E of fig. 1.
Fig. 7 is a sectional view F-F of fig. 2.
FIG. 8 is a schematic diagram of the normal operation + backwash operation of the present invention.
Fig. 9 is a sectional view a-a of fig. 8.
Fig. 10 is a sectional view B-B of fig. 8.
Fig. 11 is a sectional view F-F of fig. 9.
Number in the figure: 1 is a cylinder type main body shell, 2 is a cylinder type pre-filtering cavity, 3 is a main body cover plate, 4 is a support rod slideway, 5 is an axial backwashing runner, 6 is an oil cylinder, 7 is a self-impurity-removing gear 7, 8 is a guide rail bracket, 9 is a material inlet, 10 is a filtered material runner (a cylindrical material runner), 11 and a movable backwashing rod, 12 is an arc-shaped material channel penetrating through the circumference of the left end face of a porous plate, 13 is an outlet end arc-shaped material channel (a bottom arc-shaped material runner), 14 is a cylinder type porous plate, 15 is a cylinder type backwashing bracket, 16 is a movable backwashing impurity-removing piston, 17 is a rice-shaped backwashing runner, 18 is a bottom discharge channel, 19 is a main discharge hole, 20 is a pre-filtering material channel, 21 is a cylinder type backwashing support net, 22 is a cylinder type filter screen, 23 is an outlet plate, 24 is a backwashing bracket annular runner, 25 is an annular backwashing runner, 26, 28 is a trash discharging shell, 29 is a trash discharging high-pressure cavity inlet, 30 is a cooling channel, 31 is a trash discharging screw rod, 32 is a trash discharging screw sleeve, 33 is a heater, and 34 is a high-pressure trash decompression channel.
Detailed Description
The invention will be further described with reference to the following examples (drawings):
as shown in fig. 1, 7, 8 and 11, the backwashing net self-impurity-removing cylindrical filtering device comprises a filtering main body, an impurity-removing main body and an oil cylinder; the filter main body comprises a cylinder type main body shell 1, a cylinder type perforated plate 14, a cylinder type filter screen 22 and a cylinder type backwashing support net 21 which are sequentially sleeved in an inner cavity of the cylinder type main body shell in a coaxial mode, a main body cover plate 3 which is packaged on a body at the right end of the cylinder type main body shell and is provided with a material inlet communicated with the cylinder type pre-filter cavity 2, an outlet plate 23 packaged at the left end of the cylinder type main body shell, a movable backwashing rod 11 which is arranged in the cylinder type pre-filter cavity 2 in a penetrating mode through a central shaft hole processed by the main body cover plate 3, a movable backwashing impurity-discharging piston 16 which is arranged at the left end of the movable backwashing rod 11, and a cylinder type backwashing support 15 which is matched with the; a plurality of axial pre-filtering material channels 20 are processed on the movable backwashing impurity-removing piston body around the central axis, and an annular backwashing flow channel 25 and a meter-shaped backwashing flow channel 17 which is communicated with the annular backwashing flow channel and an axial backwashing flow channel 5 processed on the movable backwashing rod 11 are arranged on the outer circular surface of the movable backwashing impurity-removing piston; the impurity discharging main body (see figure 5) consists of an impurity discharging shell 28 connected with the right end of the movable backwashing rod 11, an impurity discharging screw 31 and an impurity discharging screw sleeve 32 which are arranged in the impurity discharging shell and provided with a self-impurity discharging gear 7, and an inner cavity (impurity discharging high-pressure cavity) of the impurity discharging shell is communicated with an axial backwashing flow channel of the movable backwashing rod 11 by 5; the right end of the impurity discharging shell is connected with the oil cylinder 6.
As shown in fig. 4, the material inlet on the main body cover plate is composed of three branch channels.
As shown in fig. 6, the trash removal body is coupled to the pole runner 4 in a sliding fit manner by a rail bracket 8.
As shown in fig. 2, 3, 9 and 10, the cylindrical backwash support 15 is a hollow structure, a backwash support annular flow passage 24 is arranged along the circumferential direction of the cylindrical backwash support, and the axial shape of the backwash support annular flow passage 24 is conical so as to increase the contact area with the cylindrical backwash support net and further increase the filtration area and the backwash area; the circular grooves for installing the cylindrical backwashing supporting net 21 and the cylindrical filter screen 22 are processed around the outer surface of the cylindrical backwashing support 15, the inner wall of the cylindrical backwashing support is in sliding fit with the movable backwashing impurity-removing piston, and the cylindrical porous plate 14 sleeved on the outer circular surface of the cylindrical filter screen 22 is combined with the cylindrical backwashing support in a static fit mode.
The cylindrical perforated plate 14 plays a role in supporting a filter screen, and the cylindrical perforated plate 14 is matched with the cylindrical backwashing support 15 and then clamped at two ends of a cavity of the filtering device and is fixed in the cavity through bolts; the annular cavity between the outer surface of the cylinder type perforated plate 14 and the inner wall of the cylinder type main body shell 1 is used as a filtered material flow channel, because the material outlet after passing through the net is positioned at the left end of the filtering device, in order to prevent the material from stagnation, the distance between the outer surface of the cylinder type perforated plate 14 and the inner wall of the cylinder type main body shell 1 is arranged in a mode of gradually increasing from small to large according to the material flow direction, the distance at the left end is twice larger than the distance at the right end, and a plurality of arc-shaped material channels 12 which axially penetrate through the circumference of the left end surface of the perforated plate and face the arc-shaped material channel 13 at the outlet end are arranged at the bottom of; the material discharge channel is designed to be flat in structure for reducing material stagnation.
The specific working principle of the invention is as follows:
firstly, when the device filters normally, the structure, function and working principle of the filtering main body (as shown in figure 1) are as follows:
scheme 1: the filter material is divided into three channels from the material inlet on the main body cover plate, and the problem that the material channel cannot be designed too large is mainly considered, otherwise, the cylindrical pre-filter cavity is correspondingly large, and thus, material stagnation (retention) can be caused to generate side effects.
And (2) a flow scheme: after the material gets into the chamber body before the cylinder is strained, flow to all around of a section of thick bamboo under the effect of melt pressure, at first pass the drum formula backwash support of fretwork, what set up along the circumferencial direction on the drum formula backwash support has backwash support stream ring shape runner, and the axial shape of backwash support runner is the toper, and the purpose is the area of contact of increase and drum formula backwash supporting network, and then increase filtration area and backwash area. The outer surface of the cylindrical backwashing support is provided with a cylindrical shallow groove which is mainly used for installing a cylindrical backwashing support net and a cylindrical filter screen. The inner wall of the cylinder type backwashing support is in sliding fit with the movable backwashing impurity-removing piston, and the outer circle of the cylinder type backwashing support is in static fit with the cylinder type porous plate.
And (3) a flow path: the material melt flows through the cylindrical backwashing supporting net after passing through the backwashing support. When in backwashing, the strength and the rigidity of the filter screen are not enough to be normally used on the cylindrical backwashing support, so that the filter screen is easy to collapse at the hollow part of the cylindrical backwashing support. Therefore, a layer of cylindrical backwashing supporting net is designed, the mesh number of the cylindrical backwashing supporting net is small, impurities can easily pass through in two directions, but the cylindrical backwashing supporting net has high strength and rigidity and is corrosion-resistant, and the cylindrical backwashing supporting net is not replaced along with a filtering net generally.
And (4) a flow chart: the material melt flows through the cylindrical filter screen after passing through the cylindrical backwashing supporting screen, and the mesh number of the filter screen is changed according to the requirement of the filtering precision of the product. And common or corrosion-resistant materials can be used.
And (5) a flow chart: after passing through the screen, the material melt passes through the cylindrical perforated plate which plays a role of supporting the filter screen, is matched with the cylindrical backwashing support and then clamped at two ends of the cavity of the filtering device, and is fixed at the bottom of the cavity through bolts. The ring channel has been seted up to drum formula perforated plate surface and has been used for the material runner, because the material export behind the net is in filter equipment's bottom, for preventing the material stagnation, the groove depth ratio of drum formula perforated plate surface ring channel (material passageway) the left side exit is twice the degree of depth of the other end, in addition at drum formula perforated plate surface ring shape material passageway deepest in the left side, toward being equipped with a plurality of outward along the bottom axial and lining up arc slot, be used as the material passageway, for reducing the material stagnation to design into the platykurtic to the material passageway, with the area of contact who increases and drum formula perforated plate surface ring shape material passageway. The position of the discharge channel is opposite to the arc-shaped discharge channel at the bottom of the filter device, so that the materials passing through the porous plate after passing through the net can smoothly pass through the discharge channel.
And (6) a flow path: clean material behind the cross net comes out from filter equipment bottom arc material runner back flow direction and strains device bottom "rice" style of calligraphy runner, and the arc runner of this centre broad narrows down through "fan-shaped" transition confluence, and the surface of device bottom is strained to the multistrand runner is whole is seted up, joins into one at last and flows to the main discharge gate on the export board from the bottom discharge gate to accomplish the filtration of whole material.
Scheme 7: when the filtering device normally works, the movable backwashing piston stops at a fixed position at the bottom of the device, at the moment, the annular backwashing flow channel, the Mi-shaped backwashing flow channel and the backwashing flow channel are in a closed state, the materials do not overflow when the melting pressure of the materials is increased, the impurity discharging screw sleeves are connected at two end faces of the impurity discharging shell, a cooling channel is arranged on each impurity discharging screw sleeve, the materials brought out by impurity discharging and the mixture of the impurities meet cold and can be solidified, and under the combined action of the screw ribs on the impurity discharging screw rod, the melt cannot overflow under any condition.
Secondly, when the device works normally and performs backwashing, the backwashing structure, function and working principle (as shown in figure 8): during the recovery of polymer, the production of plastic products and the filtration of Lyocell fiber (Lyocell) cellulose stock solution, the pressure of material melt in front of a screen is increased along with the accumulation of impurities on the surface of the screen, and after the pressure reaches a set pressure value triggering the backwashing action of the screen, heaters at two ends of an impurity-removing screw sleeve on an impurity-removing shell work, and the cooling stops. The mixture of the material and the impurities in the impurity discharging shell and the impurity discharging screw sleeve is melted into a viscous state, so that the impurity discharging screw rod is convenient to discharge. When the temperature of the impurity removing main body reaches a set temperature, the hydraulic system starts to work, and a piston rod of the oil cylinder drives the impurity removing main body, the movable backwashing rod and the movable backwashing impurity removing piston to slowly move at a controllable speed. The annular backwash flow channel on the movable backwash impurity discharge piston is connected with the annular flow channel of the backwash support instantly, the gravity backwash starts, because one annular flow channel of the backwash support is completely sealed by the movable backwash impurity discharge piston, the material melt to be filtered cannot enter, and the annular backwash flow channel is connected with the annular backwash flow channel on the movable backwash impurity discharge piston at the moment, the annular backwash flow channel is communicated with the reverse backwash flow channel in the shape of a Chinese character 'mi', the material melt and the impurity mixture in the whole channel are basically at normal pressure. Meanwhile, impurities on the surface of the filter screen can be reversely pushed out by the high-pressure material after passing through the screen, rapidly flow through the annular flow channel and the annular backwashing flow channel of the backwashing support, flow to the backwashing flow channel after converging through the Mi-shaped backwashing flow channel, the high-pressure material melt and the impurity mixture reach the impurity discharge inlet high-pressure cavity of the impurity discharge shell and then push the self-impurity discharge gear to rotate, then flow to the impurity discharge screw rods at two ends when passing through the impurity pressure discharge channel, the impurity discharge screw rods rotate under the driving of the impurity discharge gear, power is applied to the mixture of the material melt and the impurities, and the impurities are smoothly discharged.
And thirdly, the stay time of the annular backwashing flow channel on the movable backwashing impurity removal piston after being communicated with the annular flow channel of the backwashing support can be set so as to meet the backwashing effect of different types of impurities of different materials. Each backwashing process does not influence the normal work of the filter screens in other areas, and because the backwashing area is small, the flow pressure is concentrated, and the backwashing flow passages are designed and distributed in all directions, the backwashing effect is good, the efficiency is high, the short circuit phenomenon and the fluctuation are avoided, and the production is not influenced.
And fourthly, as the movable backwashing impurity removing piston is provided with a pre-filtering material channel, when the pre-filtering material channel moves out of the fixed position, the free flow of the pre-filtering material is not influenced.
And fifthly, the movable backwashing impurity discharging piston, the movable backwashing rod and the impurity discharging main body freely reciprocate under the action of the oil cylinder, and the time and displacement of each position are controllable.
Sixthly, in order to prevent the movable backwashing rod from sinking due to the weight of the impurity discharging main body, a supporting rod slideway and a guide rail support are specially designed, so that the stable operation in the backwashing process is ensured.
7. The device does not need external power during backwashing, and the melt pressure of the material melt in the device is enough to reversely backwash the filter screen and discharge impurities.
8. Because the inside melt pressure of device is great during the backwash, the velocity of flow of material fuse-element and impurity mixture can be through the mode of control row miscellaneous swivel nut outside temperature, adjusts the viscosity of material, avoids the velocity of flow to cause the inside pressure oscillation of device big at the excessive speed, influences the normal production of product. If the temperature is too low, the viscosity of the mixture is too low and even solidification is not possible, so that the impurity mixture is not discharged.
9. The movable backwashing trash removal piston can freely reciprocate, the melt pressure of the whole filter screen is reduced to a normal value after backwashing once, the movable backwashing trash removal piston returns to a fixed position, the oil cylinder stops acting, meanwhile, the trash removal threaded sleeve on the trash removal main body stops heating, and cooling is started. And the filter device works normally and waits for the next backwashing net signal and action.
10. The area of the cylindrical filter screen is overlarge, and the cylindrical filter screen can be manufactured by using a common filter screen, and the cylindrical filter screen is lower than the special manufacturing cost of a disc type screen disc and a candle wick type filter screen.
11. The filter device can be used as a filter unit, and a plurality of units are used in parallel to meet the production of products with ultrahigh yield or very many impurities, such as: when a plurality of units are connected in parallel for use, the filter screen can be backwashed by each unit in turn, so that the pressure and flow fluctuation during backwashing can be avoided, the pressure and flow of the whole system are super-stable, and the production of high-quality products is facilitated.
Claims (5)
1. The utility model provides a backwash net is from arranging miscellaneous drum formula filter equipment which characterized in that: the device comprises a filtering main body, a impurity removing main body and an oil cylinder; the filter main body comprises a cylinder type main body shell, a cylinder type perforated plate, a cylinder type filter screen and a cylinder type backwashing support net which are sequentially sleeved in an inner cavity of the cylinder type main body shell in a coaxial line mode, a main body cover plate which is packaged on a body at the right end of the cylinder type main body shell and is provided with a material inlet communicated with the cylinder type pre-filter cavity, an outlet plate packaged at the left end of the cylinder type main body shell, a movable backwashing rod which is processed through the main body cover plate and is arranged in the cylinder type pre-filter cavity in a penetrating mode through a central shaft hole, a movable backwashing impurity-removing piston arranged at the left end of the movable backwashing rod and a cylinder type backwashing support matched with the movable; a plurality of axial pre-filtering material channels are processed on the movable backwashing impurity discharging piston body around the central axis, and an annular backwashing flow channel and a meter-shaped backwashing flow channel which is communicated with the annular backwashing flow channel and an axial backwashing flow channel 5 processed on the movable backwashing rod are arranged on the outer circular surface of the movable backwashing impurity discharging piston; the impurity discharging main body consists of an impurity discharging shell connected with the right end of the movable backwashing rod, an impurity discharging screw rod and an impurity discharging screw sleeve which are arranged in the impurity discharging shell and provided with a self-impurity discharging gear, and the inner cavity of the impurity discharging shell is communicated with the axial backwashing flow channel of the movable backwashing rod; the right end of the impurity discharging shell is connected with the oil cylinder.
2. The backwash net self-draining cylindrical filter device as defined in claim, wherein: the material inlet on the main body cover plate is composed of three branch channels.
3. The backwash net self-draining cylindrical filter device as defined in claim, wherein: the cylindrical backwashing support is of a hollow structure, a backwashing support annular flow channel is formed in the circumferential direction of the cylindrical backwashing support, and the axial shape of the backwashing support annular flow channel is conical so as to increase the contact area with the cylindrical backwashing support net and further increase the filtering area and the backwashing area; the circular grooves for installing the cylindrical backwashing supporting net and the cylindrical filter screen are processed on the outer surface of the surrounding cylindrical backwashing support, the inner wall of the cylindrical backwashing support is in sliding fit with the movable backwashing impurity-removing piston, and the cylindrical perforated plate sleeved on the outer circular surface of the cylindrical filter screen is combined with the cylindrical backwashing support in a static fit mode.
4. The backwash net self-draining cylindrical filter device as defined in claim, wherein: the cylindrical perforated plate plays a role in supporting the filter screen, is matched with the cylindrical backwashing support and then clamped at two ends of the cavity of the filtering device, and is fixed in the cavity through bolts; the annular cavity between the outer surface of the cylindrical perforated plate and the inner wall of the cylindrical main body shell is used as a filtered material flow channel, because a material outlet after passing through the net is positioned at the left end of the filtering device, in order to prevent material stagnation, the distance between the outer surface of the cylindrical perforated plate and the inner wall of the cylindrical main body shell is gradually increased from small to large according to the material flow direction, the distance at the left end is twice as large as the distance at the right end, and a plurality of arc-shaped material channels which axially penetrate through the circumference of the left end surface of the perforated plate and face the outlet end arc-shaped material channel are arranged at the bottom of the annular cavity at the left end and are used as material; the material discharge channel is designed to be flat in structure for reducing material stagnation.
5. The backwash net self-draining cylindrical filter device as defined in claim, wherein: the impurity removing main body is combined with the supporting rod slideway in a sliding fit mode through the guide rail bracket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011535239.0A CN112354241A (en) | 2020-12-23 | 2020-12-23 | Self-impurity-removing cylindrical filter device with backwashing net |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011535239.0A CN112354241A (en) | 2020-12-23 | 2020-12-23 | Self-impurity-removing cylindrical filter device with backwashing net |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112354241A true CN112354241A (en) | 2021-02-12 |
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ID=74534587
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011535239.0A Pending CN112354241A (en) | 2020-12-23 | 2020-12-23 | Self-impurity-removing cylindrical filter device with backwashing net |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112354241A (en) |
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2020
- 2020-12-23 CN CN202011535239.0A patent/CN112354241A/en active Pending
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