CN110975371A - Up-flow type deep penetration pressure thickener - Google Patents
Up-flow type deep penetration pressure thickener Download PDFInfo
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- CN110975371A CN110975371A CN201911048611.2A CN201911048611A CN110975371A CN 110975371 A CN110975371 A CN 110975371A CN 201911048611 A CN201911048611 A CN 201911048611A CN 110975371 A CN110975371 A CN 110975371A
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- 239000002562 thickening agent Substances 0.000 title abstract description 13
- 230000035515 penetration Effects 0.000 title abstract description 10
- 238000007906 compression Methods 0.000 claims abstract description 41
- 230000006835 compression Effects 0.000 claims abstract description 40
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 239000000835 fiber Substances 0.000 claims abstract description 15
- 238000007789 sealing Methods 0.000 claims abstract description 13
- 238000003466 welding Methods 0.000 claims abstract description 7
- 230000000630 rising effect Effects 0.000 claims abstract description 5
- 238000005520 cutting process Methods 0.000 claims description 34
- 210000000078 claw Anatomy 0.000 claims description 15
- 238000003825 pressing Methods 0.000 claims description 15
- 230000000149 penetrating effect Effects 0.000 claims description 9
- 230000003204 osmotic effect Effects 0.000 claims description 8
- 238000001179 sorption measurement Methods 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 4
- 239000002657 fibrous material Substances 0.000 abstract description 24
- 239000000706 filtrate Substances 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 4
- 239000010410 layer Substances 0.000 description 18
- 238000003892 spreading Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 230000005540 biological transmission Effects 0.000 description 5
- 239000011229 interlayer Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000011550 stock solution Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000002955 isolation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
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- 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
- B01D29/01—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 flat filtering elements
- B01D29/03—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 flat filtering elements self-supporting
-
- 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
- B01D29/31—Self-supporting filtering elements
- B01D29/35—Self-supporting filtering elements arranged for outward flow filtration
-
- 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
- B01D29/50—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 multiple filtering elements, characterised by their mutual disposition
- B01D29/56—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 multiple filtering elements, characterised by their mutual disposition in series connection
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
Abstract
The invention provides an up-flow type deep penetration pressure thickener which structurally comprises an outer output pipe, a thickener base, a sanitary towel fiber liquid input pipe, a top sealing cover, a concentration tank, an air pump and an up-flow deep penetration pressure device, wherein the outer output pipe is fixedly arranged on the rear side face of the bottom end of the concentration tank, the top sealing cover is fixedly connected to the top end of the concentration tank in an electric welding mode, the air pump is movably connected with the concentration tank, the right end of the sanitary towel fiber liquid input pipe is arranged in the left inner portion of the top sealing cover in an embedding mode, a flow rising pipe is passively unfolded under the increase of a compression stroke, a sleeving mechanism is laterally unfolded, fiber material liquid in an input area of the flow rising pipe at the bottom can be subjected to pressure release filtration, filtrate can be discharged to the upper layer by the pressure in the inner portion, and further, the upper limit of compression can be improved, and compressed fiber material liquid with.
Description
Technical Field
The invention belongs to the field of sanitary towel concentration, and particularly relates to an up-flow type deep penetration pressure concentrator.
Background
The upflow type pressure thickener mainly separates and compresses the liquid in the stock solution and the originally mixed fiber material in the stock solution in a same body mode through reverse compression of the fiber stock solution which is crushed, can effectively compress the concentration of the fiber material of the sanitary towel water absorption sheet, and can enable the concentration of the fiber material to be higher when the water absorption sheet is pressed, so that the water absorption effect of the fiber material is enhanced.
Based on the above description, the present inventors found that the existing upflow deep-pressure thickener mainly has the following disadvantages, such as:
because in the concentrated compression jar of sanitary towel, the compression of STREAMING is in the offset pressing in-process, the pressure that appears the presswork piece and is close to the layer constantly strengthens with density easily, and then increases gradually the degree of difficulty that oozes the liquid that exists in the upflow pipe input area and after the isolation hole of presswork piece is whole is blockked up, the pressure in the upflow pipe input area can rise rapidly, and then leads to the fibrous material mixed liquid compression limit of sanitary towel preparation to appear prematurely.
Disclosure of Invention
In order to solve the technical problems, the invention provides an up-flow type deep penetration pressure thickener, which aims to solve the problems that in the conventional compression tank for sanitary towel concentration, the pressure and the density of a layer adjacent to a pressed sheet are easy to be continuously enhanced in the up-flow type compression process, the difficulty of liquid leakage existing in an input area of an up-flow pipe is gradually increased, and the pressure in the input area of the up-flow pipe can rapidly rise after isolation holes of the pressed sheet are completely blocked, so that the compression limit of a fiber material mixed liquid for sanitary towel manufacturing is prematurely caused.
Aiming at the defects of the prior art, the purpose and the effect of the up-flow deep penetration pressure thickener are achieved by the following specific technical means: the utility model provides a concentrated machine of pressure of STREAMING degree of depth osmotic pressure, its structure includes outside output tube, concentrator base, sanitary towel fibre liquid input tube, capping lid, concentrated jar, air pump machine, the degree of depth osmotic pressure device that flows upward, outside output tube fixed mounting is in concentrated tank bottoms trailing flank, the mode fixed connection that capping lid adopted electric welding in concentrated tank tops end, air pump machine and concentrated jar swing joint together, sanitary towel fibre liquid input tube right-hand member is installed inside capping left side through the mode of embedding, concentrated machine base adopts the mode fixed connection of electric welding in concentrated tank bottoms end, the inside degree of depth osmotic pressure device that flows upward that is equipped with of concentrated jar.
The upflow deep pressure device comprises four top separation adsorption sheets, a deep pushing autogenous cutting mechanism, an inner groove and an upflow pressure mechanism, wherein the four top separation adsorption sheets are fixedly welded on the inner surface of a concentration tank, the inner groove and the concentration tank are of an integrated structure, and the deep pushing autogenous cutting mechanism is fixedly connected with the upflow pressure mechanism.
Preferably, the deep pushing and air-cutting mechanism comprises a push claw, a matched locking groove, an air-cutting envelope and a discharging piece, the push claw is fixedly connected with the discharging piece, the air groove is formed in the middle of the push claw, the air-cutting envelope and the push claw are of an integrated structure, the matched locking groove is fixedly formed in the left side and the right side of the push claw, the deep pushing and air-cutting mechanism can evenly press the upflow and thorough-pressure mechanism through triangular stress setting, further keep balance on plane stress, further realize stable compression, and push and cut strips through the downward pressing of the air groove under the force application of force so as to switch the double-cutting compression net into a compression state.
Preferably, the upflow and thorough pressure mechanism comprises a pressure transmission pipe, a push-cut strip, an outer ring sleeve, a double-cut compression net, a sealing air passage and a flow-up pipe, the flow-up pipe is arranged inside the double-cut compression net in a penetrating mode, the push-cut strip is arranged in the sealing air passage in an embedded mode, the outer ring sleeve is fixedly connected with the double-cut compression net, the pressure transmission pipe is welded with the double-cut compression net, the upflow and thorough pressure mechanism can filter and press fiber materials in fiber liquid through continuous pressing, so that the mixed liquid inside is filtered and positioned at an upper layer position to be formed in the same tank body, layers with different concentrations are formed, the mixed liquid can be continuously input into the flow-up pipe, the internal pressure and the concentration are continuously enhanced, and the concentration can be further compressed through the pressure transmission pipe.
As preferred, the pipe is pressed to permeation includes that bushing mechanism, draw runner ring, traction band, exhibition prop the piece, play the filter screen, bushing mechanism props piece fixed connection with the exhibition and is in the same place, the draw runner ring props the piece with the exhibition and is connected, inside the exhibition prop the piece is located to the traction band, it installs in exhibition prop the piece side to play the filter screen, the exhibition prop the piece along with the increase of stroke can reduce the coefficient of friction with the contact surface through the draw runner ring, and then carry out the side pressure to the outside and expand to will play the filter screen and draw and expand, make the inside liquid of interlayer can not pass through the top layer filter pressing, can directly carry out the interlayer under the high pressure and carry out the interlayer through the bottom.
Preferably, the double-cutting compression net comprises a cutting strip, an upper sleeve net, a lower sleeve net and a pressing strip, the cutting strip and the upper sleeve net are of an integrated structure, the upper sleeve net and the lower sleeve net are movably connected together, and the pressing strip is installed between the upper sleeve net and the lower sleeve net in an embedded mode.
Preferably, the sleeve mechanism comprises a side sleeve piece, a brush block, a hanging piece, a sleeving cover strip, a folding sleeve and a side filter piece, the side filter piece is arranged in the folding sleeve, the brush block is arranged in the side sleeve piece, the hanging piece and the side sleeve piece are of an integrated structure, and the top end of the sleeving cover strip is connected with the hanging piece.
Compared with the prior art, the invention has the following advantagesAdvantageous effects：
The double-cutting compression net can be switched by the deep pushing autogenous cutting mechanism in the process of pushing and pressurizing the upflow penetrating and pressing mechanism, so that smaller fiber materials can be blocked and filtered, the upflow pipe is passively expanded under the increase of the compression stroke along with the increase of the compression concentration, the sleeve mechanism is laterally expanded, fiber material liquid in an input area of the upflow pipe at the bottom can be subjected to pressure release filtration, the filtrate can be extruded to the upper layer by the internal pressure, and the compressed fiber material liquid with higher concentration can be obtained while the upper limit of compression is improved.
Drawings
FIG. 1 is a schematic diagram of an upflow deep-pressure thickener according to the present invention.
Fig. 2 is a schematic structural view of a cross section of an upflow deep well pressure concentrator in front view.
Fig. 3 is a detailed structural diagram of the inside of the deep pushing autogenous cutting mechanism.
Fig. 4 is a detailed structural diagram of the interior of the upflow and transpression mechanism.
Fig. 5 is a detailed structural diagram of the interior of the pressure transmission pipe.
Fig. 6 is a detailed internal structure diagram of a double-cut compression net.
Fig. 7 is a detailed structural diagram of the interior of the sleeve mechanism.
In the figure: an outer output pipe-1, a thickener base-2, a sanitary towel fiber liquid input pipe-3, a capping cover-4, a concentration tank-5, an air pump machine-6, an upflow deep pressure device-7, a top isolating adsorption sheet-a 1, a deep pushing airlock mechanism-a 2, an inner groove-a 3, an upflow pressure mechanism-a 4, a pushing claw-a 21, a locking groove-a 22, an air groove-a 23, an airlock sleeve-a 24, a pressure-a 25, a pressure transmission pipe-a 41, a pushing and cutting strip-a 42, an outer ring sleeve-a 43, a double-cutting compression net-a 44, a sealing air duct-a 45, an upflow pipe-a 46, a sleeve mechanism-a 411, a sliding strip ring-a 412, a pulling strip-a 413, a spreading and supporting sheet-a 414, an elastic filter screen-a 415, a cutting strip-a 441, an upper sleeve-a 442, a lower sleeve net-a 411, a sleeve net-a, Pressing strip-a 444, side sleeve sheet-a 11, brush block-a 12, hanging sheet-a 13, sleeve cover strip-a 14, folding sleeve pipe-a 15 and side filter sheet-a 16.
Detailed Description
The embodiments of the present invention will be described in further detail with reference to the drawings and examples. The following examples are intended to illustrate the invention but are not intended to limit the scope of the invention.
In the description of the present invention, "a plurality" means two or more unless otherwise specified; the terms "upper", "lower", "left", "right", "inner", "outer", "front", "rear", "head", "tail", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, are only for convenience in describing and simplifying the description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed in a particular orientation, and be operated, and thus, should not be construed as limiting the invention. Furthermore, the terms "first," "second," "third," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "connected" and "connected" are to be interpreted broadly, e.g., as being fixed or detachable or integrally connected; can be mechanically or electrically connected; may be directly connected or indirectly connected through an intermediate. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Examples
As shown in figures 1 to 7:
the invention provides an up-flow type deep penetration pressure thickener which structurally comprises an outer output pipe 1, a thickener base 2, a sanitary towel fiber liquid input pipe 3, a top sealing cover 4, a concentration tank 5, an air pump machine 6 and an up-flow deep penetration pressure device 7, wherein the outer output pipe 1 is fixedly arranged on the rear side face of the bottom end of the concentration tank 5, the top sealing cover 4 is fixedly connected to the top end of the concentration tank 5 in an electric welding mode, the air pump machine 6 is movably connected with the concentration tank 5, the right end of the sanitary towel fiber liquid input pipe 3 is arranged inside the left side of the top sealing cover 4 in an embedded mode, the thickener base 2 is fixedly connected to the bottom end of the concentration tank 5 in an electric welding mode, and the up-flow deep penetration pressure device 7 is arranged inside the concentration tank 5.
The upflow deep pressure device 7 comprises a top separation adsorption sheet a1, a deep pushing airlock mechanism a2, an inner groove a3 and an upflow pressure mechanism a4, wherein the top separation adsorption sheet a1 is provided with four pieces and fixedly welded on the inner surface of the concentration tank 5, the inner groove a3 and the concentration tank 5 are of an integrated structure, and the deep pushing airlock mechanism a2 and the upflow pressure mechanism a4 are fixedly connected together.
The depth pushing and air cutting mechanism a2 comprises a push claw a21, a locking groove a22, an air groove a23, an air cutting envelope a24 and a sheet unloading a25, wherein the push claw a21 is fixedly connected with the sheet unloading a25, the air groove a23 is arranged in the middle of the push claw a21, the air cutting envelope a24 and the push claw a21 are of an integrated structure, the locking groove a22 is fixedly arranged on the left side and the right side of the push claw a21, and the depth pushing and air cutting mechanism a2 is arranged through triangular stress, so that the rising current penetrating and pressing mechanism a4 can be uniformly pressed, the rising current penetrating and pressing mechanism a4 is further balanced on plane stress, stable compression can be realized, and meanwhile, the pushing and cutting strip a42 can be pushed through force application of the air groove a23, and the double-cut compression net a44 can be switched into a compression state.
The upflow and pressure permeating mechanism a4 comprises a pressure permeating pipe a41, a push-cut strip a42, an outer ring sleeve a43, a double-cut compression net a44, a sealing air channel a45 and a riser pipe a46, wherein the riser pipe a46 is installed inside the double-cut compression net a44 in a penetrating mode, the push-cut strip a42 is installed inside the sealing air channel a45 in an embedding mode, the outer ring sleeve a43 is fixedly connected with the double-cut compression net a44, the pressure permeating pipe a41 is welded with the double-cut compression net a44, the upflow and pressure permeating mechanism a4 can filter and press fiber materials in the fiber liquid through continuous pressing, and further filter and filter the mixed liquid inside, so that the mixed liquid is located at an upper layer position to form a same tank body, layers with different concentrations can be continuously input into the riser pipe a46, the internal pressure and the concentration are continuously enhanced, and the concentration of the riser pipe a41 can be further compressed.
The permeable pipe a41 comprises a sleeve mechanism a411, a slide bar ring a412, a traction belt a413, a spreading and supporting sheet a414 and an elastic filter screen a415, wherein the sleeve mechanism a411 and the spreading and supporting sheet a414 are fixedly connected together, the slide bar ring a412 is connected with the spreading and supporting sheet a414, the traction belt a413 is arranged inside the spreading and supporting sheet a414, the elastic filter screen a415 is installed on the side surface of the spreading and supporting sheet a414, the friction coefficient between the spreading and supporting sheet a414 and a contact surface is reduced through the slide bar ring a412 along with the increase of a pressure stroke, so that lateral pressure spreading is performed towards the outside, the elastic filter screen a415 is stretched and spread, and liquid inside the interlayer can be directly conveyed through the bottom layer of the permeable pipe a41 without being filtered and pressed by the top layer.
The double-cut compression net a44 comprises a cut strip a441, an upper cover net a442, a lower cover net a443 and a pressing strip a444, the cut strip a441 and the upper cover net a442 are of an integrated structure, the upper cover net a442 and the lower cover net a443 are movably connected together, the pressing strip a444 is installed between the upper cover net a442 and the lower cover net a443 in an embedded mode, after single compression is completed, a large amount of fiber materials can be hung on grids of the upper cover net a442 and the lower cover net a443, and when the upper cover net a442 and the lower cover net a443 are placed back, most of the fiber materials can be cut through side cutting of the cut strip a441, so that the fiber materials can be rewarded into filtrate, and enough space can be ensured before next compression.
The sleeve mechanism a411 comprises a side sleeve sheet a11, a brush block a12, a hanging sheet a13, a sleeve cover strip a14, a folding sleeve a15 and a side filter sheet a16, wherein the side filter sheet a16 is arranged inside the folding sleeve a15, the brush block a12 is installed inside the side sleeve sheet a11, the hanging sheet a13 and the side sleeve sheet a11 are of an integrated structure, the top end of the sleeve cover strip a14 is connected with the hanging sheet a13, the side sleeve sheet a11 is vertically drawn along with the expansion of the expansion sheet a414, can slide and expand downwards, the side filter sheet a16 protected inside is exposed, auxiliary flow distribution at different heights can be realized, and the compressed concentration of the sleeve mechanism can be further enhanced.
After the sleeve mechanism a411 completes single compression and diversion, when filtrate above the output end flows back, the brush block a12 can brush down fiber materials on the side filter disc a16 and seal the top end of the filter disc at a position easy to scrape, so that the filter disc is prevented from being hung passively again during backflow.
The specific use mode and function of the embodiment are as follows:
in the invention, the air is inflated and pressurized from the outside to the inside, the air is directly filled into the deep pushing and air cutting mechanism a2 through the telescopic air rod, the pushing and cutting strip a42 is pushed to the inside through the guide of the air groove a23, the bottom of the air groove is connected with the double-cutting compression net a44, when the air groove is slid by air pressure, the upper sleeve net a442 and the lower sleeve net a443 which are originally in a superposed state can be alternately superposed, the filtration pore formed by the upper sleeve net a442 and the lower sleeve net a443 is reduced, the whole upflow penetrating pressure mechanism a4 is pushed by the deep pushing and air cutting mechanism a2, the triangular force application of the deep pushing and air cutting mechanism a2 can enable the upflow penetrating pressure mechanism a4 to be uniformly stressed towards the plane of pressure feeding, the upflow pipe 46 continuously divides the input liquid through the top end input pipe and feeds the input liquid towards the inside, the double-cutting compression net a44 can filter the fiber materials in the fiber liquid and filter the mixed liquid below the fiber liquid, the high-concentration fiber material layer is positioned at the upper layer, the concentration of the fiber material is compressed at the lower part of the high-concentration fiber material layer, the high-concentration fiber material layer is formed in the same tank body, the layers with different concentrations are layered, the mixed liquid is continuously input through the riser pipe a46, the internal pressure and the concentration are continuously enhanced, the pressure range is gradually increased, the pressed value of the expansion supporting sheet a414 is in direct proportion to the pressure value, the friction coefficient of the bottom contact surface can be reduced through the sliding strip ring a412, the expansion supporting sheet a is further expanded towards the outer side surface, the traction belt a413 can be pulled while the expansion supporting sheet a413 is expanded, when the card is completely expanded, the traction length of the traction supporting sheet a is just capable of stretching and expanding the side sleeve sheet a11 in a sliding mode, the side filter sheet a16 in the inner part can be exposed, different-layer grade filtering can be formed by different-layer fiber mixed liquid from high-low concentration at the bottom of the high-concentration fiber material layer formed at, a fibrous material with a high compressed concentration can be obtained.
The embodiments of the present invention have been presented for purposes of illustration and description, and are not intended to be exhaustive or limited to the invention in the form disclosed. Many modifications and variations will be apparent to those of ordinary skill in the art. The embodiment was chosen and described in order to best explain the principles of the invention and the practical application, and to enable others of ordinary skill in the art to understand the invention for various embodiments with various modifications as are suited to the particular use contemplated.
Claims (6)
1. The utility model provides a pressure concentrator of STREAMING degree of depth osmotic pressure, its structure includes outside output tube (1), concentrator base (2), sanitary towel fibre liquid input tube (3), capping (4), concentrated jar (5), air pump machine (6), the pressure equipment of rising degree of depth osmotic pressure device (7), its characterized in that:
the outer side output pipe (1) is fixedly arranged on the rear side face of the bottom end of the concentration tank (5), the top sealing cover (4) is fixedly connected to the top end of the concentration tank (5) in an electric welding mode, the air pump machine (6) is movably connected with the concentration tank (5), the right end of the sanitary towel fiber liquid input pipe (3) is arranged inside the left side of the top sealing cover (4) in an embedding mode, the concentrator base (2) is fixedly connected to the bottom end of the concentration tank (5) in an electric welding mode, and an upflow depth permeation device (7) is arranged inside the concentration tank (5);
the upflow deep pressure device (7) comprises a top separation adsorption sheet (a1), a deep pushing airlock mechanism (a2), an inner groove (a3) and an upflow pressure mechanism (a4), wherein the top separation adsorption sheet (a1) is provided with four pieces and fixedly welded on the inner surface of the concentration tank (5), the inner groove (a3) and the concentration tank (5) are of an integrated structure, and the deep pushing airlock mechanism (a2) is fixedly connected with the upflow pressure mechanism (a 4).
2. An upflow deep-penetration pressure concentrator as in claim 1 in which: the depth pushing and air-cutting mechanism (a2) comprises a push claw (a21), a matching locking groove (a22), an air groove (a23), an air-cutting envelope (a24) and a discharging piece (a25), wherein the push claw (a21) is fixedly connected with the discharging piece (a25), the air groove (a23) is arranged in the middle of the push claw (a21), the air-cutting envelope (a24) and the push claw (a21) are of an integrated structure, and the matching locking groove (a22) is fixedly arranged on the left side and the right side of the push claw (a 21).
3. An upflow deep-penetration pressure concentrator as in claim 1 in which: the upflow and transcompression mechanism (a4) comprises a transcompression pipe (a41), a push-cut strip (a42), an outer ring sleeve (a43), a double-cut compression net (a44), a sealed air passage (a45) and a riser pipe (a46), wherein the riser pipe (a46) is installed inside the double-cut compression net (a44) in a penetrating mode, the push-cut strip (a42) is installed in the sealed air passage (a45) in an embedding mode, the outer ring sleeve (a43) is fixedly connected with the double-cut compression net (a44), and the transcompression pipe (a41) is welded with the double-cut compression net (a 44).
4. An upflow deep osmotic pressure concentrator as in claim 3 in which: the penetrating pressure pipe (a41) comprises a sleeve mechanism (a411), a sliding strip ring (a412), a traction belt (a413), a stretching and supporting piece (a414) and an elastic filter screen (a415), the sleeve mechanism (a411) is fixedly connected with the stretching and supporting piece (a414), the sliding strip ring (a412) is connected with the stretching and supporting piece (a414), the traction belt (a413) is arranged inside the stretching and supporting piece (a414), and the elastic filter screen (a415) is arranged on the side face of the stretching and supporting piece (a 414).
5. An upflow deep osmotic pressure concentrator as in claim 3 in which: the double-cutting compression net (a44) comprises a cutting strip (a441), an upper covering net (a442), a lower covering net (a443) and a pressing strip (a444), wherein the cutting strip (a441) and the upper covering net (a442) are of an integrated structure, the upper covering net (a442) and the lower covering net (a443) are movably connected together, and the pressing strip (a444) is installed between the upper covering net (a442) and the lower covering net (a443) in an embedded mode.
6. An up-flow deep osmotic pressure concentrator as defined in claim 4, wherein: the sleeve mechanism (a411) comprises a side sleeve piece (a11), a brush block (a12), a hanging piece (a13), a sleeving cover strip (a14), a folding sleeve (a15) and a side filter piece (a16), wherein the side filter piece (a16) is arranged inside the folding sleeve (a15), the brush block (a12) is arranged inside the side sleeve piece (a11), the hanging piece (a13) and the side sleeve piece (a11) are of an integrated structure, and the top end of the sleeving cover strip (a14) is connected with the hanging piece (a 13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911048611.2A CN110975371A (en) | 2019-10-31 | 2019-10-31 | Up-flow type deep penetration pressure thickener |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911048611.2A CN110975371A (en) | 2019-10-31 | 2019-10-31 | Up-flow type deep penetration pressure thickener |
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| CN110975371A true CN110975371A (en) | 2020-04-10 |
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| CN201911048611.2A Withdrawn CN110975371A (en) | 2019-10-31 | 2019-10-31 | Up-flow type deep penetration pressure thickener |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1572372A (en) * | 2003-06-20 | 2005-02-02 | 沃依特制纸专利有限责任公司 | Method and device for the flotation of contaminants from an aqueous fibrous suspension |
| WO2018041355A1 (en) * | 2016-09-01 | 2018-03-08 | Sca Hygiene Products Ab | Process and apparatus for wetlaying nonwovens |
| CN109487611A (en) * | 2018-12-28 | 2019-03-19 | 四川省犍为凤生纸业有限责任公司 | A kind of efficient paper pulp filter-pressing dehydration equipment |
| CN109555971A (en) * | 2019-01-15 | 2019-04-02 | 新乡市新平航空机械有限公司 | A kind of thickener pipe-line system and its control flow |
| CN109603255A (en) * | 2019-01-29 | 2019-04-12 | 南昌健峰矿机制造有限公司 | A kind of efficient positive-pressure filtering machine |
| CN109629306A (en) * | 2019-01-13 | 2019-04-16 | 新乡市新平航空机械有限公司 | A kind of upflow pressure thickener |
| CN209475698U (en) * | 2018-12-06 | 2019-10-11 | 徐宝海 | A kind of high-efficiency concentrator |
-
2019
- 2019-10-31 CN CN201911048611.2A patent/CN110975371A/en not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1572372A (en) * | 2003-06-20 | 2005-02-02 | 沃依特制纸专利有限责任公司 | Method and device for the flotation of contaminants from an aqueous fibrous suspension |
| WO2018041355A1 (en) * | 2016-09-01 | 2018-03-08 | Sca Hygiene Products Ab | Process and apparatus for wetlaying nonwovens |
| CN209475698U (en) * | 2018-12-06 | 2019-10-11 | 徐宝海 | A kind of high-efficiency concentrator |
| CN109487611A (en) * | 2018-12-28 | 2019-03-19 | 四川省犍为凤生纸业有限责任公司 | A kind of efficient paper pulp filter-pressing dehydration equipment |
| CN109629306A (en) * | 2019-01-13 | 2019-04-16 | 新乡市新平航空机械有限公司 | A kind of upflow pressure thickener |
| CN109555971A (en) * | 2019-01-15 | 2019-04-02 | 新乡市新平航空机械有限公司 | A kind of thickener pipe-line system and its control flow |
| CN109603255A (en) * | 2019-01-29 | 2019-04-12 | 南昌健峰矿机制造有限公司 | A kind of efficient positive-pressure filtering machine |
Non-Patent Citations (1)
| Title |
|---|
| 徐红霞: "升流式压力浓缩机", 《中华纸业》 * |
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Application publication date: 20200410 |