WO2019019762A1 - 织物、极板及烟气协同净化装置 - Google Patents

织物、极板及烟气协同净化装置 Download PDF

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Publication number
WO2019019762A1
WO2019019762A1 PCT/CN2018/085963 CN2018085963W WO2019019762A1 WO 2019019762 A1 WO2019019762 A1 WO 2019019762A1 CN 2018085963 W CN2018085963 W CN 2018085963W WO 2019019762 A1 WO2019019762 A1 WO 2019019762A1
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WIPO (PCT)
Prior art keywords
plate
flue gas
twill
water film
synergistic purification
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/CN2018/085963
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English (en)
French (fr)
Inventor
王树民
赵剑
张波
沈荣胜
袁莉莉
武锡平
张东海
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHINA ENERGY CONSERVATION AND EMISSION REDUCTION Co Ltd
China Energy Investment Corp Ltd
Shandong Shenhua Shanda Energy and Environment Co Ltd
Original Assignee
CHINA ENERGY CONSERVATION AND EMISSION REDUCTION Co Ltd
China Energy Investment Corp Ltd
Shandong Shenhua Shanda Energy and Environment Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from CN201710612842.6A external-priority patent/CN107520051B/zh
Priority claimed from CN201710763515.0A external-priority patent/CN107537691B/zh
Application filed by CHINA ENERGY CONSERVATION AND EMISSION REDUCTION Co Ltd, China Energy Investment Corp Ltd, Shandong Shenhua Shanda Energy and Environment Co Ltd filed Critical CHINA ENERGY CONSERVATION AND EMISSION REDUCTION Co Ltd
Priority to EP18837745.1A priority Critical patent/EP3659709A4/en
Publication of WO2019019762A1 publication Critical patent/WO2019019762A1/zh
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/08—Filter cloth, i.e. woven, knitted or interlaced material
    • B01D39/083—Filter cloth, i.e. woven, knitted or interlaced material of organic material
    • D—TEXTILES; PAPER
    • D03—WEAVING
    • D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
    • D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
    • D03D15/20—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads
    • D03D15/283—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads synthetic polymer-based, e.g. polyamide or polyester fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2055—Carbonaceous material
    • B01D39/2065—Carbonaceous material the material being fibrous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/16—Plant or installations having external electricity supply wet type
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34—Constructional details or accessories or operation thereof
    • B03C3/40—Electrode constructions
    • B03C3/45—Collecting-electrodes
    • B03C3/47—Collecting-electrodes flat, e.g. plates, discs, gratings
    • D—TEXTILES; PAPER
    • D03—WEAVING
    • D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
    • D03D1/00—Woven fabrics designed to make specified articles
    • D—TEXTILES; PAPER
    • D03—WEAVING
    • D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
    • D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
    • D—TEXTILES; PAPER
    • D03—WEAVING
    • D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
    • D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
    • D03D15/20—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads
    • D03D15/242—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads inorganic, e.g. basalt
    • D03D15/275—Carbon fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/02—Types of fibres, filaments or particles, self-supporting or supported materials
    • B01D2239/0241—Types of fibres, filaments or particles, self-supporting or supported materials comprising electrically conductive fibres or particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/0604—Arrangement of the fibres in the filtering material
    • B01D2239/0636—Two or more types of fibres present in the filter material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1216—Pore size
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1233—Fibre diameter

Definitions

  • the invention relates to the technical field of dust removing devices, in particular to a fabric, a pole plate and a flue gas synergistic purification device.
  • the wet electrostatic precipitator is generally treated with wet-saturated flue gas after wet desulfurization.
  • the particulate matter in the outlet flue gas reaches an "ultra-low" or even lower index.
  • the wet electrostatic precipitator of the flexible plate has the advantages of less flushing water consumption and no alkali consumption compared with the rigid electrode plate (glass fiber reinforced plastic or stainless steel) wet electrostatic precipitator.
  • the flexible plate is generally made of acid-resistant organic fiber material, and is usually woven by pure short wire, and the surface has a developed fluff structure.
  • the surface of the plate In the wet saturated flue gas environment, the surface of the plate is due to capillary wicking.
  • There is a layer of water film so that the plate has a certain self-cleaning function; at the same time, due to the water storage and water retention function of the fiber material, it keeps the wet state in the wet saturated flue gas environment for a long time, thus eliminating the need for continuous water supply conditions. Underneath, meet and maintain the necessary electrical conductivity requirements of the plates.
  • the organic fiber material is used for the anode cloth mentioned in the patent 201610819283.1.
  • the wet electrostatic precipitator is a new dust removal device for treating trace dust and micro particles. It is mainly used to remove harmful substances such as dust, acid mist, water droplets, aerosols, odor and PM2.5 in wet gas. It is the ideal equipment for controlling atmospheric dust pollution.
  • the wet type electrostatic precipitator is usually referred to as WESP. It is basically the same as the dust removal method of the dry type electrostatic precipitator. The dust is charged by the high voltage corona discharge, and the charged dust reaches the dust collecting plate/tube under the action of the electric field force. It has to go through three stages of charging, collecting and cleaning.
  • the wet electrostatic precipitator uses liquid to flush the surface of the dust collecting surface for cleaning, which can effectively collect fine particles (PM2.5 dust, SO3 acid mist, aerosol), heavy metals (Hg, As, Se, Pb, Cr) and organic pollution. (polycyclic aromatic hydrocarbons, dioxins) and the like.
  • the smoke emission in the wet flue gas can reach 10mg/m3 or even 5mg/m3.
  • the dust collection performance is independent of the dust characteristics. It is suitable for the treatment of wet flue gas, especially suitable for power plants and steel mills. After the desulfurization, the dusty flue gas is treated, but the equipment investment cost is high, and it needs to be used together with other dust removal equipments. The investment technical economy and operating cost should be evaluated from the whole.
  • the wet electrostatic precipitator (hereinafter referred to as “wet electricity”) is generally treated with wet-saturated flue gas after wet desulfurization. By reducing the acid mist and fine particulate matter in the flue gas, the particulate matter in the outlet flue gas reaches “super”. Low” or even lower indicators.
  • the wet electricity can be divided into the wet electricity of the flexible plate and the wet electricity of the rigid plate. As the wet electricity collecting pole, the plate is highly efficient and uniform, which directly affects the removal efficiency of the wet electricity.
  • the plate is generally made of fiber fabric, the fiber fabric is woven from the yarn, and the twill weave is used, and the surface of the fabric has a texture with a certain diagonal angle.
  • the adverse effect of this is: in the process of engineering application, the water flow on the surface of the plate flows under a certain angle of the flow of the texture. In the lower part of the plate, the water film is biased to the side of the plate, as shown in Fig. 1. It is difficult to form a water film covering the entire surface of the electrode plate, and the area covered by the waterless film forms dust accumulation, which affects the dust removal efficiency.
  • the surface of the plates is smoother and has no such texture.
  • water tends to form a "twig"-like channel on the surface of the plates, and it is also difficult to form a full surface of the plate. Water film.
  • the wet electrostatic precipitator is an environmental protection device for removing harmful substances such as droplets, aerosols and PM2.5 carried in wet flue gas, and is an ideal device for controlling dust pollution of flue gas.
  • wet electrostatic precipitators are increasingly used.
  • the wet electrostatic precipitator is divided into a rigid plate, a flexible plate and a FRP wet electrostatic precipitator according to the dust collecting plate.
  • the flexible wet electrostatic precipitator uses excellent organic fiber as the anode dust collecting plate, and the overall uniformity and operating cost of the “near zero water consumption” and “zero alkali consumption” water film in the process of treating the wet flue gas after desulfurization. Low, easy maintenance and many other advantages, widely used.
  • the flexible wet electrostatic precipitator is mainly composed of a cathode system and an anode system
  • the anode system is mainly composed of an anode upper and lower flower plate, a column, and a dust collecting plate (flexible plate).
  • the anode upper and lower flower plates function as a limit support column, and the column is used for fixing the flexible plate, such as the flexible wet electrostatic precipitator dust collecting plate fixing device and the flexible wet dust collector provided by the invention patent 201610819283.1.
  • the anode column of the flexible wet dust collector has certain incompatibility during use, has a long manufacturing cycle, consumes a large amount of manpower and material resources during installation, and considers transportation costs, resulting in an increase in economic costs.
  • the anode column occupies a small portion of the dust collecting plate space, and increases the cross-sectional area of the wet dust collector shell under the condition that the dust collecting pole area is constant, and the weight thereof is heavy, and the supporting frame and the supporting beam model are large, resulting in wet dust removal.
  • the amount of material required for the equipment increases, resulting in waste of materials, increased processing and manufacturing costs, and resulting in uneconomical overall construction.
  • the current flexible wet electrostatic precipitator anode column occupies a small part of the dust collecting plate space, high processing, installation, transportation costs, increased support material and support beam material, etc., resulting in uneconomical overall construction, the anode system structure needs urgent improvement .
  • the main object of the present invention is to provide a fabric, a plate and a flue gas synergistic purification device, which can solve the problem that the existing fiber fabric self-cleaning function of the flue gas synergistic purification device plate is not strong, the flushing water consumption is large, and a certain water retention must be relied upon. Rate to maintain problems such as its conductivity.
  • a wet electrostatic precipitator flexible fiber fabric which is obtained by mixing a filament and a short yarn, and the warp and the weft thread are used for the warp yarn, or
  • the warp yarn adopts the short yarn
  • the weft thread adopts the filament
  • the filament is a monofilament or a multifilament
  • the short filament is composed of a plurality of strands of yarn
  • the fiber breakage is formed by using the short yarn.
  • the flexible fiber woven fabric is a twill weave structure, and the woven density ranges from (300 to 400)*(100 to 200)/the number of the warp threads and the weft threads per 10 cm, and the weight per square meter of the fabric should be It is controlled at 700 to 1000 g and has a thickness of 0.9 to 1.2 mm.
  • the surface texture angle of the twill weave structure is 45 to 75 degrees.
  • a conductive carbon fiber yarn is used as a conductive material, and the carbon fiber yarn has a diameter of 1 to 3 K, and the carbon fiber yarn is combined with the filament or the short yarn.
  • the twist is added to increase the shear resistance and then woven, and the pitch between the carbon fiber yarns in the warp and weft directions is 1 to 5 cm.
  • the flexible fiber woven fabric is a plain weave structure, and the woven density is (300-400)*(80-150)/the number of the warp threads and the weft threads per 10 cm, and the weight per square meter is 600-900 g.
  • the thickness is 0.6 to 0.9 mm.
  • the warp and the weft of the flexible fiber fabric are made of one or a combination of polyester, polypropylene and nylon.
  • the filaments have a diameter of 200D to 2000D, and the filaments have a diameter of 200D to 2000D.
  • the single short yarn is composed of 2 to 10 yarns, and the single yarn has a diameter of 10 to 40.
  • a plate for achieving uniform water film comprising the flexible fiber fabric described.
  • the plate is composed of at least two plate regions, and the surface of any of the plate regions has a twill texture, and the twill texture on the surface of any of the plate regions is parallel to each other and the horizontal distance between the twill textures is equal;
  • the direction of the twill texture on the surface of the adjacent two plate regions is opposite, and the angle of the twill texture refers to the acute angle direction angle; wherein the angle of the twill texture is the angle between the twill texture and the direction of the weft.
  • angles of the twill textures on the surfaces of the adjacent two plate regions are equal.
  • the plates are spliced by a plate region having a corresponding twill texture, or the twill texture on the surface of the plate is made of a loom.
  • the length of the monolithic plate in the warp direction ranges from 3 to 9 m
  • the length in the weft direction ranges from 350 to 450 mm
  • the length of the surface of any of the plate regions in the warp direction ranges from 0.5 to 1.2 m
  • the twill texture The angle range is 45° to 70°, and the horizontal distance between the twill textures ranges from 0.1 to 1 mm.
  • a flue gas synergistic purification apparatus comprising the above-described electrode plate.
  • the flue gas synergistic purification device comprises four plates connected end to end, the flue gas synergistic purification device further comprises: a cross connector, and the adjacent two plates are connected by the cross a connector; a locker for fixedly connecting the cross connector and the plate together.
  • the side of the plate is provided with a first locking tooth
  • the four ends of the cross connector are respectively provided with a second locking tooth
  • the locking device is used for the first locking tooth and the first Two lock teeth lock.
  • the flue gas synergistic purification device further includes a fixing assembly for fixing the top end and the bottom end of the plate.
  • the fixing component comprises: a top plate and a first plate, an upper end of the plate is wound around the upper plate, and the first plate is pressed on both sides of the plate, the first fixing member Fixing the first plate and the plate on the upper flower plate; a lower plate and a second plate, the lower end of the plate abuts against the lower plate, and the second plate is pressed at The second fixing member fixes the second flat plate and the electrode plate on the lower flower plate.
  • the flue gas synergistic purification device further includes a casing, the casing enclosing a mounting cavity, the plate is installed in the mounting cavity, and the flue gas synergistic purification device further comprises The plate is pulled by a pulling device.
  • the pulling device further includes: a short plate, a first end of the short plate is connected with the cross connector; a third plate, the third plate is fixedly connected with the short plate;
  • the composite steel plate includes a first steel plate and a second steel plate, the first end of the first steel plate is for fixed connection with an inner wall of the mounting cavity, and the first end of the second steel plate is opposite to the first steel plate a second end vertically connected; a bending stud comprising a first stud segment and a second stud segment perpendicular to each other, the first stud segment and the second steel plate passing the first nut Removably coupled, the second stud segment is detachably coupled to the third plate by a second nut.
  • the first end of the short plate is provided with a third locking tooth, and the third locking tooth is engaged with the second locking tooth of the cross connector not connected to the plate, and passes the lock The lock is locked.
  • the locker, the first lock tooth, the second lock tooth and the third lock tooth are all made of polyester or stainless steel.
  • first plate and the second plate are both made of PP or FRP.
  • the bending stud and the combined steel plate are all made of duplex stainless steel 2205 material.
  • the warp and weft yarns are woven from a combination of filament and short yarn, which combines the advantages of filaments and short filaments, that is, the short filaments have a large amount of fibers.
  • Breakpoints (intuitively expressed as "fluff"), forming a large number of "storage space", thereby increasing the function of the fabric (plate) to maintain water in a wet saturated flue gas environment, which is beneficial to the plate to some extent. Maintain high electrical conductivity;
  • the invention utilizes the smooth surface characteristics of the filaments, so that the smoothness of the surface of the fabric (plate) is greatly improved compared with the pure short filaments, so that particles or dust are not easily adhered thereto, thereby increasing the self-cleaning of the fabric.
  • the addition of carbon fiber yarn in the weaving process further improves the electrical conductivity of the fiber fabric itself, and ensures the electric field characteristics of the plate in an abnormal state such as "waterless";
  • the invention ensures the strength, the surface tension, the uniformity of the water film and the like by controlling the thickness of the warp and weft, the weaving method, the grammage of the fabric, the thickness, the texture angle and the like, and can better eliminate the surface film from causing water film drift of the surface of the fabric. Increase the strength and maintain the tension and smoothness of the surface.
  • Figure 1 is a schematic view showing the formation of a conventional flexible plate water film
  • Figure 2 is a view schematically showing a warp, weft-twill flexible fiber fabric of the present invention
  • Figure 3 is a view schematically showing a warp and weft plain flexible fiber fabric of the present invention.
  • Figure 4 is a schematic view showing the structure of the short yarn of the present invention.
  • Figure 5 is a schematic view showing the structure of the flexible plate of the present invention.
  • Figure 6 is a schematic view showing the structure of a rigid plate of the present invention.
  • Figure 7 is a schematic plan view showing the cathode and anode structures of the present invention.
  • Figure 8 is a schematic elevational view of the anode structure of the present invention.
  • Figure 9 is a schematic front view showing the electrode plate of the present invention mounted on a fixture
  • Figure 10 is a schematic elevational view of the pulling device of the present invention.
  • Figure 11 is a schematic plan view of the pulling device of the present invention.
  • spatially relative terms such as “above”, “above”, “on top”, “above”, etc., may be used herein to describe as in the drawings.
  • the exemplary term “above” can include both “over” and "under”.
  • the device can also be positioned in other different ways (rotated 90 degrees or at other orientations) and the corresponding description of the space used herein is explained accordingly.
  • the present invention proposes a fabric, a plate and a flue gas synergistic purification device for a flue gas synergistic purification device.
  • the wet electrostatic dust-removing flexible fiber fabric is made of long and short filaments (or “long and short fibers"), that is, the warp threads are filaments, the weft yarns 2 are short filaments, or the warp threads 1 are short filaments, and the weft yarns 2 are filaments.
  • the filament is a monofilament or a multifilament, and the diameter of the woven filament is 200D to 2000D, preferably 800D to 1500D;
  • the diameter of the short yarn is 200D to 2000D, preferably 800D to 1500D
  • the single short yarn is composed of 2 to 10 yarns, preferably 4 to 8 yarns, and the diameter of the single yarn is 10 to 40. 15 to 25.
  • the flexible fiber fabric is woven with a warp 1 and weft 2 plain weave or twill weave.
  • the fabric is not distinguished from the front and back, it is advantageous to use 2/2 to 6/6 weave, preferably 2/2, 4/4 weave; since in normal working condition, the fabric as the plate should have A certain strength to maintain the tension and flatness of the surface, the weaving density is about (300 ⁇ 400) * (100 ⁇ 200) (the number of warp 1 and weft 2 per 10cm), the weight per square meter of the fabric should be controlled at 700 ⁇ 1000g, thickness is 0.9-1.2mm.
  • the surface texture angle (the angle between the grain and the horizontal direction) should be controlled to be 45 to 75 degrees, preferably 45 to 60 degrees.
  • the fabric used as the plate should have a certain strength to maintain the tension and flatness of the surface, and the weaving density is about (300 ⁇ 400) * (80 ⁇ 150) (per The number of 10 cm warp 1 and weft 2) is 600 to 900 g per square meter and the thickness is 0.6 to 0.9 mm.
  • the warp yarn 1 and the weft yarn 2 of the flexible fiber fabric are made of one or a combination of polyester, polypropylene, and nylon.
  • the warp 1 and the weft 2 are made of polyester.
  • the electrode plate and the flue gas synergistic purification device for realizing uniform water film use the above-mentioned flexible fiber fabric as a dust removing cloth.
  • a flexible fiber fabric which is woven from warp 1 and weft 2, warp yarn 1 is made of polyester filament, and weft 2 is made of polyester staple yarn;
  • the filament is a multifilament with a diameter of 1500 D; the diameter of the staple is 1500 D, as shown in Fig. 3, consisting of 5 strands of yarn 3 strands, and the diameter of the single strand yarn 3 is 25.
  • the flexible fiber fabric is woven with a warp and weft 2/2 twill weave.
  • the fabric as the plate should have a certain strength to maintain the tension and flatness of the surface, and the woven density is adjusted to 300*100, so that the weight of the fabric per square meter is about 850g and the thickness is about 1.0mm.
  • the surface texture angle ⁇ (the angle between the grain and the horizontal direction) should be controlled to be 50 degrees.
  • the electrode plate of the flue gas synergistic purification device utilizes the above-mentioned wet electrostatic precipitator flexible fiber fabric as an anode cloth.
  • the warp 1 and the weft 2 are woven, the warp 1 is made of polyester filament, the weft 2 is made of polyester staple; the filament is multifilament, and the diameter is It is 1300D; the short wire diameter is 1000D, consisting of 5 strands of yarn 3 strands, and the single strand yarn 3 has 20 diameters.
  • the flexible fiber fabric is woven with warp and weft plain weave (1/1 weave).
  • the fabric as the plate should have a certain strength to maintain the tension and flatness of the surface, and adjust the woven density to 350*90, so that the weight per square meter is about 700g and the thickness is about 0.8mm.
  • the electrode plate of the flue gas synergistic purification device uses the wet electrostatic precipitator flexible fiber fabric in the exemplary embodiment as the anode cloth.
  • the embodiment of the present invention in order to solve the problem that the water film uniformity effect of the wet electrode plate described in the background is not good and the flushing water consumption is large, the embodiment of the present invention provides a pole for realizing uniformity of the water film. board.
  • An electrode plate for realizing water film uniformity is composed of at least two plate regions, and any one of the plate regions has a twill texture on the surface thereof, and the twill texture on the surface of any of the plate regions is parallel to each other. And the horizontal distance between the twill textures is equal; the direction of the twill texture on the surface of the adjacent two plate regions is opposite, and the angle of the twill texture refers to the angle of the acute angle direction; wherein the angle of the twill texture is the angle between the twill texture and the weft direction .
  • angles of the twill texture on the surfaces of adjacent two plate regions are equal.
  • angles of the twill textures on the surfaces of the adjacent two plate regions are set to be equal angles, which can ensure that the water film has the same flow velocity and direction on the surface of each plate region, which is favorable for the water film in each plate region. Uniform distribution of the surface.
  • the plate is made of the above-mentioned flexible fiber fabric:
  • the plate is woven by the warp 1 and the weft 2, and in the warp direction, the twill texture is presented in an alternating manner of left and right oblique or right and left oblique.
  • the flexible plates are formed by splicing the plate regions having the corresponding twill texture, or the twill texture on the surface of the flexible plates is made of a loom.
  • the twill texture alternates in the left and right direction of the plate region, and can be realized by setting the parameters of the loom, or by performing post-processing such as cutting, splicing, and the like on the fabric.
  • the warp direction is inclined to the left/right direction within a distance d 11 from the top end of the plate, and the angle between the twill and the weft is ⁇ 11 (an acute angle direction);
  • the twill In the surface of the second plate region, within the length distance d 12 along the warp direction, the twill is changed to the right/left oblique direction, and the angle between the twill and the weft is ⁇ 12 (an acute angle direction), in the direction of the length of the plate Left and right oblique or right and left oblique repeats.
  • the length d 14 of the monolithic flexible plate in the warp direction ranges from 3 to 9 m, preferably from 5.5 to 7.5 m; and the length in the weft direction is d 15 .
  • the range is 350 ⁇ 450mm:
  • the length d 11 of the surface of the first plate region in the warp direction ranges from 0.5 to 1.2 m, and the length d 12 of the surface of the second plate region in the warp direction ranges from 0.5 to 1.2 m;
  • the angle ⁇ 11 of the twill texture in the surface of the first plate region ranges from 45° to 70°, and the angle ⁇ 12 of the twill texture in the surface of the second plate region is also in the range of 45° to 70°.
  • the horizontal distance d 13 between the twill textures in the first plate region and the second plate region ranges from 0.1 to 1 mm. Among them, the horizontal distance d13 between the twill textures preferably ranges from 0.2 to 0.5 mm.
  • the horizontal distance d 13 between the textures is 0.2 mm.
  • the parameters of the above flexible plate are based on the nature of the flue gas and the concentration requirements of the flue gas synergistic purification device, which can minimize the occurrence of water film bias current and ensure that water film exists on more than 90% of the surface of the flexible plate. Guarantee the removal effect of water film on the ash on the plate.
  • the invention is directed to a flexible plate, and the stripe texture is presented in an alternating manner of left/right or right/left, avoiding the phenomenon of biasing caused by a single texture direction;
  • the invention realizes the uniform distribution of the water film on the electrode plate under the condition of less water distribution by the change of the surface structure of the wet electrode plate, on the one hand, the effect of cleaning the dust can be improved, and on the other hand, the large water volume flushing is avoided. The amount of wastewater generated is greatly reduced.
  • the twill texture on the surface of the rigid plate is machined or die drawn.
  • the rigid plates can be realized by FRP or stainless steel.
  • the twill texture alternates in the left and right direction of the plate region, and can be processed by a numerical control machine such as a milling machine; when it is a FRP, the twill texture alternates in the left and right direction of the plate region, and can be realized by pultrusion of the mold parameters.
  • the heights of the twill textures in all of the plate regions are equal.
  • the heights of the twill textures in all the plate regions are set to be equal, which ensures that the water film has the same flow velocity and direction on the surface of each plate region, which is favorable for the uniform distribution of the water film on the surface of each plate region.
  • the surface of the rigid plate is provided with a convex stripe having a certain inclination angle, and the texture of the stripe is presented in an alternating manner of left and right oblique or right and left oblique.
  • the length d 24 of the single rigid plate in the warp direction ranges from 4 to 8 m.
  • the preferred length d 24 of the monolithic rigid plate in the warp direction ranges from 5 to 7 m;
  • the length d 21 of the surface of the first plate region in the warp direction ranges from 1 to 2 m
  • the length d 21 of the surface of the second plate region in the warp direction also ranges from 1 to 2 m
  • the twill texture in the surface of the first plate region is
  • the angle ⁇ 21 is 45° to 75°
  • the angle ⁇ 22 of the twill texture in the surface of the second plate region is also 45° to 75°.
  • the horizontal distance d 23 between the twill textures in the first plate region and the second plate region ranges from 0.1 to 1 mm, preferably from 0.2 to 0.5 mm.
  • the raised height d 25 of the twill texture in the first plate region and the second plate region ranges from 0.05 to 0.2 mm.
  • the parameters of the above rigid plate are based on the nature of the flue gas and the concentration requirements of the flue gas synergistic purification device outlet particles, which can minimize the occurrence of water film bias flow and ensure that water film exists in more than 90% of the surface of the rigid plate. Guarantee the removal effect of water film on the ash on the plate.
  • the alternating strips in the left and right directions are added on the surface, which can also guide the water film on the surface, effectively avoiding the occurrence of "twig"-like bias current.
  • the invention realizes the uniform distribution of the water film on the electrode plate under the condition of less water distribution by the change of the surface structure of the wet electrode plate, on the one hand, the effect of cleaning the dust can be improved, and on the other hand, the large water volume flushing is avoided. The amount of wastewater generated is greatly reduced.
  • the present invention is directed to a plate, and the stripe texture is presented in an alternating left/right or right/left manner, avoiding a phenomenon of a biasing phenomenon caused by a single grain direction; for a rigid plate, an alternating left and right direction is added to the surface thereof.
  • the stripe can also guide the water film on the surface, effectively avoiding the occurrence of "twig"-like bias current.
  • the invention realizes the uniform distribution of the water film on the electrode plate under the condition of less water distribution by the change of the surface structure of the wet electrode plate, on the one hand, the effect of cleaning the dust can be improved, and on the other hand, the large water volume is avoided. Flushing reduces the amount of wastewater generated to a large extent.
  • an embodiment of the present invention further provides a smoke gas synergistic purification device.
  • the flue gas synergistic purification device comprises two structural forms, wherein:
  • the first type of flue gas synergistic purification device comprises a plate for achieving a uniform distribution of water film as shown in FIG.
  • the second flue gas synergistic purification device comprises a plate for achieving uniform water film as shown in FIG. 6.
  • the invention realizes the uniform distribution of the water film on the electrode plate under the condition of less water distribution by the change of the surface structure of the wet electrode plate, on the one hand, the effect of cleaning the dust can be improved, and on the other hand, the large water volume flushing is avoided. The amount of wastewater generated is greatly reduced.
  • the flue gas synergistic purification device in the embodiment includes four end plates 10 connected end to end, and the flue gas synergistic purification device further comprises a cross connector 20 and a lock 30, wherein two adjacent poles The plates 10 are connected by a cross connector 20; the lock 30 is used to securely connect the cross connector 20 and the plate 10.
  • the two connecting plates 10 are connected together by the cross connector 20 and the locker 30.
  • the weight of the anode system is greatly reduced, and resources are saved. It avoids pollution to the environment when processing the column, which is economical and environmentally friendly.
  • the side of the electrode plate 10 in this embodiment is provided with a first locking tooth, and the four ends of the cross connector 20 are respectively provided with a second locking tooth, and the lock 30 is used for the first locking tooth of the cross connector 20 and The second locking gear is locked, and the two adjacent plates 10 are connected together.
  • the flue gas synergistic purification apparatus in this embodiment further includes a fixing assembly for fixing the top end and the bottom end of the electrode plate 10.
  • the fixing assembly in this embodiment includes an upper flower plate 41, a first flat plate 42, a lower flower plate 43, and a second flat plate 44.
  • the first plate 42 is wound on the upper plate 10, and the first plate 42 and the plate 10 are fixed on the upper plate 41 by the first fixing member 45;
  • the lower end of the plate 10 abuts against the lower plate 43 , and the second plate 44 is pressed against the lower end of the plate 10 , and the second plate 44 and the plate 10 are fixed to the lower plate 43 by the second fixing member 46 , and the structure is simple. It is convenient to stably fix the upper and lower ends of the electrode plate 10.
  • the flue gas synergistic purification apparatus in this embodiment further includes a casing (not shown), the casing enclosing a mounting cavity, and the pole plate 10 is installed in the installation cavity, and the flue gas is synergistically purified.
  • the device also includes a pulling device 50 for pulling the plate 10.
  • the pulling device 50 further includes a short plate 51, a third flat plate 52, a combined steel plate 53, and a bending stud 54.
  • the first end of the short plate 51 is connected to the cross connector 20; the third plate 52 is fixedly connected to the short plate 51; the combined steel plate 53 includes a first steel plate 531 and a second steel plate 532, and the first end of the first steel plate 531 is used.
  • the first end of the second steel plate 532 is perpendicularly connected to the second end of the first steel plate 531; the bending stud 54 includes a first stud segment 541 and a second stud segment that are perpendicular to each other.
  • the first stud segment 541 and the second steel plate 532 are detachably connected by the first nut 55, and the second stud segment 542 and the third flat plate 52 are detachably connected by the second nut 56, so as to facilitate the plate 10 Pulling.
  • the first end of the short plate 51 is provided with a third locking tooth which meshes with the second locking tooth of the cross connector 20 which is not connected to the electrode plate 10 and is locked by the lock 30.
  • the structure is simple, and it is convenient to pull the plate 10.
  • the flue gas synergistic purification device in the embodiment includes a cross connector 20, and the cross connector 20 functions as a substitute for the column.
  • the four ends of the cross connector 20 are provided with a second lock tooth.
  • the side of the plate 10 is provided with a first locking tooth, and the cross connector 20 is matched with a pole plate 10, and the electrode plate 10 is composed of a flexible anode cloth and first locking teeth provided at the left and right ends thereof, the cross connector 20 and
  • the plate 10 is integrally connected by the locker 30.
  • the upper end of the plate 10 is wound around the anode upper plate 41.
  • the first plate 42 is distributed on both sides of the upper end of the plate 10, and the first plate 42 and the pole are passed through the first fixing member 45.
  • the plate 10, the upper plate 41, the electrode plate 10, and the first flat plate 42 are sequentially connected and fixed.
  • the lower end of the plate 10 is flush with the bottom end of the lower plate 43 , and the second plate 44 is disposed on the side of the plate 10 , and the second plate 44 , the plate 10 , and the lower plate 43 are sequentially connected and fixed by the second fixing member 46 .
  • the frame of the upper plate 41 and the lower plate 43 are fixed on the upper and lower support beams.
  • a cross connector 20 is disposed at each corner of each square hole, and a plate 10 is disposed between two adjacent cross connectors 20.
  • the wet scrubber anode system designed according to specific parameters is composed of a plurality of square holes.
  • the cross-member peripheral cross member 20 is provided with a pulling device 50.
  • the pulling device 50 is disposed between the cross connector 20 and the inner wall adjacent to the inner wall of the mounting cavity, and includes a short plate 51 of a certain height, and the plate 10 is connected with the cross.
  • the connecting end of the member 20 is provided with a third locking tooth, and the short plate 51 is connected to the cross connecting member 20 through the lock 30, and the third plate 52 is disposed on the other side of the short plate 51, and the third flat plate 52 is in the short plate 51 and The winding is performed twice, and the short plate 51 and the third flat plate 52 are joined by fasteners.
  • the third flat plate 52 is provided with two round holes on the upper and lower sides, and the bending stud 54 is inserted through the circular hole.
  • the end of the bending stud 54 is inserted into the adjusting hole of the combined steel plate 53 connected to the third flat plate 52, and the first nut 55 is used.
  • the second nut 56 adjusts the tension of the bending stud 54 .
  • the peripheral cross connector 20 is connected to the inner wall side and is provided with a plurality of pulling devices 50 , thereby controlling the flatness of the electrode plate 10 and keeping the electrode plate 10 and the discharge electrode 60 A certain distance to ensure dust removal efficiency.
  • the lock 30, the first lock tooth, the second lock tooth and the third lock tooth are all corrosion-resistant materials such as polyester or stainless steel, and the first plate 42 and the second plate 44 are both corrosion-resistant materials such as PP or FRP.
  • the curved stud 54 and the combined steel plate 53 are made of duplex stainless steel 2205, so that the pulling device 50 is a rigid member, ensuring the square hole pitch of the plate 10, avoiding frequent flashover of the voltage, breakdown of the plate 10, affecting dust removal efficiency and the like. .
  • the cross connector provided by the invention replaces the flexible wet electrostatic precipitator plate fixing device and the column in the flexible wet dust collector, the anode system is greatly reduced in weight, saves resources, and avoids environmental pollution when processing the column, which is economical and environmentally friendly.
  • the upper and lower anode frames and support beams for supporting the columns and plates are greatly reduced in size, saving processing, transportation and installation costs, saving steel and ensuring rational use of energy.
  • the elimination of the anode column increases the available area of the electrode plate, and the volume of the wet dust collector can be reduced under the premise of equal efficiency, avoiding waste and saving cost.
  • the pulling device connects the short plate side with the cross connector, the other side of the short plate is wound with the rigid third plate, and is connected by a fastener, and the third part embedded in the short plate is bent by the stud.
  • the flat plate is connected, and the end of the bent stud is moved into the adjusting plate of the combined steel plate welded with the casing to ensure that the bending stud moves the space up and down and left and right, thereby providing maximum adjustment margin.
  • the pulling device is a rigid member, which controls the flatness of the electrode plate (flexible plate), ensures the discharge interval between the anode and the cathode, and avoids the phenomenon of voltage flashover, plate breakdown, and dust removal efficiency.
  • the anode column can be eliminated, the anode flexible plate can be quickly installed, the weight of the support frame and the support beam is obviously reduced, the volume of the wet dust collector is reduced, the investment is saved, the utilization rate of the electrode plate is improved, and the dust removal efficiency is improved.

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Abstract

一种织物、极板及烟气协同净化装置，湿式静电除尘柔性纤维织物由长丝和短丝混织而成，经线（1）采用长丝、纬线（2）采用短丝，或经线（1）采用短丝、纬线（2）采用长丝，长丝为单丝或复丝，短丝为若干股纱线合股组成，利用短丝的纤维断点形成多个储水空间，以实现织物的持水性。在保持纤维织物作为极板功能的基础上极大改善了原有纤维织物性能，可以解决烟气协同净化装置的极板的现有纤维织物自清洁功能不强，冲洗耗水量大等问题。

Description

织物、极板及烟气协同净化装置 技术领域
本发明涉及除尘装置技术领域，具体而言，涉及一种织物、极板及烟气协同净化装置。
背景技术
湿式静电除尘器的处理对象一般为经过湿法脱硫后湿饱和烟气，通过降低烟气中的酸雾滴、细颗粒物含量，使出口烟气中颗粒物达到“超低”、甚至更低指标。
柔性极板的湿式静电除尘器与刚性极板(玻璃钢或不锈钢)湿式静电除尘器相比，具有冲洗水耗量少，无碱耗等突出优势。原因在于柔性极板一般为耐酸有机纤维材料制成，且通常采用纯短丝机织而成，其表面具有发达的绒毛结构，在湿饱和烟气环境中，由于毛细芯吸作用，极板表面有一层水膜，从而使极板具备一定的自清洁功能；同时，由于纤维材料的蓄水、保水功能，使其在湿饱和烟气环境中长时间保持潮湿状态，从而无需持续布水的条件下，达到并保持极板必需的一定的导电性的要求。专利201610819283.1提及的阳极布采用的就是此种有机纤维材料。
然而，由于传统柔性纤维均采用纯短丝机织，表面较粗糙，颗粒物或粉尘与极板的粘附力较强，颗粒物或粉尘需要较大的水量、较快的水速方可以冲洗下来，随着国家对燃煤电站颗粒物排放指标日益严格，以及为了适应更加复杂的工业烟气净化要求，同时减少冲洗水耗水量，柔性极板的自清洁功能及导电功能需要进一步提升，以防止有积灰及其进而引发的反电晕现象的产生，从而影响除尘效率。
此外，近年来，随着污染物“超低排放”改造在全国的开展，湿式电除尘器被广泛推广和应用。湿式电除尘器是一种用来处理含微量粉尘和微颗粒的新除尘设备，主要用来除去含湿气体中的尘、酸雾、水滴、气溶胶、臭味、PM2.5等有害物质，是治理大气粉尘污染的理想设备。湿式电除尘器通常简称WESP，与干式电除尘器的除尘基本原理相同，都是靠高压电晕放电使得粉尘荷电，荷电后的粉尘在电场力的作用下到达集尘板/管，要经历荷电、收集和清灰三个阶段。湿式电除尘器采用液体冲刷集尘极表面来进行清灰，可有效收集微细颗粒物(PM2.5粉尘、SO3酸雾、气溶胶)、重金属(Hg、As、Se、Pb、Cr)、有机污染物(多环芳烃、二噁英)等。使用湿式电除尘器后含湿烟气中的烟尘排放可达10mg/m3甚至5mg/m3以下，收尘性能与粉尘特性无关，适用于含湿烟气的处理，尤其适用在电厂、钢厂湿法脱硫之后含尘烟气的处理上，但设备投资费用较高，且需与其它除尘设备配套使用，其投资技术经济性和运行成本要从整体进行评价。
湿式静电除尘器(以下简称“湿电”)的处理对象一般为经过湿法脱硫后湿饱和烟气，通过降低烟气中的酸雾滴、细颗粒物含量，使出口烟气中颗粒物达到“超低”、甚至更低指标。 按照阳极收尘极板的形式不同，湿电可分为柔性极板湿电与刚性极板湿电。极板作为湿电集尘极，其上水膜是否高效均布直接影响湿电对颗粒物的去除效率。
对于柔性极板而言，极板一般选用纤维织物，纤维织物由纱线机织而成，且多采用斜纹织，织物表面呈现具有一定斜纹角度的纹理。这产生的不利影响为：在工程应用过程中，极板表面的水流在纹理的导流作用下按照一定的角度流动，在极板下半部分，水膜偏向极板一侧，如图1所示，较难形成覆盖极板全表面的水膜，无水膜覆盖的区域形成积灰，影响除尘效率。
对于刚性极板而言，极板表面较光滑，无上述纹理结构，然而，由于缺乏导流作用，水在极板表面易形成“枝丫”状的沟流，同样较难形成覆盖极板全表面的水膜。
由于上述两种极板存在的表面物理特性，在实际工程中均需要较大的冲洗水量方可以形成覆盖全表面的水膜以完成清灰，这增加了湿电的耗水量及其相关的电耗、碱耗等。为了适应更加复杂的、颗粒物进口浓度变化大的烟气净化要求，亟需一种极板，来减少冲洗水耗水量，实现小水量布水条件下水膜均布，进而确保高效除尘效率。
湿式电除尘器是一种用来去除湿烟气中携带的液滴、气溶胶、PM2.5等有害物质的环保设备，是治理烟气粉尘污染的理想设备。随着火电厂、炼钢厂等达到超低排放标准及节能改造，湿式电除尘器应用日益广泛。湿式电除尘器按收尘极板分为刚性极板、柔性极板及玻璃钢湿式电除尘器。其中，柔性湿式电除尘器采用优良的有机纤维作为阳极收尘极板，在处理脱硫后湿烟气过程中“近零水耗”、“零碱耗”水膜整体均布性好、运行费用低、检修维护方便等诸多优势，应用广泛。
目前，柔性湿式电除尘器主要由阴极系统、阳极系统组成，而阳极系统又主要由阳极上下花板、立柱、收尘极板(柔性极板)等组成。阳极上下花板起限位支撑立柱的作用，立柱是用来固定柔性极板的，如发明专利201610819283.1提供的柔性湿式电除尘器收尘极板固定装置及柔性湿式除尘器。然而，该类柔性湿式除尘器的阳极立柱在使用过程中存在一定的不适应性，加工制造周期长，安装时消耗大量的人力、物力，并考虑运输费用，导致经济成本增加。
同时，阳极立柱占用小部分收尘极板的空间，在收尘极面积不变的情况下增加湿式除尘器壳体横截面积，且自身重量重，支撑框架及支撑梁型号大，致使湿式除尘器设备所需材料量增加，造成材料的浪费，加工制造及安装费用增加，造成总体建设不经济等现象。
综上，目前的柔性湿式电除尘器阳极立柱占用小部分收尘极板空间，加工制造、安装、运输费用高，支撑框架及支撑梁材料量增加等造成总体建设不经济，阳极系统结构急需改进。
发明内容
本发明的主要目的在于提供一种织物、极板及烟气协同净化装置，以解决烟气协同净化装置极板的现有纤维织物自清洁功能不强、冲洗耗水量大、必须依靠一定的保水率以保持其导电性能等问题。
为了实现上述目的，根据本发明的一个方面，提供了一种湿式静电除尘柔性纤维织物，由长丝和短丝混织而成，经线采用所述长丝、纬线采用所述短丝，或所述经线采用所述短丝、所述纬线采用所述长丝，所述长丝为单丝或复丝，所述短丝为若干股纱线合股组成，利用所述短丝的纤维断点形成多个储水空间，以实现织物的持水性。
进一步地，所述柔性纤维织物为斜纹机织结构，机织密度范围为(300～400)*(100～200)/每10cm所述经线和所述纬线的根数，织物每平方米重量应控制在700～1000g，厚度为0.9～1.2mm。
进一步地，所述斜纹机织结构的表面纹理角度为45～75度。
进一步地，采用导电碳纤维纱线作为导电材料间隔混织于所述柔性纤维织物中，所述碳纤维纱线的直径为1～3K，所述碳纤维纱线与所述长丝或所述短丝复合加捻以增加抗剪能力然后进行机织，在经、纬向所述碳纤维纱线之间的间距为1～5cm。
进一步地，所述柔性纤维织物为平纹机织结构，机织密度为(300～400)*(80～150)/每10cm所述经线和所述纬线的根数，每平方米重量600～900g，厚度为0.6～0.9mm。
进一步地，所述柔性纤维织物的所述经线、所述纬线的材质为涤纶、丙纶和锦纶中一种或几种组合。
进一步地，所述长丝直径为200D到2000D，所述短丝直径为200D到2000D。
进一步地，单根所述短丝由2～10股纱线合股组成，单股纱的直径为10～40支。
根据本发明的另一方面，提供了一种实现水膜均布的极板，所述极板包括述的柔性纤维织物作。
进一步地，所述极板由至少两个极板区域构成，任一极板区域表面上均有斜纹纹理，任一极板区域表面上的斜纹纹理相互平行且斜纹纹理之间水平距离相等；相邻的两个极板区域表面上斜纹纹理的方向相反，斜纹纹理的角度均指锐角方向角度；其中，斜纹纹理的角度为斜纹纹理与所述纬线方向的夹角。
进一步地，相邻的两个极板区域表面上斜纹纹理的角度相等。
进一步地，在每个极板区域内，斜纹纹理的角度越大，沿经线方向的距离越大，斜纹纹理之间水平距离越小，水膜偏流越严重。
进一步地，所述极板由具有相应斜纹纹理的极板区域拼接而成，或所述极板表面上的斜纹纹理由织机制成。
进一步地，单块极板沿经线方向的长度范围为3～9m，沿纬线方向的长度范围为350～450mm时，任一极板区域表面沿经线方向的长度范围为0.5～1.2m，斜纹纹理的角度范围为45°～70°，斜纹纹理之间水平距离范围为0.1～1mm。
根据本发明的再一方面，提供了一种烟气协同净化装置，所述烟气协同净化装置包括上述的极板。
进一步地，所述烟气协同净化装置包括四块首尾相连的所述极板，所述烟气协同净化装置还包括：十字连接件，相邻两块所述极板之间通过所述十字连接件连接；锁合器，所述锁合器用于将所述十字连接件和所述极板固定连接在一起。
进一步地，所述极板的侧边设置有第一锁齿，所述十字连接件的四端均设置有第二锁齿，所述锁合器用于将所述第一锁齿和所述第二锁齿锁合。
进一步地，所述烟气协同净化装置还包括固定组件，所述固定组件用于将所述极板的顶端和底端固定。
进一步地，所述固定组件包括：上花板和第一平板，所述极板的上端缠绕在所述上花板，所述第一平板压设在所述极板两侧，第一固定件将所述第一平板及极板固定在所述上花板上；下花板和第二平板，所述极板的下端贴靠在所述下花板上，所述第二平板压设在所述极板上，第二固定件将所述第二平板及极板固定在所述下花板上。
进一步地，所述烟气协同净化装置还包括外壳，所述外壳围设形成安装腔，所述极板安装在所述安装腔内，所述烟气协同净化装置还包括用于对所述极板进行牵拉的牵拉装置。
进一步地，所述牵拉装置还包括：短板，所述短板的第一端与所述十字连接件连接；第三平板，所述第三平板与所述短板固定连接；组合钢板，所述组合钢板包括第一钢板和第二钢板，所述第一钢板的第一端用于与所述安装腔的内壁固定连接，所述第二钢板的第一端与所述第一钢板的第二端垂直连接；折弯螺柱，所述折弯螺柱包括相互垂直的第一螺柱段和第二螺柱段，所述第一螺柱段与所述第二钢板通过第一螺母可拆卸地连接，所述第二螺柱段与所述第三平板通过第二螺母可拆卸地连接。
进一步地，所述短板的第一端设置有第三锁齿，所述第三锁齿与所述十字连接件的未与所述极板连接的第二锁齿啮合，并通过所述锁合器锁合。
进一步地，所述锁合器、所述第一锁齿、所述第二锁齿以及所述第三锁齿均为采用聚酯或不锈钢制作而成。
进一步地，所述第一平板、所述第二平板均采用PP或FRP制作而成。
进一步地，所述折弯螺柱及所述组合钢板均采用双相不锈钢2205材质制作而成。
与现有技术相比，本发明的有益效果为：
针对于纯短纤机织而成的柔性纤维织物，经线与纬线采用长丝与短丝相结合机织而成的织物集合了长丝与短丝的优点，即短丝由于存在大量的纤维“断点”(直观表现为“绒毛”)，形成大量“储水小空间”，从而增加了织物(极板)在湿饱和烟气环境下保持水的功能，这在一定程度上有利于极板保持较高的导电性能；
本发明利用长丝表面光滑的特性，使得织物(极板)表面的光洁程度较纯短丝有了很大程度上提高，使颗粒物或灰尘不易粘附在其上，从而增加了织物的自清洁功能；同时，机织过程中添加碳纤维纱线，进一步提高了纤维织物自身的导电性能，确保了极板在“无水”等非正常状态下的电场特性；
本发明通过控制经纬线的粗细、织法、织物的克重、厚度、纹理角度等因素保证其强度、表面张力、水膜均布等要求，能够更好的消除表面纹理造成织物表面水膜偏流，提高强度、维持表面的张力与平整。
附图说明
构成本申请的一部分的说明书附图用来提供对本发明的进一步理解，本发明的示意性实施例及其说明用于解释本发明，并不构成对本发明的不当限定。在附图中：
图1示意性示出了传统的柔性极板水膜形成示意图；
图2示意性示出了本发明的经线、纬线斜纹的柔性纤维织物的图；
图3示意性示出了本发明经线、纬线平纹的柔性纤维织物图；
图4示意性示出了本发明的短丝结构示意图；
图5示意性示出了本发明的柔性极板结构示意图；
图6示意性示出了本发明的刚性极板结构示意图；
图7示意性示出了本发明的阴、阳极结构俯视图；
图8示意性示出了本发明的阳极结构的正视图；
图9示意性示出了本发明的极板安装在固定装置上时的主视图；
图10示意性示出了本发明的牵拉装置的正视图；
图11示意性示出了本发明的牵拉装置的俯视图。
其中，上述附图包括以下附图标记：
1、经线；2、纬线；10、极板；20、十字连接件；30、锁合器；41、上花板；42、第一平板；43、下花板；44、第二平板；45、第一固定件；46、第二固定件；50、牵拉装置；51、 短板；52、第三平板；53、组合钢板；531、第一钢板；532、第二钢板；54、折弯螺柱；541、第一螺柱段；542、第二螺柱段；55、第一螺母；56、第二螺母；60、放电极。
具体实施方式
需要说明的是，在不冲突的情况下，本申请中的实施例及实施例中的特征可以相互组合。下面将参考附图并结合实施例来详细说明本发明。
需要注意的是，这里所使用的术语仅是为了描述具体实施方式，而非意图限制根据本申请的示例性实施方式。如在这里所使用的，除非上下文另外明确指出，否则单数形式也意图包括复数形式，此外，还应当理解的是，当在本说明书中使用术语“包含”和/或“包括”时，其指明存在特征、步骤、操作、器件、组件和/或它们的组合。
需要说明的是，本申请的说明书和权利要求书及上述附图中的术语“第一”、“第二”等是用于区别类似的对象，而不必用于描述特定的顺序或先后次序。应该理解这样使用的数据在适当情况下可以互换，以便这里描述的本申请的实施方式例如能够以除了在这里图示或描述的那些以外的顺序实施。此外，术语“包括”和“具有”以及他们的任何变形，意图在于覆盖不排他的包含，例如，包含了一系列步骤或单元的过程、方法、系统、产品或设备不必限于清楚地列出的那些步骤或单元，而是可包括没有清楚地列出的或对于这些过程、方法、产品或设备固有的其它步骤或单元。
为了便于描述，在这里可以使用空间相对术语，如“在……之上”、“在……上方”、“在……上表面”、“上面的”等，用来描述如在图中所示的一个器件或特征与其他器件或特征的空间位置关系。应当理解的是，空间相对术语旨在包含除了器件在图中所描述的方位之外的在使用或操作中的不同方位。例如，如果附图中的器件被倒置，则描述为“在其他器件或构造上方”或“在其他器件或构造之上”的器件之后将被定位为“在其他器件或构造下方”或“在其他器件或构造之下”。因而，示例性术语“在……上方”可以包括“在……上方”和“在……下方”两种方位。该器件也可以其他不同方式定位(旋转90度或处于其他方位)，并且对这里所使用的空间相对描述作出相应解释。
正如背景技术所介绍的，现有技术中存在柔性纤维均采用纯短丝机织，表面较粗糙，颗粒物或粉尘与极板的粘附力较强，颗粒物或粉尘需要较大的水量、较快的水速方可以冲洗下来的不足，为了解决如上的技术问题，本发明提出了一种烟气协同净化装置织物、极板及烟气协同净化装置。
湿式静电除尘柔性纤维织物由长短丝(或称“长短纤”)混织而成，即其经线采用长丝，纬线2采用短丝；或经线1采用短丝，纬线2采用长丝。
长丝为单丝或复丝，机织用长丝直径为200D到2000D，优选为800D～1500D；
短丝直径为200D到2000D，优选为800D～1500D，单根短丝由2～10股纱线合股组成，优选为4～8股纱线合股，单股纱的直径为10～40支，优选15～25支。
柔性纤维织物采用经线1和纬线2平纹机织或斜纹机织。
当采用斜纹机织时，由于织物无正反面区别，益采用2/2～6/6织法，优选2/2、4/4织法；由于在正常工作状态，作为极板的织物应具备一定的强度，以维持表面的张力与平整，机织密度约(300～400)*(100～200)(每10cm经线1和纬线2的根数)，织物每平方米重量应控制在700～1000g，厚度为0.9～1.2mm。为消除表面纹理造成织物表面水膜偏流，应控制表面纹理角度(纹路与水平方向夹角)为45～75度，优选为45～60度。
当采用平纹机织(1/1织法)时，作为极板的织物应具备一定的强度，以维持表面的张力与平整，机织密度约(300～400)*(80～150)(每10cm经线1和纬线2的根数)每平方米重量600～900g，厚度为0.6～0.9mm。
柔性纤维织物的经线1、纬线2的材质为涤纶、丙纶、锦纶中一种或几种组合，优选经线1与纬线2均为涤纶材质。
实现水膜均布的极板及烟气协同净化装置采用上述柔性纤维织物作为除尘布。
本申请的一种典型的实施方式中，如图2所示，提供了一种柔性纤维织物，由经线1与纬线2机织而成，经线1采用涤纶长丝，纬线2采用涤纶短丝；长丝为复丝，直径为1500D；短丝直径为1500D，如图3所示，由5股纱线3合股组成，单股纱线3的直径为25支。
柔性纤维织物采用经纬线2/2斜纹机织。由于在正常工作状态，作为极板的织物应具备一定的强度，以维持表面的张力与平整，调整机织密度为300*100，使织物每平方米重量在850g左右，厚度为1.0mm左右。为消除表面纹理造成织物表面水膜偏流，应控制表面纹理角度α(纹路与水平方向夹角)为50度。
烟气协同净化装置的极板利用上述湿式静电除尘柔性纤维织物作为阳极布。
本申请的另一种典型的实施方式中，如图3所示，由经线1与纬线2机织而成，经线1采用涤纶长丝，纬线2采用涤纶短丝；长丝为复丝，直径为1300D；短丝直径为1000D，由5股纱线3合股组成，单股纱线3的直径为20支。
柔性纤维织物采用经纬线平纹(1/1织法)机织。作为极板的织物应具备一定的强度，以维持表面的张力与平整，调整机织密度为350*90，使得每平方米重量700g左右，厚度为0.8mm左右。
烟气协同净化装置的极板利用本典型实施方式中的湿式静电除尘柔性纤维织物作为阳极布。
根据本发明的另一方面，为了解决背景技术中所述的湿电极板的水膜均布效果不佳，冲洗耗水量大问题，本发明实施例的提供了一种实现水膜均布的极板。
本发明实施例的提供的一种实现水膜均布的极板由至少两个极板区域构成，任一极板区域表面上均有斜纹纹理，任一极板区域表面上的斜纹纹理相互平行且斜纹纹理之间水平距离 相等；相邻的两个极板区域表面上斜纹纹理的方向相反，斜纹纹理的角度均指锐角方向角度；其中，斜纹纹理的角度为斜纹纹理与纬线方向的夹角。
在具体实施例中，相邻的两个极板区域表面上斜纹纹理的角度相等。
在该实施例中，相邻的两个极板区域表面上斜纹纹理的角度设置为相等的角度，能够保证水膜在各个极板区域表面流速以及方向相同，有利于水膜在各个极板区域表面的均匀分布。
在具体实施例中，在每个极板区域内，斜纹纹理的角度越大，沿经线方向的距离越大，斜纹纹理之间水平距离越小，水膜偏流越严重。
(一)当极板为柔性极板时，该极板采用上述的柔性纤维织物制作而成：
对于柔性极板而言，极板由经线1、纬线2斜纹机织而成，在经向，斜纹纹理以左、右斜或右、左斜交替方式呈现。
而且述柔性极板由具有相应斜纹纹理的极板区域拼接而成，或所述柔性极板表面上的斜纹纹理由织机制成。
需要说明的是，当极板为柔性极板时，斜纹纹理在极板区域左右方向交替，可通过设置织机参数实现，或对织物进行裁剪、拼接等后处理方式实现。
如图1所示，在第一极板区域表面内，经向距离极板上顶端一段距离d 11内，斜纹向左/右斜，斜纹与纬向的夹角为α 11(锐角方向)；
在第二极板区域表面内，沿经线方向的长度距离d 12内，斜纹又改为向右/左斜，斜纹与纬向的夹角为α 12(锐角方向)，在极板长度方向上述左、右斜或右、左斜重复出现。
基于烟气的性质及烟气协同净化装置出口颗粒物的浓度要求，当单块柔性极板沿经线方向的长度d 14范围为3～9m，优选为5.5-7.5m；沿纬线方向的长度d 15范围为350～450mm时：
第一极板区域表面沿经线方向的长度d 11范围为0.5～1.2m，第二极板区域表面沿经线方向的长度d 12范围为0.5～1.2m；
第一极板区域表面内的斜纹纹理的角度α 11范围为45°～70°，第二极板区域表面内的斜纹纹理的角度α 12范围也为45°～70°。
第一极板区域和第二极板区域内的斜纹纹理之间水平距离d 13范围为0.1～1mm。其中，斜纹纹理之间水平距离d13范围优选范围为0.2～0.5mm。
在具体实施例中，在经向，距离极板上顶端一段距离d 11＝600mm内，斜纹向左斜，斜纹与纬向的夹角为α 11＝65°(锐角方向)；下一段距离d 12＝600mm内，斜纹又改为向右斜，斜纹与纬向的夹角为α 12＝65°(锐角方向)，在极板长度方向上述左、右斜均重复出现3次。
基于烟气的性质及烟气协同净化装置出口颗粒物的浓度要求，上述单块柔性极板的长度d 14＝6.5m；单块极板的宽度d 15＝440mm。纹理之间的水平距离d 13为0.2mm。
上述柔性极板的参数，基于烟气的性质及烟气协同净化装置出口颗粒物的浓度要求，能够最大程度上减缓水膜偏流发生，保证柔性极板表面90％以上面积均有水膜存在，从而保障水膜对极板上积灰的清除效果。
本发明针对柔性极板，条纹纹理以左/右或右/左交替方式呈现，避免了纹理方向单一进而带来的偏流现象；
本发明通过湿电极板表面结构的改变，实现了较少量布水情况下，水膜在极板上的均匀分布，一方面可以提高清灰的效果，另一方面避免了大水量冲洗，较大程度上减少了废水产生量。
(二)当极板为刚性极板时：
刚性极板表面上的斜纹纹理由机床加工或模具拉挤成型。
在本实施例中，刚性极板可采用玻璃钢或不锈钢来实现。当为不锈钢时，斜纹纹理在极板区域左右方向交替，可通过数控机床如铣床加工而成；当为玻璃钢时，斜纹纹理在极板区域左右方向交替，可通过设置模具参数拉挤成型实现。
在具体实施例中，当所述极板为刚性极板时，所有极板区域内的斜纹纹理的凸起高度相等。
在该实施例中，所有极板区域内的斜纹纹理的凸起高度设置为相等，能够保证水膜在各个极板区域表面流速以及方向相同，有利于水膜在各个极板区域表面的均匀分布。
如图5所示，刚性极板表面设置凸起的具有一定倾斜角度的条纹，且条纹的纹理以左、右斜或右、左斜交替方式呈现。
在具体实施例中，基于烟气的性质及烟气协同净化装置出口颗粒物的浓度要求，当所述极板为刚性极板，单块刚性极板沿经线方向的长度d 24范围为4～8m时，单块刚性极板沿经线方向的优选长度d 24范围为5～7m；
第一极板区域表面沿经线方向的长度d 21范围为1～2m，第二极板区域表面沿经线方向的长度d 21范围也为1～2m，第一极板区域表面内的斜纹纹理的角度α 21为45°～75°，第二极板区域表面内的斜纹纹理的角度α 22也为45°～75°。
第一极板区域和第二极板区域内的斜纹纹理之间水平距离d 23范围为0.1～1mm，优选范围为0.2～0.5mm。
第一极板区域和第二极板区域内的斜纹纹理的凸起高度d 25范围为0.05～0.2mm。
在具体实施例中，上下方向，距离极板上顶端一段距离d 21＝1m内，斜纹向左斜，斜纹与纬向的夹角为α 21＝60°(锐角方向)；下一段距离d 22＝1m内，斜纹又改为向右斜，斜纹与纬向的夹角为α 22＝60°(锐角方向)，在极板长度方向上述左、右斜均重复出现2次。基于烟气 的性质及烟气协同净化装置出口颗粒物的浓度要求，上述单块极板的长度d 24＝6m；所述纹理之间的距离d 23＝为0.3mm，斜纹凸起的高度d 25＝0.05mm。
上述刚性极板的参数，基于烟气的性质及烟气协同净化装置出口颗粒物的浓度要求，能够最大程度上减缓水膜偏流发生，保证刚性极板表面90％以上面积均有水膜存在，从而保障水膜对极板上积灰的清除效果。
对于刚性极板，在其表面增加左、右方向交替的条纹，同样可对表面的水膜起到导流作用，有效避免了“枝丫”状偏流的发生。
本发明通过湿电极板表面结构的改变，实现了较少量布水情况下，水膜在极板上的均匀分布，一方面可以提高清灰的效果，另一方面避免了大水量冲洗，较大程度上减少了废水产生量。
与现有技术相比，本发明的有益效果是：
(1)本发明针对极板，条纹纹理以左/右或右/左交替方式呈现，避免了纹理方向单一进而带来的偏流现象；对于刚性极板，在其表面增加左、右方向交替的条纹，同样可对表面的水膜起到导流作用，有效避免了“枝丫”状偏流的发生。
(2)本发明通过湿电极板表面结构的改变，实现了较少量布水情况下，水膜在极板上的均匀分布，一方面可以提高清灰的效果，另一方面避免了大水量冲洗，较大程度上减少了废水产生量。
参见图5至图11所示，本发明实施例还提供了一种烟气协同净化装置。
该烟气协同净化装置包括两种结构形式，其中：
第一种烟气协同净化装置，包括如图5所示的实现水膜均布的极板。
第二种烟气协同净化装置，包括如图6所示的实现水膜均布的极板。
本发明通过湿电极板表面结构的改变，实现了较少量布水情况下，水膜在极板上的均匀分布，一方面可以提高清灰的效果，另一方面避免了大水量冲洗，较大程度上减少了废水产生量。
参见图7所示，本实施例中的烟气协同净化装置包括四块首尾相连的极板10，烟气协同净化装置还包括十字连接件20和锁合器30，其中，相邻两块极板10之间通过十字连接件20连接；锁合器30用于将十字连接件20和极板10固定连接在一起。
本发明中采用十字连接件20和锁合器30将相邻两块极板10连接在一起，相对于现有技术中采用立柱支撑极板10的结构而言，阳极系统重量大大减轻，节约资源，避免加工立柱时对环境造成污染，既经济又环保。
本实施例中的极板10的侧边设置有第一锁齿，十字连接件20的四端均设置有第二锁齿，锁合器30用于将十字连接件20的第一锁齿和第二锁齿锁合，进而将相邻两块极板10连接在一起。
本实施例中的烟气协同净化装置还包括固定组件，固定组件用于将极板10的顶端和底端固定。
参见图8和图9所示，本实施例中的固定组件包括上花板41、第一平板42、下花板43和第二平板44。
其中，极板10的上端缠绕在上花板41，第一平板42压设在极板10两侧，通过第一固定件45将第一平板42及极板10固定在上花板41上；极板10的下端贴靠在下花板43上，第二平板44压设在极板10的下端，通过第二固定件46将第二平板44及极板10固定在下花板43上，结构简单，便于稳定地将极板10的上下两端固定。
参见图10和图11所示，本实施例中的烟气协同净化装置还包括外壳(图中未示出)，外壳围设形成安装腔，极板10安装在安装腔内，烟气协同净化装置还包括用于对极板10进行牵拉的牵拉装置50。
优选地，牵拉装置50还包括短板51、第三平板52、组合钢板53以及折弯螺柱54。
其中，短板51的第一端与十字连接件20连接；第三平板52与短板51固定连接；组合钢板53包括第一钢板531和第二钢板532，第一钢板531的第一端用于与安装腔的内壁固定连接，第二钢板532的第一端与第一钢板531的第二端垂直连接；折弯螺柱54包括相互垂直的第一螺柱段541和第二螺柱段542，第一螺柱段541与第二钢板532通过第一螺母55可拆卸地连接，第二螺柱段542与第三平板52通过第二螺母56可拆卸地连接，便于对极板10进行牵拉。
优选地，短板51的第一端设置有第三锁齿，该第三锁齿与十字连接件20的未与极板10连接的第二锁齿啮合，并通过锁合器30锁合，结构简单，便于对极板10进行牵拉。
根据上述的实施例可以知道，本实施例中的烟气协同净化装置包括十字连接件20，十字连接件20起替代立柱的作用，十字连接件20的四端均设置有第二锁齿，极板10的侧边设置有第一锁齿，与十字连接件20配合的为极板10，极板10由柔性阳极布及其左右两端设有的第一锁齿组成，十字连接件20与极板10通过锁合器30连接为一体，极板10上端缠绕阳极上花板41，第一平板42分布于极板10的上端两侧，通过第一固定件45将第一平板42、极板10、上花板41、极板10、第一平板42依次连接固定。极板10下端与下花板43底端平齐，第二平板44设于极板10一侧，通过第二固定件46将第二平板44、极板10、下花板43依次连接固定，阳极上花板41、下花板43框架固定于上下两层支撑梁上。每个方孔四角均设一个十字连接件20，两相邻十字连接件20间设有一极板10，根据特定参数设计的湿式除尘器阳极系统由多个上述方孔组成。
极板周边十字连接件20上设有牵拉装置50，牵拉装置50设于与安装腔内壁临近的十字连接件20和内壁之间，包括一定高度的短板51，极板10与十字连接件20连接端设有第三锁齿，通过锁合器30将短板51与十字连接件20连接，短板51另一侧设有第三平板52，第三平板52在短板51内并缠绕两次，用紧固件将短板51及第三平板52连接。第三平板52上下均布设两圆孔，将折弯螺柱54贯穿圆孔，折弯螺柱54端头穿入与第三平板52连接的组合钢板53调节孔内，用第一螺母55和第二螺母56调节折弯螺柱54的张紧度，周边十字连接件20连接内壁侧设有多个牵拉装置50，进而控制极板10的平整性，使极板10与放电极60保持一定的间距，从而保证除尘效率。
锁合器30、第一锁齿、第二锁齿以及第三锁齿均为聚酯或不锈钢等耐腐蚀材质，第一平板42、第二平板44均为PP或FRP等耐腐蚀材质，折弯螺柱54及组合钢板53为双相不锈钢2205材质，使得牵拉装置50为刚性件，保证极板10方孔孔距，避免电压频繁闪络，极板10击穿，影响除尘效率等现象。
本发明提供的十字连接件替代柔性湿式电除尘器极板固定装置及柔性湿式除尘器中的立柱，阳极系统重量大大减轻，节约资源，避免加工立柱时对环境造成污染，既经济又环保。
阳极立柱取消后，支撑立柱及极板用的上下阳极框架及支撑梁规格大大减小，节省加工、运输及安装费用，节约钢材，保证能源合理利用。
阳极立柱的取消使极板可利用面积增加，在同等效率的前提下可缩小湿式除尘器体积，避免浪费，节约成本。
本发明提供的牵拉装置，将短板一侧与十字连接件连接，短板另一侧缠绕刚性第三平板，并用紧固件连接，同时通过折弯螺柱将嵌入短板内的第三平板连接，折弯螺柱端头移到与壳体焊接的组合钢板调节孔内，保证折弯螺柱上下左右移动空间，提供最大限度调节裕量。
牵拉装置为刚性件，控制极板(柔性极板)的平整性，保证阴阳极间放电间距，避免电压闪络、极板击穿、除尘效率降低等现象。
可见，本发明能够取消阳极立柱，阳极柔性极板实现快速安装，支撑框架及支撑梁重量明显减轻，湿式除尘器体积减小，节省投资，极板利用率提高，从而提高除尘效率。
以上所述仅为本发明的优选实施例而已，并不用于限制本发明，对于本领域的技术人员来说，本发明可以有各种更改和变化。凡在本发明的精神和原则之内，所作的任何修改、等同替换、改进等，均应包含在本发明的保护范围之内。

Claims (25)

  1. 一种湿式静电除尘柔性纤维织物，其特征在于，由长丝和短丝混织而成，经线(1)采用所述长丝、纬线(2)采用所述短丝，或所述经线(1)采用所述短丝、所述纬线(2)采用所述长丝，所述长丝为单丝或复丝，所述短丝为若干股纱线合股组成，利用所述短丝的纤维断点形成多个储水空间，以实现织物的持水性。
  2. 根据权利要求1所述的湿式静电除尘柔性纤维织物，其特征在于，所述湿式静电除尘柔性纤维织物为斜纹机织结构，机织密度范围为(300～400)*(100～200)/每10cm所述经线(1)和所述纬线(2)的根数，织物每平方米重量应控制在700～1000g，厚度为0.9～1.2mm。
  3. 根据权利要求2所述的湿式静电除尘柔性纤维织物，其特征在于，所述斜纹机织结构的表面纹理角度为45～75度。
  4. 根据权利要求1所述的湿式静电除尘柔性纤维织物，其特征在于，采用导电碳纤维纱线作为导电材料间隔混织于所述湿式静电除尘柔性纤维织物中，所述碳纤维纱线的直径为1～3K，所述碳纤维纱线与所述长丝或所述短丝复合加捻以增加抗剪能力然后进行机织，在经、纬向所述碳纤维纱线之间的间距为1～5cm。
  5. 根据权利要求1所述的湿式静电除尘柔性纤维织物，其特征在于，所述湿式静电除尘柔性纤维织物为平纹机织结构，机织密度为(300～400)*(80～150)/每10cm所述经线(1)和所述纬线(2)的根数，每平方米重量600～900g，厚度为0.6～0.9mm。
  6. 根据权利要求1所述的湿式静电除尘柔性纤维织物，其特征在于，所述湿式静电除尘柔性纤维织物的所述经线(1)、所述纬线(2)的材质为涤纶、丙纶和锦纶中一种或几种组合。
  7. 根据权利要求1所述的湿式静电除尘柔性纤维织物，其特征在于，所述长丝直径为200D到2000D，所述短丝直径为200D到2000D。
  8. 根据权利要求1所述的湿式静电除尘柔性纤维织物，其特征在于，单根所述短丝由2～10股纱线合股组成，单股纱的直径为10～40支。
  9. 一种实现水膜均布的极板，其特征在于，所述实现水膜均布的极板包括权利要求1至8中任一项所述湿式静电除尘柔性纤维织物。
  10. 根据权利要求9所述的实现水膜均布的极板，其特征在于，所述实现水膜均布的极板由至少两个极板区域构成，任一极板区域表面上均有斜纹纹理，任一极板区域表面上的斜纹纹理相互平行且斜纹纹理之间水平距离相等；相邻的两个极板区域表面上斜纹纹理的方向相反，斜纹纹理的角度均指锐角方向角度；其中，斜纹纹理的角度为斜纹纹理与所述纬线方向的夹角。
  11. 根据权利要求10所述的实现水膜均布的极板，其特征在于，相邻的两个极板区域表面上斜纹纹理的角度相等。
  12. 根据权利要求10所述的实现水膜均布的极板，其特征在于，在每个极板区域内，斜纹纹理的角度越大，沿经线方向的距离越大，斜纹纹理之间水平距离越小，水膜偏流越严重。
  13. 根据权利要求10所述的实现水膜均布的极板，其特征在于，所述实现水膜均布的极板由具有相应斜纹纹理的极板区域拼接而成，或所述实现水膜均布的极板表面上的斜纹纹理由织机制成。
  14. 根据权利要求10所述的实现水膜均布的极板，其特征在于，单块实现水膜均布的极板沿经线方向的长度范围为3～9m，沿纬线方向的长度范围为350～450mm时，任一极板区域表面沿经线方向的长度范围为0.5～1.2m，斜纹纹理的角度范围为45°～70°，斜纹纹理之间水平距离范围为0.1～1mm。
  15. 一种烟气协同净化装置，其特征在于，所述烟气协同净化装置包括权利要求9至14中任一项所述的极板(10)。
  16. 根据权利要求15所述的烟气协同净化装置，其特征在于，所述烟气协同净化装置包括四块首尾相连的所述极板(10)，所述烟气协同净化装置还包括：
    十字连接件(20)，相邻两块所述极板(10)之间通过所述十字连接件(20)连接；
    锁合器(30)，所述锁合器(30)用于将所述十字连接件(20)和所述极板(10)固定连接在一起。
  17. 根据权利要求16所述的烟气协同净化装置，其特征在于，所述极板(10)的侧边设置有第一锁齿，所述十字连接件(20)的四端均设置有第二锁齿，所述锁合器(30)用于将所述第一锁齿和所述第二锁齿锁合。
  18. 根据权利要求15所述的烟气协同净化装置，其特征在于，所述烟气协同净化装置还包括固定组件，所述固定组件用于将所述极板(10)的顶端和底端固定。
  19. 根据权利要求18所述的烟气协同净化装置，其特征在于，所述固定组件包括：
    上花板(41)和第一平板(42)，所述极板(10)的上端缠绕在所述上花板(41)，所述第一平板(42)压设在所述极板(10)两侧，第一固定件(45)将所述第一平板(42)及所述极板(10)固定在所述上花板(41)上；
    下花板(43)和第二平板(44)，所述极板(10)的下端贴靠在所述下花板(43)上，所述第二平板(44)压设在所述极板(10)下端，第二固定件(46)将所述第二平板(44)及所述极板(10)固定在所述下花板(43)上。
  20. 根据权利要求17所述的烟气协同净化装置，其特征在于，所述烟气协同净化装置还包括外壳，所述外壳围设形成安装腔，所述极板(10)安装在所述安装腔内，所述烟气协同净化装置还包括用于对所述极板(10)进行牵拉的牵拉装置(50)。
  21. 根据权利要求20所述的烟气协同净化装置，其特征在于，所述牵拉装置(50)还包括：
    短板(51)，所述短板(51)的第一端与所述十字连接件(20)连接；
    第三平板(52)，所述第三平板(52)与所述短板(51)固定连接；
    组合钢板(53)，所述组合钢板(53)包括第一钢板(531)和第二钢板(532)，所述第一钢板(531)的第一端用于与所述安装腔的内壁固定连接，所述第二钢板(532)的第一端与所述第一钢板(531)的第二端垂直连接；
    折弯螺柱(54)，所述折弯螺柱(54)包括相互垂直的第一螺柱段(541)和第二螺柱段(542)，所述第一螺柱段(541)与所述第二钢板(532)通过第一螺母(55)可拆卸地连接，所述第二螺柱段(542)与所述第三平板(52)通过第二螺母(56)可拆卸地连接。
  22. 根据权利要求21所述的烟气协同净化装置，其特征在于，所述短板(51)的第一端设置有第三锁齿，所述第三锁齿与所述十字连接件(20)的未与所述极板(10)连接的第二锁齿啮合，并通过所述锁合器(30)锁合。
  23. 根据权利要求22所述的烟气协同净化装置，其特征在于，所述锁合器(30)、所述第一锁齿、所述第二锁齿以及所述第三锁齿均为采用聚酯或不锈钢制作而成。
  24. 根据权利要求19所述的烟气协同净化装置，其特征在于，所述第一平板(42)、所述第二平板(44)均采用PP或FRP制作而成。
  25. 根据权利要求21所述的烟气协同净化装置，其特征在于，所述折弯螺柱(54)及所述组合钢板(53)均采用双相不锈钢2205材质制作而成。
PCT/CN2018/085963 2017-07-25 2018-05-08 织物、极板及烟气协同净化装置 Ceased WO2019019762A1 (zh)

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