CN107042041A - A kind of high-temperature dusty gas dust arrester of fast changeable filter disc - Google Patents

A kind of high-temperature dusty gas dust arrester of fast changeable filter disc Download PDF

Info

Publication number
CN107042041A
CN107042041A CN201710218594.7A CN201710218594A CN107042041A CN 107042041 A CN107042041 A CN 107042041A CN 201710218594 A CN201710218594 A CN 201710218594A CN 107042041 A CN107042041 A CN 107042041A
Authority
CN
China
Prior art keywords
filter
filtering
top cover
temperature
metal shell
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.)
Pending
Application number
CN201710218594.7A
Other languages
Chinese (zh)
Inventor
刘开琪
任小勇
张会军
陈运法
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.)
Institute of Process Engineering of CAS
Original Assignee
Institute of Process Engineering of CAS
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
Application filed by Institute of Process Engineering of CAS filed Critical Institute of Process Engineering of CAS
Priority to CN201710218594.7A priority Critical patent/CN107042041A/en
Publication of CN107042041A publication Critical patent/CN107042041A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/54Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms
    • B01D46/543Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms using membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0084Filters or filtering processes specially modified for separating dispersed particles from gases or vapours provided with safety means
    • B01D46/0086Filter condition indicators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • B01D46/14Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces arranged in a star shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/42Auxiliary equipment or operation thereof
    • B01D46/44Auxiliary equipment or operation thereof controlling filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/66Regeneration of the filtering material or filter elements inside the filter
    • B01D46/70Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

The present invention provides a kind of high-temperature dusty gas dust arrester of fast changeable filter, it is main to be made up of metal shell, filtering plate rack, ceramic filter and top cover, the metal shell bottom sets unloading valve, bottom is connected with air inlet pipe, top is connected with top seal, the filtering plate rack is made up of seal base, filtering card and key, is fixed on inside metal shell.Filtering card is shape of photo holder frame structure, and edge is connected with each other, and bottom is welded in bottom plate, top inserts in top cover corresponding recesses just, the ceramic filter is intercalated in filtering card, and dust storage chamber and air-purifying chamber will be divided into inside metal shell, and the top cover sets exhaust outlet to be communicated with air-purifying chamber.Apparatus of the present invention are installed using potsherd draw and insert-type, with processing flue-gas temperature is high, filter is cheap and convenient, the corrugated structure design of replacing makes the advantages, the continuous high-efficient dedusting of many achievable high-temperature dusty gas used in parallel such as big, simple, the purification efficiency height of sealing of device filter area.

Description

A kind of high-temperature dusty gas dust arrester of fast changeable filter disc
Technical field
The invention belongs to removing for the high-temperature dust-containing flue gas of the dust separation of low-order coal pyrolysis oil gas and industrial furnace generation What dirt purification techniques field, the high temperature dust pyrolysis oil gas produced available for low-order coal pyrolytic process, and industrial furnace were produced The dust separation of high-temperature dust-containing flue gas.
Background technology
The higher oil gas composition of added value in low-order coal is extracted by pyrolytic technique, remaining semicoke be re-used as generating electricity or Gasified raw material is greatly improved the utilization ratio of low-order coal, is the important technology path that Coal Clean is efficiently utilized.But it is due to Low-order coal crushing strength is relatively low and heat endurance is poor, and granularity constantly diminishes in pyrolytic process, causes to be pyrolyzed generated pyrolysis There is substantial amounts of dust in gas.It is the key technology that low-order coal high-efficiency cleaning is utilized that gas in pyrolysis gas, oil, dirt are carried out into separation One of.When carrying out dedusting using traditional sack cleaner or electrostatic precipitator, gas temperature need to be generally reduced to 250 DEG C with Under, the tar steam and dust in pyrolysis gas are easily reunited at this temperature, are attached on filtering material and pipeline, are caused Block, cause total system can not long-time steady operation.So the low order coal pyrolysis gas of dust-laden need to carry out dry method at high temperature Dedusting.
Ceramic filter membrane tube hot precipitator is hot precipitator most widely used at present, in integrated gasification combined cycle plants And PFBC (PFBC) generates electricity etc. that good application has been obtained in system, but it is applied to low order pyrolysis of coal (IGCC) But there are problems that during gas dedusting.Low order coal pyrolysis gas dustiness is big, and complicated component, and has coagulability, it is easy to which deposition makes Filter opening is blocked, and is caused filtration resistance quickly to increase and is changed filter, it is necessary to continually shut down.Frequent shutdown causes low order pyrolysis of coal The economy of technology is not high, and therefore, it is difficult to promote.At present using ceramic membrane filter tube or the gas cleaning at high temperature of metal filtration pipe Although device can reach good filter efficiency, replacing membrane tube is cumbersome, not only causes the expense increase of consumptive material, and serious drop The low operating efficiency of total system.
The content of the invention
It is frequent and numerous that the present invention changes filtering membrane tube for existing low-order coal pyrolytic technique high temperature dusty gas deduster Trivial, causing the low problem of system overall operation efficiency, there is provided a kind of high-temperature dusty gas dedusting of fast changeable filter Device, the filtration, purification available for low order coal pyrolysis gas.
In order to solve the above problems, concrete technical scheme of the invention is as follows:
A kind of high-temperature dusty gas dust arrester of fast changeable filter, including metal shell, filtering plate rack, pottery Porcelain filter, deashing device and top cover;The metal shell bottom sets unloading valve, and bottom is connected with air inlet, top and top Lid is tightly connected;The filtering plate rack is built-in and the top half of metal shell is fixed on by welding or by hook, and And cradle top is intercalated in the corresponding groove of top cover just, soft elastic high temperature sealing material, cradle top and top are laid in groove Cap-shaped is into being tightly connected;The ceramic filter is intercalated in filtering card, and metal shell inner space is divided into dust storage chamber And air-purifying chamber, dust storage chamber communicated with air inlet pipe, and air-purifying chamber is communicated with escape pipe;The top cover sets exhaust outlet and air-purifying chamber phase Logical, the inner side of top cover sets groove, and edge sets sealing ring, and periphery is tightly connected with metal shell.
Preferably, metal shell and the top cover inwall or outer wall post heat insulation layer, from light thermal insulation fire-resistant material One or more of arbitrary proportions in material, aluminosilicate fiber cotton, rock wool, aluminium chlorate cellucotton, glass silk flosssilk wadding are mixed, and are prevented Locking apparatus hull-skin temperature is too high, causes energy waste, coking or personnel to scald.
Preferably, the filtering plate rack is made up of filtering card, key and seal base, and filtering card is top edge The photo frame type structure of insertion, ceramic filter is intercalated in filtering card, and polylith filtering card longitudinal edge is interconnected to form Section is polygon, star or zigzag cylinder, and the cylinder lower weld is sealed on sealed bottom plate.
Preferably, the filtering card, key and seal base are prepared using heat resisting steel, in the filtering card of each plane Portion can intercalation 1~n piece filters, the compressible high-temperature fibre braid of the interior use of groove, the high temperature resistant high score of intercalation filter Sub- material, or inorganic sealed with polymer composite.
Preferably, the key cross sectional shape be rectangle, trapezoidal or parallelogram, wherein, up big and down small wedge structure It is easily installed, while deashing is smooth, is capped and can be sealed after fastening bolt by encapsulant.
Preferably, the ceramic filter is porous ceramics piece or ceramic beaverboard, and size is with filtering the slotting pottery on card Ceramics groove size matches, and is made from resistant to elevated temperatures ceramic material, composition is Al2O3、SiC、SiO2、Si3N4, silicic acid Aluminium, mullite, cordierite, ZrO2In one or more be combined for main component.
Preferably, inserted slot and ceramic filter plate shape may be designed to up big and down small trapezoidal knot in the filtering card Structure, not only make it that deashing is smooth, filter it is easier for installation, and top cover can be used to apply downward pressure so that Sealing of the filter with filtering card is tighter.
Preferably, the deashing device be pulse backblowing deashing device, mechanical vibrator, one kind in ultrasonic deashing device or Any combination of several devices, online ash removal is carried out according to the highest limit value of filtering pressure drop setting or timing to ceramic filter plate.
Preferably, when the deashing device is pulse backblowing deashing device, solderable height was slightly less than inside air-purifying chamber Filter and blowback nozzle is installed in the metal partion (metp) of card, the space being each separated out, carry out pulse backblowing deashing, filtering card and dust Welding metal silk screen is may be selected in the one side of room contact, and strengthening action is played to ceramic filter.
Preferably, the top cover inwall posts heat insulation layer, and cap edge sets refractory seals ring, with metal shell It is connected and sealed using flange.Top cover inner surface sets to set in groove corresponding with filtering plate rack, groove and made pottery with intercalation High-temperature flexible encapsulant is loaded in the corresponding small projection in ceramics position, groove, during installation, filter pedestal upper end is plugged in In groove, give downward pressure by top cover and compression sealing is carried out to filtering plate rack and ceramic filter.Filtering plate rack, Filter and top cover define air-purifying chamber together, and top cover upper end sets outlet pipe, communicated with air-purifying chamber.
In another aspect of the present invention, the invention provides a kind of foregoing fast changeable filter of utilization The method that high-temperature dusty gas dust arrester carries out high-temperature dusty gas dedusting.Embodiments in accordance with the present invention, this method includes Following steps:
A) two or many playscript with stage directions devices are installed in parallel, and during the work operation of one or more device, can be exceeded filtration resistance The table apparatus for designing the upper limit is shut down and quick-replaceable filtering material;
B) filtering blast generation type one:The external air-introduced machine of blast pipe, constantly outwards pumping, in air-purifying chamber formation negative pressure, High-temperature dusty gas enters dust storage chamber from air inlet pipe, enters air-purifying chamber by ceramic filter under pressure, and grit quilt It is blocked on filter;Filter blast generation type two:By machine of being given a dinner for a visitor from afar at air inlet pipe, supply gas, entered by pressure to dust storage chamber Row dedusting;Filter blast generation type three:Above-mentioned mode one and mode two are applied in combination;
C) with the progress of filtering, the filtration resistance of equipment constantly increases.Deashing pattern one:Filtration resistance is monitored in real time, When resistance reaches the peak of setting, open deashing device and deashing is carried out to ceramic filter.Pattern two:Set a time Section, timing carries out deashing;
D) when deashing processing effectively can not reduce filtration resistance, close before this TV station dust arrester, open standby to be opened Device, it is ensured that high-temperature dust removal process is continuously run.Lugs top cover is opened, is integrally hung out on equipment, or by filtering core, Then the filter after use is extracted, in new filter wound edgewise high temperature sealing material, and is inserted into plugboard trough, is covered Upper top cover, top cover and casing seal dust arrester under fastening pressure by encapsulant.Complete the replacing of ceramic filter Afterwards, the table apparatus enters state to be opened.
Compared with existing gas cleaning at high temperature purifier, advantage of the invention is that:
(1) installed using plug-in, replacing filter is more convenient, enormously simplify filter mounting process, Improve the operational efficiency of system;
(2) using it is one or more groups of than relatively thin ceramic membrane filter piece as filter element, reduce filtration resistance, and subtract Lack the risk of potsherd fracture, and potsherd can realize standardization large-scale industrial batch production, compared to ceramic membrane mistake Chimney filter, the part for there was only tubulose using the price of the ceramic filter of identical filter area, greatly reduces filtering material Production cost;
(3) cheap due to simple in construction, many institute's invention dedusters are used in parallel, and the company of whole system can be achieved Continuous stable operation.
Brief description of the drawings
Fig. 1 is the structural representation of the high-temperature dusty gas dust arrester of fast changeable filter used in the embodiment of the present invention Figure.
Fig. 2 is the knot of the high-temperature dusty gas dust arrester cross section of fast changeable filter used in the embodiment of the present invention Structure schematic diagram.
Fig. 3 is the enlarged drawing of dotted box portion in Fig. 2.
Fig. 4 is the structural representation of top cover used in the embodiment of the present invention.
In accompanying drawing, 1- metal shells;2- fibrous insulating layers;3- seal bases;4- filters card;5- ceramic filters;6- Fixed hook;7- clamp flanges;8- top covers;9- discharge ducts;10- purge gas pipelines;11- blowback control valves;12- high temperature resistants Sealing gasket;13- refractory seals rings;14- admission lines;15- unloading valves;16- metal partion (metp)s;17- blowback nozzles;18- inserted sheets Groove encapsulant;19- keies;8a- screwed holes;8b- cap recess;Respective protrusions in 8c- grooves;8d- exhaust outlets.
Embodiment
For a better understanding of the present invention, with reference to the embodiment content that the present invention is furture elucidated, but the present invention Content is not limited solely to the following examples.
As Figure 1-3, in the present embodiment, the high-temperature dusty gas dust arrester of fast changeable filter of the present invention Mainly include metal shell 1, heat insulation layer 2, seal base 3, filtering card 4, ceramic filter 5, fixed hook 6, fastening Flange 7, top cover 8, discharge duct 9, purge gas pipeline 10, blowback control valve 11, refractory seals pad 12, refractory seals ring 13rd, fibrous encapsulation ring 8, admission line 14, unloading valve 15, metal partion (metp) 16, blowback nozzle 17, inserted slot encapsulant 18 and wedge Piece 19.
Metal shell 1 and the inwall of top cover 8 post the heat insulation layer that thickness is about 3cm, and material is aluminosilicate fiber cotton, use Heat-resisting rivet is fixed on metal shell.Filtering card 4 edge, which is welded to each other, surrounds star cylinder, bottom welding and seal base On 3, filtering plate rack is constituted.Filtering plate rack is fixed on metal shell inner space upper end by fixed hook 6, and top exceeds 1~15cm of case top edge.Filter cradle top is inserted in the groove of top cover 8, and refractory seals pad is filled with groove 12, prepared using high-temperature fibre.Top cover is connected with metal shell by clamp flange 7, and high-temperature fibre sealing is installed in centre Ring 13 is sealed.
Seal base, filtering card and key are prepared from 1Cr18Ni9Ti heat resisting steel in the present embodiment, seal base Thickness is about 5mm, and filtering card is shape of photo holder frame structure, as shown in Figures 2 and 3.The high temperature sealing material of filling inside inserted slot 18 be pyroceram fibre.The structure of key is the up big and down small wedge structure that section is convex, is given during installation by top cover Downward pressure is given, filter is compressed sealing relative to filtering card.
Ceramic filter plate is SiC porous ceramic film filters in the present embodiment, and pore-size is 1~10 μm, and porosity is about For 38%.Ceramic filter plate thickness is about 6mm, and superficial film thickness is about 100 μm, is intercalated in filtering card.
Top cover is prepared from 1Cr18Ni9Ti heat resisting steel in the present embodiment, and its structural representation is as shown in figure 4, table in top cover Face sets in groove corresponding with filtering plate rack, groove and loads high-temperature flexible encapsulant, during installation, on filtering plate rack End is plugged in groove, and giving downward pressure by top cover carries out compression sealing.Filter plate rack, filter and top cover together Air-purifying chamber is defined, top cover upper end sets outlet pipe, communicated with air-purifying chamber.
In the present embodiment using pulse backblowing deashing device to ceramic membrane filter piece carry out deashing, purge gas pipeline 10 from Enter air-purifying chamber in discharge duct 9, as shown in figure 1, welding metal dividing plate 16 on seal base, 6 small skies are divided into by air-purifying chamber Between, blowback nozzle 17 is installed in each interior volume, reverse gas cleaning is carried out to filter.
When carrying out dust separation to low rank coal high temperature pyrolysis oil gas using the present apparatus, it is installed in parallel using two table apparatus, its In a table apparatus work, a table apparatus waits to open, and specific purification technique is:
(1) low order coal pyrolysis gas enters dust storage chamber A from air inlet pipe 14;(2) the external high-power air-introduced machine of blast pipe 9, constantly Outwards pumping, negative pressure is formed in air-purifying chamber, and high temperature pyrolysis gas enters air-purifying chamber B by ceramic filter plate 5 under pressure, with Discharged afterwards from discharge duct, and grit is blocked on filter surface;(3) with the progress of filtering, the grey cake layer of formation makes Obtain filtration resistance constantly to increase, filtration resistance is monitored in real time, when resistance reaches setting value, open blowback control valve, blowback air Body is sprayed at a high speed out of blowback nozzle, and deashing is carried out to ceramic filter;(4) when deashing processing can not effectively reduce filtration resistance When, this TV station dust arrester is closed, opening device is treated while opening, residual gas is discharged, this table apparatus top cover is opened, key is extracted, In new filter wound edgewise high-temperature fibre rope, and it is inserted into plugboard trough, inserts key, carries out compression sealing, cover Top cover carries out top and compresses sealing, completes the replacing of ceramic filter, and the table apparatus enters state to be opened.
As known by the technical knowledge, the present invention can be by the embodiment party of other essence or essential feature without departing from its spirit Case is realized.Therefore, embodiment disclosed above, is merely illustrative, and is not only.It is all within the scope of the present invention Or be included in the invention in the change being equal in the scope of the present invention.

Claims (9)

1. a kind of high-temperature dusty gas dust arrester of fast changeable filter, it is characterised in that:Including metal shell, filtering Plate rack, ceramic filter, deashing device and top cover;The metal shell bottom sets unloading valve, and bottom is connected with air inlet, Top is connected with top seal;The filtering plate rack is built-in and the upper half of metal shell is fixed on by welding or by hook Part, and cradle top is intercalated in the corresponding groove of top cover just, and soft elastic high temperature sealing material, top of support are laid in groove Portion is tightly connected with top cover formation;The ceramic filter is intercalated in filtering card, and metal shell inner space is divided into Dust storage chamber and air-purifying chamber, dust storage chamber are communicated with air inlet pipe, and air-purifying chamber is communicated with escape pipe;The top cover sets exhaust outlet and net gas Room is communicated, and the inner side of top cover sets groove, and edge sets sealing ring, and periphery is tightly connected with metal shell.
2. the high-temperature dusty gas dust arrester of fast changeable filter as claimed in claim 1, it is characterised in that:Filtering Plate rack is made up of seal base, filtering card and key, and filtering card is the photo frame type structure of top edge insertion, ceramic mistake Filter disc is intercalated in filtering card, and it is regular or irregular polygon that polylith filtering card longitudinal edge, which is interconnected to form section, Shape, star or zigzag cylinder, the cylinder lower weld on seal base in being sealed.
3. plate rack is filtered as claimed in claim 2, it is characterised in that:Seal base, filtering card and key are using heat-resisting Steel is standby, inside the filtering card of each plane can intercalation 1~n piece filters, using compressible in the groove of intercalation filter High-temperature-resistant inorganic fibre braid, high temperature modification high polymer material or inorfil and polymer composite are sealed.
4. filter plate rack as described in claim 2 and 3, it is characterised in that:Key cross sectional shape is rectangle, trapezoidal or parallel four Side shape, wherein, up big and down small wedge structure is easily installed, while deashing is smooth, is capped and can be passed through sealing material after fastening bolt Material is sealed.
5. the high-temperature dusty gas dust arrester of fast changeable filter as claimed in claim 1, it is characterised in that:The pottery Porcelain filter is porous ceramics piece or ceramic beaverboard, and size matches with the slotting potsherd groove size on filtering card, It is made from resistant to elevated temperatures ceramic material, composition is Al2O3、SiC、SiO2、Si3N4, alumina silicate, mullite, cordierite, ZrO2In One or more be combined for main component.
6. the high-temperature dusty gas dust arrester of fast changeable filter as claimed in claim 1, it is characterised in that:It is described clear Apparatus for ash is any combination of pulse backblowing deashing device, mechanical vibrator, one or more of devices in ultrasonic deashing device, according to Filtering deashing is carried out to ceramic filter (plate) according to the highest limit value or timing of filtering pressure drop setting.
7. the high-temperature dusty gas dust arrester of fast changeable filter as claimed in claim 1, it is characterised in that:The top Lid and metal shell inwall or outer wall set heat insulation layer, or coating heat insulation coating, and edge seal circle is refractory seals ring, Material is high-temperature-resistant inorganic fibre braid, high temperature modification high polymer material or inorfil and high molecular composite, with gold Category housing is connected and sealed using bolt fastening.
8. top cover as claimed in claim 7, is further characterized in that:The size for the groove that inside of top cover is set and position and filter Support is corresponding, is set in groove and the projection corresponding with ceramic filter is set in high-temperature flexible encapsulant, groove, installed When to filtering plate rack and ceramic filter carry out compression sealing.
9. the high-temperature dusty gas dust arrester of fast changeable filter as claimed in claim 1, it is characterised in that its high temperature Dust collecting process comprises the following steps:
A) two or many playscript with stage directions devices are installed in parallel, when one or more work is run, and filtration resistance can be exceeded to the design upper limit A table apparatus shut down and quick-replaceable filtering material;
B) filtering blast generation type one:The external air-introduced machine of blast pipe, constantly outwards pumping, in air-purifying chamber formation negative pressure, high temperature Dusty gas enters dust storage chamber from air inlet pipe, enters air-purifying chamber by ceramic filter under pressure, and grit is blocked On filter;Filter blast generation type two:By machine of being given a dinner for a visitor from afar at air inlet pipe, supply gas, removed by pressure to dust storage chamber Dirt;Filter blast generation type three:Above-mentioned mode one and mode two are applied in combination.
C) with the progress of filtering, the filtration resistance of equipment constantly increases.Deashing pattern one:Monitoring filtration resistance, works as resistance in real time When power reaches the peak of setting, open deashing device and deashing is carried out to ceramic filter.Pattern two:Preset a time Section, timing carries out deashing;
D) when deashing processing effectively can not reduce filtration resistance, close before this TV station dust arrester, open standby device to be opened, Ensure that high-temperature dust removal process is continuously run.Lugs top cover is opened, is integrally hung out on equipment, or by filtering core, then The filter after use is extracted, in new filter wound edgewise high temperature sealing material, and is inserted into plugboard trough, covers top Lid, top cover and casing seal dust arrester under fastening pressure by encapsulant., should after the replacing for completing ceramic filter Table apparatus enters state to be opened.
CN201710218594.7A 2017-04-05 2017-04-05 A kind of high-temperature dusty gas dust arrester of fast changeable filter disc Pending CN107042041A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710218594.7A CN107042041A (en) 2017-04-05 2017-04-05 A kind of high-temperature dusty gas dust arrester of fast changeable filter disc

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710218594.7A CN107042041A (en) 2017-04-05 2017-04-05 A kind of high-temperature dusty gas dust arrester of fast changeable filter disc

Publications (1)

Publication Number Publication Date
CN107042041A true CN107042041A (en) 2017-08-15

Family

ID=59545544

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710218594.7A Pending CN107042041A (en) 2017-04-05 2017-04-05 A kind of high-temperature dusty gas dust arrester of fast changeable filter disc

Country Status (1)

Country Link
CN (1) CN107042041A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107670428A (en) * 2017-10-19 2018-02-09 苏州红恩新材料科技有限公司 A kind of screen pipe suitable for high-temperature dust-containing flue gas
CN108913222A (en) * 2018-09-14 2018-11-30 江西理工大学 A kind of pulverized coal pyrolysis produces pyrolysis Flash Gas Compression Skid System and processing method during tar
CN116514227A (en) * 2023-06-12 2023-08-01 李峰 Modularized automatic purifying device

Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU7449381A (en) * 1981-01-30 1982-08-05 Krw Energy Systems Inc. Hot gas particulate removal
US5078760A (en) * 1991-02-11 1992-01-07 Westinghouse Electric Corp. Separation of particulate from gases produced by combustion of fossil material
CA2130656A1 (en) * 1993-09-02 1995-03-03 Robert J. Cooper Filter Screen and Method of Making Same
CN2387952Y (en) * 1999-07-07 2000-07-19 北京企信科技集团 Sintered wire filter screen high-temp. dry dust-removing device
US20110041690A1 (en) * 2009-08-18 2011-02-24 Flsmidth A/S Method and apparatus for removing volatile contaminants from industrial plants
CN202105534U (en) * 2011-05-30 2012-01-11 王树宽 Crude gas filter of coal gas tar oil production device
JP2013000607A (en) * 2011-06-10 2013-01-07 Rinnai Corp Filter device
CN103663523A (en) * 2013-12-09 2014-03-26 中国科学院过程工程研究所 Spherical alumina nanocrystal and preparing method thereof
US20140290873A1 (en) * 2013-03-29 2014-10-02 Joseph A. Altieri, JR. Removable Window and Door Screens
CN104540567A (en) * 2012-05-31 2015-04-22 Advancetex国际有限公司 Filter cage and filter assembly for baghouse filter
CN104629775A (en) * 2013-11-12 2015-05-20 中国科学院过程工程研究所 Pyrolysis device for carbonaceous substance
CN204502634U (en) * 2015-03-31 2015-07-29 长安大学 A kind of high-temperature gas duster device
CN104971559A (en) * 2015-07-17 2015-10-14 深圳市普瑞美泰环保科技有限公司 Combined air filtering module
CN106147880A (en) * 2016-07-01 2016-11-23 河南龙成煤高效技术应用有限公司 Pyrolysis gas dedusting filter
CN106318472A (en) * 2016-11-01 2017-01-11 中国科学院过程工程研究所 High temperature dust-containing coal gas dust removal device
CN206950859U (en) * 2017-04-05 2018-02-02 中国科学院过程工程研究所 A kind of high-temperature dusty gas dust arrester of fast changeable filter disc

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU7449381A (en) * 1981-01-30 1982-08-05 Krw Energy Systems Inc. Hot gas particulate removal
US5078760A (en) * 1991-02-11 1992-01-07 Westinghouse Electric Corp. Separation of particulate from gases produced by combustion of fossil material
CA2130656A1 (en) * 1993-09-02 1995-03-03 Robert J. Cooper Filter Screen and Method of Making Same
CN2387952Y (en) * 1999-07-07 2000-07-19 北京企信科技集团 Sintered wire filter screen high-temp. dry dust-removing device
US20110041690A1 (en) * 2009-08-18 2011-02-24 Flsmidth A/S Method and apparatus for removing volatile contaminants from industrial plants
CN202105534U (en) * 2011-05-30 2012-01-11 王树宽 Crude gas filter of coal gas tar oil production device
JP2013000607A (en) * 2011-06-10 2013-01-07 Rinnai Corp Filter device
CN104540567A (en) * 2012-05-31 2015-04-22 Advancetex国际有限公司 Filter cage and filter assembly for baghouse filter
US20140290873A1 (en) * 2013-03-29 2014-10-02 Joseph A. Altieri, JR. Removable Window and Door Screens
CN104629775A (en) * 2013-11-12 2015-05-20 中国科学院过程工程研究所 Pyrolysis device for carbonaceous substance
CN103663523A (en) * 2013-12-09 2014-03-26 中国科学院过程工程研究所 Spherical alumina nanocrystal and preparing method thereof
CN204502634U (en) * 2015-03-31 2015-07-29 长安大学 A kind of high-temperature gas duster device
CN104971559A (en) * 2015-07-17 2015-10-14 深圳市普瑞美泰环保科技有限公司 Combined air filtering module
CN106147880A (en) * 2016-07-01 2016-11-23 河南龙成煤高效技术应用有限公司 Pyrolysis gas dedusting filter
CN106318472A (en) * 2016-11-01 2017-01-11 中国科学院过程工程研究所 High temperature dust-containing coal gas dust removal device
CN206950859U (en) * 2017-04-05 2018-02-02 中国科学院过程工程研究所 A kind of high-temperature dusty gas dust arrester of fast changeable filter disc

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107670428A (en) * 2017-10-19 2018-02-09 苏州红恩新材料科技有限公司 A kind of screen pipe suitable for high-temperature dust-containing flue gas
CN108913222A (en) * 2018-09-14 2018-11-30 江西理工大学 A kind of pulverized coal pyrolysis produces pyrolysis Flash Gas Compression Skid System and processing method during tar
CN108913222B (en) * 2018-09-14 2023-09-26 江西理工大学 Pyrolysis gas treatment device and treatment method in pulverized coal pyrolysis tar production process
CN116514227A (en) * 2023-06-12 2023-08-01 李峰 Modularized automatic purifying device
CN116514227B (en) * 2023-06-12 2024-02-13 李峰 Modularized automatic purifying device

Similar Documents

Publication Publication Date Title
CN206950845U (en) A kind of temperature gas dust remover of continuously-running
CN106318472B (en) A kind of high temperature dust coal gas dust-extraction unit
CN201735287U (en) High-temperature dust remover of ceramic filter drum
CN107042041A (en) A kind of high-temperature dusty gas dust arrester of fast changeable filter disc
CN106422562A (en) Flue gas dedusting device
CN105861077B (en) A kind of the dedusting coke removing appts and its method of the high-temperature gas that high tar is dusty
CN109867524B (en) Preparation method and device of pore diameter controllable silicon carbide asymmetric composite filter tube membrane
CN206950859U (en) A kind of high-temperature dusty gas dust arrester of fast changeable filter disc
CN112521986A (en) High-temperature efficient explosion-proof type integrated modular dust removal equipment for pyrolysis raw gas
KR20060089276A (en) High temperature dust collecting system
CN107854951A (en) A kind of emission-control equipment of coal-burning boiler
CN206198879U (en) A kind of fume dust remover
CN112066762B (en) Heat exchange device suitable for crude gas and use method thereof
CN108031208A (en) A kind of dusty gas dust-extraction unit
CN113713514A (en) Flue gas dust removal denitration filter equipment
CN103060515B (en) Composite purifying equipment of converter gas
CN202962176U (en) Biomass blowback type dust collection box
CN102935316A (en) Large-scale filter filtration core failure protection apparatus
CN101838716A (en) Process method and device for converter gas high-temperature dust removal
CN215216198U (en) Boiler feed water preheating device based on waste heat utilization
CN206325325U (en) High-temperature waste gas treating apparatus
CN206355754U (en) Conductivity ceramics film high-temp. corrosion resistant deduster
CN212548802U (en) Kiln waste gas dust collector
CN203200293U (en) Converter gas compound purification equipment
CN210786700U (en) Convection type blowing and sucking dust removal device

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170815