CN103071352A - Dust removing and waste gas removing apparatus - Google Patents

Dust removing and waste gas removing apparatus Download PDF

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Publication number
CN103071352A
CN103071352A CN2012101032049A CN201210103204A CN103071352A CN 103071352 A CN103071352 A CN 103071352A CN 2012101032049 A CN2012101032049 A CN 2012101032049A CN 201210103204 A CN201210103204 A CN 201210103204A CN 103071352 A CN103071352 A CN 103071352A
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China
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pipe
filter
communicated
strap
dedusting
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CN2012101032049A
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Chinese (zh)
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邵波
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邵波
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Priority to CN2012101032049A priority Critical patent/CN103071352A/en
Publication of CN103071352A publication Critical patent/CN103071352A/en
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Abstract

The present invention relates to a dust removing and waste gas removing apparatus. According to the present invention, two dust removing and waste gas removing pipes are respectively designed according to a dual path parallel design manner, wherein the dust removing and waste gas removing pipe comprises a dry coarse dust removing segment as well as a wet fine dust removing and waste gas removing segment which are the same. The apparatus is characterized in that the key segment of every pipe is formed by combining capture system selection, online continuous automatic filtration residue removing dust removing filter selection, online continuous dust discharging dust removing gas introduction dust remover selection and a waste gas groove; and the tubular coarse dust removing gas introduction device with characteristics of high speed coarse dust removing, no plugging in gas introduction and the multi-stage countercurrent dust and waste gas removing groove with functions of automatic water supply, agent supply and product recovery can select a groove liquid having corresponding chemical properties according to chemical properties of the waste gas to be combined so as to remove the waste gas, such that disadvantages of filtration work surface slagging and filtration clogging, high operation energy consumption, incapability of removing dust and waste gas simultaneously, low purification degree, low treatment speed, instability, large sludge amount, high work intensity, serious secondary pollution, short equipment service life and the like can be completely solved. The dust removing and waste gas removing channel apparatus is applicable for various gaseous pollution sources, and efficient and high purification degree dioxin removing can be achieved.

Description

A kind of dedusting and removing exhaust gas device
Technical field
The invention belongs to environmental technology field, is a kind of dedusting and removing exhaust gas device in the environment project specifically, is the Environmental-protection comprehensive technology of a physics dedusting and chemical removing exhaust gas.
Background technology
Along with social progress, people's environmental consciousness improves day by day, recognize that profoundly the dust of a chimney and waste gas can cause terrestrial climate to change to the pollution of environment, misfortune and the whole world, industrial and agricultural production is flourishing, to boost environmental awareness and the green technology level, especially large-scale smeltery, the cement plant, the chemical plant, power plant and funeral and interment field are wanted energy-saving and emission-reduction especially, the depositing dust low-carbon (LC), the cleaning discharging, particularly there is the particle diameter of considerable part dust very little in the flue dust of garbage burning factory, floatability is very strong, for a long time contaminated environment such as bioxin dust, serious threat human health and existence, this is worldwide problem, for descendants and the existence of oneself, must pay attention to the chalk dust removing removing exhaust gas.
In order to eliminate caused dust and exhaust emission environment in the industrial and agricultural production process, to destroy ecological problem, for a long time, people constantly make great efforts, and have invented all dedusters.In dedusting technology, current popular be traditional dry method bag pulse dedusting technology, wherein also has back-blowing bag-type dust collector, electric vibrating or beating sack cleaner, rotary counter-blowing formula dry-method bag-type deduster, the other formula dry-method bag-type deduster of inserting, pulse blowing type dry-method bag-type deduster, sinter-plate precipitators etc. are all advanced than traditional wet dedusting, also than traditional settling dust remover, various cyclone dust collectors in the inertial dust separator are good, and the flue gas cool-down dewfall blocks filter cloth and the fast knot of dedusting function inefficacy in the prior art dry-method bag-type deduster but it has not been untied all the time.
How to stop that dry-method bag-type deduster filter cloth is blocked and dedusting function lost efficacy and the phenomenon of interception small particle diameter dust, and solution can't be removed the problem of pernicious gas simultaneously, how to tackle more up hill and dale the minimum flue dust of particle diameter, be that the clearance requirement is higher, how that the filter residue on the filter cloth is faster, more effective, dispose more up hill and dale, the filtering function of guaranteeing filter cloth does not descend, that guarantees filter cloth keeps that the normal filtration function does not descend and remove at low cost pernicious gas in dedusting, in a word, these problems all are the problem to be solved in the present invention.
Summary of the invention
Purpose of the present invention: the fast knot that 1, blocks filter cloth for flue gas cool-down dewfall in the existing dedusting technology dry filtration type deduster, solve stifled filter and the large phenomenon of crushing and cause the inefficient problem of chalk dust removing removing exhaust gas, pursue to filter that crushing is little, power consumption is little, when guaranteeing that the employee changes filtering material, reduce labour intensity, stop the dust from flying secondary pollution, stop to injure the healthy phenomenon of employee, demonstrate fully hommization; 2, not only to remove solid-state dust, but also will remove chemical oxious component in the waste gas, needn't fall as the smoke directly ventilating that the means that must adopt high altitude discharge after traditional dry-method bag-type dedusting will contain remaining pernicious gas.3, not only to reduce requirement to equipment and materials, but also require the failure rate is low of equipment, reliability is high, operation energy consumption is low, the life-span is long, and has the function of the economical operation under large exhaust gas volumn fast processing and the little flue gas discharge capacity.
To achieve these goals, specialized designs the collection cigarette system of ingenious novelty scientific and reasonable for structure, on-line continuous automatic ash removing dust pelletizing system, tubular type is carried ash discharge dust pelletizing system and multi-stage countercurrent immersion dedusting and removing exhaust gas system, and consisted of the technical scheme of practical take them as core component: will collect the cigarette system, cooling system, be provided with the dust pelletizing system of pipe inner filtration strap self-cleaning system, flue filters the strap self-cleaning system outward, after multi-stage countercurrent immersion dedusting and removing exhaust gas system uses pipeline and valve is communicated with them successively, and in multi-stage countercurrent immersion dedusting and removing exhaust gas system, being communicated with respectively hutch water device and tonic device, the flue gas that this technical scheme can be finished effectively to containing dust and pernicious gas has carried out the task of physical treatment and chemical treatment.Purge gas after the processing is discharged by floss hole, and it tackles the ash and the slag that get off, and water is drained in the corresponding device by ash discharge, deslagging and discharge outlet respectively.
Concrete technical measures
Fig. 2, Fig. 3, Fig. 4 and Fig. 5 illustrate the 10 collection cigarette systems 1.0 that dedusting and removing exhaust gas device of the present invention configures from side separately, it is by air-suction cover 1.1,12 exhausting systems 1.2, non-return linkage 1.3 and 1.4 connections of air-suction cover rotation movable joint form, wherein air-suction cover 1.1 is by cover body 1.1.1, all press dividing plate 1.1.2, check plate 1.1.3, barge board 1.1.4 forms, its cover body 1.1.1 is the semicylinder body, its axis is up settled by ground, the opposing face of the air-breathing working face of cover body 1.1.1 is provided with the gas outlet, cover body 1.1.1 inside is provided with and all presses dividing plate 1.1.2, all press dividing plate 1.1.2 for be installed in one group of thin strip-plate of cover body 1.1.1 inner chamber by the requirement of hydrodynamics pressure distribution rule, per two rotor 1.2.2 that all press the gas channel that consists of between the dividing plate 1.1.2 all to face toward 12 exhausting systems 1.2, barge board 1.1.4 divides two both sides that are mounted on respectively the opposing face of the air-breathing working face of cover body 1.1.1, the rotor 1.2.2 of 12 exhausting systems 1.2 is driven by motor 1.2.1, and the startup of motor 1.2.1 operation is controlled by non-return linkage 1.3 with termination; Non-return linkage 1.3 is pressed Action of Gravity Field by louvre type and sagging only aerofoil 1.3.1, the switch 1.3.2 of motor 1.2.1 consists of, the stripe board of ending aerofoil 1.3.1 is connected in cover body 1.1.1 inboard by loose-leaf, its stripe board face can be turned to naturally by Action of Gravity Field hang, switch 1.3.2 also is installed on the position that cover body 1.1.1 is inboard with only aerofoil 1.3.1 presses mutually, the control contact of trip switch 1.3.2 when ending aerofoil 1.3.1 and under the effect of air-flow, becoming non-hang by hang and connect the circuit of motor 1.2.1, airless to get back to hang as the time spent be the control contact of clamping switch 1.3.2 and disconnect the circuit of motor 1.2.1; The gas outlet of cover body 1.1.1 is communicated with the air inlet of air-suction cover rotation movable joint 1.4 by pipeline GD; Air-suction cover rotation movable joint 1.4 is made of ash releasing tube 1.4.0, threeway 1.4.1, lower pellet shelves 1.4.2, pellet 1.4.3, hold-down screw 1.4.4, movable joint cover 1.4.5, packing suede 1.4.6, upper pellet shelves 1.4.7, nut 1.4.8, valve FM, wherein to be provided with the port of ring flange be air inlet in the centre of threeway 1.4.1, the port that its installation direction is downward, serving as ash releasing tube 1.4.0 and valve FM is communicated with, the outlet of valve FM is ash hole, and the threaded port of another pipe peripheral hardware is the gas outlet; In addition, the inwall place, cover two ends of its movable joint cover 1.4.5 is equipped with pellet position and lower pellet position, and is provided with ring flange at the one end; During assembling air-suction cover rotation movable joint 1.4, first with the fastening lower pellet shelves 1.4.2 of threeway 1.4.1 outside the epimere pipe that be installed in of hold-down screw 1.4.4, load onto pellet 1.4.3, put inside pipe wall loaded encapsulant packing suede 1.4.6's and the end that will be provided with ring flange place the movable joint cover 1.4.5 of top, pellet 1.4.3 is installed in upper pellet position at movable joint cover (1.4.5) upper port place, installing pellet shelves 1.4.7 presses pellet 1.4.3 again, use at last nut 1.4.8 that upper pellet shelves 1.4.7 is fastening, its gas outlet is communicated with the air inlet of cooling system 2 by pipeline GD, the ash hole docking of the valve FM that lime-ash shipment sack is communicated with ash releasing tube 1.4.0 below.
Fig. 6 and Fig. 7 illustrate the dust pelletizing system that dedusting and removing exhaust gas device of the present invention configures from separately side be on-line continuous automatic ash removing dust pelletizing system 3.0, it is made of filtration system 3.0 and pipe inner filtration strap self-cleaning system 3.1~3.4, filtration system 3.0 version that consists of two-way arranged side by side by the identical filtration system 3.0A of internal structure and filtration system 3.0B wherein, the version that pipe inner filtration strap self-cleaning system 3.1~3.4 consists of two-way arranged side by side by the identical pipe inner filtration strap self-cleaning system 3.1A~3.4A of internal structure and pipe inner filtration strap self-cleaning system 3.1B~3.4B, because of on-line continuous automatic ash removing dust pelletizing system 3.0A the same with the structure of on-line continuous automatic ash removing dust pelletizing system 3.0B, any one system gets final product therefore only need explain wherein, and needn't use " A or B " to be distinguished in this segment table is stated again; Filtration system 3.0 is by blast machine 3.0.0, filter strap 3.0.1, filter strap and drive 3.0.2, filter strap drive 3.0.3, filter strap sealing pressing wheel 3.0.4, filter strap sealing wheel support 3.0.5, groove lid 3.0.6 on the filter, filter strap support wheel plate 3.0.7, scarfing cinder sparge pipe and drive support 3.0.8 in the pipe, pipe inner filtration cloth belt tensioner pulley 3.0.9, filter lower groove 3.0.10, seal female groove 3.0.11, front filter bores frame 3.0.12.1, scarfing cinder water injection system 3.1.1 consists of in rear filter bores frame 3.0.12.2 and the pipe, and wherein manage inner filtration strap self-cleaning system 3.1~3.4 by scarfing cinder filter cloth device 3.1 in the pipe, filter residue precipitation bucket 3.2, pulp water filtration tank 3.3 and deslagging bucket 3.4 form, wherein, the air inlet of blast machine 3.0.0 is communicated with the gas outlet of cooling system 2 with valve FM by pipeline GD; Its gas outlet is by the air inlet corresponding connection of pipeline GD with filtration system 3.0; Filter strap 3.0.1 and filtering under the strap driving 3.0.2 driving, advance and in traveling process, slip over around one group of filtration strap drive 3.0.3 and filter strap support wheel plate 3.0.7; Cleaning and filtering cloth apparatus 3.1 is installed in by groove lid 3.0.6 and filter lower groove 3.0.10 activity on the filter and plugs together and in the chamber that consists of in dust pelletizing system 3 contained filtration strap 3.0.1, the pipe, groove lid 3.0.6 medial surface and its direction are downward on the filtration strap support wheel plate 3.0.7 installation filter, and place the reverse side that filters strap 3.0.1 windward side; Pipe inner filtration cloth belt tensioner pulley 3.0.9 and be installed in the bottom of managing interior scarfing cinder sparge pipe and drive support 3.0.8, its upper end is installed in groove lid 3.0.6 inner face and sensing below on the filter, pipe inner filtration cloth belt tensioner pulley 3.0.9 is installed on its lower end, manage interior scarfing cinder water injection system 3.1.1 and place and filter strap 3.0.1 transmission attrition surface one side, be installed on the filter in the groove lid 3.0.6 and face down, and place the reverse side that filters strap 3.0.1 windward side; Filter bores frame 3.0.12 is installed in filter lower groove 3.0.10 and places and filters strap 3.0.1 windward side one side; Scarfing cinder water injection system 3.1.1 is communicated with the delivery port of supernatant water pump 3.3.1.1 and supernatant water pump 3.3.2.1 respectively by water pipe in the pipe; Filtering strap 3.0.1 passes groove lid 3.0.6 place on the filter and will be subject to being installed in and filter upper corresponding one group of strap sealing wheel support 3.0.5 and filter the slit rotation crush seal device that strap sealing pressing wheel 3.0.4 consists of; Filtering strap 3.0.1 passes and is filtered strap drive 3.0.3 on the filter after the groove lid 3.0.6 and is transferred to the outer cleaning and filtering cloth belting 4.1 of pipe and has got on; The edge that is provided with a seal closure MF.0 above the groove lid 3.0.6 on the filter be provided with the male tooth MF.0.1 of sealing just in time with filter on groove lid 3.0.6 band packing and the female groove 3.0.11 of sealing activity plug together; The filter lower groove 3.0.10 below side's of being taper, the vertex of a cone is downward, the vertex of a cone is opening and connects respectively separately a valve FM, the outlet of these two valve FM is communicated with corresponding filter residue precipitation bucket 3.2.1 and filter residue precipitation bucket 3.2.2 respectively, filter residue precipitation bucket 3.2.1 and filter residue precipitation bucket 3.2.2 are communicated with pulp water filtration tank 3.3.1 and pulp water filtration tank 3.3.2 respectively by valve FM respectively more successively, pulp water filtration tank 3.3.1 and pulp water filtration tank 3.3.2 are communicated with supernatant water pump 3.3.1.1 and supernatant water pump 3.3.2.1 respectively, and supernatant water pump 3.3.1.1 is connected with supernatant water pump 3.3.2.1 separately that institute's sparge pipe is connected with the nozzle of scarfing cinder water injection system 3.1.1 in each self-corresponding pipe respectively; The side of being, the below taper of filter residue precipitation bucket 3.2.1 and filter residue precipitation bucket 3.2.2, the vertex of a cone are closed up as circular open and are communicated with each self-corresponding valve FM, and the outlet of these valves FM that connects is exactly slag-drip opening; Pipeline GD with after valve FM is connected in series, is gone pulp water filtration tank 3.3.1 and pulp water filtration tank 3.3.2 are communicated with them again, be about to two towers and gang up into adjustable controlled water level balance system; The inside of filter residue precipitation bucket 3.2 is provided with precipitation dividing plate 3.2G; The inboard, pulp water inlet port place of pulp water filtration tank 3.3 is provided with channel plate 3.3Q and is provided with deflector 3.3R outside the port of export of channel plate 3.3Q, above pulp water inlet port passage, be provided with pulp water filtering frame 3.3M, pulp water filtering frame 3.3M is fixed on the inwall of pulp water filtration tank 3.3 and by passage and non-passage two parts and consists of, and filter packing 3.3N is concatenated into the multilayer pyramidal structure by connecting rod 3.3P and the vertex of a cone places on the passage of pulp water filtering frame 3.3M downwards actively.
Fig. 6 also illustrates dedusting and removing exhaust gas device flue of the present invention and filters strap self-cleaning system 4 outward and be comprised of pipe outer cleaning and filtering cloth apparatus 4.1, filter residue precipitation bucket 4.2, pulp water filtration tank 4.3 and deslagging bucket 4.4, wherein the outer cleaning and filtering cloth apparatus 4.1 of pipe is comprised of the outer scarfing cinder water injection system 4.1.1 of pipe, the outer filter residue sparge pipe of pipe and drive support 4.1.2, the outer filter cloth belt tensioner pulley 4.1.3 of pipe again, the carrier base of managing outer filter residue sparge pipe and drive support 4.1.2 is installed on the filter on the groove lid 3.0.6, and bracket head is installed with the outer filter cloth belt tensioner pulley 4.1.3 of pipe; The outer scarfing cinder water injection system 4.1.1 of pipe of one group of bull also has been installed on the outer filter residue sparge pipe of pipe and drive support 4.1.2, and fountain head is installed in respectively the both sides of filtering strap, and its water spraying direction faces toward the filtration cloth cover; Manage the outer cleaning and filtering cloth belting 4.1 below side's of being taper, the vertex of a cone downwards and be opening and affixed the valve FM of correspondence respectively, the port of export of these valves FM is communicated in the top of filter residue precipitation bucket 4.2, filter residue precipitation bucket 4.2 bottoms are communicated with pulp water filtration tank 4.3 bottoms by valve FM again, supernatant water pump 4.3.1 of configuration above pulp water filtration tank 4.3; Supernatant water pump 4.3.1 connects by the outer scarfing cinder water injection system 4.1.1 of water tube and tube; The also side's of the being taper of the bottom of filter residue precipitation bucket 4.2, the vertex of a cone are closed up as circular open and are communicated with respectively each self-corresponding valve FM, and the outlet of these valves FM that connects is exactly slag-drip opening; Pipeline GD with after each self-corresponding valve FM is connected in series, all is communicated with the bottom of pulp water filtration tank 3.3.1, pulp water filtration tank 3.3.2 and pulp water filtration tank 4.3 get up respectively with them again, namely between the three, forms the automatic control people and control adjustable water level balance system.
Fig. 8 and Fig. 9 illustrate multi-stage countercurrent immersion dedusting and removing exhaust gas system 5 that dedusting and removing exhaust gas device of the present invention configures is made of two-way arranged side by side the multi-stage countercurrent immersion dedusting and removing exhaust gas 5A of system and the multi-stage countercurrent immersion dedusting and removing exhaust gas 5B of system version from separately side, because of the multi-stage countercurrent immersion dedusting and removing exhaust gas 5A of system the same with the structure of the multi-stage countercurrent immersion dedusting and removing exhaust gas 5B of system, therefore only need explaining wherein, any one system gets final product, and needn't in stating, this segment table use again " A or B " to be distinguished, they are separately by multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0, hutch water device 6, tonic device 7, inter-stage blast machine 5.1, deslagging bucket 5.2 and purified gas chimney 5.3 consist of, wherein multi-stage countercurrent immersion removing exhaust gas reactive tank 5.0 is by No. 1 groove lid 5.4.1, No. 2 groove lid 5.4.2 and No. 1 cell body 5.4.3.1, No. 2 cell body 5.4.3.2 activity plugs together and consists of two independently seal chambers, corresponding two-stage dedusting and removing exhaust gas process, set inter-stage blast machine 5.1 air flues with two cavitys have been communicated with above two cavitys, in addition, open a through hole 5.5 according to on-the-spot truth suitable At The Height on the dividing plate of being separated by between two cavitys, the water channel between two cavitys has been communicated with; Control rate of water make-up and tonic amount according to the pH value of first order trough inner water position and tank liquor respectively with hutch water device 6 and tonic device 7 that the first order of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0 is communicated with; Blast machine 5.0.0 filters flue outward strap self-cleaning system 4 by pipeline GD gas outlet is communicated with No. 1 gas distribution balance pipe 5.0.1 of the afterbody groove of the tank liquor flow direction of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0, No. 1 gas distribution balance pipe 5.0.1 is communicated with one group of No. 3 gas pipe 5.0.3, and No. 1 gas distribution balance pipe 5.0.1 of connection and one group of No. 3 gas pipe 5.0.3 are installed in the medial surface and downwards of No. 1 groove lid 5.4.1 of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0; No. 2 gas distribution balance pipe 5.0.2 is communicated with one group of No. 4 gas pipe 5.0.4, and No. 2 gas distribution balance pipe 5.0.2 of connection and one group of No. 4 gas pipe 5.0.4 are installed in the medial surface and downwards of No. 2 grooves lid 5.4.2 of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0; Passage all gathers on the gas distribution pipe among No. 3 gas pipe 5.0.3 and No. 4 gas pipe 5.0.4; Purified gas chimney 5.3 is communicated with and opening upwards with the end of the first order groove that the tank liquor of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0 flows; Bottom at multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0 is provided with valve FM, and the outlet of valve FM is exactly slag-drip opening.
Figure 10 illustrates the present invention and adopts tubular type to carry the dedusting and removing exhaust gas device of the another kind configuration of ash discharge dust pelletizing system 33.0, and tubular type carries ash discharge dust pelletizing system 33.0 to carry vertical section 33.0.3Z of ash discharge deduster 33.0.3 and horizontal segment 33.0.3P to be communicated with successively institute by ash ejector 33.0.1, appendix steering knuckle 33.0.2, tubular type to form; Its appendix steering knuckle 33.0.2 is inserted in by the horizontal appendix steering knuckle moving casing 33.0.2.0 of " T " font and decides sleeve pipe 33.0.2.2 on the appendix steering knuckle and decide sleeve pipe 33.0.2.1 and consisted of down, the lower end of deciding sleeve pipe 33.0.2.1 under the appendix steering knuckle is communicated with ash ejector 33.0.1 by valve FM, decide sleeve pipe 33.0.2.2 upper end on its appendix steering knuckle and place tubular type to carry among the vertical section 33.0.3Z of ash discharge deduster 33.0.3, vertically the vertical body 33.0.3T bottom of section 33.0.3Z is done to be communicated with ash ejector 33.0.1 by valve FM after the circle closing in downwards of scarf mode; Carry the axis of vertically section 33.0.3Z of ash discharge deduster 33.0.3 as datum line take tubular type, repeat successively to install the return air plate washer 33.0.4 of mushroom-shaped and the wind-collecting cover 33.0.5 of straw hat shape according to the gas transmission distance, the tube wall periphery is provided with the oblique sheet group of stationary stream depositing dust 33.0.6 within the vertical body 33.0.3T of the vertical section of tubular type conveying ash discharge deduster 33.0.3 33.0.3Z with being separated by spacing; Tubular type carries the connecting bend 33.0.7 other end of the vertically section 33.0.3Z upper end of ash discharge deduster 33.0.3 to carry the air inlet of the horizontal segment 33.0.3P of ash discharge deduster 33.0.3 to be communicated with tubular type; The top of connecting bend 33.0.7 is provided with cleaning eye 33.0.8; Tubular type carries the horizontal segment 33.0.3P of ash discharge deduster 33.0.3 to flow protruding 33.0.9 by downwarp, on scratch stream protruding 33.0.10, ash bucket 33.0.11, stationary stream depositing dust tube sheet group 33.0.12, upper valve 33.0.13F, lower valve 33.0.14F, gas outlet 33.0.15 forms, wherein downwarp flow protruding 33.0.9 and on scratch stream protruding 33.0.10 axis perpendicular to the flue gas streamline, the geometry of their cross section is semicircle, their semicircle dome is protruding center streamline to smoke flow channels all, but the vertical line of their both more than half round hearts in side is not on a line, cross downwarp flow the vertical line in the protruding 33.0.9 semicircle center of circle with excessively on scratch the protruding 33.0.10 semicircle circle center line connecting of stream vertical line consist of on the horizontal direction apart from poor, thereby downwarp flow protruding 33.0.9 and on scratch the air flue that consists of of the protruding 33.0.10 of stream and force stationary stream depositing dust tube sheet group 33.0.12 in the air flow direction ash bucket 33.0.11, stationary stream depositing dust tube sheet group 33.0.12 is geometry by the cross section, greatly, the downward vertical installation of little consistent thin plate with ash bucket 33.0.11 inner chamber, and be separated with each other in its bucket of certain distance ground insertion, the affixed upper valve 33.0.13F in the outside lower end of ash bucket 33.0.11 and be communicated with lower valve 33.0.14F by a segment pipe GD, the port of export of lower valve 33.0.14F is communicated with electric screw ash ejector 33.0.16, and dusty gas carries the gas outlet 33.0.15 of ash discharge deduster 33.0.3 to flow out through tubular type; The dust of ash bucket 33.0.11 lower end institute aggregation drops among the electric screw ash ejector 33.0.16 after by upper valve 33.0.13F and lower valve 33.0.14F, is discharged by its ash discharging hole 33.0.17.
Figure 11, Figure 12 and Figure 13 illustrate the dedusting and removing exhaust gas device that the present invention adopts the another kind configuration of 15 collection cigarette systems 1.5 from side separately, 15 collection cigarette systems 1.5 are comprised of track 1.5.0, height adjusting system 1.5.1, front and back regulating system 1.5.2, the 1.5.3 of left and right adjusting system, 15 exhausting system 1.5.4, charging system 1.5.5, feed regulator 1.5.5.0, and an end of its track 1.5.0 and 15 cleaner head 1.5.4.5 directions is provided with position limiting pile 1.5.0.0; Its height adjusting system 1.5.1 is installed in each two centers intersection of both sides by the wheel 1.5.1.1 with electronic brake 1.5.1.0 and is flexibly connected into " X " font bearing rod 1.5.1.3 near-earth termination, the horizontal connecting rod 1.5.1.2 of eight symmetries connects respectively bearing rod 1.5.1.3, height regulating handle 1.5.1.4 is fixed in the external end head that height is regulated screw mandrel 1.5.1.5, height is regulated nut seat 1.5.1.6 and is connected to " X " font bearing rod 1.5.1.3 center, each two radicle of both sides are flexibly connected into " V " font and just regulate the affixed height adjusting of pole 1.5.1.7 silk braid seat 1.5.1.8, height is regulated screw mandrel 1.5.1.5 and is installed in wherein, each two on both sides are rotated loose joint 1.5.1.9 and are movably connected in bearing rod 1.5.1.3 middle part, highly regulate platform 1.5.1.10 each is fixed one and is flexibly connected load pole socket 1.5.1.11 and is flexibly connected with the termination of two bearing rod 1.5.1.3 respectively without the both sides of lever operated end, the termination of two other bearing rod 1.5.1.3 wheel 1.5.1.1 is installed respectively and below highly regulating platform 1.5.1.10, roll in the guide-track groove contact form; Before and after it regulating system 1.5.2 by the front and back of end band handle regulate screw mandrel 1.5.2.1 regulate nut seat 1.5.2.2 before and after being inserted in and be installed in before and after regulate platform 1.5.2.3 middle part front and back regulate among the nut seat 1.5.2.4, front and back regulate platform 1.5.2.3 be installed in be slidingly connected in the hook groove of highly regulating platform 1.5.1.10 form; The 1.5.3 of its left and right adjusting system is installed the middle part of left and right adjusting platform 1.5.3.1 by the left and right adjusting screw mandrel screw parts 1.5.3.2 of end band handle, left and right adjusting platform 1.5.3.1 with highly regulate platform 1.5.1.10 above in the guide-track groove rolling contact form; Its 15 exhausting system 1.5.4 is affixed by 15 motor 1.5.4.1 and 15 air exhauster 1.5.4.2 rotating shaft shaft couplings, the air inlet of 15 air exhauster 1.5.4.2 and 15 cleaner head 1.5.4.5 ring flanges are fastenedly connected rear fastened support 1.5.4.3 and are fastened on the left and right adjusting platform 1.5.3.1, regulate before and after left and right adjusting platform 1.5.3.1 is installed in be slidingly connected in the hook groove of platform 1.5.2.3 form, the air outlet 1.5.4.6 of 15 air exhauster 1.5.4.2 is connected with pipeline GD with bore in the mode of ring flange; Its charging system 1.5.5 uses hinge (1.5.4.4) active link by upper end and the hopper (1.5.5.3) of securing bracket (1.5.4.3) below the middle part at the end, the shaft seat 1.5.5.1 of feed regulator 1.5.5.0 is installed at another place in the upper end of securing bracket 1.5.4.3, wherein the movable hopper of installing is faced upward the wrench 1.5.5.4 that bows, face upward at hopper that affixed top wheel 1.5.5.2 contacts with outer lower side rolling at the bottom of the hopper 1.5.5.3 on the wrench 1.5.5.4 bent axle of bowing, at hopper 1.5.5.3 vibrating motor 1.5.5.5 is installed; The gas outlet of 15 cleaner head 1.5.4.5 directly is communicated with pipeline GD in the mode of ring flange; Its feed regulator 1.5.5.0 is installed in a side of the lower iron square hinge 1.5.4.4 in loading hopper 1.5.5.3 middle part and 15 cleaner head 1.5.4.5 directions, loading hopper face upward bow wrench 1.5.5.4 motion orientation by electric switch 1.5.1.0.1 whether press come with wheel 1.5.1.1 on the electronic brake 1.5.1.0 that is with of institute electric-linked, when the motion of facing upward the wrench 1.5.5.4 that bows when loading hopper makes the vertical ground of discharging opening 1.5.5.6 of hopper 1.5.5.3, loading hopper is faced upward the wrench 1.5.5.4 that bows and is made the electric switch 1.5.1.0.1 plugged of its interlock and make electric brake 1.5.1.0 be in braking state, the motion of facing upward the wrench 1.5.5.4 that bows when loading hopper makes the discharging opening 1.5.5.6 of hopper 1.5.5.3 kick up and during away from ground, loading hopper is faced upward the wrench 1.5.5.4 that bows and made the electric switch 1.5.1.0.1 deenergization of its interlock and make electric brake 1.5.1.0 be in non-braking state; Observe from top to bottom, the geometry of 15 cleaner head 1.5.4.5 is latter half of being square, first half is rounded, and be provided with the through hole of concentric up/down perforation at its position, center of circle, circular arch top away from projected square part is provided with the seam that disconnects fully, be rendered as thus fork-shaped, 15 cleaner head 1.5.4.5 are by crossover sub 1.5.4.5.1, hoisting ring 1.5.4.5.2, equal pressing plate 1.5.4.5.3, insulation board 1.5.4.5.4, carrying bolt 1.5.4.5.5, cavity plate 1.5.4.5.6, cavity of resorption plate 1.5.4.5.7 forms, cavity plate 1.5.4.5.6 is consistent with the plane geometric shape of cavity of resorption plate 1.5.4.5.7, being anterior is the flat thin forked plate of the circular port of little prong, the structure of 15 a suction method 1.5.4.5 is to be spliced up and down by cavity plate 1.5.4.5.6 and cavity of resorption plate .5.4.5.7, the circle fork inner via hole edge of two flat thin plates supports two plates and fix up with carrying bolt 1.5.4.5.5, the plate exterior rim of two chamber plates is incited somebody to action up and down two chamber plate outward flanges supports by same light sheet material and is fixed up up and down, namely by two planes and two sides consist of a four sides sealing up and down, lower plane is circle hole shape on the head of fork, and the fully penetrating and cavity of perforation end to end in the corresponding side of lower plane on corresponding side and the afterbody of fork, the corresponding side of circle hole shape becomes its suction inlet before the penetrating fork, and the identical heatproof insulation board 1.5.4.5.4 of geometry is installed on tiling ground respectively on the outer surface of cavity plate 1.5.4.5.6 and cavity of resorption plate 1.5.4.5.7.
In the technical measures of dedusting and removing exhaust gas device of the present invention, the feature of the dedusting and removing exhaust gas device of another kind of configuration be collection cigarette system 1 air-suction cover 1.1 air inlet non-contactly low coverage aim at the dust-laden pollution sources, the gas outlet of air-suction cover 1.1 directly is communicated with the air inlet of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0 with blast machine 5.0.0 by pipeline GD.
The Figure of description explanation
Figure of description is the present invention about the schematic diagram of the operation principle of the structure of dedusting and removing exhaust gas device and embodiment thereof, is not manuscript and the installation diagram of practice of construction.
Fig. 1 has described the technique connection diagram between each parts in the dedusting and removing exhaust gas device of the present invention, has described collection cigarette system, cooling system, dust pelletizing system, the flue that the present invention relates to and has filtered interdependence and the constituent relation that mutually restricts and operation logic relation between strap self-cleaning system, multi-stage countercurrent wet dedusting removing exhaust gas system, induction system, hutch water device and the tonic device outward.
Fig. 2, Fig. 3 are the schematic diagrames of uniting the structure of describing 10 collection cigarette systems 1.0 from different separately sides with Fig. 4.
Fig. 5 is the schematic diagram of describing the internal structure of air-suction cover rotation movable joint 1.4.
Fig. 6 is the schematic diagram of describing the structure of on-line continuous automatic ash removing dust pelletizing system 3.0.
Fig. 7 is the schematic diagram of describing the internal structure of filter residue precipitation bucket 3.2.
Fig. 8 and Fig. 9 are the schematic diagrames of describing the structure of multi-stage countercurrent wet dedusting removing exhaust gas system 5.
Figure 10 describes the schematic diagram that tubular type is carried the structure of ash discharge dust pelletizing system 33.0.
Figure 11, Figure 12 are the schematic diagrames of uniting the structure of describing 15 collection cigarette systems 1.5 from different separately sides with Figure 13.
System and component names table
1. collect cigarette system 1,10 collection cigarette systems 1.0, air-suction cover 1.1, cover body 1.1.1, all press dividing plate 1.1.2, check plate 1.1.3, barge board 1.1.4,12 exhausting systems 1.2, motor 1.2.1, rotor 1.2.2, non-return linkage 1.3, end aerofoil 1.3.1, switch 1.3.2, air-suction cover rotation movable joint 1.4, ash releasing tube 1.4.0, threeway 1.4.1, lower pellet shelves 1.4.2, pellet 1.4.3, hold-down screw 1.4.4, movable joint cover 1.4.5, packing suede 1.4.6, upper pellet shelves 1.4.7, nut 1.4.8.
2. cooling system 2.
3. on-line continuous automatic ash removing dust pelletizing system 3.0, on-line continuous automatic ash removing dust pelletizing system 3.0A, on-line continuous automatic ash removing dust pelletizing system 3.0B, filtration system 3.0, filtration system 3.0A, filtration system 3.0B, blast machine 3.0.0, filter strap 3.0.1, filter strap and drive 3.0.2, filter strap drive 3.0.3, filter strap sealing pressing wheel 3.0.4, filter strap sealing wheel support 3.0.5, groove lid 3.0.6 on the filter, filter strap support wheel plate 3.0.7, scarfing cinder sparge pipe and drive support 3.0.8 in the pipe, pipe inner filtration cloth belt tensioner pulley 3.0.9, filter lower groove 3.0.10, seal female groove 3.0.11, filter bores frame 3.0.12, front filter bores frame 3.0.12.1, rear filter bores frame 3.0.12.2, pipe inner filtration strap self-cleaning system 3.1~3.4, scarfing cinder filter cloth device 3.1 in the pipe, scarfing cinder water injection system 3.1.1 in the pipe, filter residue precipitation bucket 3.2, precipitation dividing plate 3.2G, filter residue precipitation bucket 3.2.1, filter residue precipitation bucket 3.2.2, pulp water filtration tank 3.3, channel plate 3.3Q, deflector 3.3R, pulp water filtering frame 3.3M, filter packing 3.3N, connecting rod 3.3P, pulp water filtration tank 3.3.1, supernatant water pump 3.3.1.1, pulp water filtration tank 3.3.2, supernatant water pump 3.3.2.1, deslagging bucket 3.4, pipe inner filtration strap self-cleaning system 3.1~3.4, pipe inner filtration strap self-cleaning system 3.1A~3.4A, pipe inner filtration strap self-cleaning system 3.1B~3.4B.
4. flue filters strap self-cleaning system 4, the outer cleaning and filtering cloth belting 4.1 of pipe, the outer scarfing cinder water injection system 4.1.1 of pipe, the outer filter residue sparge pipe of pipe and drive support 4.1.2, the outer filter cloth belt tensioner pulley 4.1.3 of pipe, filter residue precipitation bucket 4.2, pulp water filtration tank 4.3, supernatant water pump 4.3.1, deslagging bucket 4.4 outward.
5. multi-stage countercurrent immersion dedusting and removing exhaust gas system 5, multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank 5.0, blast machine 5.0.0, No. 1 gas distribution balance pipe 5.0.1, No. 2 gas distribution balance pipe 5.0.2, No. 3 gas pipe 5.0.3, No. 4 gas pipe 5.0.4, the multi-stage countercurrent immersion dedusting and removing exhaust gas 5A of system, the multi-stage countercurrent immersion dedusting and removing exhaust gas 5B of system, inter-stage blast machine 5.1, deslagging bucket 5.2, purified gas chimney 5.3, No. 1 groove lid 5.4.1, No. 2 groove lid 5.4.2, No. 1 cell body 5.4.3.1, No. 2 cell body 5.4.3.2, through hole 5.5.
6. tubular type is carried ash discharge dust pelletizing system 33.0, ash ejector 33.0.1, appendix steering knuckle 33.0.2, appendix steering knuckle moving casing 33.0.2.0, decide down sleeve pipe 33.0.2.1, upward decide sleeve pipe 33.0.2.2, tubular type is carried ash discharge deduster 33.0.3, vertical section 33.0.3Z, vertical body 33.0.3T, horizontal segment 33.0.3P, return air plate washer 33.0.4, wind-collecting cover 33.0.5, the oblique sheet group of stationary stream depositing dust 33.0.6, connecting bend 33.0.7, cleaning eye 33.0.8, protruding 33.0.9 is flowed in downwarp, on scratch stream protruding 33.0.10, ash bucket 33.0.11, stationary stream depositing dust tube sheet group 33.0.12, upper valve 33.0.13F, lower valve 33.0.14F, gas outlet 33.0.15, electric screw ash ejector 33.0.16, ash discharging hole 33.0.17.
7. hutch water device 6.
8. the tonic device 7.
9. pipeline GD, valve FM, seal closure MF.0, the public tooth MF.0.1 of sealing.
10.15 collection cigarette system 1.5, track 1.5.0, position limiting pile 1.5.0.0, height adjusting system 1.5.1, electric brake 1.5.1.0, electric switch 1.5.1.0.1, wheel 1.5.1.1, bearing rod 1.5.1.3, horizontal connecting rod 1.5.1.2, bearing rod 1.5.1.3, height regulating handle 1.5.1.4, height is regulated screw mandrel 1.5.1.5, height is regulated nut seat 1.5.1.6, height is regulated pole 1.5.1.7, height is regulated silk braid seat 1.5.1.8, rotate loose joint 1.5.1.9, highly regulate platform 1.5.1.10, be flexibly connected load pole socket 1.5.1.11, front and back regulating system 1.5.2, screw mandrel 1.5.2.1 is regulated in front and back, regulate nut seat 1.5.2.2 before and after being inserted in, platform 1.5.2.3 is regulated in front and back, nut seat 1.5.2.4 is regulated in front and back, the 1.5.3 of left and right adjusting system, left and right adjusting platform 1.5.3.1, left and right adjusting screw mandrel screw parts 1.5.3.2,15 exhausting system 1.5.4,15 motor 1.5.4.1,15 air exhauster 1.5.4.2, securing bracket 1.5.4.3, hinge 1.5.4.4,15 cleaner head 1.5.4.5, crossover sub 1.5.4.5.1, hoisting ring 1.5.4.5.2, equal pressing plate 1.5.4.5.3, insulation board 1.5.4.5.4, carrying bolt 1.5.4.5.5, cavity plate 1.5.4.5.6, cavity of resorption plate 1.5.4.5.7, air outlet 1.5.4.6, charging system 1.5.5, feed regulator 1.5.5.0, shaft seat 1.5.5.1, top wheel 1.5.5.2, hopper 1.5.5.3, loading hopper is faced upward the wrench 1.5.5.4 that bows, vibrating motor 1.5.5.5, discharging opening 1.5.5.6.
Major function of the present invention
1. present invention is directed at dust and device of pernicious gas two pollutants design in the flue gas, can finish the processing for the pollutant of two kinds of different states of matters, have physical dry and physics wet method and remove the arbitrarily function and the chemical function of removing waste gas of the footpath dust of grain;
2. dedusting theory of the present invention is to remove the large dust of particle diameter in the dust with physical dry first as far as possible, eliminates the well difficult especially minimum dust of particle diameter that captures of flying upward property, floatability with the physics wet method afterwards.So the dedusting theory has 2 major advantages, the one, the secondary fly-up of stopping dust pollutes, the 2nd, tackle the dry ash in the flue dust as far as possible, reduce the chemical reaction in the process of gathering dust as far as possible, reduce the product of chemical reaction and go out the quantity of slag, reduce follow-up environmental protection treatment operation, the removal function of not letting slip the small particle diameter dust simultaneously;
3. the present invention can remove cleanliness according to the dust in the flue gas and the regulation and control of noxious gas emission standard combination, makes facility of the present invention be under environmental protection index and the scientific and reasonable running status of economic indicator and moves, and has except cleanliness combinatorial regulation function;
4. the present invention can regulate and control its processing energy consumption according to the instant generation of pollutant in the production process, reach amount of pollutant when large, its disposal ability increases thereupon, the amount hour, then its disposal ability is constant and energy consumption reduces thereupon, reach the purpose of energy-conservation of consumption reduction, have the combinatorial regulation function for the treatment of capacity alignment processing energy consumption;
5. facility of the present invention can come the energy-conservation removal task of finishing according to the amount of pollutant size, can realize on-bne repair again, has the function of the on-bne repair that do not stop production;
6. filtration working face of the present invention can be incessantly with the move mode deashing, thoroughly stop the fast knot that flue gas cool-down dewfall in the conventional dry sack cleaner blocks filter cloth, thoroughly solve the problem of stifled filter and filter drops, have Hand scarf filtering material working face, can constantly keep filtering the function of optimum efficiency;
7. the tubular type among the present invention carries the ash discharge dust pelletizing system both to have dedusting function, has again the function of carrying gas and constantly ash discharge to stop to stop up;
8. the upper groove lid employing male and female groove tooth of multi-stage countercurrent dedusting and removing exhaust gas reactive tank of the present invention plugs together and adds the liquid Sealing Technology, all need not to press-fit sealing with screw, has the sealing function of plugging together, and namely reduces operation labour intensity, shortens working time, raises labour efficiency;
The structures of 15 collection cigarette systems 1.5 of the present invention have absorbing smoke dust, add furnace charge, the three-dimensional function of adjusting all around up and down.
The present invention can solve the stifled filter of filtration working face slagging scorification of existing similar technology with above-mentioned functions, operation energy consumption is large, dedusting is removing exhaust gas not, not dedusting of removing exhaust gas and cause a large amount of polygamy body refuses, except cleanliness is low, unstable, scarfing cinder labour intensity is large, the problems such as secondary dust is seriously polluted, and equipment is short-lived.
Itself has sealing for some bodies of heater in the reality; the exhaust opening of sealing body of heater directly can be communicated with the air inlet of multi-stage countercurrent dedusting and removing exhaust gas reactive tank with pipeline and blast machine such as the environment treating facility configuration that contains harmful gas for discharge dust-ladens such as protective atmosphere smelting furnace, Cremation Machine, so the device of configuration belongs to the scope of protection of present invention.
The concentration that contains before harmful gas treatment for some dust-ladens in the reality is not very high just, then can only adopt primary dust removing removing exhaust gas reactive tank can obtain the device configuration of Purge gas up to standard, belongs to equally the scope of protection of present invention.
The concrete situation that contains harmful gas for some dust-ladens in the reality, separately or part adopt dedusting and removing exhaust gas parts among the present invention can obtain the device configuration of Purge gas up to standard, all belong to the scope of protection of present invention.

Claims (7)

1. one kind contains cooling system (2), electric screw ash ejector (33.0.16), the dedusting and removing exhaust gas device of hutch water device (6) and tonic device (7), it is characterized in that the collection cigarette system that configures is 10 collection cigarette systems (1.0), it is by air-suction cover (1.1), 12 exhausting systems (1.2), non-return linkage (1.3) and air-suction cover rotation movable joint (1.4) connection form, wherein air-suction cover (1.1) is by cover body (1.1.1), all press dividing plate (1.1.2), check plate (1.1.3), barge board (1.1.4) forms, its cover body (1.1.1) is the semicylinder body, its axis is up settled by ground, the opposing face of the air-breathing working face of cover body (1.1.1) is provided with the gas outlet, cover body (1.1.1) inside is provided with and all presses dividing plate (1.1.2), all press dividing plate (1.1.2) for be installed in one group of thin strip-plate of cover body (1.1.1) inner chamber by the requirement of hydrodynamics pressure distribution rule, per two rotors (1.2.2) of all pressing the gas channel that consists of between the dividing plate (1.1.2) all to face toward 12 exhausting systems (1.2), barge board 1.1.4 divides two both sides that are mounted on respectively the opposing face of the air-breathing working face of cover body 1.1.1, the rotor (1.2.2) of 12 exhausting systems (1.2) is driven by motor (1.2.1), and the startup of motor (1.2.1) operation is controlled by non-return linkage (1.3) with termination; Non-return linkage (1.3) is pressed Action of Gravity Field by louvre type and sagging only aerofoil (1.3.1), the switch (1.3.2) of motor (1.2.1) consists of, the stripe board of ending aerofoil (1.3.1) is connected in cover body 1.1.1 inboard by loose-leaf, its stripe board face can be turned to naturally by Action of Gravity Field hang, switch (1.3.2) also is installed on the position that cover body (1.1.1) is inboard with only aerofoil (1.3.1) presses mutually, the control contact of trip switch (1.3.2) when ending aerofoil (1.3.1) and under the effect of air-flow, becoming non-hang by hang and connect the circuit of motor (1.2.1), airless to get back to hang as the time spent be the control contact of clamping switch (1.3.2) and disconnect the circuit of motor (1.2.1); The gas outlet of cover body (1.1.1) is communicated with by the air inlet of pipeline (GD) with air-suction cover rotation movable joint (1.4); Air-suction cover rotation movable joint (1.4) is by ash releasing tube (1.4.0), threeway (1.4.1), lower pellet shelves (1.4.2), pellet (1.4.3), hold-down screw (1.4.4), movable joint cover (1.4.5), packing suede (1.4.6), upper pellet shelves (1.4.7), nut (1.4.8), valve (FM) consists of, the port that the centre of wherein threeway (1.4.1) is provided with ring flange is air inlet, the port that its installation direction is downward, serving as ash releasing tube (1.4.0) and valve (FM) is communicated with, the outlet of valve (FM) is ash hole, and the threaded port of another pipe peripheral hardware is the gas outlet; In addition, the inwall place, cover two ends of its movable joint cover (1.4.5) is equipped with pellet position and lower pellet position, and is provided with ring flange at the one end; During assembling air-suction cover rotation movable joint (1.4), use first the fastening lower pellet shelves (1.4.2) of threeway (1.4.1) outside the epimere pipe that are installed in of hold-down screw (1.4.4), load onto pellet (1.4.3), put inside pipe wall and loaded the movable joint cover (1.4.5) that end encapsulant packing suede (1.4.6) and that will be provided with ring flange places the top, pellet (1.4.3) is installed in upper pellet position at movable joint cover (1.4.5) upper port place, installing pellet shelves (1.4.7) presses pellet (1.4.3) again, use at last nut (1.4.8) that upper pellet shelves (1.4.7) are fastening, its gas outlet is communicated with the air inlet of cooling system (2) by pipeline (GD), the ash hole docking of the valve (FM) that lime-ash shipment sack is communicated with ash releasing tube (1.4.0) below.
2. described dedusting and removing exhaust gas device according to claim 1, it is characterized in that the dust pelletizing system that configures is on-line continuous automatic ash removing dust pelletizing system (3.0), it is made of filtration system (3.0) and pipe inner filtration strap self-cleaning system (3.1~3.4), wherein filtration system (3.0) is made of the version of two-way arranged side by side the identical filtration system of internal structure (3.0A) and filtration system (3.0B), ((3.1B~3.4B) consists of the version of two-way arranged side by side to pipe inner filtration strap self-cleaning system (3.1~3.4) for 3.1A~3.4A) and pipe inner filtration strap self-cleaning system by the identical pipe inner filtration strap self-cleaning system of internal structure, because of on-line continuous automatic ash removing dust pelletizing system (3.0A) the same with the structure of on-line continuous automatic ash removing dust pelletizing system (3.0B), any one system gets final product therefore only need explain wherein, and needn't use " A or B " to be distinguished in this segment table is stated again; Filtration system (3.0) is by blast machine (3.0.0), filter strap (3.0.1), filter strap and drive (3.0.2), filter strap drive (3.0.3), filter strap sealing pressing wheel (3.0.4), filter strap sealing wheel support (3.0.5), groove lid (3.0.6) on the filter, filter strap support wheel plate (3.0.7), scarfing cinder sparge pipe and drive support (3.0.8) in the pipe, pipe inner filtration cloth belt tensioner pulley (3.0.9), filter lower groove (3.0.10), seal female groove (3.0.11), front filter bores frame (3.0.12.1), scarfing cinder water injection system (3.1.1) consists of in rear filter bores frame (3.0.12.2) and the pipe, and wherein manage inner filtration strap self-cleaning system (3.1~3.4) by scarfing cinder filter cloth device (3.1) in the pipe, filter residue precipitation bucket (3.2), pulp water filtration tank (3.3) and deslagging bucket (3.4) form, wherein, the air inlet of blast machine (3.0.0) is communicated with the gas outlet of valve (FM) with cooling system (2) by pipeline (GD); Its gas outlet is by the air inlet corresponding connection of pipeline (GD) with filtration system (3.0); Filter strap (3.0.1) and filtering under strap driving (3.0.2) driving, advance and in traveling process, slip over around one group of filtration strap drive (3.0.3) and filter strap support wheel plate (3.0.7); Cleaning and filtering cloth apparatus (3.1) is installed in by groove lid (3.0.6) on the filter and plugs together with filter lower groove (3.0.10) activity and in the chamber that consists of in the contained filtration strap of dust pelletizing system (3) (3.0.1), the pipe, groove lid (3.0.6) medial surface and its direction are downward on filtration strap support wheel plate (3.0.7) the installation filter, and place the reverse side that filters strap (3.0.1) windward side; Pipe inner filtration cloth belt tensioner pulley (3.0.9) and be installed in the bottom of managing interior scarfing cinder sparge pipe and drive support (3.0.8), its upper end is installed in groove lid (3.0.6) inner face and sensing below on the filter, pipe inner filtration cloth belt tensioner pulley (3.0.9) is installed on its lower end, manage interior scarfing cinder water injection system (3.1.1) and place and filter strap (3.0.1) transmission attrition surface one side, be installed on the filter in the groove lid (3.0.6) and face down, and place the reverse side that filters strap (3.0.1) windward side; Filter bores frame (3.0.12) is installed in filter lower groove (3.0.10) and places and filters strap (3.0.1) windward side one side; Scarfing cinder water injection system (3.1.1) is communicated with the delivery port of supernatant water pump (3.3.1.1) and supernatant water pump (3.3.2.1) respectively by water pipe in the pipe; Filtering strap (3.0.1) passes groove lid (3.0.6) on the filter and locates will to be subject to being installed in and filter upper corresponding one group of strap sealing wheel support (3.0.5) and filter the slit that strap sealing pressing wheel (3.0.4) consists of and rotate the crush seal device; Filtering strap (3.0.1) passes on the filter groove lid (3.0.6) and is filtered afterwards strap drive (3.0.3) and is transferred to the outer cleaning and filtering cloth belting of pipe (4.1) and has got on; The top of groove lid (3.0.6) is provided with a seal closure (MF.0) on filter; The edge of seal closure (MF.0) be provided with the male tooth of sealing (MF.0.1) just in time with filter on groove lid (3.0.6) upper band packing and the activity of sealing female groove (3.0.11) plug together; Filter lower groove (3.0.10) the below side's of being taper, the vertex of a cone is downward, the vertex of a cone is opening and connects respectively separately a valve (FM), the outlet of these two valves (FM) is communicated with corresponding filter residue precipitation bucket (3.2.1) and filter residue precipitation bucket (3.2.2) respectively, filter residue precipitation bucket (3.2.1) and filter residue precipitation bucket (3.2.2) are communicated with pulp water filtration tank (3.3.1) and pulp water filtration tank (3.3.2) respectively by valve (FM) respectively more successively, pulp water filtration tank (3.3.1) and pulp water filtration tank (3.3.2) are communicated with supernatant water pump (3.3.1.1) and supernatant water pump (3.3.2.1) respectively, and supernatant water pump (3.3.1.1) is connected 3.3.2.1 with the supernatant water pump) be connected with the nozzle of scarfing cinder water injection system (3.1.1) in each self-corresponding pipe respectively by institute's sparge pipe separately; The side of being, the below taper of filter residue precipitation bucket (3.2.1) and filter residue precipitation bucket (3.2.2), the vertex of a cone are closed up as circular open and are communicated with each self-corresponding valve (FM), and the outlet of these valves (FM) that connect is exactly slag-drip opening; Pipeline (GD) with after valve (FM) is connected in series, is gone pulp water filtration tank (3.3.1) and pulp water filtration tank (3.3.2) are communicated with them again, be about to two towers and gang up into adjustable controlled water level balance system; The inside of filter residue precipitation bucket (3.2) is provided with precipitation dividing plate (3.2G); The inboard, pulp water inlet port place of pulp water filtration tank (3.3) is provided with channel plate (3.3Q) and is provided with deflector (3.3R) outside the port of export of channel plate (3.3Q), above pulp water inlet port passage, be provided with pulp water filtering frame (3.3M), pulp water filtering frame (3.3M) is fixed on the inwall of pulp water filtration tank (3.3) and by passage and non-passage two parts and consists of, and filter packing (3.3N) is concatenated into the multilayer pyramidal structure by connecting rod (3.3P) and the vertex of a cone places on the passage of pulp water filtering frame (3.3M) downwards actively.
3. described dedusting and removing exhaust gas device according to claim 1, it is characterized in that its flue filters strap self-cleaning system (4) outward by pipe outer cleaning and filtering cloth apparatus (4.1), filter residue precipitation bucket (4.2), pulp water filtration tank (4.3) and deslagging bucket (4.4) form, wherein the outer cleaning and filtering cloth apparatus of pipe (4.1) is again by pipe outer scarfing cinder water injection system (4.1.1), manage outer filter residue sparge pipe and drive support (4.1.2), managing outer filter cloth belt tensioner pulley (4.1.3) forms, the carrier base of managing outer filter residue sparge pipe and drive support (4.1.2) is installed on the filter on the groove lid (3.0.6), and bracket head is installed with pipe outer filter cloth belt tensioner pulley (4.1.3); The outer scarfing cinder water injection system (4.1.1) of pipe of one group of bull also has been installed on the outer filter residue sparge pipe of pipe and drive support (4.1.2), and fountain head is installed in respectively the both sides of filtering strap, and its water spraying direction faces toward the filtration cloth cover; Manage outer cleaning and filtering cloth belting (4.1) the below side's of being taper, the vertex of a cone downwards and be opening and affixed the valve (FM) of correspondence respectively, the port of export of these valves (FM) is communicated in the top of filter residue precipitation bucket (4.2), filter residue precipitation bucket (4.2) bottom is communicated with pulp water filtration tank (4.3) bottom by valve (FM) again, at pulp water filtration tank (a 4.3) top configuration supernatant water pump (4.3.1); Supernatant water pump (4.3.1) connects by the outer scarfing cinder water injection system (4.1.1) of water tube and tube; The also side's of being taper of bottom of filter residue precipitation bucket (4.2), the vertex of a cone are closed up as circular open and are communicated with respectively each self-corresponding valve (FM), and the outlet of these valves (FM) that connect is exactly slag-drip opening; With pipeline (GD) with after each self-corresponding valve (FM) is connected in series, respectively the bottom of pulp water filtration tank (3.3.1), pulp water filtration tank (3.3.2) and pulp water filtration tank (4.3) all is communicated with to get up with them again, namely between the three, forms the automatic control people and control adjustable water level balance system.
4. described dedusting and removing exhaust gas device according to claim 1, it is characterized in that its multi-stage countercurrent immersion dedusting and removing exhaust gas system (5) is made of the version of two-way arranged side by side multi-stage countercurrent immersion dedusting and removing exhaust gas system (5A) and multi-stage countercurrent immersion dedusting and removing exhaust gas system (5B), because of multi-stage countercurrent immersion dedusting and removing exhaust gas system (5A) the same with the structure of multi-stage countercurrent immersion dedusting and removing exhaust gas system (5B), therefore only need explaining wherein, any one system gets final product, and needn't in stating, this segment table use again " A or B " to be distinguished, they are separately by multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0), hutch water device (6), tonic device (7), inter-stage blast machine (5.1), deslagging bucket (5.2) and purified gas chimney (5.3) consist of, wherein multi-stage countercurrent immersion removing exhaust gas reactive tank (5.0) covers (5.4.1) by No. 1 groove, No. 2 groove lids (5.4.2) and No. 1 cell bodies (5.4.3.1), No. 2 cell bodies (5.4.3.2) activity plugs together and consists of two independently seal chambers, corresponding two-stage dedusting and removing exhaust gas process, a set inter-stage blast machine (5.1) has been communicated with the air flue of two cavitys above two cavitys, in addition, open a through hole (5.5) according to on-the-spot truth suitable At The Height on the dividing plate of being separated by between two cavitys, the water channel between two cavitys has been communicated with; The hutch water device (6) and the tonic device (7) that are communicated with the first order of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0) are controlled rate of water make-up and tonic amount according to the pH value of chopped-off head trough inner water position and tank liquor respectively; Blast machine (5.0.0) filters flue outward strap self-cleaning system (4) by pipeline (GD) gas outlet is communicated with No. 1 gas distribution balance pipe (5.0.1) of the afterbody groove of the tank liquor flow direction of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0), No. 1 gas distribution balance pipe (5.0.1) is communicated with one group of No. 3 gas pipe (5.0.3), and No. 1 gas distribution balance pipe (5.0.1) of connection and one group of No. 3 gas pipe (5.0.3) are installed in the medial surface and downwards of No. 1 groove lid (5.4.1) of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0); No. 2 gas distribution balance pipes (5.0.2) are communicated with one group of No. 4 gas pipe (5.0.4), and No. 2 gas distribution balance pipes (5.0.2) of connection and one group of No. 4 gas pipe (5.0.4) are installed in the medial surface and downwards of No. 2 grooves lids (5.4.2) of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0); Passage all gathers on the gas distribution pipe in No. 3 gas pipes (5.0.3) and No. 4 gas pipes (5.0.4); Purified gas chimney (5.3) is communicated with and opening upwards with the end of the first order groove that the tank liquor of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0) flows; Be provided with valve (FM) in the bottom of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0), the outlet of valve (FM) is exactly slag-drip opening.
5. described dedusting and removing exhaust gas device according to claim 1, the feature of the dedusting and removing exhaust gas device of another kind of configuration is that its adopts tubular type to carry ash discharge dust pelletizing system (33.0), and it carries vertical section (33.0.3Z) of ash discharge deduster (33.0.3) and horizontal segment (33.0.3P) to be communicated with successively by ash ejector (33.0.1), appendix steering knuckle (33.0.2), tubular type to form; Its appendix steering knuckle (33.0.2) is inserted in by the horizontal appendix steering knuckle moving casing (33.0.2.0) of " T " font to be decided sleeve pipe (33.0.2.2) and decides sleeve pipe (33.0.2.1) and consisted of down on the appendix steering knuckle, the lower end of deciding sleeve pipe (33.0.2.1) under the appendix steering knuckle is communicated with ash ejector (33.0.1) by valve (FM), decide sleeve pipe (33.0.2.2) upper end on its appendix steering knuckle and place tubular type to carry among vertical section (33.0.3Z) of ash discharge deduster (33.0.3), vertically vertical body (33.0.3T) bottom of section (33.0.3Z) is done to be communicated with ash ejector (33.0.1) by valve (FM) after the circle closing in downwards of scarf mode; Carry the axis of vertically section (33.0.3Z) of ash discharge deduster (33.0.3) as datum line take tubular type, repeat successively to install the return air plate washer (33.0.4) of mushroom-shaped and the wind-collecting cover (33.0.5) of straw hat shape according to the gas transmission distance, the tube wall periphery is provided with the oblique sheet group of stationary stream depositing dust (33.0.6) within the vertical body (33.0.3T) of the vertical section of tubular type conveying ash discharge deduster (33.0.3) (33.0.3Z) with being separated by spacing; Tubular type carries connecting bend (33.0.7) other end of vertically section (33.0.3Z) upper end of ash discharge deduster (33.0.3) to carry the air inlet of the horizontal segment (33.0.3P) of ash discharge deduster (33.0.3) to be communicated with tubular type; The top of connecting bend (33.0.7) is provided with cleaning eye (33.0.8); Tubular type carries the horizontal segment (33.0.3P) of ash discharge deduster (33.0.3) by downwarp stream protruding (33.0.9), on scratch stream protruding (33.0.10), ash bucket (33.0.11), stationary stream depositing dust tube sheet group (33.0.12), upper valve (33.0.13F), lower valve (33.0.14F), (33.0.15) forms in the gas outlet, wherein downwarp stream protruding (33.0.9) with on scratch the axis of stream protruding (33.0.10) perpendicular to the flue gas streamline, the geometry of their cross section is semicircle, their semicircle dome is protruding center streamline to smoke flow channels all, but the vertical line of their both more than half round hearts in side is not on a line, cross the vertical line in downwarp stream protruding (33.0.9) semicircle center of circle with excessively on scratch stream protruding (33.0.10) semicircle circle center line connecting vertical line consist of on the horizontal direction apart from poor, thereby downwarp stream protruding (33.0.9) with on scratch air flue that stream protruding (33.0.10) consists of and force stationary stream depositing dust tube sheet group (33.0.12) in the air flow direction ash bucket (33.0.11), stationary stream depositing dust tube sheet group (33.0.12) is geometry by the cross section, greatly, the downward vertical installation of consistent thin plate of little and ash bucket (33.0.11) inner chamber, and be separated with each other in its bucket of certain distance ground insertion, the affixed upper valve in the outside lower end of ash bucket (33.0.11) (33.0.13F) and be communicated with lower valve (33.0.14F) by a segment pipe (GD), the port of export of lower valve (33.0.14F) is communicated with electric screw ash ejector (33.0.16), and dusty gas carries give vent to anger (33.0.15) of ash discharge deduster (33.0.3) to flow out through tubular type; The dust of ash bucket (33.0.11) lower end institute aggregation drops in the electric screw ash ejector (33.0.16) after by upper valve (33.0.13F) and lower valve (33.0.14F), is discharged by its ash discharging hole (33.0.17).
6. according to claim 1 to one of 5 described dedusting and removing exhaust gas devices, the collection cigarette system that the dedusting and removing exhaust gas device of another kind of configuration adopts is 15 collection cigarette systems (1.5), it is characterized in that it is by track (1.5.0), height adjusting system (1.5.1), front and back regulating system (1.5.2), left and right adjusting system (1.5.3), 15 exhausting systems (1.5.4), charging system (1.5.5), feed regulator (1.5.5.0) forms, and its track (1.5.0) is provided with position limiting pile (1.5.0.0) with an end of 15 cleaner head (1.5.4.5) direction; Its height adjusting system (1.5.1) is installed in each two centers intersection of both sides by the wheel (1.5.1.1) with electronic brake (1.5.1.0) and is flexibly connected into " X " font bearing rod (1.5.1.3) near-earth termination, the horizontal connecting rod (1.5.1.2) of eight symmetries connects respectively bearing rod (1.5.1.3), height regulating handle (1.5.1.4) is fixed in the external end head that height is regulated screw mandrel (1.5.1.5), height is regulated nut seat (1.5.1.6) and is connected to " X " font bearing rod (1.5.1.3) center, each two radicle of both sides are flexibly connected into " V " font and just regulate the affixed height adjusting of pole (1.5.1.7) silk braid seat (1.5.1.8), height is regulated screw mandrel (1.5.1.5) and is installed in wherein, each two on both sides are rotated loose joint (1.5.1.9) and are movably connected in bearing rod (1.5.1.3) middle part, highly regulate platform (1.5.1.10) each is fixed one and is flexibly connected load pole socket (1.5.1.11) and is flexibly connected with the termination of two bearing rods (1.5.1.3) respectively without the both sides of lever operated end, the termination of two other bearing rod (1.5.1.3) wheel (1.5.1.1) is installed respectively and below highly regulating platform (1.5.1.10) in the guide-track groove rolling contact form; Before and after it regulating systems (1.5.2) by the front and back of end band handle regulate screw mandrels (1.5.2.1) regulate nut seat (1.5.2.2) before and after being inserted in and be installed in before and after regulate platforms (1.5.2.3) middle part front and back regulate in the nut seats (1.5.2.4), front and back regulate platforms (1.5.2.3) be installed in be slidingly connected in the hook groove of highly regulating platform (1.5.1.10) form; The middle part of left and right adjusting platforms (1.5.3.1) is installed by its left and right adjusting system (1.5.3) by the left and right adjusting screw mandrel screw parts (1.5.3.2) of end band handle, left and right adjusting platform (1.5.3.1) with highly regulate platform (1.5.1.10) above in the guide-track groove rolling contact form; Its 15 exhausting system (1.5.4) is affixed by 15 motor (1.5.4.1) and 15 air exhausters (1.5.4.2) rotating shaft shaft coupling, the air inlet of 15 air exhausters (1.5.4.2) and 15 cleaner head (1.5.4.5) ring flange are fastenedly connected rear fastened support (1.5.4.3) and are fastened on the left and right adjusting platform (1.5.3.1), regulate before and after left and right adjusting platform (1.5.3.1) is installed in be slidingly connected in the hook groove of platforms (1.5.2.3) form, the air outlet (1.5.4.6) of 15 air exhausters (1.5.4.2) is connected with pipeline (GD) with bore in the mode of ring flange; Its charging system (1.5.5) is used hinge (1.5.4.4) active link by upper end and the hopper (1.5.5.3) of securing bracket (1.5.4.3) below the middle part at the end, the shaft seat (1.5.5.1) of feed regulator (1.5.5.0) is installed at another place in the upper end of securing bracket (1.5.4.3), wherein the movable hopper of installing is faced upward the wrench of bowing (1.5.5.4), face upward at hopper that affixed top wheel (1.5.5.2) contacts with the rolling of hopper (1.5.5.3) outer lower side, the end on the wrench of bowing (1.5.5.4) bent axle, at hopper (1.5.5.3) vibrating motor (1.5.5.5) is installed; The gas outlet of 15 cleaner head (1.5.4.5) directly is communicated with pipeline (GD) in the mode of ring flange; Its feed regulator (1.5.5.0) is installed in a side of the lower iron square hinge (1.5.4.4) in loading hopper (1.5.5.3) middle part and 15 cleaner head (1.5.4.5) direction, loading hopper face upward the wrench of bowing (1.5.5.4) motion orientation by electric switch (1.5.1.0.1) whether press come with wheel (1.5.1.1) on institute's electronic brake of being with (1.5.1.0) electric-linked, when the motion of facing upward the wrench of bowing (1.5.5.4) when loading hopper makes the vertical ground of discharging opening (1.5.5.6) of hopper (1.5.5.3), loading hopper is faced upward the wrench of bowing (1.5.5.4) and is made electric switch (1.5.1.0.1) plugged of its interlock and make electric brake (1.5.1.0) be in braking state, the motion of facing upward the wrench of bowing (1.5.5.4) when loading hopper makes the discharging opening (1.5.5.6) of hopper (1.5.5.3) kick up and during away from ground, loading hopper is faced upward the wrench of bowing (1.5.5.4) and made electric switch (1.5.1.0.1) deenergization of its interlock and make electric brake (1.5.1.0) be in non-braking state; Observe from top to bottom, the geometry of 15 cleaner head (1.5.4.5) is latter half of being square, first half is rounded, and be provided with the through hole of concentric up/down perforation at its position, center of circle, circular arch top away from projected square part is provided with the seam that disconnects fully, be rendered as thus fork-shaped, 15 cleaner head (1.5.4.5) are by crossover sub (1.5.4.5.1), hoisting ring (1.5.4.5.2), equal pressing plate (1.5.4.5.3), insulation board (1.5.4.5.4), carrying bolt (1.5.4.5.5), cavity plate (1.5.4.5.6), cavity of resorption plate (1.5.4.5.7) forms, cavity plate (1.5.4.5.6) is consistent with the plane geometric shape of cavity of resorption plate (1.5.4.5.7), being anterior is the flat thin forked plate of the circular port of little prong, the structure of 15 suction method heads (1.5.4.5) is to be spliced up and down by cavity plate (1.5.4.5.6) and cavity of resorption plate (1.5.4.5.7), the circle fork inner via hole edge of two flat thin plates supports two plates and fix up with carrying bolt (1.5.4.5.5), the plate exterior rim of two chamber plates is incited somebody to action up and down two chamber plate outward flanges supports by same light sheet material and is fixed up up and down, namely two planes and two sides consist of a four sides sealing up and down, lower plane is circle hole shape on the head of fork, and the fully penetrating and cavity of perforation end to end in the corresponding side of lower plane on corresponding side and the afterbody of fork, the corresponding side of circle hole shape becomes its suction inlet before the penetrating fork, and the identical heatproof insulation board (1.5.4.5.4) of geometry is installed on tiling ground respectively on the outer surface of cavity plate (1.5.4.5.6) and cavity of resorption plate (1.5.4.5.7).
7. described dedusting and removing exhaust gas device according to claim 1, the feature of the dedusting and removing exhaust gas device of another kind of configuration be collection cigarette system (1) air-suction cover (1.1) air inlet non-contactly low coverage aim at the dust-laden pollution sources, the gas outlet of air-suction cover (1.1) directly is communicated with the air inlet of multi-stage countercurrent immersion dedusting and removing exhaust gas reactive tank (5.0) with blast machine (5.0.0) by pipeline (GD).
CN2012101032049A 2012-04-09 2012-04-09 Dust removing and waste gas removing apparatus Pending CN103071352A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106139756A (en) * 2016-09-08 2016-11-23 衢州乐创节能科技有限公司 A kind of runner type smoke filtration purifier
CN106474851A (en) * 2016-08-20 2017-03-08 苏州舒跃碳吸附剂有限公司 A kind of coal-burning utilities cleaner
CN108854389A (en) * 2018-07-17 2018-11-23 合肥霞康电子商务有限公司 A kind of boiler exhaust gas processing unit
CN110216402A (en) * 2019-06-24 2019-09-10 许翠英 A kind of welding system for cleaning fume and its processing method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57204219A (en) * 1981-06-10 1982-12-14 Hitachi Ltd Apparatus for treating combustion exhaust gas of boiler
JPH04141284A (en) * 1990-10-03 1992-05-14 Mitsubishi Heavy Ind Ltd Treatment of ash collected by dust collector
JP2001212430A (en) * 2000-02-03 2001-08-07 Nkk Corp Method for treating waste gases of waste incineration furnace and equipment for the same
CN1970447A (en) * 2005-11-23 2007-05-30 中国石油天然气股份有限公司 Process for ammonia method desulfurization of fume and by-producing ammonium sulfite
CN201122061Y (en) * 2007-10-09 2008-09-24 魏春水 High temperature flue gas comprehensive processing equipment
CN101462766A (en) * 2007-12-19 2009-06-24 贵阳铝镁设计研究院 Technique for cooling titanic chloride burner gas
CN101884873A (en) * 2010-06-30 2010-11-17 邵波 Process and facility for dedusting and removing exhaust gas

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57204219A (en) * 1981-06-10 1982-12-14 Hitachi Ltd Apparatus for treating combustion exhaust gas of boiler
JPH04141284A (en) * 1990-10-03 1992-05-14 Mitsubishi Heavy Ind Ltd Treatment of ash collected by dust collector
JP2001212430A (en) * 2000-02-03 2001-08-07 Nkk Corp Method for treating waste gases of waste incineration furnace and equipment for the same
CN1970447A (en) * 2005-11-23 2007-05-30 中国石油天然气股份有限公司 Process for ammonia method desulfurization of fume and by-producing ammonium sulfite
CN201122061Y (en) * 2007-10-09 2008-09-24 魏春水 High temperature flue gas comprehensive processing equipment
CN101462766A (en) * 2007-12-19 2009-06-24 贵阳铝镁设计研究院 Technique for cooling titanic chloride burner gas
CN101884873A (en) * 2010-06-30 2010-11-17 邵波 Process and facility for dedusting and removing exhaust gas

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106474851A (en) * 2016-08-20 2017-03-08 苏州舒跃碳吸附剂有限公司 A kind of coal-burning utilities cleaner
CN106139756A (en) * 2016-09-08 2016-11-23 衢州乐创节能科技有限公司 A kind of runner type smoke filtration purifier
CN108854389A (en) * 2018-07-17 2018-11-23 合肥霞康电子商务有限公司 A kind of boiler exhaust gas processing unit
CN110216402A (en) * 2019-06-24 2019-09-10 许翠英 A kind of welding system for cleaning fume and its processing method
CN110216402B (en) * 2019-06-24 2020-12-01 茂裕环保科技南通有限公司 Welding flue gas purification treatment system and treatment method thereof

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