CN206996206U - A kind of waste incineration activated carbon mixing jetting device - Google Patents

A kind of waste incineration activated carbon mixing jetting device Download PDF

Info

Publication number
CN206996206U
CN206996206U CN201720576413.3U CN201720576413U CN206996206U CN 206996206 U CN206996206 U CN 206996206U CN 201720576413 U CN201720576413 U CN 201720576413U CN 206996206 U CN206996206 U CN 206996206U
Authority
CN
China
Prior art keywords
mozzle
activated carbon
shower nozzle
waste incineration
jetting device
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.)
Active
Application number
CN201720576413.3U
Other languages
Chinese (zh)
Inventor
骆毅力
骆的
杨伦洲
杨大利
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.)
HERREL ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd
Original Assignee
HERREL ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by HERREL ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd filed Critical HERREL ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd
Priority to CN201720576413.3U priority Critical patent/CN206996206U/en
Application granted granted Critical
Publication of CN206996206U publication Critical patent/CN206996206U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

Originally it is new to relate to a kind of waste incineration activated carbon mixing jetting device, including mozzle, jet pipe, shower nozzle, incubation cavity and electric heating tube, the front end and end of mozzle are all provided with flange, and water conservancy diversion pipe end is connected with each other by flange with shower front end by flange, jet pipe is in chilling tower, and front end is located at outside extremely cold tower and connected with shower nozzle, incubation cavity includes cavity wall and warming plate, electric heating tube at least one, it is coated on around mozzle axis outside mozzle, and electric heating tube and mozzle both ends end distance between the surface are 1/6-the 1/4 of mozzle effective length.Originally it is new activated carbon transfer pipeline effectively to be protected, avoid spraying clogging caused by the factors such as the temperature difference cause activated carbon bonding etc., also flexibly the spray direction of activated carbon can be regulated and controled simultaneously, and activated carbon spray area coverage is favorably improved, effectively reduce material loss and enhance the tail gas clean-up operating efficiency of activated carbon.

Description

A kind of waste incineration activated carbon mixing jetting device
Technical field
A kind of exhaust gas cleaner is the utility model is related to, is exactly that a kind of waste incineration activated carbon mixing sprays into dress Put.
Background technology
At present after incineration treatment of garbage operation is carried out, often produce containing a large amount of peculiar smell, solid particle and drop etc. The tail gas of pollutant, therefore currently generally require to be injected directly into low temperature into high-temperature tail gas when carrying out purified treatment to tail gas Activated carbon granule, absorption solidification is carried out to pollutants such as the peculiar smell in tail gas, solid particle and drops by activated carbon granule, is easy to Pollutant is separated from tail gas, reduces the effect of tail gas pollution, while the effect of cooling operation can be also played to tail gas Fruit, but found in the use of reality, on the one hand because the shower nozzle of current sprinkling equipment is relatively fixed, therefore cause activated carbon to spray Narrow is drenched, and thereby results in area coverage deficiency after activated carbon spray, and the activated carbon in activated carbon coverage Granule density is larger, so as to have a strong impact on efficiency of the activated carbon to pollutant adsorption cleaning operation in tail gas, while also causes big Carbon content active can not be participated in effectively in tail gas clean-up operation, so as to cause larger material waste, on the other hand due to Activated carbon is asked often relatively low when spraying, therefore cause larger temperature between activated carbon spray pipeline and external high temperature air be present Difference, so as to cause spray pipeline surface condensation vapor phenomenon easily occur, and the steam after condensing contacts with activated carbon granule Afterwards, easily trigger activated carbon granule to be bonded and cause activated carbon spray pipeline to block, so as to have a strong impact on that activated carbon spray is made The stability and reliability of industry, therefore this phenomenon is directed to, there is an urgent need to develop a kind of new activated carbon spray equipment, with full The needs actually used enough.
Utility model content
In view of the shortcomings of the prior art, the utility model, which provides a kind of waste incineration activated carbon mixing, sprays into dress Put, the new structure is simple, flexible and convenient to use, and activated carbon transfer pipeline effectively can be protected, and is avoiding because of temperature difference etc. Factor causes to spray clogging caused by activated carbon bonding etc., while also flexibly the spray direction of activated carbon can be entered Row regulation and control, and activated carbon spray area coverage is favorably improved, avoid the activated carbon caused by activated carbon spray region is narrow and small After particle spray, the effect to tail gas adsorption operation is influenceed because density is excessive, while activated carbon utilization rate is improved, is separately had Reducing for effect and enhances the tail gas clean-up operating efficiency of activated carbon at material loss.
To achieve these goals, the utility model is to realize by the following technical solutions:
A kind of waste incineration activated carbon mixing jetting device, including mozzle, jet pipe, shower nozzle, incubation cavity and electrical heating Pipe, the front end and end of mozzle are all provided with flange, and water conservancy diversion pipe end passes through flange and the interconnection of shower front end and coaxial Distribution, jet pipe is in chilling tower, and front end is located at outside extremely cold tower and connected with shower nozzle, and shower nozzle is at least one, passes through shunting Pipe is connected with jet pipe, and mutually in parallel between each shower nozzle, and shower nozzle is separately connected with each other by frame and jet pipe leading exterior surface, Incubation cavity includes cavity wall and warming plate, and wherein cavity wall is airtight cavity structure, is coated on outside mozzle and by mozzle both ends The flange at place is connected with each other with mozzle, warming plate hollow tubular structures, in cavity wall and is coated on outside mozzle, and is incubated Plate is coaxially distributed with cavity wall and mozzle respectively, and warming plate both ends are connected by locating slot with cavity wall, and warming plate is at least one, Warming plate is identical with the distance between mozzle and cavity wall, electric heating tube at least one, and water conservancy diversion is coated on around mozzle axis Pipe is outer, and electric heating tube and mozzle both ends end distance between the surface are 1/6-the 1/4 of mozzle effective length.
Further, it is hinged by turntable mechanism between described shower nozzle and frame, and is set on described turntable mechanism Swing driving mechanism.
Further, described swing driving mechanism is in rotary actuator, eccentric mechanism, rocker device and swing-bar mechanism Any one.
Further, when shower nozzle is two or more, then each shower nozzle is distributed around jet pipe axis in fan-shaped.
Further, the internal diameter of described incubation cavity cavity wall is 3-5 times of mozzle maximum outside diameter.
Further, the mozzle, be all provided with least one rocking equipment in jet flow pipe outer wall.
Further, described jet pipe is located on chilling tower inside points outer surface uniform some radiating wing plates, shower Heat preservation protective layer is set on the outer surface of chilling tower outer portion.
This new structure is simple, flexible and convenient to use, activated carbon transfer pipeline can effectively be protected, avoid Yin Wen The factors such as difference cause to spray clogging caused by activated carbon bonding etc., while can also be flexibly to the spray side of activated carbon To being regulated and controled, and activated carbon spray area coverage is favorably improved, avoided living caused by activated carbon spray region is narrow and small Property charcoal particle spray after, influence the effect to tail gas adsorption operation because density is excessive, while activated carbon utilization rate is improved, It is another to effectively reduce material loss and enhance the tail gas clean-up operating efficiency of activated carbon.
Brief description of the drawings
Describe the utility model in detail with reference to the accompanying drawings and detailed description;
Fig. 1 is this new structure schematic diagram.
Embodiment
Technological means, creation characteristic, reached purpose and effect to realize the utility model are easy to understand, below With reference to embodiment, the utility model is expanded on further.
A kind of waste incineration activated carbon mixing jetting device as described in Figure 1, including mozzle 1, jet pipe 2, shower nozzle 3, Incubation cavity 4 and electric heating tube 5, the front end and end of mozzle 1 are all provided with flange 6, and the end of mozzle 1 passes through flange 6 and spray The front end of pipe 2 is connected with each other and is coaxially distributed, and jet pipe 2 is in chilling tower 7, and front end is located at outside extremely cold tower 7 and connected with shower nozzle 3 Logical, shower nozzle 3 is at least one, is connected by isocon 8 with jet pipe 2, and mutually in parallel between each shower nozzle 3, and shower nozzle 3 separately passes through machine Frame 9 is connected with each other with the leading exterior surface of jet pipe 2, and incubation cavity 4 includes cavity wall 41 and warming plate 42, and wherein cavity wall 41 is closed chamber Body structure, it is coated on outside mozzle 1 and is connected with each other by the flange 6 at the both ends of mozzle 1 with mozzle 1, warming plate 42 is empty Tubular structures, in cavity wall 41 and it is coated on outside mozzle 1, and warming plate 42 is coaxial with cavity wall 41 and mozzle 1 respectively Distribution, the both ends of warming plate 42 are connected by locating slot 43 with cavity wall 41, and warming plate 42 is at least one, warming plate 42 and mozzle The distance between 1 and cavity wall 41 are identical, electric heating tube 5 at least one, are coated on around the axis of mozzle 1 outside mozzle 1, and electricity Heating tube 5 and the both ends end distance between the surface of mozzle 1 are 1/6-the 1/4 of the effective length of mozzle 1.
In the present embodiment, it is hinged between described shower nozzle 3 and frame 9 by turntable mechanism 10, and described turntable machine Swing driving mechanism 11 is set on structure 10.
In the present embodiment, described swing driving mechanism 11 is rotary actuator, eccentric mechanism, rocker device and rocker mechanism Any one in structure.
In the present embodiment, when shower nozzle 3 is two or more, then each shower nozzle 3 divides around the axis of jet pipe 2 in fan-shaped Cloth.
In the present embodiment, the internal diameter of the described cavity wall 41 of incubation cavity 4 is 3-5 times of the maximum outside diameter of mozzle 1.
In the present embodiment, at least one rocking equipment 12 is all provided with the mozzle 1, the outer wall of jet pipe 2.
In the present embodiment, described jet pipe 2 is located on the inside points outer surface of chilling tower 7 uniform some radiating wing plates 13, Shower 2, which is located on the outer surface of the outer portion of chilling tower 7, sets heat preservation protective layer 14.
This is new in the specific implementation, and activated carbon granule is entered in mozzle by mozzle front end first, Ran Houtong Enter shower after crossing mozzle, and cooling processing is carried out with chilling tower first along shower, then by after cooling Sprayed by shower nozzle and mixed with tail gas, in mixed process, the spray scope and angle of shower nozzle can carried out according to using needs It is adjusted flexibly, to improve the coverage of activated carbon, and reduces the density after activated carbon spray, improve activated carbon and tail gas adsorption The efficiency of operation, activated carbon usage amount is reduced, simultaneously, during spray, separately by incubation cavity and point heating tube to leading Flow tube is protected and temperature adjustment, avoid because of condensation vapor and caused by activated carbon be bonded clogging.
This new structure is simple, flexible and convenient to use, activated carbon transfer pipeline can effectively be protected, avoid Yin Wen The factors such as difference cause to spray clogging caused by activated carbon bonding etc., while can also be flexibly to the spray side of activated carbon To being regulated and controled, and activated carbon spray area coverage is favorably improved, avoided living caused by activated carbon spray region is narrow and small Property charcoal particle spray after, influence the effect to tail gas adsorption operation because density is excessive, while activated carbon utilization rate is improved, It is another to effectively reduce material loss and enhance the tail gas clean-up operating efficiency of activated carbon.
It should be understood by those skilled in the art that the utility model is not restricted to the described embodiments, above-described embodiment and Simply illustrate principle of the present utility model described in specification, on the premise of the spirit and scope of the utility model is not departed from, The utility model also has various changes and modifications, and these changes and improvements both fall within claimed the scope of the utility model It is interior.The utility model requires protection scope is by appended claims and its equivalent thereof.

Claims (7)

  1. A kind of 1. waste incineration activated carbon mixing jetting device, it is characterised in that:The waste incineration activated carbon mixing sprays into dress Put and be all provided with flange including mozzle, jet pipe, shower nozzle, incubation cavity and electric heating tube, the front end and end of described mozzle, and Water conservancy diversion pipe end is connected with each other with shower front end by flange and is coaxially distributed, and described jet pipe is embedded in chilling tower, and Front end is located at outside extremely cold tower and connected with shower nozzle, and described shower nozzle is at least one, is connected by isocon with jet pipe, and each spray Mutually in parallel between head, described shower nozzle is separately connected with each other by frame and jet pipe leading exterior surface, described incubation cavity bag Include cavity wall and warming plate, wherein described cavity wall is airtight cavity structure, be coated on mozzle it is outer and by mozzle both ends at Flange and mozzle be connected with each other, described warming plate hollow tubular structures, in cavity wall and be coated on outside mozzle, and Described warming plate is coaxially distributed with cavity wall and mozzle respectively, and described warming plate both ends are connected by locating slot with cavity wall, And described warming plate is at least one, warming plate is identical with the distance between mozzle and cavity wall, and described electric heating tube is at least One, it is coated on around mozzle axis outside mozzle, and described electric heating tube is with mozzle both ends end distance between the surface 1/6-the 1/4 of mozzle effective length.
  2. A kind of 2. waste incineration activated carbon mixing jetting device according to claim 1, it is characterised in that:Described shower nozzle It is hinged between frame by turntable mechanism, and swing driving mechanism is set on described turntable mechanism.
  3. A kind of 3. waste incineration activated carbon mixing jetting device according to claim 2, it is characterised in that:Described swing Drive mechanism is any one in rotary actuator, eccentric mechanism, rocker device and swing-bar mechanism.
  4. A kind of 4. waste incineration activated carbon mixing jetting device according to claim 1, it is characterised in that:Shower nozzle is two Or during two or more, then each shower nozzle is distributed around jet pipe axis in fan-shaped.
  5. A kind of 5. waste incineration activated carbon mixing jetting device according to claim 1, it is characterised in that:Described insulation The internal diameter of chamber cavity wall is 3-5 times of mozzle maximum outside diameter.
  6. A kind of 6. waste incineration activated carbon mixing jetting device according to claim 1, it is characterised in that:The water conservancy diversion At least one rocking equipment is all provided with pipe, jet flow pipe outer wall.
  7. A kind of 7. waste incineration activated carbon mixing jetting device according to claim 1, it is characterised in that:Described jet flow Pipe uniform some radiating wing plates on chilling tower inside points outer surface, shower, which is located on the outer surface of chilling tower outer portion, to be set Heat preservation protective layer.
CN201720576413.3U 2017-05-23 2017-05-23 A kind of waste incineration activated carbon mixing jetting device Active CN206996206U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720576413.3U CN206996206U (en) 2017-05-23 2017-05-23 A kind of waste incineration activated carbon mixing jetting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720576413.3U CN206996206U (en) 2017-05-23 2017-05-23 A kind of waste incineration activated carbon mixing jetting device

Publications (1)

Publication Number Publication Date
CN206996206U true CN206996206U (en) 2018-02-13

Family

ID=61445198

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720576413.3U Active CN206996206U (en) 2017-05-23 2017-05-23 A kind of waste incineration activated carbon mixing jetting device

Country Status (1)

Country Link
CN (1) CN206996206U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113666054A (en) * 2020-05-15 2021-11-19 中冶宝钢技术服务有限公司 Active carbon conveying device and active carbon desulfurization and denitrification system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113666054A (en) * 2020-05-15 2021-11-19 中冶宝钢技术服务有限公司 Active carbon conveying device and active carbon desulfurization and denitrification system
CN113666054B (en) * 2020-05-15 2023-02-03 中冶宝钢技术服务有限公司 Active carbon conveying device and active carbon desulfurization and denitrification system

Similar Documents

Publication Publication Date Title
CN108744820A (en) A kind of ultrasonic atomization pre electrified turbulence coagulation device
CN203355927U (en) Target type impinging stream nozzle with conical firing pin
CN206996206U (en) A kind of waste incineration activated carbon mixing jetting device
CN108554662A (en) A kind of spiral gas-liquid double-fluid electrostatic atomization nozzle
CN101435663B (en) Reversed flow heat transfer eddy flow secondary atomizing induced draft cooling tower
CN201364040Y (en) Packless cyclone atomized cooling tower
CN201402068Y (en) Stuffing-free cyclone induced-air wall-flow-free cooling tower
CN207745682U (en) Dynamic wave spray equipment for smoke absorption
CN201173662Y (en) High pressure flash evaporation spray drying device
CN103383118A (en) Heat pump type spraying solution dehumidification system
CN212662727U (en) Enzyme preparation drying system with waste heat recovery
CN209246725U (en) A kind of energy saving and environment friendly cooling tower
CN108705095A (en) A kind of Nd-Fe-B permanent magnet anaerobic fuel pulverizing plant
CN206951476U (en) A kind of gathering line corrosion inhibiter coating device
CN209416081U (en) A kind of heat-accumulating type high-temperature oxidation furnace fume treatment tower
CN107029536A (en) Spiral blender and the denitrification apparatus using the blender
CN203076084U (en) Humidifying tower with dry fog humidifying coagulation device
CN208990544U (en) Denitration device for reducing dust for rotary kiln
CN207688123U (en) A kind of secondary air atomizing fuel nozzle
CN206587942U (en) A kind of shower nozzle with good atomizing effect
CN206996252U (en) A kind of fibreglass epoxy acid mist purifying column
CN206082174U (en) Enamelling machine cures tail gas processing device
CN206777889U (en) A kind of comprehensive spray block clearing mechanism for evaporator
CN110497502A (en) The low volatilization concrete segment production system of enhancement of environment type and its process for making
CN206434986U (en) A kind of simple water mist sprinkling dust arrester

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant