CN208237883U - A kind of dry mud directly enters furnace incineration system - Google Patents
A kind of dry mud directly enters furnace incineration system Download PDFInfo
- Publication number
- CN208237883U CN208237883U CN201721758884.2U CN201721758884U CN208237883U CN 208237883 U CN208237883 U CN 208237883U CN 201721758884 U CN201721758884 U CN 201721758884U CN 208237883 U CN208237883 U CN 208237883U
- Authority
- CN
- China
- Prior art keywords
- boiler
- coal
- mud
- furnace
- defeated
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model discloses a kind of dry mud directly to enter furnace incineration system, its innovative point is: including hopper, conveyer belt, coal handling system, defeated mud system, coal slime conversion platform and boiler, the coal handling system and defeated mud system are connect with coal slime conversion platform by threeway respectively, the hopper and coal slime conversion platform are located at the both ends of conveyer belt, the output end of the coal handling system is located at the furnace bottom of boiler, and the output end of the defeated mud system is located at the burner hearth position of boiler.The advantages of the utility model: mud cake is uniformly spread in burner hearth, and mud cake and air, fire coal after evenly mixing, can guarantee full combustion, not influence the fluidisation in lower furnace portion bed material.By the way that briquette is transported to furnace bottom, it can be effectively solved mud cake to mix with into easily bonding in coal bunker and in feeder track after fuel, put up a bridge, block the frequent phenomenon of coal that causes to break, reduce the disturbance to boiler operatiopn operating condition, and firing efficiency can be greatly improved.
Description
Technical field
The utility model relates to sludge treatment devices more particularly to a kind of dry mud directly to enter furnace incineration system.
Background technique
Sludge incineration processing is a kind of most common mode in chemical plant or municipal sludge processing, but industry is dirty
It can also include usually carbon cake in mud or domestic sludge, be to burn carbon cake and sludge cake together in the prior art, adopt
When burning in this way, mud cake is mixed and easily bonds, put up a bridge in coal bunker and in feeder track after matching into fuel, blocking and cause
The frequent phenomenon of disconnected coal.Mud cake, which is mixed, to be fitted over coal-fired mud and enters burner hearth emulsion zone by feeder, due between coal dropping port and air distribution plate
Height is 1 meter, and the biggish mud cake of particle sinks to rapidly emulsion zone lower part after entering furnace, and range of scatter is smaller, when the bed of material is compared with Gao Shiliu
Change poor, is easily formed and accumulated in lower furnace portion, incomplete combustion easily causes boiler slag removal difficult, and dry mud is not easy uniformly
Mix and fit in fuel, cause into furnace heat output of fuel fluctuate it is larger, be unfavorable for boiler combustion stablize.
Utility model content
It is in view of the drawbacks of the prior art and insufficient, the purpose of this utility model is to provide a kind of stable, maintenance at
This low dry mud directly enters furnace incineration system.
In order to achieve the above purposes, the technical solution adopted by the utility model is:, and a kind of dry mud directly enters furnace incineration system,
Innovative point is: including hopper, conveyer belt, coal handling system, defeated mud system, coal slime conversion platform and boiler, the coal handling system
It is connect respectively with coal slime conversion platform by threeway with defeated mud system, the hopper and coal slime conversion platform are located at conveyer belt
Both ends, the output end of the coal handling system is located at the furnace bottom of boiler, and the output end of the defeated mud system is located at the burner hearth of boiler
Position.
Further, the coal handling system includes coal transportation belt, boiler coal bunker and feeder, and the feeder is located at boiler
Furnace bottom, the exit of the coal transportation belt are located at the top of boiler coal bunker.
Further, mixing machine is provided in the boiler coal bunker.
Further, the defeated mud system includes dry mud conveyer belt, discharger, transition hopper, enters furnace conveyer and enter furnace
Device, the discharger enter furnace conveyer and enter the top that furnace apparatus is located at boiler, it is described enter furnace apparatus be located at the fire door of boiler
Place is simultaneously firmly connected with it, it is described enter furnace conveyer be located at the top into furnace apparatus and be firmly connected with it, the discharger is set
It sets in the top for entering furnace conveyer, the transition hopper is arranged between adjacent boiler, and the dry mud conveyer belt is arranged in pot
The top of furnace.
Further, the discharger is belt plow.
Further, the top side of the boiler is provided with defeated mud wind blower, and the defeated mud wind blower is fixed with boiler
Connection.
The utility model has the beneficial effect that
The utility model enters in boiler by separately conveying mud cake and briquette, by mud cake from upper end, is made by blowing
It has enough fall times after entering burner hearth between the dilute-phase zone and emulsion zone of burner hearth, and mud cake uniformly expands in burner hearth
It dissipates, mud cake and air, fire coal after evenly mixing, can guarantee full combustion, not influence the fluidisation in lower furnace portion bed material.Pass through
Briquette is transported to furnace bottom, can be effectively solved mud cake mix with into after fuel in coal bunker and in feeder track easily bonding,
It puts up a bridge, the phenomenon that blocking causes disconnected coal frequent, reduces the disturbance to boiler operatiopn operating condition, and burning effect can be greatly improved
Rate.
Detailed description of the invention
Fig. 1 is the front view of the utility model;
Fig. 2 is the left view in the utility model.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with specific embodiment party
The present invention will be further described in detail for formula.It should be appreciated that the specific embodiments described herein are only to explain
The utility model is not used to limit the utility model.
Referring to Fig. 1 and Fig. 2, present embodiment discloses a kind of dry mud and directly enters furnace incineration system, including hopper 1,
Conveyer belt 2, coal handling system 3, defeated mud system 4, coal slime conversion platform 5 and boiler 6, coal handling system 3 and defeated mud system 4 respectively with coal
Mud conversion platform 5 is connected by threeway, in use process by rotation threeway be separately connected coal handling system 3 and defeated mud system 4 from
And mud cake or briquette are conveyed, it is feasible, can using manually control or inductor control by the way of.
Hopper 1 and coal slime conversion platform 5 are located at the both ends of conveyer belt, and the output end of coal handling system 3 is located at boiler 6
Furnace bottom, the output end of defeated mud system 4 are located at the burner hearth position of boiler 6.
Coal handling system 3 includes coal transportation belt, boiler coal bunker and feeder, and feeder is located at the furnace bottom of boiler, the coal transportation belt
Exit be located at the top of boiler coal bunker.It is feasible, other coals used for combustion are placed in boiler coal bunker.It is feasible, pot
It is also provided with mixing machine in furnace coal bunker, is mixed briquette with common coal by mixing machine.
Defeated mud system 4 includes dry mud conveyer belt 41, discharger 42, transition hopper 43, enters furnace conveyer 44 and enter furnace apparatus
45, discharger 42 enters furnace conveyer 44 and enters the top that furnace apparatus 45 is located at boiler 6, enters the fire door that furnace apparatus 45 is located at boiler 6
Place is simultaneously fixedly connected with the mode of its logical welding, is entered furnace conveyer 44 and is located at the top into furnace apparatus 45 and is firmly connected with it,
The top into furnace conveyer 44 is arranged in discharger 42, and transition hopper 43 is arranged between adjacent boiler, dry mud conveyer belt 41
The top of boiler 6 is set.Feasible, boiler 6 can be set multiple.Discharger 42 can be set to belt plow.Pot
The top side of furnace 6 is provided with defeated mud wind blower, and defeated mud wind blower is fixedly connected with boiler, can will be done by defeated mud wind blower
Mud blows to corresponding region, and reduces falling speed.
The working process of the utility model is as follows: the sludge of moisture content 60% is broken into through crusher≤5cm particle after, lead to
It crosses load wagon to send to storage bucket, dry mud is then delivered to by coal slime conversion platform by dry mud conveyer belt, (three all by threeway
Conveying direction switching is crossed, mud cake is sent to boiler oil storehouse or toward being fed directly to boiler furnace direction), in dry mud conveyer belt phase
Answer boiler sites that one belt plow is respectively housed, by adjusting the height (lift and fall) of discharger, by dry mud conveyer belt
On dry mud carry out whole interceptions or partial interception completes distribution to each furnace mud amount, and fall into the transition hopper of corresponding boiler,
Then it is sent by belt conveyor and enters furnace apparatus to dry mud and fall Ni Kou;Through entered furnace apparatus by dry mud be sent into burner hearth dilute-phase zone with it is close
Between phase region, defeated mud wind is that the cold wind drawn by boiler first cooling by wind air duct by the air hose mouth in the case where falling mud pipe passes through duck-beak type
Dry mud is conveyed downwards along dredging tube, is sowed to burner hearth by tuyere, and dry mud enters furnace apparatus and falls the aperture among boiler front wall of mud mouth
Burner hearth is protruded into, mud pipe is fallen and protrudes into burner hearth part and fall mud pipe surrounding laying castable and to protect fall mud pipe.
In addition, can achieve the minimum 3T/H of single furnace, maximum 7T/H burning amount by adjusting conveying capacity, the dry mud amount of day disposition compared with
Increase by 100% or more before transformation.Dry mud conveying can reach more furnaces while directly burn dry mud by the adjusting to discharger
Purpose, and each dry mud burning amount of operation furnace can be distributed by fine tuning discharger according to each furnace operating condition.Remain fuel to
The transfer passage with mud is carried out when the operation defeated coal of furnace coal bunker, increases boiler implosion room DCS control system and original fuel, Gan Nipeng newly
Docking is completed in control section, can be according to sludge treatment needs, conditioning of mud conveying direction.
The above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, those of ordinary skill in the art couple
The other modifications or equivalent replacement that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope should all cover in the scope of the claims of the utility model.
Claims (6)
1. a kind of dry mud directly enters furnace incineration system, it is characterised in that: including hopper, conveyer belt, coal handling system, defeated mud system,
Coal slime conversion platform and boiler, the coal handling system and defeated mud system are connect with coal slime conversion platform by threeway respectively, described
Hopper and coal slime conversion platform are located at the both ends of conveyer belt, and the output end of the coal handling system is located at the furnace bottom of boiler, institute
The output end for stating defeated mud system is located at the burner hearth position of boiler.
2. a kind of dry mud according to claim 1 directly enters furnace incineration system, it is characterised in that: the coal handling system includes
Coal transportation belt, boiler coal bunker and feeder, the feeder are located at the furnace bottom of boiler, and the exit of the coal transportation belt is located at steam coal
The top in storehouse.
3. a kind of dry mud according to claim 2 directly enters furnace incineration system, it is characterised in that: set in the boiler coal bunker
It is equipped with mixing machine.
4. a kind of dry mud according to claim 1 directly enters furnace incineration system, it is characterised in that: the defeated mud system includes
Dry mud conveyer belt, transition hopper, enters furnace conveyer and enters furnace apparatus discharger, and the discharger enters furnace conveyer and enters furnace dress
Setting in the top of boiler, it is described enter furnace apparatus be located at the fire door of boiler and be firmly connected with it, it is described enter furnace convey seat in the plane
It in the top for entering furnace apparatus and is firmly connected with it, the top into furnace conveyer, the transition hopper is arranged in the discharger
It is arranged between adjacent boiler, the top of boiler is arranged in the dry mud conveyer belt.
5. a kind of dry mud according to claim 4 directly enters furnace incineration system, it is characterised in that: the discharger is plough
Discharger.
6. a kind of dry mud according to claim 1 directly enters furnace incineration system, it is characterised in that: the upper side of the boiler
While being provided with defeated mud wind blower, the defeated mud wind blower is fixedly connected with boiler.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721758884.2U CN208237883U (en) | 2017-12-16 | 2017-12-16 | A kind of dry mud directly enters furnace incineration system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721758884.2U CN208237883U (en) | 2017-12-16 | 2017-12-16 | A kind of dry mud directly enters furnace incineration system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208237883U true CN208237883U (en) | 2018-12-14 |
Family
ID=64578700
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721758884.2U Expired - Fee Related CN208237883U (en) | 2017-12-16 | 2017-12-16 | A kind of dry mud directly enters furnace incineration system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208237883U (en) |
-
2017
- 2017-12-16 CN CN201721758884.2U patent/CN208237883U/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2572893C (en) | Integrated system for the extraction of heavy ash, conversion thereof into light ash and reduction of unburnt matter | |
CN104344398B (en) | Middle warehouse formula pulverized coal carried by hot air pulverized coal preparation system | |
CN202465830U (en) | Residual heat reclaiming system for pellets and sintered ores | |
CN205721339U (en) | A kind of industrial fluidized bed boiler automation control system | |
CN208237883U (en) | A kind of dry mud directly enters furnace incineration system | |
CN202328292U (en) | Ash handling equipment for secondary air bellow of coal-fired boiler and coal-fired boiler | |
CN102506421B (en) | Circulating fluid bed (CFB) boiler coal supply system for blending combustion of middling coal | |
CN209131421U (en) | A kind of kiln integral structure and the process system using the kiln integral structure | |
CN203586193U (en) | Middle storing bin type hot wind powder feeding and manufacturing system | |
CN107940471A (en) | A kind of dry mud directly enters stove incineration system | |
CN205717287U (en) | Hot blast and exhaust gas double-medium powder delivery efficient boiler combustion apparatus | |
CN206721136U (en) | A kind of biomass and city solid waste comprehensive utilization device | |
CN107162443B (en) | Boiling lime kiln | |
CN105565687B (en) | A kind of limekiln breeze blowing induction system | |
CN201078698Y (en) | Industry furnace coal dust firing system apparatus | |
CN205717281U (en) | Pulverized coal carried by hot air high efficiency boiler emission reduction device | |
CN212481304U (en) | Household garbage pyrolysis gasification chain grate furnace | |
CN109046721A (en) | Clinker crushes drying system | |
CN204629521U (en) | Suspension circulating fluidized bed boiler for treating food wastewater | |
CN107654997B (en) | Circulating ash control system and method for circulating fluidized bed boiler | |
CN212987266U (en) | Sealing structure of boiler feed opening | |
CN206861516U (en) | Anti-blocking spray apparatus for ash for CFBB separating system | |
CN205783041U (en) | A kind of pulverized coal carried by hot air boiler of efficient burning energy-saving and emission-reduction | |
CN204313271U (en) | A kind of CFBB charging gear | |
CN205717282U (en) | Efficient burning formula pulverized coal carried by hot air boiler |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181214 Termination date: 20181216 |
|
CF01 | Termination of patent right due to non-payment of annual fee |