CN206739319U - The stove of organic waste liquid burning containing sodium salt - Google Patents
The stove of organic waste liquid burning containing sodium salt Download PDFInfo
- Publication number
- CN206739319U CN206739319U CN201720622979.5U CN201720622979U CN206739319U CN 206739319 U CN206739319 U CN 206739319U CN 201720622979 U CN201720622979 U CN 201720622979U CN 206739319 U CN206739319 U CN 206739319U
- Authority
- CN
- China
- Prior art keywords
- transition
- stove
- vertical portion
- sodium salt
- coil pipe
- 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.)
- Withdrawn - After Issue
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Abstract
The utility model provides a kind of stove of organic waste liquid burning containing sodium salt, and the stove of organic waste liquid burning containing sodium salt includes：Burning Room, vertically set, burner is provided with the top of Burning Room, burner is provided with the organic liquid waste entrance and auxiliary fuel input connected with Burning Room, and the sidewall bottom of Burning Room is provided with molten state slag-drip opening；Transition expansion chamber, including transition entrance and transition outlet, transition entrance is horizontally disposed and is connected with Burning Room, and steam pipe row is provided with transition expansion chamber, and transition outlet is arranged vertically at steam pipe row top；Exchanged heat convection cell, exports and connects with transition, and multiple heat-exchanging components are provided with the convection cell that exchanges heat, and the gas that the heat-exchanging component can discharge with transition expansion chamber carries out heat exchange.The beneficial effects of the utility model are that the schmutzband that can be reduced on heat-exchanging component is formed, can with the extension device checking maintenance cycle, meanwhile, can utilize organic liquid waste the combustion heat, improve incinerator operation economy.
Description
Technical field
Liquid waste incineration field in fine chemistry industry and petrochemical industry is the utility model is related to, is specifically a kind of organic containing sodium salt
Liquid waste incinerator.
Background technology
Burning is to handle a kind of conventional effective method of waste, nucleus equipment of the incinerator as incinerator,
Using the waste heat boiler of better economy, and it is bigger using the waste incineration disposal method for reclaiming heat to handle amount of waste
During salt bearing liquid wastes, incinerator can be relatively difficult in structure design, molten state, solid-state of the caused carrying in flue gas after burning
Sodium peroxide and inorganic sodium will be attached on heat exchange tube wall, formed " schmutzband ", reduce heat exchange efficiency, shorten equipment operation
Cycle, or even equipment is not run.
Utility model content
The utility model provides a kind of stove of organic waste liquid burning containing sodium salt, to reach the purpose for reducing schmutzband and being formed.
Technical scheme is used by the utility model solves its technical problem：A kind of stove of organic waste liquid burning containing sodium salt,
Including：Burning Room, vertically set, burner is provided with the top of Burning Room, burner is provided with to be connected with Burning Room
Organic liquid waste entrance and auxiliary fuel input, the sidewall bottom of Burning Room is provided with molten state slag-drip opening；Transition expansion chamber, bag
Transition entrance and transition outlet are included, transition entrance is horizontally disposed and is connected with Burning Room, is provided with transition expansion chamber
Steam pipe is arranged, and transition outlet is arranged vertically at steam pipe row top；Exchange heat convection cell, exports and connects with transition, heat exchange
Multiple heat-exchanging components are provided with convection cell, the gas that the heat-exchanging component can discharge with transition expansion chamber carries out heat exchange.
Further, air distribution component and spray module are provided between the transition entrance of transition expansion chamber and steam pipe row.
Further, the bottom of transition expansion chamber is provided with multiple sedimentation mouths, and sedimentation mouth is located at the lower section of steam pipe row.
Further, the separation gear pipe of gas solid separation can be carried out by being provided with transition outlet.
Further, heat exchange convection cell includes the first vertical portion, the second vertical portion and connecting portion, and the second vertical portion is arranged on
The side of first vertical portion, the both ends of connecting portion connect the upper end of the first vertical portion and the upper end of the second vertical portion respectively, and first
The lower end of vertical portion connects with transition outlet.
Further, the heat-exchanging component includes：The coil pipe of evaporator section first, is arranged in the first vertical portion, evaporator section first
Coil pipe includes the coil pipe unit of evaporator section first that multiple parallel intervals are set, each coil pipe unit of evaporator section first both with respect to
Horizontal direction tilts；The coil pipe of evaporator section second, is arranged on the top of the second vertical portion, and the coil pipe of evaporator section second includes multiple parallel
The spaced coil pipe unit of evaporator section second, each coil pipe unit of evaporator section second tilt both with respect to horizontal direction；Give
Water preheats coil pipe, is arranged on the middle part of the second vertical portion and below the coil pipe of evaporator section second, feed-water preheating coil pipe includes more
The feed-water preheating unit that individual parallel interval is set, each feed-water preheating unit is and horizontal direction parallel；Hot coil was evaporated,
It is arranged vertically in connecting portion.
Further, the first vertical portion, the second vertical portion and connecting portion are provided with soot blowing component.
Further, gradually it is inclined upwardly along molten state slag-drip opening to the direction of transition entrance, the bottom wall of Burning Room.
Further, the direction arranged along transition entrance to steam pipe, the bottom wall of transition expansion chamber tilt gradually downward.
The beneficial effects of the utility model are that the schmutzband that can be reduced on heat-exchanging component is formed, and can be examined with extension device
Maintenance cycle, make the incineration treatment method containing sodium salt of economical recovery used heat byproduct steam for being unable to stable operation originally
Become possible to；Meanwhile the combustion heat of organic liquid waste can be made full use of, the economy of incinerator operation is improved, is made originally not
The incinerator for producing economic benefit brings benefits.
Brief description of the drawings
The Figure of description for forming the part of the application is used for providing further understanding to of the present utility model, this practicality
New schematic description and description is used to explain the utility model, does not form to improper restriction of the present utility model.
In the accompanying drawings：
Fig. 1 is the structural representation of the utility model organic waste liquid burning containing sodium salt stove first embodiment；
Fig. 2 is the structural representation of the utility model organic waste liquid burning containing sodium salt stove second embodiment.
Reference in figure：10th, Burning Room；11st, organic liquid waste entrance；12nd, auxiliary fuel input；13rd, molten state deslagging
Mouthful；14th, flame retardant coating；20th, transition expansion chamber；21st, transition entrance；22nd, transition exports；23rd, steam pipe is arranged；24th, air distribution component；
25th, spray module；26th, mouth is settled；27th, separation gear pipe；30th, exchange heat convection cell；31st, the first vertical portion；32nd, the second vertical portion；
33rd, connecting portion；41st, the coil pipe of evaporator section first；42nd, the coil pipe of evaporator section second；43rd, feed-water preheating coil pipe；44th, hot plate was evaporated
Pipe；50th, electric cleaner；60th, chimney.
Embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase
Mutually combination.Describe the utility model in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
As shown in figure 1, the utility model first embodiment provides a kind of stove of organic waste liquid burning containing sodium salt, including burn
Room 10, transition expansion chamber 20 and heat exchange convection cell 30.Burning Room 10 is vertically set, and the top of Burning Room 10 is provided with combustion
Burner (organic liquid waste and auxiliary fuel cell burner), the burner have the organic liquid waste entrance connected with Burning Room 10
11 and auxiliary fuel input 12, the sidewall bottom of Burning Room 10 be provided with molten state slag-drip opening 13.Transition expansion chamber 20 included
Entrance 21 (changeover portion with certain length is formed) and transition outlet 22 are crossed, transition entrance 21 is horizontally disposed and with burning
The connection of the bottom of room 10 is burnt, steam pipe row 23 is provided with transition expansion chamber 20, transition outlet 22 is arranged vertically at steam
The top of pipe row 23.Heat exchange convection cell 30 is connected with transition outlet 22, is provided with multiple heat-exchanging components in the convection cell 30 that exchanges heat, is exchanged heat
The gas that component can discharge with transition expansion chamber 20 carries out heat exchange.
The utility model first embodiment can make in Burning Room caused flue gas in the bottom of Burning Room 10 and transition
Effective gas-liquid separation and gas solid separation are carried out in expansion chamber 20, flue gas can be reduced schmutzband is produced on heat-exchanging component, can
With the extension device checking maintenance cycle, the economical recovery used heat byproduct steam for making to be unable to stable operation originally contains sodium salt
Incineration treatment method becomes possible to；Meanwhile the combustion heat of organic liquid waste can be made full use of, improve the economy of incinerator operation
Property, the incinerator for making not producing economic benefit originally brings benefits.
Specifically, Burning Room 10, which has, burns inner chamber, and flame retardant coating 14 is equipped with the inner surface for burning inner chamber.Burning Room 10
Side wall in the middle part of be provided with peephole for observation.The lower sidewall of Burning Room 10 is provided with molten state slag-drip opening 13.Such as Fig. 1
Shown, the molten state slag-drip opening 13 is located at left lower in figure, i.e., positioned at the relative side of transition entrance 21.In the embodiment
In, gradually it is inclined upwardly along molten state slag-drip opening 13 to the direction of transition entrance 21, the bottom wall of Burning Room 10.Molten state slag-drip opening
13 incline direction and angle of inclination are adapted with the bottom wall incline direction of Burning Room 10 and angle of inclination.
Flame retardant coating 14 is set, the fire resistance of Burning Room can be increased.Wherein, the flame retardant coating 14 of side towards the fire is adopted in Burning Room 10
The chrome ore slag castable corroded with resistance to melting sodium peroxide.In the utility model embodiment, the incineration temperature of Burning Room is 1100
More than DEG C, the organic liquid waste containing sodium salt can be made fully to burn, generate harmless high-temperature flue gas (carbon dioxide, nitrogen, oxygen
Gas and water steam), caused molten state sodium peroxide drop is equably entrained in high-temperature flue gas after burning.Due to using top spray
Mode (organic liquid waste entrance 11 and auxiliary fuel input 12 are respectively positioned on the top of Burning Room 10), high-temperature flue gas (contains sodium peroxide
Drop) flow direction it is identical with gravity direction, be advantageous to high-temperature flue gas Burning Room 10 bottom carry out gas-liquid separation, avoid
Fluid spills inboard wall of furnace body.
Meanwhile as high-temperature flue gas flows vertically downwards, the sodium peroxide drop of molten condition is in Burning Room 10
Bottom be separated, and discharged by the inclined floor of Burning Room 10 by molten state slag-drip opening 13.By the high temperature of gas-liquid separation
Flue gas is entered in transition expansion chamber 20 by transition entrance.
In the utility model embodiment, air distribution is provided between transition entrance 21 and the steam pipe row 23 of transition expansion chamber 20
Component 24 and spray module 25.The high-temperature flue gas (containing molten state sodium peroxide drop) entered in transition expansion chamber 20 passes through
Air distribution component 24 and spray module 25 enter the entrance of steam pipe row 23.Wherein air distribution component 24 can drop to high-temperature flue gas
Temperature, spray module 25 provide reaction condition and cooling high temperature flue gas, the near fusing point less than sodium carbonate of high-temperature flue-gas with
Decomposition temperature, promote the carbon dioxide reaction in the sodium peroxide drop and flue gas of low melting point, make molten state sodium peroxide drop
As often as possible it is converted into sodium carbonate solid particle.
Steam pipe row 23 is provided with transition expansion chamber 20, the flue gas (650 DEG C~700 DEG C) by cooling can be made to exist
It is rapidly cooled after entering steam pipe row 23, makes the cooling solidification of sodium peroxide drop, further reduce flue gas flow rate gas-solid point
From.
Preferably, transition outlet 22 is arranged on above the outlet of steam pipe row 23, and separation gear is provided with transition outlet 22
Pipe 27, high-temperature flue gas (flue gas of the particle containing solid sodium salt) vertical upflow transition outlet 22 at, separation gear pipe 27 by
Blank pipe more than the rounded projections arranged of three rows is formed, and when flue gas is flushed to these pipes, solid particle and pipe collide, and disappear
Sink under gravity after consuming kinetic energy, flue gas will change flow direction after meeting these pipes, be crossed from pipe spaced winding and continue up stream
It is dynamic, so as to have the function that gas solid separation.
Separation gear pipe 27 is set, solid particle kinetic energy can be eliminated, flue gas is further realized gas solid separation.It is separated
Solid sodium carbonate and sodium peroxide particle afterwards is discharged by the bottom of transition expansion chamber 20.In the utility model embodiment, transition is sunk
The bottom of drop room 20 is provided with multiple sedimentation mouths 26, and sedimentation mouth 26 is located at the lower section of steam pipe row 23.And along transition entrance 21
To the direction of steam pipe row 23, the bottom wall of transition expansion chamber 20 is tilted and connected with sedimentation mouth 26 gradually downward.
In in the utility model embodiment, above-mentioned transition expansion chamber 20 can be arranged to repair and fast changeable knot
Structure, manhole (soot blowing component) is provided with transition expansion chamber 20, can observe and clear up dust in order to staff.
As shown in figure 1, heat exchange convection cell 30 includes the first vertical portion 31, the second vertical portion 32 and connecting portion 33, second is perpendicular
Straight portion 32 is arranged on the side of the first vertical portion 31, and the both ends of connecting portion 33 connect the upper end and second of the first vertical portion 31 respectively
The upper end of vertical portion 32, the lower end of the first vertical portion 31 are connected with transition outlet 22.Using the heat exchange convection cell 30 of above structure,
Area occupied can be effectively reduced, improves space availability ratio.
Specifically, heat-exchanging component includes the first coil pipe of evaporator section 41, the second coil pipe of evaporator section 42, the and of feed-water preheating coil pipe 43
Evaporated hot coil 44.The first coil pipe of evaporator section 41 is arranged in the first vertical portion 31, and the first coil pipe of evaporator section 41 includes multiple
The coil pipe unit of evaporator section first that parallel interval is set, each coil pipe unit of evaporator section first tilt both with respect to horizontal direction.
The second coil pipe of evaporator section 42 is arranged on the top of the second vertical portion 32, and the second coil pipe of evaporator section 42 is set including multiple parallel intervals
The coil pipe unit of evaporator section second, each coil pipe unit of evaporator section second both with respect to horizontal direction tilt.Feed-water preheating coil pipe
43 are arranged on the middle part of the second vertical portion 32 and positioned at the lower section of the second coil pipe of evaporator section 42, and feed-water preheating coil pipe 43 includes multiple flat
The feed-water preheating unit that between-line spacing is set, each feed-water preheating unit is and horizontal direction parallel.Hot coil 44 was evaporated along perpendicular
Nogata is to being arranged in connecting portion 33.
Wherein, the coil pipe unit of each evaporator section first of the first coil pipe of evaporator section 41 tilts 15 ° relative to horizontal direction.Steam
The coil pipe unit of evaporator section second for sending out the second coil pipe of section 42 tilts 15 ° relative to horizontal direction.By said structure relative to level
Direction is obliquely installed, and can reduce dust stratification, improves heat exchange efficiency.In the utility model embodiment, above-mentioned first vertical portion 31,
Two vertical portions 32 and connecting portion 33 are provided with soot blowing component, can be in order to deashing.The dust fraction being cleaned is by sedimentation mouth 26
Discharge, another part are dispersed in flue gas and discharged.
As shown in Fig. 2 also provide a kind of stove of organic waste liquid burning containing sodium salt in the utility model second embodiment, its with
Difference in first embodiment is, is connected with electric cleaner 50 in the lower end of the second vertical portion 32 in this embodiment, is used for
Electric precipitation is carried out to the flue gas of the second vertical portion 32 discharge.Be connected with chimney 60 in the outlet of electric cleaner 50, chimney 60 with
Air-introduced machine is provided between electric cleaner 50, is arranged to tiny structure environment for sodium salt organic waste liquid burning stove will to be contained, is easy to height
Warm flow of flue gas.
The utility model embodiment additionally provides a kind of burning process method, using above-mentioned organic waste liquid burning containing sodium salt
Stove is burned, and burning process method comprises the following steps：
Step 1, after Burning Room 10 is warming up into design temperature, sodium salt organic liquid waste will be contained by being arranged on the top of Burning Room 10
Burner atomization spray into, fully burn and generate high-temperature flue gas；
Step 2, Burning Room 10 bottom change high-temperature flue gas flow direction, make high-temperature flue gas carry out gas-liquid separation,
The slag isolated in high-temperature flue gas is discharged by molten state slag-drip opening 13, and the gas separated in high-temperature flue gas enters transition sedimentation
Room 20；
Step 3, high-temperature gas carry out gas solid separation, the solid particle being separated in high-temperature flue gas in transition expansion chamber 20
Discharged by transition expansion chamber 20, the gas being separated in high-temperature flue gas is entered in heat exchange convection cell 30 and changed with heat-exchanging component
Heat.
Wherein, in step 1, above-mentioned design temperature is 1100 DEG C, and the temperature is much larger than the fusing point of sodium peroxide, makes burning
Inorganic sodium afterwards is completely converted into the sodium peroxide of molten state.
In step 3, the separated gas that Burning Room 10 is discharged (contains molten state sodium peroxide drop, gas temperature
1100 DEG C) cooled down by air distribution component 24 and spray module 25, separated gas temperature is brought down below the fusing point of sodium carbonate
With decomposition temperature (650 DEG C~700 DEG C), molten state sodium peroxide drop is set as often as possible to be converted into sodium carbonate solid particle.
The gas (particle containing solid sodium carbonate and unconverted sodium peroxide drop) that cools enters steam pipe row 23, and cool gas
Body is cooled by reduction of speed, the sodium peroxide drop for not getting transformed into sodium carbonate is fully converted to solid-state, realizes reduction of speed gas solid separation.By
In being provided with separation gear pipe 27, separation gear pipe 27 can reduce solid particle kinetic energy and further promote gas solid separation, formation point
Gas from after.And the sodium carbonate and sodium peroxide solid particle after separating are discharged from sedimentation mouth 26.It should be noted that by mistake
The temperature of the gas crossed after the separation of the discharge of expansion chamber 20 is 350 DEG C~390 DEG C.
Wherein also include in step 3, gas (particulate containing solid sodium carbonate and the peroxide gone out after the separation of transition expansion chamber 20
Change sodium particulate) heat exchange convection cell 30 is entered, by the first coil pipe of evaporator section 41, evaporated hot coil 44, the disk of evaporator section second
Power transmission deduster 50 after pipe 42 and feed-water preheating coil pipe 43 cool.Wherein, the gas temperature of discharge heat exchange convection cell 30 is 200 DEG C
~250 DEG C.
The utility model embodiment also includes step 4, into the dedusting of electric cleaner 50 after gas up to standard, sent through air-introduced machine
Chimney 60 discharges, and the solid sodium carbonate particulate of absorption and sodium peroxide particulate are by collecting and discharging electric precipitation in electric cleaner 50
Device 50.
As can be seen from the above description, the utility model the above embodiments realize following technique effect：Can
The schmutzband reduced on heat-exchanging component is formed, and script can be made to be unable to having for stable operation and passed through with the extension device checking maintenance cycle
The incineration treatment method containing sodium salt of the recovery used heat byproduct steam of Ji property becomes possible to；Meanwhile organic liquid waste can be made full use of
The combustion heat, improve the economy of incinerator operation, make not produce the incinerator of economic benefit originally and bring benefits.
Technological process is simple, and equipment investment is low, takes up an area and saves, and technical process is safe and reliable, in the absence of the technique of danger
And equipment.
It is described above, only specific embodiment of the utility model, it is impossible to which the scope that utility model implemented, institute are limited with it
With the displacement of its equivalent assemblies, or the equivalent variations made according to the utility model patent protection domain and modification, it should all still fall within
The category that this patent is covered.In addition, between technical characteristic and technical characteristic in the utility model, technical characteristic and technical scheme
Between, can be used with independent assortment between technical scheme and technical scheme.
Claims (9)
- A kind of 1. stove of organic waste liquid burning containing sodium salt, it is characterised in that including：Burning Room (10), is vertically set, and Burning Room is provided with burner at the top of (10), be provided with the burner with The organic liquid waste entrance (11) and auxiliary fuel input (12) of Burning Room connection, the sidewall bottom of Burning Room (10) are provided with melting State slag-drip opening (13)；Transition expansion chamber (20), including transition entrance (21) and transition export (22), and transition entrance (21) is horizontally disposed And be connected with Burning Room (10), steam pipe row (23) is provided with transition expansion chamber (20), transition outlet (22) is vertically It is arranged on above steam pipe row (23)；Exchange heat convection cell (30), is connected with transition outlet (22), is provided with multiple heat-exchanging components in heat exchange convection cell (30), this is changed The gas that hot component can discharge with transition expansion chamber (20) carries out heat exchange.
- 2. the stove of organic waste liquid burning containing sodium salt according to claim 1, it is characterised in that the transition of transition expansion chamber (20) Air distribution component (24) and spray module (25) are provided between entrance (21) and steam pipe row (23).
- 3. the stove of organic waste liquid burning containing sodium salt according to claim 1, it is characterised in that the bottom of transition expansion chamber (20) Multiple sedimentation mouths (26) are provided with, sedimentation mouth (26) is located at the lower section of steam pipe row (23).
- 4. the stove of organic waste liquid burning containing sodium salt according to claim 1, it is characterised in that be provided with transition outlet (22) The separation gear pipe (27) of gas solid separation can be carried out.
- 5. the stove of organic waste liquid burning containing sodium salt according to claim 1, it is characterised in that heat exchange convection cell (30) includes the One vertical portion (31), the second vertical portion (32) and connecting portion (33), the second vertical portion 32 are arranged on the side of the first vertical portion 31, The both ends of connecting portion (33) connect the upper end of the first vertical portion (31) and the upper end of the second vertical portion (32), the first vertical portion respectively (31) lower end is connected with transition outlet (22).
- 6. the stove of organic waste liquid burning containing sodium salt according to claim 5, it is characterised in that the heat-exchanging component includes：The coil pipe of evaporator section first (41), it is arranged in the first vertical portion (31), the coil pipe of evaporator section first (41) includes multiple parallel The spaced coil pipe unit of evaporator section first, each coil pipe unit of evaporator section first tilt both with respect to horizontal direction；The coil pipe of evaporator section second (42), is arranged on the top of the second vertical portion (32), and the coil pipe of evaporator section second (42) includes multiple The coil pipe unit of evaporator section second that parallel interval is set, each coil pipe unit of evaporator section second incline both with respect to horizontal direction Tiltedly；Feed-water preheating coil pipe (43), it is arranged on the middle part of the second vertical portion (32) and below the coil pipe of evaporator section second (42), Feed-water preheating coil pipe (43) includes the feed-water preheating unit that multiple parallel intervals are set, each feed-water preheating unit with level Direction is parallel；Hot coil (44) was evaporated, was arranged vertically in connecting portion (33).
- 7. the stove of organic waste liquid burning containing sodium salt according to claim 5, it is characterised in that the first vertical portion (31), second Vertical portion (32) and connecting portion (33) are provided with soot blowing component.
- 8. the stove of organic waste liquid burning containing sodium salt according to claim 1, it is characterised in that along molten state slag-drip opening (13) to The direction of transition entrance (21), the bottom wall of Burning Room (10) are gradually inclined upwardly.
- 9. the stove of organic waste liquid burning containing sodium salt according to claim 1, it is characterised in that along transition entrance (21) to steam The direction of pipe row (23), the bottom wall of transition expansion chamber (20) tilt gradually downward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720622979.5U CN206739319U (en) | 2017-05-31 | 2017-05-31 | The stove of organic waste liquid burning containing sodium salt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720622979.5U CN206739319U (en) | 2017-05-31 | 2017-05-31 | The stove of organic waste liquid burning containing sodium salt |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206739319U true CN206739319U (en) | 2017-12-12 |
Family
ID=60569082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720622979.5U Withdrawn - After Issue CN206739319U (en) | 2017-05-31 | 2017-05-31 | The stove of organic waste liquid burning containing sodium salt |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206739319U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106989405A (en) * | 2017-05-31 | 2017-07-28 | 北京石油化工工程有限公司 | The stove of organic waste liquid burning containing sodium salt and burning process method |
-
2017
- 2017-05-31 CN CN201720622979.5U patent/CN206739319U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106989405A (en) * | 2017-05-31 | 2017-07-28 | 北京石油化工工程有限公司 | The stove of organic waste liquid burning containing sodium salt and burning process method |
| CN106989405B (en) * | 2017-05-31 | 2023-06-02 | 北京石油化工工程有限公司 | Sodium salt-containing organic waste liquid incinerator and incineration process method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105164469B (en) | Include the fluidized-bed combustion boiler of multifunctional inertia gravity separator | |
| CN102425787B (en) | Liquid slag trapping biomass combustion device and method | |
| CN105240861B (en) | A kind of high concentration salty organic waste liquid burning boiler | |
| CN100372605C (en) | Movable sulfurization active carbon heating regenerator and regeneration | |
| CN106755718B (en) | The fume waste heat utilization and dust removal integrated system and technique that pneumatic steelmaking generates | |
| CN109140461A (en) | Dangerous waste high-temperature fusion crystallite purification device and exhaust purifying method | |
| CN204986938U (en) | Energy -conserving dust removal troilite exhaust -heat boiler | |
| CN204388046U (en) | Biomass recirculating fluidized bed boiler | |
| CN112254133A (en) | Novel dangerous waste combustion online coupling plasma melting integrated system | |
| CN106906331A (en) | A kind of dry-method dust-removal device and method for reclaiming converter gas waste heat | |
| CN201724568U (en) | Electric furnace double de-dusting remaining heat reclaim device | |
| CN106433700A (en) | Coke dry quenching dust removal system and process capable of efficiently recovering heat energy | |
| CN106989405A (en) | The stove of organic waste liquid burning containing sodium salt and burning process method | |
| CN106197045A (en) | Afterheat boiler system, rotary hearth furnace high-temperature dust-containing flue gas processing system and method | |
| CN106636502A (en) | Waste heat recovery device for high-temperature slag wind quenching granulation fluidized bed boiler | |
| CN206739319U (en) | The stove of organic waste liquid burning containing sodium salt | |
| CN108546796B (en) | Full-dry type cooling device for converter flue gas and cooling method thereof | |
| CN113073170A (en) | Converter flue gas waste heat recovery system and method | |
| CN202361361U (en) | Liquid deslagging biomass combustion device | |
| CN111578723A (en) | Metallurgical high temperature dust-containing waste gas treatment system | |
| CN206666575U (en) | A kind of dry-method dust-removal device for reclaiming converter gas waste heat | |
| CN214937605U (en) | Converter flue gas waste heat recovery system | |
| CN206337286U (en) | The fume waste heat that pneumatic steelmaking is produced is utilized and dust removal integrated system | |
| CN101893388A (en) | Electric furnace double dust collection and waste heat recovery system and method | |
| CN206244715U (en) | A kind of CDQ Emission Control System of energy high efficiente callback heat energy |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20171212 Effective date of abandoning: 20230602 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20171212 Effective date of abandoning: 20230602 |
|
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |