CN209309997U - A kind of low concentration sodium salt organic waste liquid burning furnace and incineration system - Google Patents
A kind of low concentration sodium salt organic waste liquid burning furnace and incineration system Download PDFInfo
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- CN209309997U CN209309997U CN201821656315.1U CN201821656315U CN209309997U CN 209309997 U CN209309997 U CN 209309997U CN 201821656315 U CN201821656315 U CN 201821656315U CN 209309997 U CN209309997 U CN 209309997U
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- 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 relates to a kind of low concentration sodium salt organic waste liquid burning furnaces, including burner, vertical tipburn Burning Room, First Transition section, gas solid separation expansion chamber, Π shape convection cell.The utility model further relate to include aforementioned incinerator incineration system, further include waste drains pump, gasifier, electric precipitator, air-introduced machine, chimney and drum, incinerator is exported by incineration flue gas and is sequentially connected with electric precipitator, air-introduced machine and chimney.The utility model will utilize most water and light component organic liquid waste in the self-produced superheated steam gasification organic liquid waste of incineration flue gas, fused solution deslagging (sodium peroxide), sodium peroxide conversion sodium carbonate, gas-solid sedimentation separation, solid particle are disappeared the technological incorporation such as kinetic energy sedimentation separation, equipment (soot blower) deashing, artificial snaking, extend the equipment checking maintenance period, the sodium salt incineration treatment method for the economical recycling waste heat byproduct steam for being unable to stable operation originally is made to become possible.
Description
Technical field
The present invention relates to fine chemistry industry and petrochemical industry, in particular to a kind of low concentration sodium salt organic waste liquid burning
Furnace, incineration system.
Background technique
Burning is that chemical plant handles toxic, harmful waste effective means, and it is anti-to burn the oxidative pyrolysis reacted be under high temperature
It answers.Incineration treatment technology require burn reaction generate high-temperature gas must be quickly cooled down (Quench) to avoid burn back reaction and
The generation of side reaction.The method of Quench generally takes water Quench and waste heat boiler to be quickly cooled down two methods.It is small to amount of waste
Incinerator, the method for generally taking water spray Quench reprocess waste water；The incinerator bigger to waste throughput, generally
The method for being quickly cooled down byproduct steam using waste heat boiler improves the economy of incinerator operation.The low organic liquid waste of concentration,
Its burning process requires supplementation with a large amount of fuel, the water in the waste liquid that gasifies, and reaches incineration temperature.
The burning post-processing of the salt bearing liquid wastes bigger to treating capacity is relatively difficult, especially to sodium salt organic liquid waste.Such as
Fruit does not recycle heat, will lose a large amount of thermal energy, substantially reduces the economy of device operation；If recycling heat, produced after burning
Raw carrying molten state, solid-state sodium peroxide and other inorganic sodiums in flue gas will be attached on heat exchange tube wall, be formed " dirty
Dirty layer " reduces heat exchange efficiency, shortens the equipment cycle of operation, or even be unable to run equipment.
Summary of the invention
The purpose of the present invention is being improved and being innovated for disadvantage present in background technique and problem, a kind of warp is provided
Sodium salt incinerator, incineration system and the incineration treatment method for the recycling waste heat byproduct steam that Ji property is good, stability is strong.
The technical scheme is that construct a kind of low concentration sodium salt organic waste liquid burning furnace, including it is burner, vertical
The top of Burning Room is arranged in tipburn Burning Room, First Transition section, gas solid separation expansion chamber, Π shape convection cell, the burner,
Organic liquid waste and steam entry is arranged in Burning Room upper side, corresponding position setting organic liquid waste and water vapour distribution in Burning Room
Device, positioned at the lower section of burner, funnel shaped molten state slag-drip opening, the Π shape convection cell packet is arranged in the bottom of the Burning Room
The first convection section, the second changeover portion, the second convection section are included, a foot i.e. first of the Π shape convection cell is arranged in the expansion chamber
The first dry ash extraction mouth is arranged in the bottom and connection, bottom of convection section, and the side of expansion chamber passes through First Transition section and Burning Room
Side connection, the first evaporator is set in the First Transition section, the second evaporator is set in expansion chamber, the first convection section and
Third evaporator and the 4th evaporator are respectively set in second convection section, wherein third evaporator is located at the top of expansion chamber, and
Plugging is arranged in lower section, and vapor superheater is arranged in the top of Π shape convection cell i.e. the second changeover portion, sets below the 4th evaporator
Boiler water preheater is set, the corresponding position of the third evaporator, steam superheater and boiler water preheater is provided with soot blower,
The second dry ash extraction mouth is arranged in second convection section bottom of Π shape convection cell, and side is arranged incineration flue gas and exports, and is located at boiler water
Below preheater.
The third evaporator and the 4th evaporator is vertical-type evaporator, including several vertical heat exchange sleeves,
Heat exchanger tube, set header, set header are arranged above heat exchange sleeve, and the heat exchange sleeve includes heat exchange sleeve outer tube and its interior
The heat exchange sleeve inner tube in portion, set header include the set header inner tube for covering header outer tube and its inside, all heat exchange sleeves
The top of inner tube, which is connected to, covers header inner tube, bottom opening, and at least four heat exchanger tubes, heat exchanger tube is arranged around each heat exchange sleeve
Top and bottom be respectively communicated with the upper/lower terminal of heat exchange sleeve outer tube, and be connected to set header outer tube and set header
Space between inner tube, described sleeve pipe header inner tube are provided with saturation boiler water inlet, and set header outer tube setting water, vapour go out
Mouthful.
More preferably, it is uniformly arranged six roots of sensation heat exchanger tube around every heat exchange sleeve, heat exchange sleeve is square array distribution.
The incinerator inner wall lays lining.
First Transition section is arranged cold wind and protects water ejector.
Heat exchange sleeve outer tube lower head in third evaporator, the 4th evaporator is connected with tube bank or across tube bank, reduces shake
It is dynamic.
Another technical solution of the invention be construct a kind of low concentration sodium salt organic liquor incineration system, including incinerator,
Waste drains pump, gasifier, electric precipitator, air-introduced machine, chimney and drum, incinerator by incineration flue gas export with electric precipitator, draw
Blower and chimney are sequentially connected；
The gasifier includes organic liquid waste entrance, organic liquid waste outlet and organic exhaust gas outlet, and organic liquid waste outlet connects
The organic liquid waste and steam entry of incinerator are connect, organic exhaust gas exports the burner of logical waste drains pump connection incinerator；
The top of incinerator is arranged in the drum, and tedge, down-comer are separately connected the first evaporation in incinerator
Device, the second evaporator, third evaporator, steam superheater, the 4th evaporator and boiler water preheater, steam pipe connect steam
Superheater, and gasifier, burner, soot blower are connected by steam superheater；
The air-introduced machine provides negative pressure for incinerator, the electric precipitator of its upstream.
The steel structure support that gasifier and drum pass through incinerator.
The advantages of the present invention: the superheated steam gasification organic liquid waste that the present invention will utilize incineration flue gas self-produced
In most water and light component organic liquid waste, fused solution deslagging (sodium peroxide), sodium peroxide convert sodium carbonate, gas-solid
Sedimentation separation, solid particle disappear the technological incorporation such as kinetic energy sedimentation separation, equipment (soot blower) deashing, artificial snaking, extend equipment
The checking maintenance period makes the sodium salt burning disposal side for the economical recycling waste heat byproduct steam for being unable to stable operation originally
Method becomes possible.
Present invention process process is simple, and equipment investment is low, and land occupation saves, and technical process is safe and reliable, and there is no risk
Technique and equipment.
Third evaporator, the 4th evaporator vertical enable water, vapour Natural Circulation, reduce incinerator operation
Expense, unique heat exchanger tube arrangement improve the fever and chills efficiency of unit volume, reduce equipment investment.
Utilize most water and light component organic liquid waste in the self-produced superheated steam gasification organic liquid waste of incineration flue gas, drop
Low incinerator load, and the earth reduce supplement fuel usage amount, substantially increase incinerator equipment investment and device fortune
Capable economy.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of one embodiment.
Fig. 2 is the heat-exchanging tube bundle component diagram of third evaporator, the 4th evaporator.
Fig. 3 is the heat-exchanging tube bundle layout drawing of third evaporator, the 4th evaporator.
Fig. 4 is the structural schematic diagram of another embodiment.
Specific embodiment
To facilitate the understanding of the present invention, a more comprehensive description of the invention is given in the following sections with reference to the relevant attached drawings.In attached drawing
Give preferred embodiment of the invention.But the invention can be realized in many different forms, however it is not limited to this paper institute
The embodiment of description.On the contrary, purpose of providing these embodiments is make it is more thorough and comprehensive to the disclosure.
It should be noted that when element be considered as " setting " on the other element, it can be directly setting or company
Connect on the other element or may be simultaneously present centering elements.
Unless otherwise defined, the skill of all technical and scientific terms and technical field of the invention used herein
The normally understood meaning of art personnel is identical.Term used in the description is intended merely to describe specifically to implement purpose, is not
It is intended to limit the present invention.
Embodiment 1
As shown in Figure 1, a kind of low concentration sodium salt organic waste liquid burning furnace 1, including burner 101, vertical tipburn burn
Room 102, First Transition section 103, gas solid separation expansion chamber 104, Π shape convection cell 105, the burner 101 are arranged in Burning Room
Organic liquid waste and steam entry 106 is arranged in 102 top, 102 upper side of Burning Room, corresponding position setting in Burning Room 102
Organic liquid waste and water vapour distributor 107, positioned at the lower section of burner 101, the bottom setting of the Burning Room 102 is funnel shaped
Molten state slag-drip opening 108, the Π shape convection cell 105 include the first convection section 121, the second changeover portion 115, the second convection section
122, a foot i.e. bottom of the first convection section 121 and the connection of the Π shape convection cell 105, bottom is arranged in the expansion chamber 104
The first dry ash extraction mouth 109 is arranged in portion, and the side of expansion chamber 104 is connected by the side of First Transition section 103 and Burning Room 102
It is logical, the first evaporator 110 is set in the First Transition section 103, second evaporator 111, the first convection current are set in expansion chamber 104
Third evaporator 112 and the 4th evaporator 113 is respectively set in section 121 and the second convection section 122, wherein third evaporator 112
Positioned at the top of expansion chamber 104, and plugging 114 is arranged in lower section, sets in the top of Π shape convection cell 105 i.e. the second changeover portion 115
Vapor superheater 116 is set, boiler water preheater 117, the third evaporator 112, steam is arranged in the lower section of the 4th evaporator 113
The corresponding position of superheater 116 and boiler water preheater 117 is provided with soot blower 118, the second convection section of Π shape convection cell 105
The second dry ash extraction mouth 119 is arranged in 122 bottoms, and side is arranged incineration flue gas and exports 120, is located at 117 lower section of boiler water preheater.
As shown in Figure 2,3, the third evaporator 112 and the 4th evaporator 113 are vertical-type evaporator, if including
Vertical heat exchange sleeve 130, heat exchanger tube 131, set header 132 are done, set header 132 is arranged above heat exchange sleeve 130, institute
The heat exchange sleeve inner tube 134 that heat exchange sleeve 130 includes heat exchange sleeve outer tube 133 and its inside is stated, set header 132 includes casing
The top connection of the set header inner tube 136 of header outer tube 135 and its inside, all heat exchange sleeve inner tubes 134 covers in header
At least four heat exchanger tubes 131, the top and bottom of heat exchanger tube 131 are arranged in pipe 136, bottom opening, each 130 surrounding of heat exchange sleeve
The upper/lower terminal being respectively communicated with inside heat exchange sleeve outer tube 133, and it is connected to set header outer tube 135 and set header inner tube 136
Between space, described sleeve pipe header inner tube 136 is provided with saturation boiler water inlet 137, and set header outer tube setting water, vapour go out
Mouth 138.
More preferably, it is uniformly arranged six roots of sensation heat exchanger tube 131 around every heat exchange sleeve 130, heat exchange sleeve 130 is square array
Distribution.
1 inner wall of incinerator lays lining.
First Transition section 103 is arranged cold wind and protects water ejector.
133 lower head of heat exchange sleeve outer tube in third evaporator 112, the 4th evaporator 113 is with tube bank or across tube bank phase
Even, vibration is reduced.
Embodiment 2
As shown in figure 4, a kind of low concentration sodium salt organic liquor incineration system, including incinerator 1, waste drains pump 2, gasifier 3,
Electric precipitator 4, air-introduced machine 5, chimney 6 and drum 7, incinerator 1 pass through incineration flue gas outlet 120 and electric precipitator 4, air-introduced machine 5
It is sequentially connected with chimney 6；
The gasifier 3 includes organic liquid waste entrance, organic liquid waste outlet and organic exhaust gas outlet, and organic liquid waste outlet connects
The organic liquid waste and steam entry 106 of incinerator 1 are connect, organic exhaust gas exports the burner that logical waste drains pump 2 connects incinerator 1
101；
The top of incinerator 1 is arranged in the drum 7, and tedge, down-comer are separately connected the first steaming in incinerator 1
Send out device 110, the second evaporator 111, third evaporator 112, steam superheater 116, the 4th evaporator 113 and boiler water preheater
117, steam pipe connects steam superheater 116, and connects gasifier 3, burner 101, soot blower by steam superheater 116
118；
The air-introduced machine 5 is that incinerator 1, the electric precipitator 4 of its upstream provide negative pressure.
Using incinerator steel structure support gasifier and drum, make compact overall structure, occupied area is small.
Using incineration system as described in example 2 burning process the following steps are included:
1. an air-introduced machine is arranged in system, operated under tiny structure；
2. supplement fuel is entered by burner 101, heat up when Burning Room 102 burns, and drives for incinerator 1 and normal
Guarantee that safety is affected and provides supplemental heat when operation；
3. low concentration sodium salt organic liquid waste enters gasifier 3, it is incinerated the superheated steam gasification of flue gas generation；
4. the saturated vapor and light component organic liquid waste even gas distribution that generate in gasifier 3 enter having reached for tiny structure
Burning Room 102 to incineration temperature burns；
5. the organic liquid waste being concentrated in gasifier 3 is sent by waste drains pump 2 to burner 101, steamed by self-produced overheat
Enter the burning of Burning Room 102 for having reached incineration temperature after steam fog；
6. incineration temperature is much higher than sodium peroxide fusing point, the inorganic sodium of the generation after burning is made to be completely converted into molten state
Sodium peroxide；
7. top spray enters furnace after organic liquid waste atomization, burning the sodium peroxide drop even dispersion for burning the molten state generated
In high-temperature gas after burning；Top spray air-flow (drop containing sodium peroxide) is identical with gravity direction, is conducive to gas-liquid separation, avoids liquid
Drip splashing inboard wall of furnace body；
8. changing airflow direction, gas is discharged from 102 side wall of Burning Room, realizes that the sodium peroxide drop of molten state is gentle
Body separation；The sodium peroxide drop of molten state is in 10 bottom collection of Burning Room, gravity flow discharge Burning Room 102；
9. the flue gas (containing molten state sodium peroxide drop) of Burning Room discharge matches air cooling, water-spraying control simultaneously provides reaction
Condition is brought down below flue-gas temperature the fusing point and decomposition temperature of sodium carbonate, promotes molten state sodium peroxide drop as often as possible
It is converted into sodium carbonate solid particle, then is further cooled down by the first evaporator；
10. flue gas (particle containing solid sodium carbonate and unconverted sodium peroxide drop) enters expansion chamber, flue gas (contains solid
Sodium carbonate particle and unconverted sodium peroxide drop) reduction of speed, the second evaporator it is cooling to flue gas (particle containing solid sodium carbonate with
Unconverted sodium peroxide drop) further cooling (the sodium peroxide drop for being not converted into sodium carbonate is made to be fully converted to solid-state)
Plugging is arranged in reduction of speed, top of settling chamber, reduces solid particle kinetic energy, further gas solid separation；Sodium carbonate and mistake after separation
Sodium oxide molybdena solid particle is discharged from expansion chamber, and expansion chamber pipe row is designed as can repairing and Quick replacing structure；
The flue gas (particle containing solid sodium carbonate and sodium peroxide particle) of expansion chamber enters Π shape convection cell out, by the
Soot blower, people is arranged in power transmission dedusting after three evaporators, steam superheater, the 4th evaporator, boiler water preheater cooling, convection cell
Hole, third evaporator, steam superheater, the 4th vertical comb of evaporator, steam superheater square comb, with soot blower or people
Work removes product in the dry ash (solid sodium carbonate particle and sodium peroxide particle) of heat exchange pipe surface, and the dry ash a part blown down is from heavy
Room discharge is dropped, and a part is discharged from the second convection cell bottom, and another part enters electric precipitator with flue gas；
Flue gas (particle containing solid sodium carbonate and sodium peroxide particle) enters qualified discharge after electric precipitator dedusting, removes
Dirt (solid sodium carbonate particle and sodium peroxide particle) collect after electric precipitator is discharged.
Temperature control in burning process is as follows: incineration temperature >=1100 DEG C, flue gas >=1100 DEG C after burning, air distribution water spray
It is cooled to 650 ~ 700 DEG C；By-product steam expansion chamber flue-gas temperature is down to 350 ~ 390 DEG C；Flue gas goes out convection section temperature 200 ~ 250
℃。
The present invention will have using most water in the self-produced superheated steam gasification organic liquid waste of incineration flue gas and light component
Machine waste liquid disappears fused solution deslagging (sodium peroxide), sodium peroxide conversion sodium carbonate, gas-solid sedimentation separation, solid particle
The technological incorporation such as energy sedimentation separation, equipment (soot blower) deashing, artificial snaking, extend the equipment checking maintenance period, and making originally cannot
The sodium salt incineration treatment method of the economical recycling waste heat byproduct steam of stable operation becomes possible.
Present invention process process is simple, and equipment investment is low, and land occupation saves, and technical process is safe and reliable, and there is no risk
Technique and equipment.
Third evaporator, the 4th evaporator vertical enable water, vapour Natural Circulation, reduce incinerator operation
Expense, unique heat exchanger tube arrangement improve the fever and chills efficiency of unit volume, reduce equipment investment.
Utilize most water and light component organic liquid waste in the self-produced superheated steam gasification organic liquid waste of incineration flue gas, drop
Low incinerator load, and the earth reduce supplement fuel usage amount, substantially increase incinerator equipment investment and device fortune
Capable economy.
Embodiment of the present invention is only the description carried out to the preferred embodiment of the present invention, not to the present invention
Conception and scope is defined, and under the premise of not departing from design philosophy of the present invention, engineers and technicians are to this hair in this field
The all variations and modifications that bright technical solution is made should all fall into protection scope of the present invention, the claimed skill of the present invention
Art content, is all described in the claims.
Claims (8)
1. a kind of low concentration sodium salt organic waste liquid burning furnace, it is characterised in that: including burner, vertical tipburn Burning Room,
The top of Burning Room, Burning Room upper side is arranged in one changeover portion, gas solid separation expansion chamber, Π shape convection cell, the burner
Organic liquid waste and steam entry is arranged in face, and corresponding position setting organic liquid waste and water vapour distributor, are located at burning in Burning Room
Funnel shaped molten state slag-drip opening is arranged in the lower section of device, the bottom of the Burning Room, and the Π shape convection cell includes the first convection current
The a foot i.e. bottom of the first convection section of the Π shape convection cell is arranged in section, the second changeover portion, the second convection section, the expansion chamber
Portion is simultaneously connected to, and the first dry ash extraction mouth is arranged in bottom, and the side of expansion chamber is connected to by First Transition section with the side of Burning Room,
First evaporator is set in the First Transition section, the second evaporator, the first convection section and the second convection section are set in expansion chamber
Third evaporator and the 4th evaporator is inside respectively set, wherein third evaporator is located at the top of expansion chamber, and lower section setting is stifled
Pipe, the top of Π shape convection cell i.e. the second changeover portion is interior to be arranged steam superheater, and the lower section setting boiler water of the 4th evaporator is pre-
Hot device, the corresponding position of the third evaporator, steam superheater and boiler water preheater are provided with soot blower, Π shape convection cell
The second convection section bottom be arranged the second dry ash extraction mouth, side be arranged incineration flue gas export, be located at boiler water preheater below.
2. low concentration sodium salt organic waste liquid burning furnace according to claim 1, it is characterised in that: the third evaporation
Device and the 4th evaporator are vertical-type evaporator, including several vertical heat exchange sleeves, heat exchanger tube, set header, casing collection
Case is arranged above heat exchange sleeve, and the heat exchange sleeve includes the heat exchange sleeve inner tube of heat exchange sleeve outer tube and its inside, casing
Header includes covering the set header inner tube of header outer tube and its inside, the top connection set header of all heat exchange sleeve inner tubes
At least four heat exchanger tubes are arranged around each heat exchange sleeve in inner tube, bottom opening, and the top and bottom of heat exchanger tube, which are respectively communicated with, to be changed
The upper/lower terminal of thermal sleeve outer tube, and be connected to set header outer tube and cover the space between header inner tube, described sleeve pipe
Header inner tube is provided with saturation boiler water inlet, and water, vapor outlet is arranged in set header outer tube.
3. low concentration sodium salt organic waste liquid burning furnace according to claim 2, it is characterised in that: every heat exchange sleeve week
It encloses and is uniformly arranged six roots of sensation heat exchanger tube, heat exchange sleeve is square array distribution.
4. low concentration sodium salt organic waste liquid burning furnace according to claim 1, it is characterised in that: in the incinerator
Wall lays lining.
5. low concentration sodium salt organic waste liquid burning furnace according to claim 1, it is characterised in that: the setting of First Transition section
Cold wind protects water ejector.
6. low concentration sodium salt organic waste liquid burning furnace according to claim 2, it is characterised in that: third evaporator,
Heat exchange sleeve outer tube lower head in four evaporators is connected with tube bank or across tube bank, reduces vibration.
7. a kind of low concentration sodium salt organic waste liquid burning system, it is characterised in that: including as claimed in any one of claims 1 to 6
Low concentration sodium salt organic waste liquid burning furnace, waste drains pump, gasifier, electric precipitator, air-introduced machine, chimney and drum, low concentration contain
Sodium salt organic waste liquid burning furnace is exported by incineration flue gas and is sequentially connected with electric precipitator, air-introduced machine and chimney；
The gasifier includes organic liquid waste entrance, organic liquid waste outlet and organic exhaust gas outlet, and organic liquid waste outlet connection is low
The organic liquid waste and steam entry of concentration sodium salt organic waste liquid burning furnace, organic exhaust gas outlet are connected low dense by waste drains pump
Spend the burner of sodium salt organic waste liquid burning furnace；
The top of low concentration sodium salt organic waste liquid burning furnace is arranged in the drum, and tedge, down-comer are separately connected low
The first evaporator, the second evaporator, third evaporator, steam superheater, the 4th in concentration sodium salt organic waste liquid burning furnace
Evaporator and boiler water preheater, steam pipe connects steam superheater, and connects gasifier, burning by steam superheater
Device, soot blower；
The air-introduced machine provides negative pressure for low concentration sodium salt organic waste liquid burning furnace, the electric precipitator of its upstream.
8. low concentration sodium salt organic waste liquid burning system according to claim 7, it is characterised in that: gasifier and drum
Pass through the steel structure support of low concentration sodium salt organic waste liquid burning furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821656315.1U CN209309997U (en) | 2018-10-12 | 2018-10-12 | A kind of low concentration sodium salt organic waste liquid burning furnace and incineration system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821656315.1U CN209309997U (en) | 2018-10-12 | 2018-10-12 | A kind of low concentration sodium salt organic waste liquid burning furnace and incineration system |
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Family
ID=67670844
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109210551A (en) * | 2018-10-12 | 2019-01-15 | 岳阳钟鼎热工电磁科技有限公司 | A kind of low concentration sodium salt organic waste liquid burning furnace, incineration system and burning process |
| CN112197281A (en) * | 2020-08-24 | 2021-01-08 | 浙江天成工程设计有限公司 | Incineration process treatment system for organic waste liquid |
-
2018
- 2018-10-12 CN CN201821656315.1U patent/CN209309997U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109210551A (en) * | 2018-10-12 | 2019-01-15 | 岳阳钟鼎热工电磁科技有限公司 | A kind of low concentration sodium salt organic waste liquid burning furnace, incineration system and burning process |
| CN112197281A (en) * | 2020-08-24 | 2021-01-08 | 浙江天成工程设计有限公司 | Incineration process treatment system for organic waste liquid |
| CN112197281B (en) * | 2020-08-24 | 2023-02-14 | 浙江天成工程设计有限公司 | Incineration process treatment system for organic waste liquid |
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Effective date of registration: 20210812 Address after: 710006 Room 302, floor 3, Shaanxi Jian'an building, No. 158, north section of Zhuque street, Beilin District, Xi'an City, Shaanxi Province Patentee after: Shaanxi rejude Engineering Technology Co.,Ltd. Address before: 414000 Yongji Road, LINGJI Linggang industrial new area, Yueyanglou District, Yueyang City, Hunan Province Patentee before: YUEYANG MAPOWER THERMPROCESS & ELECTROMAGNETIC TECHNOLOGY Co.,Ltd. |
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