CN206500032U - It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system - Google Patents
It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system Download PDFInfo
- Publication number
- CN206500032U CN206500032U CN201720132733.XU CN201720132733U CN206500032U CN 206500032 U CN206500032 U CN 206500032U CN 201720132733 U CN201720132733 U CN 201720132733U CN 206500032 U CN206500032 U CN 206500032U
- Authority
- CN
- China
- Prior art keywords
- flue gas
- section
- denitration
- ammonia
- flue
- 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
Links
Landscapes
- Treating Waste Gases (AREA)
- Chimneys And Flues (AREA)
Abstract
The utility model be related to it is a kind of be used for the useless solid, exhaust gas processing device of liquid waste incineration system, including flue gas cool-down section, denitration section, alkali wash section and flue gas ash removal section, the end of the flue gas cool-down section is fixedly connected with the front end of the denitration section；The end of the denitration section is fixedly connected with the front end of the alkali wash section, or, the end of the denitration section is fixedly connected by quench zone with the front end of the alkali wash section；The end of the alkali wash section is fixedly connected with the front end of flue gas ash removal section；When burning useless solid, waste liquid, use exhaust gas processing device of the present utility model, the flue gas that burning is produced successively is flowed through and emitted after flue gas cool-down section, denitration section, quench zone, alkali wash section after flue gas ash removal section dedusting, therefore, device of the present utility model, vent gas treatment process is simple, easy to operate, processing procedure power consumption is low, and the tail gas after processing reaches discharging standards.
Description
Technical field
The utility model belongs to field of Environment Protection, and in particular to a kind of to be used for the vent gas treatment dress of useless solid, liquid waste incineration system
Put.
Background technology
With the fast development of China's economy, the prosperity of industrial agricultural production and the popularization of medical system are generated big
The medical waste liquid of amount, dangerous waste liquid, sludge the like waste, serious pollution is caused to environment.
Liquid waste incineration is that a kind of liquid debris of cleaning is innoxious, minimizing handling process.In order that liquid waste incineration is more
Environmental protection, needs badly and develops a kind of exhaust gas processing device.
Utility model content
In order to solve the environmental issue of liquid waste incineration, the utility model provides a kind of for useless solid, liquid waste incineration system
Exhaust gas processing device.The technical problems to be solved in the utility model is achieved through the following technical solutions：
It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system, including flue gas cool-down section, denitration section, quench zone,
Alkali wash section and flue gas ash removal section, the end of the flue gas cool-down section are fixedly connected with the front end of denitration section；
The end of the denitration section is fixedly connected with the front end of the alkali wash section, or, the end of the denitration section passes through
Quench zone is fixedly connected with the front end of the alkali wash section；
The end of the alkali wash section is fixedly connected with the front end of flue gas ash removal section；
The denitration section is by ammonia distiller, the ammonia water spray device being arranged on ammonia distiller, for carrying out dedusting to incineration flue gas
Cyclone dust collectors, for after dedusting flue gas carry out denitration Benitration reactor, the smoke inlet of the cyclone dust collectors
Locate to be fixedly connected with the exhanst gas outlet of flue gas cool-down section by pipeline, the ammonia distiller, the cyclone dust collectors take off with described
Nitre reactor is connected by pipeline, forms the flue gas flow channel passed through for flue gas；
The ammonia distiller is provided with ammonia still process smoke inlet, and the ammonia still process smoke inlet is drawn from flue gas cool-down section for injection
In ammonia still process flue gas, the top of the ammonia still process smoke inlet is provided with ammonia water spray device；
Denitrification catalyst module is provided with the Benitration reactor, the denitrification catalyst module is used for the flue gas after dedusting
Carry out denitration process.
As a preferred embodiment of the present utility model, the flue gas cool-down section includes hybrid cooling flue and is arranged on
Cooling water feeder on hybrid cooling flue, the smoke inlet of the hybrid cooling flue and the exhanst gas outlet of incinerator lead to
Piping is fixedly connected, and the ammonia still process fume gas extraction port for extracting ammonia still process flue gas is additionally provided with the hybrid cooling flue.
As a preferred embodiment of the present utility model, the quench zone includes flue gas chilling mixing chamber and multiple chillings
Water spray gun, the flue gas chilling mixing chamber is provided with the gun slot that multiple confession chilling water spray guns are passed through；
The smoke inlet of the flue gas chilling mixing chamber is fixed with the exhanst gas outlet of the Benitration reactor by pipeline to be connected
Connect.
As a preferred embodiment of the present utility model, the alkali wash section includes flush water pump, pond, is provided with alkali lye
The alkali lye circulatory pool of circulating pump, flue gas mixing arrangement, the multigroup alkali lye spray equipment for being arranged on flue gas mixing arrangement inner chamber and remove
Mist and flusher, the demisting and flusher are arranged on the top of alkali lye spray equipment；
One end of the flush water pump connects spray gun by water supply line, and the other end connection pond of the water pump is described
Spray gun is arranged on the top of the demisting and flusher.
The beneficial effects of the utility model：
When burning useless solid, waste liquid, using exhaust gas processing device of the present utility model, burn the flue gas produced and successively flow through
Emitted after flue gas cool-down section, denitration section, quench zone, alkali wash section after flue gas ash removal section dedusting, it is therefore, of the present utility model
Device, vent gas treatment process is simple, easy to operate, and processing procedure power consumption is low, and the tail gas after processing reaches discharging standards.
The utility model is described in further details below with reference to drawings and Examples.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model flue gas cool-down section；
Fig. 2 is the structural representation of the utility model denitration section；
Fig. 3 is the structural representation of the utility model quench zone；
Fig. 4 is the structural representation of the utility model alkali wash section.
In figure:11st, cool water feeder；12nd, water pump；13rd, hybrid cooling flue；14th, ammonia still process fume gas extraction port；21、
Ammonia distiller；22nd, ammonia water spray device；23rd, cyclone dust collectors；24th, Benitration reactor；25th, denitrification catalyst module；31st, chilled water (chw)
Spray gun；32nd, flue gas chilling mixing chamber；33rd, chilling water pump；41st, demisting and flusher；42nd, alkali lye spray equipment；43rd, alkali lye
Circulating pump；44th, flue gas mixing arrangement；45th, alkali lye circulatory pool；46th, flush water pump；47th, pond.
Embodiment
Reach technological means and effect that predetermined purpose is taken for the utility model is expanded on further, below in conjunction with accompanying drawing
And embodiment is to embodiment of the present utility model, architectural feature and its effect, describe in detail as follows.
Particularly point out, term of the present utility model " on ", " under ", "left", "right", " top surface ", " bottom surface ", " interior ", " outer "
Orientation or position relationship Deng instruction are, based on orientation shown in the drawings or position relationship, to be for only for ease of and describe this practicality newly
Type and simplified description, rather than instruction or the signified device of hint or element must be with specific orientation, with specific orientation
Construction and operation, therefore it is not intended that to limitation of the present utility model.
Embodiment 1：
Reference picture 1, it is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system, including flue gas cool-down section, denitration
Section, alkali wash section and flue gas ash removal section, the end of the flue gas cool-down section are fixedly connected with the front end of denitration section；
The end of the denitration section is fixedly connected with the front end of the alkali wash section, or, the end of the denitration section passes through
Quench zone is fixedly connected with the front end of the alkali wash section；
The end of the alkali wash section is fixedly connected with the front end of flue gas ash removal section；
The denitration section is by ammonia distiller 21, the ammonia water spray device 22 being arranged on ammonia distiller 21, for entering to incineration flue gas
The cyclone dust collectors 23 of row dedusting, the Benitration reactor 24 for carrying out denitration to the flue gas after dedusting, the cyclone dust collectors
It is fixedly connected at 23 smoke inlet by pipeline with the exhanst gas outlet of flue gas cool-down section, the ammonia distiller 21, the whirlwind are removed
Dirt device 23 is connected with the Benitration reactor 24 by pipeline, forms the flue gas flow channel passed through for flue gas；
The ammonia distiller 21 is provided with ammonia still process smoke inlet, and the ammonia still process smoke inlet is drawn from flue gas cool-down for injection
Ammonia still process flue gas in section, the top of the ammonia still process smoke inlet is provided with ammonia water spray device 22；
Denitrification catalyst module 25 is provided with the Benitration reactor 24, after the denitrification catalyst module 25 is used for dedusting
Flue gas carry out denitration process.
Wherein, the flue gas cool-down section includes hybrid cooling flue 13 and the temperature lowering water being arranged on hybrid cooling flue 13
Feedway 11, the smoke inlet of the hybrid cooling flue 13 is fixedly connected with the exhanst gas outlet of incinerator by pipeline, institute
State the ammonia still process fume gas extraction port 14 being additionally provided with hybrid cooling flue 13 for extracting ammonia still process flue gas.
Wherein, the quench zone includes flue gas chilling mixing chamber 32 and multiple chilling water spray guns 31, and the flue gas chilling is mixed
Close room 32 and be provided with the gun slot that multiple confession chilling water spray guns 31 are passed through；
The smoke inlet of the flue gas chilling mixing chamber 32 is solid by pipeline with the exhanst gas outlet of the Benitration reactor 24
Fixed connection.
Wherein, the alkali wash section includes flush water pump 1246, pond 47, is provided with the alkali lye circulatory pool of NaOH solution circulating pump 43
45th, flue gas mixing arrangement 44, the multigroup alkali lye spray equipment 42 and demisting and flushing dress that are arranged on the inner chamber of flue gas mixing arrangement 44
Put, the demisting and flusher are arranged on the top of alkali lye spray equipment 42；
One end of the flush water pump 1246 connects through water supply line connection spray gun, the other end connection of the water pump 12
Pond 47, the spray gun is arranged on the top of the demisting and flusher.
When burning useless solid, waste liquid, using exhaust gas processing device of the present utility model, burn the flue gas produced and successively flow through
Emitted after flue gas cool-down section, denitration section, quench zone, alkali wash section after flue gas ash removal section dedusting, it is therefore, of the present utility model
Device, vent gas treatment process is simple, easy to operate, and processing procedure power consumption is low, and the tail gas after processing reaches discharging standards.
Embodiment 2：
The useless solid, 26S Proteasome Structure and Function of liquid waste incineration system is described in detail in the present embodiment, specific as follows：
Useless solid, liquid waste incineration system, including liquid waste incineration section, useless solid incineration section, flue gas cool-down section, denitration section, quench zone,
Alkali wash section, seven sub-devices of flue gas ash removal and discharge section.According to disposing waste liquid, it is useless solid and burn the exhaust gas component produced not
Together, assembling operation is carried out from suitable skid sub-device.
Wherein, liquid waste incineration section is main fires incinerator by diesel combustion machine, waste liquid injection apparatus, combustion air blower fan, room
Constitute.Realize liquid waste incineration function.Baker and combustion-supporting is carried out by diesel combustion machine, furnace temperature reaches more than 800 DEG C, then by waste liquid
Spray into burn by liquid waste spray gun and burned completely in burner hearth.Dual firing chamber is provided with tracery wall, is formed by laying fireproof bricks, can be by
Dust and salts substances partly precipitated in the flue gas produced after liquid waste incineration get off, from bottom slag discharge discharge.
Wherein, solid incineration section of giving up is main to be made up of diesel combustion machine, give up solid feed arrangement, rotary kiln.Realize useless solid burning
Function.Baker is carried out and combustion-supporting by diesel combustion machine, furnace temperature reaches more than 800 DEG C, then is sent into useless admittedly by feed arrangement
Burning disposal is carried out in kiln.The part clinker of generation can be discharged by the slag-drip opening of rotary kiln head and afterbody.
Wherein, flue gas cool-down section is main by cooling water feeder 11, water pump 12, spray nozzle, hybrid cooling flue
13 are constituted.Wherein temperature lowering water uses normal temperature industry water.The device front end system is liquid waste incineration section or useless solid incineration section, Liang Zheke
To carry out quick assembly and connection by standby flue and flange.The high-temperature flue gas produced is burned by front end and enters hybrid cooling flue
13, the temperature lowering water sent into spray nozzle is efficiently mixed, and realizes flue gas cool-down.Smoke inlet technological temperature is 800~1200
DEG C, by adjusting cooling water, flue-gas temperature can be made to be down to 500~300 DEG C, with needed for meeting follow-up skid sub-device.
Wherein, denitration section is main by cyclone dust collectors 23, ammoniacal liquor feedway, aqua ammonia pump 12, ammonia distiller 21, ammonia water spray
Device 22, Benitration reactor 24 and denitration conventional catalyst module composition.The device front end system flue gas cool-down section, both can lead to
Cross standby flue and flange carries out quick assembly and connection.Extracting a small amount of flue gas in the ammonia still process fume extraction interface of flue gas cool-down section will
Ammoniacal liquor is evaporated in ammonia distiller 21, is then passed in Benitration reactor 24.In the reactor, it will be dropped by flue gas cool-down section
Flue gas after the gentle dedusting of cyclone dust collectors 23 carries out denitration process.Cyclone dust removal can effectively prevent catalyst blockage.The device
Inlet flue gas technological temperature is 300~400 DEG C.Realize and denitration function is carried out to flue gas using selective catalytic reduction.
Wherein, quench zone is mainly made up of chilling water feeder, water pump 12, quenching apparatus, and wherein chilled water (chw) is using normal
Temperature industrial water.The device front end system is denitration section, and both can carry out quick assembly and connection by standby flue and flange.
The device portal flue gas process temperature is 500~550 DEG C, by adjusting chilling water, can be rapidly reduced to flue-gas temperature
200 DEG C, process time is less than 0.2 second, and bioxin of jumping over easily generates humidity province, realizes and suppresses bioxin low temperature complex functionality.
Wherein, alkali wash section mainly by alkali lye feedway, NaOH solution circulating pump 43, flue gas mixing-chamber, alkali lye spray equipment 42,
Demisting and flusher 41 are constituted.The device front end system is denitration section or quench zone, and both can pass through standby flue and method
Orchid carries out quick assembly and connection.Device is entered by the flue gas after denitration or quenching, with passing through the mist of alkali lye spray equipment 42
Alkali lye after the change abundant haptoreaction in flue gas mixing-chamber.Flue gas is removed at the top of flue gas mixing-chamber by demister in flue gas
Discharged after partial drop.The device portal flue gas process temperature is 150~200 DEG C.Realize flue-gas acid gas remove function.
Wherein, flue gas ash removal and discharge section are mainly set by filtering drum dust removing equipment, smoke exhaust fan, smoke components on-line monitoring
Standby, aiutage is constituted.The device front end system is denitration section, quench zone or alkali wash section, and both can pass through standby flue and method
Orchid carries out quick assembly and connection.The device portal flue gas process temperature is less than 150 DEG C, and flue gas first passes through filter cartridge dust remover removing
Fine dusts in flue gas, then air is discharged into by smoke exhaust fan feeding aiutage.Realize flue gas ash removal, smoke components monitoring and arrange
Hood.
Above content is to combine specific preferred embodiment further detailed description of the utility model, it is impossible to
Assert that specific implementation of the present utility model is confined to these explanations.For the ordinary skill of the utility model art
For personnel, without departing from the concept of the premise utility, some simple deduction or replace can also be made, should all be regarded
To belong to protection domain of the present utility model.
Claims (4)
- Be used for the useless solid, exhaust gas processing device of liquid waste incineration system 1. a kind of, including flue gas cool-down section, denitration section, alkali wash section and Flue gas ash removal section, it is characterised in that the end of the flue gas cool-down section is fixedly connected with the front end of denitration section；The end of the denitration section is fixedly connected with the front end of the alkali wash section, or, the end of the denitration section passes through chilling Section is fixedly connected with the front end of the alkali wash section；The end of the alkali wash section is fixedly connected with the front end of flue gas ash removal section；The denitration section is by ammonia distiller (21), the ammonia water spray device (22) being arranged on ammonia distiller (21), for incineration flue gas Carry out the cyclone dust collectors (23) of dedusting, the Benitration reactor (24) for carrying out denitration to the flue gas after dedusting, the whirlwind It is fixedly connected at the smoke inlet of deduster (23) by pipeline with the exhanst gas outlet of flue gas cool-down section, the ammonia distiller (21), The cyclone dust collectors (23) are connected with the Benitration reactor (24) by pipeline, form the flue gas stream passed through for flue gas Road；The ammonia distiller (21) is provided with ammonia still process smoke inlet, and the ammonia still process smoke inlet is drawn from flue gas cool-down section for injection In ammonia still process flue gas, the top of the ammonia still process smoke inlet is provided with ammonia water spray device (22)；Denitrification catalyst module (25) is provided with the Benitration reactor (24), the denitrification catalyst module (25) is used for dedusting Flue gas afterwards carries out denitration process.
- 2. it is according to claim 1 a kind of for the useless solid, exhaust gas processing device of liquid waste incineration system, it is characterised in that The flue gas cool-down section includes hybrid cooling flue (13) and the cooling water feeder being arranged on hybrid cooling flue (13) (11), the smoke inlet of the hybrid cooling flue (13) is fixedly connected with the exhanst gas outlet of incinerator by pipeline, described mixed Close the ammonia still process fume gas extraction port (14) being additionally provided with cooling flue (13) for extracting ammonia still process flue gas.
- 3. it is according to claim 1 a kind of for the useless solid, exhaust gas processing device of liquid waste incineration system, it is characterised in that The quench zone is included on flue gas chilling mixing chamber (32) and multiple chilling water spray guns (31), the flue gas chilling mixing chamber (32) The gun slot passed through provided with multiple confession chilling water spray guns (31)；The smoke inlet of the flue gas chilling mixing chamber (32) is solid by pipeline with the exhanst gas outlet of the Benitration reactor (24) Fixed connection.
- 4. it is according to claim 1 a kind of for the useless solid, exhaust gas processing device of liquid waste incineration system, it is characterised in that The alkali wash section includes flush water pump (46), pond (47), alkali lye circulatory pool (45), the flue gas for being provided with NaOH solution circulating pump (43) Mixing arrangement (44), the multigroup alkali lye spray equipment (42) for being arranged on flue gas mixing arrangement (44) inner chamber and demisting and flusher (41), the demisting and flusher (41) are arranged on the top of alkali lye spray equipment (42)；One end of the flush water pump (46) connects spray gun by water supply line, and the other end of the water pump connects pond (47), The spray gun is arranged on the top of the demisting and flusher (41).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720132733.XU CN206500032U (en) | 2017-02-14 | 2017-02-14 | It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720132733.XU CN206500032U (en) | 2017-02-14 | 2017-02-14 | It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206500032U true CN206500032U (en) | 2017-09-19 |
Family
ID=59833331
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720132733.XU Active CN206500032U (en) | 2017-02-14 | 2017-02-14 | It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206500032U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107702112A (en) * | 2017-09-29 | 2018-02-16 | 西安山岳环保科技有限公司 | A kind of low discharge skid combined type waste liquid, useless solid burning and exhaust gas treating method |
-
2017
- 2017-02-14 CN CN201720132733.XU patent/CN206500032U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107702112A (en) * | 2017-09-29 | 2018-02-16 | 西安山岳环保科技有限公司 | A kind of low discharge skid combined type waste liquid, useless solid burning and exhaust gas treating method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204593400U (en) | A kind of industry danger waste burning system of multiple physical states | |
| CN104676606B (en) | Innocent treatment method for acrylic acid and ester waste liquid thereof | |
| CN102644922B (en) | Incineration treatment device for nitrogen-containing organic wastes and incineration treatment process | |
| CN100526716C (en) | Plasma medical refuse burning methods | |
| CN113182311B (en) | Dangerous waste treatment system based on medium-temperature pyrolysis and plasma high-temperature melting | |
| CN202141056U (en) | Integration system of hazardous waste burning and burning fly ash melting and solidification | |
| CN102221211A (en) | Melting solidification integrated method and system for incineration of hazardous wastes and incinerated fly ash | |
| CN204735529U (en) | Innoxious processing system of flying dust based on plasma melting | |
| CN106178892A (en) | Exhaust gas treating method and system are reclaimed in a kind of enamel-covered wire pyrolysis | |
| CN102168857B (en) | High-concentration saliferous organic waste liquid incinerator and incineration technique | |
| CN206944178U (en) | A kind of smoke processing system | |
| CN203642210U (en) | Flue gas treatment system for pyrolysis gasifier | |
| CN110360575A (en) | A kind of incineration system at dangerous waste disposition center | |
| CN110186056A (en) | A kind of chemical company's dangerous waste incineration processing method | |
| CN106345183B (en) | A kind of independent dedusting deentrainment tower of two-stage dynamic centrifugal demister composition | |
| CN102564149B (en) | Industrial kiln waste gas purifying and recovery process and industrial kiln waste gas purifying and recovery equipment | |
| CN111928263A (en) | System for utilize rotary kiln to burn burning furnace and handle hazardous waste | |
| CN206478649U (en) | A kind of useless solid combustion processing unit | |
| CN203396254U (en) | Device for reducing generation and emission of sintered dioxin | |
| CN110833763B (en) | Production process and equipment for organic flue gas incineration, desulfurization, dust removal and denitration | |
| CN104165364A (en) | Environment-friendly energy-saving waste incineration disposal device | |
| CN209279686U (en) | A kind of cement kiln water-cooled bypass system | |
| CN206500032U (en) | It is a kind of to be used for the useless solid, exhaust gas processing device of liquid waste incineration system | |
| CN206478656U (en) | A kind of liquid waste incinerator and a kind of liquid waste treating apparatus | |
| CN107726337B (en) | A kind of smoke processing system of garbage disposal furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20181120 Address after: 250100 house 127-1, No. 777, Tang Ye Road, Tang Ye street, Licheng District, Ji'nan, Shandong Patentee after: Shandong Ching hang Environmental Technology Co.,Ltd. Address before: 710000 No. 9 port road, international port area, Xi'an, Shaanxi W5536 Patentee before: XI'AN SHANYUE ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200402 Address after: 250100 Wanda Plaza, hi tech Zone, Ji'nan City, Shandong province Y3-622 Patentee after: SHANDONG RUNTU ENERGY-SAVING ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd. Address before: 250100 house 127-1, No. 777, Tang Ye Road, Tang Ye street, Licheng District, Ji'nan, Shandong Patentee before: Shandong Ching hang Environmental Technology Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220628 Address after: 712000 room 2105, unit 1, building 1, hengdacheng, Taicheng South Road, Yangling District, Xianyang City, Shaanxi Province Patentee after: Wu Yanxia Address before: 250100 y3-622, Wanda Plaza, high tech Zone, Jinan City, Shandong Province Patentee before: SHANDONG RUNTU ENERGY-SAVING ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220812 Address after: 710000 room 207, floor 2, building 4-b1, Xixian financial port, phase I, starting area of Fengdong new town energy gold trade zone, Xixian New District, Xi'an City, Shaanxi Province Patentee after: Xi'an kangbas Thermal Energy Technology Co.,Ltd. Address before: 712000 room 2105, unit 1, building 1, hengdacheng, Taicheng South Road, Yangling District, Xianyang City, Shaanxi Province Patentee before: Wu Yanxia |