CN106365232A - Low-temperature sprinkling and evaporation treatment method for desulfurization waste water - Google Patents

Low-temperature sprinkling and evaporation treatment method for desulfurization waste water Download PDF

Info

Publication number
CN106365232A
CN106365232A CN201611004482.3A CN201611004482A CN106365232A CN 106365232 A CN106365232 A CN 106365232A CN 201611004482 A CN201611004482 A CN 201611004482A CN 106365232 A CN106365232 A CN 106365232A
Authority
CN
China
Prior art keywords
desulfurization wastewater
desulfurization
air
waste water
treatment
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.)
Pending
Application number
CN201611004482.3A
Other languages
Chinese (zh)
Inventor
李蜀生
姜衍更
马春元
李吉业
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qingdao Daneng Environmental Protection Equipment Inc Co
Original Assignee
Qingdao Daneng Environmental Protection Equipment Inc Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Qingdao Daneng Environmental Protection Equipment Inc Co filed Critical Qingdao Daneng Environmental Protection Equipment Inc Co
Priority to CN201611004482.3A priority Critical patent/CN106365232A/en
Publication of CN106365232A publication Critical patent/CN106365232A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/10Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
    • C02F1/12Spray evaporation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/18Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The invention discloses a low-temperature sprinkling and evaporation treatment method for desulfurization waste water, comprising the steps: (1) storage; (2) settling treatment; (3) overflowing treatment; (4) evaporation treatment: countercurrent flowing and uniformly mixing air with atomized and sprinkled desulfurization waste water in an evaporation tower, evaporating the desulfurization waste water to be carried by air which achieves a saturated state at the temperature; (5) demisting treatment: removing large-particle-size liquid drops carried by the saturated moist air with a high-efficiency demister; and (6) final treatment: flowing clean saturated moist air into a desulfurization tower. The low-temperature sprinkling and evaporation treatment method for desulfurization waste water has simple process, low investment and low running cost, realizes cyclic utilization of the desulfurization waste water and zero discharge of the desulfurization waste water, and can be widely applied to desulfurization waste water treatment of flue gas desulfurization systems in station boilers and industrial boilers.

Description

Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater
Technical field
The present invention relates to a kind of low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater, can be widely applied to station boiler, industry During the desulfurization wastewater of boiler flue gas desulfurization system is processed.
Background technology
Serosity in flue gas desulfurization, in continuous cyclic process, can be enriched with cl- and heavy metal ion, one side acceleration equipment Corrosion, on the other hand affect the quality of Gypsum Fibrosum.Therefore, flue gas desulphurization system will discharge a certain amount of desulfurization slurry, to reduce Cl- and concentration of heavy metal ion in serosity.Desulfurization slurry after the process of Gypsum Fibrosum cyclone, separate from serosity by Gypsum Fibrosum, Remaining waste water is desulfurization wastewater, containing heavy metal ion, substantial amounts of solid suspension and high concentration in desulfurization wastewater Dissolubility salt is it is necessary to could discharge after treatment or reuse.
At present, three commonly used header desulfuration waste water treatment process it is impossible to remove desulfurization wastewater middle and high concentration chlorine from Son, therefore this technique can not meet the requirement of desulfurization wastewater zero-emission.
Content of the invention
It is an object of the invention to provide a kind of process is simple, investment is low, operating cost is low, desulfurization wastewater recycles, Realize the low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of desulfurization wastewater zero-emission.
In order to achieve the above object, low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, comprising:
(1) store
The desulfurization wastewater that desulfurizing tower interruption is discharged is stored in hermetic container;
(2) clarifying treatment
After hermetic container reaches certain storage capacity, desulfurization wastewater enters depositing reservoir, carries out clarifying treatment, shape by mixer. Become the desulfurization wastewater supernatant and bottom sediment, the desulfurization wastewater supernatant carries out overflow process, and bottom sediment enters dirt Mud treatment system;
(3) overflow is processed
The desulfurization wastewater supernatant in depositing reservoir is processed from overflow to run-off;
(4) evaporation process
(4.1) desulfurization wastewater that will flow out from run-off, using circulating pump by desulfurization wastewater continuous drawing to evaporating column top, with Desulfurization wastewater relies on free gravity to drop back into bottom afterwards;
(4.2) utilize heater, desulfurization wastewater is heated to 40 DEG C ~ 100 DEG C temperature;
(4.3) utilize atomizing sprayer, the desulfurization wastewater after heating is carried out continuously atomizing spray in evaporating column, and desulfurization is given up Water uniform atomizing;
(4.4) meanwhile, ambient air is constantly extracted by supply air system and be passed through evaporating column;
(4.5) air and the desulfurization wastewater after atomizing spray reverse flow uniformly mixing in evaporating column, desulfurization wastewater evaporates And carried by air, air reaches saturation at a temperature of this;
(4.6) after running a period of time, evaporation tower bottom can concentrate generation crystallization, solid sediment, enters at sludge treating system Reason;
(5) demisting is processed
Using high-efficiency demisting apparatus, remove the big particle diameter drop that saturated moist air carries;
(6) final process
Clean saturated moist air flows into desulfurizing tower.
Low temperature spraying and sprinkling evaporation desulfurization wastewater treatment system of the present invention, its operation principle is: it is airtight that desulfurization wastewater passes through water storage Container enters depositing reservoir, and from overflow to overflow pond, the desulfurization wastewater that will flow out from run-off, using following for the depositing reservoir supernatant Desulfurization wastewater reverse flow in evaporating column by desulfurization wastewater continuous drawing to evaporating column top, after air and atomizing spray for the ring pump Move and uniformly mix, desulfurization wastewater evaporates and simultaneously carried by air, and air reaches saturation at a temperature of this.Desulfurization wastewater is through spray Device back flows back into evaporation tower bottom, forms desulfurization wastewater blood circulation, desulfurization wastewater recycles, and realizes desulfurization wastewater zero-emission Put.
Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, its operation principle is: the desulfurization wastewater after heating is steaming Send out tower top and carry out atomizing spray, the reverse uniform contact of desulfurization wastewater after the bottom-up flowing of air, with atomization;The sky being passed through Gas reaches the saturation under uniform temperature, and the desulfurization wastewater carrying evaporation enters the high efficiency demister of evaporating column afterbody, air In big particle diameter drop be removed after, crystallization saturated moist air subsequently enter desulfurizing tower, desulfurization wastewater recycles, and realizes desulfurization Wastewater zero discharge.
Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, after continuous work a period of time, depositing reservoir and evaporating column Bottom can concentrate generation crystallization, solid sediment, is periodically delivered to sludge treating system.
Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, the experiment proved that, compared with traditional treatment method, technique Simply, investment is low, and operating cost is low.
In sum, low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, process is simple, invest low, operating cost Low, desulfurization wastewater recycles, and realizes desulfurization wastewater zero-emission.
Brief description
Below in conjunction with drawings and Examples, the present invention is further illustrated.
Fig. 1 is the process chart of the present invention.
Specific embodiment
Embodiment 1:
Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, comprising:
(1) store
The desulfurization wastewater that desulfurizing tower interruption is discharged is stored in hermetic container;
(2) clarifying treatment
After hermetic container reaches certain storage capacity, desulfurization wastewater enters depositing reservoir, carries out clarifying treatment, shape by mixer. Become the desulfurization wastewater supernatant and bottom sediment, the desulfurization wastewater supernatant carries out overflow process, and bottom sediment enters dirt Mud treatment system;
(3) overflow is processed
The desulfurization wastewater supernatant in depositing reservoir is processed from overflow to run-off;
(4) evaporation process
(4.1) desulfurization wastewater that will flow out from run-off, using circulating pump by desulfurization wastewater continuous drawing to evaporating column top, with Desulfurization wastewater relies on free gravity to drop back into bottom afterwards;
(4.2) utilize heater, desulfurization wastewater is heated to 40 DEG C of temperature;
(4.3) utilize atomizing sprayer, the desulfurization wastewater after heating is carried out continuously atomizing spray in evaporating column, and desulfurization is given up Water uniform atomizing;
(4.4) meanwhile, ambient air is constantly extracted by supply air system and be passed through evaporating column;
(4.5) air and the desulfurization wastewater after atomizing spray reverse flow uniformly mixing in evaporating column, desulfurization wastewater evaporates And carried by air, air reaches saturation at a temperature of this;
(4.6) after running a period of time, evaporation tower bottom can concentrate generation crystallization, solid sediment, enters at sludge treating system Reason;
(5) demisting is processed
Using high-efficiency demisting apparatus, remove the big particle diameter drop that saturated moist air carries;
(6) final process
Clean saturated moist air flows into desulfurizing tower.
Embodiment 2:
Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, comprising:
The desulfurization wastewater that desulfurizing tower interruption is discharged is stored in hermetic container;
(2) clarifying treatment
After hermetic container reaches certain storage capacity, desulfurization wastewater enters depositing reservoir, carries out clarifying treatment, shape by mixer. Become the desulfurization wastewater supernatant and bottom sediment, the desulfurization wastewater supernatant carries out overflow process, and bottom sediment enters dirt Mud treatment system;
(3) overflow is processed
The desulfurization wastewater supernatant in depositing reservoir is processed from overflow to run-off;
(4) evaporation process
(4.1) desulfurization wastewater that will flow out from run-off, using circulating pump by desulfurization wastewater continuous drawing to evaporating column top, with Desulfurization wastewater relies on free gravity to drop back into bottom afterwards;
(4.2) utilize heater, desulfurization wastewater is heated to 100 DEG C of temperature;
(4.3) utilize atomizing sprayer, the desulfurization wastewater after heating is carried out continuously atomizing spray in evaporating column, and desulfurization is given up Water uniform atomizing;
(4.4) meanwhile, ambient air is constantly extracted by supply air system and be passed through evaporating column;
(4.5) air and the desulfurization wastewater after atomizing spray reverse flow uniformly mixing in evaporating column, desulfurization wastewater evaporates And carried by air, air reaches saturation at a temperature of this;
(4.6) after running a period of time, evaporation tower bottom can concentrate generation crystallization, solid sediment, enters at sludge treating system Reason;
(5) demisting is processed
Using high-efficiency demisting apparatus, remove the big particle diameter drop that saturated moist air carries;
(6) final process
Clean saturated moist air flows into desulfurizing tower.
Embodiment 3:
Low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater of the present invention, comprising:
(1) store
The desulfurization wastewater that desulfurizing tower interruption is discharged is stored in hermetic container;
(2) clarifying treatment
After hermetic container reaches certain storage capacity, desulfurization wastewater enters depositing reservoir, carries out clarifying treatment, shape by mixer. Become the desulfurization wastewater supernatant and bottom sediment, the desulfurization wastewater supernatant carries out overflow process, and bottom sediment enters dirt Mud treatment system;
(3) overflow is processed
The desulfurization wastewater supernatant in depositing reservoir is processed from overflow to run-off;
(4) evaporation process
(4.1) desulfurization wastewater that will flow out from run-off, using circulating pump by desulfurization wastewater continuous drawing to evaporating column top, with Desulfurization wastewater relies on free gravity to drop back into bottom afterwards;
(4.2) utilize heater, desulfurization wastewater is heated to 70 DEG C of temperature;
(4.3) utilize atomizing sprayer, the desulfurization wastewater after heating is carried out continuously atomizing spray in evaporating column, and desulfurization is given up Water uniform atomizing;
(4.4) meanwhile, ambient air is constantly extracted by supply air system and be passed through evaporating column;
(4.5) air and the desulfurization wastewater after atomizing spray reverse flow uniformly mixing in evaporating column, desulfurization wastewater evaporates And carried by air, air reaches saturation at a temperature of this;
(4.6) after running a period of time, evaporation tower bottom can concentrate generation crystallization, solid sediment, enters at sludge treating system Reason;
(5) demisting is processed
Using high-efficiency demisting apparatus, remove the big particle diameter drop that saturated moist air carries;
(6) final process
Clean saturated moist air flows into desulfurizing tower.

Claims (1)

1. a kind of low temperature spraying and sprinkling evaporation method for treating desulfurized wastewater is it is characterised in that include:
(1) store
The desulfurization wastewater that desulfurizing tower interruption is discharged is stored in hermetic container;
(2) clarifying treatment
After hermetic container reaches certain storage capacity, desulfurization wastewater enters depositing reservoir, carries out clarifying treatment, shape by mixer. Become the desulfurization wastewater supernatant and bottom sediment, the desulfurization wastewater supernatant carries out overflow process, and bottom sediment enters dirt Mud treatment system;
(3) overflow is processed
The desulfurization wastewater supernatant in depositing reservoir is processed from overflow to run-off;
(4) evaporation process
(4.1) desulfurization wastewater that will flow out from run-off, using circulating pump by desulfurization wastewater continuous drawing to evaporating column top, with Desulfurization wastewater relies on free gravity to drop back into bottom afterwards;
(4.2) utilize heater, desulfurization wastewater is heated to 40 DEG C ~ 100 DEG C temperature;
(4.3) utilize atomizing sprayer, the desulfurization wastewater after heating is carried out continuously atomizing spray in evaporating column, and desulfurization is given up Water uniform atomizing;
(4.4) meanwhile, ambient air is constantly extracted by supply air system and be passed through evaporating column;
(4.5) air and the desulfurization wastewater after atomizing spray reverse flow uniformly mixing in evaporating column, desulfurization wastewater evaporates And carried by air, air reaches saturation at a temperature of this;
(4.6) after running a period of time, evaporation tower bottom can concentrate generation crystallization, solid sediment, enters at sludge treating system Reason;
(5) demisting is processed
Using high-efficiency demisting apparatus, remove the big particle diameter drop that saturated moist air carries;
(6) final process
Clean saturated moist air flows into desulfurizing tower.
CN201611004482.3A 2016-11-15 2016-11-15 Low-temperature sprinkling and evaporation treatment method for desulfurization waste water Pending CN106365232A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611004482.3A CN106365232A (en) 2016-11-15 2016-11-15 Low-temperature sprinkling and evaporation treatment method for desulfurization waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611004482.3A CN106365232A (en) 2016-11-15 2016-11-15 Low-temperature sprinkling and evaporation treatment method for desulfurization waste water

Publications (1)

Publication Number Publication Date
CN106365232A true CN106365232A (en) 2017-02-01

Family

ID=57894306

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611004482.3A Pending CN106365232A (en) 2016-11-15 2016-11-15 Low-temperature sprinkling and evaporation treatment method for desulfurization waste water

Country Status (1)

Country Link
CN (1) CN106365232A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108144429A (en) * 2018-01-03 2018-06-12 中国华电科工集团有限公司 A kind of system and method for preventing dry nozzle fouling
CN109395568A (en) * 2018-12-17 2019-03-01 新疆天富集团有限责任公司 A kind of low water consumption wet desulphurization method
CN110577313A (en) * 2019-10-11 2019-12-17 国电科学技术研究院有限公司 desulfurization wastewater zero-discharge treatment system and method
CN113184932A (en) * 2021-04-26 2021-07-30 武汉天空蓝环保科技有限公司 Utilize flue gas evaporative concentration device and desulfurization effluent disposal system

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101417826A (en) * 2007-10-26 2009-04-29 余乐 Method and system for processing desulphurization waste water
CN102489136A (en) * 2011-12-16 2012-06-13 国电环境保护研究院 Flue gas desulfurizing waste water recovering process and device
CN203807290U (en) * 2014-04-28 2014-09-03 盛发环保科技(厦门)有限公司 Novel waste heat utilization zero release device of desulfurization waste water
CN104624029A (en) * 2015-01-06 2015-05-20 山东大学 Device for integrating cooling tower, desulfurizing tower and chimney, and desulfurizing method
CN204569462U (en) * 2015-04-09 2015-08-19 西安热工研究院有限公司 Neat stress recirculation type desulfurization wastewater spraying treatment unit
CN204714545U (en) * 2015-05-14 2015-10-21 国网山西省电力公司电力科学研究院 Flue waste water evaporation desulphurization system
CN204786491U (en) * 2015-07-15 2015-11-18 南京龙源环保有限公司 Boiler smoke waste -heat application system
CN105481157A (en) * 2015-12-18 2016-04-13 王辛平 Method for zero emission treatment of desulfurization waste water based on flue gas waste heat evaporation
CN105585198A (en) * 2016-02-29 2016-05-18 西安西热水务环保有限公司 High-efficiency economical thermal power plant tail end desulfurization wastewater softening and evaporation treatment system and method

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101417826A (en) * 2007-10-26 2009-04-29 余乐 Method and system for processing desulphurization waste water
CN102489136A (en) * 2011-12-16 2012-06-13 国电环境保护研究院 Flue gas desulfurizing waste water recovering process and device
CN203807290U (en) * 2014-04-28 2014-09-03 盛发环保科技(厦门)有限公司 Novel waste heat utilization zero release device of desulfurization waste water
CN104624029A (en) * 2015-01-06 2015-05-20 山东大学 Device for integrating cooling tower, desulfurizing tower and chimney, and desulfurizing method
CN204569462U (en) * 2015-04-09 2015-08-19 西安热工研究院有限公司 Neat stress recirculation type desulfurization wastewater spraying treatment unit
CN204714545U (en) * 2015-05-14 2015-10-21 国网山西省电力公司电力科学研究院 Flue waste water evaporation desulphurization system
CN204786491U (en) * 2015-07-15 2015-11-18 南京龙源环保有限公司 Boiler smoke waste -heat application system
CN105481157A (en) * 2015-12-18 2016-04-13 王辛平 Method for zero emission treatment of desulfurization waste water based on flue gas waste heat evaporation
CN105585198A (en) * 2016-02-29 2016-05-18 西安西热水务环保有限公司 High-efficiency economical thermal power plant tail end desulfurization wastewater softening and evaporation treatment system and method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108144429A (en) * 2018-01-03 2018-06-12 中国华电科工集团有限公司 A kind of system and method for preventing dry nozzle fouling
CN108144429B (en) * 2018-01-03 2024-06-21 中国华电科工集团有限公司 System and method for preventing scaling of drying nozzle
CN109395568A (en) * 2018-12-17 2019-03-01 新疆天富集团有限责任公司 A kind of low water consumption wet desulphurization method
CN110577313A (en) * 2019-10-11 2019-12-17 国电科学技术研究院有限公司 desulfurization wastewater zero-discharge treatment system and method
CN113184932A (en) * 2021-04-26 2021-07-30 武汉天空蓝环保科技有限公司 Utilize flue gas evaporative concentration device and desulfurization effluent disposal system

Similar Documents

Publication Publication Date Title
CN101417826B (en) Method and system for processing desulphurization waste water
CN101417827B (en) Technique method for processing desulphurization waste water
CN106365232A (en) Low-temperature sprinkling and evaporation treatment method for desulfurization waste water
CN104129824B (en) Heat-engine plant desulfurized wastewater comprehensive treatment and dust granules thing discharge-reducing method
CN101417828B (en) Method and system for processing desulphurization waste water
CN102423613B (en) Ammonia desulfurization method for effectively removing chlorine and fluorine ions and heavy metal ions
CN111362342A (en) Wastewater zero discharge system and method for multi-stage treatment
WO2017177741A1 (en) Device and method for treating desulfurization wastewater by means of flue multi-stage evaporation
CN105879542A (en) Power plant desulfurization wastewater bypass treatment system and method and flue gas treatment system and method
CN109399855A (en) A kind of zero emission treatment of desulfured waste water
CN105967253A (en) Evaporation process and device of desulfurized wastewater cooling tower
CN201669043U (en) Ammonia flue gas desulfurization device
CN205760591U (en) A kind of efficient desulfurizing tower with giant
CN205500970U (en) Useless pretreatment of water system suitable for desulfurization waste water spray evaporation processing system
CN106865667A (en) A kind of desulfurization wastewater fume afterheat concentrates abatement system and its technique
CN207797091U (en) A kind of device for realizing desulfurization wastewater zero-emission using full flue gas
CN101703877A (en) Amino smoke discharging and purifying device
CN113277663A (en) Desulfurization wastewater zero-discharge treatment process
CN208762185U (en) A kind of energy-saving system suitable for handling desulfurization wastewater
CN208898533U (en) A kind of Zero discharging system of power plant desulfurization wastewater
CN217103333U (en) Desulfurization waste water zero release processing system
CN206635166U (en) Desulfurization wastewater sludge treatment equipment
CN109589750A (en) Fluorine technique is gone in a kind of economical desulfurization of aluminium electrolytic flue
CN201543374U (en) Ammonia-method flue gas desulfurization device
CN212451029U (en) Zero discharge system of sintering plant desulfurization waste water resourceization

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170201