CN104059187A - Super-macroporous adsorbent resin and preparation method thereof - Google Patents

Super-macroporous adsorbent resin and preparation method thereof Download PDF

Info

Publication number
CN104059187A
CN104059187A CN201410251408.6A CN201410251408A CN104059187A CN 104059187 A CN104059187 A CN 104059187A CN 201410251408 A CN201410251408 A CN 201410251408A CN 104059187 A CN104059187 A CN 104059187A
Authority
CN
China
Prior art keywords
parts
reaction
macroporous adsorbent
adsorbent resin
pore
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.)
Granted
Application number
CN201410251408.6A
Other languages
Chinese (zh)
Other versions
CN104059187B (en
Inventor
曹先军
王凤德
梁克俭
赵奕
李智
高川
余海燕
陈燕
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.)
Lan-Star (chengdu) New Material Co Ltd
Original Assignee
Lan-Star (chengdu) New Material Co Ltd
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 Lan-Star (chengdu) New Material Co Ltd filed Critical Lan-Star (chengdu) New Material Co Ltd
Priority to CN201410251408.6A priority Critical patent/CN104059187B/en
Publication of CN104059187A publication Critical patent/CN104059187A/en
Application granted granted Critical
Publication of CN104059187B publication Critical patent/CN104059187B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

The invention relates to a super-macroporous adsorbent resin and a preparation method thereof, belonging to the field of high polymer materials. The super-macroporous adsorbent resin is prepared from the following raw materials in parts by weight: 50-70 parts of divinylbenzene, 5-10 parts of styrene, 10-20 parts of glycol bis-methacrylate, 5-10 parts of polystyrene, 50-80 parts of diethyl phthalate, 30-50 parts of 200# gasoline, 1-2 parts of diphenyl acyl peroxide, 150-200 parts of deionized water and 1-2 parts of polyvinyl alcohol. The polystyrene and diethyl phthalate used as the pore-forming agent component for preparing the super-macroporous adsorbent resin increase the pore size of the resin and widen the application range of the resin. The second crosslinking agent increases the pore size of the resin, ensures the mechanical strength of the resin and provides the service life of the resin.

Description

A kind of especially big macroporous adsorbent resin and preparation method thereof
Technical field
The present invention relates to a kind of polymeric adsorbent and preparation method thereof, more particularly, the present invention relates to a kind of especially big macroporous adsorbent resin and preparation method thereof, belong to technical field of polymer materials.
Technical background
Macroporous adsorbent resin is that a class is containing cation exchange groups and there is the preparation of macroporous structure, there is good macroporous netlike structure and larger specific surface area, can be by physical adsorption adsorb organic compound selectively from the aqueous solution, be the novel organic polymer sorbent material growing up the sixties in 20th century, be widely used in environmental protection, food, medicine and other fields.
Macroporous adsorbent resin claims again full porous adsorption resin, and macroporous adsorbent resin is to be prepared from through polyreaction by additives such as polymerization single polymerization monomer and linking agent, pore-creating agent, dispersion agents.After polymer formation, pore-creating agent is removed, and has left hole big and small, different, that interpenetrate in resin.Therefore macroporous adsorbent resin its inside under drying regime has higher porosity, and aperture is larger, between 100-1000nm.
It is CN101058068 that State Intellectual Property Office discloses a publication number in 2007.10.24, name is called the patent of invention of " a kind of macroporous adsorption resin special used for separating antibiotic and preparation method thereof ", this patent is taking styrene-divinylbenzene macropore copolymerization bead (St-DVB Archon) as starting material, adopt 2 ~ 4 kinds of function monomers and linking agent, under the condition existing in peroxide initiator, water and minerals, carrying out the two nets of secondary, to pass through mutually crosslinking copolymerization reaction synthetic.The formula of St-DVB Archon comprises a certain proportion of: vinylbenzene, 80% Vinylstyrene, dibenzoyl peroxide, pore-creating agent (toluene, whiteruss and gasoline etc.), gelatin and distilled water.The formula that the two nets of secondary pass through crosslinking copolymerization reaction mutually comprises a certain proportion of: St-DVB Archon, 2 ~ 4 kinds of function monomers, peroxide initiator, inert diluent, stablizer and distilled water.Synthesized resin reaches 185ku/g to the equilibrium adsorption capacity of erythromycin in streptomyces erythreus fermentation cleaner liquid, is 140% of conventional polymeric adsorbent, and its selection to pigment in fermented liquid is removed the more conventional resin of ability and improved 70-90%.
It is CN101070400 that State Intellectual Property Office discloses a publication number in 2007.11.14, name is called the patent of invention of " a kind of preparation method of imidazole modified styrene tyle macroporous adsorption resin ", and this patent provides a kind of preparation method of imidazole modified styrene tyle macroporous adsorption resin.Its preparation method divides two steps, first by the salt-forming reaction of imidazoles, on 1, introduce particular functional group, realize the functionalization of imidazoles, and then react with the styrene tyle macroporous adsorption resin of chlorination reaction, realize styrene tyle macroporous adsorption resin imidazole modified.The present invention is introduced into the imidazol ion of functionalization in styrene tyle macroporous adsorption resin, utilize the physicochemical property of imidazol ion uniqueness and the controllability of physico-chemical property thereof, both polarity and the wetting ability of resin can be increased, the separation and purification scope of styrenic macroporous adsorbent resin in the field such as food, medicine can be widened again.
Macroporous adsorbent resin has a wide range of applications in environment protection, pharmaceutical cpd separation and purification field.But the aperture of product is less at present, and the separation and purification object larger to some molecular weight is difficult to reach active adsorption, limited the application of this product.
Summary of the invention
The present invention is intended to solve the less problem in prior art macroporous adsorbent resin aperture, and a kind of especially big macroporous adsorbent resin is provided, and its aperture is large compared with general macroporous adsorbent resin, has expanded its range of application.
In order to realize foregoing invention object, its concrete technical scheme is as follows:
A kind of especially big macroporous adsorbent resin, is characterized in that: comprise following according to the raw material of parts by weight meter:
Vinylstyrene 50-70 part
Vinylbenzene 5-10 part
Ethyleneglycol dimethyacrylate 10-20 part
Polystyrene 5-10 part
Diethyl phthalate 50-80 part
No. 200 gasoline 30-50 parts
Diphenyl peroxide base acyl 1-2 part
Deionized water 150-200 part
Polyvinyl alcohol 1-2 part.
A kind of especially big macroporous adsorbent resin, is characterized in that: comprise following according to the raw material of parts by weight meter:
Vinylstyrene 56-60 part
Vinylbenzene 7-9 part
Ethyleneglycol dimethyacrylate 12-18 part
Polystyrene 8-9 part
Diethyl phthalate 57-70 part
No. 200 gasoline 40-45 parts
Diphenyl peroxide base acyl 1.5-1.8 part
Deionized water 170-180 part
Polyvinyl alcohol 1.5-1.9 part.
A preparation method for especially big macroporous adsorbent resin, is characterized in that: comprise following processing step:
A, require to take raw material and fully mix in container according to formula, obtain mixture, then mixture is added in the there-necked flask of a tool plug;
B, start and stir and system oil phase is dispersed into pearl body, then temperature of reaction is raised to 75-80 DEG C, after the pearl body-shaping that oil phase is dispersed into, temperature of reaction is risen to 85 DEG C, then maintain 85 DEG C of reaction 2h, then be warming up to 90 DEG C, reaction 4h;
C, temperature is risen to 92-95 DEG C, reaction 4h, leaches reaction product pearl body, and water repetitive scrubbing is removed pore-creating agent, leaches product and is drying to obtain especially big macroporous adsorbent resin.
The present invention, in step B, described be raised to temperature of reaction 75-80 DEG C and refer to and in 0.5-1h, be raised to 75-80 DEG C.
The present invention is in step C, and the detailed process of described removal pore-creating agent is: reaction product pearl body is removed to pore-creating agent in pore-creating agent extractor, more further remove pore-creating agent in alcohol washer, then water washes away residual alcohol.
The useful technique effect that the present invention brings:
It is large not that the present invention is intended to solve the macroporous adsorbent resin aperture of prior art, the problem that Application Areas is restricted, adopt polystyrene, diethyl phthalate as one of pore-creating agent component, increase the aperture of resin, prepare especially big macroporous adsorbent resin, widened the Application Areas of this resin; The present invention has added the second linking agent, in strengthening resin aperture, has ensured the physical strength of resin, and is provided the work-ing life of resin.
Embodiment
embodiment 1
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
50 parts of Vinylstyrenes
5 parts of vinylbenzene
10 parts of ethyleneglycol dimethyacrylates
5 parts of polystyrene
50 parts of diethyl phthalates
30 parts, No. 200 gasoline
1 part of diphenyl peroxide base acyl
150 parts of deionized waters
1 part of polyvinyl alcohol.
embodiment 2
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
70 parts of Vinylstyrenes
10 parts of vinylbenzene
20 parts of ethyleneglycol dimethyacrylates
10 parts of polystyrene
80 parts of diethyl phthalates
50 parts, No. 200 gasoline
2 parts of diphenyl peroxide base acyls
200 parts of deionized waters
2 parts of polyvinyl alcohol.
embodiment 3
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
60 parts of Vinylstyrenes
7.5 parts of vinylbenzene
15 parts of ethyleneglycol dimethyacrylates
7.5 parts of polystyrene
65 parts of diethyl phthalates
40 parts, No. 200 gasoline
1.5 parts of diphenyl peroxide base acyls
175 parts of deionized waters
1.5 parts of polyvinyl alcohol.
embodiment 4
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
59 parts of Vinylstyrenes
8.5 parts of vinylbenzene
12 parts of ethyleneglycol dimethyacrylates
8 parts of polystyrene
71 parts of diethyl phthalates
46 parts, No. 200 gasoline
1.25 parts of diphenyl peroxide base acyls
190 parts of deionized waters
1.8 parts of polyvinyl alcohol.
embodiment 5
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
56 parts of Vinylstyrenes
7 parts of vinylbenzene
12 parts of ethyleneglycol dimethyacrylates
8 parts of polystyrene
57 parts of diethyl phthalates
40 parts, No. 200 gasoline
1.5 parts of diphenyl peroxide base acyls
170 parts of deionized waters
1.5 parts of polyvinyl alcohol.
embodiment 6
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
60 parts of Vinylstyrenes
9 parts of vinylbenzene
18 parts of ethyleneglycol dimethyacrylates
9 parts of polystyrene
70 parts of diethyl phthalates
45 parts, No. 200 gasoline
1.8 parts of diphenyl peroxide base acyls
180 parts of deionized waters
1.9 parts of polyvinyl alcohol.
embodiment 7
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
58 parts of Vinylstyrenes
8 parts of vinylbenzene
15 parts of ethyleneglycol dimethyacrylates
8.5 parts of polystyrene
63.5 parts of diethyl phthalates
42.5 parts, No. 200 gasoline
1.65 parts of diphenyl peroxide base acyls
175 parts of deionized waters
1.7 parts of polyvinyl alcohol.
embodiment 8
A kind of especially big macroporous adsorbent resin, comprises following according to the raw material of parts by weight meter:
59 parts of Vinylstyrenes
7.5 parts of vinylbenzene
17 parts of ethyleneglycol dimethyacrylates
8.8 parts of polystyrene
58.5 parts of diethyl phthalates
41.5 parts, No. 200 gasoline
1.7 parts of diphenyl peroxide base acyls
171 parts of deionized waters
1.8 parts of polyvinyl alcohol.
embodiment 9
A preparation method for especially big macroporous adsorbent resin, comprises following processing step:
A, require to take raw material and fully mix in container according to formula, obtain mixture, then mixture is added in the there-necked flask of a tool plug;
B, start and stir and system oil phase is dispersed into pearl body, then temperature of reaction is raised to 75 DEG C, after the pearl body-shaping that oil phase is dispersed into, temperature of reaction is risen to 85 DEG C, then maintain 85 DEG C of reaction 2h, then be warming up to 90 DEG C, reaction 4h;
C, temperature is risen to 92 DEG C, reaction 4h, leaches reaction product pearl body, and water repetitive scrubbing is removed pore-creating agent, leaches product and is drying to obtain especially big macroporous adsorbent resin.
embodiment 10
A preparation method for especially big macroporous adsorbent resin, comprises following processing step:
A, require to take raw material and fully mix in container according to formula, obtain mixture, then mixture is added in the there-necked flask of a tool plug;
B, start and stir and system oil phase is dispersed into pearl body, then temperature of reaction is raised to 80 DEG C, after the pearl body-shaping that oil phase is dispersed into, temperature of reaction is risen to 85 DEG C, then maintain 85 DEG C of reaction 2h, then be warming up to 90 DEG C, reaction 4h;
C, temperature is risen to 95 DEG C, reaction 4h, leaches reaction product pearl body, and water repetitive scrubbing is removed pore-creating agent, leaches product and is drying to obtain especially big macroporous adsorbent resin.
embodiment 11
A preparation method for especially big macroporous adsorbent resin, comprises following processing step:
A, require to take raw material and fully mix in container according to formula, obtain mixture, then mixture is added in the there-necked flask of a tool plug;
B, start and stir and system oil phase is dispersed into pearl body, then temperature of reaction is raised to 77.5 DEG C, after the pearl body-shaping that oil phase is dispersed into, temperature of reaction is risen to 85 DEG C, then maintain 85 DEG C of reaction 2h, then be warming up to 90 DEG C, reaction 4h;
C, temperature is risen to 93.5 DEG C, reaction 4h, leaches reaction product pearl body, and water repetitive scrubbing is removed pore-creating agent, leaches product and is drying to obtain especially big macroporous adsorbent resin.
embodiment 12
A preparation method for especially big macroporous adsorbent resin, comprises following processing step:
A, require to take raw material and fully mix in container according to formula, obtain mixture, then mixture is added in the there-necked flask of a tool plug;
B, start and stir and system oil phase is dispersed into pearl body, then temperature of reaction is raised to 79 DEG C, after the pearl body-shaping that oil phase is dispersed into, temperature of reaction is risen to 85 DEG C, then maintain 85 DEG C of reaction 2h, then be warming up to 90 DEG C, reaction 4h;
C, temperature is risen to 93 DEG C, reaction 4h, leaches reaction product pearl body, and water repetitive scrubbing is removed pore-creating agent, leaches product and is drying to obtain especially big macroporous adsorbent resin.
embodiment 13
On the basis of embodiment 9-12, preferred:
In step B, described temperature of reaction be raised to 75-80 DEG C and refer to and in 0.5h, be raised to 75-80 DEG C.
In step C, the detailed process of described removal pore-creating agent is: reaction product pearl body is removed to pore-creating agent in pore-creating agent extractor, more further remove pore-creating agent in alcohol washer, then water washes away residual alcohol.
embodiment 14
On the basis of embodiment 9-12, preferred:
In step B, described temperature of reaction be raised to 75-80 DEG C and refer to and in 1h, be raised to 75-80 DEG C.
In step C, the detailed process of described removal pore-creating agent is: reaction product pearl body is removed to pore-creating agent in pore-creating agent extractor, more further remove pore-creating agent in alcohol washer, then water washes away residual alcohol.
embodiment 15
On the basis of embodiment 9-12, preferred:
In step B, described temperature of reaction be raised to 75-80 DEG C and refer to and in 0.75h, be raised to 75-80 DEG C.
In step C, the detailed process of described removal pore-creating agent is: reaction product pearl body is removed to pore-creating agent in pore-creating agent extractor, more further remove pore-creating agent in alcohol washer, then water washes away residual alcohol.
embodiment 16
On the basis of embodiment 9-12, preferred:
In step B, described temperature of reaction be raised to 75-80 DEG C and refer to and in 0.8h, be raised to 75-80 DEG C.
In step C, the detailed process of described removal pore-creating agent is: reaction product pearl body is removed to pore-creating agent in pore-creating agent extractor, more further remove pore-creating agent in alcohol washer, then water washes away residual alcohol.

Claims (5)

1. an especially big macroporous adsorbent resin, is characterized in that: comprise following according to the raw material of parts by weight meter:
Vinylstyrene 50-70 part
Vinylbenzene 5-10 part
Ethyleneglycol dimethyacrylate 10-20 part
Polystyrene 5-10 part
Diethyl phthalate 50-80 part
No. 200 gasoline 30-50 parts
Diphenyl peroxide base acyl 1-2 part
Deionized water 150-200 part
Polyvinyl alcohol 1-2 part.
2. the especially big macroporous adsorbent resin of one according to claim 1, is characterized in that: comprise following according to the raw material of parts by weight meter:
Vinylstyrene 56-60 part
Vinylbenzene 7-9 part
Ethyleneglycol dimethyacrylate 12-18 part
Polystyrene 8-9 part
Diethyl phthalate 57-70 part
No. 200 gasoline 40-45 parts
Diphenyl peroxide base acyl 1.5-1.8 part
Deionized water 170-180 part
Polyvinyl alcohol 1.5-1.9 part.
3. the preparation method of a kind of especially big macroporous adsorbent resin according to claim 1 and 2, is characterized in that: comprise following processing step:
A, require to take raw material and fully mix in container according to formula, obtain mixture, then mixture is added in the there-necked flask of a tool plug;
B, start and stir and system oil phase is dispersed into pearl body, then temperature of reaction is raised to 75-80 DEG C, after the pearl body-shaping that oil phase is dispersed into, temperature of reaction is risen to 85 DEG C, then maintain 85 DEG C of reaction 2h, then be warming up to 90 DEG C, reaction 4h;
C, temperature is risen to 92-95 DEG C, reaction 4h, leaches reaction product pearl body, and water repetitive scrubbing is removed pore-creating agent, leaches product and is drying to obtain especially big macroporous adsorbent resin.
4. the preparation method of a kind of especially big macroporous adsorbent resin according to claim 3, is characterized in that: in step B, described temperature of reaction be raised to 75-80 DEG C and refer to and in 0.5-1h, be raised to 75-80 DEG C.
5. the preparation method of a kind of especially big macroporous adsorbent resin according to claim 3, it is characterized in that: in step C, the detailed process of described removal pore-creating agent is: reaction product pearl body is removed to pore-creating agent in pore-creating agent extractor, in alcohol washer, further remove pore-creating agent, then water washes away residual alcohol again.
CN201410251408.6A 2014-06-09 2014-06-09 A kind of especially big macroporous adsorbent resin and preparation method thereof Expired - Fee Related CN104059187B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410251408.6A CN104059187B (en) 2014-06-09 2014-06-09 A kind of especially big macroporous adsorbent resin and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410251408.6A CN104059187B (en) 2014-06-09 2014-06-09 A kind of especially big macroporous adsorbent resin and preparation method thereof

Publications (2)

Publication Number Publication Date
CN104059187A true CN104059187A (en) 2014-09-24
CN104059187B CN104059187B (en) 2016-08-31

Family

ID=51547139

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410251408.6A Expired - Fee Related CN104059187B (en) 2014-06-09 2014-06-09 A kind of especially big macroporous adsorbent resin and preparation method thereof

Country Status (1)

Country Link
CN (1) CN104059187B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107051410A (en) * 2017-05-26 2017-08-18 辽宁科技学院 A kind of macroporous absorbent resin and preparation method thereof
CN107266622A (en) * 2017-06-27 2017-10-20 郑泽 Macroporous absorbent resin of larger molecular weight organic matter and preparation method thereof in a kind of removal waste water
CN115044094A (en) * 2022-06-22 2022-09-13 湖北工业大学 Super absorbent resin with sponge structure and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07196752A (en) * 1993-12-28 1995-08-01 Japan Synthetic Rubber Co Ltd Modification of crosslinked polymer particles
CN1927899A (en) * 2006-09-01 2007-03-14 烟台硕德新材料有限公司 Preparation method of micron-sized monodisperse copolymerized microspheres

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07196752A (en) * 1993-12-28 1995-08-01 Japan Synthetic Rubber Co Ltd Modification of crosslinked polymer particles
CN1927899A (en) * 2006-09-01 2007-03-14 烟台硕德新材料有限公司 Preparation method of micron-sized monodisperse copolymerized microspheres

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107051410A (en) * 2017-05-26 2017-08-18 辽宁科技学院 A kind of macroporous absorbent resin and preparation method thereof
CN107266622A (en) * 2017-06-27 2017-10-20 郑泽 Macroporous absorbent resin of larger molecular weight organic matter and preparation method thereof in a kind of removal waste water
CN115044094A (en) * 2022-06-22 2022-09-13 湖北工业大学 Super absorbent resin with sponge structure and preparation method thereof

Also Published As

Publication number Publication date
CN104059187B (en) 2016-08-31

Similar Documents

Publication Publication Date Title
Wang et al. Effect of pore structure on adsorption behavior of ibuprofen by magnetic anion exchange resins
CN101912770B (en) Polymeric adsorbent and preparation method thereof
JP4931006B2 (en) Monolithic organic porous ion exchanger, method of using the same, method of production, and mold used for production
CN100467120C (en) Macroporous adsorption resin special used for separating antibiotic and its preparation method
CN104072659B (en) A kind of magnetic resin microballoon and preparation method thereof
Chen et al. Multifunctional negatively-charged poly (ether sulfone) nanofibrous membrane for water remediation
CN104448091B (en) Method for preparing aromatic carboxylic acid adsorption resin
CN104059187A (en) Super-macroporous adsorbent resin and preparation method thereof
CN103864973A (en) Preparation method for polymer microspheres having mixed absorption mode
JP2019514687A5 (en)
CN105254818A (en) High-oil-absorption resin and preparation method thereof
CN107892733B (en) Heavy metal wastewater ion adsorption resin and preparation method thereof
CN108137452A (en) The purification process of organic solvent
CN101693750A (en) Preparation method of macroporous absorption resin
CN104190264B (en) Preparation method for hollow fiber ultrafiltration membrane with chelation function
CN102585074A (en) Preparation method of high-performance macroporous adsorption resin
CN106732447A (en) A kind of macroporous absorbent resin for containing phenol industrial wastewater for processing and preparation method thereof
CN104084179B (en) A kind of polyalcohol integral pole and preparation method thereof and application
JP4929635B2 (en) Maleimide group-containing porous crosslinked polystyrene particles and method for producing the same
JP5283893B2 (en) Monolithic organic porous body, production method thereof, and monolithic organic porous ion exchanger
CN114907610B (en) Preparation method of porous polymer microsphere oil removal resin
CN108659159B (en) Molecularly imprinted microsphere for detecting teicoplanin and preparation and application thereof
CN102921317A (en) Preparation method of polysulfone ultrafiltration membrane
CN101067009A (en) Method for eliminating solvent from pearl polymer
CN110256637A (en) A kind of two dimension aromatic polyamide type quaternary ammonium salt and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160831

Termination date: 20170609

CF01 Termination of patent right due to non-payment of annual fee