CN102936386B - Viton rubber master batch and preparation method thereof - Google Patents

Viton rubber master batch and preparation method thereof Download PDF

Info

Publication number
CN102936386B
CN102936386B CN201210447777.3A CN201210447777A CN102936386B CN 102936386 B CN102936386 B CN 102936386B CN 201210447777 A CN201210447777 A CN 201210447777A CN 102936386 B CN102936386 B CN 102936386B
Authority
CN
China
Prior art keywords
viton
weight part
maleic anhydride
master batch
preparation
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.)
Expired - Fee Related
Application number
CN201210447777.3A
Other languages
Chinese (zh)
Other versions
CN102936386A (en
Inventor
胡新嵩
罗科丽
赖观品
何宗业
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.)
GUANGZHOU GLORYSTAR CHEMICAL CO Ltd
Original Assignee
GUANGZHOU GLORYSTAR CHEMICAL 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 GUANGZHOU GLORYSTAR CHEMICAL CO Ltd filed Critical GUANGZHOU GLORYSTAR CHEMICAL CO Ltd
Priority to CN201210447777.3A priority Critical patent/CN102936386B/en
Publication of CN102936386A publication Critical patent/CN102936386A/en
Application granted granted Critical
Publication of CN102936386B publication Critical patent/CN102936386B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Graft Or Block Polymers (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention discloses a kind of viton rubber master batch and preparation method thereof, first prepare viton grafted maleic anhydride expanding material and Core-shell type double-active acrylate elastic body, again by crude fluororubber, viton grafted maleic anhydride expanding material, Core-shell type double-active acrylate elastic body and rubber reinforcing filler, join in Banbury mixer, at 120 ~ 170 DEG C, melting 50 ~ 120min is blended, obtained viton rubber master batch.Reacting property of active group increase-volume in viton grafted maleic anhydride expanding material and Core-shell type double-active acrylate elastic body, easily mixes time mixing with viton and produces in mechanical properties and coordinate same synergism, improving the high-temperature stability of rubber.<!--1-->

Description

Viton rubber master batch and preparation method thereof
Technical field
The invention belongs to viton, be a kind of viton rubber master batch specifically, also relate to the method utilizing viton grafted maleic anhydride expanding material and Core-shell type double-active acrylate elastic body to prepare viton rubber master batch.
Background technology
Viton (FKM) be main chain or side chain carbon atom on containing the synthesis macromolecular elastomer of fluorine atom, it is widely used in many fields such as space flight, military project, national defence, automobile, petrochemical complex.Viton goods are mainly used in sealing member, packing ring, pad, barrier film, sebific duct, oil sealing, lining, anticorrosive products and electrical isolation goods.
Viton is most widely used is automotive field, accounts for 60 ~ 70% of application total amount.On automobile component, can be used as motor spirit flexible pipe, refueling hose, petrolift, O shape circle, and jet apparatus, power piston, valve stem, bent axle, compressor of air conditioner sealing material.The automotive sealant that rubber is made in use, except the effect by stress, strain, high temperature and low temperature, also by the erosion of oil product (oil fuel, lubricating oil), chemicals (alcohol, deicing fluid, scavenging solution, braking fluid) and biology (mould, bacterium, insect) etc.During product design, as can not be considered the independent of working conditions and synergy comprehensively, damage intensity will be caused to accelerate, cause shorten work-ing life.Particularly along with the development of automotive industry and motorway, the travel speed of automobile significantly improves, make the use temperature of oil sealing significantly increase, the oil temperature at the bent axle place of engine substantially more than 110 DEG C, therefore to the specification of quality also corresponding raising of the rubber seal to automobile accessories.Traditional viton elaxtic seal cannot meet high temperature, at a high speed, the actual operation requirements of high abrasion.
China started to develop viton from the sixties in 20th century, successively successfully developed the viton based on polyolefine such as 23 types, 26 types, 246 types, TP-2 type and carboxyl Asia pin base viton.The eighties in 20th century has developed again perfluoroelastomers and has fluoridized phosphorus rubber etc.
In order to improve the performance of viton and goods, a large amount of research work is carried out to the modification of viton and processing both at home and abroad.At present, the modification of viton mainly contains both direction: one is, pass through backbone modification, as the exploitation of fluoroether rubber, trifluoropropyl siloxane, ehter bond is introduced viton main chain, increase the flexibility of molecule, while its low-temperature performance is improved greatly, remain the original feature of viton, but due to Development and Production high cost, significantly limit its promotion and application; Two are, rubber blending, by viton and some conventional rubbers, specialty elastomer use, so that it is more excellent to obtain performance, and the material that cost is lower.
Blending and modifying is a kind of method preferably, but has the following disadvantages: the cost performance that (1) makes novel type fluorubber is not high.Fluoroether rubber, trifluoropropyl siloxane are too high due to cost of development, make its price even higher than viton, and under can only being used in the harsher environment of condition, promotion and application are restricted; (2) modification of the blending and modifying between viton to viton performance is restricted.Rubber of the same type determines it to be caused on performance deficiency by rubber self structure in improvement and is restricted, and cost difficulty reduces.Though and the blended low-temperature performance well improving viton of viton and fluoroether rubber, cost is higher; (3) the blended difficulty of the low-temperature performance to viton of viton and other rubber is kind.Blending and modifying can improve the elasticity of viton, the improvement of the single performance such as processing characteristics, but very few to improving viton low-temperature performance and considering multiple defect aspect research.
Viton itself has excellent resistance to elevated temperatures, but the use temperature of oil sealing increases substantially with automobile running velocity and significantly rises, and proposes requirements at the higher level to the heat resisting temperature of automotive sealant.Polar acrylate's rubber has heat-resisting, oil resistant, ageing-resistant and ozone resistance, good processability, the features such as elasticity is splendid, and price is only 10% of viton.If by blended for the double activated acrylic elastomer of viton and modification, then the performance of viton product will be improved.
Summary of the invention
For the deficiency that prior art exists, the object of this invention is to provide the method for the high viton grafted maleic anhydride expanding material of a kind of consistency and Core-shell type double-active acrylate elastic body blending and modifying viton.
Technical scheme of the present invention is achieved in that a kind of viton rubber master batch, prepare by the following method: first prepare viton grafted maleic anhydride expanding material and Core-shell type double-active acrylate elastic body, again by crude fluororubber, viton grafted maleic anhydride expanding material, Core-shell type double-active acrylate elastic body and rubber reinforcing filler, join in Banbury mixer, at 120 ~ 170 DEG C, melting 50 ~ 120min is blended, obtained viton rubber master batch.
Further, described crude fluororubber 100 weight part, Core-shell type double-active acrylate elastic body 20 ~ 50 weight part, viton grafted maleic anhydride expanding material 3 ~ 8 weight part, rubber reinforcing filler 10 ~ 30 weight part.
The preparation process of described viton grafted maleic anhydride joins in Banbury mixer by crude fluororubber, maleic anhydride, initiator, vulcanizing agent, promotor, at 120 ~ 160 DEG C, under the condition of rotating speed 50 ~ 100r/min, and reaction 10 ~ 30min.
Described crude fluororubber 80 ~ 130 weight part, maleic anhydride 3 ~ 8 weight part, initiator 0.5 ~ 2 weight part, vulcanizing agent 0.2 ~ 0.5 weight part, promotor 0.1 ~ 0.3 weight part.
The preparation process of described Core-shell type double-active acrylate elastic body is by acrylate monomer, joins in kneader containing the acrylate of active group, compound emulsifying agent; be warming up to 60 ~ 90 DEG C; insulation reaction 0.8 ~ 1.2h; then vulcanizing agent and oxidation-reduction initiator is added; under nitrogen protection; be warming up to 80 ~ 100 DEG C, insulation reaction 1.5 ~ 2.0h, be finally cooled to 40 ~ 50 DEG C and obtain.
Described acrylate monomer 70 ~ 100 weight part, containing acrylate 50 ~ 80 weight part of active group, compound emulsifying agent 15 ~ 30 weight part, vulcanizing agent 8 ~ 20 weight part, oxidation-reduction initiator 5 ~ 8 weight part.
Described rubber reinforcing filler comprises one or more in carbon black, white carbon black, nano-calcium carbonate, hard (china) clay.
Described initiator be benzoyl peroxide (BPO), dilauroyl peroxide (LPO), Diisopropyl azodicarboxylate (AIBN), Potassium Persulphate (KPS), dicumyl peroxide (DCP) or oxidation di-t-butyl one or more; Described vulcanizing agent be benzoyl peroxide (BPO), BPP (BPP), calcium hydroxide or magnesian one or more; Described promotor is 2-benzothiazolyl mercaptan (accelerator M), 2, one or more of 2 '-dithio-bis-benzothiazole (accelerator DM), N-cyclohexyl-2-benzothiazole sulfonamide (aniline fluid bed), N tert butyl benzothiazole 2 sulfenamide (vulcanization accelerator TBBS), tetramethyl-thiuram disulfide (vulcanization accelerator TMTD), N-cyclohexyl-2-benzene (CZ).
Described compound emulsifying agent is one or more in acrylamide sodium isopropyl xanthate, double bond containing alcohol ether sulfosuccinates sodium salt, sodium vinyl sulfonate, sodium laurylsulfonate, polyoxyethylenated alcohol sodium sulfate; Oxygenant in described oxidation-reduction initiator is one or more in Potassium Persulphate, benzoyl peroxide, dilauroyl peroxide, and reductive agent is one or more in sodium bisulfite, ferrous pyrophosphate, sulfurous acid iron.
Compared with prior art, the present invention has the following advantages:
(1) reacting property of the active group increase-volume in viton grafted maleic anhydride expanding material and Core-shell type double-active acrylate elastic body, easily mix time mixing with viton and produce in mechanical properties and coordinate same synergism, simultaneously two by the crosslinked cross-linking density and the tear resistance that wait raising rubber unvulcanizate, the introducing of ether-containing group, improves the high-temperature stability of rubber.The present invention is by the modification acrylate blend rubber of rubber master batch and weathering resistance and tear-resistant excellent property, and improving viton has resistance to low temperature; By carrying out modification to acrylate, introducing containing ether and active functional group wherein, constructing the modification acrylate of double activated (double cross connection), improve the resistance to elevated temperatures of viton further.
(2) the present invention is by adding viton grafted maleic anhydride expanding material, and compatibilization effect is good, improves the mechanics of viton and stability and reduction viton cost.
(3) the present invention by acid-acceptor, vulcanizing agent, rubber reinforcing filler, promotor with the use of, reduce the second-order transition temperature of Core-shell type double-active acrylate elastic body blending and modifying viton, improve its resistance to low temperature.
Embodiment
In following embodiment, the number of material is all expressed with weight part.
Embodiment 1
(1) viton grafted maleic anhydride expanding material is prepared.Crude fluororubber 80 parts, maleic anhydride 3 part, part dicumyl peroxide (DCP) 0.5,0.2 part, magnesium oxide, tetramethyl-thiuram disulfide 0.1 part (vulcanization accelerator TMTD) are joined in Banbury mixer, temperature be 120 DEG C, under rotating speed is the condition of 50r/min, reaction 15min, obtain viton grafted maleic anhydride (KFM-g-MAH) expanding material, recording its percentage of grafting is 1.65%.
(2) Core-shell type double-active acrylate elastic body.Preparation is by methyl acrylate 70 parts, methoxyethyl acrylate 55 parts, acrylamide sodium isopropyl xanthate 15 parts; join in kneader; be warming up to 62 DEG C; insulation reaction 0.8h, then adds benzoyl peroxide 10 parts and Potassium Persulphate-sodium bisulfite 5 parts, under nitrogen protection; be warming up to 83 DEG C; insulation reaction 1.7h, is finally cooled to 43 DEG C, obtains Core-shell type double-active acrylate elastic body.
(3) blendedly viton rubber master batch is prepared.By crude fluororubber 100 parts, Core-shell type double-active acrylate elastic body 20 parts, viton grafted maleic anhydride expanding material 3 parts, white carbon black 10 parts, be sequentially added in Banbury mixer, melting 80min at DEG C, obtains viton rubber master batch.
Embodiment 2
(1) viton grafted maleic anhydride expanding material is prepared.By viton 120 parts, maleic anhydride 6 parts, Potassium Persulphate (KPS) 1 part, benzoyl peroxide (BPO) 0.3 part, 2,2 '-dithio-bis-benzothiazole 0.2 part (accelerator DM) joins in Banbury mixer, temperature be 140 DEG C, under rotating speed is the condition of 80r/min, reaction 18min, obtain viton grafted maleic anhydride (KFM-g-MAH) expanding material, recording its percentage of grafting is 3.5%.
(2) Core-shell type double-active acrylate elastic body.By ethyl propenoate 80 parts, methyl methacrylate 75 parts, double bond containing alcohol ether sulfosuccinates sodium salt 20 parts; join in kneader; be warming up to 90 DEG C; insulation reaction 1.2h, then added BPP 8 parts and ammonium persulfate-sodium bisulfite 6 parts, under nitrogen protection; be warming up to 80 DEG C; insulation reaction 1.5h, is finally cooled to 40 DEG C, obtains Core-shell type double-active acrylate elastic body.
(3) blendedly viton rubber master batch is prepared.By crude fluororubber 100 parts, Core-shell type double-active acrylate elastic body 30 parts, viton grafted maleic anhydride expanding material 5 parts, nano-calcium carbonate 20 parts, be sequentially added in Banbury mixer, melting 100min at 150 DEG C, obtains viton rubber master batch.
Embodiment 3
(1) viton grafted maleic anhydride expanding material is prepared.By crude fluororubber 130 parts, maleic anhydride 7 part, part dilauroyl peroxide 1.5(LPO), BPP 0.5 part (BPP), N tert butyl benzothiazole 2 sulfenamide 0.3 part (vulcanization accelerator TBBS) join in Banbury mixer, temperature be 160 DEG C, under rotating speed is the condition of 100r/min, reaction 20min, obtain viton grafted maleic anhydride (KFM-g-MAH) expanding material, recording its percentage of grafting is 3.15%.
(2) Core-shell type double-active acrylate elastic body.By butyl acrylate 100 parts, hydroxyethyl methylacrylate 80 parts, sodium vinyl sulfonate 30 parts; join in kneader; be warming up to 70 DEG C; insulation reaction 1.0h, then adds 17 parts, calcium hydroxide and sodium chlorate-S-WAT 8 parts, under nitrogen protection; be warming up to 100 DEG C; insulation reaction 2.0h, is finally cooled to 50 DEG C, obtains Core-shell type double-active acrylate elastic body.
(3) blendedly viton rubber master batch is prepared.By viton 100 parts, Core-shell type double-active acrylate elastic body 45 parts, viton grafted maleic anhydride expanding material 7 parts, carbon black 30 parts, be sequentially added in Banbury mixer, melting 120min at 140 DEG C, obtains viton rubber master batch.

Claims (7)

1. the preparation method of a viton rubber master batch, it is characterized in that, first prepare viton grafted maleic anhydride expanding material and double activated acrylate elastomer, again by crude fluororubber, viton grafted maleic anhydride expanding material, double activated acrylate elastomer and rubber reinforcing filler, join in Banbury mixer, at 120 ~ 170 DEG C, melting 50 ~ 120 minutes is blended;
Described crude fluororubber 100 weight part, double activated acrylate elastomer 20 ~ 50 weight part, viton grafted maleic anhydride expanding material 3 ~ 8 weight part, rubber reinforcing filler 10 ~ 30 weight part;
The process preparing viton grafted maleic anhydride joins in Banbury mixer by crude fluororubber, maleic anhydride, initiator, vulcanizing agent, promotor, at 120 ~ 160 DEG C, under the condition of rotating speed 50 ~ 100r/min, and reaction 10 ~ 30min;
The process preparing double activated acrylate elastomer is by acrylate monomer, joins in kneader containing the acrylate of active group, emulsifying agent; be warming up to 60 ~ 90 DEG C; insulation reaction 0.8 ~ 1.2h; then vulcanizing agent and oxidation-reduction initiator is added; under nitrogen protection; be warming up to 80 ~ 100 DEG C, insulation reaction 1.5 ~ 2.0h, be finally cooled to 40 ~ 50 DEG C and obtain.
2. the preparation method of rubber rubber master batch according to claim 1, is characterized in that, described crude fluororubber 80 ~ 130 weight part, maleic anhydride 3 ~ 8 weight part, initiator 0.5 ~ 2 weight part, vulcanizing agent 0.2 ~ 0.5 weight part, promotor 0.1 ~ 0.3 weight part.
3. the preparation method of viton rubber master batch according to claim 1, it is characterized in that, described acrylate monomer 70 ~ 100 weight part, containing acrylate 50 ~ 80 weight part of active group, emulsifying agent 15 ~ 30 weight part, vulcanizing agent 8 ~ 20 weight part, oxidation-reduction initiator 5 ~ 8 weight part.
4. the preparation method of viton rubber master batch according to claim 1, is characterized in that, described rubber reinforcing filler comprises one or more in carbon black, white carbon black, nano-calcium carbonate, hard (china) clay.
5. the preparation method of viton rubber master batch according to claim 1, it is characterized in that, described initiator is one or more of benzoyl peroxide (BPO), dilauroyl peroxide (LPO), Diisopropyl azodicarboxylate (AIBN), Potassium Persulphate (KPS), dicumyl peroxide (DCP) or di-t-butyl peroxide;
Described vulcanizing agent be benzoyl peroxide (BPO), BPP (BPP), calcium hydroxide or magnesian one or more;
Described promotor is 2-benzothiazolyl mercaptan (accelerator M), 2, one or more of 2 '-dithio-bis-benzothiazole (accelerator DM), N-cyclohexyl-2-[4-morpholinodithio sulphenamide (aniline fluid bed), N tert butyl benzothiazole 2 sulfenamide (vulcanization accelerator TBBS), tetramethyl-thiuram disulfide (vulcanization accelerator TMTD).
6. the preparation method of viton rubber master batch according to claim 1, it is characterized in that, described emulsifying agent is one or more in acrylamide sodium isopropyl xanthate, double bond containing alcohol ether sulfosuccinates sodium salt, sodium vinyl sulfonate, sodium laurylsulfonate, polyoxyethylenated alcohol sodium sulfate;
Oxygenant in described oxidation-reduction initiator is one or more in Potassium Persulphate, benzoyl peroxide, dilauroyl peroxide, and reductive agent is one or more in sodium bisulfite, ferrous pyrophosphate, sulfurous acid iron.
7. a viton rubber master batch, is characterized in that, is obtained by preparation method according to claim 1.
CN201210447777.3A 2012-11-09 2012-11-09 Viton rubber master batch and preparation method thereof Expired - Fee Related CN102936386B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210447777.3A CN102936386B (en) 2012-11-09 2012-11-09 Viton rubber master batch and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210447777.3A CN102936386B (en) 2012-11-09 2012-11-09 Viton rubber master batch and preparation method thereof

Publications (2)

Publication Number Publication Date
CN102936386A CN102936386A (en) 2013-02-20
CN102936386B true CN102936386B (en) 2015-12-16

Family

ID=47695312

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210447777.3A Expired - Fee Related CN102936386B (en) 2012-11-09 2012-11-09 Viton rubber master batch and preparation method thereof

Country Status (1)

Country Link
CN (1) CN102936386B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103897314A (en) * 2014-04-01 2014-07-02 安庆丰源化工有限公司 Method for preparing high-performance fluorine rubber
CN106632868A (en) * 2016-10-21 2017-05-10 兰州理工大学 Maleic anhydride-grafted compatibilizer and its preparation method, and polytetrafluoroethylene composite
CN115028952A (en) * 2022-06-24 2022-09-09 四川道弘新材料有限公司 Fluororubber with high performance retention rate at high temperature and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1800225A (en) * 2005-12-28 2006-07-12 中国化工建设总公司常州涂料化工研究院 Latex type hydroxy acryl acid resin possessing core-shell configuration
CN101037498A (en) * 2006-03-17 2007-09-19 上海杰事杰新材料股份有限公司 Microencapsulation reinforced inorganic particle and preparation method thereof
CN102199243A (en) * 2011-04-07 2011-09-28 四川大学 Polyacrylate elastomer with core-shell structure and its preparation method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1800225A (en) * 2005-12-28 2006-07-12 中国化工建设总公司常州涂料化工研究院 Latex type hydroxy acryl acid resin possessing core-shell configuration
CN101037498A (en) * 2006-03-17 2007-09-19 上海杰事杰新材料股份有限公司 Microencapsulation reinforced inorganic particle and preparation method thereof
CN102199243A (en) * 2011-04-07 2011-09-28 四川大学 Polyacrylate elastomer with core-shell structure and its preparation method

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
刘宏治.核-壳粒子增韧聚合物的研究进展.《高分子通报》.2006,(第9期),第1-15页. *
董丽杰等.氟橡胶接枝马来酸酐的研究.《特种橡胶制品》.2008,第29卷(第4期),第12-15页第1.3节、第2节. *
陈春明等.含醚基团丙烯酸酯弹性体的合成及其对氟橡胶的改性.《合成橡胶工业》.2006,第29卷(第4期),第271-274页. *

Also Published As

Publication number Publication date
CN102936386A (en) 2013-02-20

Similar Documents

Publication Publication Date Title
CN109320658B (en) Itaconate bio-based heat-resistant oil elastomer and preparation method thereof
CN108641150B (en) Rubber material capable of being repeatedly processed and preparation method thereof
EP3333201B1 (en) Nitrile group-containing highly saturated copolymer rubber, crosslinkable rubber composition, and crosslinked rubber
CN102936386B (en) Viton rubber master batch and preparation method thereof
CN104086839B (en) The tear-resistant elastomeric material of a kind of high-strength wearable
CN102924861B (en) Modified fluororubber and preparation method thereof
CN103013012A (en) Seal rubber for water pump of automobile and preparation method of seal rubber
CN105705569A (en) Nitrile group-containing highly-saturated copolymer rubber composition and crosslinked rubber
CN101519510A (en) Method for preparing low-heat-generation fatigue-resistant vulcanized rubber
CN103013007A (en) Rubber compound for rear oil seal of automobile crankshaft and preparation method of rubber
CN102942650B (en) Core-shell type double-active acrylate elastic body and preparation method thereof
CN103013009A (en) Rocker cover gasket rubber compound and preparation method thereof
CN102936319A (en) Fluororubber-grated-maleic anhydride bulking agent and preparing method thereof
CN103013011B (en) Automobile valve sealing gasket sizing material and preparation method thereof
JP2591646B2 (en) Rubber composition with improved cold resistance
JP3749019B2 (en) Chloroprene-based rubber composition
WO2022037060A1 (en) Preparation method for reduced graphene oxide nitrile rubber and for tooth block without tooth marks
CN102935689B (en) Core-shell type double-active acrylate elastic body modification fluorubber and preparation method thereof
CN103044830B (en) Sealing rubber for butterfly valve and preparation method thereof
JPS6395242A (en) Rubber composition having improved freeze-resistance
CN110835446A (en) Low-temperature flexible high-wear-resistance fluororubber compound and preparation method thereof
CN103421129B (en) A kind of liquid phase production technique of natural rubber
CN103044831B (en) A kind of synchronous gear box lid gasket sizing material and preparation method thereof
CN106987058A (en) A kind of compressor air-breathing bellows and its processing method
CN110577682A (en) High-low temperature resistant anti-aging chloroprene rubber

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: 20151216