CN1089964A - 硫化或半硫化橡胶的快速再生方法 - Google Patents
硫化或半硫化橡胶的快速再生方法 Download PDFInfo
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- CN1089964A CN1089964A CN93112734A CN93112734A CN1089964A CN 1089964 A CN1089964 A CN 1089964A CN 93112734 A CN93112734 A CN 93112734A CN 93112734 A CN93112734 A CN 93112734A CN 1089964 A CN1089964 A CN 1089964A
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- rubber
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- elastomerics
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- 238000011069 regeneration method Methods 0.000 title description 37
- 230000008929 regeneration Effects 0.000 title description 36
- 229920001971 elastomer Polymers 0.000 claims abstract description 21
- 239000002904 solvent Substances 0.000 claims abstract description 5
- 239000000126 substance Substances 0.000 claims abstract description 5
- 230000008961 swelling Effects 0.000 claims abstract description 4
- 230000001172 regenerating effect Effects 0.000 claims abstract description 3
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 238000005987 sulfurization reaction Methods 0.000 claims description 4
- 238000006477 desulfuration reaction Methods 0.000 claims description 2
- 230000023556 desulfurization Effects 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims description 2
- 231100000614 poison Toxicity 0.000 claims description 2
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- 239000000203 mixture Substances 0.000 abstract description 8
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- 230000002588 toxic effect Effects 0.000 abstract description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 22
- 239000006229 carbon black Substances 0.000 description 18
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 16
- 239000005864 Sulphur Substances 0.000 description 16
- 238000010058 rubber compounding Methods 0.000 description 11
- 239000011787 zinc oxide Substances 0.000 description 11
- 235000021355 Stearic acid Nutrition 0.000 description 9
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 9
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- 239000008117 stearic acid Substances 0.000 description 9
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- KUAZQDVKQLNFPE-UHFFFAOYSA-N thiram Chemical compound CN(C)C(=S)SSC(=S)N(C)C KUAZQDVKQLNFPE-UHFFFAOYSA-N 0.000 description 7
- AFZSMODLJJCVPP-UHFFFAOYSA-N dibenzothiazol-2-yl disulfide Chemical compound C1=CC=C2SC(SSC=3SC4=CC=CC=C4N=3)=NC2=C1 AFZSMODLJJCVPP-UHFFFAOYSA-N 0.000 description 6
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 6
- 239000011347 resin Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- IANQTJSKSUMEQM-UHFFFAOYSA-N 1-benzofuran Chemical compound C1=CC=C2OC=CC2=C1 IANQTJSKSUMEQM-UHFFFAOYSA-N 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- REQPQFUJGGOFQL-UHFFFAOYSA-N dimethylcarbamothioyl n,n-dimethylcarbamodithioate Chemical compound CN(C)C(=S)SC(=S)N(C)C REQPQFUJGGOFQL-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 229920002943 EPDM rubber Polymers 0.000 description 3
- 229920000459 Nitrile rubber Polymers 0.000 description 3
- ATPFMBHTMKBVLS-VZEWWGGESA-N (z)-3-phenyl-n-[6-[[(e)-3-phenylprop-2-enylidene]amino]hexyl]prop-2-en-1-imine Chemical compound C=1C=CC=CC=1/C=C/C=NCCCCCCN=C\C=C/C1=CC=CC=C1 ATPFMBHTMKBVLS-VZEWWGGESA-N 0.000 description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- ZRALSGWEFCBTJO-UHFFFAOYSA-N Guanidine Chemical compound NC(N)=N ZRALSGWEFCBTJO-UHFFFAOYSA-N 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 239000005662 Paraffin oil Substances 0.000 description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 2
- 230000002939 deleterious effect Effects 0.000 description 2
- AUZONCFQVSMFAP-UHFFFAOYSA-N disulfiram Chemical compound CCN(CC)C(=S)SSC(=S)N(CC)CC AUZONCFQVSMFAP-UHFFFAOYSA-N 0.000 description 2
- 235000003599 food sweetener Nutrition 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 229910000464 lead oxide Inorganic materials 0.000 description 2
- 229920003052 natural elastomer Polymers 0.000 description 2
- 229920001194 natural rubber Polymers 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000002304 perfume Substances 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 238000009418 renovation Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000003765 sweetening agent Substances 0.000 description 2
- PIZNQHDTOZMVBH-UHFFFAOYSA-N thionylimide Chemical compound N=S=O PIZNQHDTOZMVBH-UHFFFAOYSA-N 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- OWRCNXZUPFZXOS-UHFFFAOYSA-N 1,3-diphenylguanidine Chemical compound C=1C=CC=CC=1NC(=N)NC1=CC=CC=C1 OWRCNXZUPFZXOS-UHFFFAOYSA-N 0.000 description 1
- ZEMPKEQAKRGZGQ-AAKVHIHISA-N 2,3-bis[[(z)-12-hydroxyoctadec-9-enoyl]oxy]propyl (z)-12-hydroxyoctadec-9-enoate Chemical compound CCCCCCC(O)C\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CC(O)CCCCCC)COC(=O)CCCCCCC\C=C/CC(O)CCCCCC ZEMPKEQAKRGZGQ-AAKVHIHISA-N 0.000 description 1
- HNNQYHFROJDYHQ-UHFFFAOYSA-N 3-(4-ethylcyclohexyl)propanoic acid 3-(3-ethylcyclopentyl)propanoic acid Chemical compound CCC1CCC(CCC(O)=O)C1.CCC1CCC(CCC(O)=O)CC1 HNNQYHFROJDYHQ-UHFFFAOYSA-N 0.000 description 1
- 206010060766 Heteroplasia Diseases 0.000 description 1
- 229920013646 Hycar Polymers 0.000 description 1
- VHOQXEIFYTTXJU-UHFFFAOYSA-N Isobutylene-isoprene copolymer Chemical group CC(C)=C.CC(=C)C=C VHOQXEIFYTTXJU-UHFFFAOYSA-N 0.000 description 1
- CHJJGSNFBQVOTG-UHFFFAOYSA-N N-methyl-guanidine Natural products CNC(N)=N CHJJGSNFBQVOTG-UHFFFAOYSA-N 0.000 description 1
- 239000004902 Softening Agent Substances 0.000 description 1
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
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- 239000006227 byproduct Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- SWSQBOPZIKWTGO-UHFFFAOYSA-N dimethylaminoamidine Natural products CN(C)C(N)=N SWSQBOPZIKWTGO-UHFFFAOYSA-N 0.000 description 1
- 238000006735 epoxidation reaction Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007701 flash-distillation Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 229960001708 magnesium carbonate Drugs 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 235000014380 magnesium carbonate Nutrition 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- HKOOXMFOFWEVGF-UHFFFAOYSA-N phenylhydrazine Chemical compound NNC1=CC=CC=C1 HKOOXMFOFWEVGF-UHFFFAOYSA-N 0.000 description 1
- 229940067157 phenylhydrazine Drugs 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 229940099259 vaseline Drugs 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/10—Recovery or working-up of waste materials of polymers by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/06—Recovery or working-up of waste materials of polymers without chemical reactions
- C08J11/08—Recovery or working-up of waste materials of polymers without chemical reactions using selective solvents for polymer components
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2321/00—Characterised by the use of unspecified rubbers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S525/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S525/938—Polymer degradation
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
本发明揭示了通过使用合适的溶剂溶胀橡胶块,
并限制其与或存在于有毒或脱硫化学组份中来“快速
再生硫化或半硫化橡胶的方法”。
该过程可在比常压高或低的压力下,以冷或热的
方法进行。
该过程可使用任何类型的硫化或半硫化橡胶组
合物。
由此过程可获得比那些由干燥或研磨过程获得
再生产物具有更低价格的再生产物。
Description
本发明涉及通过使用合适的溶剂溶胀橡胶块,并通过其与或存在于有毒的或脱硫化学组份中的限制来再生硫化或半硫化橡胶的方法。
所有工业上的方法为了降低其费用,增加其效率而使用更廉价的原材料,并增加其副产物的利用价值。回收工业的发展方向是寻求提供具有更低成本和改进质量的能使用配方的方法,显而易见的是,越接近原始配方的性能,所得再生产品的质量就越好。
PI-8500981中所描述的方法披露了使用有毒试剂作为溶胀橡胶块的溶剂,它描述了使用研磨机的方法,其中使用了某些有毒的化学产物同时完成了橡胶粒子的还原。该方法与使用同样的配方的常规方法所获得的产品相比,能以更低的成本低得更高质量的再生产品,常规方法是用热作为再生剂(浸煮器或压热器)并配以机械研磨(精制机)的方法。
进一步的专利和在巴西专利PI-8500981,即专利GB1334718,US2088920,US4156508,BR7606727和GB505156,其它专利及集中在澳大利亚的PC9715中所述的方法,所有的这些专利全都使用以溶胀以减弱橡胶强度,以使其中的补强成份,如纤维和金属线更易分离。在澳大利亚的方法中,尽管并未使橡胶再生,它只是将颗粒的尺寸降至0.3-0.8mm。由该过程获得的橡胶只作为其它配方中的载体。
本发明所涉及的整个橡胶(硫化或半硫化)的再生方法比巴西专利PI8500981更快,因为橡胶再生是与或是在有毒化学品中进行,在加工的同时,在过滤阶段进行颗粒还原,而不是偏重于研磨。当在压力下通过限制橡胶的情况下,会使橡胶尺寸减小,同时与有毒组份接触,随后将压力降至更低的压力,由于溶胀橡胶颗粒的溶剂产生闪蒸就会引起橡胶的第二次断裂。若每次重复此限制过程的橡胶颗粒尺寸越小,则每次获得的再生作用就越大,越均匀,且性能就越接近于原始的橡胶配方。
使用毒性组份的橡胶脱硫活化剂可改善再生性能并提高过程速度。所用的脱硫剂:胍及其衍生物如二苯基胍;肼及其衍生物如苯肼;苯胺类如苯胺等。其它较多使用的脱硫剂为油脂酸衍生物,有机金属配位化合物的混合物,异生(allogenated)衍生物,如五氯硫代苯,苯甲酸,苯二酸酐等。在该同样的过程顺序中,当橡胶配方被溶胀并由于限制作用而断裂时,可加入其它物质如增塑剂,树脂,载体,抗氧剂,促进剂,熟化剂等。这样获得的糊状的或稠厚的油在合适的干燥器中进行干燥,就可将溶剂回收并可再行使用。
本发明的限制包括一种或多种钻孔金属板,或筛网,或海绵,或多孔金属板,或任何其它的相同类型的或将它们组合起来使用的限制。
本发明过程可使用任何类型的硫化,半硫化,熟化,半熟化橡胶组合物进行。
本发明过程可以冷或热的方式来进行。
本发明过程可在比常压高或低的压力下进行。
实施例1 由下述天然橡胶配方制备:
天然橡胶 100.00
氧化锌 5.00
硬脂酸 2.00
碳黑N-330 45.00
BLE抗氧剂 1.00
芳香油 4.00
促进剂(亚磺酰胺) 0.60
硫 2.50
硫化 30分 145℃
拉伸强度 kg/cm2 285
300%模量 kg/cm2 115
断裂时的伸长 % 500
硬度 肖氏A 65
再生
样品1: 纯再生高弹体NR
样品2: 再生高弹体NR 100.00
促进剂(亚磺酰胺) 0.30
硫 1.25
101.55
硫化 30分 145℃
样品1 样品2
拉伸强度 kg/cm2 150 190
30%模量 kg/cm2 95 105
断裂时的伸长 % 480 400
硬度 肖氏A 65 67
实施例2 由下述丙烯腈橡胶配方制备:
Hycar 1042 100.00
氧化锌 5.00
硬脂酸 1.50
碳黑N-550 30.00
碳黑N-762 40.00
磷酸三 7.00
环氧化蓖麻油 8.00
促进剂(TMTMS) 0.60
硫 1.00
193.10
硫化 30分 155℃
拉伸强度 kg/cm2 160
300%模量 kg/cm2 150
断裂时的伸长 % 330
硬度 肖氏A 62
再生
样品1: 纯再生高弹体NBR
样品2: 再生高弹体NBR 193.00
促进剂(TMTMS) 0.30
硫 0.50
193.80
硫化 30分 155℃
样品1 样品2
拉伸强度 kg/cm2 80 110
300%模量 kg/cm2 60 -
断裂时的伸长 % 300 260
硬度 肖氏A 62 65
实施例3 由下述CR橡胶配方制备:
Neprene W 100.00
氧化锌 5.00
氧化镁 4.0
硬脂酸 1.0
碳黑N-110 30.00
环烷酸 4.00
氧茚树脂 4.00
凡士林 2.0
Banox H 2.0
TMTMS 0.60
DPG 0.60
硫 1.00
154.20
硫化 30分 155℃
拉伸强度 kg/cm2 255
300%模量 kg/cm2 110
断裂时的伸长 % 520
硬度 肖氏A 66
再生:
样品1: 纯再生高弹体CR
样品2: 再生高弹体CR 154.00
TMTMS 0.30
DPG 0.80
硫 0.50
155.60
硫化 30分 155℃
样品1 样品2
拉伸强度 kg/cm2 150 200
300%模量 kg/cm2 80 140
断裂时的伸长 % 500 410
硬度 肖氏A 66 68
实施例4 由下述SBR橡胶配方制备:
SBR1502 100.00
氧化锌 4.00
碳黑N-672 25.00
Banox H 1.00
Santocure 1.80
TMTD 1.30
TETD 1.30
134.40
硫化 20分 155℃
拉伸强度 kg/cm2 155
300%模量 kg/cm2 39
断裂时的伸长 % 700
硬度 肖氏A 49
再生:
样品1: 纯再生高弹体SBR
样品2: 再生高弹体SBR 134.40
Santocure 0.90
TMTD 0.60
TETD 0.60
136.50
样品1 样品2
拉伸强度 kg/cm2 65 105
300%模量 kg/cm2 15 65
断裂时的伸长 % 650 570
硬度 肖氏A 49 52
实施例5 由下述丁基橡胶配方制备:
Exxon 丁基268 100.00
氧化锌 5.00
碳黑N-550 25.00
碳黑N-762 25.00
石蜡油 10.00
TTD 1.00
MBTS 0.50
硫 2.00
168.50
硫化 20分 152℃
拉伸强度 kg/cm2 110.00
300%模量 kg/cm2 55.00
断裂时的伸长 % 400.00
硬度 肖氏A 52.00
再生
样品1: 纯再生高弹体IIR
样品2: 再生高弹体IIR 168.50
TMTD 0.50
MBTS 0.25
硫 1.00
170.25
硫化 20分 152℃
样品1 样品2
拉伸强度 kg/cm2 50 78
300%模量 kg/cm2 20 52
断裂时的伸长 % 360 310
硬度 肖氏A 52 54
实施例6 由下述BR橡胶配方制备:
BR-55 100.00
硬脂酸 2.00
氧化锌 5.00
Santocure 1.25
TMTD 0.15
硫 10.00
118.40
硫化 10分 150℃
硬度 肖氏A 66
回弹 % 92
再生
样品1: 纯再生高弹体BR
样品2: 再生高弹体BR 118.40
Santocure 0.60
TMTD 0.10
硫 2.00
121.10
硫化 10分 150℃
样品1 样品2
硬度 肖氏A 66 68
回弹 % 70 85
实施例7 由下述CSM橡胶配方制备:
HYPALON-40 100.00
密陀僧(即氧化铅) 20.00
碳酸镁 20.00
碳黑N-762 50.00
芳香油 10.00
MBTS 0.50
TETRONE A 2.00
202.50
硫化 30分 155℃
拉伸强度 kg/cm2 225
断裂时的伸长 % 200
硬度 肖氏A 73
再生
样品1: 纯再生高弹体CMS
样品2: 再生高弹体CMS 202.50
MBTS 0.25
TETRONEA 1.00
203.75
硫化 30分 155℃
样品1 样品2 拉伸强度
kg/cm2 140 180 断裂时的
伸长
% 120 100 硬度
肖氏A 73 76
实施例8 由下述FMK橡胶配方制配:
VITON B 100.00
密陀僧(即氧化铅) 15.00
碳黑MT 30.00
Diak 3 3.00
148.00
硫化 20分 177℃
加热 24小时 260℃
拉伸强度 kg/cm2 155
断裂时的伸长 % 200
硬度 肖氏A 78
再生
样品1: 纯再生高弹体FMK
样品2: 再生高弹体FMK 148.00
Diak3 1.5
149.5
硫化 20分 177℃
样品1 样品2
拉伸强度 kg/cm2 80 110
断裂时的伸长 % 160 140
硬度 肖氏A 78 82
实施例9 由下述EPDM橡胶配方制备:
NITRIFLEX EP-21 100.00
氧化锌 5.00
硬脂酸 2.00
碳黑N-660 80.00
石蜡油 10.00
MBTS 1.50
TMTD 0.80
DMDTC Zn 0.80
硫 2.00
202.10
硫化 25分 170℃
拉伸强度 kg/cm2 160.00
300%模量 kg/cm2 80.00
断裂时的伸长 % 350.00
硬度 肖氏A 73.00
再生
样品1: 纯再生高弹体EPDM
样品2: 再生高弹体EPDM 100.00
MBTS 0.70
TMTD 0.40
DMDTC Zn 0.40
硫 1.00
102.50
硫化 25分 170℃
样品1 样品2
拉伸强度 kg/cm2 60.00 100.00
30%模量 kg/cm2 35.00 60.00
断裂时的伸长 % 340.00 300.00
硬度 肖氏A 73 76.00
A.从制备基本组合物开始比较各种再生方法
1.基本组合物
2.再生高弹体A-通过研磨降低颗粒尺寸,在浆料中再生,专利PI-8500981。
3.再生-使用压热器和干法精制机。
4.再生高弹体B-通过本发明所述的限制降低颗粒尺寸,在浆料中再生。
1.基本组合物
SBR-1712 100.00
碳黑N-220 27.50
碳黑N-336 20.00
Dutrex R 4.00
氧茚树脂 5.00
Banox H 1.50
氧化锌 5.00
硬脂酸 1.00
Santocure 1.50
DPG 0.50
硫 1.50
167.50
硫化 45分 150℃
拉伸强度 kg/cm2 139.30
300%模量 kg/cm2 62.10
断裂时的伸长 % 540.00
硬度 肖氏A 58.00
磨损 mm3 0.26
2.再生高弹体A
SBR-1712 100.00
再生高弹体A 63.20
碳黑N-336 23.10
碳黑N-220 32.00
氧化锌 7.10
硬脂酸 1.40
Dutrex R 5.70
氧茚树脂 7.10
Banox H 2.20
Santocure 2.20
DPG 0.70
硫 2.20
246.90
硫化 45分 150℃
拉伸强度 kg/cm2 139.80
300%模量 kg/cm2 60.60
断裂时的伸长 % 500.00
硬度 肖氏A 58.00
磨损 mm3 0.29
3.再生-通常工业方法
SBR-1712 100.00
再生橡胶 63.20
碳黑N-336 23.10
碳黑N-220 32.00
氧化锌 7.10
硬脂酸 1.40
Dutrex R 5.70
氧茚树脂 7.10
Santocure 2.20
硫 2.20
244.00
硫化 45分 150℃
拉伸强度 kg/cm2 118.40
300%模量 kg/cm2 54.20
断裂时的伸长 % 520.00
硬度 肖氏A 58.00
磨损 mm3 0.34
4.再生高弹体B-A新方法
SBR-1712 100.00
再生高弹体B 63.00
碳黑N-336 23.10
碳黑N-220 32.00
氧化锌 7.10
硬脂酸 1.40
Dutex R 5.70
氧茚树脂 7.10
Banox H 2.20
Santocure 2.20
DPG 0.70
硫 2.20
246.70
硫化 45分 150℃
拉伸强度 kg/cm2 135.00
300%模量 kg/cm2 62.00
断裂时的伸长 % 450.00
硬度 肖氏A 58.00
磨损 mm3 0.30
Claims (5)
1、一种再生硫化或半硫化橡胶的方法,使之在合适的溶剂中溶胀,其特征在于,提供溶胀的橡胶块,并限制其与或存在于有毒或脱硫化学阻份中。
2、如权利要求1所述的方法,其特征在于,限制包括一种或多种钻孔金属板,或筛网,或海绵,或多孔金属板,或任何其它的相同类型的或将它们组合起来使用的限制。
3、如权利要求1所述的方法,其特征在于,过程可使用任何类型的硫化,半硫化,熟化,半熟化橡胶组合物进行。
4、如权利要求1所述的方法,其特征在于,过程可以冷或热的方式来进行。
5、如权利要求1所述的方法,其特征在于,过程可在比常压高或低的压力下进行。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI9300252 | 1993-01-22 | ||
BR9300252A BR9300252A (pt) | 1993-01-22 | 1993-01-22 | Processo rápido para regeneração de borracha vulcanizada ou semi-vulcanizada |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1089964A true CN1089964A (zh) | 1994-07-27 |
CN1048023C CN1048023C (zh) | 2000-01-05 |
Family
ID=4055696
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN93112734A Expired - Fee Related CN1048023C (zh) | 1993-01-22 | 1993-12-31 | 硫化或半硫化橡胶的快速再生方法 |
Country Status (5)
Country | Link |
---|---|
US (1) | US5677354A (zh) |
EP (1) | EP0608157A1 (zh) |
JP (1) | JPH06238664A (zh) |
CN (1) | CN1048023C (zh) |
BR (1) | BR9300252A (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101973189A (zh) * | 2010-10-25 | 2011-02-16 | 杭州顺源轮胎制造有限公司 | 防弹安全轮胎 |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6129877A (en) * | 1998-09-04 | 2000-10-10 | Kuc, Sr.; John | Method and system for fabricating elastomeric articles |
US6525105B1 (en) * | 1999-05-13 | 2003-02-25 | The Yokohama Rubber Co., Ltd. | Methods of separating vulcanized or unvulcanized rubber and separating rubber composite, rubber composition containing recovered rubber or recovered carbon black, and process for producing carbon black |
IL132422A0 (en) | 1999-10-17 | 2001-03-19 | Levgum Ltd | Modifier for devulcanization of cured elastomers mainly vulcanized rubber and method for devulcanization by means of this modifier |
JP2003534956A (ja) | 2000-10-06 | 2003-11-25 | ジョン ドボジー, | エラストマー材料の回収方法および装置 |
US6387966B1 (en) * | 2001-05-21 | 2002-05-14 | Vadim Goldshtein | Method and composition for devulcanization of waste rubber |
DE10237091B4 (de) * | 2002-08-13 | 2004-10-28 | Webasto Vehicle Systems International Gmbh | Gleitbackenführung für öffnungsfähige Fahrzeugdächer oder Fahrzeugklappen |
CZ298755B6 (cs) * | 2005-12-02 | 2008-01-16 | Kubánek@Vladimír | Způsob devulkanizace, nebo devulkanizace a následné vulkanizace odpadní pryže |
US7767722B2 (en) * | 2006-12-11 | 2010-08-03 | Green Source Energy Llc | Devulcanized rubber and methods |
US8404108B2 (en) | 2007-09-20 | 2013-03-26 | Green Source Energy Llc | Extraction of hydrocarbons from hydrocarbon-containing materials and/or processing of hydrocarbon-containing materials |
US8101812B2 (en) | 2007-09-20 | 2012-01-24 | Green Source Energy Llc | Extraction of hydrocarbons from hydrocarbon-containing materials |
US8272442B2 (en) | 2007-09-20 | 2012-09-25 | Green Source Energy Llc | In situ extraction of hydrocarbons from hydrocarbon-containing materials |
UA104886C2 (uk) | 2009-03-13 | 2014-03-25 | Грін Сорс Енерджі Ллк | Екстракція вуглеводнів з вуглеводневмісних матеріалів і/або переробка вуглеводневмісних матеріалів |
JP5761243B2 (ja) * | 2013-03-29 | 2015-08-12 | 株式会社安川電機 | モータ制御装置および磁極位置推定方法 |
EP3294536B1 (en) * | 2015-05-15 | 2019-09-11 | Bridgestone Corporation | Tyre sealant layer |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2088920A (en) | 1935-02-02 | 1937-08-03 | Us Rubber Prod Inc | Manufacture of articles form vulcanized rubber |
GB505156A (en) | 1937-11-26 | 1939-05-05 | Pirelli | Improvements in or relating to processes for the integral recovery of scrap vulcanised rubber |
BE438709A (zh) * | 1939-04-27 | 1900-01-01 | ||
NL287613A (zh) * | 1962-01-09 | 1900-01-01 | ||
CA954103A (en) | 1970-09-14 | 1974-09-03 | Rudolph H. Kohler | Process for cryogenically reclaiming scrap rubber |
US4098737A (en) * | 1973-01-02 | 1978-07-04 | Gould Inc. | Treatment of vulcanized rubber |
GB1554858A (en) | 1975-10-08 | 1979-10-31 | Dunlop Ltd | Method and apparatus for the recovery of vulcanised elastomeric material |
US4156508A (en) * | 1976-09-22 | 1979-05-29 | Cryogenic Recycling International Inc. | Mobile material shearing apparatus |
US4161464A (en) * | 1978-03-24 | 1979-07-17 | The B. F. Goodrich Company | Devulcanized rubber composition and process for preparing same |
JPS5641202A (en) * | 1979-09-14 | 1981-04-17 | Bridgestone Corp | Decomposition of vulcanized rubber |
BR8500981A (pt) * | 1985-03-05 | 1986-11-18 | Luiz Carlos Oliveira Da Cunha | Processo para regeneracao de borracha vulcanizada |
BR9003627A (pt) * | 1990-07-26 | 1992-02-18 | Luiz Carlos Oliveira Da Cunha | Processo de obtencao de borracha termoplastica |
US5304576A (en) * | 1992-08-14 | 1994-04-19 | Southwestern Laboratories, Inc. | Waste tire disposal and recycling |
-
1993
- 1993-01-22 BR BR9300252A patent/BR9300252A/pt not_active IP Right Cessation
- 1993-12-31 CN CN93112734A patent/CN1048023C/zh not_active Expired - Fee Related
-
1994
- 1994-01-06 EP EP19940400038 patent/EP0608157A1/en not_active Withdrawn
- 1994-01-20 JP JP465494A patent/JPH06238664A/ja active Pending
-
1996
- 1996-02-29 US US08/608,935 patent/US5677354A/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101973189A (zh) * | 2010-10-25 | 2011-02-16 | 杭州顺源轮胎制造有限公司 | 防弹安全轮胎 |
CN101973189B (zh) * | 2010-10-25 | 2012-07-04 | 杭州顺源轮胎制造有限公司 | 防弹安全轮胎 |
Also Published As
Publication number | Publication date |
---|---|
JPH06238664A (ja) | 1994-08-30 |
US5677354A (en) | 1997-10-14 |
EP0608157A1 (en) | 1994-07-27 |
BR9300252A (pt) | 1994-08-09 |
CN1048023C (zh) | 2000-01-05 |
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