JP2002187157A - Manufacturing method for expanded rubber roller and imaging device - Google Patents
Manufacturing method for expanded rubber roller and imaging deviceInfo
- Publication number
- JP2002187157A JP2002187157A JP2001229265A JP2001229265A JP2002187157A JP 2002187157 A JP2002187157 A JP 2002187157A JP 2001229265 A JP2001229265 A JP 2001229265A JP 2001229265 A JP2001229265 A JP 2001229265A JP 2002187157 A JP2002187157 A JP 2002187157A
- Authority
- JP
- Japan
- Prior art keywords
- roller
- rubber
- foamed rubber
- rubber roller
- foamed
- 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
Links
- 229920001971 elastomer Polymers 0.000 title claims abstract description 110
- 239000005060 rubber Substances 0.000 title claims abstract description 110
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 238000003384 imaging method Methods 0.000 title 1
- 239000000203 mixture Substances 0.000 claims abstract description 25
- 239000000853 adhesive Substances 0.000 claims abstract description 13
- 230000001070 adhesive effect Effects 0.000 claims abstract description 13
- 230000006835 compression Effects 0.000 claims abstract description 11
- 238000007906 compression Methods 0.000 claims abstract description 11
- 239000012790 adhesive layer Substances 0.000 claims abstract description 9
- 229920001821 foam rubber Polymers 0.000 claims abstract description 8
- 239000010410 layer Substances 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 26
- 238000005187 foaming Methods 0.000 claims description 21
- 238000004073 vulcanization Methods 0.000 claims description 20
- 229920000181 Ethylene propylene rubber Polymers 0.000 claims description 19
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 8
- 238000001125 extrusion Methods 0.000 claims description 8
- 229910052740 iodine Inorganic materials 0.000 claims description 8
- 239000011630 iodine Substances 0.000 claims description 8
- 238000005498 polishing Methods 0.000 claims description 7
- 239000004020 conductor Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000011417 postcuring Methods 0.000 claims 1
- 238000003825 pressing Methods 0.000 claims 1
- 238000000465 moulding Methods 0.000 abstract 1
- 239000006260 foam Substances 0.000 description 10
- 210000004027 cell Anatomy 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 9
- 210000000497 foam cell Anatomy 0.000 description 9
- 239000010734 process oil Substances 0.000 description 9
- 239000004088 foaming agent Substances 0.000 description 8
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- 239000011593 sulfur Substances 0.000 description 6
- 229910052717 sulfur Inorganic materials 0.000 description 6
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- NBOCQTNZUPTTEI-UHFFFAOYSA-N 4-[4-(hydrazinesulfonyl)phenoxy]benzenesulfonohydrazide Chemical compound C1=CC(S(=O)(=O)NN)=CC=C1OC1=CC=C(S(=O)(=O)NN)C=C1 NBOCQTNZUPTTEI-UHFFFAOYSA-N 0.000 description 3
- 239000004156 Azodicarbonamide Substances 0.000 description 3
- 239000004604 Blowing Agent Substances 0.000 description 3
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 3
- 235000019399 azodicarbonamide Nutrition 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- -1 sulfenamides Chemical class 0.000 description 3
- 239000011787 zinc oxide Substances 0.000 description 3
- 235000014692 zinc oxide Nutrition 0.000 description 3
- YXIWHUQXZSMYRE-UHFFFAOYSA-N 1,3-benzothiazole-2-thiol Chemical compound C1=CC=C2SC(S)=NC2=C1 YXIWHUQXZSMYRE-UHFFFAOYSA-N 0.000 description 2
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- CPGFMWPQXUXQRX-UHFFFAOYSA-N 3-amino-3-(4-fluorophenyl)propanoic acid Chemical compound OC(=O)CC(N)C1=CC=C(F)C=C1 CPGFMWPQXUXQRX-UHFFFAOYSA-N 0.000 description 1
- HLBZWYXLQJQBKU-UHFFFAOYSA-N 4-(morpholin-4-yldisulfanyl)morpholine Chemical compound C1COCCN1SSN1CCOCC1 HLBZWYXLQJQBKU-UHFFFAOYSA-N 0.000 description 1
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 235000004035 Cryptotaenia japonica Nutrition 0.000 description 1
- 244000146493 Cryptotaenia japonica Species 0.000 description 1
- BWGNESOTFCXPMA-UHFFFAOYSA-N Dihydrogen disulfide Chemical compound SS BWGNESOTFCXPMA-UHFFFAOYSA-N 0.000 description 1
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 1
- 229910000915 Free machining steel Inorganic materials 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 239000006237 Intermediate SAF Substances 0.000 description 1
- 229910000861 Mg alloy Inorganic materials 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229920006311 Urethane elastomer Polymers 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 229920000800 acrylic rubber Polymers 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 235000012538 ammonium bicarbonate Nutrition 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 229910002113 barium titanate Inorganic materials 0.000 description 1
- VJRITMATACIYAF-UHFFFAOYSA-N benzenesulfonohydrazide Chemical compound NNS(=O)(=O)C1=CC=CC=C1 VJRITMATACIYAF-UHFFFAOYSA-N 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- NJLLQSBAHIKGKF-UHFFFAOYSA-N dipotassium dioxido(oxo)titanium Chemical compound [K+].[K+].[O-][Ti]([O-])=O NJLLQSBAHIKGKF-UHFFFAOYSA-N 0.000 description 1
- 239000012990 dithiocarbamate Substances 0.000 description 1
- 150000004659 dithiocarbamates Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920005558 epichlorohydrin rubber Polymers 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 150000002357 guanidines Chemical class 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 239000003273 ketjen black 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
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002832 nitroso derivatives Chemical class 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 229920001084 poly(chloroprene) Polymers 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002296 pyrolytic carbon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001256 stainless steel alloy Inorganic materials 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 150000003557 thiazoles Chemical class 0.000 description 1
- 150000003585 thioureas Chemical class 0.000 description 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 1
- 229910001887 tin oxide Inorganic materials 0.000 description 1
- 125000005147 toluenesulfonyl group Chemical group C=1(C(=CC=CC1)S(=O)(=O)*)C 0.000 description 1
- MTPVUVINMAGMJL-UHFFFAOYSA-N trimethyl(1,1,2,2,2-pentafluoroethyl)silane Chemical compound C[Si](C)(C)C(F)(F)C(F)(F)F MTPVUVINMAGMJL-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Delivering By Means Of Belts And Rollers (AREA)
- Sheets, Magazines, And Separation Thereof (AREA)
- Rolls And Other Rotary Bodies (AREA)
- Dry Development In Electrophotography (AREA)
- Cleaning In Electrography (AREA)
- Electrostatic Charge, Transfer And Separation In Electrography (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、発泡ゴムローラの
製造方法の及び画像形成装置に関し、さらに詳しくは、
低硬度と低圧縮永久歪が両立し、微細な発泡セルを有
し、かつ硬度や電気抵抗のバラツキが小さく、複写機、
レーザープリンタ、ファクシミリなどの電子写真装置や
静電記録装置などの画像形成装置用の部材として好適に
使用される発泡ゴムローラの製造方法、及びその方法で
得られた発泡ゴムローラを装着した上記画像形成装置に
関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a foamed rubber roller and an image forming apparatus.
Low hardness and low compression set are compatible, having fine foam cells, and small variation in hardness and electric resistance.
Laser printers, a method of manufacturing a foamed rubber roller suitably used as a member for an image forming apparatus such as an electrophotographic apparatus such as a facsimile or an electrostatic recording apparatus, and the image forming apparatus equipped with the foamed rubber roller obtained by the method It is about.
【0002】[0002]
【従来の技術】近年、電子写真技術の進歩に伴い、電子
写真装置や静電記録装置等の画像形成装置には、帯電
用、現像用、転写用、トナー供給用、クリーニング用な
どに供される部品の部材として、帯電ローラ,現像ロー
ラ,転写ローラ,トナー供給ローラ,クリーニングロー
ラ、バイアスローラ、給紙ローラなどのローラ形状の部
材が多く用いられている。これらのローラは、高品位の
画像を得るために、低硬度であることが必要であり、通
常、発泡ゴムからなるローラが多用されている。しかし
ながら、発泡ゴムローラは、低硬度と低圧縮永久歪の両
立が難しく、発泡ゴムローラを低硬度のものとするため
には、発泡倍率を上げるのが効果的であるが、発泡倍率
を上げると圧縮永久歪が高くなるという問題があった。
また、最近の画像形成装置においては、高画質の画像を
得るために微細な発泡セルを有する発泡ゴムが求められ
ており、特に平均発泡セルが30〜100μmの発泡ゴ
ムで形成されたローラが求められている。さらに、発泡
ゴムローラに導電性を付与するという要求もあり、所定
の電気抵抗レベルを有し、かつ電気抵抗のバラツキの小
さいローラが求められている。2. Description of the Related Art In recent years, with the progress of electrophotographic technology, image forming apparatuses such as electrophotographic apparatuses and electrostatic recording apparatuses are used for charging, developing, transferring, supplying toner, and cleaning. Roller-shaped members, such as a charging roller, a developing roller, a transfer roller, a toner supply roller, a cleaning roller, a bias roller, and a paper feed roller, are often used as components of such components. These rollers need to have low hardness in order to obtain high-quality images, and usually rollers made of foamed rubber are often used. However, it is difficult for the foamed rubber roller to have both low hardness and low compression set, and it is effective to increase the foaming ratio in order to make the foamed rubber roller having a low hardness. There was a problem that distortion became high.
Further, in recent image forming apparatuses, foamed rubber having fine foamed cells is required in order to obtain a high-quality image. In particular, a roller formed of foamed rubber having an average foamed cell of 30 to 100 μm is required. Have been. Further, there is a demand for imparting conductivity to the foamed rubber roller, and a roller having a predetermined electric resistance level and a small variation in electric resistance has been demanded.
【0003】ところで、従来、発泡ゴムローラは以下の
ようにして製造されている。まず、発泡ゴム組成物を、
ゴム押出機を用いて円筒状に成形した後、所定寸法に切
断する。次に、ダミーシャフトを円筒状物の内径内に挿
入する。このものを加硫缶にセットし、蒸気加硫方式に
より加硫し、発泡させる。その後、加硫缶から取り出
し、さらに熱風炉で加熱することにより歪等を取り除
き、ダミーシャフトを外して、発泡ゴム円筒状物を得
る。次に、本シャフトの外周に接着剤を塗布して乾燥さ
せた後、上記発泡ゴム円筒状物にこの本シャフトを圧入
し、これをオーブン中で加熱して接着処理を行う。オー
ブンから取り出して冷却した後、発泡ゴム円筒状物の表
面を研磨して形状を整え、発泡ゴムローラを得る。発泡
ゴムローラの製造方法としては、この他にも種々の方法
があるが、従来の製造方法では、上記要求を満足する発
泡ゴムローラを得ることは難しく、かつ製造工程が複雑
であるため、製造コストが高くなるという問題があっ
た。[0003] By the way, conventionally, a foamed rubber roller is manufactured as follows. First, the foamed rubber composition,
After being formed into a cylindrical shape using a rubber extruder, it is cut into predetermined dimensions. Next, the dummy shaft is inserted into the inside diameter of the cylindrical object. This is set in a vulcanizer, vulcanized by a steam vulcanization method, and foamed. Then, it is taken out of the vulcanization can and further heated in a hot air furnace to remove distortion and the like, and the dummy shaft is removed to obtain a foamed rubber cylindrical material. Next, after applying an adhesive to the outer periphery of the shaft and drying the shaft, the shaft is press-fitted into the above-mentioned foamed rubber cylinder, and the shaft is heated in an oven to perform a bonding treatment. After being taken out of the oven and cooled, the surface of the foamed rubber cylinder is polished and shaped to obtain a foamed rubber roller. There are various other methods for producing the foamed rubber roller, but with the conventional production method, it is difficult to obtain a foamed rubber roller that satisfies the above requirements, and the production process is complicated. There was a problem of getting high.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上記事情に
鑑みてなされたもので、低硬度と低圧縮永久歪が両立
し、微細な発泡セルを有し、かつ硬度や電気抵抗のバラ
ツキが小さい発泡ゴムローラを、簡単な工程で安価に安
定して製造する方法を提供することを目的とするもので
ある。DISCLOSURE OF THE INVENTION The present invention has been made in view of the above circumstances, and has both low hardness and low compression set, has fine foam cells, and has uneven hardness and electric resistance. An object of the present invention is to provide a method for stably manufacturing a small foamed rubber roller at a low cost by a simple process.
【0005】[0005]
【課題を解決するための手段】本発明者らは、上記目的
を達成するために鋭意検討を行った結果、発泡ゴム組成
物を、接着剤層を形成したシャフトの外周に円筒状に押
出し成形して得られた未発泡ゴムローラを、加圧加硫
し、発泡させた後に後加硫することにより、上記特性を
有する発泡ゴムローラを得ることができることを見出し
た。本発明は、かかる知見に基づいて完成したものであ
る。すなわち、本発明は、シャフトの外周にゴム発泡体
層が形成された発泡ゴムローラの製造方法において、
(1)シャフトの外周に接着剤を塗布して接着剤層を形
成する工程、(2)発泡ゴム組成物を、前記接着剤層を
形成したシャフトの外周に、ゴム押出機を用いて円筒状
に押出し成形して未発泡ゴムローラを得る工程、(3)
該未発泡ゴムローラを、予め温度を調整した割り金型内
にセットし、所定時間、所定圧力で加圧しながら加硫
し、発泡させる工程、(4)割り金型を開放し、前記で
得られたローラを割り金型から取り出す工程、及び
(5)前記で得られたローラを所定の外径に調整する工
程を具備することを特徴とする発泡ゴムローラの製造方
法を提供するものである。また、本発明は、上記の製造
方法で得られた導電性発泡体ローラを装着したことを特
徴とする画像形成装置をも提供するものである。Means for Solving the Problems The present inventors have made intensive studies to achieve the above object, and as a result, have extruded a foamed rubber composition into a cylindrical shape on the outer periphery of a shaft having an adhesive layer formed thereon. It has been found that a foamed rubber roller having the above characteristics can be obtained by subjecting the unfoamed rubber roller obtained as described above to pressure vulcanization, foaming and post-vulcanization. The present invention has been completed based on such findings. That is, the present invention relates to a method for manufacturing a foamed rubber roller in which a rubber foam layer is formed on the outer periphery of a shaft,
(1) a step of applying an adhesive to the outer periphery of the shaft to form an adhesive layer; Extrusion molding to obtain an unfoamed rubber roller, (3)
Setting the unfoamed rubber roller in a split mold whose temperature has been adjusted in advance, vulcanizing and foaming while applying a predetermined pressure for a predetermined time, and (4) opening the split mold to obtain the above obtained mold. And (5) a step of adjusting the obtained roller to a predetermined outside diameter. Further, the present invention also provides an image forming apparatus equipped with the conductive foam roller obtained by the above manufacturing method.
【0006】[0006]
【発明の実施の形態】本発明の発泡ゴムローラの製造方
法においては、原料ゴム、発泡剤、加硫剤などのゴム用
添加剤を含有する発泡ゴム組成物が用いられる。原料ゴ
ムとしては、天然ゴム,ニトリルゴム,エチレンプロピ
レンゴム, スチレンブタジエンゴム,ブタジエンゴム,
イソプレンゴム,シリコーンゴム,ウレタンゴム,アク
リルゴム,クロロプレンゴム,エピクロルヒドリンゴム
等が挙げられるが、エチレンプロピレンゴムが好まし
い。エチレンプロピレンゴムとしては、特にヨウ素価が
35〜45、かつムーニー粘度ML1+4 (100℃)が
20〜50のエチレンプロピレンゴムが好適に使用され
る。ヨウ素価は35〜40が特に好ましく、ムーニー粘
度ML1+4 (100℃)は30〜45が特に好ましい。
ヨウ素価が35未満では、発泡体の圧縮永久歪が20〜
40%となり、また、ヨウ素価が45を超えると、エチ
レンプロピレンゴム発泡体のオゾン等に対する耐久性が
小さくなる。ムーニー粘度が20未満では、これを用い
た未加硫ゴム組成物の粘度が小さくなりすぎ、発泡が過
度に起こるため、セルが粗大になり、また、ムーニー粘
度が50を超えると、未加硫ゴム組成物の粘度が大きく
なり、発泡が不十分となるため、発泡体密度が大きくな
る。BEST MODE FOR CARRYING OUT THE INVENTION In the method for producing a foamed rubber roller of the present invention, a foamed rubber composition containing a rubber additive such as a raw rubber, a foaming agent and a vulcanizing agent is used. Raw rubber includes natural rubber, nitrile rubber, ethylene propylene rubber, styrene butadiene rubber, butadiene rubber,
Examples include isoprene rubber, silicone rubber, urethane rubber, acrylic rubber, chloroprene rubber, and epichlorohydrin rubber, and ethylene propylene rubber is preferred. As the ethylene propylene rubber, an ethylene propylene rubber having an iodine value of 35 to 45 and a Mooney viscosity ML 1 + 4 (100 ° C.) of 20 to 50 is particularly preferably used. The iodine value is particularly preferably 35 to 40, and the Mooney viscosity ML 1 + 4 (100 ° C.) is particularly preferably 30 to 45.
When the iodine value is less than 35, the compression set of the foam is 20 to
When the iodine value exceeds 40% and the iodine value exceeds 45, the durability of the ethylene propylene rubber foam to ozone and the like decreases. If the Mooney viscosity is less than 20, the viscosity of the unvulcanized rubber composition using the same becomes too small and foaming occurs excessively, so that the cell becomes coarse. Since the viscosity of the rubber composition increases and foaming becomes insufficient, the foam density increases.
【0007】エチレンプロピレンゴム発泡体は、上述し
たエチレンプロピレンゴムを用いたものであれば他の成
分は適宜選定すればよいが、エチレンゴム発泡体を導電
性のものとする場合、好ましくは上記原料ゴム100重
量部に対して、(A)加硫剤0.5〜5重量部、(B)発
泡剤1〜15重量部、(C)プロセスオイル10〜80
重量部、(D)充填材10〜60重量部及び(E)導電
材1〜80重量部を添加して加硫、発泡することにより
得ることができる。なお、原料ゴムとしてエチレンプロ
ピレンゴム以外のものを用いた場合も、同様に原料ゴム
100重量部に対して、(A)〜(E)成分を添加する
ことが好ましく、以下に示すものと同様の成分を添加す
ることができる。(A)成分の加硫剤としては、種々も
のを用いることができるが、エチレンプロピレンゴム組
成物の発泡及び加硫の制御を容易に行うことができる点
から、硫黄系加硫剤が好ましい。ここで、硫黄系加硫剤
とは、硫黄と加硫促進剤との組み合わせ、あるいは含硫
黄有機化合物をいう。加硫促進剤としては、チアゾール
類,スルフェンアミド類,チオウレア類,チウラム類,
ジチオカルバミン酸塩類,グアニジン類,アルデヒドア
ミン類,アルデヒドアンモニア類が挙げられ、これらの
一種を単独で又は二種以上を混合して用いることができ
る。含硫黄有機化合物としては、例えば、モルホリンジ
スルフィド,テトラアルキルチウラムジスルフィド,ジ
ペンタメチレンチウラムテトラスルフィド等が挙げられ
る。加硫剤の添加量は、エチレンプロピレンゴムゴム1
00重量部に対して0.5〜5重量部が好ましい。The ethylene propylene rubber foam may be appropriately selected from other components as long as the ethylene propylene rubber is made of the above-mentioned ethylene propylene rubber. (A) 0.5 to 5 parts by weight of a vulcanizing agent, (B) 1 to 15 parts by weight of a foaming agent, and (C) 10 to 80 parts by weight of rubber per 100 parts by weight of rubber.
Parts by weight, 10 to 60 parts by weight of (D) filler and 1 to 80 parts by weight of (E) conductive material, and vulcanization and foaming. When a material other than ethylene propylene rubber is used as the raw material rubber, it is also preferable to add the components (A) to (E) to 100 parts by weight of the raw material rubber in the same manner. Ingredients can be added. Various vulcanizing agents can be used as the component (A), but a sulfur-based vulcanizing agent is preferred because foaming and vulcanization of the ethylene propylene rubber composition can be easily controlled. Here, the sulfur-based vulcanizing agent refers to a combination of sulfur and a vulcanization accelerator or a sulfur-containing organic compound. Examples of the vulcanization accelerator include thiazoles, sulfenamides, thioureas, thiurams,
Examples thereof include dithiocarbamates, guanidines, aldehyde amines, and aldehyde ammonias. One of these can be used alone, or two or more can be used in combination. Examples of the sulfur-containing organic compound include morpholine disulfide, tetraalkylthiuram disulfide, dipentamethylenethiuram tetrasulfide, and the like. The amount of the vulcanizing agent added is ethylene propylene rubber rubber 1
The amount is preferably 0.5 to 5 parts by weight based on 00 parts by weight.
【0008】(B)成分の発泡剤としては、例えば、
p,p’−オキシビス(ベンゼンスルホニルヒドラジ
ド)(OBSH),ベンゼンスルホニルヒドラジド,ト
ルエンスルホニルヒドラジド等のスルホニルヒドラジ
ド、アゾジカルボンアミド(ADCA),アゾビスイソ
ブチロニトリル等のアゾ化合物、N,N’−ジニトロソ
ペンタメチレンテトラミン,N,N’−ジメチル−N,
N’−ジニトロソテレフタルアミド等のニトロソ化合物
などの有機発泡剤;重炭酸ナトリウム,重炭酸アンモニ
ウム等の無機発泡剤が挙げられる。これらの中でもOB
SH,ADCAあるいはこれらを併用した発泡剤が好ま
しい。発泡剤の添加量は、エチレンプロピレンゴム10
0重量部に対して1〜10重量部が好ましく、3〜8重
量部が特に好ましい。発泡剤は、その粒子径を可及的小
さくすることが、発泡セルを小さくするために好まし
い。発泡剤の粒子径は10μm以下が好ましく、5μm
以下が特に好ましい。(C)成分のプロセスオイルとし
ては、パラフィン系プロセスオイル,ナフテン系プロセ
スオイル及び芳香族系プロセスオイルを使用することが
できる。この中で、感光体等の他の部材を汚染すること
がない点から、パラフィン系プロセスオイルが好まし
い。プロセスオイルの添加量は、エチレンプロピレンゴ
ム100重量部に対して20〜70重量部が好ましく、
40〜70重量部が特に好ましい。プロセスオイルの添
加量が20重量部未満では、未発泡ゴム組成物の粘度が
大きくなって加工性が悪くなり、また、発泡が不十分と
なるため、発泡体の密度が大きくなってしまう。また、
プロセスオイルの添加量が70重量部を超えると、未加
硫ゴム組成物の粘度が小さくなりすぎ、発泡が過度に起
こるため、セルが粗大になるという不都合が生じる。
(D)成分の充填材としては、例えば、炭酸カルシウ
ム,炭酸マグネシウム,シリカ,珪酸マグネシウム,ク
レー等が挙げられる。この中で、発泡セルの安定化の点
から、炭酸カルシウムが好ましい。充填材の添加量は、
エチレンプロピレンゴム100重量部に対して10〜6
0重量部が好ましく、20〜50重量部が特に好まし
い。充填材の添加量が10重量部未満では、発泡セルが
安定せず、不均一になり、また、充填材の添加量が60
重量部を超えると、エチレンプロピレンゴム発泡体の圧
縮永久歪が大きくなってしまう。As the foaming agent of the component (B), for example,
azo compounds such as p, p'-oxybis (benzenesulfonyl hydrazide) (OBSH), benzenesulfonyl hydrazide, toluenesulfonyl hydrazide, etc .; azo compounds such as azodicarbonamide (ADCA) and azobisisobutyronitrile; Dinitrosopentamethylenetetramine, N, N'-dimethyl-N,
Organic blowing agents such as nitroso compounds such as N'-dinitrosoterephthalamide; and inorganic blowing agents such as sodium bicarbonate and ammonium bicarbonate. Among them, OB
SH, ADCA or a foaming agent using them in combination is preferable. The amount of the foaming agent added is ethylene propylene rubber 10
1 to 10 parts by weight, preferably 3 to 8 parts by weight, based on 0 parts by weight. It is preferable that the particle diameter of the foaming agent be as small as possible in order to reduce the size of the foam cells. The particle diameter of the blowing agent is preferably 10 μm or less, and 5 μm
The following are particularly preferred. As the process oil of the component (C), paraffin-based process oil, naphthene-based process oil and aromatic-based process oil can be used. Among these, a paraffin-based process oil is preferable because it does not contaminate other members such as a photoconductor. The addition amount of the process oil is preferably 20 to 70 parts by weight based on 100 parts by weight of ethylene propylene rubber,
Particularly preferred is 40 to 70 parts by weight. If the amount of the process oil is less than 20 parts by weight, the viscosity of the unfoamed rubber composition becomes large and the processability becomes poor, and the foaming becomes insufficient, so that the density of the foam becomes large. Also,
If the amount of the process oil exceeds 70 parts by weight, the viscosity of the unvulcanized rubber composition becomes too low, and excessive foaming occurs, resulting in a disadvantage that cells become coarse.
Examples of the filler for the component (D) include calcium carbonate, magnesium carbonate, silica, magnesium silicate, and clay. Of these, calcium carbonate is preferred from the viewpoint of stabilizing the foam cells. The amount of filler
10-6 per 100 parts by weight of ethylene propylene rubber
0 parts by weight is preferable, and 20 to 50 parts by weight is particularly preferable. If the amount of the filler is less than 10 parts by weight, the foam cells are not stable and become non-uniform.
When the amount exceeds the weight part, the compression set of the ethylene propylene rubber foam becomes large.
【0009】(E)成分の導電材としては、ケッチェン
ブラック,アセチレンブラック等の導電性カーボンブラ
ック;SAF,ISAF,HAF,FEF,GPF,S
RF,FT,MT等のゴム用カーボンブラック;酸化カ
ーボンブラック等のインク用カーボンブラック,熱分解
カーボンブラック,グラファイト;酸化スズ,酸化チタ
ン,酸化亜鉛等の導電性金属酸化物;ニッケル,銅等の
金属;カーボンウイスカー,黒鉛ウイスカー,炭化チタ
ンウイスカー,導電性チタン酸カリウムウイスカー,導
電性チタン酸バリウムウイスカー,導電性酸化チタンウ
イスカー,導電性酸化亜鉛ウイスカー等の導電性ウイス
カーなどが挙げられる。導電材の添加量は、エチレンプ
ロピレンゴム100重量部に対して1〜80重量部が好
ましく、5〜60重量部が特に好ましい。上記導電材の
添加により、本発明の発泡ゴムローラを、体積固有抵抗
104 〜1010Ω・cmに調整することができる。本発
明の発泡ゴムローラにおいて、体積固有抵抗は105 〜
108 Ω・cmの範囲にあることが、良好な画像を得る
点から特に好ましい。上記エチレンプロピレンゴム発泡
体には、上記の添加剤以外に、亜鉛華,ステアリン酸等
の加硫促進剤、スコーチ防止剤、粘着付与剤、その他ゴ
ム用添加剤を、本発明の効果を損なわない範囲で適宜添
加することができる。As the conductive material of the component (E), conductive carbon black such as Ketjen black and acetylene black; SAF, ISAF, HAF, FEF, GPF, S
Carbon black for rubber such as RF, FT, MT; carbon black for ink such as carbon oxide black, pyrolytic carbon black, graphite; conductive metal oxide such as tin oxide, titanium oxide, zinc oxide; nickel, copper, etc. Metals: conductive whiskers such as carbon whiskers, graphite whiskers, titanium carbide whiskers, conductive potassium titanate whiskers, conductive barium titanate whiskers, conductive titanium oxide whiskers, and conductive zinc oxide whiskers. The amount of the conductive material to be added is preferably from 1 to 80 parts by weight, particularly preferably from 5 to 60 parts by weight, per 100 parts by weight of the ethylene propylene rubber. By adding the conductive material, the foamed rubber roller of the present invention can be adjusted to a volume resistivity of 10 4 to 10 10 Ω · cm. In the foamed rubber roller of the present invention, the volume resistivity is 10 5 to
It is particularly preferable that the thickness be in the range of 10 8 Ω · cm from the viewpoint of obtaining good images. In the ethylene propylene rubber foam, in addition to the above additives, vulcanization accelerators such as zinc white and stearic acid, anti-scorch agents, tackifiers, and other rubber additives do not impair the effects of the present invention. It can be appropriately added within the range.
【0010】本発明で用いる発泡ゴム組成物は、上記原
料ゴムに加硫剤及び発泡剤以外の添加剤を110〜18
0℃程度の温度でニーダー、バンバリーミキサー等を使
用して混練する。この混練物を冷却した後に、加硫剤及
び発泡剤を添加し、50〜90℃程度の温度で混練して
発泡ゴム組成物を得る。本発明の発泡ゴムローラの製造
方法においては、まず、シャフトの外周に接着剤を塗布
して接着剤層を形成する〔工程(1)〕。シャフトとし
ては、例えば硫黄快削鋼などの鋼材に亜鉛などのメッキ
を施した金属部材、アルミニウム,ステンレス鋼,マグ
ネシウム合金などの金属部材が挙げられる。また、接着
剤としては、ホットメルトタイプ、溶剤乾燥タイプ、加
熱架橋タイプ等がある。本発明においては、いずれのタ
イプも用いることができる。この中で、加熱架橋タイプ
を用いると、工程(3)における加硫及び発泡と同時に
接着剤の加熱架橋が進行するので、発泡ゴムとシャフト
の間の接着が強固になり、工程(4)において割り金型
を開放したときに、発泡ゴムがシャフトが剥がれること
がなく、好ましい。[0010] The foamed rubber composition used in the present invention is prepared by adding additives other than a vulcanizing agent and a foaming agent to the above-mentioned raw rubber in a range of 110 to 18;
Kneading is performed at a temperature of about 0 ° C. using a kneader, a Banbury mixer or the like. After cooling the kneaded product, a vulcanizing agent and a foaming agent are added, and the mixture is kneaded at a temperature of about 50 to 90 ° C. to obtain a foamed rubber composition. In the method for manufacturing a foamed rubber roller of the present invention, first, an adhesive is applied to the outer periphery of the shaft to form an adhesive layer [Step (1)]. Examples of the shaft include a metal member obtained by plating a steel material such as sulfur free-cutting steel with zinc or the like, and a metal member such as aluminum, stainless steel, and magnesium alloy. The adhesive includes a hot melt type, a solvent drying type, a heat crosslinking type and the like. In the present invention, any type can be used. Among them, when the heat cross-linking type is used, the heat cross-linking of the adhesive proceeds simultaneously with the vulcanization and foaming in the step (3), so that the adhesion between the foamed rubber and the shaft becomes strong. When the split mold is opened, the foamed rubber is preferable because the shaft does not peel off.
【0011】次に、上記発泡ゴム組成物を、接着剤層を
形成したシャフトの外周に、ゴム押出機を用いて円筒状
に押出し成形して未発泡ゴムローラを得る〔工程
(2)〕。ゴム押出機としては、クロスヘッド式押出機
が好適に用いられる。すなわち、シャフト送り機構を備
えた口金で、発泡ゴム組成物をシャフトの進行方向と直
交する方向から押出し、発泡ゴム組成物でシャフト外周
を被覆する方法が好ましい。このように押出機により被
覆する方法ではなく、例えば、発泡ゴム組成物をシート
状に形成したものをシャフトに巻き付けることによりシ
ャフトの外周を被覆した場合、工程(3)における加硫
及び発泡の際に、発泡ゴムとシャフトの間に空隙ができ
易く、好ましくない。ゴム押出機による押出し速度は、
0.4〜4m/分が好ましい。また、押出し温度は重要で
あり、発泡ゴム組成物が加硫及び発泡する温度よりも低
い温度に設定する必要がある。押出し温度は、加硫及び
発泡工程における温度よりも30℃以上低くすることが
好ましい。押出し温度は、例えば40〜130℃とする
ことができる。Next, the above foamed rubber composition is extruded into a cylindrical shape using a rubber extruder on the outer periphery of the shaft on which the adhesive layer is formed to obtain an unfoamed rubber roller [step (2)]. As the rubber extruder, a crosshead type extruder is suitably used. That is, it is preferable to extrude the foamed rubber composition from a direction perpendicular to the traveling direction of the shaft with a die provided with a shaft feed mechanism, and cover the outer periphery of the shaft with the foamed rubber composition. Rather than the method of coating with an extruder as described above, for example, when the outer periphery of the shaft is coated by winding a foamed rubber composition in a sheet shape around the shaft, the vulcanization and foaming in step (3) Further, a gap is easily formed between the foamed rubber and the shaft, which is not preferable. The extrusion speed by the rubber extruder is
0.4 to 4 m / min is preferred. Further, the extrusion temperature is important, and it is necessary to set the extrusion temperature to a temperature lower than the temperature at which the foamed rubber composition vulcanizes and foams. The extrusion temperature is preferably lower than the temperature in the vulcanization and foaming steps by 30 ° C. or more. The extrusion temperature can be, for example, 40 to 130 ° C.
【0012】押出し成形により得られた未発泡ゴムロー
ラは、予め温度を調整した割り金型内にセットし、所定
時間、所定圧力で加圧しながら加硫し、発泡させる〔工
程(3)〕。発泡ゴムローラが微細発泡セルを有するも
のとするためには、未発泡ゴムローラを圧力下に加硫、
発泡させることが重要である。割り金型にかける圧力
は、9.8×105 〜9.8×106 Pa(約10〜100
kg/cm2 )、好ましくは1.9×106 〜7.9×10
6 Pa(約20〜80kg/cm2 )である。加硫、発
泡の温度は、発泡ゴム組成物の組成によって適宜決めら
れるが、通常140〜180℃である。また、割り金型
内で加硫、発泡させる時間は通常5〜30分程度であ
る。未発泡ゴムローラが金型のキャビティに占める割合
は、発泡ゴムローラの硬度バラツキや電気抵抗バラツキ
を小さくするために、95〜105容量%とすることが
好ましい。The unfoamed rubber roller obtained by the extrusion molding is set in a split mold whose temperature has been adjusted in advance, and is vulcanized by foaming while applying a predetermined pressure for a predetermined time [step (3)]. In order for the foamed rubber roller to have fine foam cells, the unfoamed rubber roller is vulcanized under pressure,
It is important to foam. The pressure applied to the split mold is 9.8 × 10 5 to 9.8 × 10 6 Pa (about 10 to 100 Pa).
kg / cm 2 ), preferably 1.9 × 10 6 to 7.9 × 10
6 Pa (about 20 to 80 kg / cm 2 ). The temperature for vulcanization and foaming is appropriately determined depending on the composition of the foamed rubber composition, but is usually 140 to 180 ° C. The time for vulcanization and foaming in the split mold is usually about 5 to 30 minutes. The proportion of the unfoamed rubber roller occupying the mold cavity is preferably 95 to 105% by volume in order to reduce the hardness variation and the electrical resistance variation of the foamed rubber roller.
【0013】未発泡ゴムローラを割り金型内で加硫、発
泡させた後、割り金型を開放し、ローラを割り金型から
取り出す〔工程(4)〕。割り金型を開放する際に、発
泡圧によりローラが膨張する。この膨張は、均一である
ことが、発泡セルの大きさの均一性、さらには硬度や電
気抵抗の均一性を得るために重要である。従って、割り
金型が均一に開放されるような装置設計が好ましい。After vulcanizing and foaming the unfoamed rubber roller in the split mold, the split mold is opened and the roller is taken out of the split mold (step (4)). When the split mold is opened, the roller expands due to the foaming pressure. It is important that the expansion is uniform in order to obtain uniformity of the size of the foamed cells, and also uniformity of hardness and electric resistance. Therefore, it is preferable to design the apparatus such that the split mold is opened uniformly.
【0014】次に、発泡ゴムローラを所定の外径に調整
する〔工程(5)〕。発泡ゴムローラを所定の外径に調
整する方法としては、特に限定されるものではないが、
回転砥石による研磨、ブレードによるピーリング等の方
法が挙げられる。回転砥石による研磨としては、ローラ
の長さよりも幅の狭い砥石を用いるトラバース研磨と、
ローラの長さとほぼ同等の幅を持つ砥石を用いるプラン
ジ研磨があるが、生産性が良好である点から、プランジ
研磨が好ましい。上記工程(4)及び/又は工程(5)
の後に、発泡ゴムローラの後加硫を行なう〔工程
(6)〕ことが好ましい。後加硫は、発泡ゴムローラの
発泡セルの形態を安定させ、発泡ゴムローラの硬度、寸
法及び電気抵抗の安定化、圧縮永久歪の低減、加工歪の
低減に効果がある。また、発泡ゴムローラを後加硫する
ことにより、発泡ゴム組成物に存在した低分子化合物を
気散せしめることができるので、発泡ゴムローラを画像
形成体に当接して使用する場合の汚染を防止することが
できる。後加硫の温度及び時間は、70〜200℃で、
15〜300分程度である。Next, the foamed rubber roller is adjusted to a predetermined outer diameter [Step (5)]. The method for adjusting the foam rubber roller to a predetermined outer diameter is not particularly limited,
Methods such as polishing with a rotary grindstone, peeling with a blade, and the like can be given. As polishing with a rotating grindstone, traverse polishing using a grindstone narrower than the length of the roller,
Although there is plunge polishing using a grindstone having a width substantially equal to the length of the roller, plunge polishing is preferable because productivity is good. Step (4) and / or step (5) above
It is preferable to perform post-vulcanization of the foamed rubber roller after [Step (6)]. Post-vulcanization stabilizes the form of the foam cells of the foamed rubber roller, stabilizes the hardness, dimensions and electrical resistance of the foamed rubber roller, reduces compression set, and reduces processing strain. Further, by post-vulcanizing the foamed rubber roller, it is possible to disperse the low molecular compound present in the foamed rubber composition. Therefore, it is possible to prevent contamination when the foamed rubber roller is used in contact with the image forming body. Can be. The post-vulcanization temperature and time are 70-200 ° C,
It is about 15 to 300 minutes.
【0015】このようにして得られた発泡ゴムローラ
は、低硬度と低圧縮永久歪が両立し、微細な発泡セルを
有し、かつ硬度や電気抵抗のバラツキが小さいという特
徴を有するものである。それ故、本発明の発泡ゴムロー
ラは、複写機、レーザープリンタ、ファクシミリなどの
電子写真装置や静電記録装置などの画像形成装置に装着
されて、帯電ローラ,現像ローラ,転写ローラ,トナー
供給ローラ,クリーニングローラ、バイアスローラ、給
紙ローラ等として好適に使用されるものである。The foamed rubber roller thus obtained is characterized by having both low hardness and low compression set, having fine foam cells, and having small variations in hardness and electric resistance. Therefore, the foamed rubber roller of the present invention is mounted on an image forming apparatus such as an electrophotographic apparatus such as a copying machine, a laser printer, and a facsimile, and an electrostatic recording apparatus, and includes a charging roller, a developing roller, a transfer roller, a toner supply roller, It is suitably used as a cleaning roller, a bias roller, a paper feed roller, or the like.
【0016】[0016]
【実施例】次に、本発明を実施例によりさらに詳細に説
明するが、本発明はこれらの例によってなんら限定され
るものではない。なお、実施例例で得られた導電性ロー
ラの物性は、以下の方法に従って測定した。 (1)ゴム発泡体の物性 (イ)セル径及びセル数 ハイロックス社製のCCDビデオカメラを用い、約70
倍の倍率で写真撮影を行い、画像のセル径及びセル数を
測定した。 (ロ)アスカーC硬度 JIS K6301に準拠して測定した。 (ハ)密度 ゴム発泡体の空気中での重量を、体積で除した。 (ニ)圧縮永久歪 JIS K6382(クッション用ホームラバー)に準
拠して測定した。 (ホ)体積固有抵抗値 下記の導電性ローラの抵抗から、次式により体積固有抵
抗ρを算出した。 R=(ρr2 /Ld)ln(r2 /r1 ) ただし、 R:導電性ローラの抵抗 ρ:ゴム発泡体の体積固有抵抗 L:軸方向の接触長さ d:ニップ幅 r1 :シャフトの半径 r2 : 導電性ローラの外半径 ln:自然対数 (2)導電性ローラの抵抗 被試験体ローラの両端に各500gの荷重を掛けて銅板
上に押し付け、抵抗率計R8340A(アドバンテスト
社製)を用い、100Vの電圧を印加して抵抗値を測定
した。 (3)導電性ローラの抵抗バラツキ 被試験体ローラに円筒形の金電極を1000gの荷重で
押し付け、ローラ外周の72点を抵抗率計R8340A
(アドバンテスト社製)で測定し、最大値と最小値との
差を抵抗バラツキとした。なお、第1表において、桁と
は、72点の抵抗測定値の常用対数の最大値と最小値の
差を意味する。Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. The physical properties of the conductive roller obtained in the examples were measured according to the following methods. (1) Physical Properties of Rubber Foam (a) Cell Diameter and Number of Cells Using a CCD video camera manufactured by Hilox, about 70
Photographs were taken at double magnification, and the cell diameter and cell number of the image were measured. (B) Asker C hardness Measured according to JIS K6301. (C) Density The weight of the rubber foam in the air was divided by the volume. (D) Compression set Measured in accordance with JIS K 6382 (Home Rubber for Cushion). (E) Volume resistivity The volume resistivity ρ was calculated from the following resistance of the conductive roller by the following equation. R = (ρr 2 / Ld) ln (r 2 / r 1 ) where R: resistance of conductive roller ρ: volume resistivity of rubber foam L: contact length in axial direction d: nip width r 1 : shaft Radius of conductive roller r 2 : outer radius of conductive roller ln: natural logarithm (2) Resistance of conductive roller A load of 500 g is applied to both ends of the roller to be tested and pressed on a copper plate to obtain a resistivity meter R8340A (manufactured by Advantest Co.) ), A voltage of 100 V was applied to measure the resistance value. (3) Variation in resistance of conductive roller A cylindrical gold electrode is pressed against the roller under test with a load of 1000 g, and 72 points on the outer periphery of the roller are measured with a resistivity meter R8340A.
(Manufactured by Advantest Corporation), and the difference between the maximum value and the minimum value was regarded as resistance variation. In Table 1, the digit means the difference between the maximum value and the minimum value of the common logarithm of the 72 measured resistance values.
【0017】実施例1 金属製シャフト(外径6mm,長さ260mm)の外周
に接着剤〔ロード・ファー・イースト・インコーポレイ
テッド製,ケムロック250X〕を塗布し、風乾して接
着剤付きシャフトを得た。風乾後の接着剤層の厚さは1
0〜30μmであった〔工程(1)〕。ヨウ素価が3
6、ムーニー粘度ML1+4 (100℃)が39のEPD
M100重量部に対して第1表に示す配合成分を55L
ニーダーを用いて混練して、発泡ゴム組成物を調製し、
この発泡ゴム組成物を、クロスヘッド式押出機(三葉製
作所製)を用いて、上記接着剤付きシャフトの外周に円
筒状に押出し、未発泡ゴムとシャフトとが一体となった
未発泡ゴムローラ(外径22mm、長さ240mm)を
得た〔工程(2)〕。この未発泡ゴムローラを円筒状の
割り金型内にセットし、3.2×105 Paの圧力をか
け、175℃で20分間加硫、発泡を行った〔工程
(3)〕。次いで、割り金型の圧力を開放し、シャフト
と発泡ゴムとが接着剤により強固に接着した、スキン層
付き発泡ゴムローラを得た〔工程(4)〕。この発泡ゴ
ムローラを、180℃に調整したオーブン中で4時間、
後加硫を行った〔工程(6)〕。得られた発泡ゴムロー
ラを、プランジ方式研磨により回転砥石で研磨し、外径
20mm、長さ230mmの発泡ゴムローラを得た〔工
程(5)〕。この発泡ゴムローラの物性を第1表に示
す。EXAMPLE 1 An adhesive (Chemrock 250X, manufactured by Lord Far East, Inc.) is applied to the outer periphery of a metal shaft (outer diameter 6 mm, length 260 mm) and air-dried to obtain a shaft with an adhesive. Was. Adhesive layer thickness after air drying is 1
0 to 30 μm [Step (1)]. Iodine value is 3
6. EPD with Mooney viscosity ML 1 + 4 (100 ° C) of 39
55 L of the ingredients shown in Table 1 with respect to 100 parts by weight of M
Kneading using a kneader to prepare a foamed rubber composition,
Using a crosshead extruder (manufactured by Mitsuba Seisakusho), this foamed rubber composition is extruded into a cylindrical shape around the outer periphery of the shaft with the adhesive, and a non-foamed rubber roller (in which the foamed rubber and the shaft are integrated) An outer diameter of 22 mm and a length of 240 mm) were obtained [Step (2)]. This unfoamed rubber roller was set in a cylindrical mold, and a pressure of 3.2 × 10 5 Pa was applied thereto, followed by vulcanization and foaming at 175 ° C. for 20 minutes [step (3)]. Next, the pressure of the split mold was released to obtain a foamed rubber roller with a skin layer in which the shaft and the foamed rubber were firmly adhered with an adhesive [step (4)]. The foamed rubber roller was placed in an oven adjusted to 180 ° C. for 4 hours.
Post vulcanization was performed [Step (6)]. The obtained foamed rubber roller was polished with a rotary grindstone by plunge polishing to obtain a foamed rubber roller having an outer diameter of 20 mm and a length of 230 mm [Step (5)]. Table 1 shows the physical properties of the foam rubber roller.
【0018】[0018]
【表1】 [Table 1]
【0019】(注) (1)ヨウ素価が36、ムーニー粘度ML1+4 (100
℃)が39のEPDM (2)東海カーボン社製,TB#5500 (3)日東粉化工業社製,ノーベライトA (4)出光興産社製,ダイアナプロセスオイルPW90 (5)2−メルカプトベンゾチアゾール (6)永和化成工業社製,ネオセルボンN#1000M
〔p,p’−オキシビス(ベンゼンスルホニルヒドラジ
ド)〕(Note) (1) Iodine value is 36, Mooney viscosity ML 1 + 4 (100
(C) 39 (2) Tokai Carbon Co., Ltd., TB # 5500 (3) Nitto Powder Chemical Co., Ltd., Novelite A (4) Idemitsu Kosan Co., Ltd., Diana Process Oil PW90 (5) 2-mercaptobenzothiazole ( 6) Neocelbon N # 1000M, manufactured by Eiwa Chemical Co., Ltd.
[P, p'-oxybis (benzenesulfonylhydrazide)]
【0020】[0020]
【発明の効果】本発明の発泡ゴムローラは、低硬度と低
圧縮永久歪が両立し、微細な発泡セルを有し、かつ硬度
や電気抵抗のバラツキが小さく、複写機,レーザープリ
ンタ,ファクシミリなどの電子写真装置や静電記録装置
などの画像形成装置用の部材として好適に用いられる。The foamed rubber roller of the present invention has both low hardness and low compression set, has fine foam cells, and has a small variation in hardness and electric resistance, and can be used in copiers, laser printers, facsimile machines and the like. It is suitably used as a member for an image forming apparatus such as an electrophotographic apparatus and an electrostatic recording apparatus.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) G03G 15/02 101 G03G 15/08 501A 3J103 15/08 501 501D 4F212 15/16 103 15/16 103 B29L 9:00 21/10 31:32 // B29L 9:00 B29C 67/22 31:32 G03G 21/00 312 Fターム(参考) 2H077 AC04 AD06 FA12 FA22 FA25 2H134 HA03 HA04 HA05 HA17 HA18 KD05 KD12 KE02 KE07 KH10 2H200 FA13 GA34 HA01 HA28 HB12 HB22 HB45 HB46 HB47 JA25 JA26 JA27 JB10 LC03 LC08 MA03 MA08 MA12 MA14 MA17 MB04 MC01 MC02 MC11 MC15 3F049 AA01 CA16 LA01 LB01 3F343 FA01 FB02 FC01 FC04 JA11 KB04 KB16 3J103 AA02 AA32 BA41 EA02 EA11 EA13 FA18 GA57 GA58 GA60 HA03 HA12 HA20 HA53 4F212 AA46A AA46C AB02 AB13 AG03 AG20 AH04 AH33 AR12 UA01 UB01 UB11 UB22 UC05 UG04 UG05 UK06 UN01 UN11 UW24 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) G03G 15/02 101 G03G 15/08 501A 3J103 15/08 501 501D 4F212 15/16 103 15/16 103 B29L 9 : 00 21/10 31:32 // B29L 9:00 B29C 67/22 31:32 G03G 21/00 312 F term (reference) 2H077 AC04 AD06 FA12 FA22 FA25 2H134 HA03 HA04 HA05 HA17 HA18 KD05 KD12 KE02 KE07 KH10 2H200 FA13 GA34 HA01 HA28 HB12 HB22 HB45 HB46 HB47 JA25 JA26 JA27 JB10 LC03 LC08 MA03 MA08 MA12 MA14 MA17 MB04 MC01 MC02 MC11 MC15 3F049 AA01 CA16 LA01 LB01 3F343 FA01 FB02 FC01 FC04 JA11 KB04 KB16 3J103 AA02 EA13 GA41 EA02 GA41 HA20 HA53 4F212 AA46A AA46C AB02 AB13 AG03 AG20 AH04 AH33 AR12 UA01 UB01 UB11 UB22 UC05 UG04 UG05 UK06 UN01 UN1 1 UW24
Claims (13)
れた発泡ゴムローラの製造方法において、(1)シャフ
トの外周に接着剤を塗布して接着剤層を形成する工程、
(2)発泡ゴム組成物を、前記接着剤層を形成したシャ
フトの外周に、ゴム押出機を用いて円筒状に押出し成形
して未発泡ゴムローラを得る工程、(3)該未発泡ゴム
ローラを、予め温度を調整した割り金型内にセットし、
所定時間、所定圧力で加圧しながら加硫し、発泡させる
工程、(4)割り金型を開放し、前記で得られたローラ
を割り金型から取り出す工程、及び(5)前記で得られ
たローラを所定の外径に調整する工程を具備することを
特徴とする発泡ゴムローラの製造方法。1. A method for manufacturing a foamed rubber roller in which a rubber foam layer is formed on the outer periphery of a shaft, wherein (1) a step of applying an adhesive to the outer periphery of the shaft to form an adhesive layer;
(2) a step of extruding the foamed rubber composition into a cylindrical shape using a rubber extruder on the outer periphery of the shaft on which the adhesive layer is formed to obtain an unfoamed rubber roller; Set in a split mold whose temperature has been adjusted in advance,
Vulcanizing and foaming while applying pressure at a predetermined pressure for a predetermined time, (4) opening the split mold, removing the roller obtained above from the split mold, and (5) obtaining the roller obtained above. A method for manufacturing a foamed rubber roller, comprising a step of adjusting the roller to a predetermined outer diameter.
に、(6)所定温度に調整した加熱炉中で所定時間、後
加硫を行う工程を具備するものである請求項1に記載の
製造方法。2. The method according to claim 1, further comprising, after the step (4) and / or the step (5), (6) a step of performing post-curing for a predetermined time in a heating furnace adjusted to a predetermined temperature. The manufacturing method as described.
る請求項1又は2に記載の製造方法。3. The method according to claim 1, wherein the adhesive is a heat-crosslinkable adhesive.
レンプロピレンゴムを含むものである請求項1〜3のい
ずれかに記載の製造方法。4. The method according to claim 1, wherein the foamed rubber composition contains ethylene propylene rubber as a rubber component.
5〜45、かつ100℃におけるムーニー粘度がML
1+4 が20〜50のものである請求項4に記載の製造方
法。5. An ethylene propylene rubber having an iodine value of 3
Mooney viscosity at 5 to 45 and 100 ° C is ML
The method according to claim 4, wherein 1 + 4 is 20 to 50.
ある請求項1〜5のいずれかに記載の製造方法。6. The method according to claim 1, wherein the foamed rubber composition contains a conductive material.
押出し成形の温度が、工程(3)における加硫及び発泡
の温度よりも30℃以上低いものである請求項1〜6の
いずれかに記載の製造方法。7. The method according to claim 1, wherein the temperature of the extrusion molding in the step (2) for obtaining the unfoamed roller is lower than the temperature of the vulcanization and foaming in the step (3) by 30 ° C. or more. The manufacturing method as described.
工程(3)において、未発泡ゴムローラが金型のキャビ
ティに占める割合が95〜105容量%である請求項1
〜7のいずれかに記載の製造方法。8. The method according to claim 1, wherein in the step (3) of vulcanizing and foaming the unfoamed rubber roller, the ratio of the unfoamed rubber roller to the cavity of the mold is 95 to 105% by volume.
8. The method according to any one of items 1 to 7.
(5)において、該調整が、プランジ方式の研磨機を用
いて行われる請求項1〜8のいずれかに記載の製造方
法。9. The method according to claim 1, wherein in the step (5) of adjusting the roller to a predetermined outer diameter, the adjustment is performed using a plunge type polishing machine.
度が0.1〜0.5g/cm3 、かつ圧縮永久歪が15%以
下のものである請求項1〜9のいずれかに記載製造方
法。10. The method according to claim 1, wherein the foamed rubber roller has a foamed rubber density of 0.1 to 0.5 g / cm 3 and a compression set of 15% or less. .
均発泡セル径が30〜100μmのものである請求項1
〜10のいずれかに記載の製造方法。11. The foamed rubber roller has an average foamed cell diameter of the foamed rubber of 30 to 100 μm.
11. The method according to any one of items 10 to 10.
積固有抵抗が104〜1010Ω・cmのものである請求
項1〜11のいずれかに記載の製造方法。12. The production method according to claim 1, wherein the foamed rubber roller has a volume resistivity of 10 4 to 10 10 Ω · cm.
造方法で得られた発泡ゴムローラを装着したことを特徴
とする画像形成装置。13. An image forming apparatus equipped with a foamed rubber roller obtained by the method according to claim 1. Description:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001229265A JP2002187157A (en) | 2000-10-13 | 2001-07-30 | Manufacturing method for expanded rubber roller and imaging device |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000312823 | 2000-10-13 | ||
| JP2000-312823 | 2000-10-13 | ||
| JP2001229265A JP2002187157A (en) | 2000-10-13 | 2001-07-30 | Manufacturing method for expanded rubber roller and imaging device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002187157A true JP2002187157A (en) | 2002-07-02 |
Family
ID=26602007
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006171418A (en) * | 2004-12-16 | 2006-06-29 | Yamauchi Corp | Conductive sponge roller and its manufacturing method |
| JP2007132431A (en) * | 2005-11-10 | 2007-05-31 | Inoac Corp | Method of manufacturing foam roller |
| JP2007293007A (en) * | 2006-04-25 | 2007-11-08 | Bridgestone Corp | Method of manufacturing foam roller and foam roller |
| JP2008275656A (en) * | 2007-04-25 | 2008-11-13 | Tokai Rubber Ind Ltd | Charging roll and manufacturing method thereof |
| CN101866128A (en) * | 2009-04-15 | 2010-10-20 | 东海橡胶工业株式会社 | Charged roller and manufacture method thereof |
-
2001
- 2001-07-30 JP JP2001229265A patent/JP2002187157A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006171418A (en) * | 2004-12-16 | 2006-06-29 | Yamauchi Corp | Conductive sponge roller and its manufacturing method |
| JP2007132431A (en) * | 2005-11-10 | 2007-05-31 | Inoac Corp | Method of manufacturing foam roller |
| JP2007293007A (en) * | 2006-04-25 | 2007-11-08 | Bridgestone Corp | Method of manufacturing foam roller and foam roller |
| JP2008275656A (en) * | 2007-04-25 | 2008-11-13 | Tokai Rubber Ind Ltd | Charging roll and manufacturing method thereof |
| CN101866128A (en) * | 2009-04-15 | 2010-10-20 | 东海橡胶工业株式会社 | Charged roller and manufacture method thereof |
| JP2010266844A (en) * | 2009-04-15 | 2010-11-25 | Tokai Rubber Ind Ltd | Charging roll and manufacturing method thereof |
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