TW201026777A - Conductive resin composite material - Google Patents

Conductive resin composite material Download PDF

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Publication number
TW201026777A
TW201026777A TW98133256A TW98133256A TW201026777A TW 201026777 A TW201026777 A TW 201026777A TW 98133256 A TW98133256 A TW 98133256A TW 98133256 A TW98133256 A TW 98133256A TW 201026777 A TW201026777 A TW 201026777A
Authority
TW
Taiwan
Prior art keywords
vapor
carbon fiber
composite material
grown carbon
resin composite
Prior art date
Application number
TW98133256A
Other languages
Chinese (zh)
Other versions
TWI443149B (en
Inventor
Masayuki Nishijima
Hiroshi Sato
Shoji Kawashima
Yoshinori Hitoe
Jun Suzuki
Original Assignee
Hodogaya Chemical Co Ltd
Achilles Corp
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.)
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Publication date
Application filed by Hodogaya Chemical Co Ltd, Achilles Corp filed Critical Hodogaya Chemical Co Ltd
Publication of TW201026777A publication Critical patent/TW201026777A/en
Application granted granted Critical
Publication of TWI443149B publication Critical patent/TWI443149B/en

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B1/00Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
    • H01B1/20Conductive material dispersed in non-conductive organic material
    • H01B1/24Conductive material dispersed in non-conductive organic material the conductive material comprising carbon-silicon compounds, carbon or silicon
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/04Reinforcing macromolecular compounds with loose or coherent fibrous material
    • C08J5/0405Reinforcing macromolecular compounds with loose or coherent fibrous material with inorganic fibres
    • C08J5/042Reinforcing macromolecular compounds with loose or coherent fibrous material with inorganic fibres with carbon fibres
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2369/00Characterised by the use of polycarbonates; Derivatives of polycarbonates

Abstract

The present invention is an electroconductive resin composite material comprising a polycarbonate resin and a vapor-grown carbon fiber, characterized in that the vapor-grown carbon fiber has an average fiber outer diameter exceeding 100 nm and equal to or less than 150 nm; the mixing ratio of the polycarbonate resin and the vapor-grown carbon fiber is 1 to 11.2 parts by mass of the vapor-grown carbon fiber with respect to 100 parts by mass of the polycarbonate resin; and the electroconductive resin composite material has an elongation at break of 30% or more.

Description

201026777 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種導電性樹脂複合材料。 【先前技術】 包含樹腊與導電性填充料之導電性樹脂複合材料在半導 體領域、電氣設備相關領域、汽車.航空領域中被廣泛使 用,其主要目的可列舉:保護半導體零件不受靜電影響、 藉由阻斷電磁波而防止精密機器之誤動作、防止伴隨摩擦 之靜電•發熱等。作為半導體領域等中所使用之導電性樹 脂複合材料之母材樹脂,廣泛使用聚碳酸醋,其原因可列 舉為:由粒子引起之污染少、逸氣少、表面整舞以及光澤 流動性優異,曲少、回收再利用/重複使用性優 ,聚石反酸s旨具有之優異之樹脂特性。尤其自環境負荷 或成本削減方面等考慮,該優異之回收再利用/ 重複使用性被廣泛認為係有效之物性。 另一方面’作為對母材樹脂賦予導電性之方法有在樹 月旨中添加賦予離子傳導性之材料,或添加金屬微粒子、金 屬纖維、碳微粒子、碳纖維等導電性填充料之方法。其 :雷!性能、環境問題等方面考慮,使用碳系材料來賦予 導電性正逐漸成為主流。 Λ 7於為了展現必需之導電性而使用粒徑為數㈣之 :::之情形? ’必需相對於樹脂100質量份而添加4〇〜5〇 六如Γ之上述石及粒子科琴黑(Ketjen MaCk)等碳黑亦必需 々、〜15質量份’如此之複合材料化與原本之樹脂相比 142475.doc 201026777 較,會引起黏度上升•流動性下降、或硬度上升等物性變 化。結果,成為成形加玉時之模具轉印性、光澤等外觀不 良或耐衝擊性下降之原因。碳纖維於添加3Qf量份之條件 下亦可獲得體積固有電阻率為1〇2 ncm之導電性,但仍因 添加量多而導致流動性之惡化等。 近年來’作為如上所述之導電性填充料,正使用氣相成201026777 VI. Description of the Invention: [Technical Field to Be Invented] The present invention relates to a conductive resin composite material. [Prior Art] Conductive resin composite materials including tree wax and conductive filler are widely used in the field of semiconductors, electrical equipment, automotive, and aerospace, and their main purposes are to protect semiconductor components from static electricity. Prevents malfunction of precision machines and prevents static electricity and heat accompanying friction by blocking electromagnetic waves. Polycarbonate is widely used as a base resin of a conductive resin composite material used in the semiconductor field or the like, and the reason is that the particles are less polluted, have less outgassing, are excellent in surface finish, and have excellent gloss fluidity. It has excellent koji, excellent recycling and reusability, and it has excellent resin properties. Especially in terms of environmental load or cost reduction, this excellent recycling/recyclability is widely considered to be effective physical properties. On the other hand, as a method of imparting conductivity to the base material resin, a method of adding a material imparting ion conductivity or adding a conductive filler such as metal fine particles, metal fibers, carbon particles, or carbon fibers is added. Its: Ray! In terms of performance and environmental issues, the use of carbon-based materials to impart conductivity is becoming mainstream. Λ 7 In the case of using the particle size (4) ::: in order to exhibit the necessary conductivity? 'It is necessary to add 4 〇 to 5 〇 〇 〇 上述 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 〜 Compared with 142475.doc 201026777, the resin causes a change in the physical properties such as an increase in viscosity, a decrease in fluidity, and an increase in hardness. As a result, there is a cause of poor appearance such as mold transfer property and glossiness during molding and addition of jade, or a decrease in impact resistance. The carbon fiber can also obtain a conductivity having a volume specific resistivity of 1 〇 2 ncm under the condition of adding a 3Qf component, but the fluidity is deteriorated due to a large amount of addition. In recent years, as a conductive filler as described above, a gas phase is being used.

長碳纖維(vap〇r grown carbon fiber)。氣相成長碳纖維係 利用氣相法合成之微細碳纖維,基本上係包含連續之6員 環碳結構之石墨片單層或者多層地形成之管狀結構者。 又 其係纖維直徑為奈米級、長度為微米級、 且以高的縱 橫比為-特徵之導電性填充材料。已報導有,若使用該氣 相成長碳纖維,則自其高導電性而言,藉由對樹脂刚質 量份添加數質量份之該氣相成長碳纖料獲得具有所需導 電性之樹脂複合材料(專利文獻1、2)。 先前技術文獻 專利文獻 專利文獻1 :日本專利特開2006·30696〇號公報 _ 專利文獻2 .曰本專利特開2〇〇6 225648號公報 但疋,於包含聚碳酸酯與氣相成長碳纖維之導電性樹脂 複合材料中’若直至賦予良好導電性之程度為止將氣相成. 長碳纖維添加於聚碳酸酿中,與其相反,斷裂伸長率等樹· 脂複合材料之物性•成形性下降’成為使用該樹脂複合材 料㈣成目標成形物時之問題。又,氣相成長碳纖維之纖 維直彳二極細,亦有由熔融之聚碳酸酯樹脂所引起的氣相成 142475.doc 201026777 長碳纖維表面之潤濕性惡化等,從而導致氣相成長碳纖維 自成形之樹脂複合材料脫落《尤其於半導體領域中,此成 為半導體製品之故障•損壞之原因而被視為問題。即,需 要有具備良好之導電性、聚碳酸酯本來所具有之優異之成 形性等樹脂特性以及氣相成長碳纖維之低脫落性等任一者 均為充分程度之導電性樹脂複合材料。 【發明内容】 . 發明所欲解決之問題 β 本發明之目的在於提供一種不僅保持良好之導電性,並 且氣相成長碳纖維之脫落少,且與成形性相關之斷裂伸長 率得到改善之導電性樹脂複合材料。 解決問題之技術手段 本發明者們為了解決上述問題而進行潛心研究,結果發 現以下知識見解。 即,本發明之導電性樹脂複合材料係含有聚碳酸酯樹脂 ^ 以及氣相成長碳纖維者,氣相成長碳纖維之平均纖維外徑 為超過100 1^1且150 nm以下,聚碳酸酯樹脂與氣相成長碳 纖維之含量為,相對於聚碳酸酯樹脂1〇〇質量份,該氣相 成長碳纖維為^U.2質量份,並且該導電性樹脂複合材料 之斷裂伸長率為30%以上。如上所述之導電性樹脂複合材 料表現出良好之導電性,並且氣相成長碳纖維自導電性樹 脂複合材料之脫落亦少,且成形性良好。 又本發明中’氣相成長碳纖維之纖維外徑的分布之標 準偏差為25〜40 nm,較好的是3〇〜4〇 nm即可。於氣相成長 142475.doc 201026777 碳纖維之纖維外徑在如上所述之標準偏差範圍内之情形 時,使用氣相成長碳纖維之導電性樹脂複合材料之斷裂伸 長率變得良好。 又’較好的是’氣相成長碳纖維(微細碳纖維)形成三維 網狀之氣相成長碳纖維結構體,該氣相成長碳纖維結構體 係具有複數個粒狀部且纖維直徑較各個粒狀部之外徑更細 的氣相成長碳纖維自該粒狀部延伸出複數個之態樣,並且 -該粒狀部係於該氣相成長碳纖維之成長過程中形成者。 即,較好的是氣相成長碳纖維結合複數個粒狀部而形成表 〇 現出網狀結構之氣相成長碳纖維結構體。藉由具有如上所 述之立體結構,一般認為較氣相成長碳纖維之外徑更大之 粒狀部於導電性樹脂複合材料之聚碳酸酯樹脂之基質中發 揮物理性定錨效應(anchor effect),而減少氣相成長碳纖維 自導電性樹脂複合材料之脫落。 又,本發明提供一種以氣相成長碳纖維(微細碳纖維)自 導電性複合材料之脫落減少為特徵的導電性複合材料。 即,將寬度為50 mm、長度為90 mm、厚度為3 mm之導電◎ 性樹脂複合材料浸潰於超純水2000 mL中,施加47 kHz之 超音波60秒時,自表面脫落之粒徑為0.5 μιη以上之脫落物 之數量於每單位表面積中為5〇〇〇個/cm2以下。若脫落物-之數量為如上所述,例如於本發明在半導體領域中使用之 . 清形時’可抑制由脫落物引起之半導體製品之故障•損 壞》 較好的是粒狀部具有氣相成長碳纖維之平均纖維外徑之 142475.doc 201026777 1:3倍以上之平均的與圓相當之外徑。藉此,可帶來氣相 成長碳纖維相互之間的牢固結合。 較好的是使用導電性樹脂複合材料而成形之成形物的表 面電阻值為1〇Μ〇12 Ω/□。若使用具有如上所述之表面電 阻值的成形物,可保護精密半導體零件不受靜電之破壞。 更好的是導電性樹脂複合材料之斷裂伸長率為40%以上 '(進而好的是观以上)。藉此,使用導電性樹脂複合材料 . 來射出成形等製造成形物時的成形性可進一步提高。 β Λ相成長碳纖維係包含平均纖維外徑為超過5 nm且⑽ nm以下之氣相成長碳纖維a與平均纖維外徑為超過 且200 nm以下之氣相成長碳纖維B的混合物較好的是該 混合物中之氣相成長碳纖維B之質量大於氣相成長碳纖維 A之質量。藉此,變得容易滿足上述之平均纖維外徑與纖 維外徑分布之標準偏差範圍,導電性樹脂複合材料之斷裂 伸長率變得更良好。 φ 再者,導電性樹脂複合材料可將聚碳酸酯樹脂與氣相成 長碳纖維(微細碳纖維)於該聚碳酸酯樹脂之熔融點以上之 溫度條件下加以混練而製造。 發明之效果 依據本發明,可提供一種不僅保持良好之導電性,並且 • 氣相成長碳纖維之脫落少,且與成形性相關之斷裂伸長率 得到改善之導電性樹脂複合材料。 【實施方式】 '以下’基於較好之實施形態對本發明進行詳細說明。 142475.doc 201026777 本發明中用作導電性樹脂複合材料之母材的聚碳酸酯樹 脂係藉由使各種二經基二芳基化合物與光氣進行反應之光 氣法、或者使二羥基二芳基化合物與碳酸二苯基酯等碳酸 酷進行反應之酯交換法而獲得之聚合物,作為代表性者, 可列舉由2,2-雙(4-羥基苯基)丙烷(雙酚A)製造之聚碳酸酯 樹脂。 作為上述二羥基二芳基化合物,除雙酚A以外,可列· 舉:如雙(4-羥基苯基)甲烷、M-雙(4_羥基苯基)乙烷、 2,2-雙(4-羥基苯基)丁烷、2,2-雙(4_羥基苯基)辛烷、雙& 〇 羥基苯基)苯基甲烷、2,2_雙(4_羥基苯基_3甲基苯基)丙 烷、雙(4-羥基-3-第三丁基苯基)丙烷、22_雙(4_羥基_ 3-溴苯基)丙烷、2,2_雙(4·羥基_3,5_二溴苯基)丙烷、2:雙 (4-羥基-3,5_二氣苯基)丙烷等的雙(羥基芳基)烷烴類,如 ι,ι-雙(4-經基苯基)環纽、基苯基)環己烷等 的雙(羥基芳基)環烷烴類,如4,4,_二羥基二苯基醚、4,4,_ 二羥基-3,3’-二甲基二苯基醚等的二羥基二芳基醚類,如 4’4-二羥基二苯基硫醚等的二羥基二芳基硫醚類,如φ n笨基亞m經基_3,3f_二甲基二苯基亞喊等 的二經基二芳基亞礙類,如二m基二笨基職、4,4,_二 羥基-3,3 甲基二苯基砜等的二羥基二芳基颯類等。 該等可單獨或者混合2種以上使用,進而,亦可將上述. -备基二芳基化合物與如以下所示之3價以上之紛化合物 混合使用。 作為3價以上之酚 了列舉.間苯三紛、4,6 _二甲基 142475.doc 201026777 2,4,6-二-(4-經基苯基)-庚埽、4,6_二甲基_2,4,6_三-㈠-經基 苯基)-庚烷、1,3,5-三-(4-羥基苯基)_苯、Μ1三_(4_羥基 苯基)-乙烷以及2,2-雙-[4,4-(4,4,-二羥基聯苯基)環己基]-丙 烷等。 聚碳酸酯樹脂之黏度平均分子量通常為1〇〇〇〇〜1〇〇〇〇〇, 較好的是15000〜35000,進而好的是17〇〇〇〜28〇〇〇。 本發明中所使用之氣相成長碳纖維較好的是平均纖維外 • 徑為超過1〇〇 -"且150 以下,更好的是1〇5 nm〜145 ❹ nm,進而好的是⑽邮〜14〇 nm。錢相成長碳纖維之平 均纖維外徑為100 nm以下,則包含該氣相成長碳纖維與聚 碳酸酯樹脂之導電性樹脂複合材料的斷裂伸長率為3〇%以 下,從而’使用該樹脂複合材料來射出成形等製造成形物 時的成形性下降。-般認為其原因.在於,由於平均纖維外 徑為100 nm以下之氣相成長碳纖維與平均纖維外徑超過 謂⑽之氣相成長碳纖維相崎,向母材樹脂中添加相同 ❹ f量份之情形時的碳纖維之根數變多,故而阻礙導電性樹 脂複合材料之斷裂伸長率。另一方面,若平均纖維外徑超 過⑽⑽,則樹脂複合材料每單位體積之氣相成長碳纖維 之根數變得極少’因此少量添加時導電路徑變得難以形 成,無法獲得導電性良好之樹脂複合材料。 〆 . & 了測定此處所使用之平均纖維外徑,首先利用經設定 為倍率35_倍之掃描式電子顯微鏡對測定對象氣相成長 碳纖維,隨機攝影至少3視野以上。然後,對各攝影視^ 中可測定之纖維外徑全部進行測定,以使纖維外徑之測定 142475.doc 201026777 點數合計超過50點’對其進行數量平均即可。本發明之導 電性樹脂複合材料中所使用之氣相成長碳纖維在該方法之 每1視野中’可測定約20〜50點之纖維外徑。再者,於包含 粒狀部之氣相成長碳纖維結構體中的氣相成長碳纖維之情 形時,並非以該結構體中之粒狀部,而是以氣相成長碳纖 維之外徑來作為上述纖維外徑。 氣相成長碳纖維之纖維外徑的分布之標準偏差較好的是 -25〜40nm,更好的是3〇〜4〇nm。使用標準偏差為25〜4〇nm 之氣相成長碳纖維的導電性樹脂複合材料,一般表現出 ◎ 30%以上之斷裂伸長率,若使用標準偏差為3〇〜4〇 之氣 相成長碳纖維’則一般表現出5〇%以上之斷裂伸長率。一 般認為其原因在於,後述呈三維網狀結構體之氣相成長碳 纖維中,處於該標準偏差範圍中所規定之纖維外徑之分佈 範圍中的粗纖維外徑之氣相成長碳纖維與細纖維外徑之氣 相成長碳纖維,對使用該氣相成長碳纖維之導電性樹脂複 合材料之斷裂伸長率施加互補之效果。 又’較好的是氣相成長碳纖維形成與複數個粒狀部結合© 之網狀結構之氣相成長碳纖維結構體。如上所述之結構 中,複數個粒狀部相互之間以複數個氣相成長碳 纖維相互 立體地結合’因此並非平面之分支結構,而是具有三維擴- 展0 又,粒狀部係於氣相成長碳纖維之成長過程中形成者。 因此,複數個粒狀部與氣相成長碳纖維並非藉由結著劑等 (匕括兔物質者)之僅於外觀上連接,而是兩者部分性共有 142475.doc -10- 201026777 相同之多層結構之石墨片。藉此,粒狀部與氣相成長碳纖 維牛固結合。 對於更牢固之結合而言較為理想之粒狀部之平均的與圓 相S之外徑為氣相成長碳纖維之平均纖維外徑之1,3倍以 上,更好的是1.5倍以上且5倍以下。堅固之氣相成長碳纖 維藉由如此牢固之結合而形成為網狀的氣相成長碳纖維結 構體,即使藉由混練等而添加於聚碳酸酯令,其結構體亦Vap〇r grown carbon fiber. The vapor-grown carbon fiber is a fine carbon fiber synthesized by a vapor phase method, and is basically a tubular structure in which a graphite sheet of a continuous 6-membered ring carbon structure is formed in a single layer or a plurality of layers. Further, it is a conductive filler having a fiber diameter of a nanometer order, a length of micrometers, and a high aspect ratio. It has been reported that, when the vapor-grown carbon fiber is used, a resin composite material having a desired conductivity can be obtained by adding a few parts by mass of the vapor-grown carbon fiber to a part by mass of the resin from the viewpoint of high conductivity ( Patent Documents 1, 2). PRIOR ART DOCUMENT PATENT DOCUMENT Patent Document 1: Japanese Patent Laid-Open Publication No. Hei. No. Hei. No. Hei. No. Hei. No. 2, 225, 648. In the conductive resin composite material, the gas phase is formed until the degree of good conductivity is imparted. The long carbon fiber is added to the polycarbonate, and the physical properties and the formability of the resin composite material such as the elongation at break are decreased. The problem when the resin composite material (4) is used to form a target molded article. Moreover, the fibers of the vapor-grown carbon fiber are directly thinner than the two-pole, and the vapor phase of the molten carbon resin is 142475.doc 201026777. The wettability of the surface of the long carbon fiber is deteriorated, thereby causing self-forming of the vapor-grown carbon fiber. The resin composite material is detached. Especially in the field of semiconductors, this is considered to be a cause of failure or damage of semiconductor products. In other words, it is necessary to have a conductive resin composite material having a sufficient electrical conductivity, a resin property such as excellent formability of polycarbonate, and a low exfoliation property of a vapor-grown carbon fiber. DISCLOSURE OF THE INVENTION PROBLEM TO BE SOLVED BY THE INVENTION The object of the present invention is to provide a conductive resin which not only maintains good electrical conductivity, but also has less peeling of vapor-grown carbon fibers and improved elongation at break associated with formability. Composite material. Means for Solving the Problems The present inventors conducted intensive studies to solve the above problems, and as a result, found the following knowledge. That is, the conductive resin composite material of the present invention contains a polycarbonate resin and a vapor-grown carbon fiber, and the average fiber outer diameter of the vapor-grown carbon fiber is more than 100 1^1 and 150 nm or less, and the polycarbonate resin and gas are used. The content of the phase-growth carbon fiber is 2 parts by mass based on 1 part by mass of the polycarbonate resin, and the elongation at break of the conductive resin composite material is 30% or more. The conductive resin composite material as described above exhibits good electrical conductivity, and the vapor-grown carbon fibers are less likely to fall off from the conductive resin composite material and have good moldability. Further, in the present invention, the standard deviation of the distribution of the outer diameter of the fiber of the vapor-grown carbon fiber is 25 to 40 nm, preferably 3 to 4 〇 nm. Growth in the vapor phase 142475.doc 201026777 When the outer diameter of the carbon fiber is within the standard deviation range as described above, the elongation at break of the conductive resin composite using the vapor-grown carbon fiber becomes good. Further, it is preferred that the vapor-grown carbon fiber (fine carbon fiber) forms a three-dimensional network of vapor-phase-grown carbon fiber structures having a plurality of granular portions and having a fiber diameter smaller than each of the granular portions. The gas-growth carbon fiber having a finer diameter extends from the granular portion to a plurality of forms, and the granular portion is formed during the growth of the vapor-grown carbon fiber. That is, it is preferred that the vapor-grown carbon fiber is bonded to a plurality of granular portions to form a vapor-grown carbon fiber structure having a mesh structure. By having the three-dimensional structure as described above, it is considered that the granule portion having a larger outer diameter than the vapor-grown carbon fiber exhibits a physical anchor effect in the matrix of the polycarbonate resin of the conductive resin composite material. And reducing the shedding of the vapor-grown carbon fiber from the conductive resin composite. Further, the present invention provides a conductive composite material characterized by a reduction in the fall-off of a vapor-grown carbon fiber (fine carbon fiber) from a conductive composite material. That is, a conductive ○ resin composite material having a width of 50 mm, a length of 90 mm, and a thickness of 3 mm was immersed in 2000 mL of ultrapure water, and when the ultrasonic wave of 47 kHz was applied for 60 seconds, the particle size peeled off from the surface. The amount of the detachment of 0.5 μm or more is 5 Å/cm 2 or less per unit surface area. If the amount of the detachment is as described above, for example, it is used in the field of semiconductors of the present invention. When the shape is clear, it can suppress the failure or damage of the semiconductor article caused by the detachment. The average fiber outer diameter of the growing carbon fiber is 142475.doc 201026777 1:3 times the average outer diameter equivalent to the circle. Thereby, a strong bond between the vapor-grown carbon fibers can be brought about. It is preferred that the molded article formed by using the conductive resin composite material has a surface resistance value of 1 〇Μ〇 12 Ω / □. If a molded article having the surface resistance value as described above is used, the precision semiconductor component can be protected from static electricity. More preferably, the elongation at break of the conductive resin composite material is 40% or more '(further, it is above). By using the conductive resin composite material, the moldability at the time of producing a molded article such as injection molding can be further improved. The β-phase-growth carbon fiber is a mixture of a vapor-grown carbon fiber a having an average fiber outer diameter of more than 5 nm and less than (10) nm and a vapor-grown carbon fiber B having an average fiber outer diameter of more than 200 nm and less. The mass of the vapor-grown carbon fiber B in the middle is greater than the mass of the vapor-grown carbon fiber A. Thereby, the standard deviation range of the average fiber outer diameter and the fiber outer diameter distribution described above is easily satisfied, and the elongation at break of the conductive resin composite material is further improved. φ Further, the conductive resin composite material can be produced by kneading a polycarbonate resin and a vapor-formed long carbon fiber (fine carbon fiber) at a temperature equal to or higher than the melting point of the polycarbonate resin. Advantageous Effects of Invention According to the present invention, it is possible to provide a conductive resin composite material which not only maintains good electrical conductivity, but also has less detachment of vapor-grown carbon fibers and improved elongation at break in terms of formability. [Embodiment] The present invention will be described in detail based on preferred embodiments. 142475.doc 201026777 The polycarbonate resin used as a base material of the conductive resin composite material in the present invention is a phosgene method in which various dimercaptodiaryl compounds are reacted with phosgene, or dihydroxydiaryl A polymer obtained by a transesterification method in which a base compound and a diphenyl carbonate are reacted with carbonic acid, and a representative product is exemplified by 2,2-bis(4-hydroxyphenyl)propane (bisphenol A). Polycarbonate resin. As the above dihydroxydiaryl compound, in addition to bisphenol A, there may be mentioned, for example, bis(4-hydroxyphenyl)methane, M-bis(4-hydroxyphenyl)ethane, 2,2-dual ( 4-hydroxyphenyl)butane, 2,2-bis(4-hydroxyphenyl)octane, bis & hydroxyphenyl)phenylmethane, 2,2-bis(4-hydroxyphenyl-3) Phenyl)propane, bis(4-hydroxy-3-tert-butylphenyl)propane, 22-bis(4-hydroxy-3-bromophenyl)propane, 2,2_bis(4.hydroxy-3) a bis(hydroxyaryl)alkane such as ι, i-bis (4-carbyl) such as 5_dibromophenyl)propane or 2:bis(4-hydroxy-3,5-diphenyl)propane. Bis(hydroxyaryl)cycloalkanes such as phenyl)cyclohexyl, phenyl)cyclohexane, such as 4,4,-dihydroxydiphenyl ether, 4,4,-dihydroxy-3,3' a dihydroxydiaryl ether such as dimethyl diphenyl ether, such as a dihydroxy diaryl sulfide such as 4'4-dihydroxydiphenyl sulfide, such as φ n phenyl _3,3f_Dimethyldiphenyl ylide and the like di-diyldiaryl sub-organisms, such as di-m-di-diphenyl, 4,4,-dihydroxy-3,3-methyldiphenyl Dihydroxy diaryl hydrazines such as sulfone . These may be used singly or in combination of two or more kinds. Further, the above-mentioned -diyldiaryl compound may be used in combination with a trivalent or higher compound as shown below. As a phenol with a valence of 3 or more, it is exemplified. Benzene tris, 4,6 dimethyl 142475.doc 201026777 2,4,6-di-(4-pyridylphenyl)-glyoxime, 4,6_2 Methyl-2,4,6-tri-(mono)-p-phenylphenyl)-heptane, 1,3,5-tris-(4-hydroxyphenyl)-benzene, hydrazine-1 tris-(4-hydroxyphenyl) - Ethane and 2,2-bis-[4,4-(4,4,-dihydroxybiphenyl)cyclohexyl]-propane, and the like. The viscosity average molecular weight of the polycarbonate resin is usually from 1 Torr to 1 Torr, preferably from 15,000 to 35,000, and further preferably from 17 Å to 28 Å. The vapor-grown carbon fiber used in the present invention preferably has an average fiber outer diameter of more than 1 〇〇 - " and 150 or less, more preferably 1 〇 5 nm to 145 ❹ nm, and further preferably (10) ~14〇nm. When the average fiber outer diameter of the carbon phase growth carbon fiber is 100 nm or less, the elongation at break of the conductive resin composite material containing the vapor-grown carbon fiber and the polycarbonate resin is not less than 3% by weight, thereby using the resin composite material. The moldability at the time of producing a molded article such as injection molding is lowered. The reason is that the same ❹ f amount is added to the base resin because the vapor-grown carbon fiber having an average fiber outer diameter of 100 nm or less and the average fiber outer diameter exceeds the vapor-phase growth carbon fiber of the above (10). When the number of carbon fibers is increased, the elongation at break of the conductive resin composite is inhibited. On the other hand, when the average fiber outer diameter exceeds (10) (10), the number of vapor-grown carbon fibers per unit volume of the resin composite material becomes extremely small. Therefore, the conductive path becomes difficult to form when a small amount is added, and a resin composite having good conductivity cannot be obtained. material. In the measurement of the average fiber outer diameter used here, the gas-phase-grown carbon fiber to be measured is firstly scanned by a scanning electron microscope set to a magnification of 35 times, and at least three fields of view are randomly photographed. Then, all of the outer diameters of the fibers measurable in each of the photographic images were measured so that the measurement of the outer diameter of the fibers 142475.doc 201026777 points totaled more than 50 points'. The vapor-grown carbon fiber used in the conductive resin composite of the present invention can measure the fiber outer diameter of about 20 to 50 points in each field of view of the method. Further, in the case of a vapor-grown carbon fiber in a vapor-phase-grown carbon fiber structure including a granular portion, the outer diameter of the vapor-grown carbon fiber is not used as the fiber in the structure. Outer diameter. The standard deviation of the distribution of the outer diameter of the fiber of the vapor-grown carbon fiber is preferably -25 to 40 nm, more preferably 3 to 4 〇 nm. A conductive resin composite material using a vapor-grown carbon fiber having a standard deviation of 25 to 4 〇 nm generally exhibits an elongation at break of 30% or more, and a vapor-phase growth carbon fiber having a standard deviation of 3 〇 to 4 Å is used. It generally exhibits an elongation at break of more than 5%. It is considered that the reason is that, in the vapor-grown carbon fiber which is a three-dimensional network structure described later, the outer diameter of the coarse fiber in the distribution range of the outer diameter of the fiber specified in the standard deviation range is vapor-grown carbon fiber and fine fiber. The vapor-grown carbon fiber of the diameter exerts a complementary effect on the elongation at break of the conductive resin composite material using the vapor-grown carbon fiber. Further, it is preferred that the vapor-grown carbon fibers form a vapor-phase-growth carbon fiber structure having a network structure in which a plurality of granular portions are combined. In the structure as described above, the plurality of granular portions are sterically joined to each other by a plurality of vapor-phase-growth carbon fibers. Therefore, it is not a planar branch structure, but has a three-dimensional expansion and expansion, and the granular portion is attached to the gas. The formation of phase-growth carbon fiber is formed during the growth process. Therefore, the plurality of granular portions and the vapor-grown carbon fibers are not connected by appearance only by a binding agent or the like (including a rabbit substance), but the two parts are partially 142475.doc -10- 201026777 Structure of graphite sheet. Thereby, the granular portion is combined with the vapor-grown carbon fiber. The outer diameter of the granules and the outer diameter of the circular phase S which are more desirable for a stronger bond are 1,3 times or more, more preferably 1.5 times or more and 5 times the average fiber outer diameter of the vapor-grown carbon fibers. the following. Sturdy vapor-grown carbon fiber The vapor-phase-growth carbon fiber structure formed into a network by such a strong combination, even if it is added to the polycarbonate by kneading, etc., the structure is also

侍以保持。一般認為如上所述之網狀結構於導電性樹脂複 合材料之聚碳酸酯樹脂之基質中發揮物理性定錨效應,因 而如後文所述使該氣相成長碳纖維自該導電性樹脂複合材 料之脫落減少。 =者’本說明書中所謂之「粒狀部之平均的與圓相當之 外徑」’係指測定經觀察之粒狀部之面積,作為—個正圓 而求出直徑的值。具體而言,係以電子顯微鏡對氣相成長 钱維相互之結合點即粒狀部之外形進行攝影,在該攝影 圖像::、使用適當之圖像分析軟件,例如winR〇〇f(商品 :’二谷商事股份有限公司製造)來描出各粒狀部之輪 =出=内之面積,基於該面積而計算出各粒狀部: /、圓相备之直徑,並加以平均而得者。 平2的i述氣相成長碳纖維結構體較理想的是面積基準之 之平均的Γ相當之直徑為2G〜1GG帥。此處所謂面積基準 ”與之直徑’係指使用電子顯微鏡等對 上結構體之外形進行攝影’在該攝影圖像中,、盘 使用適當之圖像分析軟件來描出各氣相成長碳 142475.doc 201026777 纖u冓體之輪廓,求出輪廊内之面積,計算出各纖維結 構體之與圓相當之直徑,並將其平均化而得者。該平均的 與圓相當之直徑係成為判斷經調配於聚碳酸酯樹脂之基質 中時的該氣相成長碳纖維結構體之纖維長度的要因。概括 而σ s平均的與圓相當之直徑小於2〇 _,則纖維長度 短,有使用其之樹脂複合材料無法獲得良好導電性之虞, 另-方面’若為超過100 _者,則有例如藉由混練等而調 ❿ 配入樹脂基質中時會產生較大之黏度上升,混合分散困難 或者成形性劣化之虞。 進而,上述氣相成長碳纖維結構體具有氣相成長碳纖維 疏鬆存在之蓬鬆結構,具體而言,較好的是其鬆密度為 0.001〜0.05 g/cm3者,更好的是〇 〇〇1〜〇 〇2 g/⑽3者。若 鬆密度超過0.05 g/cm3者,% ^彳| g # * m ⑴隻得難以糟由少量添加來改 善^碳酸醋樹脂之物性。另一方面,若為鬆密度小於 請l g/Cm3者,則所用量之氣相成長碳纖維之體積過度變 ❹ :作ΓΓ碳酸醋樹脂混合而製備複合材料時變得難以 刼作4,對操作性產生不良影響。 又’上述氣相成長碳纖維結構體由於粒 分性共有相同之多層結構之石墨片::= 二電特性等亦係非常優異者。作為本發明中所使用 者’例如較好的是在-^壓、缩密度G8 g/e 電阻值為〇._〜0·025 Q.cm以下者 n、J疋之粉末 Q.cm。更好的疋 0.005〜0.020 Ω,者右貝:J末電阻值超過°.025 者或小於〇.〇。5 ⑽者’則與聚她旨樹脂進行複合材料化時,變得難 142475.doc 12 201026777 以製造可保持所需導電性之複合材料。 又’自欲賦予上述氣相成長碳纖維結構體較高之強度以 及導電性之觀點而言’較理想的是構成氣相成長碳纖維之 石墨片中之缺陷少。具體而言,例如較好的是利用拉曼光 譜分析法(Raman spectroscopic analysis)測定之 id/Ig 比為 0.2以下,更好的是0.1以下。拉曼光譜分析中,充分大之 單結晶石墨僅出現1580 cm-1附近之波蜂(G譜帶)。由於結 * 晶為有限之微小尺寸或由於晶格缺陷,而於1360 cm·1附近 β 出現波峰(D譜帶)。因此,若D譜帶與G譜帶之強度比 (R = Il36〇/Il 580 = ID/IG)如上所述之特定值以下,貝,j表示石墨 片中之缺陷量少。 再者,此處所謂之缺陷,係指由於在構成氣相成長碳纖 維之石墨片之排列中侵入碳原子以外之不要原子、或者必 要之碳原子缺損、又或者產生偏移而產生的石墨片之排列 之不完全部分(晶格缺陷(lattice defect))等。 φ 又,如上所述之包含聚碳酸酯以及氣相成長碳纖維之本 申請案發明之導電性樹脂複合材料的斷裂伸長率較好的是 观以上,更好的是以上。若斷裂伸長率為3〇%以 • 下,則衝擊強度以及對拉伸之物性(黏著強度)下降,因此 將此種導電性樹脂複合材料成形時形成較脆之成形物。 ./吏用如上所述之導電性樹脂複合材料而成形之成形物, 右其表面電阻值為1〇M〇丨2 Ω/□,更好的是1〇6〜1〇]2 Ω/ϋ, S適合於用以保護精密半導體零件不受靜電破壞之零件容 、製造現場之地板材料等。尤其適合用於載帶等1€ I42475.doc -13- 201026777 (integrated circuit,積體雷,々、兩从 ^ ^ 積體電路)令件包裝體或磁頭之搬详田 托盤。其原因在於,自帶電之頁之搬送用 油 _ θ 电于零件上不會引起靜電短 路,而疋於該容器側緩慢地& 1Λ6 〇/π ㈣除去。於容器之電阻值小於 10 Ω/□之情形時,所蓄 、 ,φ a Α 靜電心'遽移動至該容器而產 生放電現象’由此導致精密半導體零件短路。另一方面, 於:子零件容器之表面電阻值大於!⑺㈣之情形時,表 面生之靜電難以浪漏,亦對該零件造成不良影響。 具有上述特徵之氣相成長碳纖維結構體並非特別限定 者’例如可以如下方式調製。 基本上,係以過渡金屬超微粒子相媒,將烴等有機化 合物以CVD法(ehemieal ν_ d—“,化學氣相沈積 法)進订化學熱分解而獲得纖維結構體(以下稱為中間體), 對其進一步進行高溫熱處理。 作為原料有機化合物,可使用:苯、曱苯、二甲苯等 烴’-氧化碳(C0),乙醇等醇類等。並無特別限定,但為 了獲得本發明之纖維結構體,較好的是使用分解溫度不同 之至少2種以上之碳化合物作為碳源。再者,本說明書中❿ 所述之「至少2種以上之竣化合物」,並非係指必需使用2 種以上者作為原料有機化合物者。其係指亦包括如下態樣 者:於原料有機化合物使用i種者之情形時,於中間體之-合成反應過程中,例如產生如曱苯或二甲苯之加氫脫烷基· 化(hydrodealkylation)等的反應,而於其後之熱分解反應系 統中形成分解溫度不同之2種以上之碳化合物。 .再者,熱分解反應系統中如上所述使2種以上之碳化合 142475.doc -14· 201026777 物存在作為碳源之情形時,各碳化合物之分解溫度不僅根 據碳化合物之種類而變動,亦根據原料氣體中之各碳化合 物之氣體分壓或莫耳比而變動。因此,可藉由調整原料氣 體中之2種以上碳化合物之組成比,而使用比較多之組合 來作為碳化合物。 例如可自以下化合物中選擇2種以上:甲烧、乙院、丙 烧類、丁烧類、戊烧類、己燒類、庚燒類、環丙烧、環己 烧等烷烴或環烷烴’尤其是碳數W左右之烷烴;乙烯、 丙烯、丁烯類、戊烯類、庚烯類、環戊烯等烯烴或環烯 煙,尤其是碳數卜7左右之稀烴;乙快、丙块等快煙,尤 其是碳數1〜7左右之炔烴;苯、甲苯、苯乙烯、二甲苯、 秦、甲基萘、節、菲等芳香族或雜環芳香族烴,尤其是碳 數6〜18左右之芳香族或雜環芳香族烴;甲醇、乙醇等醇 類’尤其是碳數卜7左右之醇類;此外,一氧化碳、_ 類、賴等。為了將所選擇之2種以上之碳化合物組合使 用,調整氣體分屋以便可於所需之熱分解反應溫度區域發 揮不同之刀解級度’或者調整特定溫度區域中之滯留時間 I3可®此,藉由使2種以上之碳化合物之混合比最佳 化’可高效率地製造中間體。 如上所述之2種以上碳化合物之組合中,例如於甲烷與 苯之組合中’較好的是甲燒/苯之莫耳比設為卜帽,更好 的疋1-1 200 ’進而好的是3〜1〇〇。再者該值為反應爐之 二口處的氣體組成比’例如於使用甲苯作為碳源之一之情 形時,考慮到反應爐内甲苯1〇〇%分解而以i : i生成甲燒 142475.doc 15· 201026777 及苯,另行供給不足部分之甲烷即可。例如於將甲烷/苯 之莫耳比設為3之情形時,相對於甲苯丨莫耳,添加甲烷2 莫耳即可。再者,作為如上所述之對甲苯添加之甲烷,未 必僅利用另行準備新鮮之甲烷的方法來使用,亦可將自該 反應爐中排出之排氣中所含的未反應之甲烷循環使用。 藉由設為上述範圍内之組成比,可獲得具有氣相成長碳 ,纖維以及粒狀部中任一去的古八益_、去—_ τ仕耆均充为發達之二維網狀結構的中 間體。 未必力以限足,但作為控制纖維外徑之粗細度之要 因可歹J舉原料中之煙化合物濃度、原料中之煙化合物與 觸媒金屬之濃度比率、反應爐内之滞留時間等。 因此’為了使氣相成長碳纖維之外徑變粗,例如提高原 料中之烴化合物之澧唐 了 又’原料中之烴化合物與觸 媒金屬之濃度比率係視使外私総如* < — 优便外仫變粗之程度,於烴化合物與 觸媒金屬之莫耳比中,可箱料担古嫌 』相微鐽两觸媒金屬之莫耳比。化 學氣相沈積法(CVD法)中,為Ύ丨、,w 為了以觸媒金屬為核而使氣相 成長碳纖維成長,較理想的县你纪 量 想的是使所使用之金屬觸媒亦增 氫 再者,環境氣體中,可使用氯1、氣等惰性氣體或 又’作為觸媒’係使用鐵、鍅 結、鉬等過渡金屬或者二茂 鐵、醋酸金屬鹽等過渡金屬化 。物與硫或者噻吩、硫化鐵 專硫化合物的混合物。 中間體之合成可使用通常所 叮進仃的烴等之CVD法。使成 142475.doc -16· 201026777 為特定調配比之原料之烴及觸媒之混合液蒸發,將氫氣等 作為載氣而導入反應爐内,於800〜1300°C之溫度下進行熱 分解。藉此,合成複數個中間體集合而成之數厘米至數十 厘米大小之集合體,上述中間體具有平均纖維外徑為 100〜300 nm之纖維且相互之間藉由如上述觸媒之粒子作為 核來成長之粒狀體而結合的疏鬆之三維結構。 作為包含上述反應爐之製造裝置,並無特別限定,例如 可例示具有圖1所示之結構的製造裝置。圖中所示之製造 裝置1係使原料蒸發’將氣化之原料與載氣混合,將該原 料混合氣體導入至反應爐8之内部,於反應爐8内製造氣相 成長碳纖維之集合體者。製造裝置丨具備填充有原料之原 料槽2、進行原料之搬送以及向反應爐8内之導入的填充有 載氣之氣體槽4,該等原料槽2以及氣體槽4經由原料導入 管3以及氣體導入管5而分別連接於蒸發器6。進而,蒸發 器ό係經由原料混合氣體導入管7而連接於反應爐8。而 且’製造氣相成長碳纖維之反應爐8内部形成為圓筒狀, 於成為其轴心方向之一端的上端,具備使搬送而來之原料 混合氣體導入至反應爐8内部的導入喷嘴9。又,於反應爐 8之外周部設置有加熱器作為加熱機構11,自反應爐8之外 周部加熱反應爐8之内部。而且,於反應爐8之成為軸心方 向之他端的下端側,連接有將所製造之氣相成長碳纖維儲 備而回收之氣相成長碳纖維回收器12。該氣相成長碳纖維 回收器12上連接有排出氣體之氣體排出管13。 成為原料之烴的熱分解反應主要於觸媒粒子或者以其為 142475.doc -17· 201026777 核而成長之粒狀體表面上發生。因分解而產生之碳之再社 晶化係利用該觸媒粒子或粒狀體而在一定方向上進行者, 藉此成長為纖維狀。然而,為了獲得本發明之氣相成長碳 纖維結構體m上所述之熱分解速度與成長速度之平 衡有意地變化。例如藉由如上所述,使用分解溫度不同之 至少2種以上之碳化合物作為碳源,則並非僅於一維方向 上使碳物質成長’而是以粒狀體為中心使碳物質三維地成 長曰然,此種二維之氣相成長碳纖維之成長並非僅依賴 於熱分解速度與成長速度之平衡者,亦受到觸媒粒子之結 晶面選擇性、反應爐内之滯留時間、爐内溫度分布等的影 響。又,上述熱分解反應與成長速度之平衡不僅受上述碳 源之種類的影響,亦受反應溫度以及氣體溫度等的影響。 概括而言,若成長速度快於熱分解速度,則碳物質沿著纖 維狀而成長,另一方面,若熱分解速度快於成長速度,則 碳物質沿著觸媒粒子之周面方向而成長。因此,藉由控制 熱分解速度與成長速度之平衡,使其有意地變化,可使碳 物質之成長方向不為一定方向而為多方向,從而形成三維 結構。再者,較理想的是使觸媒等之組成、反應爐内之滯 留時間、反應溫度、以及氣體溫度等最佳化,以便使所生 成之中間體中容易形成包含粒狀部與氣相成長碳纖維之三 維結構。 再者’作為高效率地製造中間體之方法,除了以最佳之 混合比使用如上所述之分解溫度不同之2種以上碳化合物 的方法以外’可列舉使供給至反應爐中之原料氣體在其供 142475.doc -18 - 201026777 ^ 口附近產生亂流的方法。此處所謂之亂流,係指激烈紊 亂之氣流,指呈旋渦狀流動之氣流。 反應爐中,原料氣體自該供給口導入反應爐内後,立即 藉由原料混合氣體中作為觸媒之過渡金屬化合物之分解而 形成金屬觸媒微粒子。此係經過如下階段而達成。即,首 先過渡金屬化合物經分解而成為金屬原子,繼而,藉由複 數個例如約100原子左右之金屬原子的碰撞而生成團簇 • (cluster)。於該所生成之團簇的階段,不發揮作為中間體 ® 之觸媒的作用,所生成之團簇藉由相互之間碰撞而更進一 步集合’成長為約3 nm〜10 nm左右之金屬之結晶性粒子, 被用作中間體之製造用金屬觸媒微粒子。 於该觸媒形成過程中,若如上所述存在由激烈之亂流引 起之渦流,則可能進行比僅作布朗運動之金屬原子或者團 簇相互之間的碰撞更激烈之碰撞。藉此,隨著每單位時間 之碰撞次數之增加,短時間内以高產率獲得金屬觸媒微粒 ❸ 子’又’因渦流而使濃度、溫度等均勻化,藉此可獲得粒 子之尺寸一致的金屬觸媒微粒子。進而,於形成金屬觸媒 微粒子之過程中,藉由因渦流而引起之激烈碰撞,形成金 屬之結晶性粒子大量集合而成的金屬觸媒微粒子之集合 體。如此,金屬觸媒微粒子快速生成,碳化合物之分解反 ' 應區域即金屬觸媒表面之面積變大。因此,促進碳化合物 之分解,從而充分供給碳物質,以上述集合體之各自之金 屬觸媒微粒子為核,氣相成長碳纖維呈放射狀地成長。另 一方面,若如上所述一部分礙化合物之熱分解速度快於碳 142475.doc -19- 201026777 物質之成長速度,則碳物質亦於觸媒粒子之周面方向成 長,於上述集合體之周圍形成粒狀部,高 所需三維結構之中間雜。再者,—般認為上 粒子之集合體中亦包括-部分活性低於其他觸媒微粒子或 者在反應途中失去活性之觸媒微粒子。一般亦認為於凝集 為集合體之前在上述觸媒微粒子之表面成長、或者於形成 集合體之後以上述觸媒微粒子為核進行成長而成之非纖維 狀或者極短之纖維狀碳物質,藉由存在於集合體之周緣位 置而形成前驅物之粒狀部。 因此,粒狀部包含複數個氣相成長碳纖維之端部、與僅 於周面方向使碳物質成長的金屬觸媒微粒子,並且,較多 形成複數個球體狀結構物之集合•集積態樣,而非單純I 球形。在如此狀態下使碳物質之成長進一步繼續,與後述 之退火處理互起作用,從而在粒狀部集合•集積之複數個 氣相成長碳纖維之端部或複數個球狀結構物鄰接者形成· 共有連續的石墨片狀層。藉此,形成以複數個粒狀部與氣 相成長碳纖維牢固結合之三維網狀之氣相成長碳纖維結構 體。 於反應爐之原料氣體供給口附近,作為所投入之原料氣 體之溫度’較好的是350〜45(TC,作為使原料氣體之氣流 產生亂流之具體方法,並無特別限定。例如可採用:原料 氣體以旋流導入反應爐内之方法’或於可干擾自原料氣體 供給口導出至反應爐内之原料氣體之氣流的位置設置某種 碰撞部等的方法。作為上述碰撞部之形狀,並無任何限 142475.doc •20- 201026777 定,若為由於以碰撞部為起點所產生之满流而於反應爐内 形成充分之高L流者即可。例如可將各種形狀之隔板、禁、 錐管、傘狀體等單獨或者組合複數個而採用配置丨個或複 數個之形態。 於圖1所例示之製造裝置丨中,作為上述碰撞部之例子, 於導入喷嘴9周圍設有整流•緩衝板1〇。整流•緩衝板係配 置於導入喷嘴9附近,作為阻礙原料混合氣體之流通的碰 龜 #之起點而發揮作用之障礙物,可藉由該障礙物與原料混 •纟氣體碰撞而產生渦流’使溫度分布與濃度分布均勻化。 整流·緩衝板之形狀並無任何限定,若為以整流•緩衝板為 起點所產生之渦流不消失,且逐次形成至反應爐8之下端 側的形狀即可。Waiter to keep. It is considered that the network structure as described above exerts a physical anchoring effect in the matrix of the polycarbonate resin of the conductive resin composite material, and thus the vapor-grown carbon fiber is made from the conductive resin composite material as will be described later. Reduced shedding. = "In the present specification, the "outer diameter of the granular portion corresponding to the outer diameter" means the measurement of the area of the observed granular portion, and the value of the diameter is determined as a perfect circle. Specifically, an electron microscope is used to image a combination of gas phase growth and mutual energy, that is, a shape of a granular portion, and the image is: using appropriate image analysis software such as winR〇〇f (product) : 'Manufactured by Ergu Trading Co., Ltd.' to trace the area of the wheel of each granular part = out = based on this area, calculate the diameter of each granular part: /, the diameter of the circle, and average it. . It is preferable that the diameter of the gas-phase-growth carbon fiber structure of the flat surface is equal to the average diameter of the area, and the diameter is 2G to 1GG. Here, the area reference "and the diameter" means that the shape of the upper structure is photographed using an electron microscope or the like. In the photographed image, the disc is used to describe each vapor-grown carbon 142475 using appropriate image analysis software. Doc 201026777 The outline of the fiber, the area inside the wheel, the diameter of each fiber structure corresponding to the circle is calculated and averaged. The average diameter corresponding to the circle is judged. The factor of the fiber length of the vapor-grown carbon fiber structure when blended in a matrix of a polycarbonate resin. Generally, the diameter of σ s which is equivalent to a circle is less than 2 〇 _, the fiber length is short, and the use thereof is used. The resin composite material cannot obtain good conductivity, and if it is more than 100 Å, for example, it can be tempered by kneading, etc., when it is blended into a resin matrix, a large viscosity rise occurs, and mixing and dispersion are difficult or Further, the vapor-grown carbon fiber structure has a fluffy structure in which a vapor-grown carbon fiber is loosely formed, and specifically, a bulk density of 0.00 is preferable. 1~0.05 g/cm3, more preferably 〇〇〇1~〇〇2 g/(10)3. If the density is more than 0.05 g/cm3, % ^彳| g # * m (1) is only difficult to make a small amount Adding to improve the physical properties of the carbonated resin. On the other hand, if the bulk density is less than lg/Cm3, the volume of the vapor-grown carbon fiber used is excessively changed: when the composite material is prepared by mixing the carbonated vinegar resin It is difficult to make a problem 4, and it has an adverse effect on the operability. Further, the above-mentioned vapor-phase-growth carbon fiber structure is excellent in particle size, and the graphite sheet having the same multilayer structure::= the second electrical property is excellent. In the invention, for example, it is preferable that the resistance value of the G8 g/e is 〇._~0·025 Q.cm or less, and the powder Q.cm of the powder is better.疋0.005~0.020 Ω, the right shell: J resistance value exceeds °.025 or less than 〇.〇. 5 (10) 'When it is composited with poly-resin resin, it becomes difficult 142475.doc 12 201026777 Producing a composite material capable of maintaining the desired conductivity. Further, it is intended to impart a higher degree to the above-mentioned vapor-grown carbon fiber structure. From the viewpoint of the degree of conductivity and conductivity, it is preferable that the number of defects in the graphite sheet constituting the vapor-grown carbon fiber is small. Specifically, for example, id/ measured by Raman spectroscopic analysis is preferable. The Ig ratio is 0.2 or less, more preferably 0.1 or less. In Raman spectroscopy, a sufficiently large single crystal graphite exhibits only a wave bee (G band) near 1580 cm-1. Since the junction crystal is a limited small size Or due to lattice defects, a peak appears in the vicinity of 1360 cm·1 (D band). Therefore, if the intensity ratio of the D band to the G band (R = Il36 〇 / Il 580 = ID / IG) is below the specific value described above, j, j indicates that the amount of defects in the graphite sheet is small. In addition, the term "defect" as used herein refers to a graphite sheet which is produced by intrusion of carbon atoms other than carbon atoms in the arrangement of the graphite sheets constituting the vapor-phase-grown carbon fibers, or the necessary carbon atoms are missing or shifted. Incomplete part of the arrangement (lattice defect) and the like. Further, the conductive resin composite material of the present invention comprising polycarbonate and vapor-grown carbon fibers as described above preferably has an elongation at break of not less than the above, more preferably more than the above. When the elongation at break is 3% by weight or less, the impact strength and the physical properties (adhesive strength) for stretching are lowered. Therefore, when the conductive resin composite material is molded, a brittle molded product is formed. The molded article formed by using the conductive resin composite material as described above has a surface resistance value of 1 〇 M 〇丨 2 Ω / □, more preferably 1 〇 6 〜 1 〇 2 Ω / ϋ. , S is suitable for the parts of the parts used to protect the precision semiconductor parts from static electricity, the floor materials of the manufacturing site, etc. Especially suitable for carrier tapes, etc. 1€ I42475.doc -13- 201026777 (integrated circuit, integrated body, 々, two from ^ ^ integrated circuit) order package or head moving detailed tray. The reason for this is that the transfer oil _ θ from the charged page does not cause an electrostatic short circuit on the part, and is slowly removed by the side of the container & 1 Λ 6 〇 / π (4). When the resistance value of the container is less than 10 Ω/□, the stored φ a 静电 electrostatic core '遽 moves to the container to cause a discharge phenomenon', thereby causing a short circuit of the precision semiconductor component. On the other hand, the surface resistance of the sub-component container is greater than! (7) In the case of (4), the static electricity generated on the surface is difficult to leak, which also adversely affects the part. The vapor-grown carbon fiber structure having the above characteristics is not particularly limited. For example, it can be prepared as follows. Basically, a transitional metal ultrafine particle phase medium is used to chemically thermally decompose an organic compound such as a hydrocarbon by a CVD method (ehemieal ν_d-", chemical vapor deposition method to obtain a fiber structure (hereinafter referred to as an intermediate). Further, the high-temperature heat treatment is carried out. As the raw material organic compound, a hydrocarbon such as benzene, toluene or xylene, or an alcohol such as ethanol, etc., may be used, and is not particularly limited, but in order to obtain the present invention. In the fiber structure, it is preferred to use at least two or more kinds of carbon compounds having different decomposition temperatures as the carbon source. Further, "at least two or more kinds of ruthenium compounds" as described in the present specification do not mean that it is necessary to use 2 Any one of the above is a raw material organic compound. It also refers to the following aspects: in the case of the use of the organic compound in the case of the raw material, in the intermediate-synthesis reaction, for example, hydrodealkylation such as toluene or xylene is produced. In the subsequent thermal decomposition reaction system, two or more kinds of carbon compounds having different decomposition temperatures are formed. Further, in the thermal decomposition reaction system, when two or more kinds of carbon compounds 142475.doc -14·201026777 are present as a carbon source as described above, the decomposition temperature of each carbon compound varies not only according to the kind of the carbon compound, but also It also varies depending on the partial pressure of gas or the molar ratio of each carbon compound in the material gas. Therefore, by adjusting the composition ratio of two or more kinds of carbon compounds in the raw material gas, a relatively large combination can be used as the carbon compound. For example, two or more of the following compounds may be selected: acacia or naphthene such as kezhu, keyuan, propyl, butyl, pentylene, hexan, gamma, propylene, cyclohexane, etc. In particular, an alkane having a carbon number of about W; an olefin or a cycloalkene such as ethylene, propylene, butene, pentene, heptene or cyclopentene, especially a dilute hydrocarbon having a carbon number of about 7; Blocks and other fast smoke, especially alkyne with a carbon number of about 1 to 7; aromatic or heterocyclic aromatic hydrocarbons such as benzene, toluene, styrene, xylene, dimethyl, methyl naphthalene, phenanthrene, phenanthrene, etc., especially carbon number An aromatic or heterocyclic aromatic hydrocarbon of about 6 to 18; an alcohol such as methanol or ethanol, especially an alcohol having a carbon number of about 7; and carbon monoxide, _, and lanthanum. In order to use the selected two or more carbon compounds in combination, the gas partitioning is adjusted so that different degrees of knife resolution can be performed in the desired thermal decomposition reaction temperature region or the residence time I3 in the specific temperature region can be adjusted. By optimizing the mixing ratio of two or more kinds of carbon compounds, an intermediate can be efficiently produced. In the combination of two or more kinds of carbon compounds as described above, for example, in the combination of methane and benzene, it is preferable that the molar ratio of the methylate/benzene is set to be a cap, and more preferably 疋1-1 200'. It is 3~1〇〇. In addition, the value is the gas composition ratio at the two ports of the reaction furnace. For example, when using toluene as one of the carbon sources, considering the decomposition of toluene in the reactor, i: i is formed to produce 142475. Doc 15· 201026777 and benzene, you can supply less than enough methane. For example, when the methane/benzene molar ratio is set to 3, methane 2 mole may be added to toluene. Further, as the methane to be added to the toluene as described above, it is not necessary to use only a method in which fresh methane is separately prepared, and the unreacted methane contained in the exhaust gas discharged from the reaction furnace may be recycled. By setting the composition ratio within the above range, it is possible to obtain a two-dimensional network structure in which the gas-growth carbon, the fiber, and the granular portion are all developed into a developed two-dimensional _, _ _ τ 耆 耆Intermediates. It is not necessarily limited, but as a factor for controlling the thickness of the outer diameter of the fiber, the concentration of the smoke compound in the raw material, the concentration ratio of the smoke compound to the catalytic metal in the raw material, and the residence time in the reactor can be used. Therefore, in order to make the outer diameter of the vapor-grown carbon fiber thicker, for example, to increase the hydrocarbon compound in the raw material, the ratio of the concentration of the hydrocarbon compound to the catalytic metal in the raw material is such that the external privacy is such as * < The degree of thickening of the outer shell is superior to that of the molar ratio of the hydrocarbon compound to the catalytic metal, and the box material can bear the ambiguity of the two catalyst metal. In the chemical vapor deposition method (CVD method), it is Ύ丨, w, in order to grow the vapor-phase-grown carbon fiber with the catalytic metal as the core, and the ideal county is to make the metal catalyst used. In addition to hydrogen, in the ambient gas, an inert gas such as chlorine or gas or a transition metal such as iron, bismuth or molybdenum or a transition metallization such as ferrocene or a metal acetate may be used as the catalyst. a mixture of sulfur and thiophene or iron sulfide specific sulfur compounds. As the synthesis of the intermediate, a CVD method of a hydrocarbon or the like which is usually introduced can be used. 142475.doc -16· 201026777 Evaporates a mixture of a hydrocarbon and a catalyst of a specific ratio of a raw material, introduces hydrogen gas or the like into a reaction furnace as a carrier gas, and thermally decomposes at a temperature of 800 to 1300 °C. Thereby, a plurality of intermediates are assembled into a collection of several centimeters to several tens of centimeters in size, and the intermediates have fibers having an average fiber outer diameter of 100 to 300 nm and are mutually coupled by a catalyst such as the above catalyst. A loose three-dimensional structure that is combined as a granule that grows from the nucleus. The production apparatus including the above reaction furnace is not particularly limited, and for example, a production apparatus having the structure shown in Fig. 1 can be exemplified. In the manufacturing apparatus 1 shown in the drawing, the raw material is evaporated, and the vaporized raw material is mixed with a carrier gas, and the raw material mixed gas is introduced into the inside of the reaction furnace 8, and a mixture of vapor-grown carbon fibers is produced in the reaction furnace 8. . The manufacturing apparatus 丨 includes a raw material tank 2 filled with a raw material, a raw material, and a gas tank 4 filled with a carrier gas introduced into the reaction furnace 8, and the raw material tank 2 and the gas tank 4 pass through the raw material introduction pipe 3 and the gas. The introduction tube 5 is connected to the evaporator 6, respectively. Further, the evaporator crucible is connected to the reaction furnace 8 via the raw material mixed gas introduction pipe 7. Further, the inside of the reactor 8 for producing a vapor-grown carbon fiber is formed into a cylindrical shape, and an introduction nozzle 9 for introducing the raw material mixed gas to be conveyed into the inside of the reaction furnace 8 is provided at the upper end which is one end of the axial direction. Further, a heater is provided as a heating means 11 on the outer circumference of the reaction furnace 8, and the inside of the reaction furnace 8 is heated from the outer periphery of the reaction furnace 8. Further, a vapor-phase growth carbon fiber recovery unit 12 for recovering the produced vapor-phase-grown carbon fiber storage is connected to the lower end side of the other end of the reaction furnace 8 in the axial direction. A gas discharge pipe 13 for exhausting gas is connected to the vapor-phase growing carbon fiber recovery unit 12. The thermal decomposition reaction of the hydrocarbon to be a raw material occurs mainly on the surface of the granules which are grown by the catalyst particles or the nucleus which is 142475.doc -17·201026777. The crystallization of the carbon produced by the decomposition is carried out in a predetermined direction by using the catalyst particles or the granules, thereby growing into a fibrous shape. However, the balance between the thermal decomposition rate and the growth rate described in order to obtain the vapor-grown carbon fiber structure m of the present invention is intentionally changed. For example, by using at least two or more carbon compounds having different decomposition temperatures as the carbon source as described above, the carbon material is not grown only in the one-dimensional direction, but the carbon material is grown three-dimensionally around the granular body. Suddenly, the growth of such two-dimensional vapor-grown carbon fibers does not depend solely on the balance between thermal decomposition rate and growth rate, but also on the crystal face selectivity of the catalyst particles, the residence time in the reactor, and the temperature distribution in the furnace. The impact of etc. Further, the balance between the thermal decomposition reaction and the growth rate is affected not only by the type of the carbon source but also by the reaction temperature and the gas temperature. In general, if the growth rate is faster than the thermal decomposition rate, the carbon material grows along the fiber shape. On the other hand, if the thermal decomposition rate is faster than the growth rate, the carbon material grows along the circumferential direction of the catalyst particles. . Therefore, by controlling the balance between the thermal decomposition rate and the growth rate, it is intentionally changed, so that the growth direction of the carbon material is not in a certain direction and is multidirectional, thereby forming a three-dimensional structure. Further, it is preferable to optimize the composition of the catalyst or the like, the residence time in the reactor, the reaction temperature, and the gas temperature, so that the formed intermediate can be easily formed into a granular portion and a vapor phase. The three-dimensional structure of carbon fiber. In addition, as a method of efficiently producing an intermediate, in addition to the method of using two or more kinds of carbon compounds having different decomposition temperatures as described above at an optimum mixing ratio, the raw material gas supplied to the reaction furnace may be listed. It is for 142475.doc -18 - 201026777 ^ The method of generating turbulence near the mouth. The term "turbulent flow" as used herein refers to a highly turbulent airflow, which refers to a flow of a swirling flow. In the reactor, the raw material gas is introduced into the reaction furnace from the supply port, and immediately after the decomposition of the transition metal compound as a catalyst in the raw material mixed gas, metal catalyst fine particles are formed. This is achieved through the following stages. That is, the first transition metal compound is decomposed to become a metal atom, and then a cluster is formed by collision of a plurality of metal atoms of, for example, about 100 atoms. At the stage of the cluster formed, the cluster does not function as a catalyst for the intermediate®, and the resulting cluster further aggregates into a metal of about 3 nm to 10 nm by collision with each other. The crystalline particles are used as metal catalyst fine particles for the production of intermediates. In the formation of the catalyst, if there is an eddy current caused by the intense turbulent flow as described above, it is possible to perform a more intense collision with the collision of metal atoms or clusters which only perform Brownian motion. Thereby, as the number of collisions per unit time increases, the metal catalyst particles are obtained in a high yield in a short period of time, and the concentration, temperature, and the like are uniformized by the eddy current, thereby obtaining the uniform size of the particles. Metal catalyst particles. Further, in the process of forming the metal catalyst microparticles, an aggregate of metal catalyst particles formed by a large number of metallic crystal particles is formed by the intense collision caused by the eddy current. In this way, the metal catalyst particles are rapidly formed, and the decomposition of the carbon compound becomes larger, that is, the area of the surface of the metal catalyst becomes larger. Therefore, the decomposition of the carbon compound is promoted to sufficiently supply the carbonaceous material, and the metallocene microparticles of the aggregate are used as the core, and the vapor-grown carbon fiber grows radially. On the other hand, if the thermal decomposition rate of a part of the hindrance compound is faster than the growth rate of the carbon 142475.doc -19-201026777 as described above, the carbon material also grows in the circumferential direction of the catalytic particles, around the aggregate. Forming a granular portion, the middle of the three-dimensional structure required. Furthermore, it is generally believed that the aggregate of the upper particles also includes - a portion of the catalyst particles which are less active than the other catalyst particles or which are inactive during the reaction. It is also considered to be a non-fibrous or extremely short fibrous carbon material which grows on the surface of the above-mentioned catalyst fine particles before agglomerating into an aggregate or which is grown by using the above-mentioned catalyst fine particles as a core after forming an aggregate. A granular portion that forms a precursor at a peripheral position of the aggregate. Therefore, the granular portion includes the end portions of the plurality of vapor-grown carbon fibers and the metal catalyst particles which grow the carbon material only in the circumferential direction, and a plurality of aggregates and accumulations of the plurality of spherical structures are formed. Rather than a simple I sphere. In this state, the growth of the carbonaceous material is further continued, and the annealing treatment, which will be described later, acts to form an end portion of a plurality of vapor-phase-growth carbon fibers aggregated or accumulated in the granular portion or a plurality of spherical structures adjacent to each other. There are a continuous layer of graphite flakes. Thereby, a three-dimensional network vapor-grown carbon fiber structure in which a plurality of granular portions are firmly bonded to the gas-phase-grown carbon fibers is formed. The temperature of the raw material gas to be supplied in the vicinity of the raw material gas supply port of the reaction furnace is preferably 350 to 45 (TC, and is not particularly limited as a specific method for causing a turbulent flow of the gas stream of the material gas. a method in which a raw material gas is introduced into a reaction furnace by a swirling flow or a method of providing a collision portion or the like at a position that can interfere with a flow of a raw material gas that is discharged from a raw material gas supply port into a reaction furnace. As a shape of the collision portion, There is no limit to 142475.doc •20- 201026777. If it is a full flow generated in the reactor due to the full flow generated from the collision part, for example, various shapes of partitions, The ban, the tapered tube, the umbrella body, and the like are used alone or in combination, and are arranged in a plurality or a plurality. In the manufacturing apparatus exemplified in Fig. 1, as an example of the collision portion, a periphery of the introduction nozzle 9 is provided. The rectifying/buffering plate is disposed in the vicinity of the introduction nozzle 9 and is an obstacle that acts as a starting point for the collision of the raw material mixed gas. The obstacle is mixed with the raw material and the turbulent gas generates a vortex to make the temperature distribution and the concentration distribution uniform. The shape of the rectifying/buffering plate is not limited, and the eddy current generated from the rectifying/buffering plate does not disappear. Further, the shape to the lower end side of the reaction furnace 8 may be sequentially formed.

將觸媒以及烴之混合氣體於設定為8〇〇〜13〇〇β(:2範圍以 溫度下加熱生成而獲得之中間體’具有由碳原子而成之點 片狀薄片貼附合起的結構。該中間體若進行拉曼光譜分 析,則D譜帶非常大,且缺陷多。又,含有未反應原料、 非纖維狀碳化物、焦油成分以及觸媒金屬。 因此,為了自如上所述之中間體中除去該等殘留物而獲 得缺陷少之所需碳纖維結構體,利用適當方法於 2400〜3000 C之高溫下進行熱處理即可。 例如,藉由將該t間體於800〜1200t下加熱而除去未反 應原料及焦油成分等揮發成分後,於24〇〇〜3〇〇〇t>c之高溫 下進行退火處理,來調製所需之結構體,同時使纖維中所 含之觸媒金屬蒸發而除去。再者,此時為了保護物質結 142475.doc 201026777 構亦可於惰性氣體環境中添加還原氣體或微量之-氧化 碳氣體》 +將上述中間體於2400〜3 〇〇〇°c之範圍之溫度下進行退 火處理,則由碳原子而成之貼片狀薄片分別結合而形成複 數個石墨片狀層’從而獲得所需之氣相成長碳纖維。 再者具有上述平均纖維外徑以及纖維外徑分布之標準 偏差值的氣相成長碳纖維,於氣相成長碳纖維之製造方法 中右為批篁式,則可為在1次製造反應中獲得者。若為 連續反應,則可為將獲得適當之製造量的丨連續期間作為i 人而獲得之氣相成長碳纖維,或者亦可為如此獲得之氣相 成長碳纖維之複數次量之混合物。 本心明中,導電性樹脂複合材料中之聚碳酸酯樹脂與氣 相成長碳纖維之含量較好的是,相對於聚碳酸醋樹脂1〇〇 質量份,氣相成長碳纖維為1〜11.2質量份,更好的是3〜7.7 質量份。若含量為如上所述,則可實現良好之導電性、與 成形性相關之斷裂伸長率之改善以及氣相成長碳纖維自樹 脂複合材料之脫落之減少。若氣相成長碳纖維之含量小於 1質量份,則無法獲得目標之導電性,因此複合材料表面 所產生之靜電難以洩漏,若大於丨丨·2,則有不僅導電性變 得過尚,並且引起母材聚碳酸酯樹脂之物性下降之虞。 又’上述氣相成長碳纖維自導電性樹脂複合材料之脫落 性為,將該複合材料(50x90x3 mm)浸潰於超純水2〇〇〇 ml 中,施加47 kHz之超音波60秒後,自該複合材料之表面脫 落的粒徑為0·5 μπι以上之顆粒之數量於該複合材料之每單 142475.doc -22- 201026777 較好的是2500個/cm2以 位表面積中為5000個/cm2以下 下。 又’關於向聚碳酸酯樹脂中添加混合氣相成長碳纖維來 製造導電性樹脂複合材料之方法,該製造方法並非特別限 定者。然而,由於對於氣相成長碳纖維之分散而言必需^ 有優異之混練性能,故而較好的是使用雙軸擠出機將聚碳 酸酯樹脂與氣相成長碳纖維熔融混練。又,本發明之導電 性樹脂複合材料自其特性而言,具有可使用熱負荷大之大 型雙轴擠出機的優點。 作為雙軸擠出機之代表例子,可列舉 〇 一 & —r公司製造)。作為同樣類體 例’可列舉TEXW品名,(股)日本製鋼所製造)、te叫商 品名,東芝機械(股)製造)、ΚΤΧ(商品名,(股)神戶製鋼所 製造)等。此外,亦可列舉FCM(商品名,公司製 U ) Kneader(商σ口名,Buss公司製造)、以及DSM(商 品名,Krauss-Maffei&司製造)等熔融混練機作為具體 例上述之中更好的疋以ZSK為代表之類型。該ZSK類型 之雙抽擠出機中’其螺桿係完全喊合型,螺桿係包含長度 與間距不同之各種螺桿區段、以及寬度不同之各種捏合盤 (或者與其相當之混練用區段)者。 雙軸擠出機中更好之態樣如下所述。螺桿形狀可使用J 條2條或者3條螺紋螺桿,尤其好的是可使用熔融樹脂 之搬送能力或剪切混練能力兩者之適用範圍廣的2條螺紋 累才干雙抽擠出機之螺桿的長度(X)與直徑⑺)之比(l/D)較 142475.doc •23- 201026777 好的是20〜50,進而好的是28〜42。L/D較大者容易實現均 質之分散,另一方面,於過大之情形時,容易由於熱劣化 而產生母材樹脂之分解。螺桿上必需具有丨處以上的由用 以提高混練性之捏合盤區段(或者與其相當之混練區段)構 成的混練區域’較好的是具有1〜3處。 作為擠出機,可較好地使用具有可將原料中之水分、或 自熔融混練樹脂產生之揮發氣體脫氣之排氣口者。排氣口 _ 較好的是設置用以將產生之水分或揮發氣體高效率地排出 :擠出機外部的真空泵。又’為了提高氣相成長韻維之馨 分散性,或者儘可能除去樹脂複合材料中之雜質,可添加 水、有機溶劑、以及超臨界流體等。進而亦可將用以除去 擠出原料中所混入之異物等的篩網設置於擠出機模頭前之 區域’以將異物自樹脂複合材料中去除。作為該篩網,可 列舉金屬絲網、換網器、燒結金屬板(圓盤濾片等)等。 口將氣相成長碳纖維向播出機供給之方法並無特別限定, 可代表性地例示以下方法。⑴將氣相成長碳纖維與聚碳酸 醋樹脂獨立地供給至擠出機中之方法。⑻將氣相成長碳© 纖=與聚碳酸醋樹脂粉末使用高速混合機等混合機進行預 2合後’供給至擠出機中之方法。㈣將氣相成長碳纖 聚碳酸醋樹脂預先炫融混練而使其成為主要顆粒,將-其作為氣相成長碳纖維源予以供給之方法。 2者’於使用平均纖維外徑不同之氣相成長碳纖維之情 形,,可於上述⑴步驟之前將氣相成長碳纖維相互混合, 而且亦可於上述⑴〜(iii)之步驟時將氣相成長碳纖維相互 142475.doc -24- 201026777 混合。 又,較好的是,將寬度為50 mm、長度為9〇 mm、厚度 為3 mm之上述導電性樹脂複合材料浸潰於超純水2〇〇〇 中,施加47kHz之超音波60秒時,自表面脫落的粒徑為。 μ^η以上之脫落物之數量於每單位表面積中為5〇⑼個/cm2 以下。若脫落物之數量為5000減“下,則例如於本 發明在半導體領域中使用之情形時,可抑制由脫落物引起 的半導體製品之故障•損壞。 本發明者目前認為最佳的本發明之形態係將實現上述各 用途中之較佳應用之範圍概括而成者,例如其代表例記载 於下述實施例中。當然本發明並非限定於該等形態者。 實施例 [氣相成長碳纖維結構體(粗徑品)之調製] 使用圖1所示之製造裝置,於下述表1所示之條件下獲得 氣相成長碳纖維結構體之中間體後,於氬氣中 進行锻燒,將作為雜曾 A _ 化。繼而,.將該中心Z 分離,進行純 μ中間體於氬氣中進行26〇〇〇c之古、田 (退火處理)’進而利用氣流粉碎機進行粉 氣相成長碳纖維之平均纖維外徑為117 =” 結構體之氣相成長•維結構體(圖2以及圖3)維讀 [氣相成長碳纖維結構體(細徑品)之調製] 使用圖1所示之制 之製造裝置,於下述表1所示之 氣相成長碳纖維結構體之中間體後’於氯氣中、件下獲得 進行煅燒,將作為 900 C下 質而3有之,、、、油等之烴分離,進行純 142475.doc -25- 201026777 化。繼而,將該中間體於氬氣中進行2600°C之高溫熱處理 (退火處理),進而利用氣流粉碎機進行粉碎。藉此,獲得 氣相成長碳纖維之平均纖維外徑為58 nm,形成三維網狀 結構體之氣相成長碳纖維結構體。 [表1] 氣相成長碳纖維外徑 粗徑品 細徑品 相對於反應爐單位斷面積之觸媒量(mol/m2/min) 0.14 0.38 相對於反應爐單位斷面積之烴量(m〇l/m2/min) 13.4 9.4 載氣流量(Nl/min) 1250 1850 原料投入溫度(°C) 400 400 反應溫度:上部(°C) 900 900 反應溫度:下部(°C) 1300 1300 [實施例1] 對於聚碳酸酯樹脂(Lexan 141R(商品名,SABIC Innovative Plastics公司製造))100質量份,添加如上所述而 獲得之氣相成長碳纖維結構體(粗徑品)6.38質量份,混合 均勻。使用螺桿直徑為30 mm之排氣式雙軸擠出機TEX-30XSST(商品名,(股)曰本製鋼所製造),將該混合物供給 至最後部之第1投入口。該擠出機於第1供給口至第2供給 口之間具有捏合盤之混練區域,且於其正後方設有開放的 排氣口。相對於螺桿直徑(D),排氣口之長度約為2D。該 排氣口之後設置有側面進料機,側面進料機後進而設置有 捏合盤之混練區域以及與其相連之排氣口。該部分之排氣 口之長度約為1.5D,在該部分中使用真空泵而設為約3 142475.doc -26- 201026777 kPa之減壓度。擠出係於料筒溫度為300°C (自螺桿根部之 滾筒大致均等地上升至模頭位置)、螺桿轉速為18〇 rprn、 以及每小時之吐出量為20 kg的條件下進行。將擠出之股 線在水浴中冷卻後,利用造粒機切斷而使其成為顆粒。將 所獲得之顆粒於120°C下乾燥5小時,再利用熱風循環式乾 燥機於100°C下乾燥24小時後,使用射出成形機(東芝機械 ' IS55FPB) ’於料筒溫度為30(TC、模具溫度為80。(:、射速 * 為20 mm/sec、以及成形週期約為60秒之條件下,製作評 • 價用試驗片。 [實施例2] 除了將氣相成長碳纖維結構體(粗徑品)之添加量設為 7.53質量份以外’以與實施例1相同之方法製作評價用試 驗片。 [實施例3] 將氣相成長碳纖維結構體(粗徑品)以及氣相成長碳纖維 鲁 結構體(細徑品)以5 ·· 1之質量比加入密閉槽中,攪拌2小時 以上’獲得氣相成長碳纖維結構體之混合物,該混合物之 氣相成長碳纖維之平均纖維外徑為1〇2 nm。除了將該混合 物之添加量設為6.38質量份,來代替氣相成長碳纖維結構 體(粗徑品)以外,以與實施例〖相同之方法製作評價用試驗 ' 片。 [比較例1] 除了將氣相成長碳纖維結構體(細徑品)之添加量設為 4.17質量份,來代替氣相成長碳纖維結構體(粗徑品)以 142475.doc -27- 201026777 外’以與實施例1相同之方法製作評價用試驗片。 [比較例2] 除了將氣相成長碳纖維結構體(細徑品)之添加量設為 6.38夤量伤,來代替氣相成長碳纖維結構體(粗徑品)以 外,以與實施例1相同之方法製作評價用試驗片。 s平價用試驗片之物性係根據以下方法進行測定。 (1) 表面電阻率 參照JIS K 7194(利用導電性塑膠之4探針法的電阻率試 驗方法)’測定位置以及測定方法係依據其,使用L〇resta GP(商品名,MCP_T6〇〇型,三菱化學(股)製造)、 UP(商品名,MCP-HT45〇型,三菱化學(股)製造),測定射 出成形之試驗片(5〇x9〇x3 mm)之表面電阻並示於表2中。 (2) 斷裂伸長率 依據IS〇527-l(通則)以及527_2(模具成型、擠出成型以 及注模塑膠之試驗條件),測定拉伸斷裂伸長率。射出成 型之試驗片之形狀以及尺寸為18〇527_2之試驗片丨八形。試 驗裝置係使用萬能材料試驗機(Intesc〇 2〇〇5_5型),試驗速 度為50 mm/min,夾頭間距離為115 mm,於23。(:、50% RH 之試驗環境下進行。算出以與上述同樣之方式成型以及測 定的5片試驗片之斷裂伸長率值之平均值,並示於表2中。 (3) 脫落性 於以超純水清洗之3000 mL玻璃燒杯中,注入超純水The mixed gas of the catalyst and the hydrocarbon is attached to a sheet-like sheet made of carbon atoms at a temperature of 8 〇〇 to 13 〇〇 β (2: a range obtained by heating at a temperature of 2) Structure. If the intermediate is subjected to Raman spectroscopy, the D band is very large and has many defects. Further, it contains unreacted raw materials, non-fibrous carbides, tar components, and catalytic metals. Therefore, in order to In the intermediate, the residue is removed to obtain a desired carbon fiber structure having a small defect, and the heat treatment may be performed at a high temperature of 2400 to 3000 C by an appropriate method. For example, by using the t-substrate at 800 to 1200 t After heating, volatile components such as unreacted raw materials and tar components are removed, and then annealed at a high temperature of 24 Torr to 3 Torr, to prepare a desired structure, and at the same time, a catalyst contained in the fibers is prepared. The metal is removed by evaporation. In addition, at this time, in order to protect the material junction 142475.doc 201026777, it is also possible to add a reducing gas or a trace amount of carbon monoxide gas in an inert gas atmosphere. + Add the above intermediate to 2400~3 〇〇〇° c When annealing is performed at a range of temperatures, the patch-like sheets made of carbon atoms are combined to form a plurality of graphite sheet-like layers to obtain desired vapor-grown carbon fibers. Further, the above average fiber outer diameter and fibers are obtained. The vapor-grown carbon fiber having a standard deviation value of the outer diameter distribution may be obtained in a single production reaction in the method of producing a vapor-grown carbon fiber, and may be obtained in a single production reaction. A gas phase-grown carbon fiber obtained as a person in a continuous production period of a suitable amount, or a mixture of a plurality of times of the vapor-grown carbon fiber thus obtained. In the present invention, a polymerization in a conductive resin composite material The content of the carbonate resin and the vapor-grown carbon fiber is preferably from 1 to 11.2 parts by mass, more preferably from 3 to 7.7 parts by mass, based on 1 part by mass of the polycarbonate resin. As described above, good electrical conductivity, improvement in elongation at break associated with formability, and reduction in vapor-off growth of carbon fiber from resin composites can be achieved. If the content of the vapor-grown carbon fiber is less than 1 part by mass, the target conductivity cannot be obtained, so that the static electricity generated on the surface of the composite material is hard to leak, and if it is larger than 丨丨·2, not only the conductivity becomes excessive, but also The physical properties of the base material polycarbonate resin are lowered. Further, the exfoliation property of the vapor-grown carbon fiber from the conductive resin composite material is such that the composite material (50×90×3 mm) is impregnated into the ultrapure water 2〇〇〇ml. In the case where the ultrasonic wave of 47 kHz is applied for 60 seconds, the amount of particles having a particle diameter of 0.5 μm or more from the surface of the composite material is preferably 142475.doc -22-201026777 per plex of the composite material. 2500 pieces/cm2 are 5,000 pieces/cm2 or less in the bit surface area. Further, the method for producing a conductive resin composite by adding a vapor-grown carbon fiber to a polycarbonate resin is not particularly limited. However, since it is necessary to have excellent kneading performance for the dispersion of the vapor-grown carbon fibers, it is preferred to melt-mix the polycarbonate resin and the vapor-grown carbon fibers using a twin-screw extruder. Further, the conductive resin composite material of the present invention has an advantage of being able to use a large-sized twin-screw extruder having a large heat load. As a representative example of the twin-screw extruder, 〇一 &-r company can be cited. As a similar example, TEXW product name, (manufactured by Nippon Steel Co., Ltd.), te, trade name, Toshiba Machine Co., Ltd., ΚΤΧ (trade name, manufactured by Kobe Steel Co., Ltd.), etc. In addition, as a specific example, a melt-kneading machine such as FFM (trade name, company-made U) Kneader (commercial name, manufactured by Buss), and DSM (trade name, manufactured by Krauss-Maffei & Good 疋 is represented by ZSK. In the ZSK type double-extracting extruder, the screw system is completely shouted, and the screw system includes various screw segments having different lengths and pitches, and various kneading discs having different widths (or a kneading section corresponding thereto). . A better aspect of the twin screw extruder is as follows. The shape of the screw can be two or three threaded screws of J, and it is particularly preferable to use a screw of a two-threaded double-extracting extruder with a wide range of application of the molten resin or the shearing and kneading ability. The ratio of length (X) to diameter (7)) (l/D) is better than 142475.doc • 23- 201026777 is 20 to 50, and further preferably 28 to 42. It is easy to achieve uniform dispersion of L/D, and on the other hand, in the case of excessively large, decomposition of the base resin is likely to occur due to thermal deterioration. It is preferable that the screw has a kneading zone formed by a kneading disc section (or a kneading section equivalent thereto) for improving the kneading property above the crucible, and preferably has 1 to 3. As the extruder, those having an exhaust port capable of deaerating the moisture in the raw material or the volatile gas generated from the melt-kneading resin can be preferably used. The vent _ is preferably provided to efficiently discharge the generated moisture or volatile gas: a vacuum pump outside the extruder. Further, water, an organic solvent, a supercritical fluid, or the like may be added in order to increase the dispersibility of the gas phase growth, or to remove impurities in the resin composite as much as possible. Further, a screen for removing foreign matter or the like mixed in the extruded raw material may be placed in a region in front of the extruder die to remove foreign matter from the resin composite material. Examples of the screen include a wire mesh, a screen changer, a sintered metal plate (such as a disk filter), and the like. The method of supplying the vapor-grown carbon fiber to the dispenser is not particularly limited, and the following method can be typically exemplified. (1) A method of independently supplying a vapor-grown carbon fiber and a polycarbonate resin to an extruder. (8) A method in which a vapor-grown carbon fiber = a polycarbonate resin powder is pre-sealed with a mixer such as a high-speed mixer and then supplied to an extruder. (4) A method in which a vapor-grown carbon fiber polycarbonate resin is preliminarily blended and kneaded to be a main particle, and is supplied as a gas phase growth carbon fiber source. In the case of using the vapor-grown carbon fibers having different average outer diameters of the fibers, the vapor-grown carbon fibers may be mixed with each other before the above step (1), and the vapor phase may be grown at the steps (1) to (iii) above. Carbon fiber is mixed with each other 142475.doc -24- 201026777. Further, it is preferable that the above-mentioned conductive resin composite material having a width of 50 mm, a length of 9 mm, and a thickness of 3 mm is immersed in 2 Torr of ultrapure water, and an ultrasonic wave of 47 kHz is applied for 60 seconds. The particle size that falls off from the surface is . The amount of the exfoliate above μ^η is 5 〇(9)/cm 2 or less per unit surface area. If the amount of the detachment is 5000 minus, the failure or damage of the semiconductor article caused by the detachment can be suppressed, for example, when the present invention is used in the field of semiconductors. The present inventors believe that the present invention is the best. The morphological system is a generalized range of the above-described applications, and the representative examples thereof are described in the following examples. Of course, the present invention is not limited to the above embodiments. Preparation of Structure (Rough Diameter)] Using the manufacturing apparatus shown in Fig. 1, an intermediate of a vapor-grown carbon fiber structure was obtained under the conditions shown in Table 1 below, and then calcined in argon gas. As a heterogeneous A _. Then, the center Z is separated, and the pure μ intermediate is subjected to argon gas at 26 〇〇〇c to the ancient field (annealing treatment), and then the gas phase pulverizer is used for the vapor phase growth. The average fiber outer diameter of the carbon fiber is 117 =" The vapor phase growth of the structure and the dimensional structure (Fig. 2 and Fig. 3) are read [Modulation of the vapor-grown carbon fiber structure (small diameter product)] Manufacturing device, After the intermediate of the vapor-phase-growth carbon fiber structure shown in the following Table 1 is obtained, it is calcined in a chlorine gas, and the hydrocarbons are dehydrated as 900 C, and the hydrocarbons such as oil are separated. Pure 142475.doc -25- 201026777. Then, this intermediate was subjected to a high-temperature heat treatment (annealing treatment) at 2,600 ° C in an argon atmosphere, and further pulverized by a jet mill. Thereby, the vapor-grown carbon fiber structure in which the average fiber outer diameter of the vapor-grown carbon fiber was 58 nm was formed to form a three-dimensional network structure. [Table 1] Vapor-grown carbon fiber outer diameter, large diameter, large diameter, relative to the unit area of the reactor, the amount of catalyst (mol/m2/min) 0.14 0.38 relative to the unit area of the reactor, the amount of hydrocarbons (m〇l) /m2/min) 13.4 9.4 Carrier gas flow rate (Nl/min) 1250 1850 Raw material input temperature (°C) 400 400 Reaction temperature: upper part (°C) 900 900 Reaction temperature: lower part (°C) 1300 1300 [Example 1 To 100 parts by mass of a polycarbonate resin (Lexan 141R (trade name, manufactured by SABIC Innovative Plastics Co., Ltd.)), 6.38 parts by mass of a vapor-phase-growth carbon fiber structure (large diameter product) obtained as described above was added, and the mixture was uniformly mixed. A ventilated twin-screw extruder TEX-30XSST (trade name, manufactured by Tosoh Steel Co., Ltd.) having a screw diameter of 30 mm was used, and the mixture was supplied to the first input port of the last portion. The extruder has a kneading zone of kneading discs between the first supply port and the second supply port, and an open exhaust port is provided directly behind the nozzle. The length of the exhaust port is about 2D with respect to the screw diameter (D). A side feeder is disposed behind the exhaust port, and a kneading area of the kneading disc and an exhaust port connected thereto are disposed behind the side feeder. The exhaust port of this portion has a length of about 1.5 D, and a vacuum pump is used in this portion to set a pressure reduction of about 3 142475.doc -26 - 201026777 kPa. The extrusion was carried out under the conditions that the cylinder temperature was 300 ° C (the drum from the root of the screw rose substantially equally to the die position), the screw rotation speed was 18 〇 rprn, and the discharge amount per hour was 20 kg. After the extruded strands were cooled in a water bath, they were cut by a granulator to be granulated. The obtained granules were dried at 120 ° C for 5 hours, and then dried at 100 ° C for 24 hours using a hot air circulating dryer, and then an injection molding machine (Toshiba Machine 'IS55FPB) was used at a cylinder temperature of 30 (TC). The mold temperature was 80. (:, the rate of fire* was 20 mm/sec, and the molding cycle was about 60 seconds, and a test piece for evaluation was prepared. [Example 2] In addition to vapor-grown carbon fiber structure A test piece for evaluation was produced in the same manner as in Example 1 except that the amount of the addition was 7.5 parts by mass. [Example 3] A vapor-phase-grown carbon fiber structure (a large diameter product) and a vapor phase were grown. The carbon fiber rib structure (small diameter product) is added to the closed tank at a mass ratio of 5 ··1, and stirred for 2 hours or more to obtain a mixture of the vapor-grown carbon fiber structure, and the average fiber outer diameter of the vapor-grown carbon fiber of the mixture is 1 〇 2 nm. A comparison test piece was prepared in the same manner as in the Example except that the amount of the mixture added was 6.38 parts by mass in place of the vapor-grown carbon fiber structure (thick diameter). Example 1] The addition amount of the vapor-phase-growth carbon fiber structure (small diameter product) was 4.17 parts by mass instead of the vapor-phase-growth carbon fiber structure (thick diameter product), which was the same as that of Example 1 except that it was 142475.doc -27-201026777. The test piece for the evaluation was produced. [Comparative Example 2] In addition to the gas-growth carbon fiber structure (thick diameter product), the addition amount of the vapor-phase-growth carbon fiber structure (small diameter product) was changed to 6.38 Å. A test piece for evaluation was produced in the same manner as in Example 1. The physical properties of the test piece for s-valency were measured by the following methods: (1) Surface resistivity is referred to JIS K 7194 (resistance by 4-probe method using conductive plastic) Rate test method) 'Measurement position and measurement method are based on L,resta GP (trade name, MCP_T6 type, manufactured by Mitsubishi Chemical Corporation), UP (trade name, MCP-HT45 type, Mitsubishi Chemical ( (manufacturing)), measuring the surface resistance of the injection-molded test piece (5〇x9〇x3 mm) and shown in Table 2. (2) Elongation at break according to IS〇527-l (general rule) and 527_2 (mold forming, Extrusion and injection molding The test conditions of the rubber were measured for tensile elongation at break. The shape of the test piece for injection molding and the test piece of the size of 18〇527_2 were eight-shaped. The test device was a universal material testing machine (Intesc〇2〇〇5_5 type). The test speed was 50 mm/min, the distance between the chucks was 115 mm, and it was carried out under the test environment of 23: (50% RH). The elongation at break of 5 test pieces which were molded and measured in the same manner as above was calculated. The average value of the values is shown in Table 2. (3) Exfoliation in ultra-pure water in a 3000 mL glass beaker washed with ultrapure water

2000 mL ’浸潰1片射出成形之試驗片(5〇Χ9〇χ3 mm)。其 後’利用 5210E-DTH(47 kHz/140 W)(商品名,BRANSON 142475.doc -28- 201026777 公司製造)施加1分鐘超音波。然後’利用液中微粒子計測A test piece (5〇Χ9〇χ3 mm) was prepared by immersing one piece of 2000 mL. Thereafter, ultrasonic waves were applied for 1 minute using 5210E-DTH (47 kHz/140 W) (trade name, manufactured by BRANSON 142475.doc -28-201026777). Then using the microparticles in the liquid to measure

器 HIAC ROYCO SYSTEM8011(商品名,fjACH ULTRA ANALYTICS公司製造)來吸引所抽出之超純水,測定塵埃 粒徑為0.5 μιη以上之發塵量,並示於表2中。 [表2] 實施例1 實施例2 實施例3 比較例1 比較例2 類型 粗徑品 粗徑品 混合品 細徑品 細徑品 平均纖維外 氣相成長 徑(nm) 117 117 102 58 58 碳織維 纖維直徑標 準偏差(nm) 26 26 36 13 13 質量份 6.38 7.53 6.38 4.17 6.38 聚碳酸酯 質量份 100 100 100 100 100 表面電阻值 Ω/cm2 6.33 xlO6 1.38x10s 2.75 x10s 5.08x10s 5.23χ103 斷裂伸長率 % 40 32 60 27 22 脫落性 - 〇 〇 〇 〇 〇 ※混合品·..細徑品:粗徑品=1 ·· 5(質量比) ※脫落性...將以0.5 μηι以上之發塵量計為5000個/cm2 作為基準值(規格值),將其以下之值作為〇。 ※纖維外徑/纖維直徑...表示除粒狀部以外之氣相成 • 長碳纖維之外徑。 如表2所示之結果所述,使用氣相成長碳纖維之平均纖 維外控超過100 nm之氣相成長碳纖維的粗徑品之實施例 1〜2中’表現出充分之表面電阻值以及較低之脫落性。在 142475.doc •29- 201026777 斷裂伸長率方面’相對於細徑品之比較例1〜2小於30%, 粗徑品之實施例1〜2則高於30%。又,藉由 、。’ 鑪給+τ 入楮宙將氧相成長碳 纖,之平均纖維外_粗之氣相成長碳纖維結構體與較細 之氣相成長咴纖維結構體混合而增大標準偏差值的混合。 ::施例3中’同樣表現出充分之表面電阻值、以及:: 徑-之實施例1〜2同樣較低的脫落性。尤其 為_,得到明顯改善。 斷裂伸長丰 產業上之可利用性The HIAC ROYCO SYSTEM 8011 (trade name, manufactured by FjACH ULTRA ANALYTICS Co., Ltd.) was used to suck the extracted ultrapure water, and the amount of dust having a dust particle diameter of 0.5 μm or more was measured and shown in Table 2. [Example 2] Example 2 Example 2 Comparative Example 1 Comparative Example 2 Type of large diameter large diameter product mixed product small diameter product small diameter product average fiber outer gas phase growth diameter (nm) 117 117 102 58 58 carbon Weaving fiber diameter standard deviation (nm) 26 26 36 13 13 parts by mass 6.38 7.53 6.38 4.17 6.38 polycarbonate mass parts 100 100 100 100 100 surface resistance value Ω/cm2 6.33 xlO6 1.38x10s 2.75 x10s 5.08x10s 5.23χ103 elongation at break % 40 32 60 27 22 Exfoliation - 〇〇〇〇〇 ※ Mixed product ·.. Small diameter: Large diameter = 1 · · 5 (mass ratio) * Shedding property ... will be dusting at 0.5 μηι or more The gauge is 5000 pieces/cm2 as a reference value (specification value), and the following values are used as 〇. * Fiber outer diameter / fiber diameter... indicates the outer diameter of the long carbon fiber except for the granular portion. As shown in the results shown in Table 2, in Examples 1 to 2 in which the average diameter of the vapor-grown carbon fibers of the vapor-grown carbon fibers of the vapor-grown carbon fibers was more than 100 nm, the results showed sufficient surface resistance values and lower values. Shedding. In the case of 142475.doc •29-201026777, the elongation at break was less than 30% with respect to Comparative Examples 1 to 2 of the small diameter product, and Examples 1 to 2 of the large diameter product were higher than 30%. Also, by . The furnace gives +τ into the 将, the oxygen phase grows the carbon fiber, and the average fiber outer _ coarse gas phase growth carbon fiber structure is mixed with the fine gas phase growth 咴 fiber structure to increase the standard deviation value. :: In Example 3, 'sufficient surface resistance values were also exhibited, and: - diameter - the same low peeling properties of Examples 1 to 2. Especially for _, it has been significantly improved. Elongation at break, industrial availability

本發明之導電性樹脂複合材料在〇A(offiee autQmati〇n, 辦么至自動化)機器領域、電氣電子設備領域等各種工業 用途中極為有用’其所發揮之工業效果極大。The conductive resin composite material of the present invention is extremely useful in various industrial applications such as 〇A (offiee autQmati〇n), electrical and electronic equipment, and the like, and the industrial effect exerted thereon is extremely large.

又本發明之導電性樹脂複合材料係藉由將上述所說明 之氣相成長碳纖維調配於聚碳酸酯樹脂中,而具有優異之 :電性、經改善之斷裂伸長率以及氣相成長碳纖維難以脫 洛之特性者。藉由該特性,導電性樹脂複合材料應對廣泛 成元條件且其成形之抗裂性優異,因此可提供可應用 ;廣泛用途中之導電性材料。作為該用途,例如可例示: 個人電腦己型電腦、遊戲機(家用遊戲機、業務用遊 戲機、彈珠台(pachink〇)以及吃角子老虎(sl〇t machine) =)顯示裝置(LCD(liquid crystal display,液晶顯示 器)、有機EL(electroluminescence,電致發光)、電子紙、 電聚顯不器、以及投影儀等)、輸電零件(以感應線圈式輸 電裝置之外罩為代表)。又,作為該用途,例如可例示印 表機、影印機、掃描機以及傳真機(包括該等之複合機)。 142475.doc -30 - 201026777 進而’作為該用途,可例示:VTR(video tape recorder, 磁帶錄影機)相機、光學膜式相機、數位靜態相機、相機 用透鏡單元、防盜裝置 '以及行動電話等精密機器。尤 其,本發明之樹脂組合物適宜用於相機鏡筒、數位相機等 數位圖像資訊處理裝置之框體、外殼、以及框。 此外,本發明之導電性樹脂複合材料亦適用於:按摩機 或咼氧治療器等醫療機器;錄像機(所謂DVD錄影機等)、Further, the conductive resin composite material of the present invention is excellent in electrical properties, improved elongation at break, and vapor-grown carbon fibers by blending the vapor-grown carbon fibers described above in a polycarbonate resin. The character of Luo. By this characteristic, the conductive resin composite material is excellent in crack resistance in the formation of a wide range of conditions, and thus it can provide a conductive material which can be used in a wide range of applications. As such a use, for example, a personal computer, a game machine (a home game machine, a business game machine, a pinball machine, and a slaughter machine =) display device (LCD) can be exemplified. Liquid crystal display, liquid crystal display, organic EL (electroluminescence), electronic paper, electro-polymerization, and projectors, etc., and transmission parts (represented by the cover of the induction coil type power transmission device). Further, as the application, for example, a printer, a photocopier, a scanner, and a facsimile machine (including these multifunction machines) can be exemplified. 142475.doc -30 - 201026777 Further, as such a use, a VTR (video tape recorder), an optical film camera, a digital still camera, a camera lens unit, an antitheft device, and a mobile phone can be exemplified. machine. In particular, the resin composition of the present invention is suitably used for a frame, a casing, and a frame of a digital image processing device such as a camera barrel or a digital camera. Further, the conductive resin composite material of the present invention is also suitable for use in a medical device such as a massage machine or a helium oxygen therapy device; a video recorder (so-called a DVD recorder, etc.),

視聽機器、以及電子樂器等家電製品;彈珠台或吃角子老 虎等遊戲裝置;以及搭载有精密感測器之家用機器人等之 零件。 另外’本發明之導電性樹脂複合材料可用於:各種車輪 零件、電池、發電裝置、電路基板、積體電路之模具、光 碟基板、匣式磁碟、光學卡、IC記憶卡、連接器、電纜耦 合器、電子零件之搬送用容器(1C卡槽箱、矽晶圓容器、 玻璃基板收納容器、磁頭托盤、以及載帶等)、抗靜電用 或者除靜電零件(電子照片感光裝置之帶電輥等)、以及各 種機構零件(包括齒輪、轉盤、轉子、以及螺絲等。包括 微型機器用機構零件)。 【圖式簡單說明】 圖1係示意性表示本實施形態之氣相成長碳纖維製造裝 置之結構的結構圖; 圖2係實施例中製造之氣相成長碳纖維結構體(相^ ^ ^ 之 5000 倍SEM(scanning electron microscope,掃推戈 顯微鏡)照片; 142475.doc •31- 201026777 圖3係實施例中製造之氣相成長碳纖維結構體(粗徑品)之 粒狀部之50000 倍 TEM(transmission electron microscope, 穿透式電子顯微鏡)照片。 【主要元件符號說明】 1 氣相成長碳纖維之製造裝置 2 原料槽 3 原料導入管 4 氣體槽 5 氣體導入管 6 蒸發器 7 原料混合氣體導入管 8 反應爐 9 導入喷嘴 10 整流·緩衝板 11 加熱機構 12 氣相成長碳纖維回收器 13 氣體排出管 14 原料混合氣體導入口 15 冷卻氣體導入口 16 冷卻氣體出口 20 金屬觸媒粒子生成區域 30 氣相成長碳纖維製造區域 142475.doc • 32·Home appliances such as audio-visual equipment and electronic musical instruments; game equipment such as pinball machines or horns, and home robots equipped with precision sensors. Further, the conductive resin composite material of the present invention can be used for various wheel parts, batteries, power generation devices, circuit boards, integrated circuit molds, optical disk substrates, cymbal disks, optical cards, IC memory cards, connectors, and cables. Couplings, containers for transporting electronic components (1C card slot, enamel wafer container, glass substrate storage container, head tray, carrier tape, etc.), antistatic or static elimination parts (electrical roller for electronic photosensitive devices, etc.) ), as well as various mechanical parts (including gears, turntables, rotors, and screws, etc., including mechanical parts for micromachines). BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a structural view schematically showing the structure of a vapor-grown carbon fiber producing apparatus of the present embodiment; and Fig. 2 is a vapor-phase growing carbon fiber structure produced in the embodiment (5000 times the phase ^ ^ ^) SEM (scanning electron microscope) photograph; 142475.doc • 31- 201026777 Fig. 3 is a 50,000-times TEM (transmission electron) of the granular portion of the vapor-grown carbon fiber structure (large diameter) manufactured in the examples. Microscope, transmission electron microscope) photograph [Description of main components] 1 Manufacturing equipment for vapor-grown carbon fiber 2 Raw material tank 3 Raw material introduction pipe 4 Gas tank 5 Gas introduction pipe 6 Evaporator 7 Raw material mixed gas introduction pipe 8 Reaction furnace 9 introduction nozzle 10 rectification/buffer plate 11 heating mechanism 12 vapor-phase growth carbon fiber recovery unit 13 gas discharge pipe 14 raw material mixed gas introduction port 15 cooling gas introduction port 16 cooling gas outlet 20 metal catalyst particle generation region 30 vapor-phase growth carbon fiber production Area 142475.doc • 32·

Claims (1)

201026777 > 七、申請專利範圍: 一種導電性樹脂複合材料,其特徵在於:其係含有聚碳 酸醋樹脂以及氣相成長碳纖維者,該氣相成長碳纖維之 平均纖維外徑為超過1 〇〇 11111且15〇 nm以下,該聚碳酸醋 樹脂與該氣相成長碳纖維之混合比係相對於聚碳酸酯樹 脂100質量份,該氣相成長碳纖維為1~11.2質量份,並且 其斷裂伸長率為3 0%以上。 ' 2. 如請求項1之導電性樹脂複合材料,其中上述氣相成長 碳纖維係將平均纖維外徑為超過5 ηιη且1〇〇 nm以下之氣 相成長碳纖維A與平均纖維外徑為超過1〇〇 nm且200 nm 以下之氣相成長碳纖維B混合均質化而成之混合物,該 此a物中來自b之氣相成長碳纖維之質量存在比大於來 自Α之乳相成長碳纖維之質量存在比。 3. 4. 如請求項1或2之導電性樹脂複合材料,其中上述氣相成 長碳纖維與粒狀部形成氣相成長碳纖維結構體,該氣相 成長碳纖維結構體具有複數個粒狀部相互立體地以該氣 相成長碳纖維結合之網狀結構。 如明求項3之導電性樹脂複合材料,其中上述粒狀部具 有上述氣相成長碳纖維之平均纖維外徑之丨· 3倍以上的與 圓相當之平均外徑。 一 5. 如請求項中任—項之導電性樹脂複合材料,其中上 述氧相成長碳纖維之纖維外徑(nm)的分布之標準偏差 2 5 〜40 〇 °、 6. 如凊求項5之導電性樹脂複合材料,其中上述氣相成長 142475.doc 201026777 碳纖維之纖維外徑(nm)的分布之標準偏差為3〇〜4〇。 7.如請求項1至6中任一項之導電性樹脂複合材料,其中氣 相成長碳纖維自上述導電性複合材料上之脫落性為,將 該複合材料(5〇χ9〇χ3 mm)浸潰於超純水2〇〇〇 mLt,施 加47 kHz之超音波60秒後,自該複合材料之表面脫落的 粒徑為0.5 μιη以上之顆粒之數量於該複合材料之每單位 表面積中為5000個/cm2以下。 8·如請求項1至6中任一項之導電性樹脂複合材料,其中使 用上述導電性樹脂複合材料而成形之成形物的表面電阻 值為 103〜1〇12 Ω/口。 9·如凊求項1至6中任一項之導電性樹脂複合材料,其中上 述導電性樹脂複合材料之斷裂伸長率為4〇%以上。 142475.doc201026777 > VII. Patent application scope: A conductive resin composite material characterized in that it comprises a polycarbonate resin and a vapor-grown carbon fiber, and the average fiber outer diameter of the vapor-grown carbon fiber is more than 1 〇〇11111 And the mixing ratio of the polycarbonate resin and the vapor-grown carbon fiber is 100 parts by mass or less, the vapor-grown carbon fiber is 1 to 11.2 parts by mass, and the elongation at break is 3 0% or more. 2. The conductive resin composite material of claim 1, wherein the vapor-grown carbon fiber has an average fiber outer diameter of more than 5 ηηη and a vapor-phase growth carbon fiber A of 1 〇〇 nm or less and an average fiber outer diameter of more than 1 A mixture of 气相nm and a vapor-grown carbon fiber B of 200 nm or less is homogenized, and the mass of the vapor-grown carbon fiber derived from b is higher than that of the carbon fiber derived from the mash. 3. The conductive resin composite according to claim 1 or 2, wherein the vapor-grown carbon fiber and the granular portion form a vapor-grown carbon fiber structure, the vapor-grown carbon fiber structure having a plurality of granular portions mutually solid The mesh structure in which the vapor phase grows carbon fibers are combined. The conductive resin composite material according to claim 3, wherein the granular portion has an average outer diameter corresponding to a circle equal to or more than 3 times the average fiber outer diameter of the vapor-grown carbon fibers. The conductive resin composite material according to any one of the claims, wherein the standard deviation of the distribution of the outer diameter (nm) of the fiber of the oxygen phase growing carbon fiber is 25 to 40 〇°, 6. In the conductive resin composite material, the standard deviation of the distribution of the outer diameter (nm) of the carbon fiber of the above-mentioned vapor phase growth 142475.doc 201026777 carbon fiber is 3 〇 4 〇. 7. The conductive resin composite material according to any one of claims 1 to 6, wherein the vapor-off carbon fiber is detached from the conductive composite material, and the composite material (5〇χ9〇χ3 mm) is impregnated. In ultra-pure water 2〇〇〇mLt, after applying ultrasonic waves of 47 kHz for 60 seconds, the number of particles having a particle size of 0.5 μm or more from the surface of the composite material is 5,000 per unit surface area of the composite material. /cm2 or less. The conductive resin composite material according to any one of claims 1 to 6, wherein the molded article formed by using the above conductive resin composite material has a surface resistance value of 103 to 1 〇 12 Ω/□. The conductive resin composite material according to any one of the items 1 to 6, wherein the conductive resin composite material has a breaking elongation of 4% by weight or more. 142475.doc
TW98133256A 2008-09-30 2009-09-30 Conductive resin composites TWI443149B (en)

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