TW393443B - Granules based on pyrogenically prepared silicon dioxide, method for their preparation and use thereof - Google Patents

Granules based on pyrogenically prepared silicon dioxide, method for their preparation and use thereof Download PDF

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TW393443B
TW393443B TW85101073A TW85101073A TW393443B TW 393443 B TW393443 B TW 393443B TW 85101073 A TW85101073 A TW 85101073A TW 85101073 A TW85101073 A TW 85101073A TW 393443 B TW393443 B TW 393443B
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Taiwan
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particles
pyrolysis
silicon dioxide
water
granules
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TW85101073A
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Chinese (zh)
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Klaus Deller
Helmfried Krause
Jurgen Meyer
Dieter Kerner
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Degussa
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附件一(A):第 85101073 年;j R:㈣-補充 p年1月呈 i、發明說明(24 ) 阖式簡要說明 圖1係爲以表格及圖式表示之依據本發明實施例1g 4所獲得之顆粒的粒徑分布。 圖2係爲以表格及圖式表示之依據本發明實施例5至 8所獲得之顆粒的粒徑分布。 圖3係爲以表格及圖式表示之依據本發明實施例9至 11所獲得之顆粒的粒徑分布。 圖4係爲以表格及圄式表示之依據本發明實施例12 至14所獲得之顆粒的粒徑分布。 (請先閱讀背面之注意事項再填寫本頁) 装【·!--- -- 訂·111111· 經濟部智慧財產局員Η消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -26-1 - A7 A7 經濟部中央樣準局貝工消費合作社印製 ._ B7_ 五、發明説明(1 ) 本發明是有關於以經熱解法製法得之二氧化矽爲主的 顆粒,彼之製備方法及彼作爲催化劑載體的用途。 已知可以高溫-或水焰水解法來從s i C交4製備出 火成(pyrogenic)砂石或二氧化砍(1111111311113£1125^1〇-pSdie der technischen Chemie,第 4版,第2 1卷,第 464 頁(1982))。 火成二氧化矽可由其極度細的顆粒、高比表面( BET)、非常高的純度、球形顆粒形狀和沒有孔洞等來 辨別出來。其於這些性質,以熱解法製得的二氧化矽來作 催化劑的載體已引起越來越多的興趣( Dr. Koth等人, Chem· Ing. Techn. 52,628(1980)。以熱解 法製得的二氧化矽有以機械裝置,比如打錠機,來塑形以 用於應用中。 另外也知道可利用噴灑乾燥法來將以熱解法製得的二 氧化矽塑形成經噴灑的顆粒以便獲得供燒結陶瓷材料使用 的起始材料(DE_ A3 6Attachment 1 (A): 85101073; j R: ㈣-supplement p in January, i. Description of the invention (24) Brief description of the formula Figure 1 is a table and diagram according to the embodiment 1g of the present invention 4 Particle size distribution of the obtained particles. Fig. 2 shows the particle size distributions of the particles obtained according to Examples 5 to 8 of the present invention in the form of a table and a diagram. FIG. 3 shows the particle size distribution of the particles obtained according to Examples 9 to 11 of the present invention in the form of a table and a diagram. FIG. 4 is a particle size distribution of the particles obtained in accordance with Examples 12 to 14 of the present invention in the form of a table and formula. (Please read the precautions on the back before filling this page) Install [·! ----Ordered · 111111 · Printed by a member of the Intellectual Property Bureau of the Ministry of Economic Affairs / Consumer Cooperative, the paper size applies to the Chinese National Standard (CNS) A4 (210 X 297 mm) -26-1-A7 A7 Central Ministry of Economics Printed by the local shellfish consumer cooperative. B7_ V. Description of the invention (1) The present invention relates to particles mainly composed of silicon dioxide obtained by a pyrolysis method, a method for preparing the same, and a use thereof as a catalyst carrier. It is known that pyrogenic gravel or shovel (1111111311113 £ 1125 ^ 1〇-pSdie der technischen Chemie, 4th edition, volume 21) can be prepared from si C cross 4 by high temperature- or water flame hydrolysis. P. 464 (1982)). Fumed silica can be distinguished by its extremely fine particles, high specific surface area (BET), very high purity, spherical particle shape, and no holes. Because of these properties, the use of silica prepared by pyrolysis as a catalyst support has attracted increasing interest (Dr. Koth et al., Chem. Ing. Techn. 52, 628 (1980). Pyrolysis The prepared silicon dioxide can be shaped by mechanical devices, such as a spindle mill, for use in applications. It is also known that the spray-drying method can be used to form the silicon dioxide prepared by pyrolysis into sprayed particles. In order to obtain starting materials for sintered ceramic materials (DE_ A3 6

此外也知道可利用噴灑乾燥法將在電弧中以熱解法製 得二氧化矽塑形成經噴灑的顆粒,彼可用作吸收媒質,或 者要不然可用作催化劑載體(DE-A 1 2 0 9 1 0 8 )。 也知道可使以熱解法製得的二氧化矽進行凝膠方法, 以及在後績進行噴灑乾燥法以塑形成顆粒。這些顆粒在塗 覆上二氧化鉻後,被使用在乙烯的聚合化中(E P _A 0 0 5 0 902, US-A 4,386,016 私紙張尺度適用中國國家橾準(CNS ) A4规格(210X297公釐) ' " ' (請先閲讀背面之注f項再填寫本頁) 訂 A7 B7 五、發明説明(2 ) 此外,二氣化矽沉澱物在烯烴的催化聚合化中作爲催 化劑載體的用逢也是爲人所知的(W0 9 1/ 0 9 8 8 1 )。 這些已知之以熱解法製得的二氧化矽噴灑顆粒有個缺 點,就它們在像聚乙烯的製備上並不是最適合用作催化劑 載體· 因此本發明目標是要由以熱解法製得的二氧化矽來發 展經噴灑的顆粒*彼可在聚乙烯的製備中用作催化劑載髖 〇 本發明提供以熱解法製得的二氧化矽爲主的顆粒,這 類顆粒具有以下的物理化學性質: (請先Μ讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局貝工消費合作社印装 平 均晶 粒大小: 1 0 至 1 2 0 β m Β Ε Τ 表面稹: 4 0 至 4 0 0 m z/ g 孔 洞 容 積: 0 • 5 至 2 • 5 ml / S 孔 徑 分 布: 直 徑 < 5 η m 的 孔洞 在 全 部 孔 洞 容 積 中 小 於5 % > 其 餘 爲 中 等 — 及 巨大 孔 洞 Ρ Η 值: 3 • 6 至 8 • 5 穿 孔 密 度· 2 2 0 至 7 0 0 S / 升 本 發明顆粒狀材料 的製備是將 以 熱 解 法 製 得 的二 氧 化 矽分布在水中,對其進行乾燥噴灑和在1 5 0至 本紙張尺度暹用中國國家揉準(CNS ) Α4规格(210X297公釐) -5 - A7 A7 經濟部中央揉準局貝工消費合作社印裂 __B7_ _ 五、發明説明(3 ) 1 ,100°C的溫度對所得顆粒進行1至8小時的加熱。 本發明也有提供以熱解法製得的二氧化矽爲主的顆粒 ,彼具有以下的物理化學性質: 平均晶粒大小: 10至120//m BET 表面稹: 40 至 400m2/g 孔洞容 稹: 0.5至2.5ml/g 孔徑分 布: 直徑<5nm的孔洞在全 部孔洞容積中小於5 %, 其餘爲中等一及巨大孔洞 pH 值·· 3. 6 至 8. 5 穿孔密 度: 220至700g /升 本發明顆粒狀材料的製備是將以熱解法製得的二氧化 矽分布在水中,對其進行乾燥噴灑和對所得顆粒進行矽烷 化作用。可使用鹵化矽烷、矽氨烷及/或矽氧烷來進行矽 烷化作用· 下列物物尤其可用作齒化矽烷: X3Si (CnH2n + 1)型式的鹵化有機矽烷 X = C 1 ,B r η = 1 至 2 0 X2(R / ) S i ( C„H2n + 1)型式的鹵化有機矽烷 X = C 1 - B r 本紙張尺度適用中國國家梂準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁)In addition, it is also known that the spray-drying method can be used to form silicon dioxide in the arc by pyrolysis to form sprayed particles, which can be used as an absorption medium or else as a catalyst carrier (DE-A 1 2 0 9 1 0 8). It is also known that the silicon dioxide produced by the pyrolysis method can be subjected to a gel method, and a spray-drying method can be performed to form particles afterwards. After being coated with chromium dioxide, these particles are used in the polymerization of ethylene (EP_A 0 0 5 0 902, US-A 4,386,016. The size of private paper is applicable to China National Standard (CNS) A4 specifications ( 210X297 mm) '"' (Please read the note f on the back before filling this page) Order A7 B7 V. Description of the invention (2) In addition, the silicon dioxide precipitated as a catalyst carrier in the catalytic polymerization of olefins Its use is also known (W0 9 1/0 9 8 8 1). These silicon dioxide spray particles, which are known to be produced by pyrolysis, have a disadvantage in that they are not the same as in the preparation of polyethylene Most suitable for use as a catalyst carrier. Therefore, the objective of the present invention is to develop sprayed particles from silicon dioxide produced by pyrolysis. * They can be used as catalyst carriers in the preparation of polyethylene. The obtained silicon dioxide-based particles have the following physical and chemical properties: (Please read the precautions on the back before filling out this page) Order the average grain size printed by the Shell Standard Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs : 1 0 to 1 2 0 β m Β Ε Τ Surface 稹: 40 to 4 0 mz / g pore volume: 0 • 5 to 2 • 5 ml / S Pore size distribution: pores with a diameter < 5 η m are less than 5% of the total pore volume > the rest are Medium—and huge holes PΗ Value: 3 • 6 to 8 • 5 Perforation density · 2 2 to 7 0 0 S / liter The granular material of the present invention is prepared by distributing silicon dioxide obtained by pyrolysis in water, Dry-spray it and use the Chinese National Standard (CNS) Α4 (210X297 mm) -5-A7 A7 at the paper size of 150 to this paper size .__ B7_ _ 5. Description of the invention (3) 1, The obtained particles are heated at a temperature of 100 ° C for 1 to 8 hours. The present invention also provides particles mainly composed of silicon dioxide prepared by pyrolysis, which have the following physical and chemical properties : Average grain size: 10 to 120 // m BET surface 稹: 40 to 400m2 / g pore volume 稹: 0.5 to 2.5ml / g pore size distribution: pores with a diameter < 5nm are less than 5% of the total pore volume, the rest for PH value of medium and huge pores · 3.6 to 8.5 Perforation density: 220 to 700 g / liter The granular material of the present invention is prepared by distributing silicon dioxide obtained by pyrolysis in water and spraying it dry And subjecting the resulting particles to silylation. Silanes can be used with halogenated silanes, silazane, and / or siloxanes. The following are particularly useful as toothed silanes: X3Si (CnH2n + 1) type halogenated organic silanes X = C 1, B r η = 1 to 2 0 X2 (R /) S i (C „H2n + 1) type of halogenated organic silane X = C 1-B r This paper size applies to China National Standard (CNS) A4 (210X297 mm) ( (Please read the notes on the back before filling out this page)

-6 - A7 B7 五、發明説明(4 ) R =焼基 η = 1 至 2 0 X (R / ) 2S i (CnH2n + 1)型式的鹵化有機矽烷 X = C 1 · B r R =院基 η = 1 至 2 0 X a S i ( CH2) R >型式的鹵化有機矽烷 X = C 1 ,B r m = 〇 . 1 至 2 0 R / =烷基,芳基(比如_CeH5) -C4F9,— 〇cf2-chf-cf3,- CeF13’ -0-CF2-CHF2 一 N Η 2 ' _ N 3 · — SCN , _ C H = C H 2 * -0 0 C ( C H 3 ) c = C H 2 -〇CH2-CH ( 0 ) C H 2 經濟部中央標準局負工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) -NH-CO-N-CO - (CH2) 5-6-A7 B7 V. Description of the invention (4) R = fluorenyl η = 1 to 2 0 X (R /) 2S i (CnH2n + 1) type of halogenated organosilane X = C 1 · B r R = courtyard η = 1 to 2 0 X a S i (CH2) R > type of halogenated organosilane X = C 1, B rm = 0.1 to 2 0 R / = alkyl, aryl (such as _CeH5) -C4F9 , — 〇cf2-chf-cf3, — CeF13 '-0-CF2-CHF2 —N Η 2' _ N 3 · — SCN, _ CH = CH 2 * -0 0 C (CH 3) c = CH 2 -〇 CH2-CH (0) CH 2 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) -NH-CO-N-CO-(CH2) 5

I_I -NH-COO-CHa* - NH-C00-CH2-CH3,- NH - ( C H 2 ) a S i (OR) 3 -Sx- (CH2) 3S i (OR) 3 (R ) X 2 S i 型式的鹵化有機矽烷 X = C 1 . B r 本紙張尺度適用中國國家橾準(CNS ) A4規格(210X297公釐) ~ 經濟部中央標率局員工消費合作社印製 A7 _B7_ 五、發明説明(5 ) R =烷基 m = 0 · 1 至 2 0 R > =烷基,芳基(比如—CeH5) —C4F9,—ocf2_chf — CF3, —C β F i3* — 0 — CF2_CHF2 -NH2,一N3,一SCN,一CH=CH2, -00C (CH3) c = ch2 -0CH2— CH (0) C H 2 -NH-CO-N-CO - (CH2) 5 I-1 -nh-coo-ch3,- nh-coo-ch2 C H 3 ' - N H - ( C H 2 ) 3 s i (OR) 3 —S x — ( C H 2 ) 3 S i (OR) 3 (R) 2XS i (CH2) m— R —型式的鹵化有機矽烷 X = C 1 . B r R =烷基 m = Ο · 1 至 2 Ο R > =烷基,芳基(比如_CeH5) -C4Fe,- OCF2-CHF-CF3, _C6F13,_0_CF2_CHF2 -NH2,- N3,— SCN,- CH=CH2, -0 0 C ( C H 3 ) c = C H 2 -0 C H 2- C H (0) C H 2 -N H - C 0 - N - C 0 - ( C H 2)5 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) 、裝r 訂 -8 - A7 經濟部中央樣準局貝工消費合作社印製 B7五、發明説明(6 ) -nh-coo-ch3,- nh-coo-ch2 C Η 3 * - Ν Η - ( C Η 2 ) 3 s i (OR) 3 -Sx- (CH2) 3S i ( 0 R ) a 以下的物質尤其可用作烷氧基矽烷 (R〇)3Si (C„H2n + 1)型式的有機矽烷 R =烷基 η = 1 至 2 0 (R、(RO)ySi ( C nH 2n+1 ) R =烷基 R / =烷基 η = 1 至 2 0 χ + y = 3 x = 1,2 y = 1,2 (RO) 3S i (CH2) m-R>型式的有機矽烷 R =焼基 η = 0 · 1 至 2 0 R> =烷基,芳基(比如- CeH5) -C4F9,- OCF2-CHF-CF3,-C e F 13* — 0—CF2— CHF2 _ N H 2 * _ N 3 · 一 SCN ’ ~ C H = C H 2 ' -0 0 C ( C H 3 ) c = C H 2 (請先閎讀背面之注意事項再填寫本頁) -II. 訂 "· 本紙張尺度逍用中國國家橾準(CNS ) A4規格(210X297公釐) 經濟部中央梂準局員工消費合作社印製 A7 B7 五、發明説明(7 ) -0CH2-CH (0) ch2 —NH— C0 — N— CO — ( C H 2 ) 5I_I -NH-COO-CHa *-NH-C00-CH2-CH3,-NH-(CH 2) a S i (OR) 3 -Sx- (CH2) 3S i (OR) 3 (R) X 2 S i Type of halogenated organic silane X = C 1. B r This paper size is applicable to China National Standard (CNS) A4 (210X297 mm) ~ Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 _B7_ V. Description of the invention (5 ) R = alkyl m = 0 · 1 to 2 0 R > = alkyl, aryl (eg —CeH5) —C4F9, —ocf2_chf — CF3, —C β F i3 * — 0 — CF2_CHF2 -NH2, one N3 , One SCN, one CH = CH2, -00C (CH3) c = ch2 -0CH2— CH (0) CH 2 -NH-CO-N-CO-(CH2) 5 I-1 -nh-coo-ch3,- nh-coo-ch2 CH 3 '-NH-(CH 2) 3 si (OR) 3 —S x — (CH 2) 3 S i (OR) 3 (R) 2XS i (CH2) m— R — Halogenated organosilane X = C 1. B r R = alkyl m = 〇 · 1 to 2 Ο R > = alkyl, aryl (such as _CeH5) -C4Fe,-OCF2-CHF-CF3, _C6F13, _0_CF2_CHF2- NH2,-N3,-SCN,-CH = CH2, -0 0 C (CH 3) c = CH 2 -0 CH 2- CH (0) CH 2 -NH-C 0-N-C 0-(CH 2 ) 5 This paper size applies Chinese National Standard (CNS) A4 specification (210X297 mm) (please read the notes on the back before filling this page), book r-8-A7 Printed by B7 Consumer Products Cooperative of the Central Samples Bureau of the Ministry of Economic Affairs 5. Description of invention (6) -nh -coo-ch3,-nh-coo-ch2 C Η 3 *-Ν Η-(C Η 2) 3 si (OR) 3 -Sx- (CH2) 3S i (0 R) a Organic silanes of the alkoxysilane (R0) 3Si (C „H2n + 1) type R = alkyl η = 1 to 2 0 (R, (RO) ySi (C nH 2n + 1) R = alkyl R / = Alkyl η = 1 to 2 0 χ + y = 3 x = 1, 2 y = 1, 2 (RO) 3S i (CH2) m-R > type of organosilane R = fluorenyl η = 0 · 1 to 2 0 R > = alkyl, aryl (eg-CeH5) -C4F9, -OCF2-CHF-CF3, -C e F 13 * — 0—CF2— CHF2 _ NH 2 * _ N 3 · One SCN '~ CH = CH 2 '-0 0 C (CH 3) c = CH 2 (Please read the precautions on the reverse side before filling out this page) -II. Order " · This paper size is free to use China National Standards (CNS) A4 Specifications (210X297 mm) A7 B7 printed by the Consumers' Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (7) -0CH2-CH (0) ch2 —NH— C0 — N— CO — (C H 2) 5

I_I -NH-COO-CHa' - NH-C00-CH2 -CH3,- NH — (CH2) 3S i ( 0 R ) a -Sx-(CH2)3Si(OR)3 (R " ) x ( R 0 ) y S i ( C H 2) m- R ^ R 〃 =烷基 x + y = 2 x = 1,2 y = 1 ,2 R~=烷基,芳基(比如—CeH5) -C4F9> - 0CF2-CHF-CF3'- C 6 F i3* — 0 — CF2— CHF2 -NH2,一N3,一SCN,一CH=CH2, -0 0 C ( C H 3 ) c = C H 2 -0CH2-CH (0) C H 2 —NH-CO-N— CO - ( C H 2 ) 5 I_! -nh-coo-ch3· - nh-coo-ch2 —CH3,-NH-(CH2)3Si ( 0 R ) 3 -Sx- (CH2) 3S i (OR) 3 較宜使用矽烷Si 108〔CH3〇)3— Si-CeH17〕,三甲氧基辛基矽烷來作矽氧化劑。 以下物質尤其可用作矽氨烷: 本紙張尺度適用中國國家標準(CNS ) A4规格(210X 297公釐) (請先閲讀背面之注意事項再填寫本頁) 訂 - 10 - 五、發明説明(8 ) R,R2Si- N -SiR2R( Η A7 B7 型式的矽氨院 R =院基 R > =烷基,乙烯基 以及比如六甲基二矽氨烷。 以下的物質尤其可用作矽氧烷: D3、D4、D5型式的環多矽氧烷(pc ),如比八甲基環四矽氧烷=D4 )lysiloxaneI_I -NH-COO-CHa '-NH-C00-CH2 -CH3,-NH — (CH2) 3S i (0 R) a -Sx- (CH2) 3Si (OR) 3 (R ") x (R 0 ) y S i (CH 2) m- R ^ R 〃 = alkyl x + y = 2 x = 1, 2 y = 1, 2 R ~ = alkyl, aryl (eg —CeH5) -C4F9 >-0CF2 -CHF-CF3'- C 6 F i3 * — 0 — CF2— CHF2 -NH2, one N3, one SCN, one CH = CH2, -0 0 C (CH 3) c = CH 2 -0CH2-CH (0) CH 2 —NH-CO-N— CO-(CH 2) 5 I_! -Nh-coo-ch3 ·-nh-coo-ch2 —CH3, -NH- (CH2) 3Si (0 R) 3 -Sx- ( CH2) 3S i (OR) 3 is more preferably a silicon oxidant using silane Si 108 [CH3〇) 3-Si-CeH17] and trimethoxyoctylsilane. The following substances are particularly useful as silazane: This paper is sized for China National Standard (CNS) A4 (210X 297 mm) (Please read the precautions on the back before filling this page) Order-10-V. Description of the invention ( 8) R, R2Si- N -SiR2R (Η A7 B7 type silamine courtyard R = courtyard R > = alkyl, vinyl and such as hexamethyldisilazane. The following materials are particularly useful as siloxy Alkane: D3, D4, D5 type cyclopolysiloxane (pc), such as octamethylcyclotetrasiloxane (D4) lysiloxane

-I. l·- HIJn It 1^1 1---^-::t I— I (請先閲讀背面之注意事項再填寫本頁J 訂 ch3 ch3-I. L ·-HIJn It 1 ^ 1 1 --- ^-:: t I— I (Please read the precautions on the back before filling in this page J Order ch3 ch3

Si 〇 / N O CH3Si 〇 / N O CH3

NN

SiSi

Si 〆 H3C 〇 0 CH3 Si ch3/ ^ch3 經濟部中央標準局貝工消費合作杜印裝 如以下型式的多矽氧烷或矽酮油Si 〆 H3C 〇 0 CH3 Si ch3 / ^ ch3 Shellfish consumer cooperation cooperation printed by the Central Bureau of Standards of the Ministry of Economy The following types of polysiloxane or silicone oil

Y-0- R ’ I • m R" 1 _ 1 Si-0 I - 1 Si-0 I 1 R, 1 R… m _ · n- Y 本紙張尺度逍用中國國家標準(CNS ) A4規格(2丨0X297公釐) -11 - B7 五、發明説明(9 )Y-0- R 'I • m R " 1 _ 1 Si-0 I-1 Si-0 I 1 R, 1 R… m _ · n- Y This paper is based on China National Standard (CNS) A4 specifications ( 2 丨 0X297mm) -11-B7 V. Description of the Invention (9)

m =0 * 1 ,2 * 3 9 … 〇〇 η =0 1 1 ,2 » 3 » • · · oo u =0 > 1 ,2 3 1 • · · … oo Y =C Η 3 ,Η - C η Η 2 η 十1 n = l至2 0 Υ =S i ( C Η 3) 3 S i ( c H 3) 2H, S i ( C Η 3 ) 2 0 Η > S i ( c H 3) 2 ( 〇 c H S i ( C Η 3 ) 2 ( C ηΗ 2 n + 1 ) n =1 至 2 0 R =烷 基 9 芳基 ( C Η 2 ) n — N Η 2、H R 院 基 ,芳 基 ( C H 2) n — N H 2 ' H R • 一 院 基 ,芳 基 ( C H 2) n N H 2 ' H R * » » = =烷基,芳基、 C C Η 2 ) n - -N Η 2、H (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印衷 本發明還提供以經熱解法製得之二氧化矽爲主的顆粒 彼具有以下的物理化學性質: 平均晶粒大小: 10至120//m BET 表面積: 40 至 400m2/g 孔 洞 容 積: 0 • 5 至 2 • 5 m 1 / S 孔 徑 分 布: 直 徑 < 5 η m 的 孔 洞 在 全 部 孔 洞 容 積 中 小 於 5 % 9 其 餘 爲 中 等 — 及 巨 大 孔 洞 碳 含 置: 0 • 3 至 1 5 • 0 重 量 % P Η 值: 3 • 6 至 8 • 5 穿 孔 密 度: 2 2 0 至 7 0 0 S / 升 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)_ 12 經濟部中央標準局貝工消費合作社印袈 A7 B7 五、發明説明(ίο) 本發明顆粒材料具宜具有中等一及巨大孔洞,其中中 等孔洞容稹在全部孔洞容積中佔有1 0至8 0%。 本發明顆粒材料的碳含置在0·3至15.0重量% 〇 本發明顆粒材料的粒徑分布是有8 0容稹%會大於8 仁m,以及有80容稹%會小於96#m。 在一個本發明較佳體系中,小於5 A m的孔洞在全部 孔洞容積中佔有比例至多爲5%。 本發明顆粒材料的製備是使以經熱解法製得之二氧化 矽分布在水中,對彼其行噴灑乾燥,使所得顆粒加熱到 15 0至1 ,100 °C的溫度達1至8小時,以及然後對 彼其行矽烷化作用。可以如上述的鹵化矽烷、烷氧基矽烷 、矽氨烷及/或矽氧烷來進行矽烷化作用。 本發明還另外提供一種以經熱解法製得之二氧化矽爲 主顆粒的製備方法,其特徵爲使以經熱解法製得的二氧化 矽一較宜爲以火焰水解法由四氯化矽製得之二氧化矽-分 布在水中,使其噴灑乾燥,所得顆粒可選擇性地加熱 1 5 0至1 ,1 00°C的溫度達1至8小時及/或進行矽 院化。 在水中的分布液具有5至2 5重量%的二氧化矽濃度 〇 噴灑乾燥法可在2 0 0至6 0 0°C的溫度下進行。轉 盤噴霧裝置或噴噴霧裝置可用於該目的中* 對顆粒的加熱可在固定床一比如窯室,和在移動床一 本紙張尺度適用中國國家揉準(CNS ) A4规格(210X297公釐) {請先閲讀背面之注意事項再填寫本頁) '裝 訂 -13 - 經濟部中央橾準局員工消费合作社印製 A7 __B7五、發明説明(11 ) 比如旋轉乾燥器,中進行。 可以如上述的鹵化矽烷、烷氧基矽烷、矽氨烷及/或 矽氧烷來進行矽烷化作用,其中矽烷化劑可選擇性地溶解 在像乙醇的有機溶劑中。 較宜使用矽烷s i 108〔(CH30)3-S i-C8H17〕,三甲氧基辛基矽烷,來作矽烷化劑。 矽烷化的進行是使顆粒材料與矽烷化劑一起噴灑,接 著在1 0 5至4 0 0°C的溫度對混合物進行1至6小時的 熱處理。 在另一種選擇的方法中,對顆粒進行矽烷化作用是以 蒸氣形式的矽烷化劑來處理顆粒材料,接著在2 0 0至 8 0 0 °C的溫度對混合物進行0 . 5至6小時的熱處理。 熱處理可在像氮氣的保護性氣體中進行。 矽烷化作用可在配備有噴灑設施之可加熱的混合器和 乾燥器中以連縝方式或以間歇方式來進行》合適的裝置例 子有犁頭混合器、轉盤乾燥器或流體化床乾燥器》 顆粒的物理化學變數,比如比表面積、粒徑分布、孔 洞容積、壓實密度及矽烷醇基團濃度、孔洞分布及P Η值 -可在特定上下限內藉著改變起始材料及進行噴灑、加熱 和矽烷化時的條件來變化。 本發明的顆粒可用作聚合化催化劑的載體*尤其是作 用於製備聚乙烯之催化劑的載體。 本發明顆粒的優點是擁有高純度、高的熱安定性、低 的矽烷醇基團濃度、一級顆粒爲微球體形狀和在全部孔洞 (請先閲讀背面之注意事項再填寫本頁) k-· *?τ %: 本紙張尺度逋用中國國家標準(CNS ) A4規格(210X297公釐) -14 - __ B7_ 五、發明説明(12) 容積中有低於5%的孔洞存在有< 5 nm的直徑。 本發明另外提供以顆粒作爲催化劑載體,尤其是用以 製備聚合化催化劑者,的用途β在一個本發明較佳體系中 ,本發明顆粒可作爲用以製造供製備聚乙烯用之催化劑的 催化_載體。 實施例 所用之經熱解法製得之二氧化矽具有底下的物理化學 性質。 (請先閲讀背面之注意事項再填寫本頁) 經濟部中央揉準局員工消費合作社印袈 本紙張尺度適用中國國家標隼(CNS〉Α4规格(210X297公釐) A7 B7 發明説明(13 經濟部中央梂準局負工消费合作社印製 氣矽90 氣矽130 氣矽150 氣矽200 氣矽300 氣矽380 氣矽0X 50 CAS註冊號碼 112945-52-5 (先前的號S |: 7631-86-9) 對水的作用 财性 外覼 鬆散的白色粉末 表面積 BET 丨)m2/g 90± 15 130 ±25 150 ± 15 200 ± 25 300 土 30 380 ±30 50土 15 一級顆粒的平 均孔徑mm 20 16 14 12 7 7 •40 壓資密度2) 正常者爲g/1 舰縮者爲g/1 伽上"V, 估Ιί·爲80 估計爲50 估計爲120 估計爲50 估計爲Π0 估計爲50 估計爲120 估計爲50 估計爲120 估計爲50 估計爲120 估計爲130 脫離載體時的 乾燥失重3> (105 1C 下 2 小 時) % < 1.0 <1.5 < 0.59) <1.5 < 1.5 < 1.5 <1.5 燃燒時失重4)7) (l,000°c 下2 小 時) % <1 <1 <1 <1 <2 <2.5 <1 pHfi|S) (¢4% 含水分布液中> 3.6-4.5 3.6-4.3 3.6-4.3 3.6-4.3 3.6-4.3 36-4.3 3.6-43 Si02 '> % >99,8 >99.8 >99.8 >99,8 >99.8 >99.8 >99.8 雜’)% <0.05 <0.05 <0.05 <0.05 <0.05 <0.05 <0.08 Fe20,,) % < 0.003 < 0.003 <0.003 < 0.003 <0,003 <0.003 <0.01 Ti02 % <0.03 <0.03 <0.03 <0.03 <0.03 <0.03 <0.03 HC1,)n) % < 0.025 < 0.025 < 0.025 < 0.025 < 0.025 <0.025 <0.025 大小超過而被 過篩掉者(依據 Mocker, 45 μπι) % <0.05 <0.05 <0.05 <0,05 <0.05 <0.05 0.2 2) 依據ISO 787/XI, JIS K 5101/丨8(未經過篩) 3) 依據DIN ISO 787/1丨.ASTM D 28(UIS KL 5101/21 4) 依據DIN 55921,ASTM D 1208, JIS Κ 5101/23 5) 依據 DIN ISO 787/IX,ASTM D 1208, MS K 5101/24. 6) 依據DINISO787/XVm, JIS K 5101/20 ,7)相對已在丨〇5°C乾燥2小時的物質 •8)相對已在1000"C焙焼2小時的物質 特別的耐濕氣包裝 i:i〇)在水:乙醉爲丨:丨的溶液中 I;,11)在經燃燒失重之組成物中的HC1含量 (請先閲讀背面之注意事項再填寫本頁) 訂 fc適用中國國家揉準(CNS)A4规格( 210X297公釐)_ _ B7 五、發明説明(14 ) 二氧化矽的製備是將液體矽化合物噴灌進由氫氣及空 氣構成的氧氫火焰中》大部份情形是使用四氯化矽來進行 。該物質會爲在氫氧反應當中形成的水所作用而水解成二 氧化矽和氫氯酸。在移離火焰後,二氧化矽會進入一個所 謂的凝結帶,其中一級氣矽(Aerosi 1 )顆粒及一級氣矽 凝塊會燒結在一起。在此階段以一種氣溶膠形式存在的產 物會在旋風器與伴隨的氣態物質分離開來,然後以經水氣 加熱的空氣來作後處準。 利用該製程可使殘餘的氫氯酸含量降低到0.025 %。由於在該製程結束時獲得之二氧化矽的鬆散密度僅約 1 5 g/ 1 ,故需進行後績的真空壓縮,因此可建立約 5 0 1或以上的壓實密度。 二氧化矽的粒徑可藉著反應條件-比如火焰溫度、氫 氣及氧氣的比例、四氯化矽的置、在火焰中的滯留時間或 凝結路徑的長度等-來加以變化。 BET表面稹是依據DIN 66 131使用氮氣 來測定的。 經濟部中央樣準局貝工消费合作杜印裝 (請先聞讀背面之注意事項再填寫本頁)m = 0 * 1, 2 * 3 9… 〇〇η = 0 1 1, 2 »3» • · · oo u = 0 > 1, 2 3 1 • · ·… oo Y = C Η 3, Η- C η Η 2 η Ten 1 n = 1 to 2 0 Υ = S i (C Η 3) 3 S i (c H 3) 2H, S i (C Η 3) 2 0 Η > S i (c H 3 ) 2 (〇c HS i (C Η 3) 2 (C ηΗ 2 n + 1) n = 1 to 2 0 R = alkyl 9 aryl (C Η 2) n — N Η 2, HR courtyard, aromatic (CH 2) n — NH 2 'HR • Uncle radical, aryl (CH 2) n NH 2' HR * »» = = alkyl, aryl, CC Η 2) n--N Η 2, H (Please read the precautions on the back before filling out this page) Employees' Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs of the People's Republic of China. The present invention also provides particles based on silica prepared by pyrolysis, which have the following physical and chemical properties: average Grain size: 10 to 120 // m BET surface area: 40 to 400m2 / g pore volume: 0 • 5 to 2 • 5 m 1 / S pore size distribution: pores with a diameter < 5 η m are less than 5 in the total pore volume % 9 the rest are medium — and huge holes Hole carbon content: 0 • 3 to 1 5 • 0 weight% P Η value: 3 • 6 to 8 • 5 perforation density: 2 2 0 to 7 0 0 S / liter The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) _ 12 Seal A7 B7, Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (ίο) The granular material of the present invention should have medium-sized and large holes, among which the medium-sized holes are contained in the entire hole volume Occupies 10 to 80%. The carbon content of the granular material of the present invention is between 0.3 and 15.0% by weight. The particle size distribution of the granular material of the present invention is 80% by volume, which will be greater than 8 m, and 80% by volume, which will be less than 96 # m. In a preferred system of the present invention, pores having a size of less than 5 Am occupy at most 5% of the total pore volume. The granular material of the present invention is prepared by dispersing silicon dioxide obtained by pyrolysis in water, spraying and drying the other particles, and heating the obtained particles to a temperature of 150 to 1, 100 ° C for 1 to 8 hours. And then silylation on each other. The silylation can be carried out as described above with respect to the halogenated silane, alkoxysilane, silamine and / or silane. The invention also provides a method for preparing the main particles of silicon dioxide obtained by pyrolysis, which is characterized in that the silicon dioxide obtained by pyrolysis is more preferably made of silicon tetrachloride by flame hydrolysis. The prepared silicon dioxide is distributed in water and spray-dried. The obtained particles can be selectively heated at 150 to 1, 100 ° C for 1 to 8 hours, and / or siliconized. The distribution liquid in water has a silicon dioxide concentration of 5 to 25% by weight. The spray-drying method can be performed at a temperature of 200 to 600 ° C. Rotary spraying device or spray spraying device can be used for this purpose. The heating of the particles can be carried out on a fixed bed such as a kiln, and on a moving bed. Please read the notes on the back before filling this page) 'Binding-13-Printed by A7 __B7 of the Consumer Cooperatives of the Central Procurement Bureau of the Ministry of Economic Affairs 5. Description of the Invention (11) Such as a rotary dryer. The silylation can be carried out as described above with a halogenated silane, alkoxysilane, silamane and / or silane, in which the silylating agent is selectively soluble in an organic solvent like ethanol. It is better to use silane i 108 [(CH30) 3-S i-C8H17], trimethoxyoctylsilane as the silylating agent. The silylation is carried out by spraying the particulate material together with the silylating agent, and then heat-treating the mixture at a temperature of 105 to 400 ° C for 1 to 6 hours. In another alternative method, the particles are silanized by treating the particulate material with a silylating agent in the form of a vapor, and then subjecting the mixture at a temperature of 200 to 800 ° C for 0.5 to 6 hours. Heat treatment. The heat treatment can be performed in a protective gas like nitrogen. Silaneization can be carried out in a flail or batch mode in a heatable mixer and dryer equipped with a spraying facility. Examples of suitable devices are plowshare mixers, rotary disk dryers or fluidized bed dryers. Physical and chemical variables of the particles, such as specific surface area, particle size distribution, pore volume, compacted density and concentration of silanol groups, pore distribution and P Η value-can be changed within a certain upper and lower limits by spraying the starting material, The conditions during heating and silylation vary. The granules of the invention can be used as supports for polymerization catalysts * especially as catalysts for the production of polyethylene. The advantages of the particles of the present invention are high purity, high thermal stability, low concentration of silanol groups, the shape of primary particles is microspheres and all pores (please read the notes on the back before filling this page) *? τ%: This paper uses China National Standard (CNS) A4 (210X297 mm) -14-__ B7_ V. Description of the invention (12) Less than 5% of holes in the volume exist < 5 nm diameter of. The invention additionally provides the use of particles as a catalyst support, especially for the preparation of polymerization catalysts. In a preferred system of the invention, the particles of the invention can be used as catalysts for the manufacture of catalysts for the production of polyethylene. Carrier. EXAMPLES The silicon dioxide obtained by the pyrolysis method used has the following physical and chemical properties. (Please read the notes on the back before filling in this page) The printed paper size of the Consumer Cooperatives of the Central Bureau of the Ministry of Economic Affairs of the People's Republic of China applies the Chinese national standard (CNS> A4 specification (210X297 mm) A7 B7 Invention Description (13 Ministry of Economy The Central Government Bureau of Standards and Consumers Cooperatives printed gas silicon 90 gas silicon 130 gas silicon 150 gas silicon 200 gas silicon 300 gas silicon 380 gas silicon 0X 50 CAS registration number 112945-52-5 (previous number S |: 7631-86 -9) Effect on water Loose white powder surface area BET) m2 / g 90 ± 15 130 ± 25 150 ± 15 200 ± 25 300 soil 30 380 ± 30 50 soil 15 average pore diameter of primary particles mm 20 16 14 12 7 7 • 40 Overdensity density 2) The normal person is g / 1 and the contractor is g / 1. Gamma " V, estimated Ι ·· 80 is estimated to be 50 estimated to be 120 estimated to be 50 estimated to be Π0 estimated to be 50 Estimated 120 Estimated 50 Estimated 120 Estimated 50 Estimated 120 Estimated 130 Weight loss on drying 3 > (105 hours at 1C)% < 1.0 < 1.5 < 0.59) < 1.5 < 1.5 < 1.5 < 1.5 Weight loss during combustion 4) 7) (2 hours at 1,000 ° c)% < 1 < 1 & l t; 1 < 1 < 2 < 2.5 < 1 pHfiS) (¢ 4% in aqueous distribution solution) > 3.6-4.5 3.6-4.3 3.6-4.3 3.6-4.3 3.6-4.3 36-4.3 3.6-43 Si02 '>% > 99,8 > 99.8 > 99.8 > 99,8 > 99.8 > 99.8 > 99.8 miscellaneous')% < 0.05 < 0.05 < 0.05 < 0.05 < 0.05 < 0.05 < 0.08 Fe20 ,,)% < 0.003 < 0.003 < 0.003 < 0.003 < 0,003 < 0.003 < 0.01 Ti02% < 0.03 < 0.03 < 0.03 < 0.03 < 0.03 < 0.03 < 0.03 HC1,) n)% < 0.025 < 0.025 < 0.025 < 0.025 < 0.025 < 0.025 < 0.025 Those who have been sieved out of size (according to Mocker, 45 μπι)% < 0.05 < 0.05 < 0.05 < 0,05 < 0.05 < 0.05 0.2 2) According to ISO 787 / XI, JIS K 5101 / 丨 8 (unscreened) 3) According to DIN ISO 787/1 丨 .ASTM D 28 (UIS KL 5101/21 4) According to DIN 55921, ASTM D 1208, JIS KK 5101/23 5) According to DIN ISO 787 / IX, ASTM D 1208, MS K 5101/24. 6) According to DIN ISO787 / XVm, JIS K 5101 / 20, 7) Relatively dried material at 丨 05 ° C for 2 hours • 8) Relatively dried material at 1000 " C for 2 hours Special moisture resistance Packaging i: i〇) in water: acetic acid solution 丨: 丨 I ;, 11) HC1 content in the composition after burning weight loss (please read the precautions on the back before filling this page) Order fc applies China National Standard (CNS) A4 (210X297 mm) _ _ B7 V. Description of the invention (14) The preparation of silicon dioxide is to spray liquid silicon compounds into an oxygen-hydrogen flame composed of hydrogen and air. The situation is to use silicon tetrachloride. This substance is hydrolyzed to silicon dioxide and hydrochloric acid by the water formed during the hydrogen-oxygen reaction. After moving away from the flame, the silicon dioxide will enter a so-called condensation zone, in which the first-stage gas silicon (Aerosi 1) particles and the first-stage gas silicon clot will sinter together. At this stage, the product in the form of an aerosol is separated from the accompanying gaseous material in the cyclone, and is then reconditioned with water-heated air. Using this process can reduce the residual hydrochloric acid content to 0.025%. Since the bulk density of the silicon dioxide obtained at the end of the process is only about 15 g / 1, a subsequent vacuum compression is required, so a compacted density of about 501 or more can be established. The particle size of silicon dioxide can be changed by reaction conditions such as flame temperature, hydrogen and oxygen ratio, placement of silicon tetrachloride, residence time in the flame or length of condensation path, etc. The BET surface radon is determined according to DIN 66 131 using nitrogen. Dumpling Packing for Shellfish Consumer Cooperation of the Central Bureau of Procurement, Ministry of Economic Affairs (Please read the notes on the back before filling this page)

孔洞容稹是由微-、中等一及巨大孔洞容積的總和來 計算得到。巨大-及中等孔洞是藉著記錄N 2等溫線和以 B E T、de Boer 和 Barrett、 Joyner 及 Halenda 的方法來 對其作評估下測得的。D> 3 0 nm的巨大孔洞是以Hg 孔率方法來測定。爲了要測定巨大孔洞*使樣品在1 〇 〇 °C的乾燥烘箱中進行1 5小時的乾燥’並在室溫及抽真空 下排氣。爲了要測定微一及中等孔洞,使樣品在1 〇 〇°C 本紙張尺度適用中國國家揉準(CNS ) A4規格(210X297公釐) -17 - 經濟部中央梂準局貝工消費合作社印製 A7 B7 五、發明説明(15 ) 的乾燥烘箱中進行1 5小時的乾燥法,並且在2 0 0 1及 抽真空下進行1小時的排氣。 矽烷醇基團濃度是以丙氨酸鋰方法來測定。S i 0H 一基團在此會與L i A 1 H4作用,而在反應當中形成的 氨氣量由壓力來測定。 測量原則 將顆粒材料稱重並加進四頸瓶中。對瓶子抽真空,以 及使油浴加熱到1 5 0°C。瓶中的溫度(由內部溫度計來 控制)會鼸著油的溫度上升到約13 0°C。起始處理當中 的壓力是使用壓力量測裝置P I2(TM2 1 0,購自 Ley bo Id,量測範圍1 03至1 0_3毫巴)來記錄。水份的 解吸可由壓力置測來監控。在起始處理結束後(在終點溫 度達3 0分鐘),所必須達到的壓力要小於1 0 _2毫巴。 在起始處理完成後,經抽真空的瓶子是藉著關閉停止 閥來與真空元件分離,並使其回復正常溫度。實際的置測 是依據對經由滴液漏斗被加進瓶中之L i A 1 H4溶液的 置測數量,而壓力上升是由所形成的氫氣來量測。如果已 知瓶子的容積,則Η 2數量可由理想氣體定律來計算。壓 力是使用量測範圍在0和1巴之間的數位量測裝置( PIi) (MKS 儀器 PR— 2000)來記錄。 所用的L i A 1 H4溶液(2%L i A 1 114溶於二甘 醉二甲醚)在實驗進行之前有先排氣以便除去隨時會揮發 的成份,後者會使壓力童測發生錯誤。基於該目的,則以 本紙張尺度適用中國國家標準(CNS )八4規格(210X297公釐) 18 - - - n I— n —1 n il n n n I n ϋ I I T ---------I - - I I I (請先閲讀背面之注意事項再填寫本頁) 經濟部t央橾準局貝工消费合作杜印製 A7 _B7_ 五、發明説明(16 ) 第二個真空幫浦來使滴液漏斗中溶液上方的壓力下降到蒸 氣壓(22 °C時爲3. 7毫巴),如此液體將會沸騰。在 無樣品下進行一個空白量測以試驗溶液的排氧是否足夠。 在測定氫氣壓力時,使用溶液的蒸氣壓來作修正。 解讅 首先藉著測定配備有磨砂口瓶塞之滴液漏斗的容積, 精確計量表成升的容稹,來對裝置作校正。只要停止閥是 由下列資驗獲得,則反應瓶的容稹將包括所有的連接點: 將大氣壓下充滿空氣的滴液漏斗連接到經抽真空的瓶 子上。然後兩個容稹之間的壓力對消是藉著開啓滴液漏斗 的栓來達到。所建立的壓力是由數位式量測裝置來指示。 反應容器的容稹是由質量平衡來獲得。在該布置下可獲得 等於243 . 8毫升的容稹VR。 所形成的氫氣莫耳數由下列方程式獲得: n = ^ RT V修JH. = Vr - V囲- V»液 P是反應瓶的壓力增加量。該值有以相當於溶劑蒸氣壓( 22 °C時爲37毫巴)的量來修正。在與22 °C差異很大 之室溫下的蒸氣壓是由蒸氣壓表來取得。選擇經稱重的樣 品有助於獲得在2 0 0和8 0 0毫巴間的P值。此時由於 溫度變化而在蒸氣壓上的些微改變對結果將幾乎沒有任何 (請先閲讀背面之注意事項再填寫本頁) 裝- 、π 4 本紙張尺度適用中國國家標準(CNS )八4規格(210X 297公釐) -19 - A7 B7_ 五、發明説明(17 ) 效果。 反應容器的容稹是藉著減去固體材料的容稹及所加入 溶液的容稹來修正。前者是由經稱重比例來獏得,而密度 及後者則是由滴液漏斗來讀得。 矽烷醇基團的密度最後可由下列方程式獲得:The pore volume is calculated from the sum of the volume of micro-, medium one and huge pores. Huge- and medium holes were measured by recording the N 2 isotherms and evaluating them using the methods of B E T, de Boer and Barrett, Joyner, and Halenda. D > The huge pores at 30 nm were measured by the Hg porosity method. In order to measure the huge holes *, the samples were dried in a drying oven at 1000 ° C for 15 hours' and vented at room temperature and under vacuum. In order to determine the micro and medium holes, the sample is at 100 ° C. The paper size is applicable to the Chinese National Standard (CNS) A4 (210X297 mm). -17-Printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards, Ministry of Economic Affairs A7 B7 5. In the drying oven of the description of invention (15), the drying method is performed for 15 hours, and the exhaust is performed for 1 hour under 2000 and vacuum. The silanol group concentration was measured by the lithium alanine method. The S i 0H group interacts with L i A 1 H4, and the amount of ammonia gas formed during the reaction is measured by pressure. Principles of measurement Weigh the particulate material and add it to a four-necked flask. Vacuum the bottle and heat the oil bath to 150 ° C. The temperature in the bottle (controlled by the internal thermometer) raises the temperature of the oil to approximately 130 ° C. The pressure during the initial treatment was recorded using a pressure measuring device P I2 (TM2 1 0, purchased from Ley bo Id, measuring range 10 3 to 10 3 mbar). Desorption of water can be monitored by pressure measurement. After the end of the initial treatment (at the end temperature of 30 minutes), the pressure that must be reached is less than 10 2 mbar. After the initial treatment is completed, the evacuated bottle is separated from the vacuum element by closing the stop valve and allowed to return to normal temperature. The actual measurement is based on the amount of L i A 1 H4 solution added to the bottle via the dropping funnel, and the pressure rise is measured by the hydrogen formed. If the volume of the bottle is known, the number of Η 2 can be calculated from the ideal gas law. Pressure is recorded using a digital measuring device (PIi) (MKS Instrument PR-2000) with a measuring range between 0 and 1 bar. The L i A 1 H4 solution (2% L i A 1 114 dissolved in diethylene glycol dimethyl ether) was vented before the experiment was carried out in order to remove any components that would volatilize at any time, which would cause errors in the pressure test. For this purpose, the Chinese National Standard (CNS) 8-4 specification (210X297 mm) is applied at this paper size. 18---n I— n —1 n il nnn I n ϋ IIT --------- I--III (Please read the notes on the back before filling out this page) Ministry of Economic Affairs, Central Bureau of quasi-bureau, Shellfish consumer cooperation, Du printed A7 _B7_ V. Description of the invention (16) The second vacuum pump is used for dripping The pressure above the solution in the funnel dropped to vapor pressure (3.7 mbar at 22 ° C), so the liquid would boil. Perform a blank measurement without the sample to test whether the solution has sufficient oxygen evolution. When measuring the hydrogen pressure, the vapor pressure of the solution is used for correction. Solution: First, the device was calibrated by measuring the volume of the dropping funnel equipped with a frosted stopper and accurately measuring the volume of the liter. As long as the stop valve is obtained by the following tests, the contents of the reaction bottle will include all connection points: Connect an air-filled drip funnel to the evacuated bottle. The pressure cancellation between the two containers is then achieved by opening the stopper of the drip funnel. The established pressure is indicated by a digital measuring device. The volume of the reaction vessel is obtained by mass balance. In this arrangement, a volumetric VR equal to 243.8 ml is obtained. The mole number of hydrogen formed is obtained from the following equation: n = ^ RT V repair JH. = Vr-V 囲-V »Liquid P is the pressure increase of the reaction flask. This value is corrected by an amount corresponding to the solvent vapor pressure (37 mbar at 22 ° C). Vapor pressure at room temperature, which is very different from 22 ° C, is obtained from a vapour pressure gauge. Choosing a weighed sample helps to obtain a P value between 2000 and 800 mbar. At this time, slight changes in vapor pressure due to temperature changes will have almost no effect on the results (please read the precautions on the back before filling this page).--Π 4 This paper size applies to China National Standard (CNS) 8-4 specifications. (210X 297mm) -19-A7 B7_ V. Description of the invention (17) Effect. The capacity of the reaction vessel is corrected by subtracting the capacity of the solid material and the capacity of the added solution. The former is obtained by weighing proportions, while the density and the latter are read by dropping funnels. The density of the silanol groups is finally obtained from the following equation:

η · N L d = -η · N L d =-

F 羅修密德(Lohschmidt)數 F:經稱重固體材料的表面 樣品依下列方式來處理: 在120 °C及0 . 2毫巴下加熱1小時:冷卻到60 °C;加入LiAlH4; 10分鐘後,讀出已上升的壓差 9 經濟部中央橾窣局負工消費合作社印袈 (請先閲讀背面之注意事項再填寫本頁)F Lohschmidt number F: The surface sample of the weighed solid material is processed as follows: heating at 120 ° C and 0.2 mbar for 1 hour: cooling to 60 ° C; adding LiAlH4; after 10 minutes , Read out the rising pressure difference 9 The seal of the Consumer Affairs Cooperative of the Central Government Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page)

A 粒徑分布是以雷射光學粒徑分析儀Cilas Granulame-tre715來測定。 穿孔容稹是依據ASTM D 4164—88來測 定*A Particle size distribution was measured with a laser optical particle size analyzer, Cilas Granulame-tre715. Perforation capacity is measured in accordance with ASTM D 4164-88 *

窗:購自Engelsmann的穿孔容置計S T A V 2003,依據 DIN 53194,第 5. 2 節 ,b — f來進行 本紙張尺度適用中國國家標準(CNS ) A4规格(2丨OXW7公釐) -20 - 經濟部中央橾準局貝工消費合作社印袈 Α7 Β7 五、發明説明(18 ) 2 5 0毫升量筒,刻度記號爲2毫升 天平,最大誤差上下限爲±0 . 1克 程序 將穿孔容童計的計數設定爲1 〇 〇 〇個鳴響。 扣除量筒重量。 將顆粒材料放進量筒中’最髙達2 5 0毫升的標記。 記錄樣品的重量(±0.1克)。 將量筒放在容量計中,並打開裝置的開關。 穿孔結束:裝置會在1 0 〇 0個鳴響以後自動切掉。 穿孔本體容積讀到1奄升的精確值· 計簏 E :顆粒材料的經稱重部份,表成克 V:容積讀值,表成毫升 W :水份含置,表成重置% (依據說明書P 0 〇 1來 測定) E X ( 1 0 0 - W ) 穿孔密度-- V X 1 0 0 當疏水性催化劑載體是在水:乙醇爲1:1的溶液中 時,則P Η值是對4%含水布液測定的。 本紙張尺度適用中國國家標準(CNS ) Α4規格(2丨0Χ297公釐) ----;---.--{裝-------,ΤΓ---^----4" (請先閲讀背面之注意事項再填寫本頁) -21 - A7 ____B7__ 五、發明説明(I9 ) 本發明顆粒的製備 使以經熱解法製得之二氧化矽完全分布在蒸餾水中》 使用依據轉子/固定子原則操作的分布用凝塊在本製程中 。使所形成的懸浮液進行噴灑乾燥。以過濾器或旋風器來 使最終產物沉澱下來· 使經噴灑的顆粒在隔焰爐中加熱。 將經噴灑乾燥法及選擇性加熱的顆粒放置在用於矽烷 化方法的混合器中,並在密集混合下可選擇性地首先與水 和然後與矽烷S i 1 0 8 (三甲氧基辛基矽烷)或 HMD S (六甲基二矽氨烷)一起噴灑·在完成噴灑後, 使材料進行1 5至3 0分鐘或以上的混合,然後加熱到 1 0 0至4 0 0 °C達1至4小時。 所用的水可以酸,比如氫氯酸,來酸化以使p Η值由 7變成1。所用的矽烷化劑可溶解在像乙醇的溶劑中· (請先聞讀背面之注意事項再填寫本頁) 經濟部中央橾準局貞工消費合作杜印製 本紙張尺度適用中國國家標準(CNS ) Α4規格(210'〆297公釐) -22 - A7 五、發明説明(20 ) 經濟部中央揉準局貝工消费合作社印製 染 實施例 對照用 1 2 3 4 對照用 5 起始氣矽 380 380 380 380 380 噴灞乾燥數據 Η2ο量(公斤) 10 10 105 105 15 氣矽量(公斤) 1.5 1.5 14.7 14.7 1.5 霧化使用 轉盤 轉盤 轉盤 轉盤 轉盤 操作酿rc) 380 380 380 440 380 廢氣獄(。〇 105 105 105 108 105 沉澱作用 過濾器 過濾器 過濾器 過濾器 旋風器 加熱數據(小時/°c) - - 2/700 2/700 - 表面修飾數據 試劑 Si 108 Si 108 HMDS • 數量[克/100克氣砂] 25 25 20 - 水量[克/100克氣矽] - - 5 5 - 加熱時間(小時) 2 2 4 - 酿 ΓΟ - 120 120 140 - 物理化學性質 it'- ^ΕΤ表面積(米2/克) 350 197 189 212 277 扎洞容積(毫升/克) 2.09 1.69 1.55 1.68 1.69 孔洞<5 rnn的孔洞容積(佔全部孔 n.d. 1.8 n.d. n.d. n.d. 磨额的%) 2-30 nm的中等孔洞(毫升/克) 1.34 1.04 1.12 1.17 0.66 yOnm的巨大孔洞(毫升/克) 0.75 0.65 0.43 0.51 1.03 ite50 _ 38 40 66 53 39 倉扎容積(克/升) 320 390 420 370 260 •Ϋ?·: _ 4.7 5.0 5.6 7.2 4.8 mm % - 10.9 10.4 3.8 - ρ院醇基國濃度(毫莫耳OH/克) 1.80 1.18 0.74 0.37 1.50 (請先閲讀背面之注意事項再填寫本頁) .裝- *νβ 本紙張尺度適用中'國國家標準(CNS〉A4規格(210X297公釐) -23 -Window: Perforated volume meter STAV 2003 purchased from Engelsmann, according to DIN 53194, section 5.2, b-f. This paper size applies Chinese National Standard (CNS) A4 specification (2 丨 OXW7 mm) -20- Printed by the Central Bureau of Standards, the Ministry of Economic Affairs, Shellfish Consumer Cooperatives, 袈 Α7 Β7 V. Description of the invention (18) 250 ml measuring cylinder, scale mark is 2 ml balance, the maximum error upper limit is ± 0.1. The count is set to 1,000 beeps. Deduct the weight of the graduated cylinder. Place the particulate material into the graduated cylinder 'up to a mark of 250 ml. Record the weight of the sample (± 0.1 g). Place the measuring cylinder in the volume meter and turn on the device. End of piercing: the device will automatically cut off after 100 beeps. The volume of the perforated body reads an accurate value of 1 liter. 簏 E: The weighted part of the granular material, expressed in grams. V: Volume reading, expressed in milliliter. W: Moisture content, expressed as reset%. ( Measured according to the instruction P 0 〇1) EX (100-W) Perforation density-VX 1 0 0 When the hydrophobic catalyst support is in a solution of water: ethanol 1: 1, the P P value is 4% aqueous cloth solution. This paper size applies Chinese National Standard (CNS) A4 specification (2 丨 0 × 297 mm) ----; ---.-- {装 -------, ΤΓ --- ^ ---- 4 " (Please read the precautions on the back before filling this page) -21-A7 ____B7__ V. Description of the invention (I9) The preparation of the particles of the present invention allows the silica obtained by pyrolysis to be completely distributed in distilled water. The rotor / stator principle operates with distributed clots in this process. The formed suspension was spray-dried. A filter or cyclone is used to settle the final product. The sprayed particles are heated in a muffle furnace. The spray-dried and selectively heated granules are placed in a mixer for the silylation process and, under intensive mixing, can be selectively mixed with water and then with silane Si 1 0 8 (trimethoxyoctyl) Silane) or HMD S (Hexamethyldisilazane) spraying together. After spraying, the material is mixed for 15 to 30 minutes or more, and then heated to 100 to 4 0 0 ° C for 1 To 4 hours. The water used can be acidified, such as hydrochloric acid, to change the pΗ value from 7 to 1. The silylating agent used can be dissolved in solvents such as ethanol ) Α4 size (210'〆297mm) -22-A7 V. Description of invention (20) Printing and dyeing examples of the Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, Printing and dyeing Examples for comparison 1 2 3 4 For comparison 5 Initial gas silicon 380 380 380 380 380 Spray drying data 2 kg (kg) 10 10 105 105 15 Gas silicon volume (kg) 1.5 1.5 14.7 14.7 1.5 Atomization using turntable turntable turntable turntable turntable operation RC) 380 380 380 440 380 waste gas ( 〇 105 105 105 108 105 Precipitation filter filter Filter filter Cyclone heating data (hour / ° c)--2/700 2/700-Surface modification data reagent Si 108 Si 108 HMDS • Quantity [g / 100 g of air sand] 25 25 20-water content [g / 100 g of air silicon]--5 5-heating time (hours) 2 2 4-brewing ΓΟ-120 120 140-physical and chemical properties it'- ^ ΕΤ surface area (meter 2 / g) 350 197 189 212 277 Pore volume (ml / g) 2.09 1.69 1.55 1.68 1.69 Pore volume of holes < 5 rnn (% of total nd 1.8 ndndnd grinding amount) Medium pores (ml / g) 2-30 nm 1.34 1.04 1.12 1.17 0.66 yOnm's huge holes (ml / g) 0.75 0.65 0.43 0.51 1.03 ite50 _ 38 40 66 53 39 Barn volume (g / l) 320 390 420 370 260 • Ϋ? ·: _ 4.7 5.0 5.6 7.2 4.8 mm%-10.9 10.4 3.8-Concentration of Alcohol-Based Countries (millimolar OH / g) 1.80 1.18 0.74 0.37 1.50 (Please read the precautions on the back before filling out this page). Packing-* νβ This paper is applicable to the national standard (CNS) 〉 A4 size (210X297mm) -23-

7 B 五、發明説明(21 ) 經濟部中央橾隼局貝工消費合作社印製 實施例 6 7 8 對照用 9 10 起始氣砂 300 300 300 0 X 50 0 X 50 喷灑乾燥數據 H2o量 (公斤) 15 105 105 10 10 氣砂量 (公斤) 1.5 14.7 14.7 1.5 1.5 霧化使用 轉盤 單一噴嘴 雙_ 轉盤 轉盤 操作離ΓΟ 380 440 440 380 380 廢氣溫度(。〇 105 108 108 105 105 沉澱作用 旋風器 過濾器 過濾器 旋風器 旋風器 加熱數據(小時/°c) 2/700 表面修飾數據 試劑 HMDS Si 108 HMDS HMDS 數量[克/100克氣矽] 15 25 20 - 3 水量[克/100克氣矽] 5 5 5 - - 加熱時間(小時) 4 2 4 5 m. ro 140 120 140 - 140 物理化學性質 BET表面積(米2/克) 222 180 195 46 41 孔洞容積(毫升/克) 1.79 1.49 1.51 0.73 0.68 孔洞<5 nm的孔洞容積(佔全部孔 n.d. 1.7 1.5 n.d. 1.2 洞容積的%) 2-3〇nm的中等孔洞(毫升/克) 0.78 0.60 0.60 0.08 0.09 >30nm的巨大孔洞(毫升/克) 1.01 0.89 0.91 0.65 0.59 粒徑d5Vm) 32 40 43 21 21 穿孔容積(克/升) 290 320 300 540 570 pH値 6 5.2 6.9 5.3 7.4 碳含量% 2.7 9.3 3.3 - 0.5 矽烷醇基團濃度(毫莫耳OH/克) 0.61 1.15 0.40 0.29 0.14 (請先閲讀背面之注意事項再填寫本頁) -se 本紙張尺度逋用中國國家標準(CNS ) A4規格(2丨OX 297公釐) B7 五、發明説明(22 ) 經濟部中央標準局貝工消費合作社印装 實施例 對照用 11 12 對照用 13 14 起始氣矽 130 130 200 200 噴灑乾燥數據 H2o量 (公斤) 15 115 15 15 氣砂量 (公斤) 1.5 1.5 1.5 1.5 霧化使用 轉盤 轉盤 轉盤 轉盤 操作溫度(。〇 380 380 380 380 廢氣Μ (。〇 105 105 105 105 沉澱作用 旋風器 旋風器 旋風器 旋題 加熱數據(小時/°C) - - - 表面修飾數據 試劑 HMDS HMDS 數量[克/100克氣矽] - 5 - 7 水量[克/100克氣矽] - - - - 加熱時間(小時) - 5 - 5 mt co - 140 - 140 物理化學性質 BET表面積(米2/克) 131 111 196 153 孔洞容積(毫升/克) 1.92 1.62 2.25 2.04 孔洞<5 run的孔洞容積(佔全部孔 洞容積的%) n.d. 1.7 n.d. 0.9 2-30 run的中等孔洞(毫升/克) 0.24 0.24 0.46 0.47 >30mn的巨大孔洞(毫升/克) 1.68 1.38 1.79 1.57 立徑d50 (μηι) 20 20 14 14 穿孔容積(克/升) 250 280 230 240 pH値 4.8 7.3 4.8 7.2 碳含量% - 1.3 - 1.7 砂烷醇基團濃度(毫莫耳OH/克) 0.83 0.44 1.16 0.56 -----^---Γ---- (請先閲讀背面之注意事項再填寫本頁) 訂 i.feN_ 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -25 - A7 ___B7 _ 五、發明説明(23 ) 依據實施例1至14獲得之顆粒的粒徑分布以表格及 圖1至4圖形表示· 實施例1、5、9、1 1及1 3爲先前技藝的對照實 施例(DE-A 3 6 1 1 449 Liu)。 本發明顆粒作爲製備聚乙烯之催化商[截醬的用涂窗施例 參考活性成份鈦,催化劑在乙烯聚合化時可達到以下 的結果: (請先閲讀背面之注意事項再填窝本頁) 經濟部中央棣準局貝工消費合作杜印製 催化劑在載體 上的實施例 產置 公斤PE/ 克鈦 評 論 實施例1 2 9 2 只用如實施例1之經噴 灑乾燥的載髖 實施例2 3 6 9 如實施例4之經化學處 理的載體 實施例3 3 7 6 如實施例6之經熱處理 和化學處理的載體 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 26 附件一(A):第 85101073 年;j R:㈣-補充 p年1月呈 i、發明說明(24 ) 阖式簡要說明 圖1係爲以表格及圖式表示之依據本發明實施例1g 4所獲得之顆粒的粒徑分布。 圖2係爲以表格及圖式表示之依據本發明實施例5至 8所獲得之顆粒的粒徑分布。 圖3係爲以表格及圖式表示之依據本發明實施例9至 11所獲得之顆粒的粒徑分布。 圖4係爲以表格及圄式表示之依據本發明實施例12 至14所獲得之顆粒的粒徑分布。 (請先閱讀背面之注意事項再填寫本頁) 装【·!--- -- 訂·111111· 經濟部智慧財產局員Η消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -26-1 -7 B V. Description of the invention (21) Example 6 printed by the Shellfish Consumer Cooperative of the Central Bureau of the Ministry of Economic Affairs 7 7 8 Controlled 9 10 Initial air sand 300 300 300 0 X 50 0 X 50 Spray drying data H2o amount ( Kg) 15 105 105 10 10 Air sand volume (kg) 1.5 14.7 14.7 1.5 1.5 Atomization using a turntable single nozzle double _ turntable turntable operation away from ΓΟ 380 440 440 380 380 exhaust gas temperature (.105 105 108 105 105 precipitation cyclone Filter filter cyclone cyclone heating data (hours / ° c) 2/700 surface modification data reagent HMDS Si 108 HMDS HMDS quantity [g / 100g gas silicon] 15 25 20-3 water volume [g / 100g gas silicon ] 5 5 5--Heating time (hours) 4 2 4 5 m. Ro 140 120 140-140 Physical and chemical properties BET surface area (m2 / g) 222 180 195 46 41 Pore volume (ml / g) 1.79 1.49 1.51 0.73 0.68 pores < 5 nm pore volume (% of all pores nd 1.7 1.5 nd 1.2% of pore volume) medium pores (mL / g) of 2-3nm 0.78 0.60 0.60 0.08 0.09 > 30nm huge pores (mL / Gram 1.01 0.89 0.91 0.65 0.59 Particle size d5Vm) 32 40 43 21 21 Perforation volume (g / l) 290 320 300 540 570 pH 値 6 5.2 6.9 5.3 7.4 Carbon content% 2.7 9.3 3.3-0.5 Silanol group concentration (millimolar) OH / g) 0.61 1.15 0.40 0.29 0.14 (Please read the notes on the back before filling in this page) -se This paper size uses the Chinese National Standard (CNS) A4 specification (2 丨 OX 297 mm) B7 V. Description of the invention (22) Example of printing by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs for comparison 11 12 for comparison 13 14 Initial gas silicon 130 130 200 200 Spray drying data H2o amount (kg) 15 115 15 15 Air sand amount (kg) 1.5 1.5 1.5 1.5 Atomization using turntable turntable turntable turntable operating temperature (. 〇 380 380 380 380 Exhaust gas M (. 105 105 105 105 105 Precipitation cyclone cyclone cyclone spin title heating data (hour / ° C)---Surface modification data reagent HMDS HMDS quantity [g / 100g gas silicon] -5-7 Water content [g / 100g of silicon gas]----Heating time (hours)-5-5 mt co-140-140 Physical and chemical properties BET surface area (m2 / g) 131 111 196 153 Pore volume ( Ml / g) 1.92 1.62 2.25 2.04 pore volume of the 5 run (% of total pore volume) nd 1.7 nd 0.9 2-30 run medium pore (ml / g) 0.24 0.24 0.46 0.47 > 30mn (Ml / g) 1.68 1.38 1.79 1.57 Vertical diameter d50 (μηι) 20 20 14 14 Perforation volume (g / l) 250 280 230 240 pH 値 4.8 7.3 4.8 7.2 Carbon content%-1.3-1.7 Concentration of salanol groups ( Millimolar OH / g) 0.83 0.44 1.16 0.56 ----- ^ --- Γ ---- (Please read the notes on the back before filling out this page) Order i.feN_ This paper size applies Chinese national standards ( CNS) A4 specification (210X297 mm) -25-A7 ___B7 _ V. Description of invention (23) Basis The particle size distributions of the particles obtained in Examples 1 to 14 are shown in tables and graphs in Figures 1 to 4. Examples 1, 5, 9, 11 and 13 are comparative examples of the prior art (DE-A 3 6 1 1 449 Liu). The granules of the present invention are used as catalysts for the preparation of polyethylene. [The example of coating the window with cutting sauce refers to the active ingredient titanium. The catalyst can achieve the following results during the polymerization of ethylene: (This page)) Example of production of printed catalysts on a carrier by the Central Ministry of Economic Affairs of the Central Bureau of Quasi-Continent Bureau of Industrial Engineering. Production of kilograms of PE per gram of titanium. Comments on Examples 1 2 9 2 Use only the spray-dried carrier as in Example 1. Hip Example 2 3 6 9 The chemically-treated carrier as in Example 4 Example 3 3 7 6 The heat-treated and chemically-treated carrier as in Example 6 This paper applies Chinese National Standard (CNS) A4 specifications (210X297) 26) Appendix I (A): 85101073 year; j R: ㈣-supplement p in January, i. Description of the invention (24) Brief description of the formula Figure 1 shows the implementation of the invention in the form of tables and diagrams Particle size distribution of the particles obtained in Example 1g 4. Fig. 2 shows the particle size distributions of the particles obtained according to Examples 5 to 8 of the present invention in the form of a table and a diagram. FIG. 3 shows the particle size distribution of the particles obtained according to Examples 9 to 11 of the present invention in the form of a table and a diagram. FIG. 4 is a particle size distribution of the particles obtained in accordance with Examples 12 to 14 of the present invention in the form of a table and formula. (Please read the precautions on the back before filling this page) Install [·! ----Ordered · 111111 · Printed by a member of the Intellectual Property Bureau of the Ministry of Economic Affairs and printed by a consumer cooperative. The paper size applies to China National Standard (CNS) A4 (210 X 297 mm) -26-1-

Claims (1)

A8 B8 C8 D8 補炙 經濟部中央標準局員工消費合作社印装 瑣婧委員明示,本鉍修正後是否變更庳實对、内容 六、申請專利範 圍 1 附 件一 第 85101073 號 專 利 串 請 案 1 中 文 串 請 專 利範 圍 修 正 本 V { I 請 1 I 民國 8 8 年 6 月 呈 先 閲 1 | 讀 1 背 1 面 | 之 1 1 • 種以經 熱 解 法 製得 之 二 氧 化 砂爲 主 的 顆 粒 它 注 旁 1 Ψ 1 具 有下 列 的 物理化 學 性 質 項 1 '1 平 均晶 粒 大 小 1 0 至 12 0 β m 4 ( 寫' 本 裝 I B E T 表 面積 4 0 至 4 0 0 m 2/ g 貝 1 1 孔 洞 容 積 0 * 5 至2 • 5 m 1 / g ί 1 孔 徑 分 布 直 徑 &lt; 5 η m 的 孔 洞 在 全 1 I 部 孔 洞 容積 中 小於 5 % t 訂 I 其 餘 爲 中等 — 及 巨 大 孔 洞 1 1 I P Η 值 3 6 至8 5 1 1 穿 孔 密 度· 2 2 0 至7 0 0 g / 升 1 1 2 — 種月 3以 製 備 如 串 請 專 利 範 圍 第1 項 之 顆 粒 的 方 Λ 1 法 ,其 特 徵 爲使以 經 熱 解 法 製 得 之 二 氧 化矽 分 布 在 水 中 且 1 I 進 行噴 灑 乾 燥 以 及 使 所得 顆 粒 加 熱 到 15 0 至 I 1 ,1 0 0 °C達1 至 8 小 時 0 1 .I I 3 — 種用以 製 備 如 中 請 專 利 範 圍 第1 項 之 顆 粒 的 方 1 法 ,其 特 徵 爲使以 經 熱 解 法 製 得 之 二 氧 化矽 分 布 水 中 且 進 1 行 噴灑 乾 燥 ,以及 使 所 得 顆 粒 進 行 矽 院 化作 用 0 1 4 • 一 種用以 製 備 如 中 請 專 利 範 圍 第1 項 之 顆 粒 的 方 1 | 法 ,其 特 徵 爲使以 經 熱解 法 製 得 之 二 氧 化矽 分 布在水 中 且 1 1 本紙張尺度適用中國國家梯準(CNS ) A4規格(210X297公釐) A8 B8 C8 D8 補炙 經濟部中央標準局員工消費合作社印装 瑣婧委員明示,本鉍修正後是否變更庳實对、内容 六、申請專利範 圍 1 附 件一 第 85101073 號 專 利 串 請 案 1 中 文 串 請 專 利範 圍 修 正 本 V { I 請 1 I 民國 8 8 年 6 月 呈 先 閲 1 | 讀 1 背 1 面 | 之 1 1 • 種以經 熱 解 法 製得 之 二 氧 化 砂爲 主 的 顆 粒 它 注 旁 1 Ψ 1 具 有下 列 的 物理化 學 性 質 項 1 '1 平 均晶 粒 大 小 1 0 至 12 0 β m 4 ( 寫' 本 裝 I B E T 表 面積 4 0 至 4 0 0 m 2/ g 貝 1 1 孔 洞 容 積 0 * 5 至2 • 5 m 1 / g ί 1 孔 徑 分 布 直 徑 &lt; 5 η m 的 孔 洞 在 全 1 I 部 孔 洞 容積 中 小於 5 % t 訂 I 其 餘 爲 中等 — 及 巨 大 孔 洞 1 1 I P Η 值 3 6 至8 5 1 1 穿 孔 密 度· 2 2 0 至7 0 0 g / 升 1 1 2 — 種月 3以 製 備 如 串 請 專 利 範 圍 第1 項 之 顆 粒 的 方 Λ 1 法 ,其 特 徵 爲使以 經 熱 解 法 製 得 之 二 氧 化矽 分 布 在 水 中 且 1 I 進 行噴 灑 乾 燥 以 及 使 所得 顆 粒 加 熱 到 15 0 至 I 1 ,1 0 0 °C達1 至 8 小 時 0 1 .I I 3 — 種用以 製 備 如 中 請 專 利 範 圍 第1 項 之 顆 粒 的 方 1 法 ,其 特 徵 爲使以 經 熱 解 法 製 得 之 二 氧 化矽 分 布 水 中 且 進 1 行 噴灑 乾 燥 ,以及 使 所 得 顆 粒 進 行 矽 院 化作 用 0 1 4 • 一 種用以 製 備 如 中 請 專 利 範 圍 第1 項 之 顆 粒 的 方 1 | 法 ,其 特 徵 爲使以 經 熱解 法 製 得 之 二 氧 化矽 分 布在水 中 且 1 1 本紙張尺度適用中國國家梯準(CNS ) A4規格(210X297公釐) ABCD 393448 六、申請專利範圍 進行噴灑乾燥,以及使所得顆粒加熱到1 5 0至 1 ,100°C達1至8小時和接著進行矽烷化作用。 5.—種用以製備如申請專利範圍第1項之以經熱解 法製得的二氧化矽爲主之顆粒的方法,其特徵爲使以經熱 解法製得之二氧化矽一較宜爲以火焰水解法由四氯化矽製 備得到的二氧化矽一分布在水中,進行噴涵乾燥法,可選 擇性使所得顆粒加熱到15 0至1,100°C達1至8小 時及/或進行矽烷化作用· 6 ·如申請專利範圍第1項之顆粒,其係用作催化劑 載體,尤其供以製備聚合催化劑。 7 .如申請專利範圔第1項之顆粒,其係作爲製造供 製備聚乙烯用之催化劑的催化劑載體· ---------裝---:---ΓΙ1Τ------^ (請先閲讀背面之注意事項再本頁) 經濟部中央梯準局貝工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -2 -A8 B8 C8 D8 The member of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs, printed a member of Zou Jing, clearly stated whether the amended bismuth will be changed, the content is 6, the scope of patent application 1 Appendix 1 No. 85101073 Patent String Request 1 Chinese String Please revise the scope of the patent. V {I Please 1 I June 1988 First Read 1 | Read 1 Back 1 Side | of 1 1 • A kind of particles mainly composed of sand dioxide obtained by pyrolysis method. 1 Ψ 1 has the following physicochemical properties 1 '1 Average grain size 1 0 to 12 0 β m 4 (Write' IBET surface area 4 0 to 4 0 0 m 2 / g shell 1 1 Pore volume 0 * 5 To 2 • 5 m 1 / g ί 1 pore diameter & <5 η m Less than 5% of the product t Order I the rest are medium — and huge holes 1 1 IP Η value 3 6 to 8 5 1 1 perforation density · 2 2 0 to 7 0 0 g / liter 1 1 2 — seed month 3 to prepare as The method of claim Λ 1 for the granules of the patent scope is characterized in that the silicon dioxide obtained by the pyrolysis method is distributed in water and spray-dried at 1 I, and the obtained granules are heated to 15 0 to I 1, 1 0 0 ° C for 1 to 8 hours 0 1 .II 3 — a method 1 for preparing particles such as those in the patent claim 1, which is characterized by the distribution of silica obtained by pyrolysis Spraying and drying in water, and siliconizing the obtained particles 0 1 4 • A method 1 | for preparing particles such as the first item in the patent scope, which is characterized by using a pyrolysis method The obtained silica is distributed in water and the size of 1 1 paper is suitable. China National Ladder Standard (CNS) A4 specification (210X297 mm) A8 B8 C8 D8 Compensation printed by member of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economy Scope 1 Attachment 1 No. 85101073 Patent String Request 1 Chinese String Request Patent Scope Amendment V {I Please 1 I Republic of China 1986 Submitted First Read 1 | Read 1 Back 1 Side | No. 1 1 Granules based on sand dioxide obtained by the solution. It has the following physical and chemical properties. 1 '1 The average grain size 1 0 to 12 0 β m 4 (Write' IBET surface area 4 0 to 4 0 0 m 2 / g shell 1 1 hole volume 0 * 5 to 2 • 5 m 1 / g ί 1 pore size distribution diameter &lt; 5 The holes of η m are less than 5% of the total volume of the holes in the whole part I. The order I is medium and the rest are medium—and the huge holes 1 1 IP Η value 3 6 to 8 5 1 1 perforation density · 2 2 0 to 7 0 0 g / liter 1 1 2 — month 3 method for preparing granules such as those in the patent claim 1, characterized in that the silicon dioxide obtained by pyrolysis is distributed in water and 1 I is spray-dried and dried The granules obtained are heated to 150 to I 1, 1 0 0 ° C for 1 to 8 hours 0 1 .II 3-a method 1 for preparing granules as described in item 1 of the Chinese patent application, characterized in that The silica dioxide produced by the pyrolysis method is distributed in water and spray-dried, and the obtained particles are siliconized. 0 1 4 • A method 1 for preparing particles such as the first item in the patent scope | , Which is characterized by the second Silicon oxide is distributed in water and 1 1 paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm) ABCD 393448 6. Spraying and drying range for patent application, and heating the obtained particles to 150 to 1,100 ° C for 1 to 8 hours and subsequent silylation. 5. A method for preparing particles mainly composed of silicon dioxide obtained by pyrolysis as described in item 1 of the scope of patent application, which is characterized in that silicon dioxide obtained by pyrolysis is more preferably The silicon dioxide prepared from the silicon tetrachloride by the flame hydrolysis method is distributed in water, and the spray drying method is performed to selectively heat the obtained particles to 150 to 1,100 ° C for 1 to 8 hours and / or Carrying out silanization · 6 · The granules according to item 1 of the scope of patent application are used as catalyst carriers, especially for preparing polymerization catalysts. 7. The granule according to item 1 of the patent application, which is used as a catalyst carrier for the manufacture of a catalyst for the production of polyethylene. --------- pack ---: --- ΓΙ1Τ ---- -^ (Please read the notes on the back first, and then this page) The paper size printed by the Central Laboratories of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, is applicable to the Chinese National Standard (CNS) A4 (210X297 mm) -2-
TW85101073A 1996-01-29 1996-01-29 Granules based on pyrogenically prepared silicon dioxide, method for their preparation and use thereof TW393443B (en)

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