TW446570B - Molten metal filtration - Google Patents

Molten metal filtration Download PDF

Info

Publication number
TW446570B
TW446570B TW87119689A TW87119689A TW446570B TW 446570 B TW446570 B TW 446570B TW 87119689 A TW87119689 A TW 87119689A TW 87119689 A TW87119689 A TW 87119689A TW 446570 B TW446570 B TW 446570B
Authority
TW
Taiwan
Prior art keywords
filter
refractory
container
molten metal
porosity
Prior art date
Application number
TW87119689A
Other languages
Chinese (zh)
Inventor
Steven Ray
Edwin Paul Stankiewicz
Original Assignee
Foseco Int
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Foseco Int filed Critical Foseco Int
Application granted granted Critical
Publication of TW446570B publication Critical patent/TW446570B/en

Links

Abstract

Molten metal is filtered using a filter (10, 28, 44) comprising a porous carbon foam substrate coated substantially throughout with a refractory metal or refractory compound formed by chemical vapour deposition, and having a filtration porosity of less than 90%, and preferably at least 75%, and a ligament solid fraction of at least 0.95, using apparatus comprising a holding vessel (1, 21, 40) having an inlet (2, 41) and an outlet (3, 22, 42) for the molten metal, at least one filter housing, the or each housing containing a filter (10, 28, 44), means for holding and sealing the filter or filters (10, 28, 44) in place, and means (5, 38) for preheating the holding vessel (1, 21, 40) and the filter or filters (10, 28, 44) prior to using the apparatus for filtering molten metal.

Description

蛭濟部中央橾準局員工消費合作社印製 44657 0 Α7 Β7 五、發明説明(/) 本發明關於熔融金屬之過濾,特別是熔融鋁金屬及 熔融鋁合金之過濾,本發明將特別參照上述金属加以說 明β 熔融金屬,特別是鋁金屬多年來以多種不同過濾裝 5 置加以過濾,且現今在鋁金屬工業中一般在鑄造前會過 濾熔融鋁金屬及熔融鋁合金。雖然過去已然有多種類型 之過濾器,現今最常使用者為陶瓷泡沫材料*其藉由聚 氨酯泡沫材料浸溃一種包含耐火材料及一黏结劑之漿艘 然後烘乾該浸溃後泡沫材料構成*且黏著微粒材料之過 10 濾器係由耐火材料及一黏結剩混合而成,以擠壓方式使 該混合物形成一所要形狀*並加熱該形狀。 陶瓷泡沫材料過濾器及其在熔触金屬過濾中之用途 揭示於數個美因專利案中,例如3090094,38939Π, 3947363,4024056,5190897 及 5520823 中•美國專利 15 案4024056中揭示一種斜面可移除阳瓷泡沫材料濾板之 應用,該板具有每公分直線約2-18孔或每英吋直線約 5-45孔(5-45ppi)之孔尺寸,此類型過濾器廣泛應用 於熔触鋁金屬之過濾中》 美國專利案3524548揭示一種鋁金屬所用之剛性多 20 孔過濾器媒艎,其藉由耐火材料粒子與一種抵抗熔融鋁 金屈之玻璃材料結合在一起製成》此種過濾器製作成一 板或營狀而使用。美國專利案3747765揭示用以過濾熔 融金屬之剛性過濾管,其由一種相似之耐火粒子摻和劑 與一預先熔合玻璃黏結劑結合在一起製成· 25 美國專利案4964993揭示之熔融金屬過濾器中包含 本紙張尺度逋用中國®家橾率(CNS)iM規格(210X297公釐) 〔讀先閱讀背面之注意事項再填寫本頁) -* 4465 7 0 經濟部中央標準局貝工消費合作杜印衷 A7 B7 五、發明説明(>) 至少一圓柱形末端封閉多孔陶瓷過濾器元件,該元件以 一垂直方位連結至一本質上水平多孔陶瓷密封板過濾器 元件。該垂直過濾器元件可由粘合之微粒耐火材料製 成*或者其可能為一陶瓷泡沫材料形式β 5 陶瓷泡洙材料過濾器已然在過去多年令成功地應用 於商業上,因為其相較於粘合微粒過濾器較易於使用, 成本低且單元留跡(unit footprint)較小。然而其孔 尺寸大於粘合微粒過濾器,因此其過濾效能較低。陶瓷 泡沫材料過濾器以約細到每公分24孔或每英吋60孔 10 ( 6〇PPi )廣泛應用。然而其在孔尺寸減少時會變得越 加難以製造,因為越加難以使較細孔尺寸之聚氨酯泡沫 材料浸潰耐火材料漿«。阻塞之孔數增加使可用以過濾 之多孔性降低》如此導致每單位表面積之流速減少,且 會在注入期間產生使用問題或使過濾能力降低。 15 粘合微粒過濾器在作為熔駐鋁金屬之過濾器時提供 數個超越陶瓷泡沫材料之優點。其大體上具有較高強度 及較大密度,且由於其具有較低之多孔性,具有一較曲 折流道且不包含阻塞孔,其在自鋁金屬中去除氧化物及 其他夹雜物方面提供一較大過濾效能。 20 然而粘合微粒過濾器之大密度及低多孔性(典型為 30-4596)會是不利條件,且限制其商業使用。由於粘合 微粒迤濾器較啕瓷泡沫材料輞密,其明顯需要更多預熱 以在過濾開始時達到該過濾器之完全灌注並使過濾性能 最佳化,而要快速且均勻達到其所要求之預熱相當困 25 難。某些粘合微粒過濾器亦具有因其預熱需求而來之其Printed by the Consumers' Cooperative of the Central Bureau of Health of the Ministry of Economic Affairs 44657 0 Α7 Β7 V. Description of the invention (/) The invention relates to the filtration of molten metal, especially the filtration of molten aluminum metal and molten aluminum alloy. The present invention will make special reference to the above metals It is explained that β molten metal, especially aluminum metal, has been filtered by many different filtering devices for many years, and now in the aluminum metal industry, molten aluminum metal and molten aluminum alloy are generally filtered before casting. Although there have been many types of filters in the past, the most common users today are ceramic foam materials * which are impregnated by a polyurethane foam material with a slurry vessel containing a refractory material and a binder and then dried by the impregnated foam material * In addition, the filter with adhesive particle material is made of a mixture of refractory material and a sticky residue, and the mixture is extruded to form a desired shape * and the shape is heated. Ceramic foam filters and their use in molten metal filtration are disclosed in several main patent cases, such as 3090094, 38939Π, 3947363, 4024056, 5190897, and 5520823 • US Patent 15 Case 4024056 discloses a slantable surface In addition to the application of ceramsite foam material filter plate, the plate has a hole size of about 2-18 holes per centimeter straight line or about 5-45 holes (5-45ppi) per inch straight line. This type of filter is widely used in fused aluminum In the filtration of metals "US Patent No. 3524548 discloses a rigid 20-hole filter media used in aluminum metal, which is made by combining refractory particles with a glass material resistant to molten aluminum and gold flexion" Made into a plate or camp and used. U.S. Pat. No. 3747765 discloses a rigid filter tube for filtering molten metal, which is made by combining a similar refractory particle admixture with a pre-fused glass binder. 25 U.S. Pat. No. 4,964,993 in a molten metal filter Contains the paper size of China® CNS iM specification (210X297 mm) [Read the precautions on the back before filling in this page]-* 4465 7 0 The Central Bureau of Standards, Ministry of Economic Affairs A7 B7 5. Description of the invention (>) At least one cylindrical end encloses the porous ceramic filter element, which is connected to a substantially horizontal porous ceramic sealing plate filter element in a vertical orientation. The vertical filter element may be made of bonded particulate refractory material * or it may be in the form of a ceramic foam material. Β 5 ceramic foam material filters have been successfully used commercially for many years because they are Synthetic particulate filters are easier to use, less costly, and have a smaller unit footprint. However, its pore size is larger than that of a bonded particulate filter, so its filtration efficiency is lower. Ceramic foam filters are widely used with a thickness of about 24 holes per cm or 10 (60 PPi) per inch. However, it becomes more difficult to manufacture as the cell size decreases, as it becomes more difficult to impregnate the finer cell size polyurethane foam with the refractory slurry «. Increasing the number of blocked pores reduces the porosity available for filtration. This results in a decrease in the flow rate per unit surface area, which can cause usage problems during injection or reduce filtration capacity. 15 Bonded particulate filters provide several advantages over ceramic foam when used as a filter for aluminum alloys. It generally has higher strength and higher density, and because of its lower porosity, it has a more tortuous flow channel and does not contain blocked pores. It provides the ability to remove oxides and other inclusions from aluminum metal. A larger filtration efficiency. 20 However, the high density and low porosity (typically 30-4596) of bonded particulate filters can be disadvantageous and limit their commercial use. Because the bonded particulate filter is denser than the ceramic foam material, it obviously requires more preheating to achieve the filter's full filling at the beginning of the filtration and optimize the filtering performance, and to quickly and uniformly meet its requirements Preheating is quite difficult and difficult. Some bonded particulate filters also have their own pre-heating requirements

本紙張尺度適用中國B家揉牟(CNS) A4洗格(2丨0X297公釐J (請先閱讀背面之注意事項再填寫本頁) 訂 線 446570 經濟部中央標準局貝工消费合作社印装 Α7 Β7 五、發明説明(>) 他缺點。舉例來說,當其以平板形式應用於鋁金屬鑄造 廠過濾設備中時,必須將該板預熱以許可熔融鋁金屬流 過該板而不凝固。該板之此種預熱通常由在該板底部表 面上之直接火焰接觸達成,由於某些粘合微粒濾板之熱 5 陡震阻力極差,會導致該濾板剝蝕》 粘合微粒過濾器之高密度亦使改變粘合微粒過濾器 元件成為一種非常勞力密集之作業。低多孔性不僅限制 每單位表面積之流速,亦增加該粘合微粒過濾器孔内之 格隙金屬速度。為克服該受限流速之問題,有必要利用 10 —種具有一非常大表面積之粘合微粒過濾器系統。此項 一般利用數捆長管完成,其需要利用一個具有一極大留 跡之箱子或容器》 在曰本專利申請案公開No. 1-141884中已提出以 —碳泡沫材料基體作為熔融金屬之過濾器,該基體經化 15 學蒸汽溉積法塗佈碳化矽。所塗佈材料具有90至99% 之多孔性,且該申請案中有說明在過濾熔融鋁金屬時若 該多孔性小於90X則對孔之阻塞及鋁金屬之損失會極 大’而若該多孔性超過99X則去除雜質之效能會很差且 該泡沫材料之強度會有所不足。 20 相較於B本專利申請案公開No.卜141884中所教 授之内容,今發現過瀘熔融金屬特別是熔融鋁金屬之較 佳過淥器可藉由以下方式製造:藉由化學蒸汽澱積法在 一碳泡洙材料基艘上澱積一耐火金屬或耐火化合物,只 要該過濾器之過濾多孔性小於90¾且具有一至少〇. 95 25 之繫帶實《率。 本紙張尺度適用令國國家揲準(CNS ) Μ规格(210X297公釐) (請先閱1*背面之注意事項再填寫本頁) ^ 訂 ! 446570 A7 B7 經濟部中央標準局負工消費合作杜印製 五、發明说明(江) 在此依據本發明提出一種過濾熔融金屬之方法,該 方法包含提供一種過濾器,該過濾器包含一種藉由化學 蒸汽濺積法大致全然塗佈一耐火金屬或耐火化合物之多 孔碳泡沫材料基體,該過濾器具有如下文中定義之小於 5 90¾之過濾多孔性,且具有如下文中定義之至少〇. 95之 繫帶實體率,且導致熔融金屬流過該過濾器以去除該熔 融金屬中所包容之夾雜物。 在本發明之内文中一繫帶(liganent)定義為構成 一泡沫材料之結構之某一大致實體交互連結支柱。 10 過ί慮多孔性(f i 1 trat ion porosi ty )定義為一泡 沫材料過濾器體在該繫帶外部且可用以過濾熔融金屬之 開放交互連結空間之總容積百分比· 空體率(void fraction)為一泡洙材料過濾器體 内空置空間之總容積除以該泡洙材料過濾器艎所佔用體 15 積,且一泡沫材料過濾器《内之空置空間為任何非實體 之容積。舉例來說,對一尺寸為100公厘X 100公厘X 100公厘且容有850000立方公厘空置空間之泡洙材料 過濾器«而言,其空體率為850000Λ100χ ΙΟΟχ 100) 或 0.85 · 20 空體率得以下式表示: 空體率=1 ~泡洙材料過瀘器《密度 泡沫材料繫帶理綸密度 舉例來說,一個質量420公克之100公厘X 1〇〇公 厘X 100公厘泡沫材料過濾器艎之密度為0.42公克/ 25 立方公分。若該泡沫材料為一鋁泡沫材料,其繫帶理論 (請先閲讀背面之注意事項再填寫本頁) 訂 線This paper size is suitable for Chinese B homes (CNS) A4 washing grid (2 丨 0X297mm J (please read the precautions on the back before filling in this page) Line 446570 Printed by the Cooper Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Β7 V. Description of the invention (>) Other disadvantages. For example, when it is used in the form of a flat plate in the filtering equipment of an aluminum metal foundry, the plate must be preheated to allow molten aluminum metal to flow through the plate without solidifying. This kind of preheating of the plate is usually achieved by direct flame contact on the bottom surface of the plate. Due to the extremely poor shock resistance of some bonded particle filter plates, the filter plate will be peeled off. The high density of the filter also makes changing the bonded particulate filter element a very labor-intensive operation. The low porosity not only limits the flow rate per unit surface area, but also increases the velocity of the gap metal in the pores of the bonded particulate filter. To overcome The problem of this limited flow rate necessitates the use of 10 types of bonded particulate filter systems with a very large surface area. This is generally done using several bundles of long tubes, which requires the use of a A box or container that remains "In Japanese Patent Application Publication No. 1-141884, it has been proposed that a carbon foam substrate is used as a filter for molten metal, and the substrate is coated with silicon carbide by a chemical vapor deposition method. The applied material has a porosity of 90 to 99%, and the application states that if the porosity is less than 90X when filtering molten aluminum metal, the blockage of pores and the loss of aluminum metal will be extremely large. Above 99X, the efficiency of removing impurities will be poor and the strength of the foam material will be insufficient. 20 Compared to the content taught in B Patent Application Publication No. Bu 141884, today it has been found that molten metal, especially molten A preferred converter for aluminum metal can be manufactured by depositing a refractory metal or a refractory compound on a carbon foam substrate based on chemical vapor deposition, as long as the filter has a filtration porosity of less than 90 ¾ And has a tie rate of at least 0.925. The paper size is applicable to the national standard (CNS) M specifications (210X297 mm) (please read the precautions on the back of 1 * before filling this page) ^ Order! 446570 A7 B7 Du printed by the Central Bureau of Standards of the Ministry of Economic Affairs and Consumer Cooperation. 5. Description of the Invention (Jiang) Herein, a method for filtering molten metal is proposed according to the present invention. The method includes providing a filter that includes a method of splashing by chemical vapor. The product method is substantially completely coated with a porous carbon foam material matrix of a refractory metal or a refractory compound. The filter has a filtration porosity of less than 5 90¾ as defined below, and has a banded solid rate of at least 0.95 as defined below. And cause molten metal to flow through the filter to remove inclusions contained in the molten metal. In the context of the present invention, a ligament is defined as a substantially solid interconnecting pillar that forms the structure of a foam material . 10 Fi 1 trat ion porosi ty is defined as the percentage of the total volume of a foam filter body outside the band that can be used to filter molten metal in the open interactive connection space · void fraction The total volume of the empty space in a foam filter is divided by the volume occupied by the foam filter, and the empty space in a foam filter is any non-solid volume. For example, for a foam material filter with a size of 100 mm X 100 mm X 100 mm and containing 850,000 cubic meters of vacant space «, its empty body rate is 850,000 Λ100χ ΙΟχχ 100) or 0.85 · 20 Void ratio can be expressed as follows: Void ratio = 1 ~ foaming material filter "Density foam material with nylon density. For example, a mass of 420 grams of 100 mm X 100 mm X 100 The density of the millimeter foam filter 艎 is 0.42 g / 25 cubic centimeters. If the foam material is an aluminum foam material, its lace theory (please read the precautions on the back before filling this page)

. -I 本紙張尺度遘用中國國家標^|t(CNS)A4¾格( 210X297公釐> ί 446570 Α7 Β7 經濟部中央標準局員工消費合作社印製 五、發明説明(ί) 密度為2.8公克/立方公分,因此其空體率為ΙΟ. 42/2. 8) 或 0. 85 » 繫帶實體率定義為構成繫帶之固體材料容積除以繫 帶所佔用之容積。 5 舉例來說,一個繫帶容積為150000立方公厘且繫 帶實體容積為75000立方公厘之100公厘X 100公厘X 100公厘過濾器具有0.50之繫帶實艘率。 較佳來說本發明方法中所用過滤器具有至少75¾之 過濾多孔性,至少80X為更佳。 10 該碳泡沫材料較佳為一網狀碳泡沫材料,且該多孔 碳基艘可能由一多孔有機基《之熱解作用構成。舉例來 說,一聚氨酯泡沫材料經過熱解,且若有需要該聚氨酯 泡沫材料可能首先浸溃一樹脂或一相似有機材料。歐洲 專利申請案公告No. 747124A揭示一種生產一碳泡沫材 15 料之適當方法,其中聚氨酯泡沫材料浸溃一樹脂,且該 浸溃樹脂後之泡沫材料以600至120(TC溫度熱解以將 聚氨酯及樹脂轉變為碳。 本文所用之化學蒸汽激積法(chemical vapour deposi t ion ) —詞包括化學蒸汽Λ積及化學蒸汽渗入。 20 在化學蒸汽激積法中固相耐火材料自氣相先導物集結成 長,舉例來說一碳化矽塗層可能藉由甲取三氯硅之分解 澱積在一多孔碳基《上。該化學蒸汽澱積可能由任何習 知技術實行之,且以化學蒸汽澱積法塗佈碳基艎之適當 方法揭示於美國專利案5154970,5283109,5372380, 25 及歐洲專利申請案公告No. 747124Α t。 本紙張尺度適用中困Η家標準(CNS > A4规格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) 訂 線-I This paper is in Chinese national standard ^ | t (CNS) A4¾ grid (210X297mm) ί 446570 Α7 Β7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of invention (ί) Density is 2.8 grams / Cubic centimeter, so its empty body ratio is 10. 42/2. 8) or 0.85 »Lace solid rate is defined as the volume of solid material constituting the lace divided by the volume occupied by the lace. 5 For example, a 100mm X 100mm X 100mm filter with a strap volume of 150,000 cubic millimeters and a strap solid volume of 75,000 cubic meters has a tie rate of 0.50. Preferably, the filter used in the method of the present invention has a filtration porosity of at least 75 °, more preferably at least 80X. 10 The carbon foam material is preferably a reticulated carbon foam material, and the porous carbon-based vessel may be composed of a porous organic matrix. For example, a polyurethane foam is pyrolyzed, and if necessary, the polyurethane foam may first be impregnated with a resin or a similar organic material. European Patent Application Publication No. 747124A discloses a suitable method for producing a carbon foam material, in which a polyurethane foam material is impregnated with a resin, and the resin impregnated foam material is pyrolyzed at a temperature of 600 to 120 (TC temperature to Polyurethanes and resins are converted to carbon. The chemical vapour depositon method used in this article — the term includes chemical vapor deposition and chemical vapor infiltration. 20 In the chemical vapor deposition method, solid-phase refractory materials are introduced from the gas phase. Aggregation and growth of materials, for example, a silicon carbide coating may be deposited on a porous carbon-based substrate by decomposition of trichlorosilane. The chemical vapor deposition may be performed by any conventional technique, and chemically A suitable method for coating carbon-based rhenium by the vapor deposition method is disclosed in U.S. Patent Nos. 5,154,970, 5,283,109, 5,372,380, 25 and European Patent Application Publication No. 747,124. T. This paper is sized to the standards of CNS > A4 (210X297mm) (Please read the precautions on the back before filling this page)

• —I— I 446570 經濟部中央標準局負工消费合作社印笨 A7 B7 五、發明説明“) 以化學蒸汽澱積法塗佈於該多孔碳基體上以生成過 濾器之耐火金屬或耐火化合物必須能與將被過濾之熔駐 金屬並存,亦即其必須抗拒該熔躲金屬,且其必須不污 染該熔融金屬。得以化學蒸汽溉積法施加於多孔碳基體 5 以生成本發明方法所用過渡器之对火金屬钇括媒及钥。 適當对火化合物包括碳化矽,氩化矽·碳化鋥,氮化锆, 硼化鍅,碳化鈮,氚化鈮,硼化鈮,碳化鈦,氮化鈦, 硼化鈦,碳化铪,氮化姶和硼化铪•較佳塗層材料為碳 化矽’因其具有適當物理特性如較小之密度及一高熱傳 10 導性,且使本發明方法中所用過濾器能夠合乎經濟效益 地製造。 明確地說,當本發明之方法利用一種已由化學蒸汽 激積法塗佈一耐火金屬或金屬化合物之網狀碳泡沫材料 實施時,該過瀘器具有數項優點超越以一有機泡沫材料 15 浸溃一微粒耐火材料漿Λ製成之習知陶瓷泡沫材料過濾 器。 所塗佈对火金屬或金屬化合物之澱積量較佳最小董 為0.25公克/立方公分。個別繫帶及過濾器體自身之 強度取決於塗伟於該繫资上之固Λ物質量。化學蒸汽激 20 精法之本質使得該碳泡沫材料整«之塗層密度可能有些 微差異,且若預期中塗層密度小於0.25公克/立方公 分則钕差異可觝導致該過濾器不具有充分抗飪強度以承 受工業環境。 個別繫帶若未塗佈足董耐火金屬或耐火化合物則可 25 能在處理中破裂,且一過濾器髏若不具有充分強度則可 本紙張尺度適用中國國家樣丰(CNS>A4规格(2丨0X297公釐) (請先閱讀背面之注意事項再填寫本頁) *τ 446 57 0 經濟部中夹標準局負工消费合作社印家 A7 B7 五、發明説明(9 ) 能在處理中破裂》在實務上發現用以在超過一星期以上 過濾熔融鋁金屬之過濾器需要有35公斤/平方公分 ( 500磅/平方英吋)之最小抗碎強度,而本發明方法 所用過濾器符合此需求。 5 就生產情況而言,本發明方法所用過濾器之一項重 要特質在於本質上該過濾器之所有空體率均可供熔融金 屬流使用,而該空體率一如先前所用定義之過濾多孔 性。就一恆定孔尺寸及表面積而言,可用多孔性越高會 使熔融金屬流速越高或格隊速度越低。一較低格陈速度 10 伴隨產生一較大熔融金屬内含物捕捉效能,因此使整體 過濾效能提高。該過濾器之多孔性較高亦產生一較大捕 捉内含物儲藏容積,如此意味著單一過濾器钜夠在其堵 塞且需要更換前過濾較大董之金屬〇 其舆習知陶瓷泡沫材料過濾器成為對比,該習知過 15 濾器在繫帶之中空t心部位内容有許多空隙,且成為該 繫帶自身之微多孔性》該空《I率部分為熔融金屬流所無 法使用,因為會需要高壓以迫使熔融金屬進入此種細微 管内,因此其不包括在過濾多孔性内》此外,許多空隊 因該陶瓷泡沫材料内形成之阻塞區域而變得無法供熔融 20 金屬流使用。如此更加降低舆該空想率相較之過濾多孔 性。 後附圈式之圖1和2顯示一習知陶瓷泡沫材料過濾 器與一本發明方法所用化學蒸汽澱積耐火金屬或耐火化 合物塗層碳泡沫材料過瀘器之對照。 25 囷1為一習知陶瓷泡沫材料過濾器之截面簡圖,該 本紙張尺度適用中國國家標车(CNS ) A4規格(2丨〇><297公釐) (請先閱讀背面之注意事項再填寫本頁) - -、?τ 4465 7 0 A7 B7 五、發明説明(?) 過渡器由一聚氨酯泡沫材料浸溃一陶瓷漿艟並點火燒熔 該泡沫材料製成〇該過濾器具有一中空繫帶核心(A) 和一容有空陈且實體率為〇· 50之陶瓷繫帶(β)β 圈2為一本發明方法所用之過濾器繫帶載面簡圖, 5 其以化學蒸汽激積法將一碳泡沫材料基體塗佈一耐火金 屬或耐火化合物製成。該過濾器具有一實體碳繫帶核心 (C)及一本質上無空陈之耐火金屬或耐火化合物(d) 繫帶塗層,該塗層之最小繫帶實髖率為0.95» 該繫帶内之空隙除降低過濾多孔性外,亦降低該陶 10 瓷泡洙材料過濾器醴之強度。 為艇應用於一工業過濾處理程序,一過濾器艟必須 有足夠強度且夠耐用以承受搬運,安裝及使用。就另一 方面而言,過濾器髏若要能有效地如一過濾器般運作則 必須具有一夠高過濾多孔性以備有低壓降及一最小過濾 15 系统留跡之工業流速下運作〇在其他參數相同時,過濾 器艘之空髏率越高則其強度趄低· 在本發明方法所用過濾器中,在100Χ之空體率加 入過濾多孔性時,對一給定空體率而言過濾器逋之強度 會達到最大值· 經濟部中央標準局貝工消费合作社印聚 (請先閱讀背面之注意事項再填寫本頁) 線 20 舉例來說,在製造本發明方法所用之一種碳化矽過 濾器時,一種名義上具有3%容積實體或97¾過濾多孔性 及本質上無空隙碳繫帶之碳泡沫材料以一均勻分布、本 質上無座陈碳化矽塗層塗佈至一 0.32公克/立方公分 之最小量。化學蒸汽液積碳化矽之一無空隙實體容積具 25 有3.2公克/立方公分之密度,且一 0.32公克/立方 本紙張尺度適用中國國家揉率(CNS> A4规格< 2丨0><297公釐) 446570 Α7 Β7 五、發明説明(^) 公分碳化矽塗層為一 10%容積為實體之碳化矽。實體之 總容積百分比為3¾碳及10%碳化矽。過濾器艘之空體率 為0.87,所有空體率均可供熔融金屬使用,是以該過 濾器之過濾多孔性為87¾。 5 過濾器内沒有黏結劑,沒有燒結輔助物(因為在過 濾器產生後沒有使該過濾器著火或燒結之需要),且沒 有雜質。因此該過濾器具有增進之與熔融金屬接觸之抗 蝕能力,且具有一較大的強度對重量比率。該過濾器與 一習知陶瓷泡沫材料過濾器相較具有較大強度及較小密 10 度。由於該過濾器之密度較小,其較易於預熱。 由於以上優點,當使用本發明方法時,可利用一種 較容有陶瓷泡沫材料過濾器或粘合微粒過濾器之系統具 有較高過濾效能及較長使用壽命之過濾系統。 本發明方法所用過濾器可能為平板形式,但其較佳 15 為管狀形式。在鋁工業中複數管一般稱為一心子 經濟部中央標準局員工消费合作社印製 (請先閱讀背面之注意事項再填寫本頁) 線 (cartridge)。雖然慣常使用平板過濾熔融鋁金屬,但 其有所缺陷,因為為提供充分過濾器表面積使大董熔融 鋁金屬能夠以一可接受生產速率處理,有必要使該濾板 製成非常大,且内部進行過濾之熔爐或容器亦要很大以 20 配合該濾板。因此之故有需要使用其形狀提供較大表面 積之過濾器,且其要求較少之配合空間,因此管狀或心 子過瀵器在以上考量中較為有利。 由習知陶瓷泡沫材料製成之管狀或心子過濾器之商 業用途甚小,因為此種過濾器難以製造,強度較低,有 25 阻塞孔,難以預熱且難以讓熔融金屬沾濕,且其僅適用 11 本纸張尺度適用中Η國家標率(CNS )八4规格Y21OX297公着) 446570 經濟部中央標準局貝工消費合作社印製 A7 B7 五、發明説明(f ts ) 於與熔融金屬接觸一段較短時間之應用。因此,商業上 應用於鋁工業中之管狀或心子過濾器通常為粘合微粒对 火過濾器。 以化學蒸汽澱積法塗佈一耐火金屬或耐火化合物且 5 具有小於9096過濾多孔性及至少0. 95繫帶實體率之碳 泡沫材料不受以上缺點困擾,這是其為何特別適合以管 狀或心子應用於本發明方法之原因。 過濾熔融金屬之方法舉例來說可能在包含以下構件 之過濾設備中賁施:一盛裝容器,其具有供該熔融金屬 10 使用之一入口及一出口;至少一過波器外軍,每·—外軍 容納一過濾器,該過濾器包含一以化學蒸汽澉積法大致 全然塗佈一耐火金屬或耐火材料之多孔碳泡沫材料基 逋,該基體具有小於90¾之過濾多孔性及至少0. 95之 繫帶實«率;將過濾器支承並密封於定位之裝置;及在 15 利用該設備過濾熔融金屬前预熱該盛裝容器及過濾器之 裝置。 因此,依據本發明之一進一步特質*在此提供一種 前述過濾熔融金屬之設備》 上迷設備中所用過濾器可能為濾板,但在一較佳貧 20 施例中使用過濾管,且該過濾器較佳來說為大致水平配 置管狀過濾器元件。 核密封裝置應能將該過瀘器密封於定位以確保所有 熔《金屬通過該過濾器而不對該過濾器施加過大力董, 且所用外罩及密封裝置之構形最好使該過濾器可輕易安 25 裝及移除。該加熱裝置舉例來說可能為一個或多個燃氣 本紙張尺度適用中國«家標率(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) 訂 線• —I— I 446570 Yin Ben A7 B7, Consumers Cooperative of Central Standards Bureau, Ministry of Economic Affairs 5. Description of the invention ") The chemical vapor deposition method must be applied to the porous carbon substrate to form a filter refractory metal or refractory compound. It can coexist with the molten metal to be filtered, that is, it must resist the molten metal, and it must not contaminate the molten metal. It can be applied to the porous carbon substrate 5 by a chemical vapor deposition method to form a transition device for the method of the present invention. The yttrium metal and yttrium are suitable for fire metal. Suitable fire retardant compounds include silicon carbide, silicon argon, hafnium carbide, zirconium nitride, hafnium boride, niobium carbide, niobium halide, niobium boride, titanium carbide, titanium nitride. , Titanium boride, hafnium carbide, hafnium nitride, and hafnium boride • The preferred coating material is silicon carbide because of its proper physical properties such as smaller density and a high thermal conductivity, and makes the method of the present invention The filters used can be manufactured economically. Specifically, when the method of the present invention is implemented using a reticulated carbon foam material that has been coated with a refractory metal or metal compound by a chemical vapor deposition method, This filter has several advantages over conventional ceramic foam filters made from an organic foam material 15 impregnated with a particulate refractory slurry Λ. The deposited amount of the coated refractory metal or metal compound is preferably the smallest. 0.25g / cm3. The strength of individual straps and filter bodies depends on the solid weight of Tu Wei's material in the system. Chemical vapor shock 20 The essence of fine method makes the carbon foam material «coating The density may be slightly different, and if the density of the intermediate coating is expected to be less than 0.25 g / cm3, the difference in neodymium may cause the filter to not have sufficient resistance to cooking to withstand the industrial environment. Or refractory compounds may break during processing, and if a filter skeleton does not have sufficient strength, this paper size can be applied to China National Sample (CNS > A4 specification (2 丨 0X297 mm) (Please read the back (Please note this page and fill in this page again) * τ 446 57 0 The Ministry of Economic Affairs of the China Standards and Standards Bureau, Consumers Cooperative, Ajia B7 B7 V. Description of the Invention (9) Can be broken in processing. Filters that filter molten aluminum for more than a week require a minimum crush strength of 35 kg / cm² (500 psi), and the filter used in the method of the present invention meets this requirement. 5 As far as production conditions are concerned, An important characteristic of the filter used in the method of the present invention is that essentially all the void fractions of the filter are available for molten metal flow, and the void fraction is as defined by the previously used filtration porosity. It is a constant pore size In terms of surface area, the higher the porosity, the higher the molten metal flow rate or the lower the cell speed. A lower cell speed10 is accompanied by a larger molten metal content capture performance, thus improving the overall filtration efficiency. The higher porosity of the filter also results in a larger storage volume for trapped inclusions, which means that a single filter will not be able to filter larger metals before they become clogged and need to be replaced. Its known ceramic foam material The filter becomes a contrast. The conventional 15 filter has many voids in the content of the hollow t center of the strap, and becomes the microporosity of the strap itself. Partly because molten metal flow cannot be used because high pressure will be required to force molten metal into such micro-tubes, so it is not included in the filtration porosity. In addition, many empty lines change due to the blocking area formed in the ceramic foam material. It cannot be used for molten 20 metal flow. This further reduces the fantasy ratio compared to the filtration porosity. Figures 1 and 2 at the back show a comparison of a conventional ceramic foam filter with a chemical vapor deposited refractory metal or refractory compound-coated carbon foam filter used in the method of the present invention. 25 囷 1 is a simplified cross-sectional view of a conventional ceramic foam filter. This paper size is applicable to China National Standard Car (CNS) A4 specifications (2 丨 〇 > < 297 mm) (Please read the note on the back first Please fill in this page again)--,? Τ 4465 7 0 A7 B7 V. Description of the invention (?) The transition device is made of a polyurethane foam impregnated with a ceramic slurry and fired and melted the foam material. The filter has a Hollow lacing core (A) and a ceramic lacing (β) β ring with a solid content of 0.50 are available. The schematic diagram of the filter lacing load surface used in the method of the present invention. The vapor deposition method is made by coating a carbon foam substrate with a refractory metal or a refractory compound. The filter has a solid carbon lace core (C) and a substantially no-laundry refractory metal or refractory compound (d) lace coating. The minimum true hip ratio of the coating is 0.95 »within the lace In addition to reducing the filtration porosity, the voids also reduce the strength of the ceramic 10 ceramic foam 洙 material filter 醴. For boats to be used in an industrial filtration process, a filter must be strong enough and durable enough to withstand handling, installation, and use. On the other hand, for the filter to function effectively as a filter, it must have a sufficiently high filtration porosity to provide low pressure drop and an industrial flow rate with a minimum filtration of 15 system traces. When the parameters are the same, the higher the cross section rate of the filter vessel, the lower the strength. In the filter used in the method of the present invention, when the filter porosity is added at a 100 dimensional void rate, the filter is filtered for a given empty rate. The strength of the device will reach its maximum value. Printed by the Central Laboratories of the Ministry of Economic Affairs of the Bayer Consumer Cooperative (please read the precautions on the back before filling this page). Line 20 For example, a silicon carbide filter used in the method of the present invention A carbon foam material with a nominally 3% volume solid or 97¾ filtration porosity and essentially void-free carbon lacing is coated with a uniformly distributed, essentially seatless, aged SiC coating to a thickness of 0.32 g / cubic The smallest amount in centimeters. One of the non-voided solid volumes of chemical vapor liquefied silicon carbide has a density of 3.2 grams per cubic centimeter, and a paper size of 0.32 grams per cubic centimeter applies to the Chinese national kneading rate (CNS > A4 specifications < 2 丨 0 > < 297 mm) 446570 Α7 Β7 V. Description of the invention (^) The silicon carbide coating with a centimeter is a solid silicon carbide with a volume of 10%. The total volume percentage of the entity is 3¾ carbon and 10% silicon carbide. The filter body has a hollow body ratio of 0.87. All hollow body ratios are available for molten metal. The filter porosity of the filter is 87¾. 5 There is no adhesive in the filter, no sintering aids (because there is no need to fire or sinter the filter after the filter is generated), and there are no impurities. Therefore, the filter has improved corrosion resistance in contact with molten metal, and has a large strength-to-weight ratio. Compared with a conventional ceramic foam filter, the filter has a stronger strength and a lower density of 10 degrees. Because the filter has a lower density, it is easier to preheat. Due to the above advantages, when the method of the present invention is used, a filtration system having a higher filtration efficiency and a longer service life than a system containing a ceramic foam filter or a particulate filter can be used. The filter used in the method of the invention may be in the form of a flat plate, but preferably it is in the form of a tube. In the aluminum industry, plural tubes are generally called Yixinzi. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page). Although it is customary to use a flat plate to filter molten aluminum metal, it has disadvantages because in order to provide sufficient filter surface area to enable Da Dong's molten aluminum metal to be processed at an acceptable production rate, it is necessary to make the filter plate very large and internally The furnace or container to be filtered must also be large to fit the filter plate. Therefore, it is necessary to use a filter whose shape provides a large surface area, and it requires less fitting space. Therefore, a tubular or cardiac filter is more advantageous in the above considerations. Tubular or cored filters made from conventional ceramic foam materials have very little commercial use because they are difficult to manufacture, have low strength, have 25 blocked holes, are difficult to preheat, and are difficult to wet molten metal. Only applicable to 11 This paper standard is applicable to China National Standards (CNS) 8 4 specifications Y21OX297 (publication) 446570 A7 B7 printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (f ts) In contact with molten metal For a short period of time. Therefore, tubular or core filters commercially used in the aluminum industry are usually bonded particulate to fire filters. A carbon foam material coated by a chemical vapor deposition method with a refractory metal or a refractory compound and having a filtration porosity of less than 9096 and a solid rate of at least 0.95 is not affected by the above disadvantages, which is why it is particularly suitable for tubular or Reasons for applying the method of the present invention. The method of filtering molten metal may be applied, for example, in a filtering device including the following components: a container having an inlet and an outlet for the use of the molten metal 10; at least one external wave transformer, each ... 95 The foreign army accommodates a filter that includes a porous carbon foam material base that is substantially completely coated with a refractory metal or refractory material by a chemical vapor deposition method, and the base has a filtering porosity of less than 90¾ and at least 0.95. The means for securing the belt; the device for supporting and sealing the filter in place; and the device for preheating the container and the filter before filtering the molten metal using the device. Therefore, according to a further feature of the present invention * here is provided a device for filtering molten metal as described above. The filter used in the above device may be a filter plate, but in a preferred embodiment, a filter tube is used, and the filter The filter is preferably a tubular filter element disposed substantially horizontally. The nuclear sealing device should be able to seal the filter in position to ensure that all molten metal passes through the filter without applying excessive force to the filter, and the configuration of the cover and sealing device used should preferably make the filter easily accessible. Install and remove. The heating device may be, for example, one or more gas. The paper size is applicable to the Chinese «house standard rate (CNS) A4 size (210X297 mm) (please read the precautions on the back before filling this page).

(Subniftted on MSchJ^ioil)(Subniftted on MSchJ ^ ioil)

Enel.⑴ 10 燃燒器或電熱器,其可能位於一裝在該盛裝容器頂部之 蓋子内。該過濾器位在該盛裝容器内關於該入口之位置 相s重要,如此當該盛裝容器經由該入口充滿熔融金屬 時’該盛裝容器内熔融金屬表面超過該過濾器之高度足 以灌注該過濾器,亦即開始讓熔融金屬流過該過濾器。 由於該盛裝容器之内表面必須承受熔融金屬如鋁金 屬且不應污染該金屬,該盛裝容器應以一耐火材料製成 或以一对火材料為襯裡’該耐火材料應符合以上需求。 為減少通過該盛裝容器壁體之熱損失,可能將一耐火熱 絕緣材料襯裡安裝於該盛裝容器外殼與該耐火襯裡之 間。同樣為減少熱損失亦可能以一熱絕緣材料作為該蓋 之襯裡。 構成該盛裝容器内部接觸金屬表面之適當耐火材料 實例為密度約1. 8公克/立方公分之溶凝娃石可鑄造材 料。該盛裝容器壁體及該蓋之熱絕緣材料實例為密度小 於1. 4公克/立方公分且亦具有包容塊狀或毯狀或模組 形式材料之陶瓷纖維之耐火可鑄'造材料。 圖式說明 請 先 閱 讀 背 Si 之 注 意 事 項 再 填 寫 頁 訂 t 經 20 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 25 本發明今參照附屬圖式圖3至7加以說明,圖中: 圖1為一習知陶瓷泡沫材料過濾器之截面簡圖; 圖2為一本發明方法所用之過遽器繫帶載1面簡圖; 圖3為一通過依據本發明容有複數過濾管之熔融金 屬過滤設備之水平截面圖; 圖4為一通過圖3設備之垂直載面圖; 13 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公* )Enel.⑴ 10 burner or electric heater, which may be located in a lid on top of the container. The position of the filter in the containment container with respect to the inlet is important, so that when the containment container is filled with molten metal through the inlet, 'the surface of the molten metal in the containment container exceeds the height of the filter enough to fill the filter, That is, starting to flow molten metal through the filter. Since the inner surface of the container must bear molten metal such as aluminum and should not contaminate the metal, the container should be made of a refractory material or lined with a pair of refractory materials. The refractory material should meet the above requirements. To reduce the heat loss through the wall of the containment container, a refractory insulation liner may be installed between the containment container shell and the refractory liner. It is also possible to line the cover with a thermal insulation material to reduce heat loss. An example of a suitable refractory material constituting the inner contacting metal surface of the container is a fused silica stone castable material having a density of about 1.8 g / cm3. An example of the thermal insulation material of the container wall and the lid is a refractory castable material made of ceramic fibers with a density of less than 1.4 g / cm3 and also containing materials in the form of blocks or blankets or modules. Schematic description Please read the precautions of Si before filling in the page t. Printed by the Ministry of Economic Affairs, Intellectual Property Bureau, Employees' Cooperatives 25 The present invention is described with reference to the accompanying drawings 3 to 7, which are as follows: A schematic cross-sectional view of a conventional ceramic foam material filter; FIG. 2 is a schematic view of a load carrying device used in the method of the present invention; FIG. 3 is a molten metal filtering device having a plurality of filter tubes according to the present invention Horizontal section view; Figure 4 is a vertical section view through the equipment of Figure 3; 13 This paper size applies to China National Standard (CNS) A4 specifications (210 X 297 mm *)

五、發明說明() 經濟部智慧財產局員工消費合作社印製 圖5巧一圖3熔融金屬過濾設備之詳細圖,其中顯 不該過濾管如何定位於該設備中並支承於定位; 圖6為一通過依據本發明之熔融金屬過濾設備另一 實施例之垂直截面圖;且 5 圖7為依據本發明之熔融金屬過濾設備又一實施例 之垂直載面圖。 詳細說明 今參照圖3至5,一種過濾熔融金屬之設備包含一 10对火襯裡容器卜一熔融金屬入口 2,一熔融金屬出口 3, 及一耐火襯裡蓋4’該蓋内具有加熱裝置5。容器1内部 以一耐火隔板8分隔為一入口室6和一出口室7,該隔 板橫越容器1延伸並接近該容器頂部,且其具有一孔9 連接入口室6和出口室7。一組十一個過濾管丨〇定位於 15容器1底座附近使過濾器管10排成向上堆疊之三排,該 過濾管為熱解網狀碳泡沫材料形式,已然經化學蒸汽澱 積法塗佈碳化矽’且具有87%之過濾多孔性及〇. 995之 、 繫帶實體率。每一過遽管1〇之一端插入一对火板11之 Λ 一凹口内,每一過濾管之另一端定位於一耐火板12之一 20 穿孔凹口内使該凹口内之孔與隔板8内之孔9對準。過 濾管10藉由支承裝置13支承並密封於定位而不對過濾 器管10施加過大力量,該支承裝置安裝於過濾器管1〇 上方接近該管鄰接隔板8孔9之末端t過濾管在容器 1内之位置使容器1頂部超過頂排過濾管1〇之高度足以 25 使該過濾器在入口室6充滿熔融金屬時得到灌注。 在用該設備以過濾熔融金屬前,容器1之内部及過 本紙張尺度適用中困國家標準(CNS>A4規格(210 X 297公爱) I------ l·--I > 裝!^----訂 i I----- (請先M讀背面之注意事項再填寫本頁)V. Description of the Invention () Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, Figure 5 and Figure 3, a detailed diagram of the molten metal filter equipment, showing how the filter tube is positioned in the device and supported in position; Figure 6 is A vertical cross-sectional view of another embodiment of a molten metal filtering device according to the present invention; and FIG. 7 is a vertical sectional view of another embodiment of the molten metal filtering device according to the present invention. DETAILED DESCRIPTION Referring now to Figures 3 to 5, a device for filtering molten metal includes a pair of 10 fire-lined containers, a molten metal inlet 2, a molten metal outlet 3, and a refractory lining cover 4 '. The cover has heating means 5 therein. The inside of the container 1 is divided into an inlet chamber 6 and an outlet chamber 7 by a refractory partition 8 which extends across the container 1 and approaches the top of the container, and has a hole 9 connecting the inlet chamber 6 and the outlet chamber 7. A group of eleven filter tubes are positioned near the base of 15 containers 1 so that the filter tubes 10 are arranged in three rows stacked upward. The filter tubes are in the form of pyrolytic reticulated carbon foam material and have been coated by chemical vapor deposition. Cloth silicon carbide 'and has a filtration porosity of 87% and a solid rate of 0.995. One end of each passing tube 10 is inserted into a notch of a pair of fire plates 11, and the other end of each filter tube is positioned in one of a refractory plate 12. 20 The perforated notch makes the hole in the notch and the partition 8 The inner hole 9 is aligned. The filter tube 10 is supported and sealed in position by applying a support device 13 without applying excessive force to the filter tube 10. The support device is installed above the filter tube 10 near the end of the tube adjacent to the 8 hole 9 of the partition plate. The filter tube is in the container. The position inside 1 makes the height of the top of the container 1 above the top row of filter tubes 10 high enough to allow the filter to be filled when the inlet chamber 6 is filled with molten metal. Before using this equipment to filter the molten metal, the internal standard of container 1 and the paper size are applicable to the national standard (CNS > A4 specification (210 X 297 public love) I ------ l · --I > Install! ^ ---- Order i I ----- (Please read the precautions on the back before filling in this page)

A “6570 經濟部中央標準局員工消費合作社印製 Α7 Β7 五、發明説明(丨、) 濾管10由加熱裝置5加以預熱,該加熱裝置舉例來說 可為燃氣燃燒器或電熱器。在熔融鋁金屬過濾之案例 中,對過濾管10之内表面而言有必要預熱到至少600 °C。加熱裝置5亦維持容器1上熔融金属之溫度· 5 使用時熔融金屬經由入口2進入入口室6,通過過 濾管10過濾,通過隔板8内之孔9進入出口室7,然 後經由出口 3排出該容器。 參照圖6, 一種用以過濾熔躲金屬之設備包含一耐 火槻裡容器21及一耐火襯裡蓋子23,該容器具有一熔 10 融金屬入口(圈中未示)及一熔融金屬出口 22。容器21 内部以一耐火隔板26分隔為一出口室24和一·入口室 25,該隔板橫越容器21延伸且具有一孔27連接出口室 24和入口室25。四個過濾管28為熱解網狀碳泡沫材料 形式,已然經化學蒸汽激積法塗佈碳化矽,且具有87¾ 15 之過瀘多孔性及0.995之繫帶實饉率,該過濾管以直線 排列定位於入口室25内接近容器21之底座。每一過濾 管28之一端插入一对火板29之一凹口内,且每一過濾 管之相反端定位於一耐火板30之一穿孔凹口内使該凹 口内之孔舆隔板26内之孔27對準《過濾管28藉由支 20 承裝置31支承並密封於定位而不對過濾器管28施加過 大力量,該支承裝置安裝於過濾器管28上方接近該管 鄰接觫板26孔27之末端。過濾管28在容器21内之位 置使容JI 21頂部超過過濾管28之高度足以使該過濂器 在入〇室25充滿熔融金屬時得到灌注》 25 耐火襯裡蓋子23具有兩孔32和33,該孔分別舆 15 本紙張尺度適用中國國家輮率(CNS ) Μ規格(2丨OX297公釐) (請先閲讀背面之注項再填寫本頁) 訂' 線 4465 7 0 Α7 Β7 五、發明説明(k) 位在室24和25上方之容器頂部内孔34和35及兩栓塞 36和37成一直線。在該設備使用前,栓塞36和37升 高使其封閉蓋23内之孔32和33,且蓋23及容器21 之内部藉由燃氣燃燒器38預熱。在預熱後栓塞36和37 5 下降以封閉該容器頂部内之孔34和35。 使用時熔融金屬進入入口室25,通過過濾管28過 濾,穿過隔板26内孔27進入出口室24,再經由出〇 22 排出容器21。過濾期間容器21内之熔融金屬藉由位在 入口室25及出口室24内之浸入式加熱器39維持於所 10 要溫度β 以下實例亦用以對本發明加以說明: 實例一 實務上經發現用以在一商業基礎上過濾熔融鋁金屬 15 之過遽管必须具有大於35公斤/平方公分(500碎/ 平方英叶)之最小抗碎強度。進行一系列之實驗以建立 抗碎強度與過濾多孔性間之關係。 經濟部中央標準局貝工消费合作社印製 {請先閱讀背面之注意事項再填寫本頁) 名義上9 796過據多孔性且具有無空陈唉繫·帶之破泡 沫材料基《I藉由化學蒸汽聚積法塗佈數種不同層級破化 20 矽以產生具有0.995繫帶實體率及某範圍過濾多孔性之 濾板。對每一層級碳化矽及每一多孔性製造數個有塗佈 板β自每一板切割一載面並決定其抗碎強度。繫帶實撤 率係由架設磨光一板截面再以目測方式檢測繫帶之方式 計董。 25 每一層級碳化矽塗層之碳化矽實雉容積率(%),過 本紙張尺度適用中國國家揉準(CNS ) A4規格(2丨OX297公漦) 4465 7 0 A7 B7 五、發明説明( 及最小抗碎強度均顯示於下夹由 碳化矽货體容積 率(¾) 過濾多孔性(《 ) 斤 2 — 95 3 94 4 93 5 92 碎強度(公 方公分) 90 91 15. 5 丄一-I ---- 21. 1 28ΓΓ 10 W "δΤ ~35Γ2~ 70"JT7? ~59. 8 (請先閱讀背面之注意事項再填寫本頁) 實例二 製備兩個30.5公分x 30.5公分x 2.5公分厚之波 5 板’一板具有約每公分26孔(26ppc)或每英吋65孔 (65ppi)之孔數,另一板具有約每公分32孔或每英吋 80孔之孔數,兩者均具有87X之過濾多孔性及0.995之 繫帶實艘率。網狀聚氨酯泡沫材料經熱解生成碳泡沫材 料,且該碳泡沫材料經加工至所要尺寸》然後該碳泡沫 1〇 材料藉由化學蒸汽澉積法塗佈碳化矽生成過濾器。一過 濾器插入一 50公分深濾杯内,該過濾器及濾杯經一燃 氣吹管預熱。經發現由於該過濾器之高熱傳導能力及低 熱質董(thermal mass)’該過濾器幾乎立即變熱。然 後約3175公斤之熔联6061鋁合金倒入該瀘杯内並通過 15 該過濾篇。在使用每公分32孔或每英吋80孔過濾器之 測試中,該疼觖鋁合金經加入额外之5至50微米尺寸 氡化銘予以污染*在使用每公分26孔或每英对65孔過 訂 經濟部中央標準局貝工消費合作杜印裝A "6570 Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (丨,) The filter tube 10 is preheated by a heating device 5, which may be a gas burner or an electric heater, for example. In the case of molten aluminum metal filtration, it is necessary for the inner surface of the filter tube 10 to be preheated to at least 600 ° C. The heating device 5 also maintains the temperature of the molten metal on the container 1 · 5 molten metal enters through the inlet 2 during use The inlet chamber 6 is filtered by the filter tube 10, enters the outlet chamber 7 through the hole 9 in the partition plate 8, and is then discharged through the outlet 3. Referring to Fig. 6, a device for filtering molten metal includes a refractory container 21 and a refractory lining cover 23, the container has a molten metal inlet (not shown in the circle) and a molten metal outlet 22. The interior of the container 21 is divided into an outlet chamber 24 and an inlet chamber by a refractory partition 26 25. The partition extends across the container 21 and has a hole 27 connecting the outlet chamber 24 and the inlet chamber 25. The four filter tubes 28 are in the form of pyrolytic reticulated carbon foam material and have been coated with silicon carbide by chemical vapor deposition method And have The filtration porosity of 87¾ and 15 and the strapping efficiency of 0.995 are arranged in a straight line in the inlet chamber 25 near the base of the container 21. One end of each filter tube 28 is inserted into a recess of a pair of fire plates 29 In the mouth, and the opposite end of each filter tube is positioned in a perforated recess of a refractory plate 30 so that the hole in the recess and the hole 27 in the partition plate 26 are aligned with the "filter tube 28 supported by the support device 31 and Sealed in position without exerting excessive force on the filter tube 28, the support device is installed above the filter tube 28 near the end of the tube adjacent to the hole 26 of the fascia 26. The position of the filter tube 28 in the container 21 exceeds the top of the container JI 21 The height of the filter tube 28 is sufficient to allow the filter to be filled when the chamber 25 is filled with molten metal. 25 The refractory lining cover 23 has two holes 32 and 33, respectively. ) M size (2 丨 OX297mm) (Please read the note on the back before filling in this page) Order 'line 4465 7 0 Α7 Β7 V. Description of the invention (k) The inner hole on the top of the container above chambers 24 and 25 34 and 35 and two plugs 36 and 37 are in line. In this device Before use, the plugs 36 and 37 are raised to close the holes 32 and 33 in the cover 23, and the inside of the cover 23 and the container 21 is preheated by the gas burner 38. After the preheating, the plugs 36 and 37 5 are lowered to The holes 34 and 35 in the top of the container are closed. In use, molten metal enters the inlet chamber 25, is filtered through a filter tube 28, passes through the inner hole 27 of the partition plate 26, enters the outlet chamber 24, and is discharged out of the container 21 through the outlet 22. The molten metal in the container 21 is maintained at the desired temperature by an immersion heater 39 located in the inlet chamber 25 and the outlet chamber 24. The following example is also used to illustrate the present invention: Example 1 has been found in practice to be used in A commercial filter base for filtering molten aluminum metal 15 must have a minimum crushing strength greater than 35 kg / cm2 (500 pieces / square inch leaf). A series of experiments were performed to establish the relationship between crush strength and filtration porosity. Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives (Please read the precautions on the back before filling this page) Nominally 9 796 has a porous foam material based on the porosity and has airless chandelier and belts. The chemical vapor deposition method coats several different levels of broken silicon 20 to produce a filter plate with a solid rate of 0.995 and a certain range of filter porosity. For each layer of silicon carbide and for each porosity, several coated plates β were made. A load-bearing surface was cut from each plate and its crushing strength was determined. The actual withdrawal rate of the lacing is calculated by erection and polishing a plate section and then visually inspecting the lacing. 25 The silicon carbide solid volume ratio (%) of each layer of silicon carbide coating. The size of this paper is applicable to China National Standard (CNS) A4 (2 丨 OX297) 漦 4465 7 0 A7 B7 V. Description of the invention ( And the minimum crushing strength are shown in the lower clip. The volume ratio of the silicon carbide cargo body (¾) filtration porosity (") kg 2 — 95 3 94 4 93 5 92 crushing strength (cm²) 90 91 15. 5 -I ---- 21. 1 28ΓΓ 10 W " δΤ ~ 35Γ2 ~ 70 " JT7? ~ 59. 8 (Please read the precautions on the back before filling this page) Example 2 Prepare two 30.5 cm x 30.5 cm x 2.5 cm thick wave 5 plates' One plate has about 26 holes (26ppc) per inch or 65 holes (65ppi) per inch, and the other plate has about 32 holes per cm or 80 holes per inch Both have a filtering porosity of 87X and a solid rate of 0.995. The reticulated polyurethane foam material is pyrolyzed to produce a carbon foam material, and the carbon foam material is processed to the desired size. Then the carbon foam material is 10 A filter is formed by coating silicon carbide by chemical vapor deposition method. A filter is inserted into a 50 cm deep filter Inside, the filter and filter cup were preheated by a gas blow pipe. It was found that due to the high thermal conductivity and low thermal mass of the filter, the filter became hot almost immediately. Then about 3175 kg of fusion 6061 aluminum alloy was poured into the cup and passed the 15 filter. In the test using a filter of 32 holes per cm or 80 holes per inch, the aluminum alloy was added with an additional 5 to 50 micron size. Inscriptions are contaminated * When using 26 holes per centimeter or 65 holes per British order, the Central Bureau of Standards of the Ministry of Economic Affairs, Shellfish Consumer Cooperation Du printed equipment

.I I I 17 :446570 經濟部中央榡準局貝工消費合作社印笨 A7 B7 五、發明説明(士) 慮器之案例中’約t費1小時使所有熔融銘金屬過渡, 對應流速約為0_ 05公斤/分/平方公分。在每公分32 孔或每英吋80孔過濾器之案例中使用約〇. 03公斤/分 /平方公分之流速。在兩測試中對過濾後合金取樣,且 5 利用一夾雜物濃度技術測試失雜物之存在。兩樣本均全 然無夾雜物。 實例三 一外徑為4英吋且内徑為2英吋之管狀過濾器藉由 10 具有每公分26扎或每英吋65孔之孔數之網狀聚氨酯泡 珠材料熱解而成’並將所生成碳泡沐材料藉由化學蒸汽 澱積法塗佈碳化矽,從而產生一種具有87%過濾多孔性 及0· 995繫帶實體率之過濾器。該管狀過濾器切為2〇5 公厘長並作為一種熔融鋁金屬過濾器在附屬圖式之圖7 15 垂直裁面圖中所示之一種濾箱中受測試。 以耐火材料襯裡之濾箱40具有一入口室41及一出 口室42,兩室由一耐火隔板43加以分隔《管狀過濾器 44水平定位於接近濾箱40底部45處,其一端插入耐 火板46内,另一端插入隔板43之一凹口 47内。一纖 20 維墊密片(圖中未示)環繞過濾管44末端安裝以將過 濾管44密封於定位,並防止熔融金屬旁流。隔板43具 有一礼48與過濾管44之末端對準。入口室41超過過 濾管44之高度為240公厘。濾箱40内側及過濾管44 藉由插入入口室41及出口室42内之兩燃氣燃燒器預熱 25 至該過濾管紅熱。小心避免入口室41内燃燒器之直接 _______ IS_____ 本紙張尺度逋用中(CNS ) 21GX297公 (請先聞讀背面之注$項再填寫本頁) -訂 -線. 446570 A7 B7 五、發明説明(β ) 火焰影響到過濾管44。預熱後過濾管44之表面未有碎 裂跡象。 純度99. 5%之熔融鋁合金以746°C之溫度自一 800 公斤容量傾斜熔爐倒入濾箱40。當該熔融合金超過過 5 濾管44之高度約達到200公厘時該熔融合金開始注入 過濾管44’如困在過濾管44内之空氣逸至表面且炼融 合金出現在出口室42内所表示。一旦達到穩定狀態, 兩室内熔融金屬頂部高度差約為25公厘。 依序鑄造三個粗胚’每一粗胚長度約3.5公尺,直 10 徑約190公厘❶填充速率約為95公厘/分,對總量為 800公斤之溶融合金而言約等於8公斤/分之流速》在 鑄造間隔間約有15分鐘’是以過滅管44總共浸在該溶 融合金内2. 5小時β 在第三個粗胚鋒成後’過濾管44自慮箱40内移出 15 並受檢視。在該過遽器材料内沒有任何退化跡象。該過 濾器材料自該嫁融鋁合金中去除夾雜物之效能由該過濾 管之切片顯微檢視得到證實。 (請先閱讀背面之注意事項再填寫本莨) 訂 線 經濟部中央標準局貝工消費合作社印製 ' 1/ . 本紙張尺度適用中國困家標準(CNS ) Α4規格(210Χ297公釐).III 17: 446570 Yin Ben A7 B7, Shellfish Consumer Cooperative of Central Bureau of Standards, Ministry of Economic Affairs 5. In the case of the device, it takes about 1 hour to make all the molten metal transition, and the corresponding flow rate is about 0_ 05 Kg / min / cm2. In the case of a filter of 32 holes per cm or 80 holes per inch, a flow rate of about 0.03 kg / min / cm2 is used. The filtered alloy was sampled in two tests, and 5 the presence of impurities was tested using an inclusion concentration technique. Both samples were completely free of inclusions. Example 31: A tubular filter with an outer diameter of 4 inches and an inner diameter of 2 inches was prepared by pyrolyzing 10 mesh polyurethane foam beads with a hole number of 26 bars per cm or 65 holes per inch. The generated carbon foam material was coated with silicon carbide by a chemical vapor deposition method, thereby generating a filter having a filtration porosity of 87% and a solid rate of 0.995 band. The tubular filter was cut to a length of 205 mm and tested as a molten aluminum metal filter in a filter box shown in the attached drawing in the vertical cutout of Figure 7 15. The filter box 40 lined with refractory material has an inlet chamber 41 and an outlet chamber 42. The two chambers are separated by a refractory partition 43. The tubular filter 44 is positioned horizontally near 45 at the bottom of the filter box 40, and one end is inserted into the refractory plate 46, the other end is inserted into a notch 47 of the partition 43. A fiber 20-dimensional gasket (not shown) is installed around the end of the filter tube 44 to seal the filter tube 44 in place and prevent molten metal from bypassing. The partition 43 is aligned with the end of the filter tube 44 in a manner 48. The height of the inlet chamber 41 beyond the filter tube 44 is 240 mm. The inside of the filter box 40 and the filter tube 44 are preheated by the two gas burners inserted into the inlet chamber 41 and the outlet chamber 42 to the filter tube to be red hot. Be careful to avoid direct burners in the entrance room 41 _______ IS_____ This paper size is in use (CNS) 21GX297 (please read the note on the back before filling this page)-order-line. 446570 A7 B7 V. Invention Explanation (β) flame affects filter tube 44. There were no signs of chipping on the surface of the filter tube 44 after preheating. A molten aluminum alloy having a purity of 99.5% is poured into a filter box 40 from a 800 kg capacity inclined furnace at a temperature of 746 ° C. When the height of the molten alloy exceeds 5 mm, the filter tube 44 reaches approximately 200 mm. The molten alloy begins to be injected into the filter tube 44 '. If the air trapped in the filter tube 44 escapes to the surface, and the molten metal appears in the outlet chamber 42. Means. Once stable, the height difference between the tops of the molten metal in the two chambers is about 25 mm. Sequential casting of three rough embryos' each rough embryo is about 3.5 meters in length and about 190 millimeters in diameter. The filling rate is about 95 millimeters per minute, which is about 8 for a total of 800 kg of molten fusion gold. The flow rate of kg / min is about 15 minutes in the casting interval. 'The immersion tube 44 is immersed in the molten metal for a total of 2.5 hours. After the third rough embryo front is formed,' the filter tube 44 is a self-contained box 40. Move in 15 and watch. There were no signs of degradation in the bowl material. The effectiveness of the filter material in removing inclusions from the grafted aluminum alloy was confirmed by microscopic inspection of the filter tube. (Please read the precautions on the back before filling in this card.) LINE PRINTED Printed by Shellfish Consumer Cooperative, Central Bureau of Standards, Ministry of Economic Affairs' 1 /. This paper size applies to China Standard for Households (CNS) Α4 (210 × 297 mm)

五、發明說明( 1 8 第87119689號專利申請案 R OP Patent ν^ρρΐη 5t7 I 1 A7 B7 圖示之主要部分代號說明 中文說明書修正頁•附件(一)V. Description of the invention (1 8 No. 87119689 patent application R OP Patent ν ^ ρρΐη 5t7 I 1 A7 B7 Description of the main part of the diagram Code description Chinese manual correction page • Attachment (1)

Amended Pages of Chinese Specification-Encl. (8$ -f- δ- M 2~ a i£X)~ (Submitted on 2, 2000) 經濟部智慧財產局員工消費合作社印製 1 容器 2 溶融金屬入口 3 熔融金屬出口 4 耐火襯裡蓋 5 加熱裝置 6 入口室 7 出口室 8 耐火隔板 9 孔 10 過濾管 11 耐火板 12 耐火板 13 支承裝置 21 容器 22 出口 23 蓋子 24 出口室 25 入口室 26 隔板 27 28 過濾管 29 对火板 30 耐火板 31 支承裝置 32〜 35 子L 36〜 37 栓塞 38 燃燒器 40 遽箱 41 入口室 42 出口室 43 对火隔板 ------r---*---------„— —訂---------線 Y (請先閱讀背面之注意事項再填寫本頁) Λ74««/men 本紙張尺度通用中囤画家標準(CNS>A4規格<210 X 297公* ) I 4 4 6 5 7 0 A7Amended Pages of Chinese Specification-Encl. (8 $ -f- δ- M 2 ~ ai £ X) ~ (Submitted on 2, 2000) Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 1 Container 2 Molten metal inlet 3 Molten metal Outlet 4 Refractory lining cover 5 Heating device 6 Inlet room 7 Outlet room 8 Refractory partition 9 Hole 10 Filter tube 11 Refractory plate 12 Refractory plate 13 Support device 21 Container 22 Outlet 23 Cover 24 Outlet room 25 Inlet room 26 Partition 27 28 Filtration Tube 29 to fire plate 30 Refractory plate 31 Supporting device 32 to 35 Sub L 36 to 37 Plug 38 Burner 40 Box 41 Entrance chamber 42 Exit chamber 43 Fire partition -------- r --- *- ------- „— —Order --------- Line Y (Please read the notes on the back before filling in this page) Λ74« «/ men This paper standard is commonly used in the painter standard (CNS > A4 size < 210 X 297 male *) I 4 4 6 5 7 0 A7

B7五、發明說明(19 ) 44 過濾管 45 底部 46 耐火板 47 凹口48 iL (請先閱讀背面之注意事項再填寫本頁) I ------^ I I 訂·- - ------ 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準<CNS)A4規格(210 X 297公釐)B7 V. Description of the invention (19) 44 Filter tube 45 Bottom 46 Refractory plate 47 Notch 48 iL (Please read the precautions on the back before filling this page) I ------ ^ II Order ·--- --- Printed by the Consumers' Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs, the paper size applies to the Chinese National Standard < CNS) A4 (210 X 297 mm)

Claims (1)

446 Λ8 Β8 C8 D8 第们丨19689號專利申請案 ROC Patent Appln. No. 87119689 俺正中诛丨fe ffl Φ々本·料件f二 Amended Claims in Chinese -Enel II n〇) (Submitted on Hey X , 2000) 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 六、申請專利範圍 1 種過濾炫融金屬之方法,包含提供一過遽器, 該過濾器包含一多孔碳泡沫材料基體,該基體以 化學热Ά知積法大致全然塗佈·-耐火金屬或而j 火化合物’及導致炼融金屬流過該過淚器以去除 該熔融金屬容有之夾雜物’該方法之特徵在於該 過遽-器具有如前文定義小於9 0 %之過;慮多孔’性及 至少〇·95之繫帶實體率。 如申請專利範圍第1項之方法,其特徵在於該 過渡器具有至少7 5 %之過;慮多孔性。 如申請專利範圍第2項之方法’其特徵在於該 過濾器具有至少8 0 %之過濾多孔性。 如申请專利範圍第1至3項中任一項之方法, 其特徵在於該碳泡沫材料基體為一網狀碳泡沫 材料。 如申請專利範圍第1至3項中任一項之方法, 其特徵在於該耐火金屬為鶴或銦。 6. 如申請專利範圍第1至3項中任一項之方法, 其特徵在於該耐火化合物為碳化矽,氮化矽,碳 化锆,氮化錯,硼化錯,碳化鈮’氮化鈮,硼化 鈮’碳化鈦,氮化鈦,硼化鈦,碳化铪,氮化铪 或硼化铪。 7. 如申請專利範圍第丨至3項中任一項之方法, 其特徵在'於該碳泡沫材料基體塗佈至至少〇.25 公克/立方公分之密度。 却申請專利範圍第1至3項中任 2. 3. 4. 5. 8. 項之方法 (請先閱讀背面之注意事項再填寫本頁) 22 本紙張尺度遙用中BJ國家揉牟(CNS ) Α4規格(2丨0Χ297公釐) 87488/menu 4 46 57 Ο Λ8 Β8 桃厂d_D8 六、申請專利範圍 其特徵在於該過濾器之最小抗碎強度至少為3 5 公斤/平方公分。 9 ·如申請專利範圍第1至3頊中任一項之方法, 其特徵在於該過濾器為一板狀或一管狀形式。 10. —種過濾設備,其包含一具有/出口(2, 41)及一 出口 (3,22,42 )之炼融金屬盛裝容器 (1,2 1,4 0 ),至少一過濾器外罩’該外罩容有一 過濾器( 1 0, 28, 44),該過濾器包含一藉由化學蒸 汽澱積法大致全然塗佈一耐火金屬或耐火化合 物之多孔碳泡沫材料基體’用以將過濾器 ( 1 0, 28, 44 )支承於定位並密封之裝置’及在利用 該設備以過濾熔融金屬之前用來預熱盛裝容器 (1,21,40)及過濾器(10, 28,44)之裝置(5, 38) ’ 其特徵在於該過濾器(1〇,28,44)具有如前文定 義小於90%之過濾多孔性及至少0. 95之繫帶實 體率。 π.如申請專利範圍第ίο項之設備’其特徵在於該 過濾器( 1 0, 28, 44)具有至少 75°/d之過濾多孔 性。 經濟部智慧財產局員工消費合作社印取 ----卜ί—— > (請先閱讀背面之注意事項再填寫本頁) 12.如申請專利範圍第11項之設備’其特徵在於該 過濾器(1 0,2 8,4 4 )具有至少8 0 %之過渡多孔 性。 1 3 如申請專'利範圍第1 0至1 2項中任一項之設備, 其特徵在於該碳泡沫材料基體為一網狀碳泡珠 杖料。 23 本紙張尺度適用中國國家搮準(CNS ) A4现格(2丨〇X297公釐) ' -- 7^ 44657 Ο Λ8 Β8 C8 經濟部智慧財產局員工消费合作社印製 六、申請專利範 D8 圍 1 14. 如 中 請專利範圍第1 〇至12項中 任 一項 之 設備 1 1 其 特 徵在於該耐火金屬為鎢或鉬。 ! 15. 如 中 請專利範圍第1 〇至丨2項中 任 一項 之 設備 1 1 其 特 徵在於該耐火化合物為碳化矽,氮 化 石夕, 碳 先 閲 1 j 化 鍅 ’氮化鍅’硼化锆,碳化銳 氮化 鈮 ,硼 化 讀 背 面 1 鈮 碳化鈦’氮化鈦’硼化鈦, 石发 化銓 ♦ C化 鈐 之 注 [ 或 硼 化铪。 意 事 項 1 r I 16. 如 中 請專利範圍第1 〇至12頊中 任 一項 之 設備 5 4 填 1 ! 其 特 徵在於該碳泡沫材料基體塗佈至至少0 · 25 % 本 η 1 公 克 /立方公分之密度。 1 17. 如 中 請專利範圍第1 〇至1 2項中 任 一項 之 設備 > 1 I 其 特 徵在於該過濾器(1 0, 28, 44) 之最 小 抗碎 強 1 度 至 少為35公斤/平方公分。 訂 I 18. 如 中 請專利範圍第10至12項中 任 一項 之 設備 9 1 1 其 特 徵在於該過濾器(1 0, 28, 44 ) 為板 狀 或管 狀 1 1 形 式 〇 1 I 19. 如 中 請專利範圍第18項之設備 其特 徵 在於 該 1 盛 裝 容器(1,21)由一橫越該盛 裝 容器 (1 ,21) 延 1 1 伸 之 耐火隔板(8, 26)分隔為一 入 口室 (6 ,.2 5 )和 1 I *— 出 口室(7, 24) ’該隔板(8, 26)具 有一 孔 (9, 27) 1 \ 連 接 該入口室(6, 25)和該出口 % :(7, 24), 管狀 過 1 濾 器 (10, 28)定位於接近該盛裝 容 器(1 ,21)底 座 1 I 處 每」管狀過濾器(1〇, 28)之 一 端插 入 一耐 火 1 I 板 (1 1,29)之一凹口内,且其相 反 端位 於 '^耐 火 1 1 (1 ,30)之一穿孔凹口内,使該 凹 口内 之 孔與 該 1 1 J 24 本紙張尺度速用中國國家揉準(CNS ) A4*l格(210X297公簸) 446 57 Ο Α8 Β8 __I!___ 六、申請專利範圍 隔板(8,26)之孔(9,27)對準,且該管狀過濾器 (10,28)藉由裝在該管狀過濾器(1〇, 28)上方之 支承裝置(1 3, 3 1 )支承並密封於定位。 20.如申請專利範圍第19項之設備,其特徵在於該 盛裝容器(21)具有一耐火襯裡蓋子(23),該蓋具 有兩孔(32, 33),該孔分別與位在室(25, 24〕上方 之容器頂部内之孔(34,35)及兩栓塞(36, 37)成 一直線,該栓塞升高時封閉蓋子(2 3)内之孔 (32, 33 ),下降時封閉該盛裝容器頂部内之孔 (34’ 35)。 (請先閱讀背而之注意事項再填一巧本1) \水. 訂 經濟部智慧財產局員工消費合作社印製 本紙張疋度適用中困Η家橾率(CNS > A4現格(210X297公釐)446 Λ8 Β8 C8 D8 No. 丨 19689 Patent Application ROC Patent Appln. No. 87119689 俺 正中 诛 fe ffl Φ々 本 · 件 f 二 Amended Claims in Chinese -Enel II n〇) (Submitted on Hey X, 2000) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. 6. Application for a patent. A method of filtering bright metal, including providing a filter. The filter contains a porous carbon foam matrix, which is chemically heated. The method of coating is known to be applied almost completely-refractory metal or flame compound 'and cause molten metal to flow through the lacrimal device to remove inclusions contained in the molten metal.' This method is characterized by the As defined above, it is less than 90%; considering the porosity and at least 0.95 lacing solid rate. For example, the method of claim 1 in the scope of patent application is characterized in that the transition device has a passivity of at least 75%; porosity is considered. The method according to item 2 of the patent application is characterized in that the filter has a filtering porosity of at least 80%. The method according to any one of claims 1 to 3, wherein the carbon foam material matrix is a reticulated carbon foam material. The method according to any one of claims 1 to 3, wherein the refractory metal is crane or indium. 6. The method according to any one of claims 1 to 3, characterized in that the refractory compound is silicon carbide, silicon nitride, zirconium carbide, nitride, boride, niobium carbide, niobium nitride, Niobium boride 'titanium carbide, titanium nitride, titanium boride, hafnium carbide, hafnium nitride or hafnium boride. 7. The method as claimed in any one of claims 1-3, characterized in that the carbon foam material substrate is coated to a density of at least 0.25 g / cm3. But apply for any of the items 1 to 3 in the scope of patents 2. 3. 4. 5. 8. (please read the precautions on the back before filling this page) 22 This paper is used in BJ countries (CNS) ) Α4 specification (2 丨 0 × 297 mm) 87488 / menu 4 46 57 〇 Λ8 Β8 Tao factory d_D8 6. The scope of patent application is characterized by the minimum crushing strength of the filter of at least 35 kg / cm². 9. The method according to any one of claims 1 to 3, wherein the filter is in the form of a plate or a tube. 10. A filtering device comprising a metal melting container (1,2,1,4 0) with / outlet (2, 41) and an outlet (3, 22, 42), and at least one filter cover ' The housing contains a filter (10, 28, 44), which includes a porous carbon foam substrate 'approximately and completely coated with a refractory metal or refractory compound by chemical vapor deposition method to filter the filter ( 1 0, 28, 44) Supported by a device positioned and sealed 'and a device for preheating the holding container (1,21,40) and the filter (10, 28,44) before using the device to filter molten metal (5, 38) 'It is characterized in that the filter (10, 28, 44) has a filtration porosity of less than 90% as defined above and a lace solid rate of at least 0.95. π. The device according to the scope of the patent application, characterized in that the filter (10, 28, 44) has a filtering porosity of at least 75 ° / d. Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs ---- Buί—— > (Please read the precautions on the back before filling out this page) 12. If the device for the scope of patent application for item 11 is characterized by the filter The device (10, 2 8, 4 4) has a transitional porosity of at least 80%. 1 3 If the device of any one of the items 10 to 12 of the patent application scope is applied, it is characterized in that the carbon foam material matrix is a reticulated carbon foam bead rod material. 23 This paper size applies to China National Standards (CNS) A4 (2 丨 〇297297mm) '-7 ^ 44657 Ο Λ8 Β8 C8 Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 6. Application for patents D8 1 14. The device according to any one of patents Nos. 10 to 12 is requested. 1 1 is characterized in that the refractory metal is tungsten or molybdenum. 15. 15. Please refer to the equipment 1 of any of the patent scope Nos. 10 to 2 1 1 characterized in that the refractory compound is silicon carbide, nitride nitride, carbon first read 1 j Chemical '' fluoride nitride 'boron Zirconium carbide, anthracitic niobium nitride, boronization read on the back side 1 Niobium titanium carbide 'titanium nitride' titanium boride, Shi Fahua 铨 ♦ C 钤 钤 Note [or hafnium boride. Matters needing attention 1 r I 16. Please refer to the equipment of any one of the patent range 10 to 12 顼 5 4 Fill 1! It is characterized in that the carbon foam material substrate is coated to at least 0 · 25% of this η 1 g / Cubic centimeter density. 1 17. The device according to any one of the patents Nos. 10 to 12 > 1 I is characterized in that the minimum crushing strength of the filter (1 0, 28, 44) is at least 35 kg / Cm2. Order I 18. The device 9 1 1 as claimed in any of the patent scope items 10 to 12 is characterized in that the filter (1 0, 28, 44) is in the form of a plate or a tube 1 1 〇 I I 19. For example, the equipment in the scope of patent claim 18 is characterized in that the 1 container (1, 21) is divided into an inlet by a refractory partition (8, 26) extending across the 1 (1, 21) container. Chamber (6, .2 5) and 1 I *-exit chamber (7, 24) 'The partition (8, 26) has a hole (9, 27) 1 \ connecting the entrance chamber (6, 25) and the Outlet%: (7, 24), tubular filter 1 (10, 28) is positioned close to the base of the container (1, 21) 1 I. Insert a fire-resistant 1 at each end of the tubular filter (10, 28) One of the notches in the I plate (1 1, 29), and the opposite end is located in one of the perforated notches of the refractory 1 1 (1, 30), so that the hole in the notch and the 1 1 J 24 paper scale speed Using China National Standards (CNS) A4 * l (210X297 male dustpan) 446 57 〇 Α8 Β8 __I! ___ 6. Application for patent scope partition (8, 26) The holes (9, 27) are aligned, and the tubular filter (10, 28) is supported and sealed in position by a supporting device (1 3, 3 1) mounted above the tubular filter (10, 28). . 20. The device according to item 19 of the scope of patent application, characterized in that the container (21) has a refractory-lined lid (23), the lid has two holes (32, 33), and the holes are respectively located in the chamber (25). , 24] The holes (34,35) in the top of the container and the two plugs (36, 37) are in a line. When the plug is raised, the holes (32, 33) in the lid (2 3) are closed, and when it is lowered, the plug is closed. The hole (34 '35) in the top of the container. (Please read the precautions and fill in a copy of the book 1) \ Water. Order the paper printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. Furniture ratio (CNS > A4 now available (210X297 mm)
TW87119689A 1997-11-28 1998-11-27 Molten metal filtration TW446570B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US6685897P 1997-11-28 1997-11-28

Publications (1)

Publication Number Publication Date
TW446570B true TW446570B (en) 2001-07-21

Family

ID=22072171

Family Applications (1)

Application Number Title Priority Date Filing Date
TW87119689A TW446570B (en) 1997-11-28 1998-11-27 Molten metal filtration

Country Status (2)

Country Link
TW (1) TW446570B (en)
ZA (1) ZA9810643B (en)

Also Published As

Publication number Publication date
ZA9810643B (en) 1999-05-24

Similar Documents

Publication Publication Date Title
US3893917A (en) Molten metal filter
US6635339B1 (en) Open-cell expanded ceramic with a high level of strength, and process for the production thereof
US4056586A (en) Method of preparing molten metal filter
Jo et al. Characterization of ceramic composite membrane filters for hot gas cleaning
EP0178926A2 (en) Multiple-use molten metal filters
KR102631663B1 (en) filter handling device
JPH0431728B2 (en)
JP5792740B2 (en) Molten metal container and manufacturing method thereof
EP0402673A2 (en) Transfer tube
JPH06206718A (en) Extra-high purity silicon carbide and high temperature semiconductor processing device produced by said silicon carbide
CN107915475A (en) A kind of gradient pore high temperature filtration ceramic tube and preparation method thereof
Jo et al. Preparation of ceramic membrane filters, from waste fly ash, suitable for hot gas cleaning
EP1511589B1 (en) Filter device for molten steel filtration
US5189273A (en) Microwave absorbing heater
TW446570B (en) Molten metal filtration
US5004629A (en) Transfer tube
EP2304065B1 (en) Improved method for filtering molten aluminum and molten aluminum alloys
WO1999028273A1 (en) Molten metal filtration
JP2006312895A (en) Particulate material filter
JP4458611B2 (en) Porous silicon carbide filter
RU2815946C1 (en) Method of making ceramic filter element for cleaning hot gas
KR102517386B1 (en) Apparatus and method to manufactue ceramic filter having ultra-fine filtration layer
GB2313069A (en) Molten metal filtration apparatus
CN112226631A (en) Sodium purification equipment for sodium reduction tantalum powder and process thereof
JP2847550B2 (en) Silica glass filter