TW500758B - A process for producing an amino resin molding material - Google Patents

A process for producing an amino resin molding material Download PDF

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Publication number
TW500758B
TW500758B TW88111235A TW88111235A TW500758B TW 500758 B TW500758 B TW 500758B TW 88111235 A TW88111235 A TW 88111235A TW 88111235 A TW88111235 A TW 88111235A TW 500758 B TW500758 B TW 500758B
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Taiwan
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amine
resin
weight
parts
molding material
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TW88111235A
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Chinese (zh)
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Kuen-Yuan Huang
Hung-Shing Chen
Jr-Fu Chen
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Chang Chun Plastics Co Ltd
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Priority to TW88111235A priority Critical patent/TW500758B/en
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Publication of TW500758B publication Critical patent/TW500758B/en

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Abstract

This invention provider a process for producing an amino resin molding material, which is characterized by the use of water-soluble liquid amino resin containing more than 75% solid content and having at least one methylol group. The liquid amino resin is blended with other additives in a blender to form a blend in a semi-drying state, then the blend is directly subjected to a mixing step, to produce the amino resin molding material through a crosslinking reaction of the liquid amino resin. According to the present process, the drying step required by the conventional process could be eliminated without the use of the expensive and unworkable solid amino resin.

Description

500758 五、發明說明(1) [技術背景] 傳統胺基樹脂成形材料之製法分為乾式及溼式兩種。 乾式法係將固體樹脂直接與紙、木粉等纖維質材料與無機 填充料、滑劑、促進劑、色料等成分,於固(粉)體乾式狀 態下直接粉碎、混合、混練、冷卻、造粒等而製備。如日 本特開平6-571 00及7-1 1 850 1所揭示者。其缺點為作為原 料之固體胺基樹脂生產不易,價格昂貴,且製程中樹脂有 硬化之虞,軟化點無法提高以及製程中多為粉體輸送易發 生污染及清理問題。 溼 粉等纖 材料、 卻、造 填材、 中進行 品,例 者。此 劑,增 乾燥過 性,造 添加有 溶劑在 產上亦 工、成貝,j 維質材 滑劑、 粒等而 添加劑 混合、 如曰本 製程雖 加了乾 程中由 成困擾 機溶齊J 乾燥時 不理想 係以含有溶劑之液 料含浸、乾燥後, 促進劑、色料等, 製得。或將上述液 專原料一併加入快 乾燥及混練等步驟 特開昭 59-189162、 未使用價昂之固體 燥去除溶劑之步驟 於樹脂中殘留之甲 ;再者,製程後段 稀釋使溶解後才能 又會揮發而污染環 體胺基樹脂先與 再與固體原料如 經粉碎、混合、 體樹脂原料與其 速混合機類的特 後再經冷卻、造 特公平6-74372 胺基樹脂卻另外 ’使成本增加。 醛及溶劑會產生 易發生白化分層 進行含浸混合, 境,對人體造成 無機充填 混練、冷 它固體充 殊混合機 粒製成成 所揭示 添加溶 又,在其 臭味及毒 ’須再度 此等有機 危害,生 本發明人有鑑於此 對有關製程深入研究找尋改善方500758 V. Description of the invention (1) [Technical background] Traditional amine-based resin molding materials are divided into two types, dry and wet. The dry method uses solid resin directly with fibrous materials such as paper and wood flour, and inorganic fillers, lubricants, accelerators, colorants and other components. In the solid (powder) dry state, it is directly crushed, mixed, kneaded, cooled, It is prepared by granulation or the like. As disclosed in Japanese Unexamined Patent Publication No. 6-571 00 and 7-1 1 850 1. The disadvantages are that the production of solid amine-based resins as raw materials is not easy, the price is high, and the resin may be hardened during the process, the softening point cannot be increased, and pollution and cleaning problems are likely to occur during powder transportation during the process. Wet powder and other fibrous materials, but also fillers, intermediate products, for example. This agent enhances the drying performance, and the solvent is added to produce the product, and the shellfish, j-dimensional materials, lubricants, granules, etc. are mixed with the additives. Although this process is added, it will be dissolved during the drying process. J It is not ideal to dry it by impregnating it with a solvent-containing liquid material, and then drying it with an accelerator, colorant, etc. Or add the above liquid special raw materials together with the steps of quick drying and kneading, etc. JP 59-189162, without using expensive solid drying steps to remove solvent residues in the resin; Furthermore, the latter part of the process can only be diluted after the solution is dissolved. It will also volatilize and contaminate the ring-shaped amine-based resin. It is then mixed with solid raw materials such as pulverized, mixed, bulk resin raw materials and high-speed mixers, and then cooled. Increased costs. Aldehydes and solvents will produce prone whitening and layering for impregnation and mixing, which will cause inorganic filling and kneading to the human body. It will be made of solid filled mixing granules. In view of such organic hazards, the inventors of the present invention have in-depth research on the relevant processes to find ways to improve

聊758 案號 88111235Chat 758 case number 88111235

五 、發明說明(2) 法因而完成本發明 [發明之詳細說明] 】、本發明之目的係提供^種胺基樹脂成型材料之半乾式 製法’該製法不需使用有機溶劑亦不需經過乾燥、之步驟。 本發明所提供之胺基樹脂成型材料之製法,係單獨使 用=形份高於75%且至少含一個羥甲棊之水溶性液體胺基 樹脂或與其他自硬性樹脂併用,於半乾燥狀態下,與其"他 添加物經加熱混練步驟即可使液體胺基樹脂聚合成較大分 子量之胺基樹脂成型材料,而完成本發明。本發明之方法 ϊ ΐ工Γ:乾、溼式方法之優點而摒除其缺點,與傳統溼 ;產生=且ί:明之方法可省略乾燥步驟亦可避免製程 毋臭味之溶劑,同時可解決乾式製法中 及粉體物造成之輪送清理問 避免粉體飛揚略有機溶劑之使用,並 亦即? ί象 具有里濟及環保上之利用性。 -個經甲基單獨使用固形份高於m且含有至少 樹脂併用:乂 :機:胺基:脂為原料或與其他自硬性 不致結塊進滑!、促ΐ劑:色料等,…燥而 體胺基樹脂交聯並製。此合後經加熱混練步驟使液 又聊亚ι成粉末或粒化物者。 2明中所使用之液體胺基樹脂 聚氰胺等胺基化合物或 ^策造係以尿素、二 催化劑之存在下經加敲、ζ η彳,、甲醛或其衍生物於 ㈣拌而分別製成尿素甲酸樹5. Description of the invention (2) The method has thus completed the present invention [detailed description of the invention]], the purpose of the present invention is to provide ^ semi-dry manufacturing method of amine-based resin molding materials' This method does not require the use of organic solvents or drying Steps. The method for preparing the amine-based resin molding material provided by the present invention is used alone = a water-soluble liquid amine-based resin having a content of more than 75% and containing at least one hydroxyformamidine or used in combination with other self-hardening resins in a semi-dry state After the heating and kneading step with the other additives, the liquid amine-based resin can be polymerized into an amine-based resin molding material with a relatively large molecular weight to complete the present invention. The method of the present invention ϊ ΐ: the advantages of dry and wet methods and eliminate their disadvantages, and the traditional wet; produce = and: the method can omit the drying step can also avoid the process of odorless solvents, and can solve the dry method In the production method and the rotation cleaning caused by the powder, it is necessary to avoid the use of organic solvents in the powder flying, which means that it has the utility of environmental protection and environmental protection. -Each methyl group has a solid content higher than m and contains at least a resin. Use it together: 机: organic: amine: fat or other self-hardening materials that will not agglomerate and slip! , Promoting agents: colorants, etc .... Dry and bulk amine-based resins are crosslinked and made. After that, the liquid is mixed into powder or granules by heating and kneading steps. 2 Liquid amine-based resins such as melamine and other amine-based compounds used in the Ming Dynasty are prepared separately by adding urea, ζ η 彳, formaldehyde or its derivatives in the presence of urea and a second catalyst. Urea formate

500758 五、發明說明(3) ---- 脂、三聚氰胺甲醛樹脂及三聚氰胺酚甲醛樹脂等胺基樹 脂。該反應中胺基化合物對甲醛及其衍生物之比例需控制 在甲醛或甲醛衍生物(下文表示)與胺基化合物(=以 Μ表示)之F/M莫耳比例為u以上’使樹脂中可作為架橋劑 之甲醛(F)多於尿素或三聚氰胺(Μ)才能產生交聯硬化。五 應之F/M可為1·〇至6.0之範圍内,以ι·〇至2·5為宜。 本發明製法所製付之胺基樹脂成型材料具有較習知方 法製付者為咼之成品流動性及熱變形溫度,其值分別為8 〇 至95cm 及 180 至200 °C。 所用催化劑可為例如週期表中第I、第π族之鹼金 屬、驗土金屬之氧化物或氫氧化物或氨水溶液及其他胺類 之鹼性物質等。上述催化劑可單獨或二種以上合併使用, 其添加量以對反應物總重量比$ 5%為宜。 反應溫度可為50 °C至100 °C之範圍内,此反應過程主 要係獲得水溶性之胺基樹脂,故在反應物之膠化時間(Ge 1 Time)達預定目標時即減壓乾燥以停止反應,並依所需固 形份之含量而調整乾燥程度以控制水分含量,使固形份之 含量達50%以上,以75%以上為宜,即製得具有水溶性且含 有至少一個羥甲基之液體胺基樹脂,其脫水程度係控制在 其固形份達75%或更高。膠化時間係依據J IS K6909之方 法,於熱板上至不會拉絲之時間。 上述液體胺基樹脂若於迴流反應階段繼續反應至具特 定分子量後,再配合減壓脫水,於1 〇 〇 °C以下抽真空至特 定軟化點或膠化時間後洩出急速冷卻即得固體胺基樹脂。500758 V. Description of the invention (3) ---- Amino resins such as grease, melamine formaldehyde resin and melamine phenol formaldehyde resin. In this reaction, the ratio of the amine compound to formaldehyde and its derivatives needs to be controlled at a molar ratio of F / M of the formaldehyde or formaldehyde derivative (represented below) to the amine compound (= represented by M) above u. More formaldehyde (F) can be used as bridging agent than urea or melamine (M) to produce cross-linking hardening. The F / M of the five applications may be in the range of 1.0 to 6.0, and preferably ι · 0 to 2.5. The amine-based resin molding material prepared by the manufacturing method of the present invention has the fluidity and heat distortion temperature of the finished product compared to those made by conventional methods, and the values are 80 to 95 cm and 180 to 200 ° C, respectively. The catalyst used may be, for example, alkali metals of Groups I and π in the periodic table, oxides or hydroxides of earth test metals or aqueous ammonia and other basic substances of amines. The above catalysts can be used singly or in combination of two or more kinds, and the addition amount thereof is preferably 5% to the total weight of the reactants. The reaction temperature can be in the range of 50 ° C to 100 ° C. This reaction process is mainly to obtain a water-soluble amine-based resin. Therefore, when the gelation time (Ge 1 Time) of the reactant reaches a predetermined target, it is dried under reduced pressure to Stop the reaction, and adjust the degree of drying to control the moisture content according to the content of the desired solid content, so that the content of the solid content reaches 50% or more, preferably 75% or more, that is, the product is water-soluble and contains at least one methylol group. For liquid amine-based resins, the degree of dehydration is controlled at a solid content of 75% or higher. Gelation time is based on the method of J IS K6909. If the above liquid amine-based resin continues to react to a specific molecular weight in the reflux reaction stage, it is then dehydrated under reduced pressure, and evacuated to a specific softening point or gelation time below 1000 ° C to release the solid amine after rapid cooling. Based resin.

A:\15785.ptd 第6頁 刈0758 五、發明說明(4) 本發明之胺基樹腊成型材料即德使^ -案號88111235 年4月夺日 n 補充 上述方法 所得 、 —Η Η W π 一 % /私厂 之液體胺基樹脂並可配合其他酚醛樹脂或熱硬化型樹脂及 /、他添加物以半乾燥方式進行混合而製得。亦即,將前述 各樹脂與紙、木粉纖維質材料、無機充填材料、滑劑、促 j,二色料等,於捏合機、球磨機、轉鼓、快速混合機等 〃设備中均勻攪拌混合後,洩入滾筒機或單、雙軸押出 ί I ΐ ί I於此步驟中在60至i4(rc溫度之加熱狀態下藉 绫$ L ^虱方式控制水分含量使達到成品之規格要求。混 =。!^至15至4代並以粉碎機打碎成顆粒狀或粉 狀而獲件本發明之胺基樹脂成型材料。 所使用之紛駿樹腊或熱硬化型樹脂之量為等 有ίϋί!”添加量之一半,且需能使配方中所 響i作性則程所::持於半乾式,不會造成結塊或影 響操作性為原貝,卜所使用樹腊其各成分之反應莫耳分率在 尬以反應莫耳分率總和=胺基樹脂所佔總樹腊重量% 反應時之F/M莫耳比+㈣樹脂所 量% 重量%χ埶璲化创枓萨拓ί ΐ 熱化型樹脂所佔總樹脂 二Λ 應時之F/M莫耳比之總和)。 本發明中所用之紙、木粉纖維質 重量%以上之可通過80#篩之粒子為 各有 佳。紙、木粉纖維質材料之添:ί佳,95重量%以上更 25%至75%之範圍。'丨為胺基樹脂重量之 氧 本發明中所使用之 化物(例如··氧化鎂、 無機充填 氧化、 材料包括金屬氧化物或氫 氧化辞、氧化鍾、氧化A: \ 15785.ptd Page 6 刈 0758 V. Description of the invention (4) The amine-based wax molding material of the present invention is the German envoy ^-Case No. 88111235 April 4, n Supplementary to the above method, -Η Η W π 1% / private liquid amine-based resin can be mixed with other phenolic resins or thermosetting resins and / or other additives in a semi-dry manner. That is, the aforementioned resins and paper, wood flour fiber material, inorganic filling materials, lubricants, j-colors, etc. are uniformly stirred and mixed in a kneading machine, a ball mill, a drum, a rapid mixer and the like After that, it is discharged into the drum machine or extruded with single or double shafts. In this step, under the heating state of 60 to i4 (rc temperature), the moisture content is controlled by 绫 $ L ^ lice to achieve the specifications of the finished product. =. ^ To 15 to 4 generations and crushed into granules or powder with a pulverizer to obtain the amine-based resin molding material of the present invention. The amount of fenjun tree wax or thermosetting resin used is equal to ίϋί! "Add one half of the amount, and it must be able to make the formula in the formula :: keep in the semi-dry type, will not cause agglomeration or affect the operability of the original shellfish, the ingredients of the tree wax used The molar fraction of the reaction is the sum of the molar fraction of the reaction = the weight of the total wax of the amine-based resin. The F / M molar ratio of the reaction + the weight of the resin.% By weight. Topology ΐ The total F / M molar ratio of the total resin 2 Λ (the sum of the F / M molar ratio of the thermal resin). Paper and wood flour fiber weight% or more can pass through 80 # sieve are each good. Paper and wood flour fiber material addition: ί Jia, 95 weight% or more, 25% to 75% range. '丨 is the oxygen of the amine-based resin. The compounds used in the present invention (such as magnesium oxide, inorganic filling oxidation, materials including metal oxides or hydroxides, oxidizing bell, oxidation

2001.01 04. 008 500758 五、發明說明(5) ------ 銘、氫氧化鋁、氫氧化鎂等),金屬碳酸鹽(例如:碳酸 鎮、碳酸鈣、碳酸辞等),金屬硫酸鹽及硫化物( · 暇两、硫酸鋇、硫化辞等)、金屬矽酸鹽(例如:發酸鎮、 :夕酸_等),石夕化物(例如:氧化石夕、二氧化♦、碳化石夕 等)’礦物質粉(例如:金剛砂、剛玉粉、滑石粉、石夕藻 土、高嶺土、矽石等),或玻璃纖維(玻璃纖維長度L對’玻 璃纖維直徑D之比例為L/D = 5000以下之範圍)等,無機充填 材料之添加比例為胺基樹脂重量U至5 〇 %之範圍。 ' 本發明中所使用之滑劑包括脂肪系滑劑(例如··硬脂 酸、硬脂酸辞、硬脂酸鎂、硬脂酸鈣、硬脂酸丁酯等)、 脂肪醯胺系滑劑(例如:十二烷醯胺、十四烷醯胺、油酿 胺、硬脂醯胺等飽和或不飽和單醯胺型滑劑以及雙油醯 胺、雙硬脂醯胺等飽和或不飽和雙醯胺型滑劑)、醇系滑 劑(例如:PEG400、PEG1 000、高級醇等)、石臘系滑劑^主 要為含28至90個碳的直鏈型碳氫化合物,例如:液蝶、石 臘、石油臘(Paraffin Wax)、薩醇臘(Sasol Wax)等)以及 含矽之滑劑(例如:矽油等),滑劑之添加比例為佔胺基樹 脂重量0· 1%至20%之範圍。 本發明中所使用之促進劑包括無機酸系促進劑(例 如··硫酸、硼酸、磷酸、鹽酸等),有機酸系促進劑(例 如··草酸、安息香酸、联酸if、對-甲苯續酸等),有機胺 鹽系促進劑(前述酸類與三乙醇胺、三乙基胺、2-甲基-2-胺基-1-丙醇等所成之鹽類,例如:CATANITT〇、 CATANITTO-A等)、無機金屬鹽系促進劑(例如··亞硫酸鋅2001.01 04. 008 500758 V. Description of the invention (5) ------ Ming, aluminum hydroxide, magnesium hydroxide, etc.), metal carbonates (such as: carbonate, calcium carbonate, carbonate, etc.), metal sulfates And sulfides (· 2, barium sulfate, sulfide, etc.), metal silicates (for example: acidic acid,: acid, etc.), stone compounds (for example: oxidized stone, oxidized oxide, carbonized stone) Etc.) 'mineral powder (for example: emery, corundum powder, talc powder, celite, kaolin, silica, etc.), or glass fiber (the ratio of the length of glass fiber L to the diameter of glass fiber D is L / D = The range is less than 5000), etc., and the addition ratio of the inorganic filler is in the range of U to 50% by weight of the amine resin. '' The lubricants used in the present invention include fatty lubricants (eg, stearic acid, stearic acid, magnesium stearate, calcium stearate, butyl stearate, etc.), fatty ammonium lubricant Agents (eg: saturated or unsaturated monoammonium type lubricants such as dodecylamine, myristylamine, oleylamine, stearylamine, and saturated or unsaturated dioleamide, distearylamine, etc. Saturated stilbene-based lubricants), alcohol-based lubricants (eg: PEG400, PEG1000, higher alcohols, etc.), paraffin-based lubricants ^ are mainly straight-chain hydrocarbons containing 28 to 90 carbons, for example: Liquid butterfly, paraffin wax, petroleum wax (Paraffin Wax), Sasol Wax (Sasol Wax, etc.) and silicone-containing lubricants (such as: silicone oil, etc.), the additive ratio of the lubricant is 0.1% by weight of the amine-based resin To the 20% range. The accelerators used in the present invention include inorganic acid-based accelerators (eg, sulfuric acid, boric acid, phosphoric acid, hydrochloric acid, etc.), and organic acid-based accelerators (eg, oxalic acid, benzoic acid, diacid if, p-toluene, etc.) Acids, etc.), organic amine salt-based accelerators (the salts of the aforementioned acids with triethanolamine, triethylamine, 2-methyl-2-amino-1-propanol, etc., for example: CATANITT〇, CATANITTO- A, etc.), inorganic metal salt-based accelerators (such as ...

A:\15785.ptd 第8頁 500758 -is_8mi235A: \ 15785.ptd Page 8 500758 -is_8mi235

fo 年 AA m 么、發明說明(6) L————— 等)等等,促進劑之添加比例為胺基樹脂重量〇· οΐϋ 20% 之範圍。 五 列舉下列實施例、配方實例及比較例更詳細說明本發 明’但本發明並非侷限於此。 實例中之軟化點係以環球法測定。該法係將一環置於 包有薄銘落紙之玻璃片上加熱,於環中敢入2 0g试樣’存 升溫至試料融化後,取出該環置於環架上冷卻20分鐘後將 鋼球置於試片中央並移至水浴中以每分鐘5± 0‘5 °C之速度 升溫,讀取試料開始軟化,鋼球掉下25· 4mm時之溢度,即 為軟化溫度。膠化時間係於1 5 〇 °C下測定。又,實施例、 配方實例及比較例中之“份,,均為重量份。 [實施例] 例 1 將2000公克37%之甲酪水溶液、15公克10%氫氧化鈉 水溶液及1850公克三聚氰胺裝入燒瓶中,於8〇。(^下迴流加 熱反應2小時後,綠減壓乾燥,獲得固形份8 5 % ,膠化時 間6至7分鐘之約25Q0公克三聚氰胺一甲醛樹脂。 复Jfe例2 、依據實施例1之相同配方與方法進行反應,但反應完 成後繼續於90C卞減壓乾燥,獲得軟化點為9〇 π,膠化時 間為3至4分鐘之約21 〇〇公克固體三聚氰胺—甲醛樹脂。 复』Μ列3 將2000公克37%之甲醛水溶液、1〇公克28%氨水溶液 及1500公克三聚氰胺裝入燒雖中,於1〇〇ec下迴流加熱反fo AA m, invention description (6) L ——————, etc.), etc., the addition ratio of the accelerator is in the range of 20% by weight of the amine resin. Fifth, the following examples, formulation examples and comparative examples are listed to explain the present invention in more detail, but the present invention is not limited thereto. The softening points in the examples were determined by the ring and ball method. In this method, a ring is placed on a glass sheet covered with a thin sheet of paper to heat, and a 20 g sample is dared to be stored in the ring. After the sample is warmed up and the sample is melted, the ring is placed on a ring frame and cooled for 20 minutes. Place it in the center of the test piece and move to a water bath to heat up at a rate of 5 ± 0'5 ° C per minute. Read the sample to start softening. The degree of overflow when the steel ball falls 25.4 mm is the softening temperature. The gelation time was measured at 150 ° C. In addition, "parts" in the examples, formulation examples, and comparative examples are all parts by weight. [Examples] Example 1 2,000 g of a 37% methyl butyrate aqueous solution, 15 g of a 10% sodium hydroxide aqueous solution, and 1,850 g of melamine were charged. Put it into a flask and heat the reaction at 80 ° C for 2 hours, then dry it under reduced pressure to obtain a solid content of 85% and a gelation time of 6 to 7 minutes, about 25Q0 grams of melamine-formaldehyde resin. Compound Jfe Example 2 2. The reaction was carried out according to the same formula and method of Example 1, but after the reaction was completed, it was dried under reduced pressure at 90 ° C. to obtain a softening point of 90 π and a gelation time of about 2 to 100 minutes of solid melamine— Formaldehyde resin. Column 3: 2000 grams of 37% aqueous formaldehyde solution, 10 grams of 28% ammonia solution, and 1500 grams of melamine were charged into the baking, and heated under reflux at 100 ec.

15785.ptc 第9頁 2001· 04.04· 010 500758 五、發明說明(7) 應2小時後’減壓乾燥,獲得固形份85%,膠化時間5至6分 鐘之約2400公克三聚氰胺—甲醛樹脂。 實施例4 將20 00公克37%之甲醛水溶液、4〇公克六亞甲基四胺 及1100公克尿素裝入燒瓶中,於5〇〇c下迴流加熱反應1〇〇 分鐘後’減壓乾燥,獲得固形份85%,膠化時間5至6分鐘 之約1 800公克尿素—曱醛樹脂。 實施例5 將680公克酚、600公克37%之曱醛水溶液、15公克10〇/〇 氫氧化鈉水溶液裝入燒瓶中,於80 t下迴流加熱反應6〇分 鐘後冷卻至45 °C,繼之再添加1 900公克37%之曱醛水溶液 及2000公克三聚氰胺並於85。(:下迴流加熱反應60分鐘,然 後以10公克10%氫氧化鈉水溶液中和,再經減壓乾燥可獲 得固形份85%,膠化時間4分30秒之約2000公克三聚氰胺-酚-甲醛樹脂。 實施例6 依據實施例5之相同配方與方法進行反應,但反應完 成後繼續於90 °C下減壓乾燥,獲得軟化點為90 °C,膠化時 間為2分30秒至3分30秒之約1 70 0公克固體三聚氰胺-酚-甲 醛樹脂。 實施例7 將940公克酚、2000公克37%之曱醛水溶液、5公克50 %氫氧化納水溶液裝入燒瓶中,於60至70 °C下迴流加熱反 應60分鐘後減壓乾燥並添加1.8公克醋酸中和之,再於9015785.ptc Page 9 2001 · 04.04 · 010 500758 V. Description of the invention (7) After 2 hours, it should be dried under reduced pressure to obtain a solid content of 85% and a gelation time of 5 to 6 minutes. About 2400 grams of melamine-formaldehyde resin. Example 4 20,000 g of a 37% aqueous formaldehyde solution, 40 g of hexamethylenetetramine, and 1100 g of urea were charged into a flask, and the reaction was heated under reflux at 500 c for 100 minutes and dried under reduced pressure. Approximately 1,800 grams of urea-formaldehyde resin with a solids content of 85% and a gelation time of 5 to 6 minutes. Example 5 680 grams of phenol, 600 grams of a 37% aqueous solution of acetaldehyde, and 15 grams of a 10/0 sodium hydroxide aqueous solution were charged into a flask, and the mixture was heated under reflux at 80 t for 60 minutes, and then cooled to 45 ° C. Add 1 900 grams of 37% aqueous formaldehyde solution and 2000 grams of melamine at 85. (: Heated under reflux for 60 minutes, then neutralized with 10 grams of 10% aqueous sodium hydroxide solution, and then dried under reduced pressure to obtain a solid content of 85%, gelation time of about 2000 grams of melamine-phenol-formaldehyde 4 minutes 30 seconds Resin. Example 6 The reaction was performed according to the same formula and method as in Example 5, but after the reaction was completed, it was dried under reduced pressure at 90 ° C to obtain a softening point of 90 ° C and a gelation time of 2 minutes 30 seconds to 3 minutes. Approximately 1,700 grams of solid melamine-phenol-formaldehyde resin in 30 seconds. Example 7 A flask was charged with 940 grams of phenol, 2000 grams of a 37% aqueous formaldehyde solution, and 5 grams of a 50% aqueous sodium hydroxide solution. The reaction was heated at reflux at 60 ° C for 60 minutes, then dried under reduced pressure and neutralized by adding 1.8 g of acetic acid.

A:\15785.ptd 第10頁 500758 五、發明說明(8) V下繼續減壓乾燥,獲得軟化點為8〇 v,膠化時間為60至 70秒之约1 700公克固體酚—甲醛樹脂。 [胺基樹脂成型材料之配方實例] 配方實例1 實施例1之樹脂 100份 紙粉 55份 滑石粉 15份 硬脂酸辞 3份 酜酸酐 1份 二氧化鈦 2份 將上述原料於快速混合機中快速攪拌混合2 0分鐘後’线入 滚筒機中加熱混練5 混練完成後以冷風冷卻1,以快速氣碎 機(Speed Mill)打碎 ,獲得顆粒狀或粉狀之三聚氰胺—甲 醛樹脂成型材料。 配方實例2 實施例3之樹脂(固形份75%) 70份 實施例2之樹脂 30份 紙粉 55份 滑石粉 15份 硬脂酸辞 3份 联酸酐 1份 二氧化鈦 2份 依據配方實例1之相同方法,獲得顆粒狀或粉狀之三 聚氰胺-曱醛樹脂成型材料。A: \ 15785.ptd Page 10 500758 V. Description of the invention (8) Continue drying under reduced pressure at V to obtain a softening point of 80V and a gelation time of about 1 700 grams of solid phenol-formaldehyde resin at 60 to 70 seconds. . [Formulation example of amine-based resin molding material] Formulation Example 1 100 parts of paper resin, 55 parts of talc, 15 parts of stearic acid, 3 parts of acetic anhydride, 1 part of titanium dioxide, 2 parts of the resin of Example 1 After mixing and mixing for 20 minutes, the wire is rolled into a drum machine and heated and kneaded. 5 After the kneading is completed, it is cooled with cold air and broken with a Speed Mill to obtain granular or powdered melamine-formaldehyde resin molding material. Formulation Example 2 Resin of Example 3 (solid content 75%) 70 parts of resin of Example 2 30 parts of paper powder 55 parts of talcum powder 15 parts of stearic acid 3 parts of dianhydride 1 part of titanium dioxide 2 parts of the same as in Formula Example 1 Method: A granular or powdered melamine-formaldehyde resin molding material is obtained.

A:\15785.ptd 第11頁 500758 五、發明說明(9) 配方實例3 實施例3之樹脂(固形份75%) 100份 木粉 55份 滑石粉 15份 硬脂酸鋅 3份 酜酸酐 1份 二氧化鈦 2份 依據配方實例1之相同方法, 獲得顆粒狀或粉狀之三 聚氰胺-甲酸樹脂成型材料。 配方實例4 實施例4之樹脂(固形份75%) 100份 紙粉 50份 滑石粉 10份 硬脂酸辞 3份 硬脂酸鎂 1份 酜酸酐 0· 5份 二氧化鈦 1份 依據配方實例1之相同方法, 獲得顆粒狀或粉狀之尿 素-甲醛樹脂成型材料。 配方實例5 實施例4之樹脂 70份 實施例2之樹脂 30份 木粉 55份 滑石粉 15份A: \ 15785.ptd Page 11 500758 V. Description of the invention (9) Formulation example 3 Resin of Example 3 (solid content 75%) 100 parts of wood powder 55 parts of talcum powder 15 parts of zinc stearate 3 parts of acetic anhydride 1 2 parts of titanium dioxide According to the same method as in Formula Example 1, granulated or powdered melamine-formic acid resin molding material was obtained. Formulation Example 4 The resin of Example 4 (solid content 75%) 100 parts of paper powder 50 parts of talcum powder 10 parts of stearate 3 parts of magnesium stearate 1 part of acetic anhydride 0.5 part of titanium dioxide 1 part of Formula Example 1 In the same way, a granular or powdery urea-formaldehyde resin molding material is obtained. Formulation Example 5 70 parts of resin of Example 4 30 parts of resin of Example 2 Wood powder 55 parts Talcum powder 15 parts

A:\15785.ptd 第12頁 500758 五、發明說明(ίο) 硬脂酸鋅 3份 硬脂酸鎂 1份 酜酸酐 0· 8份 二氧化鈦 1份 依據配方實例1之相同方法, 獲得顆粒狀或粉狀之尿 〇 素-三聚氰胺-甲醛樹脂成型材料 配方實例6 實施例5之樹脂 100份 紙粉 55份 滑石粉 15份 硬脂酸鋅 3份 亞硫酸 3份 二氧化鈦 2份 依據配方實例1之相同方法, 獲得顆粒狀或粉狀之三 聚氰胺-紛-曱_樹脂成型材料。 配方實例7 實施例1之樹脂(固形份75%) 70份 實施例6之樹脂 30份 紙粉 55份 滑石粉 15份 硬脂酸鋅 3份 亞硫酸辞 3份 二氧化鈦 2份 < 依據配方實例1之相同方法, 獲得顆粒狀或粉狀&/A: \ 15785.ptd Page 12 500758 V. Description of the invention (ίο) Zinc stearate 3 parts Magnesium stearate 1 part Magnetic anhydride 0.8 parts Titanium dioxide 1 part According to the same method as in Formula Example 1, obtain a granular or Powdered Urea-Melamine-Formaldehyde Resin Molding Material Formulation Example 6 The resin of Example 5 100 parts of paper powder 55 parts of talcum powder 15 parts of zinc stearate 3 parts of sulfurous acid 3 parts of titanium dioxide 2 parts The same as in Formula Example 1 Method, to obtain granular or powdered melamine-isocyanate resin molding material. Formulation Example 7 Resin of Example 1 (solid content 75%) 70 parts of resin of Example 6 30 parts of paper powder 55 parts of talcum powder 15 parts of zinc stearate 3 parts of sulfite 3 parts of titanium dioxide 2 parts < according to the formulation example 1 the same way to obtain granular or powdery & /

A:\15785.ptd 第13頁 500758 五、發明說明(11) 聚氰胺-酚-甲醛樹脂成型材料。 配方實例8 實施例3之樹脂(固形份75%) 70份 實施例7之樹脂 3 0份 紙粉 5 5份 滑石粉 1 5份 硬脂酸鋅 3份 亞硫酸鋅 3份 二氧化欽 2份 依據配方實例1之相同方法,獲得顆粒狀或粉狀之三 聚氰胺-酚-甲醛樹脂成型材料。 比較例1 100份 5 5份 實施例2之樹脂 紙粉 1 5份 3份 1份 2份 滑石粉 硬脂酸鋅 酜酸酐 二氧化鈦 、將上述原料於球磨機中混合6至8小時後’洩入滾筒機 ,犯,依據配方實例1之相同方法,獲得顆粒狀或粉 狀之二聚氰胺-曱酿樹脂成型材料。 比較例2 依據實施例1之反應方式 制水分而獲得固形份為6〇%之 但改變減壓乾燥之條件以控 樹脂,於1 0 0份該樹脂中添A: \ 15785.ptd Page 13 500758 V. Description of the invention (11) Melamine-phenol-formaldehyde resin molding material. Formulation Example 8 Resin of Example 3 (solid content 75%) 70 parts of resin of Example 7 30 parts of paper powder 5 5 parts of talc 1 5 parts of zinc stearate 3 parts of zinc sulfite 3 parts of dioxin 2 parts According to the same method as in Formulation Example 1, a granular or powdered melamine-phenol-formaldehyde resin molding material was obtained. Comparative Example 1 100 parts 5 5 parts of the resin paper powder of Example 2 15 parts 3 parts 1 part 2 parts talc powder zinc stearate gallate anhydride titanium dioxide, the above raw materials were mixed in a ball mill for 6 to 8 hours and then 'drained into a roller' Machine, guilty, according to the same method as in Formula Example 1, a granular or powdered melamine-brewed resin molding material was obtained. Comparative Example 2 According to the reaction method of Example 1, water was produced to obtain a solid content of 60%, but the conditions for drying under reduced pressure were changed to control the resin, and 100 parts of the resin was added.

A:\15785.ptd 第U頁 500758 五、發明說明(12) 25份紙漿,以捏合機捏合5〇分鐘後,於90 °C之烘箱内烘乾 2小時’而製得乾燥物a。 乾燥物A 150份 滑石粉 15份 硬脂酸鋅 3份 酜酸酐 1份 二氧化鈦 2份 將上述原料於球磨機中混合6至8小時後,可獲得粉狀 之三聚氰胺-甲盤樹脂成型材料 •,或洩入滚筒機内混練, 再依據配方實例1之相同方法, 酸樹脂成型材料。 比較例3 獲得顆粒狀之三聚氰胺-甲 依據實施例1之反應方式但改變減壓乾燥之條件以控 制水分而獲得固形份為50%之樹脂,於1〇〇份該樹脂中添加 2 5份紙漿’以捏合機捏合$ q分鐘後,於9 〇 °c之烘箱内棋乾 2小時,而製得乾燥物b。 乾燥物B 150份 硬脂酸鋅 3份 酜酸酐 0 · 5份 二氧化鈦 2份 將上述原料於球磨機中混合6至8小時後,可獲得粉狀 之尿素~甲醛樹脂成型材料;或洩入滾筒機内混練,再依 據配方實例1之相同方法,可獲得顆粒狀之尿素—甲醛樹脂 成型材料。A: \ 15785.ptd Page U 500758 V. Description of the invention (12) 25 parts of pulp are kneaded with a kneader for 50 minutes and then dried in an oven at 90 ° C for 2 hours' to obtain a dried product a. Dried product A 150 parts talc powder 15 parts zinc stearate 3 parts tartaric anhydride 1 part titanium dioxide 2 parts After mixing the above raw materials in a ball mill for 6 to 8 hours, a powdered melamine-formaldehyde resin molding material can be obtained, or Drain into the drum machine and knead, and then according to the same method of Formula Example 1, acid resin molding material. Comparative Example 3 Granular melamine-formaldehyde was obtained. According to the reaction method of Example 1, but changing the conditions for drying under reduced pressure to control moisture, a resin having a solid content of 50% was obtained. 25 parts of pulp was added to 100 parts of the resin. 'After kneading with a kneader for $ q minutes, it was dried in an oven at 90 ° C for 2 hours to prepare a dried product b. Dried product B 150 parts zinc stearate 3 parts acetic anhydride 0 · 5 parts titanium dioxide 2 parts After mixing the above raw materials in a ball mill for 6 to 8 hours, powdered urea ~ formaldehyde resin molding material can be obtained; or leaked into the drum machine After kneading, and according to the same method as in Formula Example 1, granular urea-formaldehyde resin molding material can be obtained.

A:\15785.ptd 第15頁 500758 五、發明說明(13) 比較例4 實施例6之樹脂 100份 紙粉 55份 滑石粉 15份 硬脂酸鋅 3份 亞硫酸鋅 3份 二氧化欽 2份 將上述原料於球磨機中混合6至8小時後,洩入滾筒機 内混練’再依據配方實例1之相同方法,獲得顆粒狀之三 聚氰胺-酚-甲醛樹脂成型材料。 比較例5 依據實施例5之反應方式但改變減壓乾燥之條件以控 制水分而獲得固形份為5〇%之樹脂,於1〇〇份該樹脂中添加 25份紙浆’以捏合機捏合5〇分鐘後,於9〇 〇◦之烘箱内烘乾 2小時,而製得乾燥物c。 1 50份 15份 乾燥物C 滑石粉 3份 3份 2份 硬脂酸辞 亞硫酸鋅 一氧化欽 將上述原料於球磨機中混合6至8小時後,洩入滾筒機 内混練,依據配方實例丨之相同方法,獲得顆粒狀之三聚 氰胺-酚-甲醛樹脂成型材料。 將配方實例1至8與比較例所得成品之特性列於表1。A: \ 15785.ptd Page 15 500758 V. Description of the invention (13) Comparative Example 4 The resin of Example 6 100 parts of paper powder 55 parts of talcum powder 15 parts of zinc stearate 3 parts of zinc sulfite 3 parts of dioxin 2 After mixing the above raw materials in a ball mill for 6 to 8 hours, the mixture was discharged into a drum machine and kneaded. Then, according to the same method as in Formula Example 1, a granular melamine-phenol-formaldehyde resin molding material was obtained. Comparative Example 5 A resin having a solid content of 50% was obtained according to the reaction method of Example 5 but changing the conditions for drying under reduced pressure to control moisture. 25 parts of pulp was added to 100 parts of the resin and kneaded by a kneader 5 After 0 minutes, it was dried in an oven for 2 hours to obtain a dried product c. 1 50 parts 15 parts dry matter C talcum powder 3 parts 3 parts 2 parts stearate zinc sulfite zinc oxide The above raw materials are mixed in a ball mill for 6 to 8 hours, and then drained into a drum machine for kneading, according to the formula example 丨In the same way, a granular melamine-phenol-formaldehyde resin molding material was obtained. The properties of the finished products obtained in Formulation Examples 1 to 8 and Comparative Examples are shown in Table 1.

A:\15785.ptd 第16頁 500758 _ 案號88111235_私年4月4日 秦正 五、發明說明(14) 匕一―一…u」 由表1可知本發明方法以液體胺基樹脂所配製之胺基樹脂 成型材料,在成品特性上並不遜於傳統者(比較例1至5 ), 甚至在成品流動性及熱變形溫度二點上更優於傳統冬成形 材料。由此可知本發明之成形材料確實具有進步性,而在 製程中不論成本上、環境上亦均具優點。 表1成品特性之比較 三聚氰胺-甲醒樹脂麵材料 尿素-(三聚氰胺)-甲醛樹脂成型材料 三聚氰胺-酚-甲醛樹脂成型材料 特1生 實例 1 _ 2 實例 3 腿 例1 t匕铰 例2 W5 實例 4 WJJ 實例 5 臓 例3 15^ 實例 6 EJj 貢例 7 配方 .實例 3 腿 例4 臟 例5 §i3i7(^spiral flow) (cm)* 80 85 85 80 75 85 85 80 85 80 85 80 75 (Chappy Strength) (kg-Xcm/cm Xcm) 4.0 4.2 4.2 4.2 3.8 4.0 3.8 ' 4.0 4.0 4.2 4.0 4.2 4.0 (Flexural Strength) (kg/mm Xxrtrn) 10 9.5 10 10 9 10 10 11 10 10 10 10 10.5 OcV/mm)料 (Dieleoric Strength) 10 10 10 10 11 10 10 11 10 10.5 10.5 10 11 耐13Il(sec)料 (Arc Resistance) 140 140 1S0 180 140 120 120 120 180 180 140 180 180 Ig^^lOhsuIation Resistance) (Ν)Ε10ΧΩ 60 40 60 20 60 60 1C0 1C0 60 50 60 20 •20 耐熱性CC)料 (Heat Resistance) 150 150 150 150 150 120 130 120 140 140 150 140 140 (Deflection Temp) 185 180 185 175 165 120 130 120 185 180 1S5 170 165 *流動性測試條件爲155flc X lOOkg/cni2 X 4(3g 料依據JIS K6911方法測試 11^1 — 15785,ptc 第 17 頁 2001* 04· 04‘018A: \ 15785.ptd Page 16 500758 _ Case No. 88111235_ Qin Zhengwu on April 4th, the description of the invention (14) 一一 —u ... From Table 1, we can know that the method of the present invention is based on liquid amine resin. The formulated amine-based resin molding materials are not inferior to the traditional ones in the characteristics of the finished products (Comparative Examples 1 to 5), and even better than the traditional winter molding materials in terms of fluidity and heat distortion temperature of the finished products. It can be seen from this that the forming material of the present invention is indeed progressive, and has advantages in terms of cost and environment in the manufacturing process. Table 1 Comparison of the characteristics of the finished product Melamine-methacrylic resin surface material urea- (melamine) -formaldehyde resin molding material melamine-phenol-formaldehyde resin molding material Special Example 1 _ 2 Example 3 Leg example 1 t-dagger example 2 W5 example 4 WJJ example 5 臓 example 3 15 ^ example 6 EJj tribute example 7 recipe. Example 3 leg example 4 dirty example 5 §i3i7 (^ spiral flow) (cm) * 80 85 85 80 75 85 85 80 85 80 85 80 75 75 ( Chappy Strength) (kg-Xcm / cm Xcm) 4.0 4.2 4.2 4.2 3.8 4.0 3.8 '4.0 4.0 4.2 4.0 4.2 4.0 (Flexural Strength) (kg / mm Xxrtrn) 10 9.5 10 10 9 10 10 11 10 10 10 10 10.5 OcV / mm) Dieleoric Strength 10 10 10 10 11 10 10 11 10 10.5 10.5 10 11 13Il (sec) Arc Resistance 140 140 1S0 180 140 120 120 120 180 180 140 180 180 Ig ^^ OhsuIation Resistance ( Ν) Ε10 × Ω 60 40 60 20 60 60 1C0 1C0 60 50 60 20 • 20 Heat Resistance 150 150 150 150 150 120 130 120 140 140 150 140 140 (Deflection Temp) 185 180 185 175 165 120 130 120 185 180 1S5 170 165 * Flowability test conditions are 155flc X 100kg / cni2 X 4 (3g material according to J IS K6911 method test 11 ^ 1 — 15785, ptc page 17 2001 * 04 · 04’018

Claims (1)

758 修正j丨 Μλ f zzzM 申請專利範圍 六 一種胺基樹脂成型材料之製法,其特徵為使用固形份 高於75%且至少含一個羥甲基之水溶性液體胺基樹脂, 另外配合華他固體或液體自硬性樹脂,於半乾燥狀態 下直接與其他添加劑在60至14〇 t之溫度加埶混練、冷 卻至15至4 (TC後造粒而製得; … 其中該其他固體或液體自硬性樹脂與該至少含一 個羥甲基之液體胺基樹脂之總量佔全部成分繚重 20至70重量%。 "" 2·如申請專利範圍第丨項之製法,其令之液體胺基樹脂係 使用選自尿素、三聚氰胺類胺基化合物或其衍生物盎 甲醛或其衍生物,在甲醛/胺基化合物之F/M莫耳比^ 1·〇至6· G之範圍内,使用鹼或鹼土金屬之氧化物或氫 氧化物或氨水及其他胺類鹼性物質作為催化劑而製 者。 3. 如申請專利範圍苐1項之製法,其中該添加劑為紙、木 粉纖維質材料、無機充填材料、滑劑、促進 料。 4. 如申請專利範圍第丨項之製法,其中該其他固體或液體 自硬性樹脂之量為該至少含—個羥甲基之胺基樹脂之 10至50重量%者。 5. 如申請專利範阻第3項之製法’其中該添加劑係含達8〇 重量%至95重量%之可通過80#篩之粒子,且添加量 基樹脂之25至75重量%者。 …胺 6. 如申請專利範圍第3項之製法,其中該無機充填材料 選自金屬氧化物及氫氧化物、金屬碳酸鹽、金屬硫酸'、758 Amended j 丨 Μλ f zzzM Patent application scope Six methods of manufacturing an amine-based resin molding material, which are characterized by using a water-soluble liquid amine-based resin with a solid content of more than 75% and containing at least one methylol group, in addition to Huata Solid or liquid self-hardening resin, in a semi-dry state, directly mixed with other additives at a temperature of 60 to 140 t, kneaded, and cooled to 15 to 4 (TC after granulation;… wherein the other solid or liquid The total amount of the hard resin and the liquid amine-based resin containing at least one methylol group accounts for 20 to 70% by weight of all the ingredients. &Quot; " The base resin is selected from urea, melamine-based amine-based compounds or derivatives thereof, aldehyde formaldehyde or derivatives thereof, and is used in a range of formaldehyde / amine-based F / M mole ratio ^ 1.0 to 6 · G. Alkali or alkaline earth metal oxides or hydroxides or ammonia and other amine alkaline substances are used as catalysts. 3. For example, the method of making a patent application scope item 1, wherein the additive is paper, wood flour fiber material Inorganic filling materials, lubricants, and accelerators. 4. According to the manufacturing method of item 丨, the amount of the other solid or liquid self-hardening resin is 10 to 50 of the amine-based resin containing at least one methylol group. 5. The production method according to item 3 of the patent application, wherein the additive contains 80% to 95% by weight of particles that can pass through 80 # sieve, and 25 to 75% by weight of the resin is added. % .... Amine 6. The production method according to item 3 of the scope of patent application, wherein the inorganic filling material is selected from the group consisting of metal oxides and hydroxides, metal carbonates, and metal sulfuric acid ', 15785.ptc 2001· 04· 〇4· 〇19 )υυ758 88111235 七年 修正 申請專利 "" ^^— -- 蜜或硫化物、金屬矽酸鹽及矽化物,礦物質粉及坡 纖維:其添加量為胺基樹脂重量之1至5 0重量%者。 如申請專利範圍第3項之製法,其中該滑劑為脂 劑、脂肪醯胺系滑劑、醇系滑劑、石臘系滑劑以 '滑 一素系α劑,其添加量為胺基樹脂重量之〇 發 2〇重量%者。 · 1重量%至 ^申請專利範㈣3項之製法,其中該促 系促進劑 '有機酸系促進劑、 為無機酸 機金屬鹽系促進劑,其添加比=;=劑、無 0.01至20重量%者。 】馬胺&樹知重量之 9. 一種由如申請專利範圍第丨至8 之胺基樹脂成型材料,其特項任一項之製法所製得 流動性及180至200 °c夕敖鉍p為具有80至95cm之成品 L之熱變形溫度者。15785.ptc 2001 · 04 · 〇4 · 〇19) υυ758 88111235 Seven-year amendment application patent " " ^^--honey or sulfide, metal silicate and silicide, mineral powder and slope fiber: its The amount added is 1 to 50% by weight based on the weight of the amine-based resin. For example, the manufacturing method of item 3 of the patent scope, wherein the lubricant is a fat agent, a fatty ammonium-based lubricant, an alcohol-based lubricant, and a paraffin-based lubricant, and the added amount is an amine group. Resin weight is 20% by weight. · 1% by weight to ^ method of patent application 3 items, wherein the accelerating accelerator 'organic acid accelerator, inorganic acid organic metal salt accelerator, the addition ratio =; = agent, no 0.01 to 20 weight %By. 】 Mamine & Tree Known Weight 9. A fluidity and 180-200 ° C bismuth produced from the amine-based resin molding material as described in the patent application No. p is a heat distortion temperature of the finished product L having 80 to 95 cm. 2001· 04· 04· 0202001 · 04 · 04 · 020
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