TW415965B - A process for the recovery of cobalt and/or manganese from ash containing cobalt and/or manganese as oxides thereof - Google Patents

A process for the recovery of cobalt and/or manganese from ash containing cobalt and/or manganese as oxides thereof Download PDF

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TW415965B
TW415965B TW86117333A TW86117333A TW415965B TW 415965 B TW415965 B TW 415965B TW 86117333 A TW86117333 A TW 86117333A TW 86117333 A TW86117333 A TW 86117333A TW 415965 B TW415965 B TW 415965B
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Taiwan
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bromide
manganese
cobalt
acid
ash
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TW86117333A
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Chinese (zh)
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David John Royall
Julie Ann Bartlett
Roger Gaskell Fairhurst
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Ici Plc
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Priority claimed from GBGB9623897.7A external-priority patent/GB9623897D0/en
Priority claimed from GBGB9625033.7A external-priority patent/GB9625033D0/en
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Publication of TW415965B publication Critical patent/TW415965B/en

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

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  • Manufacture And Refinement Of Metals (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Catalysts (AREA)

Abstract

Cobalt and/or manganese is recovered from the ash obtained following incineration of the catalyst containing residue arising from the liquid phase oxidation of an aromatic carboxylic acid such as terephthalic acid. Recovery is effected by contacting the ash with an organic acid or an organic acid anhydride such as acetic anhydride, optionally in the presence of bromide ions (e.g. HBr). So that the cobalt and/or manganese metals are recovered as monocarboxylic acid soluble salts thereof thus permitting recycle thereof to liquid phase oxidation process.

Description

415965 iL C7 五、創作説明(3 ) ,利用醋酸,將該等金羼加以固收。 美國專利第4 , 5 4 fi , 2 0 2號中,竭示了藉加入冰醋酸, 或冰醋酸與水的混合物,並將混合物在有歷力及遢拌裝置 的S應器中加熱的方式,自固態的芳香族羧酸焚燒爐灰份 中固收鈷及錳的方法。雖然吾人瞭解氫溴酸會輿鈷及錳的 氣化物相反應,但該案中所敘逑的反應卻並沒有溴时參與 經濟部中央標準局貝工消費合作社印策 而本發明所 錳的氣化物的灰 使甩或不使用溴 機酸酐相接觸並 最好t回收 醋酸鹽的型態1 本發明尤其 芳香族羧酸的-例如溴)所構成 相氧化處理步驟 含有催化金鼷的 吾人發琨, 收方法中的情況 方法中有引人溴 邸可大幅提升闸 本發明傜基 之後所取得的氣 ,但是,在使用 含有鈷及/或 步驟涉及:在 提供者亦為一種用以從其中 份中回收鈷或錳的方法,其 離子的情況下,促使灰份與一有機酸或有 將鈷或錳加以回收。 而得的鈷或錳,是以其各自的可溶於水的 現。 適用於在芳香族羧酸的生産 過程中,經由 烴前驅質置於一由一鈷或錳或一促進劑( 溶劑内施以液 所取得的其中 的催化条統所組成的一羧酸 ,在渉及因母液淨流的處理 殘料的處理。 鈷及錳的画牧可以不引入溴 下,利用醋酸或醋酸酐來進 化物離子的情況f,不必仰 牧的效果。 於理論理解,在繼熱解(例 化鈷或氣化錳,其溶解雖然 了 一脂肪酸或脂肪酸酐,例 化物離子到回 行,但在反應 賴高溫高壓, 如焚燒處理) 本來非常困難 如,在,使用了 ---------ly-------訂—-------Φ (t先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家橾隼(CNS ) A4規格(210X297公釐)415965 iL C7 V. Creation Instructions (3): The acetic acid is used to solidly collect these gold tinctures. U.S. Patent No. 4, 5 4 fi, 202 describes the method of adding glacial acetic acid, or a mixture of glacial acetic acid and water, and heating the mixture in a S reactor with a history and mixing device. A method for solidly collecting cobalt and manganese from solid ash of an aromatic carboxylic acid incinerator. Although I understand that the hydrobromide will react with the gaseous phase of cobalt and manganese, the reaction described in this case does not include bromine when it participates in the policy of the Central Bureau of Standards of the Ministry of Economic Affairs, the Shellfish Consumer Cooperative, and the manganese gas of the invention The ash of the compound is in the form of contact with or without the use of bromoanhydride and preferably recovers the acetate salt. 1 The phase oxidation treatment step of the present invention, especially of aromatic carboxylic acids such as bromine, contains catalyzed gold. Circumstances in the collection method In the method, there is an attractive bromine that can greatly improve the gas obtained after the invention is based on the hydrazone. However, the use of cobalt and / or steps involves: the provider is also a In the method of recovering cobalt or manganese, in the case of ions, it promotes the recovery of ash and an organic acid or cobalt or manganese. The resulting cobalt or manganese is their respective water-soluble appearance. It is suitable for the production of aromatic carboxylic acid. A carboxylic acid composed of a catalytic system obtained by applying a solution of cobalt or manganese or a promoter in a solvent via a hydrocarbon precursor is used in渉 and the treatment of residual materials due to the mother liquor net flow. The painting of cobalt and manganese can use acetic acid or acetic anhydride to evolve the ion ions without introducing bromine. F, no need to rely on the effect of grazing. In the theoretical understanding, the following Pyrolysis (exemplified by cobalt or gasified manganese, although its dissolution is a fatty acid or fatty acid anhydride, the ions of the compounds return to the line, but the reaction depends on high temperature and pressure, such as incineration). It was originally very difficult, such as, using- ------- ly ------- Order ----------- Φ (t read the precautions on the back before filling out this page) This paper size is applicable to China National Standard (CNS) A4 Specifications (210X297 mm)

經濟部中央標準局員工消費合作社印製 415965 A7 __B7五、發明説明(/ ) 本發明係有鼷芳番族羧酸,比方說,對酞酸及異鉍酸 的生産方法β 就對酞酸一般在商業上的製造而言,其方法不外乎將 對二甲苯躲同氣併置於一具有較低階的脂肪族羧酸溶劑( 例如醋醸),以及一已溶解的重金屬催化条統(通常為鈷 、錳及一溴的促進劑)所構成之液相内進行氣化反應β自 反匾瀘内抽取一存在於溶剤内的對砵酸泥漿,施以一固液 相分離方法,以生成粗级對於酸晶鼷(該晶體可再作進一 步的處理),同時又生成有母液濾出物,該母液中的成份, 除了供作氣化反應使用的催化劑及促進尚之外,尚包括了 已溶解的對私酸以及多種不同的伴随生成物(By-products) 及雜質。造些伴隨生成物及雜質的來源不止一種,比方説 ,供作反應處理的對二甲苯進料中的少數雜霣,也可能是 肇因於對二甲苯的不完金氧化所産生的局部氣化生成物或 在對二甲苯氣化成對私酸的競抗倒反應中所生成的伴隨生 成物。 將回收而得的母液,抽取其中的一大部份,回輪至氣 化反暱方法内,以便將催化劑及促進劑回輪至氧化反應方 法内,而在此同時油取其中之一小部份作為淨流·翰至一 溶劑画收糸統内,以將反應過程中的雜質及伴随生成物的 幅量抑控於可容忍的範圍之内。就溶劑回收糸统而言,其 中的母液淨流必須作一蒸發處理,以將存在於母液淨流内 的相當幅貴的脂昉酸溶劑及水(可回输至氣化反應方法内> 加以排除掉,而留下一含有對认酸、雜質/伴隨生成物及 (請先閱讀背面之注項再填寫本頁)Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 415965 A7 __B7 V. Description of the invention (/) The present invention is an aromatic aromatic carboxylic acid. For example, the production method of p-phthalic acid and isobismuth acid β For commercial manufacturing, the method is nothing more than hiding para-xylene from the same air and placing it in a lower-order aliphatic carboxylic acid solvent (such as acetic acid), and a dissolved heavy metal catalytic system (usually It is a promoter of cobalt, manganese and monobromide) to carry out gasification reaction in the liquid phase. Β Extracts an acetic acid slurry that exists in the solution from the retort, and applies a solid-liquid phase separation method to generate Crude grade acid crystal rhenium (the crystal can be further processed), and at the same time, a mother liquor filtrate is generated. In addition to the catalyst and promotion for the gasification reaction, the components in the mother liquor also include Dissolved para-acids and many different by-products and impurities. There are more than one source of concomitant products and impurities. For example, a few impurities in the para-xylene feed for reaction treatment may also be local gas caused by the endless gold oxidation of para-xylene. A chemical product or a concomitant product produced in the reaction of p-xylene gasification to a pivalic acid. A large part of the recovered mother liquor is extracted and recycled to the gasification reaction method, so that the catalyst and the accelerator are recycled to the oxidation reaction method, and at the same time, a small part of the oil is taken As a net flow, the solvent is collected in a solvent system to control the amplitude of impurities and accompanying products in the reaction process to a tolerable range. As far as the solvent recovery system is concerned, the net stream of the mother liquor must be subjected to an evaporation process in order to return a considerable amount of the fatty acid solvent and water (which can be returned to the gasification reaction method) existing in the net stream of the mother liquor. Exclude it, leaving one that contains acid, impurities, and accompanying products (please read the note on the back before filling this page)

*1T - 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0X297公釐)* 1T-This paper size applies to China National Standard (CNS) A4 specification (2 丨 0X297 mm)

五、創作説明(ίΗ) 醋酸酐,又併用了一溴化物的情況下,即可輕易加以溶解 〇 溴化物可以在一開始的階段時先行引入,以使酐與灰 份的反應作用得以在有溴化物離子介人的情況下順利進行 。但是,亦可反其道而行,在酸或酐與灰份已經開始反應 作用之後,才將溴化物離子引入。所採用的澳化梅的量’ ---------/------:-訂---------京 (_請先閱讀背面之注意事項再填寫本頁) 經濟部中央標率局負工消費合作社印袈 本紙張尺度適用中國國家標準(CNS) Α4規格(210Χ297公釐) ί ~~~V. Creative Instructions (ίΗ) Acetic anhydride can be easily dissolved in the case of using monobromide. Bromide can be introduced at the beginning stage, so that the reaction between the anhydride and ash can be used. The case of bromide ions intervened smoothly. However, the opposite is also possible, after the acid or anhydride has reacted with the ash before the bromide ion is introduced. The amount of Australian plum used '--------- / ------:-Order --------- Jing (_Please read the precautions on the back before filling in this Page) The printed standard of the printed papers of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs applies to the Chinese National Standard (CNS) Α4 specification (210 × 297 mm) ί ~~~

415965 經濟部中央標準局員工消費合作社印製 A7 B7五 '發明説明(二) 若干存在於原始母液濾出物内的重金臑催化爾所組成的濃 縮物β如此的灌縮物即殘料.邸可視為廢棄物處理掉,但 若仍有經濟價值可言,則可作進一步的利用處理,以便將 其中有價值的成份,例如金羼催化劑加以回收,循環利用 。對於此一殘料的典型的下游處理模式包括:催化_的回 收、加熱分解,以將殘料中的所有有捸成份全部清除掉( 例如可在一高溫爐内作一焚燒處理),或作一免氣或有氣 的生物學處理,以減少對於化學氧的需求(COD)。 所以,本發明的要旨乃在有已到達第三期或第四期, 且輻董已達相當位準的催化金属介入的前提下,經由上述 殘料的熱解方法,而將該等存在於殘料中之原型態為該等 催化金颶的氣化物的成份脱氣後加以回收的方法,因此該 等催化金靨不溶於水,且僅能勉強溶於酸中6 在美國專利3341470號案中所掲示者為將殘料焚燒為 灰份氣化物,以及繼而將如此所取得的灰份置於其中含有 氯化物的硫酸内加以溶解的方法。錳及鈷的成份藉差以硪 酸納對其溶液作一處理,以使钻及錳成為其磺酸沉澱析出 的方式加以回收β如此回收而得的硪酸鹽再以醋酸處理, 以製得醋酸鹽回_至氣化反應方法内操作。 在美國專利478662 1號案中所掲示者乃自存在於焚化 燼的灰份内,由飛灰份及熔渣所構成的混和金饜氧化物中 回收以其醋酸鹽的形態所呈現的鈷、錳及其他金屬的方法 ,該方法係在以鈷金屬或聯胺( hydrazine >併用為遢原 劑的情況下,在近乎沸點或回流溫度以及大氣壓的條件下 (請先閲讀背面之注意事項再填寫本頁) 訂 本紙張尺度適用中國國家標準(CNS > A4规格(210X297公釐) 415965 iL C7 五、創作説明(3 ) ,利用醋酸,將該等金羼加以固收。 美國專利第4 , 5 4 fi , 2 0 2號中,竭示了藉加入冰醋酸, 或冰醋酸與水的混合物,並將混合物在有歷力及遢拌裝置 的S應器中加熱的方式,自固態的芳香族羧酸焚燒爐灰份 中固收鈷及錳的方法。雖然吾人瞭解氫溴酸會輿鈷及錳的 氣化物相反應,但該案中所敘逑的反應卻並沒有溴时參與 經濟部中央標準局貝工消費合作社印策 而本發明所 錳的氣化物的灰 使甩或不使用溴 機酸酐相接觸並 最好t回收 醋酸鹽的型態1 本發明尤其 芳香族羧酸的-例如溴)所構成 相氧化處理步驟 含有催化金鼷的 吾人發琨, 收方法中的情況 方法中有引人溴 邸可大幅提升闸 本發明傜基 之後所取得的氣 ,但是,在使用 含有鈷及/或 步驟涉及:在 提供者亦為一種用以從其中 份中回收鈷或錳的方法,其 離子的情況下,促使灰份與一有機酸或有 將鈷或錳加以回收。 而得的鈷或錳,是以其各自的可溶於水的 現。 適用於在芳香族羧酸的生産 過程中,經由 烴前驅質置於一由一鈷或錳或一促進劑( 溶劑内施以液 所取得的其中 的催化条統所組成的一羧酸 ,在渉及因母液淨流的處理 殘料的處理。 鈷及錳的画牧可以不引入溴 下,利用醋酸或醋酸酐來進 化物離子的情況f,不必仰 牧的效果。 於理論理解,在繼熱解(例 化鈷或氣化錳,其溶解雖然 了 一脂肪酸或脂肪酸酐,例 化物離子到回 行,但在反應 賴高溫高壓, 如焚燒處理) 本來非常困難 如,在,使用了 ---------ly-------訂—-------Φ (t先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家橾隼(CNS ) A4規格(210X297公釐)415965 A7 B7 printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs of the People's Republic of China (5) Invention description (2) Several concentrates such as heavy metal catalysts present in the filtrate of the original mother liquor, such as condensate β, are residues. It can be regarded as waste disposal, but if there is still economic value at all, it can be further used for treatment, in order to recover valuable components, such as gold catalyst, for recycling. The typical downstream processing mode for this residue includes: catalytic recovery, thermal decomposition, to remove all the radon components in the residue (for example, an incineration treatment in a high temperature furnace), or An aerobic or aerobic biological treatment to reduce the need for chemical oxygen (COD). Therefore, the gist of the present invention is to exist in the third stage or the fourth stage, and the catalyst metal has reached a certain level of intervention, through the pyrolysis method of the above-mentioned residues, so that these exist in The prototype state in the residue is the method of degassing the components of the catalytic gold hurricane and recovering them. Therefore, the catalytic gold tincture is insoluble in water and can only be slightly soluble in acid. 6 US Patent No. 3341470 What is shown in the case is a method of incineration of the residue into an ash gaseous substance, and then dissolving the ash thus obtained in sulfuric acid containing chloride therein. The components of manganese and cobalt are treated with sodium osmium acid solution, so that the drill and manganese can be recovered in the form of precipitation of sulfonic acid. The phosphonium salt thus recovered is then treated with acetic acid to obtain The acetate is operated back to the gasification reaction method. In the case of U.S. Patent No. 4,786,661, the cobalt, which is present in the form of its acetate, is recovered from the mixed gold osmium oxide composed of fly ash and slag in the ash content of incinerated ash. Manganese and other metals, this method is based on cobalt metal or hydrazine (hydrazine > combined with rhenium agent, under the conditions of near boiling point or reflux temperature and atmospheric pressure (please read the precautions on the back before (Fill in this page) The size of the paper used for this edition is in accordance with the Chinese national standard (CNS > A4 size (210X297 mm) 415965 iL C7. V. Creation Instructions (3)) The acetic acid is used to collect these gold tinctures. US Patent No. 4 No. 5 4 fi, No. 202 shows the method of adding glacial acetic acid, or a mixture of glacial acetic acid and water, and heating the mixture in a S reactor with a calendar and mixing device. A method for the solid recovery of cobalt and manganese in the ash of an aromatic carboxylic acid incinerator. Although I understand that hydrobromic acid reacts with the gaseous phase of cobalt and manganese, the reaction described in this case does not participate in the economy without bromine Central Bureau of Standardization The ash of the manganese gaseous substance produced by the present invention is in the form of contact with or without the use of bromoanhydride and preferably recovers the acetate form. 1 The present invention is particularly composed of aromatic carboxylic acids such as bromine). The oxidation treatment step contains my hair catalyzed by gold, and the method in the collection method has an attractive bromine that can greatly improve the gas obtained after the hydrazone of the present invention is used. However, the use of cobalt and / or steps involves: In the case where the provider is also a method for recovering cobalt or manganese from its contents, in the case of ions, it promotes the recovery of ash and an organic acid or the recovery of cobalt or manganese. The resulting cobalt or manganese is Each of them is soluble in water. It is applicable to the catalysis obtained by the application of a hydrocarbon precursor in the production of aromatic carboxylic acids via a cobalt or manganese or a promoter The monocarboxylic acid composed of the system is treated with radon and the residual material due to the net flow of the mother liquor. The painting of cobalt and manganese can be evolved using acetic acid or acetic anhydride without introducing bromine. The effect of animal husbandry. Understand that after pyrolysis (instantiated cobalt or gasified manganese, its dissolution although a fatty acid or fatty acid anhydride, the ions of the compounds return to the line, but the reaction depends on high temperature and pressure, such as incineration treatment) was originally very difficult, such as, Used --------- ly ------- Order ----------- Φ (t read the precautions on the back before filling this page) This paper size is applicable to Chinese countries 橾 隼(CNS) A4 specification (210X297 mm)

五、創作説明(ίΗ) 醋酸酐,又併用了一溴化物的情況下,即可輕易加以溶解 〇 溴化物可以在一開始的階段時先行引入,以使酐與灰 份的反應作用得以在有溴化物離子介人的情況下順利進行 。但是,亦可反其道而行,在酸或酐與灰份已經開始反應 作用之後,才將溴化物離子引入。所採用的澳化梅的量’ ---------/------:-訂---------京 (_請先閱讀背面之注意事項再填寫本頁) 經濟部中央標率局負工消費合作社印袈 本紙張尺度適用中國國家標準(CNS) Α4規格(210Χ297公釐) ί ~~~V. Creative Instructions (ίΗ) Acetic anhydride can be easily dissolved in the case of using monobromide. Bromide can be introduced at the beginning stage, so that the reaction between the anhydride and ash can be used. The case of bromide ions intervened smoothly. However, the opposite is also possible, after the acid or anhydride has reacted with the ash before the bromide ion is introduced. The amount of Australian plum used '--------- / ------:-Order --------- Jing (_Please read the precautions on the back before filling in this Page) The printed standard of the printed papers of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs applies to the Chinese National Standard (CNS) Α4 specification (210 × 297 mm) ί ~~~

415965 A? ___ B7 五、發明説明(y ) 相對於每一契耳的鈷或錳而言,使用0.5〜1.5或1.8莫耳 即可,只要不超過2. Q莫耳,即為允當。 就本發明方法的實際操作而言,所使用的溴化物的量 只要大致與灰份中的鈷或錳的成份的契耳當量相當即可。 若所使用的溴化物的量少於灰份中的鈷或錳成份的莫耳當 量時,則金屬的回收效率將必相對降低。但,瘥不見得就 是一項不利因素,因為在一比較欠缺溴化物的體糸下進行 操作,反而可以促成最後溴化物對金屬成扮的比例值的彈 性諏整,且可減少甚至消除對其中含有樓成份的準氣釀( offgas)處理的需求β又,在此情況下,在方法處理後所 殘餘的其中含有鈷/錳成份的殘料即可再回循供本發明方 法作進一步的處理& 最好,所使用的溴化物以溴化氫為宜,但若擬採用其 他溴化物,例如乙醒基溴化物亦可。所以,就本發明之一 理想實施例而言,存在於灰份内的每一其耳的金羼,宜相 對使用約一莫耳的溴化氫。舉例言之,在灰份内同時含有 姑及錳的氣化物的情況下,所使用的溴化氫的比例,柑對 於造兩種金颺而言,均各為一莫耳對一莫耳《»但是,亦可 採用較大量的溴化物,但是,在此情況下,在反應方法中 所生成的溴可能會造成含溴氣體的處理及處置方面的問題 β但,這也不見得完全是不利的,溴化物的量較多,反而 有利於對為生産芳香族羧酸,而翰至一氣化反應方法内的 催化劑/促進劑糸統中的溴化物對金颶的比值的控制。 在有採用溴化物離子的情況下,溴化物以引入於一液 相媒之内的方式為宜,例如,可置於一腊肪酸(比方說醋 本紙張尺度適用中國國家標準(CNS ) Λ4規格(210X297公釐) 4 (請先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局員工消費合作社印製 415965 Α7 Β7 五、發明説明(r) 酸)内或置於水内溶解β 所採用的有機酸酐可以使用醋酸酐所採用的有檐酸 使用醋酸邸可》取一有機酸及一有機酸辭的混合物使用, 經證明極為有效〇最好此一混合物像含有一有槺酸及一相 對匾的酸酐,例如:取一由醋酸及酸酐所組成的混合物卽 可適合供用於反應方法内。若在摻有一有機酐的供反應用 混合物中有水存在於其内,則酐可完全或局部水解成相對 應的酸,且在反應方法中有使用所生成的酸酐混合物。 含有金屬氣化物的灰份可以是濕的。灰渣可從一娓態 氣化方法中回收而得,也可以是先在一乾燥狀態下生産, 然後再作一沖洗處理後所取得》 吾人發現在反應方法中,所出現的水份,若超出一定 的幅量,則可能對金屬的回收迪成不利的影鬱。反應方法 以在乾燥情況下進行為宜,但若保留一些水份,亦不致於 對鈷或錳的回收造成重大不利的影響。反醮中的混合物中 的水的成份,其重量百分比例最好能抑控於30 %以下,能 維持於20Χ以下更好,若能抑制於15Χ以下就更為理想。水 份的介入反應的混合物中,其方式可為使用滬灰份或比方 説,将溴化氳置於水中W成水溶液的型態引人。以一有機 酐介入的情況下,將濕灰份引人反臁方法内,可以藉使之 與酐發生作用,以形成相對應的酸之方式,將其中一部份 的水份加以排除β因此,如果使用湄灰份,而又希望在相 當乾燥的條件下進行反應操作時,可在一有機酐内添加以 濕灰份,如此卽可使水份與之反應而生成一有機酸•此一 本紙張尺度適用中國國家標率(CNS ) Α4規格(210Χ297公釐) (請先閱讀背面之注意事項再填寫本頁)415965 A? ___ B7 V. Description of the invention (y) For each cobalt or manganese, use 0.5 ~ 1.5 or 1.8 moles, as long as it does not exceed 2. Q moles, which is acceptable. For the practical operation of the method of the present invention, the amount of bromide to be used may be approximately equivalent to the equivalent of the cobalt or manganese component in the ash. If the amount of bromide used is less than the molar equivalent of the cobalt or manganese component in the ash, the metal recovery efficiency will be relatively reduced. However, radon may not be a disadvantage, because operating under a relatively bromine-deficient body can actually promote the elastic adjustment of the final bromide to metal ratio, and can reduce or even eliminate it. The demand for offgas processing containing ingredients is β. In this case, the residual material containing the cobalt / manganese content remaining after the method treatment can be recycled for further processing by the method of the present invention. & Preferably, the bromide used is hydrogen bromide, but other bromides such as ethyl bromide are also possible. Therefore, in accordance with one preferred embodiment of the present invention, about one mole of hydrogen bromide is preferably used for each ear of gold tincture present in the ash. For example, in the case where the ash also contains a manganese-containing gas, the proportion of hydrogen bromide used is one mole to one mole for the two types of Jinyang. »However, a larger amount of bromide can also be used. However, in this case, the bromine generated in the reaction method may cause problems in the treatment and disposal of the bromine-containing gas. However, this may not be entirely disadvantageous. Of course, the amount of bromide is large, but it is conducive to the control of the ratio of bromide to golden hurricane in the catalyst / promoter system in the Han to Yi gasification reaction method for producing aromatic carboxylic acids. In the case where bromide ions are used, the bromide is preferably introduced into a liquid medium, for example, it can be placed in a fatty acid (for example, the vinegar paper size applies the Chinese National Standard (CNS) Λ4 Specifications (210X297 mm) 4 (Please read the precautions on the back before filling this page) Order printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 415965 Α7 Β7 V. Description of the invention (r) Acid) or dissolve in water β The organic acid anhydride used can be acetic anhydride, the eucalyptic acid used is Acetic Acid, and a mixture of an organic acid and an organic acid is proven to be extremely effective. It is best that this mixture contains an acid And an acid anhydride of a relative plaque, for example, a mixture of acetic acid and acid anhydride can be used for the reaction method. If water is present in the reaction mixture containing an organic anhydride, the anhydride can be completely or partially hydrolyzed to the corresponding acid, and the resulting acid anhydride mixture is used in the reaction method. The ash containing metal vapors may be wet. Ash and slag can be recovered from a single-state gasification method, or it can be produced after being dried in a dry state, and then processed after being washed. "I found that in the reaction method, the water that appears, if Exceeding a certain amount may adversely affect the recovery of metal. The reaction method is preferably carried out under dry conditions, but if some water is retained, it will not cause a significant adverse effect on the recovery of cobalt or manganese. The weight percentage of the water component in the mixture in the reaction is preferably controlled to 30% or less, and it is better to maintain it to 20 × or less, and it is more desirable to suppress it to 15 × or less. The mixture of water involved in the reaction can be made by using Shanghai ash or, for example, putting thallium bromide in water to form an aqueous solution. In the case of the intervention of an organic anhydride, the wet ash is introduced into the reaction method, and it can be reacted with the anhydride to form a corresponding acid, and a part of the water is excluded. Therefore, If you use Mae ash, and you want to carry out the reaction operation under relatively dry conditions, you can add wet ash in an organic anhydride, so that water can react with it to generate an organic acid. This paper size applies to China National Standards (CNS) Α4 specifications (210 × 297 mm) (Please read the precautions on the back before filling this page)

,S1T 經濟部中央橾隼局員工消費合作社印製 ' ’ A7 B7 五、發明説明(L ) 水解反匾會生成熱,所以當熱已停止,不再産生時,即意 味著水解已告完成,其後可再添加酐或乾酸,以終结整傾 反應方法。但若灰份内的水份太多,多到無法經由酐的水 解加以排除,或者所使用者為酸而非酐,以致其中所存在 的水份對於整餡反應足以構成不利的影響時,則自可在灞 灰份引入反醮艙内之前先作一乾燥處理。因存介於反應方 法内的水份對酐的水解作用所生成的有機酸,最好在反應 方法的s—部位内運用,例如,可回输至一芳香族酸前驅 質氣化反應方法内,而灰份正是自此一反應方法中生成》 所生成的酸劑的數量與催化_回收反應混合物内的水份的 數量成正比,所以,在反應混合物内所容許的水的數量宜 加以控制,以使回收而得的催化劑對所生成的酸爾的比例 值恰好適於直接回輸至起始氧化反鼴方法内·》 經濟部中.央標準局員工消費合作杜印裂 (請先閱讀背面之注意事項再填寫本頁) 美國專利44 91)297號案中所掲示者為使鈷及錳,以其 各自的草酸鹽二水合物鹽類的塱態,自氣化母液中直接沉 鎩而出加以回收,繼之以將該等草酸鹽二水合物置入醋酸 或醋酸酐内與乙酵基溴化物、溴化氫或兩者的混合物作用 ,以轉換為一可溶解於醋酸内的型態。但該美國專利案4490297 號案並未渉及殘料的焚化,亦未論及如何將處於第三期或 第四期的鈷或錳,以其各自的氣化物之型態,加以回收利 用的問題。在此同一美國專利案44 90 2 9 7號案中有提到針 對每一莫耳的鈷或錳草酸鹽二水合物,宜使用2〜4,尤其 最好是2〜2·2某耳的溴化氫及3〜4,尤其最好是3·1〜3_5 莫耳的醋酸酐。 本紙張尺度適用中國國家標準(CNS ) Α4規格{ 21〇X 297公釐)S1T printed by the Consumer Cooperative of the Central Government Bureau of the Ministry of Economic Affairs' A7 B7 V. Description of the Invention (L) The hydrolysis of the anti-plaque will generate heat, so when the heat has ceased and no longer occurs, it means that the hydrolysis has been completed, Thereafter, an anhydride or a dry acid may be added to terminate the trimming reaction method. However, if there is too much water in the ash, it can not be eliminated by the hydrolysis of the anhydride, or the user is an acid rather than an anhydride, so that the water present therein is sufficient to adversely affect the whole filling reaction. It can be dried before the ash content is introduced into the reaction tank. The organic acid generated by the hydrolysis of the anhydride by the water contained in the reaction method is preferably used in the s-position of the reaction method. For example, it can be returned to an aromatic acid precursor gasification reaction method. The ash content is generated from this reaction method. The amount of acid agent generated is directly proportional to the amount of water in the catalytic-recovery reaction mixture. Therefore, the amount of water allowed in the reaction mixture should be added. Control so that the ratio of the recovered catalyst to the acid acid produced is just suitable for direct input back to the initial oxidation reaction method. "In the Ministry of Economic Affairs. Central Standards Bureau employee consumption cooperation Read the notes on the back and fill in this page) US Patent No. 44 91) No. 297 shows that the cobalt and manganese in the state of their respective oxalate dihydrate salts are directly from the gasified mother liquor Sink out and recover, and then place the oxalate dihydrate in acetic acid or acetic anhydride and interact with ethynyl bromide, hydrogen bromide, or a mixture of both to convert it into a soluble in acetic acid. Within the form. However, the US Patent No. 4490297 did not deal with the incineration of the residue, nor did it discuss how to recover the cobalt or manganese in the third or fourth phase with their respective gaseous forms. problem. In this same U.S. Patent No. 44 90 2 9 7 it is mentioned that for each mole of cobalt or manganese oxalate dihydrate, 2 to 4, preferably 2 to 2 or 2 Hydrogen bromide and 3 ~ 4, especially preferably 3 · 1 ~ 3_5 mole of acetic anhydride. This paper size applies Chinese National Standard (CNS) Α4 specification {21〇X 297 mm)

—V 1:产' 415965 A? B7 經濟部中央標準局貝工消費合作社印製 五、發明説明 ( 'Ϊ ) 1 但 吾 人 所 發 現的一 頗 為 令 人 驚訝 的 事 實是 * 在有使用 I 溴化物 的 情 況 下 ,尤其 在 有 使 用 溴 化 氳 的 慵況 下 ,即使所 1 1 I 使用 的 劑 量 低 於 標準化 學 計 量 標 準 « 金 羼 的回 收 率亦可大 1 I 請 1 I 幅提 升 ! 而 且 若溴化 物 能 增 加 至 灰 份 中 的每 一 莫耳金屬 先 閲 I I 1 I 均可 對 配 一 莫耳 的溴化物 之 地 步 » 則 回 收 效率 接近100%。 背 面 1 I 之 1 由於所使 用 的 溴化物的 數 最 只 須 限 制 至 每 一莫 耳的鈷或猛 注 素 1 1 對配 —· 莫 耳 的 溴化物之 程 度 t 所 以 回 收 而 得的 金 屬之溴化 項 再 1 I 物對结 催 化 金 臑 的比值 乃 適 於 直 接 回 输 至 芳香 族 酸的氣化 填 寫 1 本 I 反應 方 法 内 0 頁 、J 1 1 焚 化 處 理 可 揉任何 一 種 適 當 的 技 術 % 經由 高 溫镇化作 1 [ 用, 而 將 厂 可 據 以生成 灰 份 的 J 液 體 或 固 體加以 處理的方 1 式。 1 訂 I 就本 發 明 的 一更精 確 的 觀 點 而 言 » 其 所提 供 者乃一用 1 以生 産 一 芳 香 族 羧酸, 例 如 9 一 用 生 産 對瓠酸或異鉍酸的 1 1 方法 * 其 中 1 I 該 芳 香 族 的 一前驅 質 置 於 含 有 厂 鈷或 錳 的化合物 1 1 A 的」 催 化 系 统 的 C】〜Cb 一 羧酸溶 劑 内 » 作一 氣 化處理β 1 [ 反 應 匾 域 内油出 一 含 有 存 在 於溶剤 基質 母 液内的芳 1 1 香族 酸 晶體 成份的泥漿 然後将 此 泥 漿 作 一固 液 相分離處 1 | 理, 且 至 少 提 取 一部份的母 液加以 處理 * 以生 産 出含有 1 I 姑或 錳 的殘料 〇 1 該殘料 作 一 熱解處 理 J 以 生 成 含 有 鈷或鏟 的 氣化物的 1 1 灰渣 ύ 1 I 最 好 是在 有 溴化物離 子 介 入 的 情 況 下 ,以 __. 有機酸或 1 1 1 本紙張尺度適用中國國家標準(CNS〉厶4規格(210X297公釐)—V 1: Produce '415965 A? B7 Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (' Ϊ) 1 But what I found quite a surprise is that * I bromine is used In the case of compounds, especially in the case of thallium bromide, even if the dosage of 1 1 I used is lower than the standard stoichiometric standard «recovery rate of gold tincture can be larger 1 I please increase 1 I! And if Bromide can be added to the ash. For every mole of metal, see Read II 1 I. For a mole of bromide, the recovery efficiency is close to 100%. Since the number of bromide used on the back 1 I 1 is limited to each mole of cobalt or bolus injection 1 1 to match the degree of the bromide of moore, the bromine recovered from the metal The chemical term and the ratio of I to catalyzed gold tincture are suitable for direct return to the gasification of aromatic acids. Fill in 0 pages of this I reaction method, J 1 1 Incineration can be rubbed with any appropriate technology.% Via High-temperature ballasting is used in a way that the plant can generate J-liquid or solid based on ash for treatment. 1 Order I In terms of a more precise view of the invention »it is provided by the use of 1 to produce an aromatic carboxylic acid, such as 9-the 1 1 method of producing p-ortho- or isobismuth acid * where 1 I The aromatic precursor is placed in the catalytic system containing the plant cobalt or manganese compound 1 1 A "C" ~ Cb in a carboxylic acid solvent »for a gasification treatment β 1 [the oil produced in the reaction plaque contains a presence A slurry of aromatic 1 1 aromatic acid crystals in the mother liquor of the dissolving matrix, and then use this slurry as a solid-liquid phase separation 1 | process, and extract at least a part of the mother liquor for processing * to produce 1 I or Manganese residue 〇1 This residue is subjected to a pyrolysis treatment J to produce a gaseous product containing cobalt or a shovel 1 1 ash residue 1 I It is best to use __. Organic with the intervention of bromide ions Acid or 1 1 1 This paper size applies to Chinese national standards (CNS> 厶 4 specifications (210X297 PCT)

v/ 415965 A7 B7 五、發明説明(S ) 有機酸酐作一處理,以回收得以鹽類的型觼所呈現且可溶 於前逑一羧酸内的鈷或錳。 當溴離子存在時,可以在一開始的時候溴離子就已存 在,或者,在有機酸(或酐)開始反應之後,將溴離子引 入。 回收的鉉以及/或錳豔最好回循至氣化匾域内。 在使用溴化物離子的情況下,本發明方法的一明顙的 有利因素在於:在回收而得的成份中,最後所成就的溴化 物對金屬的比值,可在毋痛著藉助於如同美國專利案44 90297 中所敘述的對溶液中的溴化物的濃度加以諝整或作一處置 的情況下,順利回輸至氣化區域内,這是因為本發明回收 方法中,對於溴化物離子的處理而言,大致可維持一標準 化學計量原則,亦卽就每一其耳的溴化物而言,可萃取出 恰為一莫耳的鈷或錳成份β 相形之下,雖然正如美國專利案4786621中所指出 的,氫溴酸可作為自苯(1,2,4 )三羧酸的生産方法所得 的殘料中回收鈷及錳時的一還原劑利用,但在此情沅下, 溴化物對金靨成份的比值並不理想β同樣的,就美國專利 案4298580號案而言,其所倡言的利用氫溴酸操作,以沉 澱出以其溴化物的型態所呈現的鈷及鏟成份(毎一莫耳的 金羼至少必須配用二莫耳的氫溴酸).由於其溴化物對金 属成份的比值偏高,也不夠理想。 就本發明的理想實施方法而言,之所以可以在使用較 少量的溴化物就可以進行無礙,主要是由於有酐的介入, 本紙張尺度適用中國國家標隼{ CNS ) Α4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) — 丁 ♦-6 經濟部中央標隼局員工消費合作社印製 / N.·- .---:.. Λάά^:β/v / 415965 A7 B7 V. Description of the Invention (S) Organic acid anhydride is treated as a process to recover the cobalt or manganese present in salt-formed amidines and soluble in the former ammonium carboxylic acid. When bromide ions are present, bromide ions can be present from the beginning, or bromine ions can be introduced after the organic acid (or anhydride) begins to react. The recovered plutonium and / or manganese are preferably recycled into the area of the gasification plaque. In the case of using bromide ions, a clear and advantageous factor of the method of the present invention is that among the recovered components, the final bromide-to-metal ratio can be achieved without the help of a patent such as the US patent. In the case where the bromide concentration in the solution is trimmed or disposed of as described in Case 44 90297, it is smoothly returned to the gasification area, because the bromide ion treatment in the recovery method of the present invention In general, it can maintain a standard stoichiometric principle, and for every bromide, it can extract exactly one mole of the cobalt or manganese component β, although as in US Patent No. 4,786,621 It is pointed out that hydrobromic acid can be used as a reducing agent when recovering cobalt and manganese from the residue obtained from the production method of benzene (1,2,4) tricarboxylic acid. However, in this case, the bromide The ratio of gold tincture is not ideal. The same is true for the case of U.S. Patent No. 4298580, which advocates the use of hydrobromic acid to precipitate out the cobalt and shovel components presented in the form of its bromide ( A mole of gold Must be equipped with at least two molar hydrobromic acid). Due to its high ratio of brominated metal component, is not ideal. As far as the ideal implementation method of the present invention is concerned, the reason why it can be carried out without using a small amount of bromide is mainly due to the intervention of anhydrides. This paper size is applicable to the Chinese National Standard {CNS) A4 specification (210X297 (Mm) (Please read the notes on the back before filling out this page) — Ding ♦ -6 Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs / N. ·-. ---: .. Λάά ^: β /

經濟部中央標準局員工消費合作社印製 415965五、發明説明(1 ) 以及有鈷或錳的溴醋酸鹽的成形。本發明方法,簡而言之 ,其反應可以下列化學式代表: M2 0¾ +2A〇i 0 + 2HBp -♦ 2M(Ac)i Br + Ha 0 其中字母M可同時代表鈷以及或鍤。 但當然,實際涉及的反應逮比上式所代表者更為複雜 ,因為飛灰份係一呈高度氧化狀態下的氧化物之複雜混合 物。有少置的氫溴酸可以氣化為溴氣,該澳氣具有高度的 腐蝕性,而且足以造成環境污染公害。吾人發現,在反應 方法中添加以少麗的烴後合物之後,可將此一溴氣後合物 大量衮滅。該烴邸可作為操作中的氣化方法的前驅質;例 如躭「對釤酸的生産而言,即為對二甲笨;就異杯酸的生 産而言,則為間二甲苯」。但由於為成此一目的所箱的烴 的數量較少,幾乎只要一黏點的烴即已足夠。其他的可添 加,以抑制溴化物的氣化為溴的化合物,包括一些還原薄 ,例如蟻酸、甲醛及乙醛。 如前所述,所生成的含有鈷或錳鹽所構成的溶液特別 適合用於直接回输至氣化匾域内。在氧化方法涉及對其中 含有催化成份的母液作一局部回循處理的情況下,極可能 含有溴化物離子促進劑(主要以揮發性的有機溴化物的型 態)的損耗情形發生。在此情況下,就必須在補充催化劑 來增加溴化物離子的進料,以確保氣化反應方法中的溴化 物對催化金屬總量的比值能維持於必要的位準,所增加供 應的溴化物的數量視回循的母液的數量而定。最後回收而 得的溶液的溴化物對金颶成份的比值可輕易加以調整,以 本紙張尺度適用中國國家標準(CNS ) Α4規格{ 210Χ297公釐) (請先閱讀背面之注意事項再填寫本頁) '1、π 415965 經濟部中央標準局員工消費合作社印製 A7 B7五'發明説明(β) 促成所要達成的比值,所以,在本發明催化薄回收方法中 有使用溴化物離子的情況下,回收程序所使用的溴化物數 量之前,應先考慮到為諝整回循至氣化反應方法的母液中 的溴化物成份,所需的溴化物的幅度.此外,有待處理的 存在於殘料中的鈷/錳的數量亦臁加以考量。如此,在母 液循流内所減少的溴化物的數量,即坷藉對在催化劑回收 方法中所使用的溴化物的量作適當的決定而得到補傻。 在催化劑回收方法中所使用的有機酸或酸酐最好相同 ,或為取自舆在氧化反匾中作為芳香族酸的一溶劑使用的 酸相同的酸所衍生而得的#酐。如此則所回收而得的偁化 溶液即可直接回輸至氣化反睫方法之内。芳香族酸的氧化 ,一般而言,是在一醋酸溶剤内進行的,所以,就催化》 的回收而言,無論是使用醋酸或醑酸酐,均極為便利。 至於對於存在於殘料中的有污染性金靨成份,包括鐵 、銅、及鉻在内的成份的淸除,可以在本發明的酐/溴化 物處理完成之後,依據諸如英國專利案1413488及1319172 號案中所掲示的已知技術,加以處理清除》另外亦可遘择 ,比方説,離子交換處理以除去鐵》 HS下述的數傾實例,對本發明作進一步的酾示 ,以利了解。 實施例1 在迴流狀態下,將重0.9985克而其中含有重量百分比 分別約佔333;〜36Χ的鈷舆錳的飛灰扮,聯同25 al的醋酸 酐及33¾的溴化氫,置於由重1·5克、0_0061莫耳的HBr所 本紙張尺度適用中國國家標準(CNS ) A4規格(210X29?公釐) ~~ 一 (請先閱讀背面之注意事項再填寫本頁) 訂 經濟部中夾榡準局負工消費合作社印裂 κ 415965 Α7 _ Β7 五、發明説明(I丨) 組成的冰醋酸内攪拌及加熱持鐘兩小時β此一混合物冷卻 後,再以5G ml的蒸皤水稀釋,以便將多餘的酐分解》如 此所生成的溶液作一遇濾處理,並添加蒸餾水至U以 使之呈現一粉紅色的溶液。將此一溶液作一原子發射光辑 儀分析襄理後,發現該溶液中含有0.23X的錳以及0.236% 的鈷、總量為O.C08莫耳的金!«,绝計所萃取而得有1.2 莫耳的金》成份外,加原先所添加的1莫耳的溴化物離子 »元素溴的總量經以X光的螢光分析的結果為0.384X,所 以該溶液中的溴化物對金屬成份的比值為β.82。此一结果 顯示溴化物的生成量損失了 0.10 4克&殘料重0.291 7克。 實施例2 在遛流狀態下,將重1.0002克而其中含有重量百分比 約分別約佔333Ϊ〜363;鈷與錳的飛灰份,聯同25 Bl的醋酸 酐及33¾的溴化氫,置於由重2.5克,0.0102 Μ耳的HBr所 組成的冰醋酸内攪拌及加熱持缠兩小時。此一混合物先冷 卻,再以50 Bl的蒸脯水稀釋,以便將過剩的酐分解。如 此所取得的溶液作一過濾處理,並添加蒸皤水至100 Bi, 以使之呈現一粉紅色的溶液β此一溶液以原子發射作一分 析後,顯示其中含有〇·283ϋί的錳及Q. 2983!的鈷,金靥成份 的總莫耳值為0.0102,其所顯示缌計為抽萃出1莫耳的金 靥外加原先所添加入的1臭耳的溴化物元素溴總量以X 光的螢光分析結果為0.597%,所以溶液中溴化物對金靨成 份的比值為1.03。所生成的溴化物其損失量為0,219克。 殘料重0.1113克。 本紙張尺度適用中S國家裸^ ( CNS ) A4規格(210X297公釐) 一Ί七 (請先閱讀背面之注意事項再填寫本頁) 訂 415965 A7 B7 五、發明説明(丨>) 實施例3 在迴流狀態下,將重25克而其中含有重量比例分別約 佔33X〜36X的鈷與鏟的飛灰份,職同2 50 b1的醏酸酐舆33¾ 的溴化氣,置於由重75克、0.3056莫耳的HBr所組成冰醋 酸内後拌 及加熱持鑲兩小時。一開始加熱随即同時有溴 氣釋出。此一混合物先冷卻,然後再以100 »1的蒸腺水稀 釋,以便將過剩的酐分解。如此生成的溶液作一過濾處理 ,验添加蒸皤水至5QQ ml,以使之呈現一粉红色的溶液。 以原子發射所作的分析顯示該溶液中含有1.49¾的錳及1.53X 的鈷,金靨總量為0.26 5契耳,亦卽緦計有0.87莫耳的金 屬與1莫耳的原先所添加的溴離子一併萃取〇溴结量以X 光的螢光分析結果為4.6% (總共0.288莫耳 >,所以最後 得到的溴化物對金属成份的比值為1.52β澳分析顯示損耗 量為796。殘料重1.1克,其中16.56%是鈷、16.33%是鏟 β所以,在溶液内所回收的姑及錳,其回收率均在97.5% 以上。 實施钶4 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事項再填寫本頁) 將重10克而其中含有重量百分比分別約佔3355〜36Χ的 鈷及錳的飛灰份,勝同90 al的醋酸酐及33Χ的溴化氳,置 於重30克、0.122莫耳的HBr所組成的冰醋酸及10 _1的對 二甲苯之内橿拌,以抑制溴的生成,然後在邇流狀態下加 熱2小時。未見有任何溴氣釋出。此一混合物先冷卻,然 後再以70 的蒸皤水稀釋,以將遇剩的酐分解β如此所 生成的溶液作一過濾處理,且将有機層分離,水層則添加 本紙依尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) 4〆 415965 經濟部中央標準局買工消費合作杜印製 A7 B7 _五、發明説明(〇 ) 以蒸皤水至500 Bl,以使之呈現一粉紅色的溶液。其有機 層以氣醴色餍分析法及質量光譜分析法同步加以分析,结 果顯示其結構大致為對二甲苯、對xylyl溴化物、甲基采 基器酸鹽及4'4-二甲基bi benzyl所組成的混合物,而且這 些成份均為對蛛酸的前驅質。粉紅色的水溶液以原子發射 法加以分析後,顯示其中含有0.604$的鏟及0.618X的鈷, 總董為0.1 0 7契耳的金匾成份,顯示總量為0.88其耳的金 靨聯同原先所添加的1其耳之溴化物離子一併萃取^ 奮施例5 將重5克而其中分別含有重量百分比約佔33ΙΪ〜363:的 鈷與鍤的飛灰份,在20G°C的溫度及自生狀態的氪氣壓力 下與40 ml的醋酸酐搜拌並加熱2小時β其後壓力上升至75 Psie在此一混合物冷卻至周阖溫度之後,即以50 b1的蒸 皤水稀釋,以便將過剩的酐分解。如此所生成的溶液作一 遇濾處理,並添加以蒸《水至200 nl,以使之呈現一褐色 的溶液《»以原子放射所作分析結果顯示該一溶液中含有0.46X 的錳與0.4 5 3!的鈷,原先進料中的金靨成份的回牧率為50Ϊ 。殘料重2. 4克。 實施例6 將依烕應藕合的爾漿/原子發射光嫌分析法(ICP/AES )所測定的重量約為1克的由39.3Χ的錳與38.U的鈷所構 成的飛灰份與適量的醋酸、水及HBr發生反,以成就如 表1中所掲示的各種水的百分比值,以及1的金鼷成份 對溴化物之比值。 本紙張尺度適用中國國家標率(CNS ) Λ4規狢(210Χ 297公釐) (請先閲讀背面之注項再填寫本頁)Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 415965 V. Invention Description (1) and the formation of bromoacetate with cobalt or manganese. In short, the method of the present invention can be represented by the following chemical formula: M2 0¾ + 2A〇i 0 + 2HBp-2M (Ac) i Br + Ha 0 wherein the letter M may represent cobalt and or thallium simultaneously. But of course, the actual reaction involved is more complicated than that represented by the above formula, because fly ash is a complex mixture of oxides in a highly oxidized state. A small amount of hydrobromic acid can be gasified to bromine gas, which is highly corrosive and sufficient to cause environmental pollution. I have found that after adding Shao Li's hydrocarbon post compound to the reaction method, this mono bromine gas post compound can be annihilated in a large amount. The hydrocarbon house can be used as a precursor for a gasification process in operation; for example, "for the production of osmic acid, it is dimethylbenzyl; for the production of isoxalic acid, it is meta-xylene". However, because the amount of hydrocarbons boxed for this purpose is small, only a sticky hydrocarbon is sufficient. Other compounds can be added to inhibit the gasification of bromide to bromine, including some reducing compounds such as formic acid, formaldehyde and acetaldehyde. As mentioned earlier, the resulting solution containing cobalt or manganese salts is particularly suitable for direct return to the gasification plaque domain. In the case where the oxidation method involves a partial recycling process of the mother liquor containing the catalytic component therein, it is highly likely that the loss of the bromide ion promoter (mainly in the form of a volatile organic bromide) will occur. In this case, it is necessary to supplement the catalyst to increase the feed of bromide ions to ensure that the ratio of bromide to the total catalytic metal in the gasification reaction method can be maintained at the necessary level. The increased supply of bromide The amount depends on the amount of mother liquor recycled. The ratio of the bromide to the gold hurricane component of the finally recovered solution can be easily adjusted, and the Chinese National Standard (CNS) A4 specification {210 × 297 mm) is applied to this paper scale (please read the precautions on the back before filling this page) ) '1, π 415965 A7 B7 printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs' invention description (β) promotes the ratio to be achieved. Therefore, in the case of using the bromide ion in the catalytic thin recovery method of the present invention, Before recovering the amount of bromide used in the process, the amount of bromide required for the bromide component in the mother liquor recycled from the gasification reaction method should be considered. In addition, the residue to be treated is in the residue. The amount of cobalt / manganese is also taken into account. In this way, the amount of bromide to be reduced in the circulation of the mother liquor, i.e., by making an appropriate decision on the amount of bromide used in the catalyst recovery method, is obtained. The organic acid or acid anhydride used in the catalyst recovery method is preferably the same, or the #anhydride derived from the same acid as the acid used as a solvent for the aromatic acid in the oxidation reaction plate. In this way, the recovered tritiated solution can be directly returned to the gasification anti-eyelash method. The oxidation of aromatic acids is generally carried out in a solution of acetic acid. Therefore, in terms of catalytic recovery, whether acetic acid or acetic anhydride is used, it is extremely convenient. As for the removal of the contaminating gold rhenium components present in the residue, including iron, copper, and chromium, after the anhydride / bromide treatment of the present invention is completed, such as according to British Patent No. 1413488 and The known technology shown in case No. 1319172 can be processed and removed. Alternatively, for example, ion-exchange treatment to remove iron. HS The following examples of tilting will be used to further illustrate the present invention for better understanding. . Example 1 In a reflux state, a fly ash weighing 0.9985 g and containing approximately 333 wt% of cobalt; ~ 36 × of cobalt and manganese, together with 25 al of acetic anhydride and 33¾ of hydrogen bromide, were placed in The paper size of HBr, which weighs 1.5 grams and 0_0061 mol, is applicable to the Chinese National Standard (CNS) A4 specification (210X29? Mm) ~~ 1 (Please read the precautions on the back before filling this page) Order in the Ministry of Economic Affairs The quasi-stationary consumer work cooperative print κ 415965 Α7 _ Β7 V. Description of the invention (I 丨) The glacial acetic acid was stirred and heated for two hours. After the mixture was cooled, the mixture was cooled with 5G ml of distilled water. Dilute in order to decompose the excess anhydride. The solution so produced is filtered once, and distilled water is added to U to make it a pink solution. This solution was analyzed by an atomic emission photometer, and it was found that the solution contained 0.23X manganese and 0.236% cobalt, and the total amount of gold was O.C08 Mor !! 1.2 Moore's Gold ", plus the addition of 1 mole of bromide ion» elemental bromine added previously, the result of X-ray fluorescence analysis is 0.384X, so the bromide in this solution is The ratio of the components is β.82. This result shows that the amount of bromide produced was lost by 0.10 4 g & the residue weight was 0.291 7 g. Example 2 In a flowing state, put 1.002 grams in weight and contained about 333 to 363 weight percents; fly ash of cobalt and manganese, together with 25 Bl of acetic anhydride and 33¾ of hydrogen bromide, It was stirred and heated in glacial acetic acid consisting of 2.5 g, 0.0102 M ear of HBr for two hours. This mixture was cooled and then diluted with 50 Bl of distilled water to decompose the excess anhydride. The solution thus obtained was subjected to a filtration treatment, and distilled water was added to 100 Bi to make it a pink solution. Β This solution was analyzed by atomic emission, and it was found to contain 0.283 ϋ manganese and Q. The total mole value of the 2983! Cobalt and gold tincture components is 0.0102, which is shown as the extraction of 1 mole of gold tincture plus the 1 bromine element bromine element added previously. The total bromine is X The result of light fluorescence analysis was 0.597%, so the ratio of bromide to gold tincture in the solution was 1.03. The amount of bromide formed was 0,219 grams. The residue weighed 0.1113 grams. This paper size is applicable to S countries naked (CNS) A4 specification (210X297 mm) Ί7 (Please read the precautions on the back before filling this page) Order 415965 A7 B7 V. Description of the invention (丨 >) Example 3 Under reflux, the brominated gas weighing 25 grams and containing the fly ash of cobalt and shovel with a weight ratio of about 33X ~ 36X, respectively, and the equivalent of 2 50 b1 of acetic anhydride and 33¾ are placed in a weight of 75 G, 0.3056 moles of HBr in glacial acetic acid, mix and heat for two hours. At the beginning of heating, bromine gas was released at the same time. This mixture is cooled and then diluted with 100 »1 of distilled gland water to decompose the excess anhydride. The resulting solution was filtered, and distilled water was added to 5QQ ml to make it a pink solution. Analysis by atomic emission shows that the solution contains 1.49¾ of manganese and 1.53X of cobalt. The total amount of gold is 0.26 5 deciles. It also includes 0.87 moles of metal and 1 mole of the original addition. Bromine ions were extracted together. The X-ray fluorescence analysis result of the bromine binding amount was 4.6% (total 0.288 moles), so the final bromide-to-metal component ratio was 1.52β. The analysis showed a loss of 796. The weight of the residual material is 1.1 grams, 16.56% of which is cobalt and 16.33% of which is shovel β. Therefore, the recovery rate of palladium manganese recovered in the solution is more than 97.5%. Implementation 钶 4 Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (Please read the precautions on the back before filling this page) It will weigh 10 grams and contain fly ash of cobalt and manganese with a weight percentage of approximately 3355 ~ 36 ×, which is better than 90 acetic anhydride and 33 × bromide. Thorium, stir in glacial acetic acid consisting of 30 g, 0.122 moles of HBr and 10 _1 para-xylene to inhibit the formation of bromine, and then heat in a flowing state for 2 hours. Nothing was seen Bromine gas is released. This mixture is cooled and then steamed with 70 Dilute it to filter the remaining anhydride solution β, so the resulting solution is filtered, and the organic layer is separated. The water layer is added to the paper according to the Chinese National Standard (CNS) A4 specification (210X297 mm) 4〆415965 Duo printed A7 B7 produced by the Central Bureau of Standards, Ministry of Economic Affairs and Consumer Cooperation _V. Description of the invention (〇) Steamed water to 500 Bl to make it a pink solution. The organic layer was analyzed by gas-colored method. And mass spectrometry were analyzed simultaneously, and the results showed that the structure was roughly a mixture of p-xylene, p-xylyl bromide, methyl aminate, and 4'4-dimethyl bi benzyl, and these components were all It is the precursor of spider acid. After the pink aqueous solution is analyzed by atomic emission method, it shows that it contains 0.604 $ of shovel and 0.618X of cobalt. The total amount of gold plaque is 0.1 0 7 deciles, showing the total amount is Extraction of 0.88 gold ears together with the bromide ions originally added 1 ear ^ Fen Example 5 will weigh 5 grams and each of them will contain about 33 IΪ ~ 363: weight fly ash Serving at 20G ° C and It was mixed with 40 ml of acetic anhydride under the pressure of thoron in the green state and heated for 2 hours. Then the pressure rose to 75 Psie. After the mixture was cooled to the ambient temperature, it was diluted with 50 b1 of distilled water to dilute it. The excess anhydride is decomposed. The resulting solution is treated with a filtration treatment and added with steamed water to 200 nl to make it a brown solution. Analysis by atomic radiation shows that the solution contains 0.46X The manganese and cobalt of 0.4 5 3 !, the reversion rate of the gold tincture component in the original material is 50Ϊ. Residue weighs 2.4 grams. Example 6 A fly ash consisting of 39.3 × of manganese and 38.U of cobalt was weighed to about 1 gram, as determined by ICP / AES. Contrast with the proper amount of acetic acid, water and HBr to achieve the percentage values of various waters as shown in Table 1, and the ratio of gold tincture component to bromide. This paper size applies to China National Standards (CNS) Λ4 Regulation (210 × 297 mm) (Please read the note on the back before filling this page)

:vy V 415965 A7 B7 五、發明説明()V/ ) 此一混合物加以搜拌並作迺流處理持續2小時,結果 整匾呈現深綠色,且生成溴氣。此一混合物搦置冷卻一宿 夜,且分別添加以5Q stl的蒸躕水。在過濾處理後,所得 的濾出物添加以蒸皤水至〗,然後再繼之以ICP/AES 分析處理,其結果數據揭不如表1。 結果數據顯示反應所生成的混合物中所存在的水成份 可減少鈷及鏟的回收最。 表1 〈請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 水份X 錳回收量% 鈷回收最χ 0 81.6 82 . 3 4,4 80 73.6 14.4 71.3 70 19.4 59 57.2 23.4 57 . 9 56.4 28.1 56.9 5 5.6 51.3 41.8 43 本紙張尺度適用中國國家榡準(CNS ) M規格(210X297公釐) A7 B7 藏 415965 i、發明説明(^r) ι實施例7 將重25克而其中含有39.3X的錳及38.35¾的鈷之飛灰 份躲同250 ml的冰醋酸及60.5 ml — 8Br占33%的醋酸加以 攪拌,以成就1: 1的金靨成份總量對溴化物的比值。可觀 察出少量的溴氣之生成。其後此混合物在迺流狀態下加熱 2小時,以生成更多的溴氣。然後將眈混合物冷郤、»置 ,再添加蒸皤水至500 Bl,並作一過濾處理。殘料在室溢 下乾操並_其淨重(1.9克)β此一濾出物添加蒸皤水至 1 0 0 0 ml,並作ICP/AES分析,溶液内的金屬成份的回收率 經計算結果得知,分别為78¾的錳及76JK的鈷。該一溶液同 時亦以X光的螢光加以分析後,得知其中含有重量比例佔 2. 03¾的溴化物。 實施例8 對從實施例7中所取得的乾燥殘料中抽取1.37 9 7克, 利用25 Bl的冰醋酸及存介於醋酸内的3.34 al的33X HBr 作進一步的萃取處理,以依據對存在於殘料内的金屬成份 的估測量為準據而成就一 1: 1的金靨成份總量對溴化物的 比值。此一混合物施以迴流處理持缠2小時,然後冷卻並 擱置一宿夜,再添加蒸餾水至50 al ^在過濾處理後,濾 出物添加蒸皤水至100 BU以ICP/AES加以分析後,可成 就一依據對殘料中的金羼成扮的估測量為準所算定的錳為 23S;,及鈷為86X的回收率^溶液内的溴化物緦量,以X光 的螢光澜定後,其重量百分比值為1.23%。此一結果顯示 取自一第一金羼成份抽萃的殘料足以循回至一第二萃取方 本紙張尺及读用t闺國家捸進 ( CNS ) Λ4規格f 210;<.29_7公犛) 一1卜 (請先閲讀背面之注意事項再填寫本頁): vy V 415965 A7 B7 V. Description of the invention () V /) This mixture was searched and mixed and treated as a stream for 2 hours. As a result, the entire plaque was dark green and bromine gas was generated. This mixture was left to cool overnight, and 5Q stl of distilled water was added separately. After the filtration process, the obtained filtrate was added with distilled water to 然后, and then followed by ICP / AES analysis and processing. The results are not as good as Table 1. The results show that the presence of water in the mixture produced by the reaction can reduce the recovery of cobalt and shovel. Table 1 (Please read the notes on the back before filling out this page) Moisture printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economy X Manganese recovery% Cobalt recovery χ 0 81.6 82. 3 4,4 80 73.6 14.4 71.3 70 19.4 59 57.2 23.4 57. 9 56.4 28.1 56.9 5 5.6 51.3 41.8 43 This paper size is applicable to China National Standard (CNS) M specification (210X297 mm) A7 B7 Tibet 415965 i. Description of the invention (^ r) Example 7 will be repeated 25 grams of fly ash containing 39.3X of manganese and 38.35¾ of cobalt are stirred with 250 ml of glacial acetic acid and 60.5 ml — 8Br of 33% acetic acid to achieve a total ratio of 1: 1. Bromide ratio. The formation of a small amount of bromine gas can be observed. The mixture was then heated under a simmer for 2 hours to generate more bromine gas. Then, the radon mixture was cooled, left to stand, and then distilled water was added to 500 Bl, and filtered. Residues were dried under room overflow and _ its net weight (1.9 g) β. This filtrate was added with distilled water to 100 ml and analyzed by ICP / AES. The recovery rate of metal components in the solution was calculated. As a result, it was found that the manganese was 78¾ and the cobalt was 76JK. This solution was also analyzed by X-ray fluorescence, and it was found that it contained bromide in an amount of 2.03¾ by weight. Example 8 Extract 1.37 97 g from the dry residue obtained in Example 7 and use 25 Bl of glacial acetic acid and 3.34 al of 33X HBr stored in acetic acid for further extraction treatment. The estimation of the metal content in the residue is based on the ratio of the total amount of bromide to bromide. This mixture was subjected to reflux treatment for 2 hours, then cooled and left overnight, and then distilled water was added to 50 al ^ After the filtration treatment, the filtrate was added with distilled water to 100 BU and analyzed by ICP / AES. It can be achieved that the manganese is calculated as 23S based on the estimation of the composition of gold in the residue, and the recovery of cobalt is 86X. The amount of bromide in the solution is determined by X-ray fluorescence. Its weight percentage value is 1.23%. This result shows that the residual material extracted from a first gold tincture ingredient is enough to be recycled to a second extraction paper ruler and read with the Chinese National Standard (CNS) Λ4 specification f 210; < .29_7 public牦) 1 1 (please read the notes on the back before filling this page)

,1T - 經濟部中央標準局員工消費合作社印製 4備is A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明(丨u) 法,以成就進一步的金屬成份回收量。 實施例9〜1 4 取備一糸列的合成〃飛灰份〃化合物,據以提供其结 對鈷的重量百分比值分別為2:1、1:1及1:2的樣品。此等 搛品傜取自一對已知金屬原料成份施以對二甲苯氣化處理 的工廠的灰渣化殘料,在550°C的高溫下攧置一宿夜後所 製得,然後再在對之施以二度灰份化處理之前,在其上添 加定量的醋酸鈷溶液,以生成所要的鈷對錳的比值,以及 利用ICP/AES,分別測定錳及鈷的重量。 取其中的每一合成飛灰渣樣品以蒸皤水冲洗,以將其 中的納成份排除掉然後乾燥。不論是已沖洗遇或未沖洗遇 的樣品均依下述方法作一萃取處理。精確地_量取約1克 的飛灰份量,並舆25 ail的插酸及存介於醑酸内容稹量約 為33%的HBr混合.以成就其值為1:1的金屬成扮總量對澳 化物的比值〇此一混合物施以2小畤的迺流處理,其後可 觀满出溴氣的生成β此混合物再冷卻一宿夜,並添加蒸钃 水至50 ·1β遇濾處理後,濾出物添加蒸讅水100 *1 ,殘 料則在室溫狀態下乾燥 溶液以ICP/AES分析其金屬成份,並以X光的螢光分 析其溴化物。其結果顯示如表2^ 表2 (請先閲讀背面之注意事項再填寫本頁), 1T-Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 4 Prepared is A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs V. Invention Description (丨 u) method to achieve further metal component recovery. Examples 9 to 1 4 A series of synthetic 〃 fly ash 备 compounds were prepared to provide samples with a weight percentage of cobalt of 2: 1, 1: 1, and 1: 2. These counterfeit products are obtained from ash residues from a plant where a pair of known metal raw materials are subjected to p-xylene gasification treatment, and are left to stand overnight at a high temperature of 550 ° C. Before subjecting it to a second degree of ashing treatment, a quantitative amount of cobalt acetate solution was added thereto to generate a desired ratio of cobalt to manganese, and the weights of manganese and cobalt were measured by ICP / AES, respectively. Take each sample of synthetic fly ash residue and rinse it with distilled water to remove the sodium content and dry it. Both the rinsed and unrinsed samples were subjected to an extraction process as described below. Accurately _ Measure about 1 gram of fly ash and mix it with 25 ail of acid insertion and HBr containing about 33% of the content of acetic acid. In order to achieve a total of 1: 1 metal, The ratio of the amount to the Australian compound. This mixture was subjected to a stream of 2 畤 迺, and then the bromine gas was generated. Β This mixture was cooled overnight, and distilled water was added to 50 · 1 β. Then, the filtrate was added with distilled water 100 * 1, and the residue was dried at room temperature to analyze its metal components by ICP / AES, and its bromide was analyzed by X-ray fluorescence. The results are shown in Table 2 ^ Table 2 (Please read the notes on the back before filling this page)

本紙張尺度適用中國國家標準(CNS ) Λ4規格(210Χ 297公釐)-iV .弋病415^65 A7 B7 五、發明説明(β) mm 序號 mm mam mm 動回棚 0®»百分比 獅回赌 0®*百分比 mmmm ί·ΜΜ百册 1 2.2:1 無 65 75 0.29 2 1.1:1 無 63 71 0.43 3 1:2.2 無 73 55 0.37 4 2.2:1 有 68 79 0.29 5 1.1:1 有 58 67 0.31 6 1:2.2 有 72 54 0.34 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印聚 實施例1 5〜1 9 取重約1克而其中的錳含遣及鈷含量經ICP/AES拥定其 值分別為39,3X及38.4X的飛灰份與25 al的冰醋酸,及存 在於醑酸之内且測定量為33X的HBr反應作用,以成就各種 不同的金靥成份對溴化物的比值。在每一不同比值®案下 ,反應劑品均施以簡單的混合,並撕置約18小時,然後再 添加蒸皤水至50 Bl。如此生成的混合物作一過濾處理, 濾出物添加以蒸脯水至l〇fl ml,然後依ICP/AES作一分析 。金颶成份對溴化物的比值及回收而得的金觸成份的最值 分別顯示如表3 β 1訂 本紙張尺度適用中國國家標準(CNS )八4说格(2ίΟΧ297公釐〉This paper scale applies Chinese National Standard (CNS) Λ4 specification (210 × 297 mm) -iV. Rickets 415 ^ 65 A7 B7 V. Description of the invention (β) mm Serial number mm mam mm Moving back booth 0® 0® * Percent mmmm ΙΜΜ 100 volumes 1 2.2: 1 no 65 75 0.29 2 1.1: 1 no 63 71 0.43 3 1: 2.2 no 73 55 0.37 4 2.2: 1 yes 68 79 0.29 5 1.1: 1 yes 58 67 0.31 6 1: 2.2 Yes 72 54 0.34 (Please read the notes on the back before filling out this page) Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Example 1 5 ~ 1 9 Take a weight of about 1g and the manganese contains Cobalt content has been determined by ICP / AES. Its fly ash content is 39, 3X and 38.4X, and 25 al of glacial acetic acid, as well as HBr reaction in osmic acid with a measured amount of 33X to achieve various Ratio of gold tincture to bromide. In each case with different ratios, the reactants were simply mixed and allowed to stand for about 18 hours before adding distilled water to 50 Bl. The resulting mixture was subjected to a filtration treatment, and the filtrate was added with distilled water to 10 fl ml, and then analyzed by ICP / AES. The ratio of the golden hurricane component to the bromide and the maximum value of the recovered gold contact component are shown in Table 3 β1. The paper size is in accordance with Chinese National Standard (CNS) 8 and 4 (2ί〇 × 297 mm)

415965 A7 s__ll 五、發明説明(e) 表3 實施 例序 號 金靨成份 總置對溴 化物的比值 錳回收量 的重量百 分比值 鈷回收量 的重ft百 分比值 15 1:1 41.7 44.1 16 2:1 28 28.7 17 4:1 16.5 18.2 18 8:1 11.4 11.7 19 1:2 53.4 54.7 (請先閱讀背面之注意事項再填寫本頁)415965 A7 s__ll V. Description of the invention (e) Table 3 Example No. of the ratio of gold tincture components to bromide weight percentage of manganese recovery weight percentage value of cobalt recovery ft percentage value 15 1: 1 41.7 44.1 16 2: 1 28 28.7 17 4: 1 16.5 18.2 18 8: 1 11.4 11.7 19 1: 2 53.4 54.7 (Please read the notes on the back before filling this page)

,1T 經濟部中央橾準局貝工消費合作社印製 以上结果顯示,利用一室溫方法邸可回收到相當高比 例的金靥成份,但若将反應劑品加熱至迺流溫度,則囫收 量可進一步的提升β又,在增加溴化物對金屬成份的比值 後,可據以增加金羼成份的回收率,但在值差棰大的金靥 成份對溴化物的比值範圍内,均可回收操作。 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐)Printed by the 1T Shellfish Consumer Cooperative of the Ministry of Economic Affairs of the Ministry of Economic Affairs, the above results show that a relatively high percentage of gold tincture can be recovered using a room temperature method, but if the reactant is heated to the flow temperature, it will be collected. The amount can further increase β. After increasing the ratio of bromide to metal, the recovery rate of gold tincture can be increased, but within the range of the ratio of gold tincture to bromide with a large value difference. Recycling operation. This paper size applies to China National Standard (CNS) Α4 specification (210 × 297 mm)

Claims (1)

第私’ ’ 7 3 3 i弟取制*讀老 申請專利範心 Λ8 ( :18 '% 08 .卜 1)8 申請專利範圍 2No. ’’ 7 3 3 I ’m making * reading the old application for patent Fan Xin Λ8 (: 18 '% 08. Bu 1) 8 patent application scope 2 .種自其中含有氧化钴及/.或氧錄的成份之灰份中回收 姑及/或錳的方法,其步驟包栝:以一有機酸,或有機酸 酐,或前述二者的混合物,在有溴化物介入的情況下(溴 化物的量為:就每一莫耳的鈷或錳而言,係在〇 . 5至2 莫耳之間),與灰份相接觸,在該反應混合物中,含有重 量百分比3 0%以下的水,其溫度為介於周圍溫度至逆流 溫度之間,從而將蛄及錳的成份以能溶解的鹽的形式加以 回收。 .根據申讀專利範圍第1項的方法,其中的有機酸酐是醋酸 軒,有機酸是醋酸,而溴化物是以溴化氫或溴化乙醯的形 式介入反應的。 111 - - I I--彳 — I -- (請先閱讀背面之注意事項再填寫本頁) Γ 經濟部中央#準局貝工消費合作社印策 本紙張尺度適用中國典家梯率(CNS)A4规格(210X297公瘦) 第私’ ’ 7 3 3 i弟取制*讀老 申請專利範心 Λ8 ( :18 '% 08 .卜 1)8 申請專利範圍 2A method for recovering palladium and / or manganese from ash containing cobalt oxide and / or oxygen content, the steps include: using an organic acid, or an organic anhydride, or a mixture of the foregoing, in In the presence of bromide (the amount of bromide is: between 0.5 and 2 moles per mole of cobalt or manganese), contact with ash, in the reaction mixture It contains water below 30% by weight, and its temperature is between the ambient temperature and the countercurrent temperature, so that the components of rhenium and manganese can be recovered in the form of soluble salts. According to the method in the first patent application, the organic anhydride is acetic acid, the organic acid is acetic acid, and the bromide is involved in the reaction in the form of hydrogen bromide or acetamidine bromide. 111--I I-- 彳 — I-(Please read the notes on the back before filling in this page) Γ The Ministry of Economic Affairs Central # Associate BureauBei Gong Consumer Cooperative Co., Ltd. Printing policy This paper standard applies to Chinese Coder Slope (CNS) A4 specifications (210X297 public thin) No. '7 3 3 I made * read the old application patent Fan Xin Λ8 (: 18'% 08. Bu 1) 8 patent application scope 2 .種自其中含有氧化钴及/.或氧錄的成份之灰份中回收 姑及/或錳的方法,其步驟包栝:以一有機酸,或有機酸 酐,或前述二者的混合物,在有溴化物介入的情況下(溴 化物的量為:就每一莫耳的鈷或錳而言,係在〇 . 5至2 莫耳之間),與灰份相接觸,在該反應混合物中,含有重 量百分比3 0%以下的水,其溫度為介於周圍溫度至逆流 溫度之間,從而將蛄及錳的成份以能溶解的鹽的形式加以 回收。 .根據申讀專利範圍第1項的方法,其中的有機酸酐是醋酸 軒,有機酸是醋酸,而溴化物是以溴化氫或溴化乙醯的形 式介入反應的。 111 - - I I--彳 — I -- (請先閱讀背面之注意事項再填寫本頁) Γ 經濟部中央#準局貝工消費合作社印策 本紙張尺度適用中國典家梯率(CNS)A4规格(210X297公瘦)A method for recovering palladium and / or manganese from ash containing cobalt oxide and / or oxygen content, the steps include: using an organic acid, or an organic anhydride, or a mixture of the foregoing, in In the presence of bromide (the amount of bromide is: between 0.5 and 2 moles per mole of cobalt or manganese), contact with ash, in the reaction mixture It contains water below 30% by weight, and its temperature is between the ambient temperature and the countercurrent temperature, so that the components of rhenium and manganese can be recovered in the form of soluble salts. According to the method in the first patent application, the organic anhydride is acetic acid, the organic acid is acetic acid, and the bromide is involved in the reaction in the form of hydrogen bromide or acetamidine bromide. 111--I I-- 彳 — I-(Please read the notes on the back before filling in this page) Γ The Ministry of Economic Affairs Central # Associate BureauBei Gong Consumer Cooperative Co., Ltd. Printing policy This paper standard applies to Chinese Coder Slope (CNS) A4 specifications (210X297 male thin)
TW86117333A 1996-11-18 1997-11-18 A process for the recovery of cobalt and/or manganese from ash containing cobalt and/or manganese as oxides thereof TW415965B (en)

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GBGB9623897.7A GB9623897D0 (en) 1996-11-18 1996-11-18 Production of aromatic carboxylic acids
GBGB9625033.7A GB9625033D0 (en) 1996-12-02 1996-12-02 Production of aromatic carboxylic acids

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