TW384553B - Process for recovering organic hydroxides from waste solutions - Google Patents

Process for recovering organic hydroxides from waste solutions Download PDF

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Publication number
TW384553B
TW384553B TW87101828A TW87101828A TW384553B TW 384553 B TW384553 B TW 384553B TW 87101828 A TW87101828 A TW 87101828A TW 87101828 A TW87101828 A TW 87101828A TW 384553 B TW384553 B TW 384553B
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Taiwan
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solution
hydroxide
selective
organic
ion
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TW87101828A
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Chinese (zh)
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Roger D Moulton
Mark W Hellums
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Sachem Inc
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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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/84Recycling of batteries or fuel cells

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  • Water Treatment By Electricity Or Magnetism (AREA)

Description

經濟部中央標準局®C工消费合作社印製 A7 B7 五、發明説明(\) 坊街镅爐 本發明係有闞一種由廢棄溶液中,回收有機氫氣化物的 方法。,特而言之本發明係有W —種回收有機氬氧化物的 方法·包括霄化電池和鹽沈灘步驟•,金臑淸除步》或包括 > 4 大小堪擇性分隔物或大小«揮腰的步《之一 »明的昔醫 四级銨氫氧化物例如駕氣化四甲銨(TMAH)和籯氧化四 乙銨(TEAH)為強有機_,,此巳經知道許多年;> 已發現該四 级铵氫氧化物之各種用途,,包括當做有機溶謂中的酸之滴 定劑#當做極譜法中支»«解霣之用途丨四级銨fi氧化物 的水溶液丨特別是TMAH溶液:已廣泛當做印刷電路板和微 霣子晶片製造的光阻嬲之顯影劑。,為了各種原因·,希望最 小化使用於印刷電路板和微《子晶片製埴中的願彩鬭之全 部曇。t最小化全部量之氫氣化物顯影劑的一個方法為再使 用廢顯影劑/ 然而,廢顬影劑包含該等包括鐮子雒質和非霪子雜質 。離子雄質包括隈離子例如納丨鉀\鋅和鈣及除離子例 如鹵化物、硝酸鹽.、碳酸腹.、羧酸鹽、硫酸鹽〜非離子雄 % · · 質包括光阻劑 '界面活性劑、,胺類和大量其他有機分子, r 廢顯影fl!亦包含較低濃度之氫氣化顯影劑η因此.,仍鼸鱭 需要於可使用之方式有效回收fi氣化物顯影_以使其可再 使用•,藉此最小化使用於印刷《路板和》«子晶片製造中 的顧影劑之全都量〆 本紙張尺度適用中國國家標率(CNS ) A4规格(2丨Ο X 297公釐)Printed by the Central Standards Bureau of the Ministry of Economic Affairs® C Industrial Consumer Cooperative A7 B7 V. Description of the Invention (\) Fangjie Oven This invention is a method for recovering organic hydrogen compounds from waste solutions. In particular, the present invention is a W-type method for recovering organic argon oxides. Including the step of the battery and the salt sinking beach. The step of removing the gold sacrifice "or including > 4 size optional partitions or sizes. «Waist-in-steps" one of the famous medical quaternary ammonium hydroxides such as Tetramethylammonium (TMAH) and Tetraethylammonium Oxide (TEAH) are strong organic compounds. ; ≫ Various uses of the quaternary ammonium hydroxide have been discovered, including as a titrant of the acid in organic solvents # as a branch in polarography »« Solution of quaternary ammonium 丨 aqueous solution of quaternary ammonium fi oxide丨 TMAH solution in particular: It has been widely used as a photoresist developer for printed circuit boards and micro wafers. For various reasons, I hope to minimize all of the color chips used in printed circuit boards and microchips. One method of minimizing the total amount of hydride developer is to reuse the waste developer / however, the waste developer contains these including falconium and non-dipper impurities. Ion androgenic substances include gadolinium ions such as sodium, potassium, zinc, and calcium, and deionizing agents such as halides, nitrates, carbonates, carboxylates, sulfates, and non-ionic males. Agents, amines, and a large number of other organic molecules, r waste development fl! Also contains a lower concentration of hydrogenated developer η. Therefore, it is still necessary to effectively recover the fi gas development in a usable manner so that it can be used. Reuse • to minimize the amount of filming agents used in the printing of "road boards and" «sub-chip manufacturing. This paper size is applicable to China National Standard (CNS) A4 specification (2 丨 〇 X 297 mm) )

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丨棘. C 經濟部中央標準局貝工消费合作社印製 A7 ΒΊ_五、發明説明(> ) 美圈専利第4,714,53 0» (Hale及其研究同仁)掲述一 種製備高婢度四级按籮氧化物之《解方法:其係利用一種 包含由隔離子交換膜分開的陰極«解液間釅,和»極液間Μ 之霣池f該方法包括將四级铵氫氧化物的水溶液進料到鵰 極液間隔;將水加至陰極霣解液闋隔中,·和將直流電通邊 霣解電池,Μ在陰欏電解液間隔中產生贜後回收之較离纯度 的四级按氫氧化物。>該’530専利也描述一種改良 '其包括 在將蠹氣化物進料到霣解霣池的釅極液間隔之前於高溫加 热四级铵氫氧化物。 美圃専利第4,9 38,854 (Sharifian及其研究同仁)亦掲 述一種藉由降低潛在化物含量來纯化四級铵氩氧化物之 霣解方法。,霣解霣池藉由可為陰離子或隱離子選擇性膜的 分隔物匾分為隈極液間限,和陰極霣解液間隔t除極霣解液 間鵰中的陰極包括鋅丨鎘、v錫、,鉛,、鋦或钛.、或其合金、、 隶或录齊? 日本公開専利第60—13198 5虢(1985)(1&以1^810及其 研究同仁)掲述一種在由跚難子交換臢@分為»極室和路 極室的電解霣池中製造一種高肫度之四鈒銨氬氧化物的方 法。.將包含雑貢之四级铵氳氧化物溶液進料到隈極室和在 水被進料到陰槿室之後在二個霣極之間供靡直流霣?從播 槿室獾得纯化之四級铵氬氧化物?該純化之四级技氫氧化 物包含減少量之_金颺· _ 土金羼,,陰_子等等。 * ' « »职的癧诚 110 窝本ί 裝. 訂 線- 本纸張尺度適用中國國家橾準(CNS ) Α4規格(210X297公釐) 經濟部中央標準局貝工消费合作社印製 A7 B7 五、發明説明(、) 在一具艚實施例中·,本發明係有醑一種從包含有機氫 氧化物和雜質之«索溶液中回收有機氫氧化物的方法/包 括: 完成(Ala-Alb),(A2)和(A3)之一, (Ala)從廢索溶液中沈澱有機氬氧化物作為不溶鹽丨及 (Alb)從廢索溶液中除去不溶鹽且將該鹽放置在一液驩中 以形成第二溶液^ (A2)或. (A2al)將廢棄溶液進料至包括至少二届間隔、、一陰極.、一 隈極和大小選擇性分隔物之第一霣化電池中,*且將 霣流通過第一霣化霣池·.藉此雜質遷移通過大小選 擇性分隔物 (A2a2)從第一電化電池中回收包含有檐離子的第二溶液 或 (A2bl)從廢棄溶液中形成包含鎗鹽和雜霣之第一溶液 (A2b2)在懕力下將第一溶液與大小選擇性膜接觸,·其中至 少一部分的雜霣通過大小選揮性膜,,箱此提供包含 鎢鹽和減少數量的雜質之第二溶液,; (A3)將廢棄溶液與金羼繡子淸除藺接觸以除去金靥雕子雜 質,,其中步《(A3)在步《(B)和(C)在之前或之後完成 9 (B)將得自(Alb)之第二溶液 '得自(A2a2)或(A2b2)之第 二溶液或得自(A3)之廢棄溶液進料至包含至少二僱間 本紙張尺度逋用中國國家標準(CNS ) A4規格(21 OX 297公釐) (請先閱讀背面之注$項再填寫本頁) oi 裝· 訂 丨—線 A7 B7 _ 五、發明説明(w ) 隔·*一陰極 '一隔槿和分隔物之第一電化霣池中且將 霣流通遇第一電化電池鞴此再生有櫬氫氣化物,;和 (C)從第一電池回收有檐氫氧化物,。 在另一具《實施例中\本發明係有鼷一種從包含有機 氫氧化物和雑霣之廢索溶液中回收有機氳氣化物的方法,· 包括下列步驟:、從廢棄溶液中沈轘有機氫氧化物作為不溶 SR 從廢索溶液中除去該鹽且將該鹽放置在一液臞中Μ形 成第二溶液,;將第二溶液進料至包含至少二個間隔#•一》 極:一跚極和分隔物之電化電池中和將霣流通邊m池,,藉 此再生有機氫氧化物/和從電池中回收有機氬氧化物。 在另一具《實胨例中,本發明係有Μ—種從包含鎗氩 氣化物#和雜質之廢棄溶液中,回收鏽氫氧化物的方法/包括 下列步驟、:將無懺邇或無櫬酸加至廢索溶液中而沈灘水不 溶性鳍鼸,;從睡棄溶液中除去該麴鹽且將該鎗蘧放置在一 液«中以形成第二溶液將第二溶液進料至包含至少三個 間隔•,一陰極•.一陲極和二溷分隔物之m化霣池中和將霣 流通通霣池、•鞴此再生鎗氫氣化物.;和從霣池中回收鎗氩 氣化物.。 仍在另一具«實施例中,,本發明係有Μ—種從包含四 鈒氫氧化物和雑質之廢粢溶液中回收四级氳氧化物的方法 ,包括下列步驟丨從18索溶液中沈澱四,级氫氧化物作為水 不溶性鼸彳將得自廢索溶液中之四级鼸加至一液《中鶼此 形成第二溶液i將第二溶液進料至包含至少二個間隔.,一 本紙張尺度適用中固國家樣準(CNS ) A4规格(210X297公釐) (請先聞讀背面之注$項再填寫本買) oi 裝_ 訂 ,線 經濟部中央標隼局貝工消费合作社印製 經濟部中央標準局貝工消費合作社印裝 A7 _B7_ 五、發明说明(s) 陰極·、一》極和分隔物之霣化霣池中和將霣流通過霣池., 鞴此在鬣池中再生四級氫氧化物和從電池中回收四级氫 氧化物 在另一具钃實雎例中•.本發明係有鬭一種從包含有機 氬氧化物和雜質之被污染溶液中回收有機氩氧化物的方法. ,包括下列步骤.:將被污染溶液進料至包含至少二價間隔 •一陰極:一》槿和大小β揮性分«物之第一電化霣池中 和將霣潦通遇第一電池:鞴此蟾質遷移通《大小理揮性分 隔物;,從第一電化《池中回收包含有機雛子之第二溶液和 將第二溶液進料至包含至少二價闔隔·一陰極* 一》槿和 * « 分隔物之第二電化電池中和將霣滾通逋第二電化《池/藉 此纯化有櫬氬氧化物;和從第二電化霣池中回收有機氬氧 化物。· 在另一具體實施例中 > 本發明係有醑一種從含銥氩氣 化物和雜質之被污染溶液中回收鎗氢氧化物的方法包括 下列步嫌:t將被污染溶液進料至包含至少二镅藺隔,* 一険 極隈極和大小選擇性》離子遵擇臢之第一«化電池中 和將霣流通過第一霣池:_此金屬離子雜霣S移通通大小 理揮性隈離子選揮性膜;,從第一霣化m池中回收包含鎢雛 子之第二溶液和將第二溶液進料至包含至少二個間隔t,一 陰檯•一鵰檯和分隔物之第二«化《池中和將«流通《第 « 二霄化霣池,藉此純化錶氫氧化物;和從第二霣化霣池中 回收鎗氫氧化物。 % 本紙張尺度適用中國國家標準(CNS ) A4规格(2丨0X297公釐) (請先閱讀背面之注f項再填寫本頁) oi 裝· 經濟部中央標準局貝工消费合作社印装 A7 B7__ 五、發明説明(t ) 仍在另一具«實施例中,本發明係有闞一種從包含鍮 氲氧化物和雜質之被汚染溶液中回收鳍氩氣化物的方电/ 包括下列步骤:包含從被污染癢液形成鎗鹽和蟾霣之第一 溶液;.在屋力下接觸第一溶液與大小《揮性膜•其中至少丨 thorn. C Printed by the Central Bureau of Standards, Ministry of Economic Affairs, Shellfish Consumer Cooperative, printed A7 ΒΊ_5. Description of the invention (>) Beautiful Circle No. 4,714,53 0 »(Hale and his research colleagues) describe a method of preparing high-quality According to the "solution method" of tritium oxide: it uses a cathode containing a cathode separated by a separator exchange membrane «solution solution 酽,» and »electrode solution M 霣 pond f. This method involves the quaternary ammonium hydroxide Aqueous solution is fed to the electrolyte solution compartment; water is added to the catholyte solution compartment, and the DC power is used to decompose the battery, and the fourth stage of the relatively pure purity is recovered after generation of tritium in the electrolyte compartment. Press hydroxide. > The '530' also describes an improvement 'which comprises heating the quaternary ammonium hydroxide at a high temperature before feeding the radon gas to the radon polar interval of the tritium bath. Meipu No. 4,9 38,854 (Sharifian and colleagues in his research) also described a method for purifying quaternary ammonium argon oxide by reducing the content of potential compounds. The decomposing bath is divided into the 隈 electrode liquid interval by a separator plaque which can be an anion or hidden ion selective membrane, and the cathode 霣 solution interval t is divided by the cathode 锌 液 cadmium, v tin ,, lead, ytterbium or titanium., Or its alloys, li or recorded? Japanese Public Lecture No. 60-13198 5 (1985) (1 & 1 ^ 810 and its research colleagues) describes a method of manufacturing in an electrolytic cell that is exchanged by a stupid child @ divided into »a pole chamber and a pole chamber A method for high-intensity tetraammonium argon oxide. . Feed the quaternary ammonium phosphonium oxide solution containing tribute to the dysprosium chamber and supply DC dysprosium between the two dysprosiums after the water is fed into the hibiscus chamber? Obtained purified quaternary ammonium argon oxide from the hibiscus chamber? The purified fourth-grade technical hydroxide contains a reduced amount of _Jin Yang · _ Tujin, yin_zi and so on. * '«» Economy 110 Woben Binding. Binding-This paper size is applicable to China National Standards (CNS) Α4 size (210X297 mm). Printed by A7 B7, Cooper Cooperative of Central Bureau of Standards, Ministry of Economic Affairs. Explanation of the invention (,) In one example, the present invention is a method for recovering organic hydroxide from a solution containing organic hydroxide and impurities / including: Complete (Ala-Alb) One of (A2) and (A3), (Ala) precipitates organic argon oxide from the waste cable solution as an insoluble salt, and (Alb) removes the insoluble salt from the waste cable solution and places the salt in a liquid solvent To form a second solution ^ (A2) or (A2al) feed the waste solution into a first tritiated cell including at least two intervals, a cathode, a pole, and a size-selective separator, * and The flow is passed through the first chemical cell. By this, impurities are migrated through the size-selective separator (A2a2) to recover the second solution containing eaves ions from the first electrochemical cell or (A2bl) to form The first solution of gun salt and miscellaneous solution (A2b2) Membrane contact, · At least a part of the impurities are selected by a size-selective membrane, and a second solution containing a tungsten salt and a reduced amount of impurities is provided; (A3) The waste solution is brought into contact with the gold embroidery 淸In order to remove the impurities of the golden eagle, where steps "(A3) in steps" (B) and (C) are completed before or after 9 (B) the second solution obtained from (Alb) is obtained from (A2a2) Or the second solution of (A2b2) or the waste solution obtained from (A3) is fed to a paper size containing at least two papers, using Chinese National Standard (CNS) A4 specifications (21 OX 297 mm) (please read the back first) Please fill in this page for the $ item) oi Assembling and ordering 丨 —Line A7 B7 _ V. Description of the invention (w) Separate * * a cathode '-Separate the first electrochemical cell in the hibiscus and the separator, and pass it through. The first electrochemical cell is then regenerated with tritium hydroxide, and (C) the eaves hydroxide is recovered from the first cell. In another example, the present invention is a method for recovering organic radon gas from a waste cord solution containing organic hydroxide and radon, which includes the following steps: The hydroxide is used as an insoluble SR to remove the salt from the waste solution and place the salt in a liquid solution to form a second solution; the second solution is fed to a solution containing at least two intervals Neutralization of the electrochemical cell with the separator and separator will pass tritium to the side cell, thereby regenerating the organic hydroxide / and recovering the organic argon oxide from the cell. In another example, the present invention is a method of recovering rust hydroxide from a waste solution containing gun argon gas # and impurities / including the following steps: Osmic acid was added to the waste cable solution while the beach water-insoluble fin cricket was removed; the osmium salt was removed from the sleeping solution and the gun was placed in a liquid «to form a second solution. At least three intervals •, a cathode • a methane cell with a single electrode and two plutonium separators and a plutonium circulation tank, a regenerative gun hydrogenate; and a gun argon gas recovery from the plutonium tank Compound ... In still another embodiment, the present invention relates to a method for recovering quaternary tritium oxide from a waste solution containing tetrahydroxide hydroxide and tritium, including the following steps. In the precipitation of four, grade hydroxide as water-insoluble 鼸 彳 will be obtained from the waste cable solution of the quaternary 鼸 added to a liquid "in this way to form a second solution i feed the second solution to contain at least two intervals. , A paper size applies to the China Solid State Standard (CNS) A4 specification (210X297 mm) (please read the note on the back before filling in this purchase) Printed by the Consumer Cooperatives. Printed by the Central Standards Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives. A7 _B7_ V. Description of the Invention (s) Cathode ·,》, and the separator and the decontamination of the pond and the flow through the pond., Here Regeneration of quaternary hydroxides in hyenas and recovery of quaternary hydroxides from batteries. In another example, the present invention relates to a method for recovering from a contaminated solution containing organic argon oxide and impurities. Method for recovering organic argon oxide, including the following steps: will be polluted The solution is fed to the first electrochemical cell containing at least two valence intervals. One cathode: one hibiscus and size β volatile matter. The first battery will meet the first battery: the toad will migrate through Volatile separators; from the first electrochemical "recovering a second solution containing organic chicks and feeding the second solution to a solution containing at least a bivalent barrier · a cathode * a" hibiscus and * «the second separator Neutralization of the electrochemical cell will pass through the second electrochemical cell, thereby purifying the argon oxide; and recovering the organic argon oxide from the second electrochemical cell. · In another embodiment > The present invention is a method for recovering gun hydroxide from a contaminated solution containing iridium argon gas and impurities including the following steps: t feed the contaminated solution to a At least two separators, * one pole, one pole, and one size-selective ion, "the first ion-selective ionizer" that neutralizes the battery and passes the current through the first cell: _ This metal ion is mixed through the large and small electrodes. Selective ion-selective membranes; recover the second solution containing tungsten chicks from the first tritium m pool and feed the second solution to at least two intervals t, a negative stage, a carved stage and a separator The second «Chemical Pond and Circulation» No. «Second Dimensional Chemical Plutonium Pond to purify the surface hydroxide; and the gun hydroxide was recovered from the second Chemical Plutonium Pond. % This paper size is in accordance with Chinese National Standard (CNS) A4 specification (2 丨 0X297mm) (Please read the note f on the back before filling out this page) V. Description of the invention (t) In still another embodiment, the present invention is a method for recovering fin argon gas from a contaminated solution containing thorium oxide and impurities / including the following steps: The first solution of gun salt and toadstool is formed from the contaminated itch solution; the first solution is contacted with the size "volatile film of which at least under room force"

一部分的雑質通通大小«揮性•《此提供一種包含鏽H 和減少數量之雑質的第二溶液.;將第二溶液進料至包含至 少二個間膈.,一樓極,,一颶極和分隔物之電化霣池中和將 霣潦通遘霣池•.藉此姹化鎢氲氧化物;和從電池中回收錶 * 氫氣化物丨 在一具臞實腌例中:本發明係有醐一種從包含有檐氲 氧化物和雜質之廢索溶液中回收有檐氫氧化物的方法/包 括下列步驟:、接觴《棄溶液與金屬雛子淸除_以除金屬離 子雑質;、將廢索溶液進科至包含至少二個間隔,,一除榧4· 一限極和分隔物之霣化霣池中和將霣滾通通霣池.,藹此再 生有檐fi氧化物I及從霣池中回收有«氫氧化物.。 在另一具«實施例中,本發明係有鬭一種從包含鎗氫 氧化物和包括金靨離子雜質的雑質之廢棄溶液中回收鎗氬 氣化物的方法:包括下列步驟接觸廢棄溶液與環醚化合 物,,鞴此減少在廢棄溶液中之金屬雛子_霣之量.;將廢棄 洁液進料至包含至少二個間隔一除極:Γ跚極和«雛子 選擇性膜之電化電池中和將電流通邊霣池·.鶊此鎢離子通 1A颶鐮子遘揮性膜及再生鎗氫氧化物;.及從電池中回收鑲 氫氣化物。, -10- 本紙張尺度適用中國國家標準(CNS > A4规格(210X297公釐] (請先閱讀背面之注$項再填寫本頁) 裝· 訂 經濟部中央樣準局貝工消费合作社印製 A7 B7 五、發明说明(q ) 仍在另一具體實豳例中.·本發明係有》—種從包含有 檐氫氧化物和雜質之廢索溶液中回收有供氫氣化物的方法 ·,包括下列步《丨賻廢索》液雄料至包含至少二個Μ 一陰極,t 一陽極和分闲物之霣化霣池中和將霣潦通嬝電池 ,箱此有機雛子通過分隔物和再生有嫌氫氧化物.;及從電 池中回收有機氬氣化物。 仍在另一具體實施例中*本發明係有醑一種從包含嫌 fi氧化物和包括金羼艫子雜霣的雑質之廢棄溶液中回收鎗 氫氧化物的方法包括下列步驟,:括下列步驟丨將廢棄溶 液進科至包含至少二僩間隔、一陰槿,.一隔極和分隔物之 霣化電池中和將霣滾通通霣池〃鞴此鎗離子通遇分隈物和 再生鎗氢氧化物;及從霣池中回收鳍fi氧化物接觸銥氫 氧化物溶液與環醚化合物K除去金颺鐮子雜霣.;及回收雄 氩氧化物〇 本發明方法的结果 > 可獲得再生之有機氫氧化物的再 生溶液\其中濃度和姹度蝤加丨再生有機氳氣化物的廢棄 溶液不但提供節省费用•而且提供因除去合成新氫氧化物 « 化合物溶液和伴生之昂資純化方法和減少8索溶液排出物 的毒性之需要的環境利益t。在有機氫氧化物從溶液中除去 之後可回收增加量之水s此外不禰要齡存大悬化學品,。經 由本發明獾得之較离濃度和純度之有機氫氧化物溶液可有 效地使用在很多其中霄要氤氡化物溶液之應用中,。 忒的鏞Mt跄明 (請先閱讀背面之注f項再填寫本頁) d 裝· ,線 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 經濟部中央橾準局貞工消费合作社印製 A7 __B7__ 五、發明説明(8 ) _1為一種根據本發明之包含一個單位«池之二間隔 電化電池的《Ε要園示,; _2為根據本發明的三間釅霣化電池的紙要示。 _3為一種包含二個軍位於單極姐戆之_2竃池的單 位霣池之堆叠的霣化霣池之«要示/ _4為一種根據本發明的四1«隔電化鬌池的《要圏示 0 5為一種根據本發明的另/一四閜隔霣化電池的《Κ要 圖示。 _6為一種根據本發明之包含二β_5的單位m池之 霣化電池的概要匾示。 拳 7為一種包含二個軍位於雙極姐戆之麵2的單位m 池之堆叠的電化電池之概要鼷示/ 鼷8為一種包含二個於雙極姐態之單位霣池的堆曼之 «化《池之«要示。, _9為根據本發明的另/一三問限電化霣池之《要鼷示 〇 画10為一種根據本發明包含二腰單位鼇池的霣化霣池 之«要示。. _11為一種包含二傾於雙極組皤之覃位霣池的堆叠之 電化霄池之概要圓示.。 _1 2為一種根據本發明的另一四閜膈霣化霣池之概要 鼸示。. -12- 本紙张尺度適用中鬮國家梯準(CNS > A4规格(2丨OXW7公釐i ' ' (請先閱讀背面之注$項再填寫本頁) oi 裝. 訂 A7 B7_ 五、發明説明(1 ) 有檐氫氧化物通常可Μ下式為特徽 A (OH)x ( I ) 其中A為有櫬或無機基團和x為等於A之價的整數;>在一 個具《«施例中》有櫬氢氧化物應該可充份地溶解在溶液A part of the maggots has a large size «Effectiveness» This provides a second solution containing rust H and a reduced amount of arsenic .; The second solution is fed to contain at least two interlayers. Hurricanes and separators in the galvanic cell and through the cell • This way tungsten tungsten thorium oxide is recovered; and the table is recovered from the battery * Hydrogenation 丨 In a solid salting example: the present invention The invention relates to a method for recovering eaves hydroxide from a waste solution containing eaves oxide and impurities / including the following steps :, followed by "removal of waste solution and metal chicks to remove metal ion species; 1. Dispose the waste cable solution to a tank containing at least two compartments, one to remove the four poles, one to the poles and the separator, and the rolls to pass through the pools, and then regenerate the eaves fi oxide I And «hydroxide ... In another embodiment, the present invention relates to a method for recovering gun argon gas from a waste solution containing gun hydroxide and thoron containing gold ion impurities. The method includes the following steps: contacting the waste solution and the ring Ether compounds, so as to reduce the amount of metal __ in the waste solution; feed the waste cleaning solution to an electrochemical cell containing at least two intervals and a depolarizer: Γ and neutralization of the electrochemical cell Pass the current through the pond. This tungsten ion is passed through the 1A hurricane sickle, the volatile film and the regenerating gun hydroxide; and the hydrogen hydride is recovered from the battery. -10- This paper size applies to Chinese national standards (CNS > A4 size (210X297 mm) (please read the note on the back before filling in this page) Preparation of A7 B7 V. Description of the invention (q) is still in another specific example. The present invention has "a method for recovering the hydrogenated supply from a waste cord solution containing eaves hydroxide and impurities." Including the following steps "丨 Waste Waste" liquid material to contain at least two M-a cathode, t-anode and the rest of the waste cell and pass the battery, the box of this organic chick through the separator And regenerating susceptible hydroxides; and recovering organic argon gas from batteries. Still in another specific embodiment * The present invention has a 从The method for recovering gun hydroxide in a high-quality waste solution includes the following steps: Including the following steps: 1. Disposing the waste solution into a tritium battery containing at least two spacers, a hibiscus, a separator, and a separator to neutralize Roll the plutonium through the plutonium. This gun ion will encounter the particles and Regenerate gun hydroxide; and recover fin-fi oxide from the limulus pond to contact the iridium hydroxide solution and cyclic ether compound K to remove gold yang sickle impurities; and recover male argon oxide. Result of the method of the present invention > Regeneration solution of regenerated organic hydroxide can be obtained, where the concentration and concentration are increased. The waste solution of regenerated organic rhenium gas not only provides cost savings, but also provides a solution for removing new synthetic hydroxide «compound solution and associated capital Purification method and environmental benefits required to reduce the toxicity of the effluent of the 8-line solution. After the organic hydroxide is removed from the solution, an increased amount of water can be recovered. In addition, there is no need to store large suspended chemicals. Via the present invention The organic hydroxide solution obtained at a relatively low concentration and purity can be effectively used in many applications in which the compound solution is important. (Please read the note f on the back before filling out this Page) d. · The size of the paper is applicable to the Chinese National Standard (CNS) A4 (210X297 mm). Printed by the Zhengong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 __B7__ V. Description of the invention (8 ) _1 is a kind of "E to garden display" containing one unit «Chi No. 2 interval electrochemical battery according to the present invention; _2 is a paper to display three battery cells according to the present invention. _3 is a type containing two army single cells戆 ister _2 of the unit of the unit of the unit of the unit of the unit of the unit of the unit «To show / _4 is a four 1« electrically isolated unit according to the present invention "To show 0 5 is another The “K” of a four-cell battery is illustrated. _6 is a schematic plaque of a unit battery containing two β_5 units according to the present invention. Boxing 7 is a bipolar sister cell containing two troops. The outline of the electrochemical cell stacked in the unit m pool of the face 2 / 鼷 8 is a kind of «Transformation of the Pool» to show the two units in the bipolar sister unit 霣 池. _9 is the "remark" of the other / one-three-three-dimensional electric-restricted electrochemical cell according to the present invention. Draw 10 is the «remark" of the present invention that includes a two-waisted unit Ao pond. _11 is a schematic illustration of a stacked electrochemical pool that includes a two-pronged tanning pool in a bipolar system. _1 2 is a schematic illustration of another tetramerization pond according to the present invention. -12- The standard of this paper is applicable to the standard of China and China (CNS > A4 specification (2 丨 OXW7mm i '' (please read the note on the back before filling in this page)). Order A7 B7_ V. Description of the invention (1) The eaves hydroxide can usually be represented by the special emblem A (OH) x (I) where A is a fluorene or an inorganic group and x is an integer equal to the valence of A; > "In the Examples" Rhenium hydroxide should be fully soluble in solution

I 中例如水,,酵或有機液鱷,.或其混合物Μ允許一有效的回 收率。 在另一具級實施例中 '本«明方法係使用於製備«純 化之有機有櫬氳氧化物例如四级按氩氣化物,·四级鱗氳氧 化物和三级銃氫氧化物?逭些有機氫氣化物可統稱為錶類 氫氣化物?在此和其他具體實施例中·. Α在上述式(I )為 雄化合物,,和式(I )表示一種鎢氫氣化物,》 四级銨和四鈒鏞氩氧化物可以下式為特徽 _ R2 +For example, water, yeast, or organic liquid crocodile, or a mixture thereof M allows an effective recovery. In another embodiment, the present method is used to prepare «purified organic rhenium oxides such as quaternary argon oxide, quaternary phosphonium oxide and tertiary hydrazone hydroxide? Can these organic hydrides be collectively referred to as surface hydrides? In this and other specific examples, A is the androgen compound in the above formula (I), and formula (I) represents a tungsten hydride, and quaternary ammonium and tetrafluorene argon oxide can be represented by the following formula _ R2 +

II

RrA-R3 OH* 川)RrA-R3 OH * Sichuan)

I R4 _ 其中A為氮或《原子,,R t ,,R2 ,* R3和Rt分別為包含1 到約20個碳原子之烷基,.包含從2到約20«磺原子之羥烷 基或烷氣烷基•.芳基基圏·,粳芳基基團:成IU和112與A 可一起形成一雑«基·.但其條件為如果雑·基包含C = A基 \ -13- _-Vi- .'· :.. 本纸張尺度適用中國國家標準(CNS ) A4界传(^^x297公釐) . V. (請先«讀背面之注$項再填寫本頁) oi裝· 訂 經濟部中央揲準局貝工消费合作社印製 l· A7 B7 五、發明説明(丨G ) 、則R3為第二鍵,。 可為直 雎例包 辛基、, 異十三 可為翔 各種輿 分別為 之羥烷 、.丁氣 例包括 更多的 方法再 _或支鰱· 翥 括甲基、.乙 異辛基、壬 基、.十六基 烷基基團例 構物等等。 泰 包含一到十 基基團.。烷 甲基、丁氧 苯基丨苄基 羥基基圃取 生或纯化的 和包含1到20個 基、,丙基Ϊ 丁基 基,、癸基.、異癸 和十八基基匾/ 如羥乙基和羥丙 在一較佳具鼸實 個碾原子之烷基 氧烷基基圈之特 丁基等.。各種芳 >,和同等物基圃 代.。 四级技氬氧化物I R4 _ where A is nitrogen or "atom, Rt ,, R2, * R3 and Rt are alkyl groups containing 1 to about 20 carbon atoms, respectively. Hydroxyalkyl groups containing 2 to about 20« sulfonic atoms Or alkane alkyl. Aryl 圏 ·, japonica aryl groups: IU and 112 and A can form a 雑 «group together with A, but only if the 雑 · group contains C = A group \ -13 -_-Vi-. '·: .. This paper size applies to Chinese National Standard (CNS) A4 Circle (^^ x297mm). V. (Please read the note on the back before filling in this page)装 Ordering and printing printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 5. Description of the invention (丨 G), then R3 is the second key. Examples include straight octyl, iso-titanium, and other different types, such as hydroxyalkane. Butane examples include more methods, or branching, including methyl, ethyl isooctyl, Nonyl, .hexadecyl alkyl groups and the like. Thai contains one to ten radicals. Alkylmethyl, butoxyphenyl, benzylhydroxyl group is derived or purified and contains 1 to 20 groups, propyl, butyl, decyl., Isodecyl and octadecyl plaque / such as Hydroxyethyl and hydroxypropane are preferably t-butyl and the like having an alkyloxyalkyl radical with a solid atom. Various Fang >, and equivalent base generation. Four-stage argon oxide

該等烷基Ri至IU 礦原子的烷基之特殊實 、戊基\己基,、庚基\ *、十二基、十三基、 R i 9 Rz ,R3 和 R4 也 基\羥丁基、羥戊基的 雎例中,.R 1 - IU基圏 和包含二到三儸碳原子 殊資胞例包括乙氣乙基 基和羥芳基基圈的實施 *其中苯環已被一儷或 * 該等可根據本發明 可K式III表示 r2The special alkyl groups of the alkyl Ri to the IU ore atom, pentyl \ hexyl, heptyl \ *, dodecyl, tridecyl, R i 9 Rz, R3 and R4 are also methyl \ hydroxybutyl, In the case of hydroxypentyl, .R 1-IU radicals and special cells containing two to three carbon atoms include implementations of ethyl ethyl and hydroxyaryl rings * where the benzene ring has been * These can be represented by K in formula III according to the present invention.

RrN-R3 OH- (III) 經濟部中央搮準局哭工消費合作社印製 R4 其中Ri - R4如式II中所定義。在較佳具鼸實施例中.,Ri 礁 -R4為包含1到約4個磺原子之烷基和包含2或3價破原子之 羥烷基基團?最常根據本轚明方法鲔化的四鈒銨氰氧化物 5 本紙張尺度適用中國國家標準(CNS > A4規格(2ί〇χ297公4 A7 B7 五、發明説明( \\ 將為氫氧化四甲銨(TMAH)或 氫氧化物之特殊實雎例包括 、氤氣化四丙铵.、氫氣化四 化三甲基羥乙按,、氫氧化三 二羥基乙铵,、氰氧化甲基三 氫氧化苯基三乙»,、氬氧化 教f、氧氧化二甲基吡咯錠、 • m 化二異丙基味唑啉鎗、氳氣 式II的四级鱗氫氧化物 其可根據本發明的方法纯化 化四乙供、.氩氧化四丙網、. 羥乙».、氬氧化二甲基二羥 氰氧化苯基三甲钂、氫氧化 鑄等等。 氫氧化四乙 氩氧化四甲 丁》、.籯氧 甲基甲氧乙 羥乙按丨氫 苄基三甲» 氫氧化二甲 化N-烷基吡 代表的實施 ),.包括氫 霣氧化四丁 乙鱗、氫氧 苯基三乙雄 « (TEAH) .〇 銨.、氩«化 化四正辛按 銨,·駑氧化 氧化苯基三 .、氩氧化苄 基六氫吡錠 腚等等。 例,其中A 4 氧化四甲鑄 期丨氫氧化 化三甲基羥 和氫氣化苄 其他該 四乙銨 .、氫氧 二甲基 甲銨.、 基三乙 、瓤氣 =P ( ,、氫氧 三甲基 乙鱗、 基三甲 (請先閏讀背面之注$項再填寫本頁)RrN-R3 OH- (III) Printed by Crying Consumer Cooperatives, Central Bureau of Standards, Ministry of Economic Affairs R4 where Ri-R4 are as defined in Formula II. In a preferred embodiment, Ri reef -R4 is an alkyl group containing 1 to about 4 sulfonic atoms and a hydroxyalkyl group containing 2 or 3 valence broken atoms? Tetraammonium cyanide oxide most commonly converted in accordance with the method of the present invention 5 This paper is in accordance with Chinese national standards (CNS > A4 specification (2ί〇χ297 公 4 A7 B7) V. Description of the invention (\\ Specific examples of methylammonium (TMAH) or hydroxide include, trifluoroammonium gasification, trimethylhydroxyethyl tetrahydrogenation, tridihydroxyethylammonium hydroxide, Phenyltriethyl hydroxide, argon oxidation, f, dimethylpyrrole oxyoxidation, m-diisopropyl oxazoline gun, tritium quaternary scale hydroxide of type II which can be used according to the present invention The method is to purify tetraethyl ether, argon oxidation of tetrapropane, hydroxyethyl », argon oxidation of dimethyl dicyanocyanide to oxidize phenyltrimethylammonium hydroxide, cast hydrogen hydroxide, etc. 、 Hydroxymethylmethoxyethoxyethyl according to 丨 Hydroxybenzyltrimethyl »represented by N-alkylpyridine dimethyl hydroxide), including hydrogen peroxide oxidation of tetrabutyl ethyl scale, hydroxyphenyltriethyl and« (TEAH) .Ammonium, argon hydratium tetra-n-octylammonium, hydrazine oxidized phenyl trioxide, argon oxidized benzyl hexahydropyridine, etc. For example, where A 4 is oxidized during the casting phase of tetramethyl chloride, trimethylhydroxyl hydroxide and benzyl hydrogen are other tetraethylammonium hydroxide, dimethyldimethylammonium hydroxide, trimethylethyl, tritium gas = P (,, Trimethyl ethyl hydroxide scale, trimethyl methoxide (Please read the note on the back before filling in this page)

OI -裝. 訂 在另一具Μ實施例中丨該等可根據本發明之方法純化 之三鈒銃氩氧化物可以下式表示. R2 1OI- 装. Order In another M embodiment 丨 these arsenic argon oxides can be purified according to the method of the present invention can be expressed by the following formula.

RrS* OH* (IV)RrS * OH * (IV)

I r3 其中Ri :R2和Rs分別為包含1到約20價碳原子之烷基 -15- 本紙張尺度適用中國國家標準(CNS ) A4规格(21(^X297公 線 經濟部中央標準局負工消費合作社印製I r3 where Ri: R2 and Rs are alkyl groups containing 1 to about 20 valent carbon atoms, respectively.-This paper size applies to China National Standard (CNS) A4 specifications (21 (^ X297 Central Bureau of Standards of the Ministry of Economics and Work Printed by Consumer Cooperatives

A7 B7 經濟部中央揉準局貝工消费合作社印氧 五、發明説明( ) 9 包 含 2到約 20 個 碳 原 子 之 羥 烷 基 成 烷 氧 基 烷 基 % 芳 基基 圈 或 羥基芳 基 基 團 \ 或 Ri 和R2 與 S可 一 起 形 成 雄 瓖基 $ 但 其 條件為 如 果 m 環 圈 H 包 含 C: S基 則Rs 為 第 二 鍵.。 Μ 式IV表 示 之 级 銪 氫 氣 化 物 的 實 施 例 包 括 氫 氣 化三 甲 鐮 氫氧化 三 乙 * 氫 氧 化 三 丙 等 等 0 » 該 等在根 據 本 發 明 方 法 中 典 化 或 再 生 之 腰 棄 m 液 (B 染 溶 液 )為混合物 較佳為溶液 m ,包含可氧化液艚和约0.01 % 到 約 50里董 % 之 有 櫬 氫 氧 化 物 和 通 常 將 包 含 改 變 量 之一 種 或 上不想 要 的 雜 霣 > 例 如 陰 離 子 如 鹵 化 物 \ 碳 酸 鹽,、 甲 黢 鼸 、.亞硝 酸 鹽 % « 硝 m 鹽 〇 疏 酸 81 等 等 一 些 隈 離 子例 如 包 括 鋅和鈣 • 納 N \ 鉀 之 金 翳 和 一 些 中 性 物 種 • * 例 如 光阻 鑲 • 甲 酵λ胺 等 等 〇 可 氣 化 液 Η 可 為 水 水 和 — 種 有 镶溶 劑 例 如 _等等 之 混 合 物 .〇 在 一《具 體 實 m 例 中 « 本 發 明 的 方 法 有 效 地 減 少 存在 於 有 櫬 氫氧化 物 例 如 四 级 妓 氲 氧 化 物 之 溶 液 中 的 饑 子 和非 離 子 雜 霣 在 進 一 步 具 黼 實 m 例 中 • 本 發 明 的 方 法 產 生減 少 有 機 氫氧化 物 例 如 四 級 銨 氫 氣 化 物 的 溶 液 中 的 金 颺離子 雑 質 Μ 及有機雑 質 的 结 果 〇 有 機氫氧 化 物 是 商 業 上 可 利 用 的 〇 此 外 t • 有 機 氫 氧化 物 可 從 相當的 有 櫬 m 例 如 有 相 當 之 有 機 鹵隹 物 .* 碳 酸 鼸., 甲 酸 鹽 \硫酸 H 等 等 製 備 0 各 種 的 製 備 方 法 描 述 於 在 美a 専 利 第 4,911 ,781 號 (Sha r i f i an及 其 研 究 同 仁 )和第5 ,286 ,354 號 (Bard及其研究間仁) 螫 因 此 其 合 併 於 此 處 以 供 參考 18- 訂 本紙張尺度適用中國國家標準(CNS > A4规格(210X297公釐)A7 B7 Printed oxygen by the Central Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, 5. Description of the invention () 9 Contains 2 to about 20 carbon atoms of hydroxyalkyl to alkoxyalkyl %% aryl ring or hydroxyaryl group \ Or Ri and R2 and S can form an androyl group $ only if the m ring H contains a C: S group and Rs is the second bond. Examples of grade VIII hydrides represented by Formula IV include hydrogenated trimethylsalmonium triethyl hydroxide * tripropyl hydroxide, etc. 0 »These are m-liquids that are normalized or regenerated in the method according to the present invention (B dye (Solution) is a mixture, preferably solution m, containing oxidizable liquid rhenium and about 0.01% to about 50% by weight of phosphonium hydroxide and usually will contain varying amounts of one or more unwanted impurities, such as anions such as Halides, carbonates, formazan, nitrite% «nitrate salt 〇 thio acid 81 and so on some ions such as zinc and calcium • Na N \ potassium gold 翳 and some neutral species • * For example Photoresistance • Formazan λ amine, etc. 〇 Gasifiable liquid Η Can be a mixture of water and water-a type of solvent such as _ and so on. 〇 In a specific example «The method of the present invention effectively reduces Quaternary hydroxide The solution and the non-ionic impurities in the solution are further described in the following examples: • The method of the present invention generates a gold ion ions M and organic ions in a solution that reduces organic hydroxides such as quaternary ammonium hydride. The result is that organic hydroxides are commercially available. In addition, t • Organic hydroxides can be equivalent from 榇 m. For example, there are equivalent organic halides. * 鼸 鼸., Formate \ sulfuric acid H, etc. Preparation 0 Various preparation methods are described in U.S.A. No. 4,911,781 (Sha rifi an and his colleague) and No. 5,286,354 (Bard and his research colleague) 螫 therefore incorporated here for Reference 18- The paper size of the edition applies to the Chinese national standard (CNS > A4 size (210X297 mm)

經濟部中央揉準局貝工消费合作社印氧 A7 B7_ 五、發明説明(Λ ) 。對於如何獲得或製備有機氫氣化物並沒有特別的限制4。 在根據本發明的方法中.·有機《氣化物例如該等上述 者在一種包括三種可採用的步骤之至少一種的方法中從廢 索溶液中纯化或再製,。雖然在大部份之例子中值實拖三種 « » 可採用的步驟之一 *.但多於一饀之三種變化步»可被實施, 。三個可採用的步«之第一個包括沈澱步朦<?三個可採用 的步驟的第二個包括利用大小缠揮分隔物或大小《揮性膜4 〇三個可採用的步驊的第三儸包括接觸廢棄溶液與金羼雛 子清除劑,。 在被使用於一方法中之後,廢棄溶液可為一種有檐氫 » 氧化物的溶液,.尤其在與印刷霣路板和微«子晶片製造有 鼷之顯影方法中$由於通程的结果.,雜質進入而且污染溶 液換句铦說、廢棄溶液可為有櫬氫氣化物的廢溶液?除 有嫌氫氧化物外丨廢棄溶液可包含上述任何一種_質及/ 或相當於有檐氫氧化物的有檐鼸及/或其他微粒子.。 在完成三個可採用的步«之至少一儒之前%包含有櫬 氫氧化物和雜霣之廢棄溶液可選揮性被濃繕、。亦即,·廢索 溶液中的有機氫氣化物的濃度可在三個可採用的步驟之前 先蝤加、。在大部份具《實施例中較佳為在實雎本發明之 前濃嫌廢棄溶液、。濃級步《在箱熟該技鷗者為已知且包括 蒸發•離子交換·霣滲析•,和逆滲透 * % 三《可採用的步》的第一《包括沈霣步驟、。步《包括 沈濺廢秦溶液中有襯氬氧化物作為不溶解鼸t•和較佳水不 -17- (請先閱讀背面之注^I-項再填寫本頁)The Central Government Bureau of the Ministry of Economic Affairs, Printed Oxygen A7, B7_, Shellfish Consumer Cooperatives V. Description of Invention (Λ). There are no particular restrictions on how to obtain or prepare organic hydrides4. In the method according to the present invention, an organic gaseous substance such as the above is purified or reconstituted from a waste solution in a method including at least one of three applicable steps. Although in most cases it is actually one of three «» steps that can be taken *. But more than one of the three change steps »can be implemented,. The first three steps include the precipitation step. The second one of the three steps includes the use of large and small spacers or the size of the film. Three available steps: The third puppet includes contact with the waste solution and the golden pupae scavenger. After being used in a method, the waste solution can be a solution of eaves hydrogen »oxides, especially in the development method with printed circuit boards and micro« sub-wafer manufacturing »due to the results of the pass. Impurities enter and contaminate the solution. In other words, can the waste solution be a waste solution with tritium hydroxide? In addition to suspected hydroxides, the waste solution may contain any of the above-mentioned substances and / or eaves and / or other particles equivalent to eaves hydroxide. Before completing at least one of the three available steps, at least one of the waste solutions containing tritium hydroxide and tritium is optionally concentrated. That is, the concentration of the organic hydride in the waste solution can be increased before the three applicable steps. In most of the examples, it is preferable to concentrate the waste solution before implementing the present invention. Concentrated step "The person who knows this technique in the box is known and includes evaporation, ion exchange, tritium dialysis, and reverse osmosis. *% The first step of the" available steps "includes the immersion step. Step "Includes argon oxide lining as insoluble in splattered waste Qin solution as insoluble 鼸 t • and better water -17- (Please read the note ^ I- on the back before filling this page)

OI •裝. 訂 :線 本紙張尺度適用中國國家揉準(CNS ) A4规格(210X297公釐) A7 B7_ 五、發明説明() 溶性鼸Λ術語不溶解鹽表示在溶液中完全地成部份地不溶 解的《彳術語水不溶性《表示在水中完全地或部份地不溶 解的鼸。.雖然其較佳形成實質上不溶解及/戒水不溶解性 的Μ,.但是其它不一定需要。.需要的是Μ至少部份是不溶OI • Binding. Binding: The size of the paper is suitable for the Chinese National Standard (CNS) A4 (210X297 mm) A7 B7_ 5. Description of the invention The term "water-insoluble", which is insoluble, means that the water is completely or partially insoluble in water. Although it is preferred to form M that is substantially insoluble and / or water-insoluble, others are not necessarily required. What is needed is that M is at least partially insoluble

I t 解的(及/或水不溶性的)。.不溶解鹽的溶解度較佳視溫度 而改變.。因此,.其較佳為減少或降低顢棄溶液的潘度同時 沈澱不溶解鹽,。 將蘧或酸加入至駸棄溶液中藉此產生沈濂之不溶解膻 . ♦ 。至少部份之不溶解鼸由包含有機«離子得自有嫌氫氧 化物)和陰雕子·(得自加入之醴或酸)的化合物所構成.。不 溶解鹽可包含其他化合物.。加入之»或酸較佳為無嫌鼸或 無檐酸。.產生沈澱的不溶解鹽的鼸之實例包括銨.•納.,鉀 和其他金羼過氯酸ML;銨.,納 >.鉀和其他金層六氟鋁酸鑒 ;铵/納,鉀和其他金靨六氟娣酸Μ。铵•納,鉀和其他 • · ♦ # 經濟部中央揉準局負工消费合作社印装 (婧先閲讀背面之注$項再填寫本頁) 金屬六氟砷酸盟.;铵,.納,.鉀和其他金屬六氟磷酸鼸.;銨 、納,·鉀和其他金麵六氟矽酸鹽;.铵,.納:鉀和其他金雇 六氟钛酸鹽.;銨.,納.·鉀和其他金屬六氟睡酸馥.;铵.,納 ,鉀和其他金羼磺化物和磺酸Μ 銨:纳•、鉀和其他金靨 逢»酸鹽:>铵·,納.·鉀和其他金臑過瞄酸鼸銨,.納鲆 和其他金羼溴化物.;技•.納,•鉀和其他金羼苷味酸鼸,;技 •納鉀和其他金羼进錳酸鹽等等°產生沈澱的不溶解鹽 之酸的實例包括過氮酸,.IS碘酸••包括四氟礪酸之氟晒|酸 ,·六氟磷酸k,氫溴酸< 苷味酸·.壜艋酸和任何—般相當於 -18 - 本紙張尺度逍用^^國^橾準(CNS M4规格1210X297公釐) ' A7 B7 Λ、發明説明(β) 上列鹽的酸,。 該等沈澱之不溶解臁包括由有櫬»離子和任何一個上 列相當的陰離子所構成的鹽S特殊實例包括有檐過氯酸 ,有櫬_化物鹽、,有櫬氟鹽(包含氟原子之陰雛子),·例如 上列任何一《六氟化合物:有嫌溴» :有循墮酸鹽.·有機 通艋酸黷•、或任何一僑栢當於上列陰雕子的鼸,。被加至廢 索溶液中之鹽或酸係根據包括有機氳氣化物特定定義.,所 得不溶解臞和任何金羼離子轅質的鹽之相對溶解度的許多 因素而理擇·。 一旦不溶解鹽已沈載.,其可藉由任何箱熟該技藝之人 士習知的任何方法單離;包括但是不限制於傾淅;遘籌/ 和離心法。、然後經覃離的不溶解鹽可遘揮地洗滌且放置在 一届液臁中•、藉此形成一新溶液丨液髖可能是水成以水為 基質*,例如:水和一種有«溶莆例如酵或乙二_等等之混 合物。、因為不溶解鹽只需要至少些微地溶解在新溶液中,· 所以不溶解粒子可存在於新溶液中?然後將新溶液進料到 電化«池中、。 經濟部中央梯準局貝工消费合作社印製 (請先閲讀背面之注$項再填寫本頁) 在將新溶液進料到霣化電池之前·•溶液的瀣度可蝤加 薄此«加在其中之不溶鹽的溶解度》。對於不溶鹽.,完全溶 解在新溶液是不需要的而是改為僅至少@微地溶解,。Μ 於埴一點ν溶解度埔加覿也可被加至新溶液中Μ增加不溶 解鼸的表觀溶解度。,在一個具鱺實雎例中、•如果溶液為水 的L加入很少量的_·*例如甲酵或乙酵可壜加不溶鼸之 -19- 本紙張尺度適用中國國家揉準(CNS ) Α4^格(2丨0X297公釐) 經濟部中央標準局貝工消费合作社印製 A7 B7 五、發明説明() 溶解度。、或者及/或額外地/新溶液可被加热,•攪動成放 置在K力下K便蝤加不溶解臞之溶解度、。 三僩可採用的步朦的第二個包括利用大小應揮性分_ 物或大小遘擇性臏。、廢索溶液,*它可巳經避揮地被壤鎺之 後,,與大小選擇性分隔物,•例如大小選擇性«難子選擇性 膜*、或大小選擇性膜,•例如奈米過籌膜接觸、。大小«擇分 瞞物或膜允許某些鐮子通逢:%包括大小、,分子量.,和逢 料之大小和類型之許多因索而定》 一般而言,v在逭個具黼實施例中廢索溶液在被進料至 霣化«池內之前先進行二個步驟中的一俪,。第一《步»包 括將廢索溶液進料至包含分隔物.•和較佳大小選揮性曝離 子選揮性膜之第一電化《池内·;和第二步《包括形成有機 鹽•例如鎗鹽•,接著接觸有機鼸溶液與大小選擇性膜例如 奈米逢濾膜《雖然兩儡步驟可在廢棄溶液進科至霣化霣池 之前實施,·但是其較佳為僅實施二«步骤的其中一僩,。 在一個具體實雎例中.•在接觸興廢棄溶液與大小選揮 性分隔物或膜之前\ «理廢棄溶液Μ形成包含一種得自β 棄溶液中的有機》饑子的有櫬《(之溶液?較佳·*在廢索溶 液與大小選揮性臢例如奈米過濾膜的接觸之前肜成有糴鼸 。在較佳具tt實梅例中,•有嫌》為高分子#鎗鼸》有機Μ 可為溶解於或完全地或部扮地不溶於溶液中?有機鼸的溶 解度較佳視溫度而改變%在其中醆索溶液與大小選擇性膜 ••例如奈米«濾膜接觸的具黼實施例中/新形成的有機臁 -20- 本纸張尺度適用中國國家揉準(CNS ) Α4ίΙ格(2丨0X297公釐) (請先閱讀背面之注$項再填寫本I ) -裝. 線 經濟部中央揉準局貝工消費合作社印製 A7 B7 五、發明説明(θ ) 較不易通嬝大小選揮性膜.,藕此燴加通過大小遍揮性膜的 轅質之相對·、 在一個具β實《Ε例中.·將鹽或酸加至廢索溶液中鶊 此形成高分子量有機β。加入之鼸或酸較佳為無循鹽或無 慊酸。形成有櫬鼸的鹽之實例包括銨,、納·,鉀和其他金臛 過氯酸鹽;、銨:納:鉀和其他金羼六氟鍚酸鼸,;銨·.納· « 鲆和其他金羼六氟綈酸臁?銨;納,.卿和其他金靨六氟砷 酸!I ;銨.,納•鉀和其他金羼六氟磷駿鼸;,銨,納鉀和 % % ’ 其他金屬六氟矽酸蠼;、銨,•納,•鉀和其他金麵六氟钛酸鹽 ;铵*納.,押和其他金鼷六氟睡酸Μ ;銨•納.,鲆和其他 金軀碘化物和碘酸鼸;銨.,納·.鉀和其他金颺邊__臞; 銨*.納·•鉀和其他金颺逢昧酸:铵.,納i鉀和其他金屬 溴化物·;铵•,納.,鉀和其他金屬氟化物和氱化物;按,納 •鉀和其他金屬苦味酸》;铵.,納.,鲆和其他金羼味酸馥 :铵〜納:鉀和其他金靥硝酸蘧銨.,納••鉀和其他金羼 通鯭酸鹽等等?形成有櫬鼸之酸的實例包括逢氮酸,氫_ 酸,、包括四氟_酸之氟顆酸,六氟磷酸,氫碕酸,硝酸, * · 9 $ * 磷酸•、亞磷酸,、多磷酸,、氫氯酸,蠤溴酸:苦味酸;過艋 酸和任何一般相當於上列《的酸,。 在另一具嫌實施例中,*有櫬Μ經由使用離子交換系統 之離子交換技術而形成。.離子交換可在管柱發生.。有機鹽 至少部份是由包含有搬暘離子(得自有嫌氬氧化物)和陰離 子(得自加入鹽成酸或得自離子交捵)之化合物所構成.。 -21- 本紙張尺度適用中國國家標準(CNS ) Α4规格(2丨0X297公釐} (請先閱讀背面之注f項再填寫本頁) -58 A7 ^__B7__ 五、發明説明(β) 有機豔不κ二氧化破的中和來形成。,在疽儸具臞實施 例中••因為該等相當之有嫌碳酸》和碳酸氫鼸複雜化通程, (請先閱讀背面之注^^項再填寫本頁) •降级大小遘擇性分《物和大小《揮性膜及/或電化爾堆 •所Μ碳酸氫鼸和破酸鼸的形成是不想要的·。 該等有檐醒包括該等由有機«饑子和任何一個上列相 當的播霱子《所構成之鱷,特殊實例包括有檐氣化物鼸.* 有櫬遇氰酸》,.有籣碘化物蘧*·有機氟鼸(包含氟原子之 陰離子)例如在上列的任何一種六氟化合饬,有機溴薩* ♦ · 有檐苷味酸鹽:有檐通鍤酸鼙,有檐硝酸Η或任何相當於 上列的馥。有櫬鹽的陰離子係根據包括有搌鵰離子之特殊 定義丨所得有機鹽和任何金羼離子雜質的鹽之相對溶解度 的許多因素而選揮,。 在另一具體實施例中•在選擇性濃鏞醆棄溶液之後和 « 在形成有嫌鹽之後《,廢棄溶液可在壓力之下與大小«揮性 縝接觸 '在一較佳具髏實施例中.•大小選擇性膜為例如奈 米遇濾膜的微通濾膜。應用的懕力通常為至少約IOOpsί, 和較佳約200到約1,000 psi:和更佳約300到約800 psi.。 經濟部中央標準局員工消費合作社印製 在另一較佳具艚資施例中·*尤其是有機釀已形成之後 •有櫬嬲的潇度調蝥至Μ使為約1厘ft%和約5重量%之 蘭的溶液。,大小遘揮性膜通常為壓力霣池辨於藥筒的形式 。廢索溶液在足夠颳力下與大小選揮性膜接觸》此金鼷離 子雜質通通大小埋擇性_。.在典型的搡作中:廢棄溶液的 一部分·.例如四分之一 •,一半#•或四分之三•,被強迫穿« -22- 本紙張尺度逍用中國囷家梯準(CNS }A4规格(210X297公釐) 經濟部中央標準扃貝工消费合作社印製 A7 ΒΊ_ 五、發明説明(θ ) 大小理擇性膜而留下不通邊大小選擇性膜的部分有櫬 部分不通通大小理揮性膜之包含有機蘧的溶液包含被 滅少的數量之金屬離子雜»及/或鎢饑子對金靨離子雜質 的比大於在大小接觴蘧揮性膜接觸之前的比.。有櫬鹽藉由 溶雕和回收技術從大小邇揮性膜獲得纟疽個包含有機臞之 溶液然後被進料到霣化霣池以純化及/或再生有機氤氧化 物。》 大小選擇性膜之實例包括得自Kinyat-Weiz«iann公 司的MPF-3 4奈米過漶_ ;得自LCI公司的Desal-5;和得自 Hydronautics的ESNA奈米遢濾膜4。其他的奈米遇濾膜為 可得自 Dow and Fil· Tec、 在另一具驩實施例中t將腰棄溶液•.其已被遘擇地濃 嫌•,進料至包含大小選揮分«物之第一電化罨池,。在埴俪 具體*胨例中丨本發明的方法包括使用二個霣化電池。在 埴個具讎實施例中;第一《化«池包含至少一«極* 一陰 極,,和一分限物a可選擇性地、第一m化霣池進一步包含 雙極性膜。在一較佳具臞實胨例中t•分隔物為陽雕子遘揮 性賸·、和更佳為大小雄揮性限離子埋擇性膜^。廢棄溶液被 進料到第一電化電池、,因此金屬離子雑質^•例如鋰•納, 和鉀,、藉由因電流通通電化霣池的结果而p邊大小适揮分 性隔物所κ離開廢液。a在本發明所有的具鱷賁施例所用的 電化霣池之有闞描述(时綸於後)可以應用在逭個具钃實雎 例的第一電化轚池,*且為了籣短的緣故不在此區段麗複f -23- 本纸張尺度適用中國國家標準(CNS ) A4规格(210 X 297公釐) HM. (請先聞讀背面之注$項再填寫本頁) •裝. 經濟部中央標準局貝工消费合作社印製 A7 B7 五、發明説明(w) 在埴個具«實雎例中的霣化霣池包含至少二僑間釅,; 即V進料一回收間隔和廢液間隔,·和選擇性水間ffi及/或 通過間隔。,在些某具鱷實腌例中/根據逭個具臞實雎例的 第一 «化m池可具有二備或在κ上之上述各間隔》。例如** 在一《具鼸實胨例中*根據逭個具黼實施例之第一霣化霣 池可具有二個進料一回收復間隔,,一傾水間隔、,和二個廢 液闢隔。溶液被進枓到各個間隔,。溶液可為水基質>•酵或 二酵為基質,、或其他有循溶液或其組合、。在較佳具鱷實施 例中,,被進料至各個間隔内的溶液為水溶液。, 被進料至進料一回收間隔內的溶液包含欲再生或純化 至某濃度之有機氫氧化物和雜霣,·例如金羼離子_質4。最 初進料至進料一回收間隔內的有櫬氳氧化物之濃度在約1 重量%到約20重量%之範國和更佳約2重量%到約重量10 重量%。在大部份實例中溶液也包含金雇離子雑質•例如 % * 鋰離子,、納離子,,鉀離子鎂離子、,和鈣離子,。 廢棄溶液間隔最初被進料溶液且較佳為水溶液丨被進 料到廢棄溶液間隔的溶液可為包含或不包含離子化合物, 在霣流通過第一電化《池之後,有機氫氧化物可從進料一 回收間隔回收。、從進料-回收間隔回收的有檐氢氧化物的 _度可相同的或高於最初被進料到進料-p收間隔的溶液 中的有機氫氧化物之開始濃度。, 一旦施加一《流•《金羼離子雑質移動穿過分隔物/和 在較佳具體實施例中移動穿過大小遘揮性隈離子雄揮性膜 _ 2 4 _ 本紙張尺度適用中國國家揉準(CNS ) A4说格(210X297公釐) (請先《讀背面之注$項再填寫本頁) .q·It is hydrolyzed (and / or water-insoluble). The solubility of insoluble salts preferably changes depending on the temperature. Therefore, it is preferred to reduce or decrease the pan of the rejection solution while precipitating insoluble salts. Add osmium or acid to the abandon solution to produce a heavy insoluble 膻. ♦. At least part of the insoluble 鼸 is composed of compounds containing organic «ions derived from quasi-hydroxide) and Yinzi · (from the added osmium or acid). The insoluble salt may contain other compounds. The added »or acid is preferably non-stigmatizing or eucalyptus. Examples of rhenium that produces precipitated insoluble salts include ammonium, sodium, potassium, and other gold perchlorate, ML; ammonium, sodium, and potassium and other gold hexafluoroaluminate; ammonium / nano, Potassium and other gold hexafluorophosphonate M. Ammonium • Na, Potassium and others • · ♦ # Printed by the Central Labor Bureau of the Ministry of Economic Affairs, Consumer Cooperatives (Jing first read the note on the back and then fill out this page) Metal Hexafluoroarsenate .; Ammonium, .Na, Potassium and other metals rhenium hexafluorophosphate; ammonium, sodium, potassium and other gold hexafluorosilicates; ammonium, sodium: potassium and other gold hexafluorotitanates; ammonium, sodium · Potassium and other metals hexafluorophosphonates; ammonium., Sodium, potassium and other gold sulfonates and sulfonic acids. Ammonium: sodium •, potassium and other gold salts »acid salts: > ammonium, sodium. · Potassium and other gold sulphate, ammonium sulphate, sodium sulphide and other gold sulphide bromide; technical • sodium, potassium and other stilbene glycosides, sodium sulphate and other gold sulphate into manganese Examples of acids that cause precipitation of insoluble salts include perazoic acid, .IS iodic acid •• Fluorine including tetrafluoroacetic acid | acid, hexafluorophosphate k, hydrobromic acid < aglycone Acid · .Acidic acid and anything—generally equivalent to -18—this paper size is free to use ^^ Country ^ 橾 standard (CNS M4 specification 1210X297 mm) 'A7 B7 Λ, the acid of the salt listed in the description of the invention (β), . The precipitated insoluble hydrazones include salts consisting of uranium ions and any of the equivalent anions listed above. Specific examples include perchloric acid, hydrazone salts, and fluorinated salts (including fluorine atoms). Yin Yinzi), · For example, any one of the above listed "Hexafluoride: Suspected of bromine": There is cyclic acid salt. · Organic hydrazone acid, or any of the cymbals of the above-mentioned Yin sculpture, . The salt or acid to be added to the waste solution is selected based on a number of factors including the specific definition of organic rhenium vapors, the relative solubility of the resulting salt that does not dissolve osmium and any gold ions, and rhenium. Once the insoluble salt has been loaded, it can be isolated by any method known to anyone skilled in the art; including, but not limited to, decantation; and / or centrifugation. , And then washed by Qin Li ’s insoluble salt and placed in a liquid bath. This will form a new solution. The liquid hip may be water-based and water-based. * For example: water and a kind of « Solvents such as mixtures of yeast or ethylene glycol. 2. Because the insoluble salt only needs to be slightly dissolved in the new solution, so can the insoluble particles be present in the new solution? The new solution is then fed into the electrochemical cell. Printed by the Central Laboratories of the Ministry of Economic Affairs, Shelley Consumer Cooperatives (please read the note on the back, and then fill out this page) Before feeding the new solution to the battery, the thickness of the solution can be thinned «加Solubility of insoluble salts in it. For insoluble salts, complete dissolution in the new solution is not required but instead only at least @ 微 地 soluble. At a point of ν solubility, pegasus can also be added to a new solution to increase the apparent solubility of insoluble plutonium. In a practical example, • If the solution is water, add a small amount of _ · * For example, formazan or acetic fermentation can add insoluble -19- This paper is applicable to Chinese national standards (CNS) ) Α4 ^ (2 丨 0X297 mm) A7 B7 printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention () Solubility. Or, and / or in addition / new solution can be heated, agitated to place K under the K force, then add the solubility of insoluble ,. The second step that can be used in the three-step method includes the use of size-dependent features or size-selective measures. , Waste cable solution, * it can be evacuated to soil, and with size-selective separators, such as size-selective «difficult sub-selective membranes *, or size-selective membranes, such as nanometer Chip contact ,. Size «Selective concealment or film allows certain sickles to meet:% includes size, molecular weight, and many sizes and types depending on the material" In general, v in a specific embodiment The medium waste cable solution is subjected to one of two steps before being fed into the tritium tank. The first "step" consists of feeding the waste cord solution to the containing separator. • and the first electrification "selective ion selective membrane of a better size" in the pond; and the second step "including the formation of organic salts. Gun salt, followed by contact with an organic tritium solution and a size-selective membrane, such as a nano-filtration membrane. "Although the two steps can be carried out before the waste solution is sent to the tritium tank, it is better to perform only two steps." One of them. In a specific example. • Before contacting the waste solution with a size-selective separator or membrane \ «Restoring the waste solution M to form an organic compound containing an organic substance from a β waste solution» (of Solution? Better. * Before contacting the waste cable solution with a size-selective filter, such as a nanofiltration membrane. In the preferred example, • You suspect "is polymer # 枪 鼸》 Organic M can be dissolved in or completely or partially insoluble in solution? The solubility of organic tritium is preferably changed depending on the temperature% in which the solution is in contact with a size-selective membrane. With the example / newly formed organic 臁 -20- This paper size is applicable to China National Standards (CNS) Α4ίΙ (2 丨 0X297 mm) (Please read the note $ on the back before filling in this I)- Equipment. Printed by A7 B7 of the Central Working Group of the Ministry of Economic Affairs, Shellfish Consumer Cooperative. 5. Description of the invention (θ) It is not easy to select the size of the volatile film. In a case with β, E. Add salt or acid to the waste solution to form Molecular weight organic β. The phosphonium or acid added is preferably non-cyclic salt or non-phosphonic acid. Examples of phosphonium-forming salts include ammonium, sodium, potassium, and other gold perchlorate; and ammonium: sodium: Potassium and other gold rhenium hexafluorophosphonates; ammonium .. Na · «鲆 and other gold rhenium hexafluorophosphonates? Ammonium; Na,. Qing and other gold hexafluoroarsenate! I; Ammonium., Na • Potassium and other gold hexafluorophosphamide;, ammonium, sodium potassium and%% 'other metals hexafluorosilicate; ammonium, • sodium, • potassium and other gold hexafluorotitanates; ammonium * sodium ., Ammonium and other gold hexafluorosuccinates M; Ammonium Na., Ammonium and other gold iodides and iodine iodate; Ammonium., Na .. Potassium and other Jin Yangbian __ 臞; Ammonium · • Potassium and other Jinyang Fengyan acids: ammonium, sodium, potassium and other metal bromides ·; ammonium •, sodium, potassium and other metal fluorides and phosphonium compounds; press, sodium • potassium and other metal picric acid 》; Ammonium., Na., Samarium and other gold saccharic acid 馥: Ammonium ~ Na: Potassium and other gold osmium ammonium nitrate., Na •• Potassium and other gold osmium sulfonate etc.? Examples of acids include Including fluoric acid including tetrafluoro acid, hexafluorophosphoric acid, hydrofluoric acid, nitric acid, * · 9 $ * phosphoric acid •, phosphorous acid, polyphosphoric acid, hydrochloric acid, phosphonium bromide: picric acid; over Perylene acid and any acid generally equivalent to those listed above. In another suspected embodiment, 榇 M is formed via ion exchange technology using an ion exchange system. Ion exchange can occur in a column. Organic Salt is made up at least in part of compounds containing transporting ions (from argon oxide) and anions (from adding salt to acid or from ion exchange). -21- This paper applies to China National Standard (CNS) Α4 Specification (2 丨 0X297 mm) (Please read the note f on the back before filling this page) -58 A7 ^ __ B7__ V. Description of the Invention (β) Neutralization of Organic Kappa Dioxide To form. In the embodiment of the anthracnose method • Because the equivalent is too carbonic acid ”and bicarbonate complicate the process, (please read the note ^^ on the back before filling this page) • Selective size reduction Divided into "materials and sizes" Volatile membranes and / or electrochemical reactors • The formation of tritium bicarbonate and tritium disulfide is unwanted. Such eaves include such crocodile composed of organic «hungry sons and any one of the above-listed sows, special examples include eaves gaseous 鼸. * 榇 榇 遇 cyanic acid", 籣 籣 籣Compound 蘧 * · Organic fluorene (anion containing fluorine atom) such as any of the hexafluoride fluorene, organic bromide * ♦ · Eucalyptus gluconate: Eucalyptus acetic acid, Eucalyptus nitrate Or any equivalent of the 馥 listed above. The anion with a phosphonium salt is selected based on a number of factors including the relative solubility of the organic salt obtained and the salt of any gold ionic impurity impurity. In another specific embodiment, after the selective concentrated depletion solution and «after the formation of salt, the waste solution can be brought into contact with the size« volatile hydrazone »under pressure in a preferred embodiment Medium. • Size-selective membranes are, for example, microfiltration membranes with nanofiltration membranes. The applied pressure is usually at least about 100 ps, and preferably about 200 to about 1,000 psi: and more preferably about 300 to about 800 psi. Printed by the Consumer Standards Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs in another preferred example of funding * * especially after organic brewing has been formed 5 wt% blue solution. The size of the volatile membrane is usually in the form of a pressure tank distinguished from the cartridge. The waste cable solution is in contact with the size selective membrane under sufficient scraping force. This gold ions ion impurity can pass through the size selective. In a typical work: a part of the waste solution .. For example, a quarter •, half # • or three quarters •, forced to wear «-22- This paper is scaled to the standards of the Chinese family (CNS } A4 size (210X297 mm) A7 printed by the Central Standard of the Ministry of Economic Affairs, Shellfish Consumer Cooperative Co., Ltd. Ⅴ. Description of the invention (θ) The size of the selective membrane and the impenetrable size are left. The organic thin film containing organic rhenium solution contains a small amount of metal ion impurities and / or tungsten ions to gold ions impurity ratio is greater than the ratio before the large volatile film contact. The osmium salt is obtained from the large and small volatile membranes by solvent engraving and recovery technology, and a solution containing organic tritium is then fed to a tritium tank to purify and / or regenerate organic tritium oxide. Examples include MPF-3 4 nanometers from Kinyat-Weiz «iann; Desal-5 from LCI; and ESNA nanometers filter 4 from Hydronautics. Other nanomembrane filters In order to be obtained from Dow and Fil · Tec, in another embodiment, the waist is abandoned. Liquid .. It has been selectively concentrated, and it is fed to the first electrochemical cell containing the selected material. In specific examples, the method of the present invention includes the use of two chemical compounds. Battery. In one embodiment, the first cell includes at least one electrode and a cathode, and optionally a separator a, and the first cell further includes a bipolar membrane. In a preferred embodiment, the t • separator is a male engraved volatile residue, and more preferably a male-sized ion-limiting ion-selective membrane. The waste solution is fed to the first electrochemical cell, Therefore, metal ion ions such as lithium, sodium, and potassium, leave the waste liquid with the p-side sized spacer κ due to the result of current flow through the galvanic cell. A In all of the present invention, The description of the electrochemical cell used in the crocodile cockroach example (after the time) can be applied to the first electrochemical cell with actual examples, and it is not included in this section for short reasons. This paper size is applicable to Chinese National Standard (CNS) A4 (210 X 297 mm) HM. (Please read the note on the back before filling in (This page) • Equipment. Printed by A7 B7, Shellfish Consumer Cooperative, Central Bureau of Standards, Ministry of Economic Affairs 5. Description of the invention (w) In the case of «Real Example», the chemical tank contains at least two overseas Chinese, ie V The feed-recovery interval and the waste liquid interval, and the selective water interval ffi and / or the pass interval. In some cases of crocodile marinated cases / according to one of the first exemplified cases Have two preparations or the above intervals on κ ". For example, ** In a" example with real examples * according to a first embodiment of the first chemical tank, there may be two feeds and a recovery multiple interval , A pour water interval, and two waste liquid barriers. The solution was poured into each interval. The solution may be a water-based > fermentation or secondary fermentation as a substrate, or other circulating solutions or a combination thereof. In the preferred alligator embodiment, the solution fed into each interval is an aqueous solution. The solution that is fed to the feed-recovery interval contains organic hydroxides and impurities that are to be regenerated or purified to a certain concentration, such as, for example, gold ions. The concentration of the hafnium oxide in the initial feed-to-feed-recovery interval ranges from about 1% to about 20% by weight, and more preferably from about 2% to about 10% by weight. In most cases, the solution also contains metal ions, such as lithium ion, lithium ion, sodium ion, potassium ion, magnesium ion, and calcium ion. The waste solution interval is initially fed with a solution, and preferably an aqueous solution. The solution fed to the waste solution interval may or may not contain ionic compounds. After the flow passes through the first electrochemical cell, the organic hydroxide may be removed from the solution. Recycling interval of material one. The degree of eaves hydroxide recovered from the feed-recovery interval may be the same or higher than the starting concentration of the organic hydroxide in the solution initially fed into the feed-p collection interval. Once applied, a “flow” of “gold ions” is moved through the separator / and in a preferred embodiment, it is moved through the size 遘 遘 隈 ions male film _ 2 4 _ This paper size applies to China CNS A4 Grid (210X297mm) (please read the "$" on the reverse side before filling out this page) .q ·

•IT i! 經濟部中央梂準局貝工消費合作社印製 A7 _B7_五、發明説明(vl ) • m入廢棄溶液間隔内。,结果;從進料一回收間隔回收的 溶液顧著地包含較少的μ金颺離子雜質。大小選揮性隠離 子«擇性膜之實例包括得自Tokuyaia Soda之CNS離子遘 揮性膜和得自Asahi玻瑱之CSV饑子邐揮性膜 可被用於根據埴個具騮實施例中的第一霣化電池之» 個具》實施例將參考式被說明纟雄然第一霣化霣池的二 個具體實施例描述於_式中、但是該等箱热該技馨者明顧 可知其他很多沒有明確地描述在_式中之具鐮實施例內者 存在於本發明的範臞《 在說明於圓1中之第一霣化電池的一钃具《實施例中 * _ 1為一種電化電池1Q的籌要示/該電化電池10包含 陽極lli陰極12和在開始於陽極11:分隔物13 (其在較佳 具》實施中為大小S揮性膜)《*其在較佳具«實施例中為 大小S擇性限離子«擇性膜之順序的單位霣池。霣化霣池 10包含二個間隔、即:進料一回收間隔14和廢液間隔15,。 在說明於圖1中之電化電池10的操作中·,將包含有機 氫氧化物和金靥離子雜霣的溶液進料到進料一回收間隔14 。將水進料到廢液間隔15。在陽極和陰極之間建立和保持 一電位以產生横過電池的霣流**因此至少一些金屬離子雑 質被吸引向陰極且通過分隔物13進入廢液彳間隔15内丨有櫬 «氧化物保留在進料一回收間隔Μ產生所需要的包含較少 ft之金屬離子雜質之(與最初進料至其中之溶液比較)氫氧 化物溶液。《從進料一回收間隔14回收包含較少最之金屬雛 -25- 本紙張尺度適用中國國家標準(CNS ) A4«L«· ( 210X297公釐) (讀先閱讀背面之注f項再填寫本頁) d -裝. -β ,線 鯉濟部中央樣準局貝工消费合作社印掣 A7 B7__ 五、發明説明(/) 子雜質之新溶液,。 霣化«池之另一具«實施例說明於園12中/其為一種 包含二悝單位霣池之霣化爾池180的撅要_示/雖然其中 可包含更多單位霣池。該霣化電池180包含陲極181 ··陰槿 182且在開始於陽*181·,第一大小«揮性腸離子«擇性膜 183,雙極性膜184;和第二大小遘揮性》離子選揮性臢185 之次序。、雙極性臢184具有其面對鷗極181之陰鐮子邐揮性 側(未顥示)和面對路極182之隔難子雄擇性供(未顯示)〆 霣化®池180包含四β閜隔,即:第一進料一回收間ΒΙΐβδ ,第一廢液間隔187.·第二逭料-回收間隔188,和第二廢 液間隔189 〇· 在說明於圈12中之霣化電池180的搡作中•將包含有 « 機氩氧化物和金屬離子雑質的溶液進料到進料一回收間隔 186和188。將水進料到駸液間隔187和189。在暘極和陰極 之間建立和保持一霣位以產生横通«池的《流.*因此至少 一些金颶離子雜質被吸引向陰極且通過第一或第二大小選 擇性隔離子選擇性膜183或185進入分別之«液間隔187或 189内。有機氫氧化物保持在進料一回收間隔中Μ產生所 两要的包含較少量之金鼷離子雜質的(與最初進料至其中 之溶液比較)氬氧化物溶液。.從進料一回昀間隔186或188 回收包含較少量之金臑鐮子_質之新有搌氫氧化物溶液。 從進料一回收間隔回收的包含較少金屬鐮子嫌質之Κ 索溶液可進料至第二電化«池所Μ有懺氫氧化物然後可被 -2 6 * 本^張尺度適用中ΐ固家標準(CNS ) Α4規格(210X297公釐) (請先閱讀背面之注f項再填寫本買) 訂• IT i! Printed by the Shellfish Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 _B7_ V. Description of Invention (vl) • Enter the interval between waste solutions. As a result, the solution recovered from the feed-recovery interval accidentally contained less µgolden ion impurities. Examples of selective membranes include the CNS ion membranes from Tokuyaia Soda and the CSV membranes from Asahi Glass. The membranes can be used in accordance with one embodiment. The first embodiment of the first battery is described with reference to the formula. Two specific embodiments of the first battery are described in the following formula. It can be seen that many other examples that are not explicitly described in the _ formula exist in the scope of the present invention, "A tool for the first battery cell described in circle 1" in the embodiment * _ 1 is An outline of an electrochemical cell 1Q / The electrochemical cell 10 includes an anode 11i cathode 12 and a starting at the anode 11: separator 13 (which is a size S volatile film in the implementation of the "better") "* It is better A unit having a sequence of «selective membrane of size S selective limit ion» in the embodiment. The tritiated tank 10 includes two intervals, namely, a feed-recovery interval 14 and a waste liquid interval 15. In the operation of the electrochemical cell 10 illustrated in Fig. 1, a solution containing an organic hydroxide and an Au ion is fed to a feed-recovery interval 14. Feed water to the waste interval 15. Establish and maintain a potential between the anode and the cathode to generate a flow across the battery ** so at least some metal ion species are attracted towards the cathode and enter the waste liquid through the separator 13 in the interval 15. There are `` oxides '' Retention at the feed-recovery interval M produces the required hydroxide solution containing less ft of metal ion impurities (compared to the solution originally fed into it). "Recycling from the feed-recycling interval 14 to the metal containing the fewest metal -25-This paper size applies to Chinese National Standard (CNS) A4« L «· (210X297 mm) (Read the f note on the back before filling (This page) d -pack. -Β, line A7 B7__ printed by the Central Bureau of Standards and Quarantine Bureau of the Ministry of Economic Affairs of the People ’s Republic of China, the fifth edition of the invention (/) a new solution of impurities. The embodiment of the «Another Pond» of the 霣 说明 is described in the garden 12 / it is a type of 霣 尔 尔 池 180 180 containing two 悝 units 霣 / / Although it may contain more units 霣 霣. The tritium battery 180 contains tritium pole 181 ... yin hibiscus 182 and starts at yang * 181 ·, the first size «volatile intestinal ion« selective film 183, bipolar film 184; and the second size 遘The order of ion selectivity 臜 185. The bipolar salamander 184 has its yin sickle facing the gull pole 181 (not shown) and the diarrhea facing the road pole 182. The male is optional (not shown). Four β 閜 compartments, namely: the first feed-recovery compartment B1ΐβδ, the first waste liquid interval 187. · the second waste liquid-recovery interval 188, and the second waste liquid interval 189. During the operation of the battery 180 • A solution containing organic argon oxide and metal ion species is fed to the feed-recovery intervals 186 and 188. Water was fed to the mash solutions at intervals 187 and 189. Establish and maintain a niche between the cathode and the cathode to create a flow across the cell. * Therefore at least some of the gold ion impurities are attracted to the cathode and pass through the first or second size selective isolator-selective membrane 183 or 185 enter the «fluid interval 187 or 189 respectively. The organic hydroxide is maintained in the feed-recovery interval M to produce the desired argon oxide solution (compared to the original feed to it) containing a smaller amount of gold sulfide ion impurities. From a feed cycle of 186 or 188, a new solution of osmium hydroxide containing a small amount of golden cymbal sickle is recovered. The κ cord solution containing less metal sickle materials recovered from the feed-recovery interval can be fed to the second electrochemical cell, and then the hydroxide can be -2 6 * This standard is applicable. Gujia Standard (CNS) Α4 specification (210X297 mm) (Please read the note f on the back before filling in this purchase) Order

J 經濟部中央樣準局負工消费合作社印笨 A7 B7五、發明説明(4) 純化及/或再生,。 三個可採用之步《的第三個包括將廢索溶液與金颺離 子潇除鵡接觸。將包含有機氩氧化物和雜質之廢棄痗液 在其鱺揮性地濃嫌之後,與金屬離子淸除劑接觸金颺離 子涛除_為一棰在四鈒銨離子存在下與金臑離子«揮地反 應或錯合之化合物。,在埴上下文中4•金羼離子包括_金羼 •錶土金颺,,通波金靨和其他金屬的雛子纟更明確地說 ,金羼艨子包括鋰k,納,、鉀:» •.绝••鈹,,鎂f钙:緦,· 鋇:钪•钛,釩,,鉻•艋.•嫌,•鈷,嫌•,鋦•鋅,•釔,雎 $ \ % * *·.·♦ •鈮•,鉬•软I.,铑,.鈀《銀》鎘•鎢,,嫌♦•銥,•鉑,金· # » 鋁•.猫,,錫,鉛•銻,鉍、•鉈和其他的鐮子。在較佳具雔 * * · · 實施例中,金層鐮子淸除劑包含環醚化合物I。在更佳具艚 ·· 實施例中,.金鼷鐮子淸除爾包含至少一個冠醚或穴狀配艚 (cryt and)。,在另一具《實施例中,,金羼離子淸除劑包含 一種含醚部分之聚合物:和更詳言之包含環醚部分或穴狀 配髏部分之聚合物? 環醚化合物之特殊例子包括冠醚例如12-冠醚- 4(1,4 ,7,10-四氧基環十二烷);,15-冠鍵-5 (1,4,7,10,13-五氧 基環十五烷);18-冠醚-6 (1,4,7, 10,13,16-六縝基環十 % 八烷;(12-冠醚-4)-2-甲酵(2-(羥甲基>Γ12-冠醚-4-).; ( + )- (18-冠醚- 6)-2,3 ,11,12-四羧酸,4’-胺笨並-15-¾ 黼 -5; 4·-胺笨並-18-冠_-6;2-(胺甲基>-15-冠醚-5;2-(胺 甲基)·18-Η_-6; 4’-胺基-5*.-硝基笨並-15-S 醚-5; 1- -27- (請先聞讀背面之注f項再填寫本頁) d 裝· 訂J Central Bureau of Standards and Quarantine, Ministry of Economic Affairs, Consumer Cooperatives, Ben Ben A7 B7 V. Description of Invention (4) Purification and / or regeneration. The third step that can be used, the third involves contacting the waste cord solution with Jin Yang's ions. After the waste liquid containing organic argon oxide and impurities is volatile, it is contacted with a metal ion scavenger to remove gold ions. This is a reaction with gold ions in the presence of tetraammonium ions « Reactive or incompatible compounds. In the context of 埴, 4 羼 gold ions include _ 羼 羼 表 surface soil Jin Yang, Tung Bo 靥 靥 and other young metal 纟 more specifically, gold 羼 艨 包括 includes lithium k, sodium, potassium: •. Absolute •• Beryllium, Magnesium f: Calcium: Barium • Barium: Titanium • Titanium, Vanadium, Chromium ··· ♦ • Niobium •, Molybdenum • Soft I., Rhodium,. Palladium “Silver” Cadmium • Tungsten, Suspect ♦ • Iridium, • Platinum, Gold · # »Aluminum • Cat, Tin, Lead • Antimony Bismuth, 铊, and other sickles. In a preferred embodiment, the gold layer sickle scavenger comprises a cyclic ether compound I. In a more preferred embodiment, the golden pheasant herb comprises at least one crown ether or cryt and. In another example, the gold ion ion scavenger contains a polymer containing an ether moiety: and more specifically a polymer containing a cyclic ether moiety or a cavity-shaped cross-linking moiety? Specific examples of cyclic ether compounds include crown ethers such as 12-crown ether-4 (1,4,7,10-tetraoxycyclododecane); 15-crown bond-5 (1,4,7,10, 13-pentaoxycyclopentadecane); 18-crown ether-6 (1,4,7, 10,13,16-hexafluorenyl ring ten% octane; (12-crown ether-4) -2- Formazan (2- (hydroxymethyl)> Γ12-crown ether-4-) .; (+)-(18-crown ether-6) -2,3, 11,12-tetracarboxylic acid, 4'-amine Benzo-15-¾ 黼 -5; 4 · -amine Benzo-18-crown_-6; 2- (Amine methyl > -15-Crown ether-5; 2- (Amine methyl) · 18- Η_-6; 4'-Amino-5 * .- Nitrobenz-15-S ether-5; 1- -27- (Please read the note f on the back before filling this page) d Binding

本紙張尺度適用中國國家標率(CNS > Α4规格(210X297公釐) ---·-»·— β 經濟部中央樣準局貝工消費合作社印製 A7 ___B7_ 五、發明説明(>♦) 吖-12-冠醚-4; 1-吖-15-S_-5; 1-吖-18-S 醚-6;苯並 t ' -’12_冠醚_4;苯並-15-冠醚-5J苯並-18-冠B-6卩雙【(苯 並-15-冠醚-5)-15-基甲基】庚二酸鼸;,4’-溴苯並-18-冠 醚-6;二笨並-18-冠醚-6;.二笨並-24-冠醚-8/ 二苯並-30-¾ 醚-10 ; ar,ar’-二-第三-丁基二苯並-18-S 醚-6; ' 4 二環己烷並-18-冠醚- 6;,二環己烷並-24-S醚-8; 4’-甲 醢基苯並-15-冠»-5; 2-(二羥甲基)-12-冠醚-4; 2-(二 羥甲基)-15-冠醚- 5;· 2-(二羥甲基)-18-冠醮-6; 4’-¾基 苯並-15-冠醚-5; 4-乙烯基苯並-18-H醚-6; 1,8-二羥基 % -二苯並-14-冠醚-4; 1,11-二醇-20-H醚-6;聚【(二苯並 -18-B醚-6〉-共甲醛】,•及2-甲基-2-十二烷基丙二酸雙[ * 12-冠醚- 4)-2-甲基]酗、;製備環醚化合物的各種式子和方 法之實例被描述在美國專利第5,393,892號中,(:”1[〇1^&1[ t 等人,,其之摞的因此合併在此處Μ供參考<1穴狀S鱷包括 在環结構中額外地包含氮原子的環醚化合物•例如2.2.2- cryptate和 2^2.1-cryptate〇 在一個具«賞施例中,該等金鼷離子淸除劑可沒有進 % 一步製備而被使用。>在另一具«實施例中·,該等金羼離子 澝除劑被合併至聚合物中所K聚合物包含環醚部分,且特 « 別是冠醚部分:特殊實例為甲醛和二苯並f 18-冠醚-6的一 俚聚合物產物。在另一具體實施例中*該等金羼鐮子濟除 « * 劑成包含金屬離子清除劑之聚合物被附接至撐»上。撐體 % 可為聚合物珠,膜•,含矽嗣之化合物.,或a接到依次被連 « -28- 本紙張尺度速用中國國家標準(CNS ) A4规格(210X297公釐) (請先閱讀背面之注$項再填寫本頁) d -裝· 訂 -線 經濟部中央梯準局負工消费合作社印製 A7 _B7_ 五、發明説明(/) 接到金羼離子淸除9S的矽詷化合物或其聚合物·t砂4,矽凝 腰,,玻璃·》玻璃纖維,,氧化鋁.·氣化辣,·氣化檢,或氧化 肽· *或其他的包含金鼷離子濟除劑之介質。 % 廢棄溶液Μ多種不同的方式與金属鐮子淸除劑接觸· 通常視金靨離子濟除劑的狀態而定,。例如1,廢棄溶液可與 容器中的金羼離子淸除劑合併·,廢棄溶液可通邊其中包含 在撐嫌上的金羼難子清除爾的管柱••廢棄溶液可通遘包含 金屬鐮子淸除劑等等之介質:廢棄溶液輿金羼離子淸除_ 接觸之方法沒有特別的限制,。在較佳具鱷實施例中I•當金 羼雕子淸除繭被附到聚合物珠上時/聚合物珠本身包含在 管柱中,、然後廢棄溶液通遴管柱〜在其中金羼雕子清除莆 被附到是存在於容器中的聚合物珠上之具霾實施例中4,廢 棄溶液被加入,且容器可遘擇地振盪或其它的攪動》♦接著 分開聚合物珠和溶液? 在較佳具體實施例中·_在涉及電化霣池之步«前進行 廢棄溶液與金羼離子清除劑的接觴是簠要的。,结果/實》 量的金靥離子沒被引入《化轚池內。、因為在一些具«實施 例中,,廢棄溶液中的實質量之金屬離子可減少涉及電化電 池之步驟的效力:所Μ逭很重要,。Μ於逭广點,實的 金羼黻子可能汚染被回收的有機氫氧化物,。在另一具《實 施例中,廢溶液被進料到電化霣池•和從電化《池中回收 之溶液後來與金羼離子清除麵接觸*在逭第三個可採用的 -29- ϋ張尺度適用中國國家標準(CNS ) Α4規格(210X297公釐) (請先閲讀背面之注$項再填寫本頁) 4. 訂This paper size applies to China's national standard (CNS > A4 specification (210X297mm) --- ·-»· — β Printed by the Shell Sample Consumer Cooperative of the Central Sample Bureau of the Ministry of Economy A7 ___B7_ V. Description of the invention (> ♦ ) Acryl-12-crown ether-4; 1-acyl-15-S_-5; 1-acyl-18-S ether-6; benzot '-'12_crown ether_4; benzo-15-crown Ether-5J Benzo-18-crown B-6 pyrene bis [(benzo-15-crown ether-5) -15-ylmethyl] pyrene pivalate; 4'-bromobenzo-18-crown ether -6; dibenzyl-18-crown ether-6; dibenzyl-24-crown ether-8 / dibenzo-30-¾ ether-10; ar, ar'-di-tertiary-butyl di Benzo-18-S ether-6; '4 Dicyclohexano-18-crown ether-6 ;, Dicyclohex-24-S ether-8; 4'-Methylfluorenylbenzo-15- Crown »-5; 2- (dimethylol) -12-crown ether-4; 2- (dimethylol) -15-crown ether-5; · 2- (dimethylol) -18-crown Pyrene-6; 4'-¾ylbenzo-15-crown ether-5; 4-vinylbenzo-18-H ether-6; 1,8-dihydroxy% -dibenzo-14-crown ether- 4; 1,11-diol-20-H ether-6; poly [(dibenzo-18-B ether-6> -co-formaldehyde], and 2-methyl-2-dodecyl propane Acid bis [* 12-crown ether-4) -2-methyl]; various formulas and formulas for preparing cyclic ether compounds An example is described in U.S. Patent No. 5,393,892, (: "1 [〇1 ^ & 1 [et al., Which is hereby incorporated herein by reference, < Cyclic ether compounds that additionally contain nitrogen atoms in the ring structure, such as 2.2.2-cryptate and 2 ^ 2.1-cryptate. In one embodiment, the gold ion ion scavengers can be prepared without further steps. Is used. ≫ In another «embodiment, the gold ion ion scavengers are incorporated into the polymer, and the K polymer contains a cyclic ether moiety, and in particular« a crown ether moiety: a special example is Monomer polymer product of formaldehyde and dibenzof 18-crown ether-6. In another specific embodiment * the gold tincture is eliminated «* agent is attached to a polymer containing a metal ion scavenger is attached To the brace »The brace% can be polymer beads, membranes, compounds containing silicon gallium, or can be connected in order. -28- This paper is a Chinese national standard (CNS) A4 specification (210X297) Li) (Please read the note on the back before filling in this page) d-Binding · Ordering-Printed by the Central Laboratories of the Ministry of Economic Affairs, Off-line Consumer Cooperatives A 7 _B7_ V. Description of the invention (/) The silicon sulfide compound or its polymer that has received 9S to remove 9S · t sand 4, silicon condensate waist, glass, glass fiber, aluminum oxide, gasification, · Gasification test, or oxidized peptide. * Or other media containing gold ions elimination agent. % Waste solution M is contacted with metal sickle scavenger in many different ways. It usually depends on the state of the gold scavenger ion scavenger. For example, 1, the waste solution can be combined with the gold ion ion scavenger in the container. The waste solution can be passed through the column containing the metal ions contained in the support. • The waste solution can include metal sickle. The medium of the sterilizer, etc .: the waste solution and the metal ions are eliminated. The method of contact is not particularly limited. In a preferred embodiment of the crocodile I. When the golden eagle eagle eagle owl is attached to the polymer beads / the polymer beads themselves are contained in a column, and then the waste solution is passed through the column ~ Carving scoops are attached to the haze on the polymer beads that are present in the container. In Example 4, the waste solution is added, and the container can be optionally shaken or otherwise stirred. ♦ The polymer beads and solution are then separated. ? In a preferred embodiment, it is essential that the contact between the waste solution and the gold ion scavenger is performed before the step involving the electrochemical cell. The result / actual amount of gold ions was not introduced into the "chemical bath". Because, in some embodiments, the actual mass of metal ions in the waste solution can reduce the effectiveness of the steps involving the electrochemical cell: it is important. In the broader point, the solid gold dipper may contaminate the recovered organic hydroxide. In another example, the waste solution was fed into an electrochemical cell, and the solution recovered from the electrochemical cell was later brought into contact with the gold ion removing surface. * In the third available -29-sheet The scale is applicable to China National Standard (CNS) Α4 specification (210X297 mm) (Please read the note on the back before filling this page) 4. Order

A A7 __B7_ 五、發明説明(务) 步骤之具體實腌例中、,換句話說,在與金屬離子淸除劑接 % 觸κ前或之後、包含有機氫氧化物例如上文所述者之廢棄 瘠液被加入至«化電池中* 在根據本發明的方法中丨有檐氬氧化物例如該等上述 者在一種包括一種包括一 «化電池之步驟中純化或再製 包括霄化霣池之步驟可藉由霣解榷中的霣解或鞴由在霣滲 析霣池中的《滲析進行。該電化《池 >一般而言/包含至 少一»極、,一陰極、和分隔物及/或一個或更多個装κ用 · K定位操作在隔極和陰檯之間的單位《池許多包含各種 單位霣池和多單位霣池之電解和霣滲析電池係描述於此處 •其係使用於本發明之方法中。,多單位霣池可由在隔極和 陰極之間的許多間皤界定(參見••例如·_6)·>或多簞 位電池可由包括限極和陰極之許多間隔)界定(參見,> 例如 ,_3)。包括隈極和除極之多單位電池可為軍極姐態(參 » 見、例如或雙極組態(參見,例如,_7)。對 於可使用之單位《池的數目沒有特別限制,。在一涸具鱺實 施例中i使用於根據本發明中的«化電池包含1到約2 5« 軍位«池和較佳為1到約10個單位霣池。 « 該等單位霣池可包含二個或以上之由曝極•除極:和 之分隔物或分離物界定之間隔:該分隔物禅分鑪物可為(U 經控制细孔大小或细孔大小分佈而允許或不允許某些雕子 通過分隔物或分離物之非鑲子微孔性擴敗陣鑒例如屏摹>、 濾器、膈膜等>•成(2)離子性分隔物成分難物例如路離子 -30- 本纸張尺度適用中國國家標率(CNS) A4规格(210X297公鏟) (請先閱讀背面之注項再填寫本頁) d -裝. 訂 · 0 線 經濟部中央標準扃男工消费合作社印製 5;A A7 __B7_ 5. In the specific example of the step of the invention description, in other words, before or after contact with the metal ion scavenger, it contains organic hydroxides such as those described above. The waste barren liquor is added to the «chemical battery * in the method according to the invention 丨 eaves argon oxide such as those described above in a step including a step including a« chemical battery purification or reformation step including Xiaohuan pond It can be carried out by dialysis in the dialysis or by dialysis in the dialysis dialysis tank. The galvanic "pool> generally / contains at least one» pole, a cathode, and a separator and / or one or more devices for use with K positioning operation between the separator and the cathode "pool Many electrolytic and dialysis cells containing various unit and multi-unit cells are described herein. They are used in the method of the present invention. A multi-unit cell can be defined by a number of cells between the separator and the cathode (see, for example, _6), or a multi-cell cell can be defined by a number of intervals including the limit and the cathode (see, > For example, _3). A multi-unit battery including a pole and a pole can be military-grade (see », for example, or a bipolar configuration (see, for example, _7). There are no special restrictions on the number of units that can be used. In a modified embodiment, i is used in accordance with the present invention. The «chemical battery contains 1 to about 2 5« military position «pool and preferably 1 to about 10 unit pools.« These unit pools may contain Two or more intervals defined by the exposed electrode • depolarized: and its separator or separator: The separator can be divided into two parts: (U Controlled pore size or pore size distribution allows or disallows a certain These carvings pass through the non-inserted microporous expansion array of partitions or isolates, such as screens, filters, diaphragms, etc. > Paper size applies to China National Standards (CNS) A4 specification (210X297 male shovel) (Please read the note on the back before filling out this page) d-Packing. Order · Printed by the Central Standard of the Ministry of Economics 扃 Printed by Male Workers' Cooperatives 5;

經濟部中央棣準局貝工消費合作社印製 i '發明説明() 霣揮性臢和»離子埋揮性膜;因為他們的使用在有機氳氧 化物的製備中通常產生較高鈍度和較高產率•所以其為較 « 佳者。使用於本發明霣化霄池中的各種分隔物更完全地說 % 明於下.。 根據本發明之電化霣池包含至少二涸間隔i即•進料 參 · 間隔和回收間隔。視需要選揮性地.,根據本發明之電化電 池可包含至少一儸水間隔丨通通間隔及/或無櫬Μ或無櫬 酸回收間蹋。、在某些具鱷實施例中:根據本發明之霣化霄 池可具有二個或Κ上之上述各間限在其他具«實施例中 *霣化轚池可具有二個或Μ上之一β或Μ上的上列間隔/ 例如*.在一個具臞實豳例中;霣化霣池可具有一個進科間 隔*·二個水間隔和一個回收間隔 溶液被進枓到各間隔。,溶液可為水基質丨_或二酵基 質i另一有機溶液或其組合•。在一較佳具體實梅例中4,進 料至各間隔內的溶液為水溶液f進料至進料間隔内的溶液 包含於某濃度之欲再生或鈍化的有檐氫氧化物(水不溶解 鹽、有機鼸及/或有機氩氣化物)。,最初進料至進料間隔 内的水不溶性》\有檐《及/或有機氫氧化物的濃度在約 0. 1 Μ到約2 Μ之範圃*。在較佳具體實施例中••濃度為約0.2M 到約1Μ。在包含二個或以上進料間隔之霣扣罨池中/對於 各進料間隔濃度可相同或不同/進料到《池的溶液中的水 不溶性鼸·,有機籩及有櫬氫氧化物之濃度為約1簠量%到 約20重量%和較常在2里量%和10簠量%之閜<。進料間隔 -31- 本纸張尺度適用中國國家標準(CNS ) Α4ϋ格(210X297公釐) . . t-'' · . ^·τ=-一一丄 : (請先閱讀背面之注$項再填寫本頁) 訂Printed by the Central Laboratories of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives, "Invention Description" (霣) and »ion-implanted membranes; because their use usually produces higher inertness and relative in the preparation of organic rhenium oxides High yield • So it is better than «. The various partitions used in the trickle ponds of the present invention are more fully described below. The electrochemical cell according to the present invention contains at least two intervals i, i.e., a feed parameter interval and a recovery interval. Optionally, the electrochemical cell according to the present invention may include at least one water interval, a communication interval, and / or an OM-free or acid-free recovery compartment. In some embodiments of the crocodile, the 霣 霣 pond according to the present invention may have two or the above-mentioned intervals on other K. In other embodiments, the 霣 轚 pond may have two or 上The intervals listed above on a β or M / For example *. In a practical example; a chemical tank can have one entrance interval * two water intervals and a recovery interval solution are entered into each interval. The solution may be a water matrix or a second enzyme matrix or another organic solution or a combination thereof. In a preferred embodiment, the solution fed into each interval is an aqueous solution. The solution fed into the feeding interval contains a concentration of eaves hydroxide (water insoluble) to be regenerated or passivated. Salt, organic krypton, and / or organic argon gas). , Water insolubility within the initial feed-to-feed interval "\ Eaves" and / or a range of organic hydroxides with a concentration of about 0.1 Μ to about 2 Μ *. In a preferred embodiment, the concentration is from about 0.2M to about 1M. In a dehydration tank containing two or more feed intervals / concentrations can be the same or different for each feed interval / fed to the "water-insoluble water in the solution of the water", organic water and water Concentrations are about 1% by weight to about 20% by weight and more often 2% by weight and 10% by weight. Feeding interval -31- This paper size applies Chinese National Standard (CNS) Α4ϋ 格 (210X297mm).. T- '' ·. ^ · Τ = -one by one: (Please read the note on the back first (Fill in this page again)

M 經濟部中央標準局另工消费合作社印簟 A7 B7 五、發明説明(β) ,如術箱所暗示V保持包含欲藉由本發明再製和處理於開 始自廢液之形式的有嫌氫氧化«之溶液(。 回收間隔最初被進料溶液且較佳為水溶液,。進料到回 收‘間隔的溶液可包含或不包含雛子化合物#。在將霣流通« 霣化電池之後,,可從回收間隔回收或獲得於某濃度之有檐 氢氧化物Α在將霣流通逢電化霣池之後t•在回收藺播之有 機氬氧化物的濃度通常高於最初進料到進料間晡内的有機 氫氧化物之濃度丨在一個具黼實施例中••回收間釅中的有 檐氨氧化物的漘度為約0.1 MM上。>在另一具«實嫌例中, 回收間隔中的有機氲氣化物的濃度為約0.2M以上。在較佳 具體實施例中,,回收間隔中的有機氫氧化物的濃度約1MM 上。t在包含二個或Μ上回收間隔之電化«池中/從該等回 收間隔回收之溶液中的有檐氫氧化物之灞度在各回收間限 可相同或不同。 水間隔(若存在的話)包含一種在某濃度之雛子化合物 的溶液,。包含離子化合物之水間隔用Μ維持専霣性且可降 低搡作霣池霣壓<i鐮子化合物為在溶液中離子化的化合物 ,例如電解質*離子化合物的資施例包括》類,,金羼鹽類 和酸類或任何當溶解在水中時形成陰離子和隈離子的化合 物。在較佳具趙實施例中,,雕子化合物與相f進料到進料間 隔内的氫氣化物相同《i在另一較佳具«實施例中2 «子化 合物之陰雕子或隈離子與進料到進料間隔内的有機明離子 成睹離子有機氫氧化物之陰雕子相同•。在另一具«實胞例 -32- 本紙張尺度適用中國國家標準(CNS ) A4规格(2丨OX297公漦) (請先《讀背面之注$項再填寫本頁) ;裝. 訂 4! Α7 Β7 經濟部中央橾车局貝工消费合作社印«. 五、發明説明(β) 中,•離子化合物與被進料到進料間«內的有櫬氫氧化物不 間。在進料至水間矚中之溶液中的難子化合物之濃度在約 * 0. 1 Μ到約5H之範匪。在一較佳具驩實施例中/濃度為約0.3 Μ到約3Μ。和在一最佳具體資雎例中*濃度為约0.5Μ到約 a % 2M\在包含二個或K上水間隔之霣化霣池中.·在進料至水 間隔内的溶液中之離子化合物的濃度對於各水間隔可相同 或不同<? 通通間隔(若存在的括)最初被進料溶液且較佳為水瘠 液。,被维料到通邊間隔的溶液可包含或不包含鐮子化合物 。鐮子化合物,,如果存在的話•,可與水間《的雛子化合物 相同或不同的;> 在使用通遇間晡的具艚實拖例中/在ff滾 通遇霣化霣池之後}有機氫氧化物通邊通逢間隔·》因為大 部份不受歡迎的雑質不通過通壜間隔•.所Μ通過間鼷可用 Μ進一步婢化有機氫氧化物。, 無檐鹽或無機酸回收間隔〜如果存在的结t,最初被進 料溶液且較佳為水溶液%被進料到無機鹽或無嫌酸回收間 隔的溶液可包含或不包含難子化合物。.離子化合物:如果 存在结,可與水間隔之離子化合物相同或不同•在其中使 用無機鹽或無櫬酸回收間隔之具«實施例I霣流 通過電化霣池之後,、有嫌隈離子遷移至除禪同時來自水不 溶性鱷的陰離子從進料間隔通通到無櫬鹽或無機酸回收間 隔。.因為大部份不受歡迎的雜質不通過進入無嫌馥或無播 酸回收間隔中,所Μ無拥鼸或無拥酸可被回收且使用•,尤 « 9 -33- d. (請先閲讀背面之注意事項再4寫本頁) -裝. 訂 線 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 4! 經濟部中央標準局員工消費合作社印製 A7 B7_ 五、發明说明() 其在連讀搡作中·,當鹽或酸加至廢棄溶液中時/沈覼廢棄 溶液水不溶性馥時》。 將參考_式說明幾個可使用在本發明中的霣化霣池之 具Η資雎例,雖然很多各種霄化霣池的具钃實廉例描述於 在式中%但箱热孩技藝者顯而易知的,:其他很多沒有明 確地描述於具0實施例者存在於本發明範醒内之鼸式中。 • 一霣化霣池之具《實施例脫明於在圈1中/其為一種 霣化轚池10的概要圈示V孩電化霣池1Q包含鵰極ut,陰極 12和在開始於陽極11'分隔物13 ;其在較佳具Η資施中為 限雛子選擇性膜之顒序的單位«池。、霣化霣池1〇包含二個 間隔;1即\進料間隔14和回收間隔15«此霣池較佳可與三 種可採用的步驟之一姐合使用4。 在說明於_1之霣化霄池10的搡作中,,將包含水不溶 性鼸例如通氯酸銪,•有機鹽及/或有機氫氧化物的溶液進 料到進料間隔14。將水進料到回收間隔15,。在鵰槿和除極 之間建立和保持一電位Μ產生横««池的霣滾•因此鎗》 離子或有機播繡子被吸引向除極且通遇分隔物13進入回收 間隔15内。鎢隈離子或有機曝雕子在回收間隔中與氫氧化 物離子合併Μ產生所两要的雄氬氧化物,。雜質不會被吸引 至陰極或不會通過分隔物且因此保留在進料間皤中,。再生 之銪氫氧化物被形成且從回收間隔15中回收。. 霣化霣池之另一具體實雎例說明於·2中,* _2為一 種霣化霣池20的概要示·,該電化霣池20包含»檯21 :播 -3 4 - 本紙張尺度適用中國國家標準(CNS > Α4規格(2丨QX297公瘦) (請先Μ讀背面之注意事項再填寫本瓦) d裝· 訂 41 經濟部中央樣隼局貝工消费合作社印«. A7 B7五、發明説明Ui ) 槿2 2和包含開始於曝極21、除離子薄揮性鎮2 3和矚讎子選 揮性膜24之順序的單位單池,。《化霄池20包含三個間隔,; 即·,無嫌鹽或有機酸回收間隔2 5/遺料間隔2 6和回收間隔 27此霣池較佳輿三個可採用的步》之任何一届一起姐合 使用丨 在說明於圃2之《化《池的搡作中/將包含於水不溶 性醱丨有機81及/或有機氫氣化物的溶液逭料至進料閟隈 26»將水進料到無機鹽或有檐酸閜限回收2 5和回收間1127 。在陽極和陰檯之間建立和保持一霣位以產生横遢霣池的 霣流、因此水不溶性鹽,,有檐醴及/或有機氳氧化物之有 櫬陽離子被吸引到陰極且通邊播離子選揮性膜24進入回收 間隔27,。該有櫬》«子在回收間W中與氫氧化物離子合併 Μ產生所需要的有櫬氫氧化物丨雜質被吸引到隈檯及/或 它們不會被吸引至陰極及/或它們不會通通播極S擇性膜 24及/或保留在進料間隔中,再生之有機氫氧化物被形成 且從回收間隔27回收;> 同時·,水不溶性籩、有檐鹽及/或 有機氲氧化物的陰離子被吸引到陽極鞴此通過陰饑子雄擇 性縝2 3進入無櫬觼或無櫬酸回收間隔25内丨陰離子與隈鐮 子組合Κ在無機Μ成無懺酸回收間隔25中產生酸或鼸_。然 後從無檐邇或無機酸回收間瞄25回收酸或ρ \所Μ當利用 連鱭方法時t其可被重複使用Κ沈澱額外的水不溶性鹽。 » 在另一個具鼸實雎例中·一種與·2«化霣池相间之 «化霣池•除了二個利用於單極姐態的單位霣池之多單元 -35- 本紙張Λ度適用中國國家標準(CNS )八姑1格(210Χ297公釐) -------d {讀先閲讀背面之注f項再填寫本買) -裝 訂 經濟部中央標率局貝工消费合作社印製 A7 B7 五、發明説明(从) «池之外••說明於圈3 ·, _3為一種霣化®池30之«要圓 示,,該霣化霣池30包含第一暘極31·,第二隈極32:除極35 和二偭包含颺始於第一陰檯31,第一陰離子薄擇性臢33, » * 第一隔離子薄揮性腆34,,»極35,第二》鑛子選揮性膜36 ’和第二除麯子雄揮性_37之順序的單位霣池。說明於圓 3之霣化電池3 0包含六«間隔;即,第一無機鹽或無櫬酸 * · 回收間隔38,第一進料間隔39,,第一回收間隔40 :第二回 收間隔41·第二進科閜颺4 2和第二無櫬》或無櫬酸回收間 搞43丨埴個電池較佳可與三個可採用的步骤的任何之一姐 合使用·。 在說明於圖3之《化m池的掸作中 >將水溶液進科到 無機》或無櫬酸回收和回收間膈將包含水不溶性鹽,•有 櫬鼴及/或有櫬氲氣化物之港液進料至進料聞隔。β在鵰極 和除極之間建立和保持一電位κ產生横遘霣池的霣流t,因 此不溶鹽,、有機蘧及/或有機氫氧化物的有機隕離子被吸 引向除槿箱此通過第一或第二限離子選擇性臌34和3 6進入 回收間隔40和41內。,间時,》水不溶性鹽,:有櫬鹽及/或有 櫬氫氣化物的陰離子被吸引到個別播極藉此通過第一或第 二険雛子遘揮性腠3 3或3 7進入無機Μ或回收酸回收間隔38 和43内。_有檐播離子與氬氧化物雛子姐合Μ在回收間隔40 和41中產生所要的有機籯氧化物/然後從無镢間嗝4 0和41 回收有機氫氣化物》陰離子與跚離子姐合Μ在無饑Κ或無 機酸回收間隔38和43中齑生酸或鹽。,然後從無機臁回收或 -36- 本紙張尺度適用中國國家標準(CNS ) Α4Λ格(210><297公釐) : ·*' ' +· - til 攀+V^· ___·.». ........... 1Ι.Β--1ί ~11. M J-.J -«11^·»- . _ (請先閎讀背面之注項再填寫本頁) -裝_ 訂 111 經濟部中央標準局負工消費合作社印裝 A7 _ B7五、發明説明(Vi ) 無機酸回收間隔3 8和4 3回收酸或》>,所Μ當利用連讀方法 時其可被重複使用以沈《額外的水不溶性 電化«池之另一具體寅雎例脫明於園‘中/·4為一 種電化霣池50之概要_示〆該霣化霣池50包含颺極51/陰 極5 2和一開始於跚《51:陰難子選擇性_5 3f•第一曝離子 埋揮性_54和第二釅雕子雄揮性膜55之順序的軍位霣池。 • 霣化霣池5 0包含四個間隔j即:無機鼸或無機酸回收間隔 56,,進料間隔57,,通邊閜隔58 ;和第二回收間隔59/疽價 «池較佳可與三個可採用的步《的任何一個姐合使用 在說明於圈4之霣化《池50的搡作中•,將包含水不溶 性醱•,有櫬鹽及/或有櫬氫氧化物之溶液進料至進料間ffi 57。,將水進料到無機鼸或無機酸回收間明56 :通過間隔58 和回收間嗝59中<»在隔極和陰極之間建立和保持一霣位Μ 產生横遴電池的電流/因此水不溶性»,,有檐鹽及/或有 機氫氣化物的有櫬矚鐮子被吸引向除極和通邊第一和第二 陽離子遘擇性膜5 4或5 5和通過間隔5 8進入回收間隔59內_。 有機陽離子在回收間嗝中與氫氧化物離子合併以產生所需 要的有搬氫氧化物。艙質被吸引到鵑極•及/或他們不被亊 » 吸引到険捶,,及/成他們不通過第一和第二«離子S擇性 膜通通5 4和5 5及/或保留在進料間隔中。再生之有機氫氧 化物被形成且從該等回收間隔5 9回收;> 同時;水不溶性醱 ,有嫌鹽及/或有懺氫氧化物的陰雕子被吸引到陽播《此 通過陰離子堪擇性膜5 3進入無機鹽或無搬酸回收間隔56内 -37- 本紙張尺度適用中國國家標準(CNS ) Α4規格(2丨0X297公羡) {請先闻讀背面之注$項再填寫本贾) d 裝. *•11M The Central Standards Bureau of the Ministry of Economic Affairs, a separate consumer cooperative, A7 B7 V. Description of the invention (β), as indicated by the surgery box, V remains to contain suspected hydroxides that are intended to be reprocessed and processed in the form of self-waste liquid by the present invention « The solution (. The recovery interval is initially fed with a solution and is preferably an aqueous solution. The solution fed to the recovery 'interval may or may not contain the chick compound #. After the plutonium is circulated through the «battery, the The eaves hydroxide A recovered or obtained at a certain concentration after circulating the water through the galvanic pond. The concentration of the organic argon oxide in the recovered water is usually higher than the organic hydrogen initially fed into the feed room. Concentration of oxides 丨 In one example, the degree of eaves ammonia oxide in the recovery chamber is about 0.1 MM. ≫ In another case, the organic in the recovery interval The concentration of radon gas is about 0.2M or more. In a preferred embodiment, the concentration of the organic hydroxide in the recovery interval is about 1 MM. T In the electrochemical cell containing two or M recovery intervals «in the pool / Solvents recovered from these recovery intervals The degree of eaves hydroxide in can be the same or different at each recovery interval. The water interval (if present) contains a solution of the young compound at a certain concentration, and the water interval containing ionic compounds is maintained by 専 霣It can reduce the pressure of the operation and the pressure of the pond. ≪ i Si compound is an ionized compound in the solution, such as the electrolyte * ion compounds. Examples include 类, 羼 salts and acids or any when dissolved in Compounds that form anions and sulfonium ions in water. In the preferred embodiment, the compound of the eagle and the hydride fed into the feed interval of phase f are the same. "I is in another preferred embodiment" 2 «The female compound or ytterbium ion of the child compound is the same as the organic ion of the organic ion hydroxide in the feed-to-feed interval. In another« Cell example-32- This paper size Applicable to China National Standard (CNS) A4 specification (2 丨 OX297) 漦 (Please read the “$” on the back side before filling out this page); Pack. Order 4! Α7 Β7 Printed by the Bayou Consumer Cooperative of the Central Automobile Bureau of the Ministry of Economic Affairs «. 5. In the description of the invention (β), The ionic compound is not different from the hydrazone hydroxide fed into the feed room. The concentration of the refractory compound in the solution fed to the water is between about * 0.1M to about 5H. In a preferred embodiment, the concentration is from about 0.3M to about 3M. And in a preferred embodiment, the concentration is about 0.5M to about a% 2M. The concentration of ionic compounds in the solution in the water interval. · The concentration of ionic compounds in the solution fed to the water interval may be the same or different for each water interval. ≪? The interval (if present) is initially fed with the solution and Preference is given to aquatic fluids. The solution to which the through edge is spaced may or may not contain sickle compounds. The sickle compound, if present •, may be the same as or different from the chick compound in the water; >; In the practical example of using the pass-through method / after the pass-through pass through the passivation tank} organic hydroxide pass-through meeting interval "" because most of the unwelcome callouts do not pass through壜 Intervals • The organic hydroxides can be further oxidized by γ. The recovery interval of non-salt salt or inorganic acid ~ If there is a knot t, the solution which is initially fed with the solution and preferably an aqueous solution% is fed to the inorganic salt or non-acid recovery interval may or may not contain a refractory compound. Ionic compounds: If there is a junction, they can be the same as or different from the ionic compounds separated by water. In the case where an inorganic salt or an acid-free acid recovery interval is used, «Example I After the flow through the electrochemical cell, there is a suspected ion migration. At the same time, the anions from the water-insoluble crocodile pass through from the feed interval to the phosphonium-free salt or inorganic acid recovery interval. .Because most of the undesired impurities do not pass into the non-susceptible or non-seeded acid recovery interval, all unsupported or unsupported acids can be recovered and used •, especially «9 -33- d. (Please Please read the precautions on the back before writing this page)-Binding. The paper size of the binding thread applies to the Chinese National Standard (CNS) A4 (210X297 mm) 4! Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7_ V. [Explanation of the Invention] () It is read in series. When salt or acid is added to the waste solution / when the waste solution is water-insoluble. References will be given to explain some examples of chemical conversion pools that can be used in the present invention. Although many practical examples of various various chemical conversion pools are described in the formulas, the box-heater artist shows It is easy to know that many others are not explicitly described in the formulas in the present invention within the scope of the present invention. • The description of the “Electrical Cell” in Example 1 is shown in circle 1 / which is a general outline of the “Electric Cell” 10. The electric cell 1Q contains the electrode ut, the cathode 12 and the anode 11 ′. Separator 13; it is preferably a sequence of limited-chamber selective membrane units «pool. The chemical tank 10 contains two intervals; 1 is the \ feed interval 14 and the recovery interval 15 «This tank can be used in conjunction with one of the three available steps4. In the operation of the chemical tank 10 described in _1, a solution containing a water-insoluble solvent such as sodium perchlorate, an organic salt, and / or an organic hydroxide is fed to the feed interval 14. Feed water to recovery interval 15 ,. Establishing and maintaining a potential M between the hibiscus and the depolarizing electrode generates a horizontal «« pool of the roll • so the gun »The ions or organic embroidery are attracted to the depolarizing electrode and pass through the partition 13 into the recovery interval 15. Tungsten thorium ions or organic exposure ions are combined with hydroxide ions during the recovery interval to produce the desired male argon oxide. Impurities are not attracted to the cathode or pass through the separator and therefore remain in the feed cell. Regenerated hafnium hydroxide is formed and recovered from the recovery interval 15. Another specific example of the chemical conversion tank is described in · 2, * _2 is a general illustration of the chemical conversion tank 20, which contains »台 21: 播 -3 4-This paper is applicable to the standard China National Standard (CNS > Α4 specification (2 丨 QX297 male thin) (Please read the precautions on the back before filling in this tile) d Pack · Order 41 Printed by the Shellfish Consumer Cooperative of the Central Sample Bureau of the Ministry of Economic Affairs «. A7 B7 V. Description of the invention Ui) Hibiscus 2 2 and a unit cell containing the order starting from the exposure electrode 21, deionized thinner town 23, and the selective membrane 24. "Huaxiao Pool 20 contains three intervals; that is, no salt or organic acid recovery interval 2 5 / relic interval 26 and recovery interval 27. This pond is better than three possible steps." It will be used together by the sisters in the operation of the "Chemical Pond" described in the garden 2 / will be contained in water-insoluble 酦 丨 organic 81 and / or organic hydrogen hydride solution feed to the feed 閟 隈 26 » Expected inorganic salt or eucalyptus acid limit recovery 25 and recovery room 1127. Establish and maintain a niche between the anode and the negative stage to generate the flow of water across the pond, so water-insoluble salts, and the nuclei cations of the eaves and / or organic tritium oxide are attracted to the cathode and pass through The ion selective membrane 24 enters the recovery interval 27 ,. The "榇" ions are combined with hydroxide ions in the recovery room W to produce the required 榇 hydroxides 丨 impurities are attracted to the platform and / or they will not be attracted to the cathode and / or they will not The selective membrane 24 and / or remain in the feed interval, and the regenerated organic hydroxide is formed and recovered from the recovery interval 27; > At the same time, water-insoluble radon, eaves salt and / or organic radon The anion of the oxide is attracted to the anode, and it is selective through yin and yang. It enters the non-ortho- or non-ortho-acid recovery interval 25. The combination of anion and cymbal f. Produces acid or 鼸 _. The acid or ρ can then be recovered from the canopy or inorganic acid recovery chamber, which can be reused when using the flail method to precipitate additional water-insoluble salts. »In another practical example, one of the two types of« Chemical Ponds »and 2« Chemical Ponds », except for the two units used in the unipolar sisterhood-35- This paper is suitable for China National Standard (CNS) Bagu 1 grid (210 × 297 mm) ------- d {read the note f on the back before filling in this purchase)-printed by the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (from) «Beyond the pool •• Description in circle 3 ·, _3 is a kind of 霣 池 30« To show, the 霣 霣 30 contains the first pole 31 ·, the Two poles 32: Dipole 35 and two poles contain Yang starting from the first female platform 31, the first anion is thinly selective 臜 33, »* The first insulator is thin and thin 腆 34 ,,» pole 35, the second " The unit of the order of the ore-selective film 36 'and the second quarantine _37 is 挥. The tritium battery 3 0 described in the circle 3 contains six «intervals; that is, the first inorganic salt or non-phosphonic acid * · Recovery interval 38, first feed interval 39, first recovery interval 40: second recovery interval 41 · The second advanced battery 4 2 and the second free battery or the free acid recovery room to make 43 batteries are preferably used with any of the three steps that can be used. In "Operation of chemical tanks" explained in Figure 3> "Into the inorganic solution of the aqueous solution" or non-acetic acid recovery and recovery room will contain water-insoluble salts, with and / or with gaseous compounds The port liquid is fed to the feed scent. β establishes and maintains a potential between the carved pole and the depolarized pole, κ generates a current t across the pond, so insoluble salts, organic tritium, and / or organic hydroxide ions are attracted to the hibiscus box. Through the first or second ion-limiting ions, 34 and 36, enter recovery intervals 40 and 41. At this time, "Water-insoluble salts": Anions with osmium salts and / or hydrazones are attracted to individual broadcast poles to pass through the first or the second larvae and enter the inorganic M 3 or 3 7 Or recover acid within recovery intervals 38 and 43. _Combined with eaves ions and argon oxide to produce the desired organic tritium oxide in the recovery intervals 40 and 41 / then recover the organic hydrogen hydride from the non-titanium ion 4 0 and 41 "The anion and the counter ion Acids or salts are generated in starvation K or inorganic acid recovery intervals 38 and 43. , And then recycle from inorganic thorium or -36- This paper size applies the Chinese National Standard (CNS) Α4Λ lattice (210 > < 297 mm): · * '' + ·-til Pan + V ^ · ___ ·. ». ........... 1 Ι.Β--1ί ~ 11. M J-.J-«11 ^ ·»-. _ (Please read the notes on the back before filling this page)-装_ Order 111 Printed by the Central Bureau of Standards of the Ministry of Economic Affairs and Consumer Cooperatives for printing A7 _ B7 V. Description of the invention (Vi) Inorganic acid recovery interval 3 8 and 4 3 Recovery of acid or "> It has been reused in Shen's "Extra Water-Insoluble Electrochemical« Another Specific Example of a Pond Distinguished from the Garden '/ 4 "is a summary of an electrochemical cell 50_shows that this chemical cell 50 contains Yang 51 / Cathode 5 2 and the beginning of the order "51: Yin Dizi Selective_5 3f • First Exposure Ion Implantation_54 and Second Emperor Sculpture Male Order 55 in order. • Tritiated pond 50 contains four intervals j, namely: inorganic tritium or inorganic acid recovery interval 56, feed interval 57, through edge interval 58; and the second recovery interval 59 / three Used in conjunction with any of the three available steps in the operation of the "Pond 50" described in circle 4, will include water-insoluble 酦 •, 酦 salts and / or 榇 hydroxides The solution was fed to feed room ffi 57. Feed water to the inorganic rhenium or inorganic acid Recovering 56: through the space 58 and the recovery 嗝 59 < establish and maintain a position M between the separator and the cathode to generate a current across the battery / therefore Water-insoluble », the erect salty and / or organic hydride of the eye-catching sickle is attracted to the depolarizing and pass-through first and second cation selective membranes 5 4 or 5 5 and enters the recycling through the space 5 8 Within interval 59. The organic cations are combined with the hydroxide ions in the recovery methane to produce the desired mobile hydroxide. The capsules are attracted to the cuckoo poles and / or they are not attracted to the cormorants, and / or they do not pass through the first and second «Ion S selective membranes 5 4 and 5 5 and / or remain in During the feed interval. Regenerated organic hydroxides are formed and recovered from these recovery intervals 59; > At the same time, water-insoluble tritium, yin sculptures that are suspected of salt and / or tritium hydroxide are attracted to the positive seeding "this through anion Optional film 5 3 enters the recovery interval of inorganic salt or acid-free acid within 56 -37- This paper size applies to Chinese National Standard (CNS) Α4 specifications (2 丨 0X297 public envy) {Please read the note on the back before reading (Fill in Benja) d Pack. * • 11

»- 經濟部中央標準局貝工消費合作社印装 A7 B7五、發明説明()φ ) 。陰鐮子和皤離子姐合K在無櫬鹽或無機酸回收間隔56中 產生酸或鼸》。然後從無嫌鼸或無嫌酸回收間隔56回收酸或 馥•,所以當利用連績方法時•其可被簠禊使用以沈溅顗外 的水不溶性Μ 〃 «化霣池之另一具《實施例說明於匯5中> _5為一 種電化《池60之概要圈示,,該電化電池包含陽極61 ;陰極 62和一個開始於隈極61、雙植性膜63·、播鐮子邐擇性膜64 •和曝離子選揮性之順序單位霣池,。孩雙極性臢6 3具 有面對隔極61之陰離子遘擇性側(未顧示)和面射瞎極6 2之 播離子選擇性側(未顧示),。霣化霣池60包含四個間限即 ,水間隔66;無櫬鹽或無檐酸回收間嗝67,,進料間隔68和 回收間隔69^>瑄俚《池較佳可與三個可採用的步骤的任何 —個组合使用丨 在說明於圔5之《化«池60的搡作中*將包含水不溶 # 性鹽V有櫬鹽及/或有檐氫氧化物之溶液進料至進料閜皤 68丨將水進料到無播鼸或無機酸回收間隔67和回收間隔69 。水和離子化合物進科水間隔66。,在隈極和睹極之間建立 和保持一霣位Μ產生横通電池的霣流V因此水不溶性鹽· ♦ 有櫬鹽及/或有櫬籯氧化物的有櫬陽離子被吸引向除極和 通過陽離子選擇性膜6 5進入回收間皤6 9内々有櫬鵰饑子在 回收間隔中與氲氧化物雕子合併以產生所霄要的有機氫氣 化物丨雜質被吸引到陽極^及/成他們不被吸引到陰極/ 及/或他們不通過隕離子埋揮性膜6 5及/成保留在進料閭 -3 8 本紙張尺度適^中國國^梯準(CNS ) Λ4規格(210X297&i ) (請先閲讀背面之注$項再填寫本頁) οί 裝· 訂 A7 B7 經濟部中央標準局負工消費合作社印製 五、發明説明(β ) 皤中#。再生之有櫬氫氧化物被形成且從該等回收間隔69回 收丨同時,.水不溶性鱷*有機蘧及/或有機籯氧化物的離 離子被吸引到播槿藉此通過陰雛子選擇性K 64進入無機醱 或無檐酸回收間隔67内。陰離子和隋離子姐合Μ在無櫬馥 或無機酸回收闢隈67中瀣生酸或鹽丨然後從無櫬鼸或無嫌 酸回收間隔67回收酸或鹽、所Μ當利用建績方法時,其可 被籯禊使用Μ沈覼顗外的水不溶性馥,。 霣化霄池之另一具Η資施例說明於画6中;圈6為一 種包含二個與腫5相同之單位霣池的電化霣池7 0之《要· 示。•«化《池70包含播極71·除極7 2和一個開始於》極71 *第一雙極性縝73:第一陰離子遘揮性膜74·第一隕難子秦 · «擇性膜75 ;第二雙捶膜76,、第二陰鐮子遘擇性臟77和第 二隈霱子堪擇性膜78之順序的單位電池,。該等雙槿性膜73 和7 6具有面對隈極71之陰鑪子«揮性側(未顯示)和面對陰 槿72之》離子選擇性(未顯示)。,電化霣池70包含1:個間 闲;即、水間隔79;第一無檄鹽或無機酸回收間隔80,第 —進料間隔81 ;第一回收間隔82,,第二無機鼸或無櫬酸回 收間隔83;第二進料間隔84和第二回收間隔85f埴個霣池 較佳可與三個可採用的步嫌的任何一個組合使用,。 在說明於_6之«化電池7 0的操作中v將包含水不溶 性鼸•,有機鼸及/或有拥氫氧化物之溶液進料至進料間隔 81和84。,將水進料到無櫬Η或無機酸回收間隔和回收閜隔 。水和離子化合物進料水間隔79 在陽《和除極之間建立 -39- (請先閱讀背面之注意事項再填寫本頁)»-Printed by the Shellfish Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Invention Description () φ). Yin sickle and osmium ions generate acid or sulfonium in phosphonium-free salt or inorganic acid recovery interval 56. Then the acid or hydrazone is recovered from the suspicion or suspicion acid recovery interval 56, so when the continuous method is used, it can be used to splash water insoluble 顗 outside 顗 〃 The embodiment is described in Shui 5> _5 is an outline of an electrochemical cell 60. The electrochemical cell includes an anode 61, a cathode 62, and a starting electrode 隈 61, a double-planted membrane 63 ·, and a soy stalk. Selective Membrane 64 • Sequential unit with selective ion exposure. The bipolar 臜 6 3 has an anion selective side (not shown) facing the separator 61 and an ion-selective side (not shown) facing the blind electrode 6 2. Tritium pond 60 contains four intervals, namely, water interval 66; no salt or no eucalyptic acid recovery interval 67, feed interval 68 and recovery interval 69 ^ > Any combination of steps that can be used 丨 In the operation of "Chemical Pool 60" described in 圔 5, feed a solution containing water-insoluble # nature salt V osmium salt and / or eaves hydroxide To feed 閜 皤 68 丨 feed water to the non-seeded or inorganic acid recovery interval 67 and recovery interval 69. Water and ionic compounds enter the water interval 66. The establishment and maintenance of a unitary position between the tritium pole and the tritium pole generates a flow V across the battery, so water-insoluble salts. ♦ Tritium cations with tritium salts and / or tritium oxides are attracted to the depolarizer. And through the cation-selective membrane 6 5 into the recovery chamber 皤 6 9 々 榇 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 饥 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 雕 in a recovery interval to produce the desired organic hydride They are not attracted to the cathode and / or they are not retained in the feed through the meteorological ion-implanted membranes 6-5 and / or into the feed 尺度 -3 8 This paper is suitable for China ^ Ladder Standard (CNS) Λ4 specification (210X297 & i) (Please read the note on the back before filling in this page) οί Binding and ordering A7 B7 Printed by the Central Standards Bureau of the Ministry of Economic Affairs and Consumer Cooperatives. V. Invention Description (β) 皤 中 #. Regenerated osmium hydroxide is formed and recovered from these recovery intervals 69. At the same time, the water-insoluble crocodile * organic osmium and / or organic osmium oxide ion is attracted to the seed so as to selectively pass through the female chick 64 enters the inorganic radon or manganese acid recovery interval 67. Anions and sulphur ions are combined to generate acids or salts in the hydration-free or inorganic acid recovery solution 67, and then recover the acid or salt from the hydration-free or non-acid recovery interval 67, so when using the construction method It can be used in water-insoluble materials other than MEMS. Another example of the funded Xiaochi Pool is shown in Figure 6. Circle 6 is a "remark" of an electric pool 70 containing two units of the same unit as the tumor 5. • «Hua" Pond 70 contains sowing pole 71 · Depolarization 7 2 and one starting from "pole 71 * the first bipolar 缜 73: the first anion 遘 volatile film 74 · the first meteorite Qin ·« selective film 75; a unit cell of the second pair of diaphragms 76, the second yin sickle selective viscera 77, and the second double cricket optional membrane 78. These double hibiscus membranes 73 and 76 have ion selectivity (not shown) of the shaded furnace facing the pole 71 (volatile side (not shown) and facing hibiscus 72). The electrochemical cell 70 includes 1: a free space; that is, a water interval 79; a first hafnium-free salt or inorganic acid recovery interval 80, a first feed interval 81; a first recovery interval 82, a second inorganic thorium or no The acid recovery interval 83; the second feed interval 84 and the second recovery interval 85f are preferably used in combination with any of the three available steps. In the operation of «Chemical Battery 70" described in _6, v will contain water-insoluble 溶 •, organic 鼸 and / or hydroxide-containing solutions to the feed intervals 81 and 84. Feed the water into the hydrazone-free or inorganic acid recovery compartment and the hydration compartment. Water and ionic compound feed water interval 79 is established between the anode and the depolarizer -39- (Please read the precautions on the back before filling this page)

-56-56

X 本紙張尺度通用中國國家標準(CNS ) Α4规格(210X297公釐) 經濟部中央揉準局貝工消费合作社印掣 A7 _B7_ 五、發明说明(从) 和保持一霣位Μ產生横過《池的«潦•,因此水不溶性鹽/ 有櫬鼸及/或有櫬氫氧化物的有機»離子被吸引向離極和 通邊第一或第二隔鐮子瓖擇性臢7 5或78遺入個別回收間Μ 82和85内。,有櫬》離子在回收閜ffi中與氬氣化物離子合併 以產生所需要的有櫬氫氣化物>。雑質被吸引到曝檯,•及/ 或他們不被吸引到陰極**及/或他fl不通離子選揮性 膜通通及/或保留在進料闥颸中、苒生之有機氫氣化物被 形成且從該等回收間隔82和85回收。,同時·,水不溶性鱷.· 有機鹽及/或有截軀氧化物的陰雛子被吸引到隈槿藉此通 逢第一或第二陰離子遘揮性臢7 4或7 7進入個別的無機鱷或 無檐酸回收間隔80或83内f陰離子和跚離子組合Μ在無供 tt或無櫬酸回收間隔中產生酸或然後從無機tt或無機 酸回收間隔80和83回收酸或》、所Μ當利用連饋方法時, 其可被重複使用Κ沈澱額外的水不溶性鹽,。 在另一價具《實庵例中丨一種輿_2之電化電池相同 的霣化電池t •、除了二届利用於雙極姐態的軍位霣池之多單元霣池之外 •'說明於HB7 ;画7為一種電化電池90之《要臞示<•孩霣 化霣池90包含第一限極91·第一陰植92和開始於第一睹檯 » 91·第一陰離子S擇性膜93··第一鵰離子選揮性_ 94,第 二険極95·,第二暘槿96·,第二陰難子選揮性膜97,和第二 Ν»難子選擇性»198之順序的單位霣池。說明於_ 7之霣化 電池90包含六個間隔;,即、第一無櫬鹽或無嫌酸回收間隔 -40· 本紙張Λ度適用中國國家揉準(CNS > A4规格(210X297公釐) (請先閱讀背面之注f項再填寫本頁) .裝· 訂 經濟部中央標隼扃貝工消费合作社印*. A7 £7_ 五、發明说明(VI ) 99{第一進料閏PR100·,第一回收閭隔101·,第二無機鹽或 無機酸回收間皤102,,第二進料間釅1〇 3和第二回收閜隔104 S個電池較佳可與三個可採用的步驟的任何之一組合使 用。· 在說明於圈7之電化電池的搡作中,·將水溶液進科 到無檐臃或無檐酸回收和回收闖釅彳將包含水不溶性簾_· 有機鼸及/或有機氫氧化物之溶液進料至進料閱HI。在》X This paper size is in accordance with the Chinese National Standard (CNS) A4 specification (210X297 mm). Printed by the Central Government Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperatives. A7 _B7_ V. Description of the invention (from) and keeping one position M across the "pool" «潦 •, so water-insoluble salts / organics with 榇 鼸 and / or 榇 hydroxide» ions are attracted to the first and second septa of the polar and through edges selective 镰 7 5 or 78 Into individual collection rooms M 82 and 85. The "榇" ions are combined with the argon ions in the recovered 閜 ffi to produce the required 榇 hydride >. Substances are attracted to the exposure platform, and / or they are not attracted to the cathode ** and / or other ion-selective membranes are passed through and / or retained in the feedstock, and the generated organic hydrogen compounds are Formed and recovered from these recovery intervals 82 and 85. At the same time, water-insoluble crocodile. · Organic chicks and / or females with truncated oxides are attracted to the hibiscus to meet the first or second anion 遘 臜 4 7 4 or 7 7 into the individual inorganic The crocodile or manganic acid recovery interval within 80 or 83 is a combination of f anions and cationic ions. In the no-supply or acetic acid recovery interval, acid is generated or then recovered from the inorganic tt or inorganic acid recovery intervals 80 and 83 When using the continuous feed method, it can be reused to precipitate additional water-insoluble salts. In another example, "An example of an electrified battery with the same battery type t, except for the second multi-unit military pool which is used in the military position pool of the bipolar sister state." Described in HB7 ; Draw 7 is a kind of electrochemical battery 90 "To be displayed" < • Children's battery 90 contains the first limit 91 · the first Yin plant 92 and starts at the first station »91 · the first anion S selective Membrane 93 ·· The first ionic selectivity _ 94, the second 険 pole 95 ·, the second hibiscus 96 ·, the second yin-selective membrane 97, and the second Ν »selectivity» 198 The unit of order is 霣 池. It is explained that the battery 90 of _ 7 contains six intervals; that is, the first recovery interval of no salt or acid. -40 · This paper Λ degree is applicable to the Chinese national standard (CNS > A4 size (210X297 mm) ) (Please read the note f on the back before filling this page). Assemble and order the seal of the Central Ministry of Economic Affairs and the Seal of the Shellfisher Consumer Cooperative *. A7 £ 7_ V. Description of the Invention (VI) 99 {第一 进 料 闰 PR100 ·, The first recovery compartment 101 ·, the second inorganic salt or inorganic acid recovery compartment 102, and the second feed compartment 103 and the second recovery compartment 104 S batteries are preferably used with three Use any one of the steps in combination. · In the operation of the electrochemical cell described in circle 7, · Dispense the aqueous solution into the eaves or eucalyptus recovery and recycling. The water insoluble curtain will include water-insoluble curtains.-Organic鼸 and / or organic hydroxide solution is fed to the feed HI.

I 極和除極之間建立和保持一霣位K龜生横邊霣池的霣流/ 因此不溶鹽•,有櫬鼸及/或有櫬氩氧化物的有嫌陽雛子被 吸引向蹌極和通逢第一或第二NR雛子選擇性膜94和98進入 回收間隔101和10 4内j同時、水不溶性Μ ;有嫌鹽及/或 有櫬氢氧化物的除離子被吸引到》槿藉此通過第一或第二 陰鑲子選擇性膜93或9 7進入無機鼸或無櫬酸回收間隔9 9和 102内纟有機隈離子與氫氧化物齄子组合Μ在回收間隔101 和104中產生所要的有機氬氣化物f然後從回收間瞞101和 104回收有機氫氧化物。> 陰離子與限麯子组合Μ在無機鼸 或無檐酸回收間隔99和102中產生酸或贿;> 然後從無機《I 或無櫬酸回收間瞞99和102回收酸或蘧\所Μ當利用連鑛 方法時丨其可被重複使用Κ沈箱額外的水不溶性Μ,。 在另一個具«實施例中·# 一種包含於雙《组態之簞位 霣池的多軍位電池之霣化霣池/說明於圈8«·圏8為一種 霣化電池11Q之概要酾示·》該霣化霣池110包含第一鵰極m •第一除捶112且在開始於第一除«111·,第一陽雛子雄 -4 1 - 未紙乐尺度適用中國國家標準(CNS ) A4規格Τ210Χ297^|Γ) (请先閱讀背面之注^^項再凑寫本頁) d裝 訂 .4! Λ 經濟部中央樣率局負工消费合作社印策 A7 __B7_五、發明説明(彳) 擇性膜113·,第二跚離子遘擇性膜114,第二陰樋115,第 1 4 二陽極116 >第三陽麯子遘揮性膜ιΐ7·和第四限離子遘擇 性_118之顒序。》說明於_8之霣化霄池110包含六儒閜隔 ;即,,第一進料間隔119'第一通逢間隔120,第一回收間 1*121,、第二進料間隔122· 第二通通間隔12 3和第二回收 間隔124。、埴個«池較佳可輿三儼可採用的步骤的第三個 步驟组合使用 在說明於_8之霣化霣池的搡作中•將水溶液進料到 通邊和進料間皤丨將包含有櫬鼸或有嫌氬氣化物之溶液進 料至進料間隔。.在ΝΙ極和陰極之間建立和保持一電位Μ產 生横遇霣池的電流/因此有镟鹽或有機氫氧化物的有攏》 饑子被吸引向陰極藉此通過第一或第二隈離子遘揮性膜U4 和118進入個別回收間隔121和124内$ 有糴播離子在回收 間隔121和124中與氫氣化物鐮子合併以產生所需要的有櫬 氪氧化物。然後有«氳氧化物被從該等回收間隔121和124 * 中回收<> 電化«池之另一具體實施例說明於_9中/睡9為一 種霣化霄池130之概要圔式:該霣化霣池130包含限槿131 ,除極13 2和在開始於陽極131; 第一陽鐮子遘擇性膜133 和第二陽離子選擇性膜134之順序的單位γ«化«池130包 含三個間隔&即,,進料間隔135,,通通間隔13 6和回收間隔 137。·埴個霣池較佳可與三個可採用的步《的第三個步嫌 組合使用丨 _ 4 2 _ 本紙張尺度適用中國國家標準(CNS ) A4规格(210X297公釐) — (請先《讀背面之注$項再填寫本頁)Establishes and maintains a stream of K-shaped cross-border ponds between the I and depolarization poles / therefore insoluble salt •, susceptible larvae with radon and / or argon oxide are attracted to the radon and When the first or second NR selective membranes 94 and 98 enter the recovery intervals 101 and 104, they are simultaneously water-insoluble, and the deionization of susceptible salts and / or tritium hydroxide is attracted to This is through the first or the second negative insert selective membrane 93 or 9 7 into the inorganic rhenium or osmotic acid-free recovery interval 9 9 and 102. The organic ions and hydroxide ions are combined in the recovery intervals 101 and 104. The desired organic argon gas f is generated and the organic hydroxide is recovered from the recovery chambers 101 and 104. > The combination of anion and curcumin M produced acids or bribes in the recovery intervals 99 and 102 of inorganic gadolinium or eucalyptic acid; and then recovered the acids or gadolinium from the inorganic gallium or non-acidic acid recovery compartment 99 and 102 When using the continuous ore method, it can be reused for additional water insolubility of the CK sink. In another «embodiment · # A type of multi-military battery unit included in the dual configuration battery / description in circle 8« · 8 is a summary of a type of battery 11Q 酾Indicated · "The 霣 霣 110 110 contains the first carving pole m • The first 捶 捶 112 and begins with the first« 111 ·, the first male Yang Zixiong-4 1-Chinese paper standard applicable to the paper scale ( CNS) A4 specification Τ210χ297 ^ | Γ) (Please read the note ^^ on the back before writing this page) d Binding. 4! Λ Printing policy of the Central Consumer Samples Office of the Ministry of Economic Affairs, Consumer Cooperatives A7 __B7_ V. Description of the invention (彳) Selective membrane 113 ·, the second ion selective membrane 114, the second negative ion 115, the first 4 second anode 116 > the third positive song 遘 volatile membrane 7 and the fourth limiting ion 遘Sequence of optional _118. 》 As explained in _8, the Xiaohua Xiaochi 110 contains six Confucianisms; that is, the first feeding interval 119 ', the first meeting interval 120, the first recovery interval 1 * 121, and the second feeding interval 122 · The second communication interval 12 3 and the second recovery interval 124. The third step of «A better tank, a better tank, and a lower one" can be used in combination in the operation of the 霣 8 霣 Chemical Tank. • Feed the aqueous solution to the through edge and the feed room. 丨A solution containing krypton or argon-like gas is fed to the feed interval. Establishing and maintaining a potential M between the N1 electrode and the cathode produces a current across the cell / so there is a hydrazone salt or organic hydroxide. The starvation is attracted to the cathode to pass the first or second Ion volatile membranes U4 and 118 enter the individual recovery intervals 121 and 124. The ions are ionized and merged with the hydride sickle in recovery intervals 121 and 124 to produce the required erbium oxide. Then there is a specific embodiment of the «Plutonium oxide is recovered from these recovery intervals 121 and 124 * < > Electrochemical« pool. The _9 in / Sleep 9 is a general formula of the fluorinated Xiaochi 130: The tritium pond 130 contains a hibiscus 131, a depolarizer 13 2 and a unit which starts at the anode 131; the first positive Sickle selective membrane 133 and the second positive cation selective membrane 134 «Chem« 130 Contains three intervals & namely, feed interval 135, open interval 136, and recovery interval 137. · A large pool can be used in combination with the third step of the three available steps. __ 4 2 _ This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm) — (please first (Read the Note $ on the back and fill out this page)

訂 m. A7 _B7_ 五、發明说明(Μ) 在說明於·9之《化《池130的搡作中ν將包含有機 81或有櫬氫氧化物之溶液進料至進料間播135« 將水進料 到通通間隔136和回收間隔137〇。在矚極和陰極之間建立 和保持一霄位Κ產生横通霣池的霣流,> 因此有循鹽或有櫬 氫氧化物的有機隔難子被吸引向陰檯和通邊隕離子選揮性 膜進入回收間隔137内有櫬皤離子在回收間隔中與氳氣 化物雕子合併Μ產生所需要的有機氳氧化物雜質被吸引 到隔極;及/或他們不被吸引到陰極及/或他們不通通 隈離子遘擇性供通《及/或保留在進料間隔中,純化之有 拥氫氧化物被形成且從該回收間隔137回收/ 霣化«池之另一具«實施例說明於 10中/ 10為一 種包含二個單位罨池之電化«池140之《要示,。該轚化 電池140包含陽極141,#陰極14 2且在開始於隈極141,第一 雯極性膜143¾第一隕離子選揮性膜144,,第二雙極性膜145 和第二陽離子選擇性膜146之順序。,雙槿性臢14 3和14 5具 有面對陽極141之陰離子遘擇性俩(未顯示)和面對陰極142 之陽離子«擇性側(未顯示)。,電化電池140包含五個間隔 ,•即,水間限147>第一進料間隔148,第一回收間隔149 9 ΨOrder m. A7 _B7_ V. Description of the invention (M) In the description of "9" in the work of "Pond 130", ν will feed the solution containing organic 81 or tritium hydroxide to the feed room and broadcast 135 « Water is fed into the pass interval 136 and the recovery interval 1370. Establishing and maintaining a square position between the cathode and the cathode generates a current flowing across the pond, and therefore the organic refractory with salt or thorium hydroxide is attracted to the meridian and the passivation ion The selective membrane enters the recovery interval 137, and thorium ions are merged with the radon gaseous ions in the recovery interval. The organic thorium oxide impurities required for production are attracted to the separator; and / or they are not attracted to the cathode and / Or they can't pass through the ion selective supply "and / or remain in the feed interval, the purified bound hydroxide is formed and recovered from this recovery interval 137 / tritium« another of the pool «embodiment Explained in 10/10 is a kind of electrification «pool 140" containing two units 罨 池. The tritiated battery 140 includes an anode 141, #cathode 14 2 and starts at the cathode 141, the first polar film 143¾, the first meteoselective membrane 144, the second bipolar membrane 145, and the second cation selectivity. Sequence of the films 146. The bismuth fluorenes 14 3 and 14 5 have an anion selective surface facing the anode 141 (not shown) and a cation selective surface facing the cathode 142 (not shown). The electrochemical cell 140 includes five intervals, that is, the water interval 147 > the first feed interval 148, and the first recovery interval 149 9 Ψ

I ,第二進料間隔15 0和第二收回間隔151。疽個®池較佳可 « 參 與三個可採用的步驟的第三個步«組合使用 在脫明於醒10之《化«池140的操作中》,將包含有機 氫氧化物之溶液進料至該等進料間隔148和150/將水進料 到回收間隅。,將水和離子化合物進料到水間_·。在陽極和 -4 3 - 本紙张尺度適用中國國家標準(CNS ) Μ规格(2丨0X297公釐) (請先閲讀背面之注$項再填寫本頁) oi 裝. 訂 經濟部中央標準扃貝工消费合作社印装 4 A7 B7 五、發明说明(V) 除極之間建立和保持一霣位K產生横過霄池的霣流,,因此 有機氫氧化物的有櫬陽雕子被吸引向陰極和通遴第一或第 二I»離子堪擇性嫫14 4或14 6進入傾別回收間隔14 9或151內 。有檐限鏟子在回收閜播150中輿氬氧化物離子合併Μ產 生所需要的有拥氫氣化物γ雜質被吸引到隱極/及/或他 們不被吸引到陰極,,及/或他們不通過陽離子邇揮性膜通 邊及/或保持在進科間隔中彡再生之有《氬氧化物被形成 且從該等回收間隔15 2和155回收,》 在另一具髓實胨例中,,包含Κ雙極姐應利用的二届單 位霣池之多單元霄池的電化霣池丨說明於_11中,,圈11為 -穗包含第一陽極161,,第一除極16 2和開始於在第一陰極 161,,第一雙極性腰163ί 第一陽離子選擇性膜164:第二 陰極165,,第二I»極166/第二雙極性臢167、和第二鵰籬 子選擇性膜168的順序之霣化電池160的繁要圖示。該等雙 極性膜具有面對陽極之陰雕子理1揮性側(未顧示)和面對陰 極之隈離子埋擇性側(未顯示)丨說明於國11中之電化《池 160包含六個間隔、即/第一水間隔169,第一進料間隔170 i 經濟部中央標準局負工消费合作社印«. ,第一回收間隔171,,第二水間隔172 i第二進料間隔173 和第二回收間隔174« 埴個電池較佳可與三個可採用的步 料有建 進含間 液包之 溶將極 水 0, 陰 1 ^和 丨將間 ,,水 中到在 作料 、 搡進隔 的物間 丨池合料 °»霣化進 用化子到 使電雕料 合之和進 组11水液 驟圓將溶 步於 。•的 個明隔物 三說間化 第在收氣 的 回氫 鼸 到檐 --------0^ — — (請先聞讀背面之注$項再壤寫本頁) -44- 本紙張尺度適用中國國家標準(CNS ) Α4規格(2丨0Χ297公釐) 41 經濟部中央標準局貝工消费合作社印«. A7 B7 五、發明説明(IV、) 立和保持一電位Μ產生横遇電池的電流•因此有檐氫氧化 物的有機隕鐮子被吸引向播極藉此通過第一或第二隕離子 選擇性膜164和16 8逢入個別之回收間隔171和172內。》 離子與氫氧化物雕子合併以在回收聞限171和174中逢生所 霈要的有機氫氧化嫌/然後從回收間限171和174回收有糴 氳氧化物。· 因為所要的產物是有機籯氧化物;所以回收間隔包含 水/酵、•有懺液臞或水和酵及/或有機溶_的混合物之洛 液,,但其條件為回收間隔包含足夠的水以使可形成或再生 所要的有櫬氳氧化物。再生一詞用Μ指示溶液中來自有循 氬氧化物之«機有櫬限離子和随檐氬氧化物離子, 本發明方法之搡作可為連續或批次?本發明方法之操 作通常可為連鱭且某些間隔為不蹰地循環,。循瓖驩由泵10 及/或藉由氣體排出產生 可使用各種的材料作為電化《池中的陽播。、例如/限 榧可由金屬(例如呔)塗佈之電極、鉅、雎、绐或該等金羼 • * 之合金製造丨通常#,該等隈極將具有非可鈍化和觸媒薄膜 •其可包含金屬的贵金靥例如鉑.、銥i姥或其合金.,或包 含至少一個貴金屬例如鉑t、銥、_釕;鈀或铑之氧化物或混 合氣化物的導«氧化物的混合物。#在一個p佳具《實施例 中•«極為尺寸安定之賜極例如其上具有氧化釕及/或氣 化銥的钛基質之隔樋>> 巳在電化霣池中作為》極之各種材料可被包含在使用 _ 4 5 _ 本紙張尺度適用中國國家揉準(CNS ) A4规格(210X297公釐) --------裝— (請先閱讀背面之注f項再球寫本頁)I, the second feed interval 150 and the second withdrawal interval 151. It is better to use the "three-step" third step of the three available steps. "Combined use in the operation of" Hua «Pond 140" of awakening 10, feed the solution containing organic hydroxide To these feed intervals 148 and 150 / feed water to the recovery booth. , Feed water and ionic compounds into the water _ ·. In the anode and -4 3-This paper size applies Chinese National Standards (CNS) M specifications (2 丨 0X297 mm) (Please read the note on the back before filling this page) oi Packing. Order the central standard of the Ministry of Economic Affairs Industrial and consumer cooperative printing 4 A7 B7 V. Description of the invention (V) Establishing and maintaining a bit K between the depolarizers generates a current across the pond, so the Liyang carving of organic hydroxide is attracted to The cathode and the pass through the first or second I »ion are selectively 嫫 14 4 or 14 6 into the decantation recovery interval 14 9 or 151. The shovel-limited shovel is used to collect the argon oxide ions in the recovery broadcast 150 to produce the entrained hydride γ impurities that are attracted to the hidden electrode and / or they are not attracted to the cathode, and / or they do not pass Cationic volatile membranes pass through the edge and / or remain in the admission interval. Regeneration is "Argon oxide formed and recovered from these recovery intervals 15 2 and 155," In another example, The electrochemical cell containing the multi-unit Xiao pond of the second-stage unit cell that K bipolar sister should use is described in _11, circle 11 is-spike contains the first anode 161, and the first depolarization is 16 2 and starts at At the first cathode 161, the first bipolar waist 163, the first cation selective membrane 164: the second cathode 165, the second I »pole 166 / the second bipolar 臜 167, and the second ridge selectivity membrane. The main illustration of the sequence 168 of the battery 160 is shown. These bipolar membranes have a volatile side (not shown) facing the anode, and an erbium ion-selective side facing the cathode (not shown). Six intervals, ie, the first water interval 169, the first feed interval 170 i printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs «., The first recovery interval 171, and the second water interval 172 i the second feed interval 173 and the second recovery interval 174 «One battery can be used with three available materials. The solution is built into the solution containing the water solution. The water will be 0, anion 1 and 丨.搡 Into the separated room 丨 Pond mixture ° »霣 Inject the chemist to the sum of the electric carving material into the group 11. The water and liquid circle will be dissolved. • The individual partitions of the three-story interstitials are in the gaseous hydrogen returning to the eaves -------- 0 ^ — — (please read and read the note on the back before writing this page) -44 -This paper size is applicable to Chinese National Standard (CNS) A4 specification (2 丨 0 × 297mm) 41 Printed by the Sheller Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs «. A7 B7 V. Description of the invention (IV,) Establish and maintain a potential Μ generated Current across the battery • The organic meteorological sickle with eaves hydroxide is therefore attracted to the broadcast pole where it passes through the first or second meteorological ion selective membranes 164 and 16 8 into the individual recovery intervals 171 and 172. 》 The ions are combined with the hydroxide sculptures to produce the organic hydroxide that is required in the recovery limits 171 and 174 / and then recover the plutonium oxide from the recovery limits 171 and 174. · Because the desired product is an organic osmium oxide; the recovery interval contains water / ferment, or liquid with a liquid solution or a mixture of water and yeast and / or organic solvents, but only if the recovery interval contains sufficient Water so that the desired hafnium oxide can be formed or regenerated. The word regeneration uses M to indicate that the organic ions and argon oxide ions from the circulating argon oxide are present in the solution. Can the operation of the method of the present invention be continuous or batch? The operation of the method according to the invention can usually be flail and some intervals can be looped without interruption. The cycle is generated by the pump 10 and / or by gas venting. Various materials can be used as the electrochemical seeding in the pond. , For example / limited 榧 can be made of metal (such as 呔) coated electrodes, giant, 雎, 绐 or alloys of these gold 羼 • * 丨 usually #, these 隈 electrodes will have non-passivable and catalyst films Precious metals such as platinum, iridium, or alloys thereof, which may contain metals, or mixtures of at least one precious metal such as platinum t, iridium, ruthenium; oxides of palladium or rhodium, or oxides of mixed gases . # 在 一个 佳佳 《In the Example • «Extremely dimensionally stable electrodes such as a titanium substrate with ruthenium oxide and / or vaporized iridium on it > > 巳 is used as an electrode in an electrochemical cell Various materials can be included in use (Write this page)

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•I 經濟部中央樣隼局員工消费合作社印製 A7 B7 五、發明説明(A) 於本發明上迷和其他具髑資雎例的霣池中,。陳檷材料包括 嫌、,嫌、、不锈綱、、鍍嫌的钛、、石墨*、碳綱(嫌)或其合金等 等。術語:;合金”使用於廣泛常雄中且包括二僱或Μ上之金 颺的均匀混合物Μ及一金羼塗佈在另一金羼上。 與本發明方法之三個可採用的步*組合利用的電化« 池包含至少一個分隔物〜例如饑子«揮性臢;和視需要之 至少一個雙槿性_ Ϋ間隔為界定在二儸下列之間的區域j 分隔物及/或雙極性膜及/或陽極及/成陰檷。分«物及• I Printed by the Consumer Cooperatives of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs A7 B7 V. Description of the invention (A) In the fans of this invention and other legally qualified pools. The materials of Chen Li include susceptible, susceptible, stainless steel, titanium-plated, titanium *, graphite *, carbonaceous (susceptible), or alloys thereof. Term: "alloy" is used in a wide range of Changxiong and includes a homogeneous mixture M of Jin Yang or M and one gold tincture coated on another gold tincture. Combination with the three possible steps * of the method of the present invention The used electrochemical cell contains at least one separator ~ for example, hunger 挥; and at least one bi-sexuality as needed _ Ϋ interval is defined as a region between two or less j partition and / or bipolar membrane And / or anode and / 成 阴 檷. 分 «物 和

I /或雙極性膜作為擴擻障壁及/或氣«分離物彳 可被利用於本發明之分隔物可選自廣泛的微孔性擴敗 陣翬、.屏幕、,濾器、,膈膜等等Η其包含所需要大小的细孔 Μ允許有機氲氧化物之隁離子(例如鳍明雛子)遷移向睹極 。該微孔性分隔物可從各種材料製備;包括塑膠例如聚乙 烯、聚丙烯和特夫掄*陶瓷等等%例如·,除了 示中所列 之分隔物之外•可使用微孔性分隔物例如非離子性分隔物 。商菜上可利用的微孔性分隔物之特殊實施例包括/ Cel-anese Celgard和Norton Zitex。、當本發明之方法被利用 於純化較高分子量有機氳氧化物例如氫氧化正四丁《和氫 氧化四正丁铵時,、微孔性分《物特別有效。· 使用於本發明之《池和方法中之播離子理擇性膜可為 任何該等已經使用在有櫬氫氧化物之霣化學純化或再生中 者。較佳:嫌離子交換縝應包含高持久性材料例如Μ氟破 糸列為基質之膜或得自聚苯乙烯或聚丙烯糸列的較不贵 -4 6 _ 本紙張尺度適用中國國家標率(CNS > Α4规格(210Χ297公嫠) (請先閱讀背面之注$項再填寫本頁) ;裝· 訂 A7 ___B7___ 五、發明説明(β) 之物質。,然而*、較佳,使用於本發明之》離子理揮性贓包I / or bipolar membranes can be used as expansion barriers and / or gas separators. The separators that can be used in the present invention can be selected from a wide range of microporous expansion arrays, screens, filters, membranes, etc. It contains pores of the required size to allow the ions of organic plutonium oxides (such as fins) to migrate to the pole. The microporous separator can be made from a variety of materials; including plastics such as polyethylene, polypropylene, and Teflon * ceramics, etc.% For example, in addition to the separators listed in the illustration • Microporous separators can be used For example, non-ionic separators. Specific examples of microporous separators that can be used on commercial dishes include / Cel-anese Celgard and Norton Zitex. The microporous fraction is particularly effective when the method of the present invention is used to purify higher molecular weight organic phosphonium oxides such as n-tetrabutyl hydroxide and tetra-n-butylammonium hydroxide. · The ion-selective membrane used in the cell and method of the present invention may be any of those that have been used in the chemical purification or regeneration of rhenium hydroxide. Better: Suspected ion-exchange catalysts should contain highly durable materials such as membranes based on fluorocarbons or less expensive from polystyrene or polypropylene queues. 4 6 _ This paper applies Chinese national standards (CNS > Α4 size (210 × 297) ((Please read the note on the back before filling in this page); Binding and ordering A7 ___B7___ V. Substance of invention description (β). However, *, better, used in The invention of the "ionistic volatile bag

I 括含限離子堪擇性基的氟化膜;例如全氟磺酸和全齷磺酸 和/或全氟羧酸•,全氟碳聚合物贓例如由Ε.Ι · dupont Nenours & Co. Kffl_”Nafion",,例如杜邦陽離子 Nafion 902腰販售者。其他龐合的陽離子選揮性膜包括苯乙烯二 乙烯基苯共聚物膜(•其包含陽雕子選揮性基例如磺酸鹽基I includes fluorinated membranes containing optional ion-limiting groups; for example, perfluorosulfonic acid and perfluorinated sulfonic acid and / or perfluorocarboxylic acid. Kffl_ "Nafion ", such as DuPont's cationic Nafion 902 waist seller. Other covalent cationic selective films include styrene divinylbenzene copolymer films Base

I ,楼酸鹽基*·及其他Raipore Cationic R1010,(得自 Pall RAI),·及得自 Tokuyama Soda 的 NEOSEPTA CMH 和 NE-OSEPTA CM1膜,,因較高分子之四级化合物而特別有用 鐮子選擇性膜之製備和结構描述於化學技術百科全窨中( E π c y c 1 〇 p e d i a 〇 f C h e b i c a 1 T e c h n ο 1 〇 g y)標題為”膜技術( M e ai b r a n c e T e c h η ο 1 o g y) * 之章節中,K i r k - 01 h e r,第三 版,第15卷,第92-131頁,維斯父子·狃約,1 985。因此 I » * * 該數頁合併於此處以供參考其所掲示之各種可使用於本發 明方法中之隈離子S擇性膜 >。較佳在《化霣池中使用至少 一個陽離子選擇性膜9 任何可被利用之陰雕子薄擇性膜包括該等使用於微_( 水之去嫌方法的膜。較佳•膜應依相W之存在於霣池中的I, Louate * and other Raipore Cationic R1010, (available from Pall RAI), and NEOSEPTA CMH and NE-OSEPTA CM1 membranes from Tokuyama Soda, particularly useful for higher molecular class IV compounds The preparation and structure of subselective membranes are described in the encyclopedia of chemical technology (E π cyc 1 〇pedia 〇f C hebica 1 T echn ο 1 〇gy) entitled "Membrane Technology (M e ai brance T ech η ο 1 ogy) * in the chapter, K irk-01 her, third edition, volume 15, pages 92-131, father and son · Weiss, 1 985. Therefore I »* * The number of pages is incorporated here for Reference is made to a variety of osmium ion S selective membranes which can be used in the method of the present invention. It is preferred to use at least one cation selective membrane 9 in a chemical tank. The membrane includes such membranes that are used in the micro-water removal method. It is better that the membrane should be in the pond according to the phase.

% I 特殊陰_子(例如*鹵化物離子)選擇卩除雕子選揮性膜之 製備和结構描述於化學技術百科全窖中標{|1為”膜技術》之 章節中,,Kirk-0th*er·第三版,第15卷,第92-131頁. 雎斯父子γ紐約· 1985丨因此該數頁合併於此處Μ供參考 其所掲示之各種可使用於本發明方法中之陰離子選揮性膜 -4 7 - 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) (锖先聞讀背面之注$項再填寫本I ) -裝.% I Special anion (such as * halide ion) selective eliminator. The preparation and structure of the selective membrane are described in the chapter of the encyclopedia of chemical technology {| 1 for "membrane technology". * er · Third Edition, Volume 15, Pages 92-131. Fence & Sons, New York · 1985 丨 This page is hereby incorporated by reference for the various anions shown which can be used in the method of the present invention Optional film-4 7-This paper size applies Chinese National Standard (CNS) Α4 specification (210 × 297 mm) (锖 first read the note on the back and fill in this I)-Pack.

.IT .線 經濟部中央標準局與工消費合作社印裝 44 經濟部中央標準局兵工消費合作杜印製 A7 B7 五、發明说明(0) 〇 在陰鐮子埋揮性膜之中,,其可被利用於化電池且為商 業上可利用者為下列:,AMFLOH,.糸列310,Μ由美國檐器 和錮{造公司生產之被四级銨基取代的氟化聚合物為基質, I0HAC ΜΑ 3148,ΜΑ 3236 和 ΜΑ 3475,Μ 經衍生自 Ritter- 秦 ·Printed by the Central Bureau of Standards of the Ministry of Economic Affairs and the Industrial and Consumer Cooperatives 44 Printed by the Central Bureau of Standards of the Ministry of Economic Affairs and Industrial Cooperation Du printed A7 B7 V. Description of the invention (0) It can be used in chemical batteries and is commercially available as follows: AMFLOH, 糸 310, M quaternary ammonium group-substituted fluorinated polymer produced by the United States eaves and 锢 造 company as the matrix , I0HAC ΜΑ 3148, ΜΑ 3236, ΜΑ 3475, Μ are derived from Ritter- Qin ·

Pf aulder公司人造沸石部門產生的不均聚氰乙烯之四级銨 取代的聚合物為基霣、由Tosoh公司製造的Tosflex IE- SF34或IE-SA 48v其為一種被設計成在_性介質為安定的The quaternary ammonium-substituted polymer of Heterogeneous Polyvinyl Chloride produced by Pfaulder's Synthetic Zeolite Division is based on rhenium, Tosflex IE-SF34 or IE-SA 48v manufactured by Tosoh Corporation. Stable

臌;,得自 Tokuyaaa Soda公司的 NEOSEPTA AMH、t NE0SEPTA ACM、 NEOSEPTA AFH或 NEOSEPTA ACLE-SP;和得自 Asahi玻 » 璃的Selenion AMV和Selenion AAV。在一個具臞實施例中 * · ,,Tosflex IE-SF34和NEOSEPTA AMH険雛子交換膜為較佳 ,,因為他們在餘性溶液中(例如在本發明方法中所形成之 含氫氧化物之溶液)的穩定性#。 使用於該等«化霣池中之雙極性膜為複合膜,,其包括 三個部分:陽離子選揮性側或區域,陰縧子理揮性俩或區 參 » 域,^和介於在二涸區域之間的界面。.當直流霣流横過雯極 性膜時,具陽離子遘揮性側向或面對除極•藉由H +和OH — 離子(其可藉由在«場影響下發生於界面的水解離產生)之 傳送達成導霣性 > 雙極性膜被描述於/例神美國専利2,82 9,095、4,024,043(單一薄膜雙極性膜)和 4,116,889(平 擠雙播性膜)。使用於本發明方法中的該等雙《性膜包括 Tokuya^a Soda之 NEOSEPTA BIPOLA 1 ' WSI BIPOLAR和 Aq- -4 8 - ¥紙張尺度適用中國國家梯準(CNS > A4规格(210X297公釐j -------d (請先閲讀背面之注f項再填寫本頁) -裝. 訂 # Α7 Β7 五、發明説明(β) ualytics雙檯性膜。 在包括電化霣池之步鼸係藉由在陽極和陰榧之間施加 霣流(通常為直流鬣)而產生f通遢霄化霄池的霣流通常為 霣池之設計和性能指示的直流霣、(其在諳熟該技藝為顬 而易知的及/或可由常式實驗決定)·。通常使用《流密度 在每平方形吋約0.1和約50安培之間,,和較佳為電潦密度 在每平方吋約1和約10安培之間。,較高或較低《流密度可 被使用於某些確特殊應用<> «流密度》加至電池一段足以 形成所要數量或濃度的有機氬氣化物的時間,。 在包括電化《池之步骤期閭·、其通常希望,:在«池内 的液體之溫度可維持在約5*0到約75*C之範圔内,*較佳約 25X3到約45Ό,且特佳湛度維持在約35*Ct。也在包含霣化 « 電池之步驟期間.,通常希望:電池內的液體之PH為鹹性或 * 酸性。,在一個具鱺實施例中、,進料間隔的PH為約1至約13 ,較佳約4至約10,水間隔之pH為約0至約14:回收間播 之PH為約12至約14 %通通間隔之pH為約12至約144,無機酸 或鹽回收間隔之PH為約0至約4。,因為所申讅之方法為一 種包括氬氧化物離子及/或酸離子的純化方法,•當方法資 際進行時PH改變•且特別地i當方法貢際進行時·· PH通常 «臌;, NEOSEPTA AMH, NEOSEPTA ACM, NEOSEPTA AFH or NEOSEPTA ACLE-SP from Tokuyaaa Soda; and Selenion AMV and Selenion AAV from Asahi Glass. In a specific embodiment *, Tosflex IE-SF34 and NEOSEPTA AMH (R) seed exchange membranes are preferred because they are in a residual solution (such as a hydroxide-containing solution formed in the method of the present invention). ) Stability #. The bipolar membranes used in these chemical baths are composite membranes, which include three parts: the cationic selective side or region, the yin zongzi, the two or the region parameters, and The interface between the two regions. . When the DC flow crosses the polar film, it is cationic and lateral or facing the depolarization. • By H + and OH — ions (which can be produced by hydrolysis at the interface under the influence of the field). The transmission is achieved > Bipolar membranes are described in / example of the United States, 2,82 9,095, 4,024,043 (single-film bipolar membrane) and 4,116,889 (flat extrusion bi-layer membrane). The double-sex films used in the method of the present invention include NEOSEPTA BIPOLA 1 'WSI BIPOLAR and Aq- 4 8-¥ of Tokuya ^ a Soda. The paper size is applicable to China's national standard (CNS > A4 size (210X297 mm) j ------- d (please read the note f on the back before filling this page)-装. Order # Α7 Β7 V. Description of the invention (β) ualytics dual-layer film. It is the direct current that is generated by the application of a current between the anode and the cathode (usually a direct current), which is the direct current of the design and performance indicators of the pond. (It is known in the art as (Easy to know and / or can be determined by routine experimentation). Generally "flow density is between about 0.1 and about 50 amps per square inch, and preferably electric density is about 1 and Between about 10 amps., Higher or lower "flow density can be used for certain special applications < >« flow density "is added to the battery for a time sufficient to form the desired amount or concentration of organic argon gas, In the period including the step of electrolysis "the pond," it is usually hoped that: The degree can be maintained within the range of about 5 * 0 to about 75 * C, * preferably about 25X3 to about 45Ό, and the special good degree is maintained at about 35 * Ct. It is also during the step including the battery 霣. It is generally expected that the pH of the liquid in the battery is salty or * acidic. In one embodiment, the pH of the feed interval is about 1 to about 13, preferably about 4 to about 10, and the water interval The pH is about 0 to about 14: the recovery interplanting pH is about 12 to about 14%. The pH of the pass interval is about 12 to about 144, and the pH of the inorganic acid or salt recovery interval is about 0 to about 4. The method of plutonium is a purification method that includes argon oxide ions and / or acid ions. • The pH changes when the method is carried out. • Especially when the method is carried out .. PH usually «

蝤加、。 V 雖然不願受到任何理論之限制\但根據本發明之«化 電池的搡作係根據(部份)由於施加霣流的结果有櫬氳氣化 物的》鼸子從進科阏隔移動到回收間隔。 . -49- 本紙張尺度適用中國國家標率(CNS > A4规格(210X297公釐) -li ........—_ _____________________-------- -------- (請先閱讀背面之注項再填寫本頁) σ裝. 訂 經濟部中央梯準局貝工消费合作社印掣Add ,. V Although not willing to be limited by any theory, according to the present invention, the operation of chemical batteries is based on (in part) the occurrence of tritium gas due to the application of tritium. interval. . -49- This paper size applies to China's national standard (CNS > A4 size (210X297 mm) -li ........——_ _____________________-------- ------ -(Please read the note on the back before filling out this page) σ Pack. Order printed by the Shellfish Consumer Cooperative of the Central Elevator Bureau of the Ministry of Economic Affairs

經濟部中央標準扃貝工消费合作社印I A7 B7____ 五、發明説明(紅) 下列實庵例說明本發明的方法S除非指示否則在下列 實施例和在說明書別處和申謫専利範中、*所有的份和百 分比Μ屋量計、•所有的灌度為攝氏度.·和壓力為在或接近 大氣懕力丨 奮編俐1 將過氣酸加至包含1Μ水性ΤΜΑΗ、7.04 ΡΡ*納、33 ρρ· • « 鉀和各種產生沈灘之四甲基銨逢氯酸鹽的有懺物質之廢液 中。,鞴由過濾收集固驩四甲基銨通氯酸鼸且加至水中鞴此 形成第二溶液(四甲基銨遇氯酸鹽沒有宪全溶解在水中),。 將第二溶液進料至根據·2之霣化《池的進料間隔内,。隱 極是用氧化釕塗佈之钛做成的,,和陰極是用鍊做成的/水 進料至回收間隔和無機酸或無櫬馥間隔内纟豳加一霣位藉 此造成四甲銨陽離子向陰槿移動、藉Μ在回收間隔中產生 具有減少金羼雜質之氫氧化四甲铵j回收間隔中的氫氧化 四甲铵之濃度在1. 18ΜΜ上$回收間皤亦包含少於〇.65ρρ· 納和少於〇.28ρρ·鉀且實霣上沒有非TMAH之有嫌金羼,。 奮嫵锎2 將氫釀酸加至包含1M水性ΤΜΑΒ、、7.04 ρρ·納,、33 PP· 鉀和各種產生沈澱之碘化四甲基铵的有機物質之廢液中 藉由通癉收集固體四甲基铵碘化物,且加至声中鞴此形成第 二溶液(四甲基銨磺化物沒有完全溶解在水中)《。將第二溶 % 液進料至根據圈5之電化電池的進料間隔内。t陽極是用氧 化釕塗佈之钛做成的、•和陰極是用嫌黻成的水進料至回 -50- 本紙張尺度適用中國國家梯準(CNS ) A4規格(2丨OX297公着) (請先聞讀背面之注^^項再填寫本頁) -裝. 訂 線 A7 ____B7_ 五、發明説明(叫) 收間隔和無櫬酸成無機鹽間限內丨將磺氫酸之稀釋水溶液 進料至水間嗝ξ雎加一霣位藉此造成四甲銨»雛子向陰極 移励\藏Μ在回收闋隔中產生具有減少金羼雑質之氩氧化 四甲铵、。回收間隔中的氫氣化四甲銨之濃度在1.18 Μ以上 、回收間隔亦包含少於0.6 5ρρ·納和少於0.28ρρ·鉀且實質 上沒有非ΤΜΑΗ之有櫬金屬,。Printed by the Central Standard of the Ministry of Economic Affairs and Consumers' Cooperatives I A7 B7____ V. Description of the Invention (Red) The following examples illustrate the method of the present invention. Unless indicated otherwise, in the following examples and elsewhere in the description and in the application, * All All parts and percentages are measured by a house scale. All irrigation degrees are in degrees Celsius. And the pressure is at or near atmospheric pressure. Fenbian Li 1 Add peroxyacid to 1M aqueous TMA, 7.04 PP * sodium, 33 ρρ · «Potassium and various tetrakimonium ammonium chlorate-producing waste liquids that produce sunk. Glycerol tetramethylammonium perchlorate is collected by filtration and added to water to form a second solution (tetramethylammonium is not completely dissolved in water with chlorate). The second solution was fed into the feed interval of the cell according to · 2. The salient pole is made of titanium coated with ruthenium oxide, and the cathode is made of chain / water is fed to the recovery interval and the inorganic acid or non-interval interval plus a bit to thereby cause the top four The ammonium cations move to the hibiscus, and the concentration of tetramethylammonium hydroxide in the recovery interval is reduced by the amount of tetramethylammonium hydroxide in the recovery interval. The concentration of tetramethylammonium hydroxide in the recovery interval is 1.18ΜΜ. 〇.65ρρ · sodium and less than 0.28ρρ · potassium and there is no non-TMAH suspected gold ions. Fenque 2 Add hydrogen acid to a waste liquid containing 1M aqueous TMAB, 7.04 ρρ · sodium, 33 PP · potassium and various organic substances that produce precipitated tetramethylammonium iodide, and collect the solid by purging. Tetramethylammonium iodide was added to the sound and a second solution was formed (the tetramethylammonium sulfide was not completely dissolved in water). The second solution was fed into the feed interval of the electrochemical cell according to circle 5. t The anode is made of titanium coated with ruthenium oxide, and the cathode is fed back to -50 with water that is formed into the water.-This paper size applies to China National Standard (CNS) A4 specification (2 丨 OX297) ) (Please read the note ^^ on the back before filling in this page)-Packing. Thread A7 ____B7_ V. Description of the invention (called) Within the interval between the free space and the inorganic acid to form an inorganic salt 丨 Dilute the sulfuric acid The aqueous solution is fed to the water and 嗝 ξ 雎 plus one bit to thereby cause tetramethylammonium »to move the cathode to the cathode. In the recovery compartment, argon oxidized tetramethylammonium with reduced gold content is generated. The concentration of tetramethylammonium hydride in the recovery interval is 1.18 M or more, the recovery interval also contains less than 0.6 5ρρ · nano and less than 0.28ρρ · potassium, and there is substantially no non-TMA non-fluorene metal.

謇淪供I S 將包含6 · 3 ρρ·納' 0 . 93 ppi鉀之1Μ四甲基铵水溶液( 混合氲氧化物和氣化物)進枓至根據_1之霣化霣池的進 料一回收間隔内丨隔《是用氧化釕塗佈之钛做成的/和險 極是用鎳做成的纟將0.1Μ HC1溶液進料至廢棄溶液間隔,。 施加11小時之11 ·Α霣流,。從進料一回收間《回收之溶液 包含0.9 6Μ氩氧化四甲铵和氯;3.2ρρ·納和0.34ρρ·鉀將 此溶液進枓至根摊園9之霣化電池的進料間皤内卩》極是 用氧化釕塗佈之钛做成的丨和除極是用鎳做成的將水進 料至回收和通通間隔內;梅加一霣位藉此造成四甲銨Μ離 子向陰極移動;薄以在回收間瞞中產生具有減少金屬雄質 和有機之氫氧化四甲铵。、回收間限中的氬氧化四甲銨之濃 度在1.2 ΜΚ上S回收間隔亦包含少於3 ΡΡ·納和少於0.3 ΡΡ·鉀且實質上沒有非ΤΜΑΗ之有機金屬、 奮觖俐4 將氫氣酸加至四级技氫氧化物之廢棄溶液藉此形成四 级氯化技溶液。該溶液包含1.0 5%四级氣化銨和0.91 ρρ· -5卜 本紙張尺度適用中國國家標率(CNS > 乂4^格(210Χ297公釐) (請先閱讀背面之注f項再填寫本頁)For the IS, the 1M tetramethylammonium aqueous solution (mixed with tritium oxide and gaseous) containing 6 · 3 ρρ · n '0.93 ppi potassium was fed to the feed-recovery interval of the tritium pond according to _1 The inner spacer is made of titanium coated with ruthenium oxide and / or the pole is made of nickel. 0.1M HC1 solution is fed to the waste solution space. Apply 11 Α 霣 flow for 11 hours. From the feed 1 recovery room, the recovered solution contains 0.9 6M argon oxidized tetramethylammonium and chlorine; 3.2ρρ · nano and 0.34ρρ · potassium. The "卩" pole is made of titanium coated with ruthenium oxide, and the depolarizer is made of nickel. Water is fed into the recovery and pass-through interval; a megamechanical position is used to cause tetramethylammonium ions to the cathode. Move; thin to produce tetramethylammonium hydroxide with reduced metal and organic in the recovery compartment. The concentration of tetramethylammonium argon oxide in the recovery interval is 1.2 MK. The recovery interval also contains less than 3 PP · nano and less than 0.3 PP · potassium and there is substantially no non-TMA organic metal. Hydrogen acid is added to the waste solution of the fourth-stage hydroxide, thereby forming a fourth-stage chloride solution. The solution contains 1.0 5% quaternary ammonium gasified and 0.91 ρρ · -5. The paper size is applicable to China's national standard (CNS > 乂 4 ^ (210 × 297 mm)) (Please read the note f on the back before filling (This page)

訂 經濟部中央樣隼局貝工消费合作社印褽 經濟部中央標準局Λ工消费合作社印裂 A7 __B7_ 五、發明説明(姑) 納。將壓力霣池裝備MPF-34奈米lift濾膜、。四级氯化铵溶 液之一半在450 psig懕力下強迫通過該膜f該沒有通15膜 之溶液的部分包含1.7 %四級氣化铵和0.92 pp·»^。將此 溶液進料至根據_2之霣化霣池的進料間皤内。播極是用 « 氧化釕塗佈之呔做成的·和陰極是用嫌儎成的.。水進料至 回收間隔和無檐酸或無機K間限内。施加一霣位藉此造成 * 四甲铵限雕子向険極移動,藉Μ在回收間跚中產生具有減 « 少金羼和有櫬雜霣之氫氧化四甲銨,。回收間m中的氫氧化 四甲铵之濃度在1.2 MM上。回收間隔亦包含少於0.5 ρρ· • . 納且實質上沒有非TMAH之有欐金属》。Order the seal of the shelling consumer cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs A7 __B7_ of the Central Bureau of Standards of the Ministry of Economic Affairs. The pressure tank was equipped with MPF-34 nanometer lift filter. One and a half of the quaternary ammonium chloride solution was forced through the membrane at a pressure of 450 psig. The portion of the solution without 15 membranes contained 1.7% quaternary ammonium vapor and 0.92 pp · »^. This solution was fed into the feed cell of a chemical tank according to _2. The emitter is made of ruthenium oxide-coated hafnium and the cathode is made of hafnium. Water is fed into the recovery interval and within the eucalyptus or inorganic K interval. Applying a nib to thereby cause the tetramethylammonium-restricted sculpture to move toward the pole, and by using M to produce tetramethylammonium hydroxide with reduced «less gold 羼 and mixed 霣 ,, in the recovery. The concentration of tetramethylammonium hydroxide in recovery m was 1.2 MM. The recovery interval also contains less than 0.5 ρρ · •. Sodium and is substantially free of non-TMAH ferrous metals.

奮_俐R t 將氫氩酸加至四级銨氫氧化物之廢棄溶液箱此形成四 鈒氯化铵溶液。該溶液包含4.7 7%四级氯化铵和1.77 ρρ· % 納。將壓力霣池装備Desa卜5奈米過濾膜。四级氯化銨物 % 4 溶液之一半在450 psig懕力下強迫通遢該膜?該沒有通邊 膜之溶液的部分包含6.35%四级氯化铵和1.77 ρρ·納,。將 此溶液進料至根據國2之霄化霣池的進料間晡内t。《極是 用氣化釕塗佈之钛做成的和睹極是用嫌做成的。《水進料 至回收間隔和無機酸或無機鼸間膈內丨施加一電位鶊此造 成四甲銨隔離子向陰極移動,.藉Μ在回收和播中產生具有 減少金屬和有機雜霣之氫氣化四甲技,回收間限中的氫氧 化四甲铵之濃度在1.8 HK上。、回收間隔亦包含少於1 ρρ· 納且實質上沒有非ΤΜΑΗ之有機金鼠。 -52- 本紙張尺度適用中國國家標準(CNS > Α4规格(2丨0X297公釐) (請先W讀背面之注$項再填寫本頁) -裝_ -、11 經濟部中央標準局貝工消费合作社印製 A7 B7 五、發明説明(Μ) 奮觖俐ft 將碳酸氫納加至四級銨氫氧化物之廢棄溶液中藉此形 成四级碳駿氲銨溶液,。該溶液包含0.095 %四级碳酸氳銨 和0.91 ρρ·納。將壓力霣池裝備MPF-3 4奈米通濾膜。四 ' s 级碳酸氫铵溶液之一半在4 50 psig壓力下强迫通過該膜。 • 沒有通通膜之該溶液的部分包含0.149 %四级碳酸氫銨和 1.75ppb納。、將此溶液進料至根據_5之霄化霣池的進料 間隔内 '陽極是用氧化釕塗佈之呔做成的,·和瞜極是用嫌 做成的 ' 水進料至回收間隔和無機酸或無機鹽閭搞和。 TMAH之溶液進料至水間隔$施加一電位藉此造成四甲銨限 離子向除極移動,,蘋以在回收間隔中產生具有減少金屬和 有機雜質之氫氧化四甲銨,。回收間隔中的氫氧化四甲銨之 濃度在1MM上彳回收間隔亦包含少於0.5ρρ·納且實霣上沒 非TMAH之有機金羼。 瞀嫵俐7 將碳酸氫納加至四级銨氫氧化物之廢棄溶液中藉此形 成四级碳酸氫铵溶液4。該溶液包含4.01%四級碳酸氫銨和 0.6 9扣)》納\將壓力電池裝儋〇6 88 1-5奈米過濾膜。四级破 % 酸氫铵溶液之一半在450 psig壓力下強迫通遢該縝4。該沒 有通通膜之溶液的部分包含5.8 3%四级碳_氫銨和1.28 PP·納將此溶液進料至根據_4之霣化霄池的進料間限 内'隔極是用氧化釕塗佈之肽做成的•和除極是用嫌做成 的《•水進料至回收·,通過和無機酸或無檐臁間隔内,。施加 -53- (請先閱讀背面之注11^項再填寫本頁) •裝. 訂 線 本紙張尺度適用中國國家揉準(CNS ) A4規格(210X297公釐) 經濟部中央揉準局貝工消费合作社印製 A7 __B7_ 五、發明説明(0 ) 一霣位箱此造成四甲妓隱鐮子向險檯移動t•鞴以在回收藺 隔中產生具有減少金靨和有機雄霣之氬氧化四甲铵,。回收 間隔中的氫氧化四甲銨之濺度在1.5MM上。、回收間嗝亦包 含少於1 . 1 PP·納且資質上沒非TMAH之有機金羼.。 奮_锎8 . 將包含水性2.5%TMAH、3.75PP·鉀和各種有機物質的 廢棄溶液輿商業上可得到之包含冠釀之聚合物(一種甲醱 和二苯並18-S醚-6之產物)推通 '從聚合物分離溶液及_ 由遇滹收集。,將第二溶液進料至根據·8之電化霣池的進 料間隔内丨隈極是用氧化釕塗佈之肽做成的:和陰極是用 嫌做成的水和離子化合物進料至回收和通通間隔內,。施 加一霣位蕹此造成四甲銨»離子向陰檷移療I,.藉Κ在回收 間隔中產生具有減少金羼雑霣和減少有嫌雜霣之再生氫氣 化四甲铵回收間W中的氫氣化四甲銨之濃度在8%Μ上 。回收間隔亦包含少於0 . 58 ρρ·钾且實質上沒非ΤΜΑΒ之有 櫬金屬。 « 奮嫌俐9 · 將包含水性2.5%ΤΜΑΗ、340 ppb鉀和各種有嫌物霣的 廢棄溶液與商乘上可得到之包含冠醚之聚合物(一種甲醛 軔二苯並18-冠醚-6之產物)推邇4。從聚合榔分雛溶液及藉 由邊濾收集$將第二溶液進料至根據園8之電化霣池的進 料閜隔内。釅捶是用氧化釕塗佈之呔做成的,·和路極是用 難 嫌做成的,。水和雕子化合物通料至回收和通通闖皤内。施Fen Li Li added hydrogen argon acid to the waste solution tank of the quaternary ammonium hydroxide to form a tetraphosphonium ammonium chloride solution. The solution contained 4.7 7% of quaternary ammonium chloride and 1.77 ρρ ·% nano. The pressure cell was equipped with a Desa 5 nanometer filter membrane. One-half of the solution of quaternary ammonium chloride% 4 was forced to pass through the membrane at 450 psig. The portion of the solution without a through-membrane contains 6.35% tetraammonium chloride and 1.77 ρρ · ,. This solution was fed into the feed chamber of a chemical tank in accordance with country 2. "The pole is made of titanium coated with vaporized ruthenium, and the pole is made of suspicion. "Water is fed into the recovery interval and between the inorganic acid or the inorganic ions, and a potential is applied. This causes the tetramethylammonium isolator to move to the cathode. The hydrogen is used to reduce the metal and organic impurities during recovery and sowing Tetramethylammonium technology, the concentration of tetramethylammonium hydroxide in the recovery interval is 1.8 HK. The recovery interval also includes organic golden rats less than 1 ρρ · nanometer and substantially free of non-TMAΤ. -52- This paper size applies to Chinese National Standards (CNS > Α4 size (2 丨 0X297mm) (please read the note on the back before filling in this page)-installed _-, 11 Central Bureau of Standards, Ministry of Economic Affairs A7 B7 printed by the Industrial and Commercial Cooperatives Fifth, the description of the invention (M) Fen Li ft added sodium bicarbonate to the waste solution of the quaternary ammonium hydroxide to form a quaternary carbon ammonium solution. The solution contains 0.095 % Ammonium quaternary ammonium carbonate and 0.91 ρρ · nano. The pressure cell is equipped with an MPF-3 4 nm pass membrane. One and a half of a four's ammonium bicarbonate solution is forced through the membrane at a pressure of 4 50 psig. • None The part of the solution that passes through the membrane contains 0.149% of quaternary ammonium bicarbonate and 1.75 ppb nanometers. This solution is fed into the feed interval of the 霣 5 chemical tank, the anode is coated with ruthenium oxide It is made, and the hydrazone is made with the susceptible 'water feed to the recovery interval and the inorganic acid or inorganic salt, and the TMAH solution is fed to the water interval to apply a potential to thereby cause the tetramethylammonium limit. As the ions move towards the depolarizer, Ping Yi produces hydroxides with reduced metal and organic impurities in the recovery interval. Tetramethylammonium. The concentration of tetramethylammonium hydroxide in the recovery interval is 1MM. The recovery interval also contains less than 0.5ρρ · nano and there is no non-TMAH organic gold tincture. 瞀 妩 利 7 The sodium bicarbonate Add it to the waste solution of quaternary ammonium hydroxide to form a quaternary ammonium bicarbonate solution 4. This solution contains 4.01% quaternary ammonium bicarbonate and 0.6 9 buckles) "Nano \ Pressure battery pack 〇88 88 1 -5 nanometer filter membrane. One-half of the four-stage broken% ammonium bicarbonate solution was forced to pass through the plutonium at 450 psig. The part of the solution without a membrane is composed of 5.8 3% quaternary carbon ammonium hydrogen and 1.28 PP. This solution is fed into the feed interval of the tritium tank according to _4. The separator is made of ruthenium oxide. The coated peptide is made of hydrazine, which is made of suspicion, and the water is fed to the recycling, through the interval with inorganic acid or eaves. Imposition -53- (Please read Note 11 ^ on the back before filling out this page) • Binding. The size of the paper is applicable to the Chinese National Standard (CNS) A4 (210X297 mm). Printed by the Consumer Cooperative A7 __B7_ V. Description of the Invention (0) A box of four places caused the four-year-old prostitutes to move to the danger station t • 台 to produce argon oxidation with reduced gold ions and organic male ions in the recovery compartment. Tetramethylammonium. The tetramethylammonium hydroxide splash in the recovery interval was 1.5MM. Recycling booths also contain organic gold badges that are less than 1.1 PP · N and are not non-TMAH qualified. Fen_ 锎 8. A waste solution containing water-based 2.5% TMAH, 3.75PP · potassium and various organic substances will be commercially available and a polymer containing crown brew (a formamidine and dibenzo 18-S ether-6 The product) was pushed through 'separating the solution from the polymer and collecting it by Yu. The second solution is fed into the feeding interval of the electrochemical cell according to · 8. The electrode is made of a peptide coated with ruthenium oxide: and the cathode is fed to Within the recovery and communication interval. The application of one site caused the tetramethylammonium ion to transfer to the yin, and I used the K to generate a regenerated hydrogenated tetramethylammonium hydrogen recovery chamber in the recovery interval with reduced gold ions and reduced susceptible ions. The concentration of tetramethylammonium hydroxide is 8% M. The recovery interval also contains less than 0.58 ρρ · potassium and is substantially free of non-TMA fluorinated metal. «Fen Yan Li 9 · A waste solution containing 2.5% water-based TMA, potassium 340 ppb and various kinds of suspected gadolinium and a commercially available crown ether-containing polymer (a formaldehyde gallium dibenzo 18-crown ether- The product of 6) shoved 4. Separate the chick solution from the polymer and collect it by side filtration to feed the second solution into the feed compartment of the electrochemical cell according to the garden 8. Rhenium is made of ruthenium oxide-coated rhenium, and He Luji is made of unbelievable. Water and sculpture compounds are fed into the recovery and communication facilities. Shi

I -54- 本紙flt尺度適用中國國家標準(CNS ) Α4規格(2丨0X297公釐) --------OI裝— (请先»讀背面之注意Ϋ項再填寫本頁) 訂 A7 B7__ 五、發明説明(θ ) 加一電位藉此造成四甲技Μ離子向除槿移動,•藉Η在回收 間隔中產生具有減少金屬雑質和減少有檐雑質之再生氬氧 化四甲銨。回收W隔中的氫氧化四甲枝之濃度在上 。商收間Μ亦包含少於17 ppb鉀且實Λ上沒非ΤΜΑΗ之有機 金屬' 而本發明已在相翮的較佳具臞實施例中被解釋•其 t 將被了解是其各種修正對於諳熟該技藝.者在讀說明窨時為 顯而易知的。因此:其將被了解的是:意欲掲示在此處之I -54- This paper's flt scale is applicable to China National Standard (CNS) Α4 specification (2 丨 0X297mm) -------- OI package— (Please read the “Notes on the back side” before filling this page) Order A7 B7__ V. Description of the invention (θ) A potential is added to cause the tetramethylammonium ion to move to the hibiscus, and by using the tritium in the recovery interval, the regeneration of argon oxidized tetramethylammonium with reduced metal and eaves quality is achieved. Ammonium. The concentration of tetramethyl hydroxide in the recovered W partition is above. The commercial collection M also contains less than 17 ppb potassium and there is no organic metal other than TIMA, and the present invention has been explained in the related preferred embodiment. Its t will be understood to be its various modifications to Those who are familiar with this technique are obvious and easy to understand when reading the instructions. Therefore: it will be understood that:

• I 本發明附加的申謫専利範涵篕該修正>。 (請先Μ讀背面之注$項再填寫本頁)• I The additional claims of the present invention contain the amendment>. (Please read the note on the back before filling in this page)

OI -裝·OI-Outfit ·

.•IT ,線 經濟部中央揉车局貝工消费合作社印裂 -55- 本纸張尺度適用中鬮國家標準(CNS > A4規格(210X297公瘦). • IT, line Printed by the Central Government Bureau of the Ministry of Economic Affairs of the Bayan Consumer Cooperatives -55- This paper size applies to the China National Standard (CNS > A4 size (210X297 male thin))

Claims (1)

經濟部中央揉準局ec工消费合作社印*. A8 B8 C8 ______ D8'申請專利範圍 ι· 一種從包含有檄氫氧化物和雜質之_棄溶液中回收有檐 氳氣化物的方法、,包括: 完成(灰1&-灰11>),(灰2)和(灰3)之一, (Ala)從廢索溶液中沈激有機氫氧化物作為不溶馥;及 9 (Alb)從暇索溶液中除去不溶醱且將該醴放置在一液體 中Μ形成第二溶液; (Α2)或 (A2al)將廢索溶液進料至包括至少二俚間隔、一陰極、 一隈極和大小《揮性分隔物之第一霣化電池^, 且將電流通通第一霣化霣池/藉此雜質邐移通遘 大小遘揮性分隔物;4 (A2a2)從第一霣化霣池中回收包含有機雛子的第二溶液 ;或 (A2bl)從廢棄溶液中形成包含豁邇和雜質之第一溶液 (A2b2)在壓力下將第一溶液與大小S擇性臌接觸,其中 # 至少一部分的雜質通過大小選擇性膜、,藉此提供 包含鎗鼸和減少數董的雜質之第二溶液 (A3)將廢棄溶液與金羼離子淸除劑接觸K除去金靥離子 雑質*其中步驟(A3)在步驟(B)和(C)在之前或之後 » 宪成;· (B)將得自(Alb)之第二溶液、得自(A2a2)或(A2b2)之 第二溶液或得自(A3)之廢索溶液進料至包含至少二 個間隔,一陰極* 一鵰檯和分隔物之第一《化電池 % (請先閱讀背面之注$項再赛寫本Ϊ) ο 裝· 訂 ϋ線· 本紙張尺度逋用中《國家揉準(CNS ) A4規格(210X297公釐) 經濟部中央揉率局貞工消费合作社印装 A8 B8 C8 _ D8 六、申請專利範圍 中且將«流通通第一«化霣池藉此再生有播氫氣化 物;和 (C)從第一電池中回收有櫬氳氧化物,。 2·—種從包含有櫬氫氧化物和雑資之廢棄溶液中回收有機 «氧化物的方法:包括: (A) 從廢棄溶液中沈溉有櫬氫氧化物作為不溶鼸;及 4 (B) 從廢棄溶液中除去該鹽且將該鼸放置在一液艚中Μ 形成第二溶液; % (C) 將第二溶液進料至包含至少二個間颺、一陰極,一 * « 隔極和分隔物之電化霣池中和將m流通通電池,藉 « 此再生有機氬氧化物;和 (D) 從電池中回收有禳氫氧化物。 % 3. 根據申誧專利範園第2項的方法其中在步驟(A)中沈 澱之不溶鹽為至少一俚通氱酸鼸•、供化物Μ ·,和蕹鹽。 善 4. 根據申謫專利範園第2項的方法,其中在步驟(Α)中有 檐氫氣化物係藉由將無櫬蘧或無機酸加至廢棄溶液中而 5. 根據申請専利範醒第2項的方法,k其中霣化霣池包括至 少四届間隔、•一陰極,、一限極、且從隁極到陰極之次序 為、雙極性膜•,陰鐮子選擇性膜,和》離子選擇性膜/第 二溶液被進料到由除離子和限離子遘揮的膜所形成的間 隔中、和有櫬氫氧化物從由陽離子選揮性膜和陰瘡所形成 的間隔中回收、。 tr 本紙張尺度適用中國•家糅率(CNS ) A4规格(210X297公釐) ---------II (請先W讀背面之注f項再填寒本霣) 訂 41 R2 I R、N-R3 I R4 A8 B8 C8 ^___ 六、申請專利範圍 β.根據申嫌専利範_第5項的方法,,其中無機鹽成無櫬黢 從由雙極性膜和陰鐮子«擇性膜所形成的間隔中回收。 , 7. 根據申請專利範麵第2項的方法>,《化《池包含至少三 個間隔•、一陰極,ν—陽極,,和從隔極到除極之次序為/ 陰離子選擇性麟和NI雛子埵揮性腆ι·第二溶液被進料至 由陰離子和限離子選擇性臢所形成的閬隔中,•和有_氬 氧化物從由陲離子選擇性顏和陰極所形成的間ffi中回收 0 \ 8. 根據申請專利範園第2項的方法·其中在«索溶液之有 % *機氲氧化物為Μ下式表示的四級铵氫氧化物 OH· (III) R 1 ,R2 ,R3和R4分別為包含1到約10個碳原子之烷 基,%芳基:或R1和R2為和氮原子一起可形成芳族或非 芳族雑環之烷基丨但其條件為如果雜環基包含C = N- ·則 R3為第二鍵。 \ 9. 一種從含四级氫氧化物和雜質之廢索溶液中回收四级氫 氧化物的方法丨包括,: (A) 從廢索溶液中沈箱四级氫氧化物作為水不溶》; (B) 將得自廢棄溶液中的四级鹽加至一液艚中* »此形 本紙張尺度逋用中國國家橾準(CNS ) A4规格(210X297公釐) --------------TT------om (請先閱讀背面之注$項再填寫本頁) 經濟部中央揉率局貝工消費合作社印氧Printed by the Central Government Bureau of the Ministry of Economic Affairs of the EC Industrial and Consumer Cooperatives *. A8 B8 C8 ______ D8 'Patent Application Scope · A method for recovering eaves gas from a waste solution containing thorium hydroxide and impurities, including: : Completion of one of (ash 1 & -ash 11 >), (ash 2) and (ash 3), (Ala) impregnating the organic hydroxide from the waste cable solution as insoluble tritium; and 9 (Alb) from Remove the insoluble plutonium from the solution and place the plutonium in a liquid to form a second solution; (A2) or (A2al) feed the waste cord solution to include at least two plutonium intervals, a cathode, a pole, and The first chemically-separated battery, and the current is passed through the first chemically-suppressed battery / thus the impurities are transferred to the size of the volatile separator; 4 (A2a2) is recovered from the first chemically-suppressed battery and contains A second solution of organic chicks; or (A2bl) forms a first solution (A2b2) containing waste and impurities from the waste solution. The first solution is brought into contact with the selective sulfonium under pressure, where # at least a portion of the impurities pass through Size-selective membrane, thereby providing a second solution (A3) containing guns and reduced impurities The waste solution is contacted with the gold ion ion scavenger K to remove the gold ion ion substance * where step (A3) is before or after steps (B) and (C) »成 成; · (B) will be obtained from (Alb) The second solution, the second solution obtained from (A2a2) or (A2b2), or the waste cable solution obtained from (A3) is fed to a first solution containing at least two compartments, a cathode *, a stand, and a separator. Battery (% please read the note on the back before writing the match) ο Binding, binding line, and paper size in use "National Standards (CNS) A4 (210X297 mm)) Printed by Zhengong Cooperative Cooperative A8 B8 C8 _ D8 VI. In the scope of patent application and the «circulation through the first« chemical tank to regenerate the hydrogenated hydrocarbons; and (C) the recovery of tritium oxide from the first battery Things. 2 · —A method for recovering organic «oxides from a waste solution containing thorium hydroxide and thallium hydroxide: including: (A) immersing thorium hydroxide as insoluble thorium from the waste solution; and 4 (B ) Remove the salt from the waste solution and place the mash in a liquid mash to form a second solution;% (C) Feed the second solution to a solution containing at least two interlayers, a cathode, and a * «separator Neutralize the galvanic cell with the separator and pass m through the battery to regenerate the organic argon oxide; and (D) recover the tritium hydroxide from the battery. % 3. The method according to item 2 of the Shenyang Patent Fanyuan, wherein the insoluble salt precipitated in step (A) is at least one hydrazone, hydrazine, and sulfonium salt. Good 4. The method according to item 2 of the Shenyang Patent Fanyuan, wherein the eaves hydrogenate in step (A) is obtained by adding a non-water or inorganic acid to the waste solution. 5. According to the application Two methods, in which the tritium cell includes at least four intervals, a cathode, a limit, and the order from the pole to the cathode is, bipolar membrane, yin sickle selective membrane, and The ion-selective membrane / second solution is fed into the space formed by the deionized and ion-restricted membrane, and the hafnium hydroxide is recovered from the space formed by the cationic-selective membrane and vulva . tr This paper size is applicable to China • Furniture Ratio (CNS) A4 specification (210X297mm) --------- II (please read the note f on the back and fill in the cold copy) Order 41 R2 IR 、 N-R3 I R4 A8 B8 C8 ^ ___ VI. Application for patent scope β. According to the method of applying for Lifan _ Item 5, in which the inorganic salt is formed from the bipolar membrane and the Yin sickle «selective The space formed by the film is recovered. 7. According to the method of patent application No. 2 >, "The cell contains at least three compartments, a cathode, ν-anode, and the order from separator to depolarization is / anion-selective ion. The second solution is fed into the barrier formed by the anion and ion-selective ion, and the argon oxide is formed from the ion-selective ion and the cathode. Recovered from the intermediate ffi 0. 8. According to the method of the patent application Fanyuan Item 2, in which «% of the solution solution * the organic oxide is quaternary ammonium hydroxide OH represented by the following formula: (III) R 1, R2, R3, and R4 are alkyl groups containing 1 to about 10 carbon atoms,% aryl groups: or R1 and R2 are alkyl groups that together with nitrogen atoms can form aromatic or non-aromatic fluorene rings, but their Provided that if the heterocyclyl contains C = N- · R3 is a second bond. \ 9. A method for recovering quaternary hydroxide from a waste cable solution containing quaternary hydroxide and impurities 丨 including: (A) Caching the quaternary hydroxide as water insoluble from the waste cable solution "; (B) Add quaternary salt from the waste solution to one solution * »This paper size is in accordance with China National Standard (CNS) A4 (210X297 mm) -------- ------ TT ------ om (Please read the note on the back before filling in this page) The Central Rubbing Bureau of the Ministry of Economic Affairs, Shellfish Consumer Cooperative, printed oxygen '申請專利範固 成第二溶液; % (C) 將第二溶液逭科至包含至少二個間明·,一陰極•一 (請先"讀背面之注$項再#寫本頁) I 颶槿和分隔物之霣化霣池中和將電流通遘霣池t •藉 此在電池中再生四级氫氧化物;和 (D) 從霣池中回收四級氬氧化物P 根據申請專利範疆第9項的方法,,其中四级氬氧化物在 步骤(A)中鞴由將無機鼸或無機酸加入廢棄溶液中而沈 澱。 ♦ Π.根據申請專利範_第9項的方法•其中«化電池包括至 I 少三儷間隔,,一陰極、一陽槿,.和從矚極到陰極之次序 為\除雕子适揮性膜和限齄子邇擇性贓丨第二溶液被進 料至由陰雛子遘揮性膜和隈離子遘擇性膜所形成的間嗝 中,,和從由陲離子遘擇性膜和陰播所形成的間晡中回收 四鈒氫氧化物<; 12.—種從含有機氫氧化物和雜質之廢棄溶液中回收檐氫氧 化物的方法%有包括: 經濟部中央櫺率局貝工消费合作社印裝 (A) 將廢棄溶液進料至包含至少二個間隔;一陰極,•一 隈槿和大小遘揮性分隔物之第一霄化霣池中和將電 潦通遇霣池,.藉此雜質遷移通過大小選揮性分隔物t ♦ t (B) 從第一 «化«池中回收包含有櫬離子之第二溶液和 將第二溶液進料至包含至少二個間隔,.一除極.·一 陽極和分隔物之第二電化霣池中和將《流通通第二 本紙張尺A逍用中國國家揉準(CNS)A4规格(210x297公羡) J | ................ ....--- A8 B8 C8 ----- D8 六、申請專利範困 霣化霣池•、藉此純化有循氫氧化物和 (c)從第二霣化《池中回收有機氫氧化物; 13.根據申請專利範第12項的方法 '進一步包括在步》(A) I 之前先増加被污染溶液中有糴箄氣化物的濃度,。 14·根據申請専利範圃第13項的方法·_其中有循氫氧化物濺 度蝤加之步嫌包括至少一個蒸發f、電滲淅或逆滲透/ 15.根據申誚専利範圔第12項的方法4•其中有機氫氧化物為 四级铵氲氧化物:四级嫌簠氧化物或三级毓氫氧化物/ 16·根據申請専利範第12項的方法,•其中第一《化《池之 大小選擇性分隔物為陽離子缠擇性膜,。 17. 根據申請專利範圃第12項的方法:其中第一霣化«池包 括至少三個間隔\一陰極、一限極•且從播極到陰槿之 次序為、雙棰性顏和大小遘擇性膜限離子s揮性膜.*在 步驟(A)中將裔棄溶液進料至由雙極性臢和大小S揮性 限離子選擇性膜所形成的間隔中,,和在步»(B)中從由 雙極性膜和大小埋擇性限離子選擇性膜所形成的間隔中 回收第二溶液$ 18. 根據申謫專利範麵第12項的方法*其中第二霣化電池包 參 括至少三個間隔*、一陰極,一陽槿,*且從陽極到陰極之 ' % % 次序為•、第一陽離子龌擇性膜和第二隈鐮子《擇性膜· 在步»(Β)中將第二溶液進料至由陽檯和第一陽離子選 揮性膜所形成的間隔中/和在步驟(C)中從由第二陽雛 子遘揮性膜和陰極所形成的間隔中回收有機觝氧化物。 龜 -5 ' 本紙張尺度逋用中國國家梯準(CNS ) Α4规格(210 X 297公釐) --------Q^.-- (請先Η讀背面之注$項再#寫本X ) 訂 經濟部中央橾率局貝工消費合作社印裝 中請專利範圍 A8 B8 C8 D8 經濟部t央榣準局Λ工消费合作社印蓑 19·—種從含鎗氫氣化物和雜質之廢棄 物的方法:包括: (A) 從廢索溶液中形成包含鏽鼸和 (B) 在壓力下接觸第一溶液與大小 一部分的雑質通«大小選擇性 籩和減少數量之雄質的第二溶 (C) 將第二溶液進料至包含至少二 隕極和分隔物之霣化電池中和 此纯化錶氫氧化物;、和 (D) 從電池中回收中銪氬氧化物。 » 2〇·根據申請專利範園第19項的方法., 無機酸或無機鼸中和廢棄溶液。 « 21. 根據申誚專利範圍第19項的方法*, 被汚染的溶液通遇離子交換系統,。 22. 根據申請專利範_第19項的方法,· 選揮性膜是奈米過濾膜。 23. 根據申請專利範晒第19項的方法· % 0. 1重悬%到約20重量妬的銪鹽。. 24. 根據申猜専利範園第19項的方法••其中® 少三個間隔•一陰極,,一陽播,,且從隈捶 為2除極,•陰離子選擇性膜和陽鑪子堪揮 (C)中將第二溶液進料至由陰雕子理揮性 擇性麟所形成的間隔中:和在步K(D>中 -6- 溶液中回收鎗氫氧化 雄資之第一溶液. 選擇性 膜.,鶊 液·: 儒間限 將霣流通通霣池/藉 膜/其中至少 此提供包含鎗 一除極/ 一 其中步驟(A)包括Μ 其中步驟(Α)包括將 其中步驟(B)中的大小 其中第二溶液包含約 化霣池包括至 到除極之次序 性膜/在步驟 膜和隈難子埋 從由鵑_子選 (請先閱讀背面之注$項再楼寫本頁) ----裝----11訂 α 本紙張尺度適用中國國家椹率(CNS ) A4规格(210X297公釐) 經濟部中央椹车局貝工消费合作社印製 A8 E84553 !S _____ D8 _ '申請專利範圍 揮性膜和陰極所形成的間隔中回收銥氫氧化物,。 25.根據申謫専利梅圃第2 4項的方法,,其中該方法為埋續且 從由陰離子邐擇性膜和播極所形成的間隔回收之無_蘧 或無機酸被使用於步骤(A)中K形成第一溶液 26·—種從含有檐氫氧化物和包括金饜雕子雜質的雜質之磨 索溶液中回收有檐氫氧化物的方法包括,: (A) 接觸廢棄溶液輿金羼雛子澝除ffiM除金鼷離子雑霣 ♦ 9 I (B) 將得自A3之廢棄溶液進料至包含至少二僩間隔* 一 除極t,一限極和分隔物之霄化霣池中和將霣流通埵 霣池 ',薄此再生有櫬氫氧化物/及 (C) 從霣池中回收有播氫氧化物? 27. 根據申誚專利範匾第2 6項的方法,其中在步驟(A)之前 先增加廢棄溶液中有> 氫氧化物的濃度,。 28. 根據申請専利範画第2 7項的方法其中有櫬氫氧化物濃 度》加之步骤包括至少一《蒸發或逆滲 29. 根據申請專利範圃第2 6項的方法,、其中金廳離子濟除劑 包括至少一個瓖醚化合物:包含醚部分之聚合物和包含 冠_部分之聚合物,。 30. 根據申請專利範圈第2 6項的方法·,其中分隔物為隱鐮子 選揮性臢和得自(A)之廢棄溶液被進料至由隈棰和陽雛 子埋擇性膜所形成的間隔\和有機氬氧化物溶液從由隈 離子遘擇性棋和除極形成的間隔中回收.。 本紙張尺度適用中围國家揉率(CNS ) Μ规格(210X297公釐) --------------1T------QI (請先閱1^面之注f項再填寫本頁) 384553 Α8 Β8 C8 D8 77、申請專利範圍 31.根據申猜専利範圃第2 6項的方法•、其中在廢棄溶液之有 機氬氧化物為Μ下式表示的四级銨氰氧化物 R, 3 - R2—·Ν·丨R4 + ΟΗ- 經濟部中央揉準局Λ工消费合作社印策 R1 ,R2 ,. R3和R4分別為包含1到約10價碳原子之烷 基\芳基:或R1和R2為_性基,.其和氮原子一起可形 成芳族或非芳族雜環、,但其條件為如果_環基包含C=N-*則R3為第二鐽 32. 根據申請專利範圔第26項的方法;其中廢棄溶液更進一 步包含相當於有機氫氧化物的有機鹽,。 33. —種從含有機氢氣化物和包括金羼離子雜質的雜質之廢 索溶液中回收有懺氫氧化物的方法1包括: (A) 將醆棄溶液進料至包含至少二個間隔丨一陰極a,一 暘極和分隔物之電化電池中和將霣流通遇電准,箱 此有櫬離子通過分隔物和再生有櫬《氧化物,; (B) 從電池中回收有機氫氧化物溶液,; (C) 接觸有櫬氫氧化物溶液與金羼離子清除劑Μ除去金 羼離子雜霣;^ (D) 回收有機鲺氧化物.。 34. 根據申請専利範園第3 3項的方法••其中金羼離子清除劑 -8 - (請先Η讀背面之注$項再填寫本頁) 訂- ο 本紙張尺度適用中«國家梂準(CNS)Α4规格(210x297公兼) 經濟部中央橾率局Λ工消费合作社印装 E84&53 μ ___ D8'申請專利範圍 包括至少一個環醚化合物和包含醚部分之聚合物,。 35. 根據申謫専利範國第3 3項的方法|•其中分隔物為陽離子 理揮性膜和顢棄溶液被進料至由陽極和隔離子遘揮性膜 所形成的間隔中·,和有機氬氧化物溶液從由陽離子理擇 性縝和除極形成的間隔中回收,。 36. 根據申請専利範第33項的方法,,其中在廢索溶液之有 棰氫氧化物為Μ下式表示的四趿铵氫氧化物 R1 Γ-Ν-—R4 R3 + ο R 1 : R2 ν· R3和R4分別為包含1到約10涸碳原子之院 基\芳基、或R1和R2驗性基,、其為_(性基#,其和氣原 子一起可形成芳族或非芳族雜環丨但其條件為如果雜瑁 基包含C = Ν -,則R3為第二鐽。· ---------0»^.------订------ο (請先聞讀背面之注$項再«寫本買) 本紙張尺度逋用中國國家揉率(CNS > Α4规格(210X297公釐)'Apply for a patent solution to solidify the second solution;% (C) Divide the second solution to contain at least two intersects, one cathode and one (please first read the note $ Item on the back and then #write this page) I neutralize the hydrangeas and separators in the plutonium tank and pass the current through the cell t to thereby regenerate the fourth-level hydroxide in the battery; and (D) recover the fourth-level argon oxide from the plutonium P according to the application The method according to item 9 of the patent, wherein the quaternary argon oxide is precipitated in step (A) by adding an inorganic plutonium or an inorganic acid to the waste solution. ♦ Π. Method according to Patent Application _ Item 9 where «Batteries include at least three intervals, one cathode, one hibiscus, and the order from attention to cathode is \ The second solution is fed into the membrane formed by the female membrane and the ion-selective membrane, and from the ion-selective membrane and the cathode. Recovery of Tetrahydroxide Hydroxide from the Ladder Formed by Seeding 12. 12. A method for recovering eaves hydroxide from waste solutions containing organic hydroxides and impurities% includes: Printing by industrial and consumer cooperatives (A) Feed the waste solution to a tank containing at least two compartments; a cathode, a hibiscus, and a large and small volatile separator in the first tank and pass the electricity to the tank , So that the impurities migrate through the size-selective separator t ♦ t (B) recover the second solution containing thallium ions from the first «chemical« cell and feed the second solution to at least two compartments, One depolarization. One anode and separator of the second electrochemical cell and the second paper A Xiao uses the Chinese National Standard (CNS) A4 specifications (210x297). J | ..... --- A8 B8 C8 ----- D8 VI. Patent application for chemical treatment of chemical tanks, to purify cyclic hydroxide and (c) Recovery of organic hydroxide from the second chemical reaction tank; 13. Method according to item 12 of patent application 'Further includes increasing the concentration of radon gas in the contaminated solution before step (A) I. 14 · According to the method of applying for the benefit of the project No. 13 _ which includes the hydroxide splash plus steps including at least one evaporation f, electroosmosis or reverse osmosis / 15. According to the application of the project Method 4 • In which the organic hydroxide is a quaternary ammonium hafnium oxide: a quaternary ammonium halide oxide or a tertiary hafnium hydroxide / 16. According to the method of application No. 12 of Lilifan, • the first of which The size-selective separator of the cell is a cation-entangled membrane. 17. The method according to item 12 of the patent application: where the first puppet «pool includes at least three compartments, a cathode, a limit pole, and the order from the broadcast pole to the hibiscus is, double-sex, and size Selective membrane-limiting ion s-volatile membranes. * In step (A), feed the waste solution into the space formed by the bipolar europium and size S-selective ion-selective membranes, and in step » (B) The second solution is recovered from the gap formed by the bipolar membrane and the size-selective ion-limiting selective membrane. 18. The method according to item 12 of the application patent application * wherein the second tritiated battery pack Include at least three intervals *, one cathode, one hibiscus, and * the order of% from the anode to the cathode is •, the first cationic selective film and the second sickle "selective film in step» ( In step (B), the second solution is fed into the space formed by the balcony and the first cation-selective volatile film and / or in step (C) from the space formed by the second positive-electrode volatile film and the cathode. Organic hafnium oxide is recovered. Turtle-5 'This paper size uses China National Standard (CNS) Α4 size (210 X 297 mm) -------- Q ^ .-- (Please read the note on the back side first. ## Manuscript X) Order the patent scope A8 B8 C8 D8 of the Central Government Bureau of the Ministry of Economic Affairs in the printing of the patent scope A8 B8 C8 D8 Ministry of Economic Affairs t Central Government Bureau Λ Industrial Consumer Cooperative Association's Seal 19 · —A kind of waste from guns containing hydrogen and impurities Method: (A) forming a second solution containing rust from a waste cable solution and (B) contacting the first solution with a portion of the sizing agent under pressure «size selectivity» and reducing the amount of male substance (C) feeding the second solution to a tritiated cell containing at least two meteorites and a separator to neutralize the purified epihydroxide; and (D) recovering the tritium argon oxide from the cell. »2〇 · According to the method of the 19th patent application, neutralize the waste solution with inorganic acid or inorganic rhenium. «21. According to the method of the patent application No. 19 *, the contaminated solution meets the ion exchange system. 22. According to the method of the 19th patent application, the selective membrane is a nanofiltration membrane. 23. According to the method of the patent application No. 19,% 0.1 resuspension from about 20% to about 20 weight jealous salt. 24. According to the method of Shenchai Yuli Fanyuan's item 19 •• Among which ® there are three less intervals • One cathode, one yang sowing, and 2 from 除 to depolarize, • Anion-selective membrane and anode furnace In step (C), the second solution is fed into the space formed by the selective selective ridge of the sculptors: and in step K (D > in the -6- solution, the first gun oxyhydroxide is recovered. Solutions. Selective membranes, liquids :: Confucian interstitial fluids pass through the pond / boring membrane / where at least this offer contains a gun depolarization / a where step (A) includes M where step (A) includes where The size in step (B) in which the second solution contains a reduction tank, including a sequential membrane to the depolarization / the membrane and the dysprosium are buried in the step by the cuckoo _ subselect (please read the note on the back side first) (Floor this page) ---- Installation ---- 11 orders α This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm) Printed by A8 E84553 by the Bayou Consumer Cooperative of the Central Automobile Bureau of the Ministry of Economic Affairs! S _____ D8 _ 'The scope of the patent application is to recover iridium hydroxide in the space formed by the volatile film and the cathode. 25. According to the application The method of item 24 of Limeipu, wherein the method is submerged and recovered from the space formed by an anion-selective membrane and a soot-free or inorganic acid is used in step (A) to form K First solution 26 · A method for recovering eaves hydroxide from a grind solution containing eaves hydroxide and impurities including impurities of golden eagle carvings includes: (A) contacting a waste solution to remove the golden worms ffiM removes metal ions ♦ 9 I (B) feed the waste solution from A3 to a tank containing at least two 僩 intervals * one eliminator t, one limiter and separator, and circulate 霣埵 霣 池 ', regenerate 榇 hydroxide and / or (C) recover the hydrated hydroxide from the 霣 pond? 27. According to the method in item 26 of the Shen patent patent plaque, in step (A) Prior to increasing the concentration of the hydroxide in the waste solution, 28. According to the application of the method of Lifan painting item 27, which has the concentration of hydroxide, the step includes at least one "evaporation or reverse osmosis 29. According to The method of applying for patent No. 26, wherein the Jintang ion-eliminating agent includes at least one tritium Ether compound: a polymer containing an ether moiety and a polymer containing a crown moiety. 30. The method according to item 26 of the patent application circle, wherein the separator is a cryptic compound and obtained from (A The waste solution of) was fed to the space formed by the selective film of osmium and yangyangzi, and the organic argon oxide solution was recovered from the space formed by the selective ion and depolarization of osmium ion ... Applicable to Central China Kneading Rate (CNS) M specifications (210X297 mm) -------------- 1T ------ QI (please read the note f of 1 ^ face first) (Fill in this page) 384553 Α8 Β8 C8 D8 77, scope of patent application 31. According to the method of item 26 of Shenchai Lifanpu, where the organic argon oxide in the waste solution is quaternary ammonium cyanide oxidation represented by the following formula物 R, 3-R2— · Ν · 丨 R4 + ΟΗ- The Central Government Bureau of the Ministry of Economic Affairs, R & D, R2, R2,. R3 and R4 are alkyl groups containing 1 to about 10 valent carbon atoms, respectively. Group: or R1 and R2 are _ nature groups, which together with the nitrogen atom can form aromatic or non-aromatic heterocyclic rings, but the condition is that if the _ ring group contains C = N- *, then R3 is the second 鐽 32 . The method according to item 26 of the patent application; wherein the waste solution further contains an organic salt equivalent to an organic hydroxide. 33. A method 1 for recovering thorium hydroxide from a waste solution containing organic hydrogen hydride and impurities including gold rhenium impurities, including: (A) feeding the thorium solution to at least two compartments 丨A cathode a, a cathode and a separator in an electrochemical cell neutralize the thallium current, and there is a thorium ion passing through the separator and the thallium oxide is regenerated. (B) The organic hydroxide is recovered from the battery. Solution ,; (C) contacting the osmium hydroxide solution and the gold ions scavenger M to remove gold ions ions; ^ (D) recovering organic rhenium oxide. 34. According to the method of applying for 専 利范 园 item 3 3 •• Among them, gold ions ion scavenger-8-(please read the note on the back before filling in this page) Order-ο This paper is applicable to «Country 梂Standard (CNS) Α4 (210x297). E84 & 53 μ ___ D8 'patent application scope of the Central Government Bureau of the Ministry of Economic Affairs includes at least one cyclic ether compound and a polymer containing an ether moiety. 35. The method according to item 3 of Shen Lili Fan Guo | • wherein the separator is a cationic volatile film and the rejection solution is fed into the space formed by the anode and the separator 遘 volatile film, and the organic The argon oxide solution is recovered from the gap formed by cation-selective tritium and depolarization. 36. The method according to claim 33, wherein the ammonium hydroxide in the waste solution is a tetraammonium hydroxide R1 Γ-Ν-—R4 R3 + ο R 1: R2 ν · R3 and R4 are respectively a radical or aryl group containing 1 to about 10 涸 carbon atoms, or R1 and R2 test groups, which are _ (性 基 #, which together with gas atoms can form aromatic or non-aromatic groups Heterocyclic ring 丨 But if the heterofluorene group contains C = Ν-, then R3 is the second 鐽. · --------- 0 »^ .------ Order ---- --ο (Please read the note on the back of the item before buying in «copies») This paper size is based on the Chinese national rubbing rate (CNS > Α4 size (210X297 mm)
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* Cited by examiner, † Cited by third party
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CN117164070A (en) * 2023-11-03 2023-12-05 浙江百能科技有限公司 Device, system and method for coupling treatment of aromatic ring salt-containing wastewater and hydrogen storage
CN117164070B (en) * 2023-11-03 2024-02-23 浙江百能科技有限公司 Device, system and method for coupling treatment of aromatic ring salt-containing wastewater and hydrogen storage

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