TW304887B - - Google Patents

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Publication number
TW304887B
TW304887B TW084109238A TW84109238A TW304887B TW 304887 B TW304887 B TW 304887B TW 084109238 A TW084109238 A TW 084109238A TW 84109238 A TW84109238 A TW 84109238A TW 304887 B TW304887 B TW 304887B
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TW
Taiwan
Prior art keywords
ozone
filter material
item
filter
ether
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TW084109238A
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Chinese (zh)
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Hoechst Ag
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/66Ozone
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/007Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8671Removing components of defined structure not provided for in B01D53/8603 - B01D53/8668
    • B01D53/8675Ozone
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biomedical Technology (AREA)
  • Toxicology (AREA)
  • Treating Waste Gases (AREA)
  • Control Or Security For Electrophotography (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

經濟部中央標隼局員工消費合作社印装 A7 _______B7 _ 五、發明説明(1 ) 本發明和用於將臭氧自氣體和液體中移除的濾材,濾 膜及使氣體或液體與含有聚芳醚(..polyarylene ether) 之濾材接觸的方法有關》 已知在電子照相、影印及印刷製程中會有少量的臭氧形 ' / 成。所用像影印機或雷射印表機的設備會不斷將所產生的 臭氧排放到周遭的大氣中。臭氧就味道而言是一個污染物 ’同時即令是小的濃度也會對健康有損害的效果。爲補正 這點,已發展出許多的方法來從這類設備釋出的空氣體氣 流中移除臭氧。在這些方法中,臭氧不是被破壞掉,就是 以化學方式或物理方式來結合。 已知可以加熱或使與金屬觸媒作用來破壞臭氧(參見 JP-60 1 9 7 223 和 JP — 60 19 115)。然而臭氧熱破壞的缺點是能量的消耗和完成臭 氧分解所需的高溫。 此外,還知道使氣體氣流流經濾'•膜來以催化方式使臭 氧發生分解(參見JP — 58 0 8 1 425)。使濾 膜的基本材料與一個或以上的金屬化合物,金屬或合金-比如鐵化合物’锰化合物或鎳化合物-浸漬(impregnate) 在一起 ,並 且另外 加入包括像鈀或鉑等貴金屬 的化合 物或金屬至濾膜中。這些觸媒非常貴,並且通常只有一定 的使用年限,這是因爲雜相觸媒會迅速被各種不同的觸媒 毒劑給去活化。 另外也知道一種包含有礬土或活化碳等載體材料的濾 膜’它是和會與臭氧作用的乙烯型不飽和化合物侵漬在一 本紙張尺度適用中國國家橾準(CNS ) A4規格(2丨0x297公慶) - - ml d^t • * I (請先閱讀背面之注意事項再填寫本頁) -4 - 附件A :第841〇9238號專利申請案中文説明書修正頁^04887 修正 民國85年05月修正 8a5.2i 4 充 五、發明説明(2 ) 起(參見DE 37 28 802)。該化合物,比如 萜,其缺點是在許多情形下一視所用載體材料而定一具有 揮發性,於是會以小置形式被帶走,進而漏失掉。還有就 是,只有小部份的濾膜重量可被用作活性成份。 此外,已知在由纖維平板構成,用於使臭氧分解的濾 膜中,其纖維含有使臭氧分解的觸媒(參見J P_ 0 3 270 718)。在較佳體系中爲多孔的這些纖維是由 具有下列可與臭氧發生劇烈反應之官能基的聚合物所組成 :比如一SH,=S,一1^只2,=?^11,_€1^和 —OH。所提及的臭氧分解用觸媒是由像金,銀,銅,鈀 ,鐵,鎳,鈷和錳的金屬,或其氧化物,和礬土及矽藻土 所構成。製造濾膜所需的纖維是以傳統的紡絲方法來獲得 ,它是使觸媒分布在紡絲溶液中,並在紡絲後使均勻地分 布在纖維中。加入第二個聚合物,並使與第一個聚合物一 起引發相分離,以及對紡絲產物進行各種處理,如此可獲 得包含有觸媒顆粒的多孔用。所得纖維接著以傳統方法來 製造以製成濾膜。被視爲適當的聚合物僅總括地提及.只 (請先閲讀背面之注意Ϋ項再填寫本頁) 經濟部中央標準局貝工消費合作社印裂 且以濾 移 時 用的氧 費 種除臭 很 一移將 是 供氧中 亦 提臭體 造 下將液 製 點中和 的 缺 體 體 膜 述液氣 濾 上和自 該 無。體 於 , 在法氣 用 外 要方自。種 之 是及於醚 I 此 標膜用芳供 除 目濾種聚提 , 的,一有外 腈 明材供含另 烯。發濾提包還 丙的本的明材明 聚賣此氧發濾發 了 昂因臭本該本 示常 除 , 揭非 移 材 本紙張尺度逋用中國國家揉率(CNS ) A4規格(2丨Ο X四7公釐)_ 5 - A7 B7 五、發明説明(3 ) 除的濾膜,它含有一個包含有聚芳醚的濾材。 本發明還提供一種用於將臭氧·.自氣體和液體中移除的 方法,它使用到包含有聚芳醚的濾材’並使氣體或液體與 濾材表面接觸。 聚芳醚是一·種含有至少一個芳醚單元(一 A — 0—, 其中A是伸芳基)。伸芳基是用來指具有兩個鍵結位置的 芳基單元’比如一CeH4—。單—或多環芳族化合物可形 成伸芳基單元,比如苯,吡啶,棻,菲(phenanthrene) 和慈(anthracene)。較宜爲經取代的伸芳基單元。伸芳 基上的取代基可以是: C 1— C 18院基 比如一 c Η C 2Η 2 η 5 -C3H7,〜C4H9,- C5Hai ,-C ( C H 3 ) 3 , -ch2-ch (ch3) 2; C i 一 c i e羥基—烷基,比如—C H 3"〇 H, -C2H4〇H . -c3H6OH - -ch2-ch (ch3) 2- (請先閲讀背面之注意事項再填寫本頁) i -裝· 訂 經濟部中央標準局貝工消費合作社印繁 C 1— C 18 —院氧基 芳氧基 C Η 2 Ο Η ; 比如—〇ch3,—〇c2h5 -OC3H7,- 0 c 4H 9 ' -0〇5ΗΧ1, _qCHz_ C H ( C H 3) 2, -0C2H4-Ch ( c h 3 ) 2, 比如一OCeH5, 2_氧基—棻基 本紙張尺度適用中國國家標準(CMS ) A4規格(210X297公釐) A7 B7 五、發明説明(4 ) 芳 基, 比 如 苯 基, 某基,C H 3 • C Η 3 C 6 H 4 -, ( C Η 3 ) 3 c eH 4-; 芳 基-C I -C i 8 -烷基,比 如 — C H 2 C 6 H 5 » 一 C 2Η 4 c eH 5 ; 鹵 素, 比 如 — F, —C 又,—B 胺 基 ( — N H 2) I 羥 基 ( 一 0 H ) ) 羧 基 ( — c 0 0 H ), 硝 基 ( ""'丨 .N 〇 2) ,以及 氫 ( —- H )° 特別適宜者爲帶有一個或以上線型或有分枝的C = -C18-烷基,較宜爲<:1一〇6-烷基'的伸芳基單元。 聚芳醚爲包含至少一個如化學式(1)之單元的寡聚 物或聚合物: r装 訂 球 · - - (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 \7 I Ο %1/ A4 rL I 1 TJ %/ X I k ΛΙ/ rL 1 .TJ TJ T I ♦1 \»y A2 單T 11.基, A 芳橋 中伸架 其述氧 , 上是 成似 ◦ 構類, 所爲元 別 單 I 分基 (, 芳 式同伸 學不的 化或代 的同取 上相被 以可未 個A4^ 兩 α 代 由Γ取 或 Α 經Printed and printed by the Central Standard Falcon Bureau Employee Consumer Cooperative of the Ministry of Economic Affairs A7 _______B7 _ V. Description of the invention (1) The present invention and the filter material, filter membrane and gas or liquid containing polyaryl ether for removing ozone from gas and liquid (..Polyarylene ether) is related to the method of contacting the filter material. It is known that there will be a small amount of ozone in the process of electrophotography, photocopying and printing. The equipment used, such as photocopiers or laser printers, continuously emits the generated ozone into the surrounding atmosphere. Ozone is a pollutant in terms of taste. At the same time, even a small concentration can have a harmful effect on health. To remedy this, many methods have been developed to remove ozone from the air stream released by such equipment. In these methods, ozone is either destroyed or combined chemically or physically. It is known that ozone can be destroyed by heating or acting with a metal catalyst (see JP-60 1 9 7 223 and JP — 60 19 115). However, the disadvantages of ozone thermal destruction are energy consumption and the high temperature required to complete the decomposition of ozone. In addition, it is also known that a gas stream flows through a filter to decompose ozone in a catalytic manner (see JP — 58 0 8 1 425). Impregnate the basic material of the filter membrane with one or more metal compounds, metals or alloys such as iron compounds' manganese compounds or nickel compounds, and additionally add compounds or metals including noble metals such as palladium or platinum to In the membrane. These catalysts are very expensive and usually only have a limited service life because the heterogeneous catalysts are quickly deactivated by various catalyst poisons. In addition, a filter membrane containing carrier materials such as alumina or activated carbon is also known. It is infiltrated with ethylenic unsaturated compounds that can interact with ozone on a paper scale. It is applicable to the Chinese National Standard (CNS) A4 specification (2丨 0x297 Gongqing)--ml d ^ t • * I (please read the precautions on the back before filling in this page) -4-Annex A: Amendment Page of Chinese Specification of Patent Application No. 841〇9238 ^ 04887 Amend Republic of China In May, 1985, 8a5.2i 4 was amended and the description of the invention (2) started (see DE 37 28 802). The disadvantage of this compound, such as terpene, is that in many cases it is volatile depending on the carrier material used, so it is taken away in a small form and is lost. Also, only a small part of the filter weight can be used as the active ingredient. In addition, it is known that in a filter membrane composed of fiber flat plates for decomposing ozone, the fibers contain a catalyst for decomposing ozone (see J P_0 3 270 718). The fibers that are porous in the preferred system are composed of polymers with the following functional groups that can react violently with ozone: such as a SH, = S, a 1 ^ only 2, =? ^ 11, _ € 1 ^ And -OH. The ozone decomposition catalyst mentioned is composed of metals like gold, silver, copper, palladium, iron, nickel, cobalt and manganese, or their oxides, and alumina and diatomaceous earth. The fibers required to manufacture the filter membrane are obtained by the traditional spinning method, which distributes the catalyst in the spinning solution and distributes them evenly in the fibers after spinning. The second polymer is added, and the phase separation is initiated together with the first polymer, and the spinning product is subjected to various treatments, so that porous materials containing catalyst particles can be obtained. The resulting fibers are then manufactured by conventional methods to make filter membranes. Polymers deemed appropriate are only mentioned collectively. Only (please read the note Ϋ on the back before filling in this page) The Peking Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs is printed and divided by the oxygen charge used for the filtration. The smell will be moved in the oxygen supply and the smelly body will be produced. The liquid body will be neutralized and the liquid membrane will be filtered and removed. In terms of, use external parties in qi. This is the same as ether I. This standard membrane is used for the addition and removal of the seed filter, and there is an external nitrile material for the addition of vinyl. The original material of the hair filter bag is returned to the market. The oxygen hair filter has been sold. The oxygen is odorous. The book is often removed, and the non-moving material is used. The paper standard uses the Chinese national rubbing rate (CNS) A4 specification (2 丨Ο X 4 7 mm) _ 5-A7 B7 5. Description of the invention (3) The filter membrane to be removed contains a filter material containing polyaryl ether. The present invention also provides a method for removing ozone from gases and liquids, which uses a filter material containing polyarylene ether 'and brings the gas or liquid into contact with the surface of the filter material. Polyarylene ether is a species containing at least one aryl ether unit (one A — 0—, where A is arylene). Aryl group refers to an aryl unit having two bonding positions, such as a CeH4-. Mono- or polycyclic aromatic compounds can form aryl units, such as benzene, pyridine, phenanthrene, phenanthrene and anthracene. It is more preferably a substituted arylene unit. The substituents on the arylene group may be: C 1-C 18 group such as a c Η C 2Η 2 η 5 -C3H7, ~ C4H9, -C5Hai, -C (CH 3) 3, -ch2-ch (ch3) 2; C i-cie hydroxy-alkyl, such as -CH 3 " 〇H, -C2H4〇H. -C3H6OH--ch2-ch (ch3) 2- (please read the precautions on the back before filling in this page) i -Finishing and ordering the Infinite C 1— C 18 —Yuanoxy aryloxy C Η 2 Ο Η of the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy; for example —〇ch3, —〇c2h5 -OC3H7,-0 c 4H 9 -0〇5ΗΧ1, _qCHz_ CH (CH 3) 2, -0C2H4-Ch (ch 3) 2, such as an OCeH5, 2_ oxy-棻 basic paper scale applicable to the Chinese National Standard (CMS) A4 specification (210X297 mm) A7 B7 5. Description of the invention (4) Aryl, such as phenyl, certain group, CH 3 • C Η 3 C 6 H 4-, (C Η 3) 3 c eH 4-; aryl-CI -C i 8 -Alkyl, such as — CH 2 C 6 H 5 »a C 2Η 4 c eH 5; halogen, such as — F, —C and, —B amine (— NH 2) I hydroxy (-0 H)) carboxyl ( — C 0 0 H), nitro (" " '丨 .N 〇2), and hydrogen (--H) ° Particularly suitable for those with one or more linear or branched C = -C18-alkyl, more preferably <: 1_〇6-alkyl ' Extend aryl unit. Polyarylene ether is an oligomer or polymer containing at least one unit of formula (1): r Binding balls ·--(Please read the precautions on the back before filling this page) Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs Printed \ 7 I Ο% 1 / A4 rL I 1 TJ% / XI k ΛΙ / rL 1 .TJ TJ TI ♦ 1 \ »y A2 Single T 11. Base, A Fang bridge stretched out its oxygen, the above is It is similar to the construction class, the elementary unit I is the base (the aromatic homology is not extended or the same phase of the generation is replaced by Γ or Α by the A4 ^ two α generations.

A 之和 A X 元 、A sum A X yuan,

白 I 選 ο 是 C 且 I 並, > I 同 ο 不 S 或 ί 同 ’ 相| 可 S Υ I οWhite I election ο is C and I is combined, > I is the same ο not S or ί the same phase | may S Υ I ο

ο Sο S

2 ο C 至 1X 在 數 碳 本紙張尺度適用中國國家標华(CNS ) A4坑格(2I0 X 297公釐) 7 .經濟部中央標準局員工消費合作社印製 A7 __________ 07___五、發明説明(5 ) 6的伸院基(alkylene)或次院基(alkylidene)的兩價 連結基團,以及n,m,i ,j ,k,1 ,〇和p可在彼 此無關下是0或整數1 ,2,3或4,其總和必須至少爲 2。 較佳的聚芳醚爲含有如化學式(I I )之重覆單元的 聚(2 ’ 6 ——甲基苯氧化物(phenyiene 〇xide)2 ο C to 1X apply to the China National Standard (CNS) A4 grid (2I0 X 297 mm) on the carbon paper scale 7. The A7 printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs __________ 07___ V. Description of invention ( 5) The bivalent linking group of alkylene or alkylidene of 6, and n, m, i, j, k, 1, 〇 and p can be 0 or integer 1 independently of each other , 2, 3 or 4, the sum of which must be at least 2. The preferred polyarylene ether is poly (2 '6 ---- methyl phenyl oxide (phenyiene oxide) containing repeating units of formula (I I)

其製備方法爲已知,或者是聚(2,6 -二甲基苯氧化物 )與多苯乙烯或聚醯胺的聚合物摻合物。 另外適用的聚芳醚包含至少一個如化學式(I I I ) 的單元或由兩個以上的化學式(I Γ I )的單元所構成The preparation method is known, or it is a polymer blend of poly (2,6-dimethylphenyl oxide) and polystyrene or polyamide. Further suitable polyarylene ethers contain at least one unit of formula (I I I) or consist of more than two units of formula (I Γ I)

其中 X和y 分別爲0至包括1的數字範圍,X和y的總和 必須爲1 ,以及 尺1’尺2,尺3和114 爲上述伸芳基的取代基,並且可以 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) " -8 - I I —I I 11 - 1- - - ” ^in i ---I , HI. . . (請先閱讀背面之注意事項再填寫本頁) 304887 A7 _______B7__ 五、發明説明(6 ) 相同或不同。R : .,R 2,R 3和R 4較宜爲 Ci_ C18 —院基,尤其是(31- C6_院基。 ~個聚芳醚可包含兩個或以上的不同化學式(I I I )單元。 合適的聚芳醚通常是那些平均分子量Μ ~在1 0 0 0 至2,〇〇〇,〇〇〇g /莫耳,較宜在10,〇〇〇至 5(30,〇〇〇g /莫耳和尤其是在20 ,000至 2〇〇〇,〇〇〇g/莫耳,之間者》 聚芳醚也可與一個或以上的其他聚合物摻合在一起。 聚芳醚也可以是團塊共聚物》 依據本發明,含有至少一個聚芳酸的摻合物可用來將 臭氧自氣體和液體中移除掉》適合的摻合物例子爲聚芳醚 摻合物,它包含多苯乙烯均聚物和/或多苯乙烯共聚物/ 或聚醯胺和/或聚烯烴。 聚芳醚的例子及其製備有條列在” U 1 1 mann工業化學 百科全書 〃 (Ullmann’s Encyclopedia of Industrial Chemistry),第 5 版,第 A 2 1 卷,B. Elbers (編輯) ’ VCH,Weinheim-Basel,劍橋-紐約,1 9 9 2,入門篇 (entry )"聚(苯氧化物)^,第6 0 5 — 6 1 4頁中 ,在此將其納入參考資料。 聚芳醚及聚芳醚摻合物在底下將稱作聚合物。 聚合物可以粉末,顆粒,纖維,不織布,織物,薄膜 和/或塑形物件等形式來使用。粉末擁有市售的傳統粒徑 ,同時也有可能使用顆粒。就此而言有一點很重要,就是 本紙張尺度逋用中國國家標準(CNS ) A4規格(210X297公釐)Where X and y are in the range of 0 to 1 respectively, the sum of X and y must be 1, and ruler 1 ', ruler 2, ruler 3 and 114 are the substituents of the above arylene group, and can be applied to China on this paper scale National Standard (CNS) A4 Specification (210X297mm) " -8-II —II 11-1---”^ in i --- I, HI ... (please read the precautions on the back before filling in this Page) 304887 A7 _______B7__ Fifth, the invention description (6) is the same or different. R:., R 2, R 3 and R 4 are more preferably Ci_C18-courtyard, especially (31-C6_ courtyard. ~ A poly Aromatic ethers may contain two or more units of different chemical formula (III). Suitable polyarylene ethers are generally those with an average molecular weight M ~ from 1,000 to 2,000, 0.000 g / mole, preferably Between 10,000 and 5,000 (30,000 and 2,000 g / mole and especially between 20,000 and 2,000 and 10,000 g / mole, polyarylene ether can also be used with a Or other polymers blended together. Polyarylene ethers can also be agglomerate copolymers. According to the present invention, a blend containing at least one polyaromatic acid can be used to separate ozone from gas and liquid Examples of suitable blends are polyaryl ether blends, which include polystyrene homopolymers and / or polystyrene copolymers / or polyamides and / or polyolefins. Examples and preparations are listed in the "U 1 1 mann Encyclopedia of Industrial Chemistry" (Ullmann's Encyclopedia of Industrial Chemistry), 5th Edition, Volume A 21, B. Elbers (Editor) 'VCH, Weinheim-Basel, Cambridge-New York, 1 9 9 2, entry (entry) " poly (phenylene oxide) ^, pages 6 0 5 — 6 1 4 and it is included here as reference material. Polyarylene ethers and polyarylene ethers The blend will be referred to as a polymer underneath. Polymers can be used in the form of powders, granules, fibers, non-woven fabrics, fabrics, films, and / or shaped objects. Powders have a conventional particle size that is commercially available, and it is also possible . In this regard, it is very important that this paper standard uses the Chinese National Standard (CNS) A4 specification (210X297 mm)

In. ϋ^— HI ^^1 · 士穴 I i — In ml 1 ---- TJ. 03-e • - -- (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 經濟部中央標準局負工消費合作社印裝 A7 _ B7 五、發明説明(7 ) 所要處理的液體或氣體要能在不受千擾下流經粉末,比如 固定床形式者。如果聚合物被用作纖維時,這些纖維是以 短纖維,針狀布(needlefelt),不織布材料,針薄布( card sliver)或織物來應用。薄膜或薄膜屑(scrap)也 可以適當形式來使用。 通常聚合物也可以未經摻雜的材料來應用。然而,也 有可能加入填粒-比如白堊,滑石,陶土或雲母,和/或 纖維狀補強劑-比如玻璃纖維和碳纖維,晶須(wh i Sker )及另外的添加物及處理助劑一比如潤滑劑,釋出劑,抗 氧化劑和U V安定劑。 對聚合物載體材料進行塗覆可藉著將聚合物溶液(溶 劑例子爲甲苯及氯仿)塗敷到載體材料上。要進行浸漬可 使有吸收能力的載體材料飽和。所用載體材料通常是無機 物質-比如玻璃,矽膠,鋁氧化物,·砂,陶瓷組成物,金 屬及有機物-比如塑膠。 也有可能將金屬,尤其是貴金屬和過渡金屬,或金屬 氧化物-比如過渡金屬氧化物,塗敷到聚合物物質上。金 屬或金屬氧化物可以浸漬法來塗敷到聚合物上,然後以小 的金屬叢(cluster)形式存在。 本發明方法可在低於所用聚合物之軟化點的任何溫度 下進行。一般來講,所用溫度是在_1 0和80 °C,較宜 在0和5 0 °C,之間。 臭氧的移除通常是定量的,在眾多因素中,反應時間 端視所要純化之氣體或液體的接觸時間或流速,聚合物之 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X 297公釐) I i I — .裝 訂— 冰 * · I * (請先閱讀背面之注意事項再填寫本頁) 504887 A7 B7 年 月85· 5. 2 i 五、發明説明(8 ) 表面積,濾膜裝置之幾何形狀和溫度而定。聚芳醚與要被 純化媒質的接觸時間一般是在0. 001秒和10分鐘, 較宜在0.01秒和5分鐘,以及尤其適宜在0.5至1分鐘,之 間。然而,這些時間可加以縮短或延長。聚合物比表面稹 的大小對聚合物的濾膜作用會有明顯的影響。一般而言, 聚合物的濾膜作用越大,則聚合物比表面積也就越大。聚 合物有大的比面積和多孔結構,再加上經證明有利之相配 的微孔(micropore)及大孔(macropore)比値,則對滤 膜的效率將特別有利。聚合物的濾膜效率也會分別受到結 晶度和聚合物無定形部份大小的影響。聚合物有高的無定 形部份時,通常對聚合物的濾膜活性會有良好的效果。 具有大表面稹的聚芳醚,比如粉末,纖維或隔膜,的 製備可參見1 9 9 4年1 1月8日提出之德國申請案檔案 參考號碼P 44 39 478. 0,題名爲’用於將 成份自氣體及液體中移除之以聚合物爲主的濾材'中的說 明,在此將其納入參考資料。 經濟部中央標準局負工消費合作社印製 (請先聞讀背面之注意事項再填寫本頁) 本發明的濾膜及濾材可用在所有含臭氧的氣體氣流和 液體中。於是它們可被用來移除減菌時所用或影印機裝置 所產生的臭氧,並且也可用於液體中臭氧的移除及解毒作 用0 附圖之簡沭: 圇1係示依本發明之方法自水中將臭氧移除的製程圖° 實施例 實施例中所需用作起始物的臭氧是從有純氧供應的市· 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐)_ 3〇4887 A7 B7 五、發明説明(9 ) 售臭氧產生器中產生。使用以UV分光儀爲主的H〇riba( Industriestr.8,D-61449 Steinbach) A P 0 A 350 E量測裝置來讀臭氧濃度。然後以空氣或氬氣來將臭氧/ 氧氣混合物稀釋到特定的濃度。由於已知臭氧在水中及在 潮濕氣體中會緩慢分解,所以使用乾燥氣體來進行稀釋。 稀釋後,將氣體氣流分成幾部份。使其中一部份流經一個 空管,同時使另一部份流經充滿有濾材的相對應垂直管子 。爲使它能容納聚合物,在玻璃管底部以多孔玻璃平板( 玻璃料)密封起來。使流速規則以便每個單位時間內有相 等的容積流經這兩根管子》 實施例1 將購自Aldrich之各個不同數量的聚〔2 ,6 —二甲 基-對—苯氧化物〕(Tg211°C,Tm268 °C,鬆 散密度0 . 4 7 g/cm3)充填進直徑約爲2 5mm且 經濟部中央橾準局員工消费合作社印製 (請先閲讀背面之注意事項再填寫本頁) 在底部有以玻璃料密封的玻璃管中》使含臭氧的氣體氣流 流經該粉末床。依序設定流速及臭氧濃度。在依照表中各 個情形.所指示的整個期間進行量測。 表1 容積流量(1/小時) 時間(小時) 樣品軍暈(克) 臭氧濃度 流經濾膜後的臭氧 濃度(mg/m3) 50 2 10.7 10,500 _ 1) 40 0.33 10 40000 - 120 24 1.9 0.66 - 120 3.5 3.5 0.66 - 1) 未偵測到 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0 X 297公釐) -12 - 經濟部中央標準局負工消費合作社印製 A7 B7 五、發明説明(10) 實施例2 9 0°C下使15克的聚(2 ,6 -二甲基苯氧化物) ,商品S®Blendex HPP 820,溶解於8 5克的N —甲基 吡咯烷酮(Ν Μ P )中。使用刮刀將部份的該溶液塗抹到 玻璃平板上來形成濕潤厚度約爲2 0 0微米的薄膜(玻璃 平板及括刀都預先有加熱到7 0 °C)。將該經塗抹的濕潤 薄膜浸漬在4 5 °C的水中,2分鐘後使所得隔膜與玻璃平 板分隔開來,並放置在水中2 4小時以便移除殘餘的溶劑 。然後使隔膜在空氣中乾燥》將直徑2公分的圓形部分夾 住固定在隔膜測試小盒(cell)中,並使含有1 0 0 p p b臭氧的空氣氣流流經過去。在隔膜中的平均滯留時 間只有2m s。對流經隔膜的空氣氣流分析其臭氧含量( 使用 Rhode & Schwarz的臭氧量測儀ML 9810)。 吾人發現臭氧濃度低於1 p p b的可偵測下限。即令在2 小時後,臭氧的濃度仍低於1 p P b'這顯示在小於1微 秒的滯留時間下即可將臭氧完全去除掉。 實施例3 重覆實施例2的實驗,但改以購自通用電氣( General Electric) ,USA 的聚合物慘合*®N〇ry ( 它是由P P 0及多苯乙烯的均質摻合物所構成)來取代 Blendex。可獲得和實施例1 一樣的結果,表示在超過2 小時的測試期間和2 m s的帶留時間下可將臭氧完全移除 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) _^ϋ I I - I -1 I - - I <士良 - In IK n 0¾ 、v'e , · · (請先閲讀背面之注意事項再填寫本頁) 13 - 經濟部中央標準局貝工消費合作社印製 A7 _;_ B7 五、發明説明(11) . 實施例4 使8 0克的N -甲基吡咯烷酮和2 0克的多苯氧化物 混合以生成一個在溫度超過7 0°C下仍保持均質的成形溶 液。使溶液過濾,加熱在8 0°C和然後經由紡絲管路( 9 0°C)輸送到濕式紡絲的紡絲頭(8 0°C)。紡絲頭具 有1 0 0個直徑爲0 · 2 m m的孔洞。在紡絲當中.,將紡 絲頭浸漬在3 5 °C的沉澱水浴中。在沉澱浴中的沉澱部份 爲7 5公分長。在流經一系列的沖洗浴後,纖維會濕潤纏 繞起來。 該方法的一個變化是纖.維紙漿的製造,它是在凝結後 (於室溫水中),直接機械粉碎獲得。以水對以這種方式 製造的紙漿進行幾天的處理,然後在5 0°C下乾燥》 實施例5 ' 使用多孔P P 〇濾膜或濾膜紙漿來由氣體氣流中將臭氧移 除 將濾材放在長3 0公分和內徑2 _ 3公分的玻璃管中 。然後室溫下使含有臭氧的氣體流玻璃管路。使用 Fischer臭氧分析儀(機型®〇zotron 23)來量測玻璃管 路上游及下游的臭氧濃度。結果整理在底下的表2中。 ^^1 ^^1 1. -I - 1^1 m —1 - - - •士i— 1^1 1 I HI ^^1 U3. ··· (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨〇 X 297公釐) 14 - 304887 五、發明説明(12) A7 B7 表2 聚合物材料 多苯氧化物fBlendex HPP 820) 多苯氧化物(®Blendex HPP 820) 形態 纖維紙漿(厚度5〇μπι) 纖維紙漿(厚度200μιη) 比表面桢[m2/g] 300 400 樣品 [g] 6.2 3.1 鬆散面楨: 100 cm3 30 cm3 載體氣體 氧氣 氧氣 相對濕度[%] 0 0 載體氣體容積流量[l/h] 100 100 臭氧濃度一入口處[mg/m3] 10,000 10,000 臭氧濃度一實驗結承後出 口處[mg/m3] 3.25 1 測試持續期間[h] 3.25 1 臭氧吸收率(自身重量%) 52% 32% (請先Μ讀背面之注意事項再填寫本筲) 實施例6 . 將P P 0粉末加入已預先加熱至9 0°c的MMP ( 1 dm3)溶液中,並使用高速攪拌器來使溶解。將聚合物 濃度調整在5至2 0%,較宜爲1 5%。所用 Blendex Η PP 8 20型多苯氧化物粉末具有〇 - 2至0. 5 mm的粒 徑和1. lm2/g的比表面積。 將均質聚合物溶液放在經加熱的滴液漏斗中,並調整 其溫度爲8 0°C。然後將溶液逐滴加入其溫度調整在4 0 至8 0 °C之間和用作沉澱浴的有攪拌的水浴中。另一種選 擇則是,也有可能使用經加熱的噴嘴頭以便將液滴加進沉 澱浴中。藉著適當選擇滴液噴嘴,滴落速率和沉澱浴中的 攪拌速度下,則有可能變化球液的形態及大小。 當液滴撞擊沉澱浴時,聚合物溶液的液滴會以球形凝 固。藉著持續加入新配製經加熱的水,則懸浮的圓球會連 Γ 經濟部中央標準局員工消費合作社印装 I張 -紙 本 導 標 家 國 I國 中 一用 ;適 I釐 公 A7 五、發明説明(13) 同所用沉澱浴溶液(水/ Ν Μ P )由沉澱浴中溢流出來。 沉澱浴中圓球的滯留時間在5和2 0分鐘之間。 反覆以水沖洗後,於9 0°C的真空乾燥烘箱(2 0 0 毫巴)中進行數小時的乾燥,如此可得耐磨損之比表面積 至少爲50rri/g(BET量測法)的PPO顆粒,它還 具有作爲臭氧濾膜的優異性質。 實施例7 將實施例6的濾材放在長30公分和內徑2. 3公分 的玻璃管中。然後室溫下使含有臭氧的氣體流經玻璃管路 。使用Fischer臭氧分析筚(機型®0zotron 23)來量 測玻璃管路上游及下游的臭氧濃度。結果整理在底下的表 3中。 (請先閲讀背面之注意事項再填寫本頁) -裝· 經濟部中央樣準局員工消費合作社印袈 表3 聚合物材料 多苯氧化物C®Blendex HPP 820) 多苯氧化物(®Blendex HPP 820) 形態 顆粒(粒徑1.5 - 2.5 mm) 顆粒(粒徑[5 - 2.5 mm) 比表面積[nWg] 87 40 樣品重量[g] 6.2 6.2 鬆散面積: 28 cm3 29 cm3. 載體氣體 氧氣 氧氣 相對濕度[%] 0 0 載體氣體容積流量[1/h] 100 100 臭氧濃度一入口處[mg/m3] 10,000 10,000 臭氧濃度一實驗結束後出 口處[mg/m3] 0.0 0.0 測試持績期間[h] 2.1 1.8 臭氧吸收率(自身歡量%) 34% 29% 本紙張尺度適用中國國家標準(CNS > A4規格(2丨0X297公釐) S04887 A7 B7 五、發明説明() 實施例8和9 使用P P 0顆粒來自水中移除溶解的臭氧· 實驗步驟 使用粒徑在1.5至2. 5mm的PPO顆粒,並依 據實施例6的相逆轉(phase inversion)方法來製備。 •另外,以機械方式使顆粒進行預粉碎,密集地以丙醇 及水來沖洗和接著在1 0 0°C的乾燥烘箱中進行8小時的 乾燥。經粉碎材料的平均徑粒爲1 mm,以及其鬆散密度 爲 0. 2 至 0. 25g/cm3。 爲使用於液相中,則將經乾燥的疏水性P P 0材料放 在玻璃吸附管中(內徑2. 3cm,長20cm),並以 水/乙醇混合物來使飽和以便濕潤孔洞。然後以馬達經由 吸附濾膜將水打進來以使殘餘的乙醇分布開來。 對充填有1 . 5升飮用水的泡狀'管柱通以含臭氧的氧 經濟部中央橾準局員工消費合作社印製 f^i^l· ^^^^1 a t—^1 nn nn 、ve - -(請先閱讀背面之注意事項再填寫本頁) 氣(2 0克的03/m3)。使用齒輪泵將加有臭氧的飮用 水持續抽出來使經由吸附濾膜然後流回泡狀管柱(參見圖 1)。以氧化還原電位的非直接方式分析在吸附小盒前後 的臭氧濃度。測試結果整理在底下的表4中。 本紙张尺度適用中國國家標準(CNS > A4说格(210X297公釐) 17 - 經濟部中央標隼局員工消費合作社印製 A7 B7 五、發明説明(15) 表4 實施例 8 9 材料 多苯氧化物(PPO) 多苯氧化物(PPO: 形態 顆粒 顆粒 平均粒徑[μηι] 1000 1000 樣品重量[g] 5.9 10 濾膜容積[cm3] 25 42 濾膜長度[cm] 6 10 濾膜橫截面[cm2] 2:3 2.3 液體 飮用水(加有臭氧) 飮用水咖有臭氧) 雜流量(液體)[升/小時] 20 40 滞留時間(液體)[秒] 4.5 3.8 載體氣體 氧氣 氧氣 氧濃度(在載體氣體中)[g/m3] 20.0 20.0 源電位[Mv](未加有臭氧的飮 用水) 200 210 1原電位[Mv](流經濾膜之前加 有臭氧的飮用水) 820 (估計有4 mg/升 的〇3) 860 (估計有4 mg/ 升的〇3) 1原電位[Mv](流經濾膜之後加 有臭氧的飮用水) 1小時測試期間 2小時測試期間 4小時測試期間 6小時測試期間 270 (< 0_3 mg/升的 03) 250 (< 0.3 mg/升的 03) 230 (< 0.3 mg/升的 03) 300 (< 0.5 mg/升的 03) 230 (< 0.2 mg/升的 〇3) 220 (< 0.2 mg/升的 03) 210 (<0.2 mg/升 的〇3) 全部測試期間[小時] 6 ---------.裝— - · (請先閱讀背面之注意事項再填寫本頁) 本紙浪尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 18 -In. Ϋ ^ — HI ^^ 1 · Shixue I i — In ml 1 ---- TJ. 03-e •--(please read the precautions on the back before filling out this page) Employees of Central Bureau of Standards, Ministry of Economic Affairs Consumer cooperatives print A7 _ B7 printed by the Ministry of Economic Affairs, Central Bureau of Standards, Consumer Cooperatives V. Invention description (7) The liquid or gas to be processed must be able to flow through the powder without being disturbed, such as in the form of a fixed bed. If polymers are used as fibers, these fibers are applied as staple fibers, needlefelt, non-woven materials, card slivers or fabrics. Films or film scraps can also be used in appropriate forms. Generally polymers can also be applied with undoped materials. However, it is also possible to add fillers-such as chalk, talc, clay or mica, and / or fibrous reinforcements-such as glass fibers and carbon fibers, whiskers (wh i Sker) and other additives and processing aids such as lubrication Agent, release agent, antioxidant and UV stabilizer. The polymer carrier material can be coated by applying a polymer solution (solvent examples are toluene and chloroform) to the carrier material. Impregnation can saturate the absorbent carrier material. The carrier materials used are usually inorganic substances-such as glass, silicone, aluminum oxide, sand, ceramic compositions, metals and organics-such as plastics. It is also possible to apply metals, especially precious metals and transition metals, or metal oxides, such as transition metal oxides, to the polymer substance. The metal or metal oxide can be applied to the polymer by dipping, and then exists in the form of small metal clusters. The process of the invention can be carried out at any temperature below the softening point of the polymer used. Generally speaking, the temperature used is between 0 and 80 ° C, preferably between 0 and 50 ° C. The removal of ozone is usually quantitative. Among many factors, the reaction time depends on the contact time or flow rate of the gas or liquid to be purified. The original paper scale of the polymer is applicable to the Chinese National Standard (CNS) A4 specification (210 X 297 ) I i I — .Binding — ice * · I * (please read the precautions on the back before filling this page) 504887 A7 B7 year month 85 · 5. 2 i V. Invention description (8) Surface area, membrane device Depending on the geometry and temperature. The contact time of the polyarylene ether with the medium to be purified is generally between 0.001 seconds and 10 minutes, more preferably between 0.01 seconds and 5 minutes, and particularly preferably between 0.5 and 1 minute. However, these times can be shortened or extended. The size of the polymer specific surface hull will have a significant effect on the polymer's membrane function. Generally speaking, the greater the filter function of the polymer, the greater the specific surface area of the polymer. Polymers with a large specific area and porous structure, coupled with a proven micropore (micropore) and macropore (macropore) ratio, will be particularly beneficial to the efficiency of the membrane. The efficiency of the polymer membrane is also affected by the crystallinity and the size of the amorphous part of the polymer, respectively. When the polymer has high amorphous parts, it usually has a good effect on the membrane activity of the polymer. For the preparation of polyarylene ethers with large surface grains, such as powders, fibers, or separators, please refer to the German application file reference number P 44 39 478. 0, titled 'for The description of polymer-based filter media that removes components from gases and liquids is included here as reference material. Printed by the Consumer Labor Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) The filter membrane and filter material of the present invention can be used in all gas streams and liquids containing ozone. So they can be used to remove ozone used in sterilization or photocopier equipment, and can also be used for the removal and detoxification of ozone in liquids. 0 BRIEF DESCRIPTION OF THE DRAWINGS: 囵 1 shows the method according to the invention Process diagram for removing ozone from water ° Examples The ozone used as a starting material in the examples is from a city with pure oxygen supply. This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X 297 mm ) _ 3〇4887 A7 B7 V. Description of the invention (9) Produced in the sale of ozone generator. The ozone concentration was read using a Horiba (Industrytr. 8, D-61449 Steinbach) A P 0 A 350 E measuring device mainly based on a UV spectrometer. The ozone / oxygen mixture is then diluted to a specific concentration with air or argon. Since ozone is known to decompose slowly in water and in humid gases, dry gas is used for dilution. After dilution, the gas flow is divided into several parts. Let one of them flow through an empty tube, while the other part flows through the corresponding vertical tube filled with filter material. In order to allow it to contain polymers, the bottom of the glass tube is sealed with a porous glass plate (frit). Make the flow rate regular so that each unit of time has an equal volume flowing through the two tubes "Example 1 Each different amount of poly [2,6-dimethyl-p-phenyloxide] purchased from Aldrich ( Tg211 ° C, Tm268 ° C, bulk density 0.47 g / cm3) Filled with a diameter of about 25 mm and printed by the Consumer Cooperative of the Central Central Bureau of Economics of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) In a glass tube sealed with frit at the bottom, a gas stream containing ozone flows through the powder bed. Set the flow rate and ozone concentration in sequence. Measure in the entire period indicated in the table according to the circumstances. Table 1 Volume flow rate (1 / hour) Time (hour) Sample military halo (gram) Ozone concentration Ozone concentration after flowing through the filter (mg / m3) 50 2 10.7 10,500 _ 1) 40 0.33 10 40000-120 24 1.9 0.66 -120 3.5 3.5 0.66-1) The paper standard is not detected. The Chinese National Standard (CNS) A4 specifications (2 丨 0 X 297 mm) -12-Printed by the Ministry of Economic Affairs Bureau of Central Standards A7 B7 Five 3. Description of the invention (10) Example 2 15 g of poly (2,6-dimethylphenyl oxide), commercial product S®Blendex HPP 820, was dissolved in 85 g of N-methylpyrrolidone at 90 ° C (Ν Μ P). Use a spatula to apply part of this solution to a glass plate to form a film with a wet thickness of about 200 microns (both the glass plate and the knife are heated to 70 ° C in advance). The coated wet film was immersed in water at 45 ° C. After 2 minutes, the resulting membrane was separated from the glass plate and placed in water for 24 hours to remove residual solvent. Then, the diaphragm was dried in the air >> The circular part with a diameter of 2 cm was clamped and fixed in a diaphragm test cell, and an air stream containing 100 p p b ozone was passed therethrough. The average residence time in the diaphragm is only 2m s. The air flow through the diaphragm was analyzed for ozone content (using Rhode & Schwarz's ozone meter ML 9810). I found that the ozone concentration is below the detectable lower limit of 1 p p b. Even after 2 hours, the ozone concentration is still below 1 p P b ', which shows that ozone can be completely removed in a residence time of less than 1 microsecond. Example 3 The experiment of Example 2 was repeated, but the polymer was purchased from General Electric (USA) * ®Norry (which is a homogeneous blend of PP 0 and polystyrene) Composition) to replace Blendex. The same results as in Example 1 can be obtained, indicating that ozone can be completely removed during the test period of more than 2 hours and with a residence time of 2 ms. This paper scale applies the Chinese National Standard (CNS) A4 specification (210X297 mm) _ ^ ϋ II-I -1 I--I < Shiliang-In IK n 0¾, v'e, · (please read the precautions on the back before filling in this page) 13-Bei Gong Consumption of the Central Standards Bureau of the Ministry of Economic Affairs A7 _; _ B7 printed by the cooperative. V. Description of the invention (11). Example 4 80 g of N-methylpyrrolidone and 20 g of polyphenyl oxide are mixed to produce a product at a temperature exceeding 70 ° C The forming solution remains homogeneous. The solution was filtered, heated at 80 ° C and then transported to the spinning head (80 ° C) of the wet spinning via a spinning line (90 ° C). The spinning head has 100 holes with a diameter of 0 · 2 mm. During spinning, immerse the spinning head in a precipitation water bath at 35 ° C. The precipitation part in the precipitation bath is 75 cm long. After flowing through a series of showers, the fibers are wet and entangled. A variation of this method is the manufacture of fiber-dimensional pulp, which is obtained by direct mechanical crushing after coagulation (in room temperature water). The pulp produced in this way was treated with water for several days and then dried at 50 ° C. Example 5 'Using a porous PP 〇 filter membrane or filter membrane pulp to remove ozone from the gas stream to remove the filter material Placed in a glass tube with a length of 30 cm and an inner diameter of 2_3 cm. Then the ozone-containing gas is allowed to flow into the glass tube at room temperature. Use the Fischer ozone analyzer (model ® 〇zotron 23) to measure the ozone concentration upstream and downstream of the glass pipe. The results are summarized in Table 2 below. ^^ 1 ^^ 1 1. -I-1 ^ 1 m —1---• Taxi— 1 ^ 1 1 I HI ^^ 1 U3. (Please read the precautions on the back before filling this page ) This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (2 丨 X 297 mm) 14-304887 V. Description of the invention (12) A7 B7 Table 2 Polymer material polyphenyl oxide fBlendex HPP 820) Polybenzene oxidation (®Blendex HPP 820) Morphological fiber pulp (thickness 50 μm) Fiber pulp (thickness 200 μm) Specific surface frame [m2 / g] 300 400 Sample [g] 6.2 3.1 Loose surface frame: 100 cm3 30 cm3 Carrier gas oxygen oxygen Relative humidity [%] 0 0 Carrier gas volume flow rate [l / h] 100 100 Ozone concentration at the inlet [mg / m3] 10,000 10,000 Ozone concentration at the outlet after the experiment is completed [mg / m3] 3.25 1 Test duration [ h] 3.25 1 Ozone absorption rate (self weight%) 52% 32% (please read the precautions on the back first and then fill in this note) Example 6. Add PP 0 powder to the MMP which has been pre-heated to 90 ° C ( 1 dm3) solution, and use a high-speed stirrer to dissolve. The polymer concentration is adjusted to 5 to 20%, preferably 15%. The Blendex H PP 8 20 type polyphenyl oxide powder used has a particle diameter of 0-2 to 0.5 mm and a specific surface area of 1.1 lm2 / g. Place the homogeneous polymer solution in a heated dropping funnel and adjust its temperature to 80 ° C. The solution was then added dropwise to a stirred water bath whose temperature was adjusted between 40 and 80 ° C and used as a precipitation bath. Another option is that it is also possible to use heated nozzle tips to add droplets to the precipitation bath. By properly selecting the drip nozzle, the drip rate and the stirring speed in the precipitation bath may change the shape and size of the bulb. When the droplet hits the precipitation bath, the droplet of the polymer solution solidifies in a spherical shape. By continuing to add freshly prepared heated water, the suspended ball will be printed with 1 sheet of the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs-a paper guide for the home country and the middle school; suitable for one centimeter A5. Description of the invention (13) The precipitation bath solution (water / NMP) used is overflowed from the precipitation bath. The residence time of the balls in the precipitation bath is between 5 and 20 minutes. After repeated washing with water, it is dried in a vacuum drying oven (200 mbar) at 90 ° C for several hours, so that the specific surface area of wear resistance is at least 50rri / g (BET measurement method) PPO particles, it also has excellent properties as an ozone filter. Example 7 The filter material of Example 6 was placed in a glass tube having a length of 30 cm and an inner diameter of 2.3 cm. Then at room temperature, the gas containing ozone flows through the glass tube. Use the Fischer Ozone Analyzer (Model 0zotron 23) to measure the ozone concentration upstream and downstream of the glass pipe. The results are summarized in Table 3 below. (Please read the precautions on the back before filling out this page)-Outfit · Central Sample Bureau of the Ministry of Economic Affairs Employee Consumer Cooperative Printed Table 3 Polymer Material Polyphenyl Oxide C®Blendex HPP 820) Polyphenyl Oxide (®Blendex HPP 820) Morphological particles (particle size 1.5-2.5 mm) Particles (particle size [5-2.5 mm) Specific surface area [nWg] 87 40 Sample weight [g] 6.2 6.2 Loose area: 28 cm3 29 cm3. Carrier gas oxygen oxygen relative humidity [%] 0 0 Carrier gas volume flow rate [1 / h] 100 100 Ozone concentration at the entrance [mg / m3] 10,000 10,000 Ozone concentration at the exit after the experiment [mg / m3] 0.0 0.0 Test performance period [h] 2.1 1.8 Ozone absorption rate (volume%) 34% 29% This paper scale is applicable to Chinese national standard (CNS & A4 specifications (2 丨 0X297mm) S04887 A7 B7 V. Description of invention () Examples 8 and 9 Use PP 0 particles come from water to remove dissolved ozone. The experimental procedure used PPO particles with a particle size of 1.5 to 2.5 mm and was prepared according to the phase inversion method of Example 6. • In addition, the particles were made mechanically Pre-crushing, intensively propanol and To rinse and then dry for 8 hours in a drying oven at 100 ° C. The average diameter of the crushed material is 1 mm, and its bulk density is 0.2 to 0.25 g / cm3. For use in liquid In the phase, the dried hydrophobic PP 0 material is placed in a glass adsorption tube (inner diameter 2.3 cm, length 20 cm), and saturated with a water / ethanol mixture to wet the pores. The motor is then passed through the adsorption filter Bring water in to distribute the residual ethanol. The bubble-shaped column filled with 1.5 liters of water is printed with ozone-containing oxygen. The Ministry of Economic Affairs, Central Bureau of Industry, and Consumer Cooperatives printed f ^ i ^ l · ^^^^ 1 at— ^ 1 nn nn, ve--(please read the precautions on the back before filling in this page) gas (20 g of 03 / m3). Use a gear pump to use ozone-added water Continue to draw out to pass through the adsorption filter and then flow back to the bubble column (see Figure 1). Analyze the ozone concentration before and after the adsorption box in an indirect way of the redox potential. The test results are summarized in Table 4 below. This paper The Zhang scale applies the Chinese national standard (CNS & A4) (210X297mm) 17-Ministry of Economic Affairs Printed by the Central Standard Falcon Bureau Employee Consumer Cooperative A7 B7 V. Description of the invention (15) Table 4 Example 8 9 Material Polyphenyl oxide (PPO) Polyphenyl oxide (PPO: morphological particle average particle size [μηι] 1000 1000 Sample weight [g] 5.9 10 Membrane volume [cm3] 25 42 Membrane length [cm] 6 10 Membrane cross-section [cm2] 2: 3 2.3 Liquid water for pontoon (with ozone added) Water for pontoon with ozone) Miscellaneous flow (Liquid) [liter / hour] 20 40 Residence time (liquid) [second] 4.5 3.8 Carrier gas oxygen Oxygen oxygen concentration (in carrier gas) [g / m3] 20.0 20.0 Source potential [Mv] (without ozone added) Biao water) 200 210 1 primary potential [Mv] (water with ozone added before flowing through the filter) 820 (estimated 4 mg / liter of 〇3) 860 (estimated 4 mg / liter of 〇3) 1 original Potential [Mv] (water with ozone added after flowing through the filter) 1 hour test period 2 hour test period 4 hour test period 6 hour test period 270 (< 0_3 mg / liter of 03) 250 (< 0.3 mg Per litre 03) 230 (< 0.3 mg / litre 03) 300 (< 0.5 mg / litre 03) 230 (< 0.2 mg / litre 03) 220 (< 0.2 mg / litre 03) 210 (< 0.2 mg / L of 〇3) All test periods [hours] 6 ---------. Packing--(Please read the precautions on the back before filling this page) Standards apply to China National Standard (CNS) A4 specifications (210X297mm) 18-

Claims (1)

304887 --—η 公告本 Α8 Β8 po D8 年犛 -9. 1 6 "WxLj 補言 、申請專利範圍 附件A : 1 .—種用 包含有聚芳醚, 的平均分子量爲 少一個式一 A — C C 6烷基取 2 .如申請 含如化學式(I 氧化物〕 第84109238號專利申請案 中文申請專利範圍修正本 民國85年9月修正 以自氣體與液雔中移除臭氧的濾材,該材 或聚芳醚與聚苯乙烯之摻和物,該聚芳醚 10,000至500, 000且包含至 Ο —所示之芳醚單元,其中A爲視需要經 代之單環的C6 — C12芳基。 專利範圍第1項的濾材,其中聚芳醚爲包 I )之重複單元的聚〔2,6 —二申基苯304887-η Bulletin Α8 Β8 po D8 Year Y-9. 1 6 " WxLj Supplement, Patent Application Scope Annex A: 1.-The species contains polyarylene ether, and the average molecular weight is one less than Formula One A — CC 6 alkyl is taken as 2. If the application contains the chemical formula (I oxide) Patent Application No. 84109238, the Chinese application patent scope amendment is amended in September 1985 to remove ozone from gas and liquid carbohydrate, the filter Material or a blend of polyarylene ether and polystyrene, the polyarylene ether is 10,000 to 500,000 and contains aryl ether units as shown in Ο-, where A is a monocyclic C6- C12 aryl group. The filter material of the first item in the patent scope, in which polyaryl ether is a poly [2,6-dishenylbenzene with a repeating unit of package I) (請先閲讀背面之注意Ϋ項再填寫本頁) If 3 .如申請專利範圍第1項的濾材,其中聚芳醚的平 均分子量Μ*在2 0 0 0至2,0 0 0 ,〇 〇 〇之間。 經濟部中央橾準局月工消費合作社印製 4 .—種用以自氣體及液體中移除臭_氧的濾膜,其中 該濾膜含有如申請專利範圍第1項的濾材。 5 .—種用以自氣體及液體中移除臭氧的方法,其包 含以含有聚芳醚或聚芳醚與聚苯乙烯之摻合物的濾材在 一 1 0至+8 0°C的溫度下處理含有臭氧的氣體及液體共 〇. 1秒至10分鐘,以及令該氣體或液體與濾材表面緊 密接觸,其中該聚芳醚的平均分子量爲1 〇 〇 ,〇 〇 〇至 本紙浪尺度適用中國國家揉準(CNS ) A4規格(210X297公釐) A8 B8 C8 D8(Please read the note Ϋ on the back first and then fill in this page) If 3. For the filter material of the first item of the patent application, the average molecular weight of the polyaryl ether M * is from 2 0 0 0 to 2, 0 0 0, 〇〇 Between 〇. Printed by the Yuegong Consumer Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs 4. A filter membrane for removing odor and oxygen from gases and liquids, where the filter membrane contains the filter material as specified in item 1 of the patent application. 5. A method for removing ozone from gas and liquid, which comprises using a filter material containing a polyarylene ether or a blend of polyarylene ether and polystyrene at a temperature of 10 to + 80 ° C The ozone-containing gas and liquid are processed for a total of 0.1 seconds to 10 minutes, and the gas or liquid is in close contact with the surface of the filter medium, wherein the average molecular weight of the polyarylene ether is 100, 000 to the original paper wave scale. China National Standard (CNS) A4 specification (210X297mm) A8 B8 C8 D8 六、+請專利範固 5 0 0,〇 〇 〇且包含至少一個式一 A - 0 —所示之聚芳 醚單元,其中,A爲視需要經Ci-C 6烷基所取代之單環 的c 6— c 12芳基。 6 .如申請專利範圍第5項的方法,其中濾材是以粉 未形式來使用。 7 .如申請專利範園第5項的方法,其中濾材是以織 維形式來使用。 8 ·如申請專利範圍第5項的方法,其中濾材是以薄 膜來使用。 9 .如申請專利範圍第5項的方法,其中濾材是以塑 形物件形式來使用。 (請先Η讀背面之注意事項再填寫本頁) 經濟部中央梯準局只工消费合作社印製 本紙張尺度逋用中國國家橾準(CNS)A4规格( 210x297公*) - 2 -Six, please patent Fan Gu 5,000, and contains at least one polyaryl ether unit represented by the formula A-0-, where A is a single ring substituted with Ci-C 6 alkyl as needed C 6- C 12 aryl. 6. The method as claimed in item 5 of the patent scope, in which the filter material is used in the form of powder. 7. The method as described in item 5 of the patent application park, in which the filter material is used in the form of texture. 8. The method as claimed in item 5 of the patent scope, in which the filter material is used as a thin film. 9. The method as claimed in item 5 of the patent application, in which the filter material is used in the form of plastic objects. (Please read the precautions on the back first and then fill out this page) Printed by the Ministry of Economic Affairs, Central Bureau of Standards and Commerce, Co-operative Consumer Cooperative. This paper is based on China National Standards (CNS) A4 (210x297) *-2-
TW084109238A 1994-08-15 1995-09-04 TW304887B (en)

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