TW210992B - - Google Patents

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TW210992B
TW210992B TW081104607A TW81104607A TW210992B TW 210992 B TW210992 B TW 210992B TW 081104607 A TW081104607 A TW 081104607A TW 81104607 A TW81104607 A TW 81104607A TW 210992 B TW210992 B TW 210992B
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Taiwan
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block copolymer
soil
block
copolymer
thermoplastic
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TW081104607A
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Chinese (zh)
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Micro Environmental 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/204Keeping clear the surface of open water from oil spills

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Λ (i 15 6 210992 五、發明説明() 本發明係有關從水體、土壤、水流、船腹、及諸如修 車廠與工廠地板、銷甲板及類似的固體表面回收有機液及 石油有關產品的技術,這些石油產品包括原油、及精煉石 油餾分物。 有許多處理石油有關污染物之溘出物的方法已被提出 。許多用做油溢出物吸收劑的材料也已被提出,這些材料 包括大量的稻草、黏土、矽土或板狀矽薄土(Kieselguhr) 顆粒。同時,也有人提出單獨使用諸如多孔聚苯乙烯顆粒 及多孔聚乙烯毛圃等之發泡聚合體材料,或和諸如固態無 機填料等之其他添加劑一起使用。 美國專利第3, 518, 183號揭示使用一痼大面積之單乙烯 基芳香族共軛二嫌塊狀共聚物(Monoinyl arene-Conjugated diene block copolymer)與水面上的油跡及油溢出物接觸 ,將油吸入塊狀共聚物之內,再將吸滿油漬的塊狀共聚物 與水分離。該塊狀共聚物可與圍繞在海域纘井台周圍的環 形管狀網結合;也可和欄木及堤結合,Μ防止油跡漂入港 口或沿部份海岸線漂移。 美國專利第4,941,978號揭示使用一種包含苯乙烯k 狀共聚物及乙烯/丁烯共聚物彈性物之粒狀彈性組合物, 處理水體上之油溢出物。 本發明係有關使用一種撤粒狀之熱塑性彈性塊狀共聚 物,從泥土及水中回收油及其他液體污染物之技術。而本 發明的觀念之一,係有關一種將有機液污染物從混有該污 染粒之一値水溶液中除去的方法,包括將該溶液通過一値 本紙張尺度逍用中a Η家《毕(CNS)T4规怙(2丨0X297公;¢) - 4 - 81. 6. 10,000張(H) 請 先 閲 背 而 之 注 急 事 項 再· 填 % 本-頁 π 線 經濟部屮央檁準局貝工消坨合作杜印3i Λ 6 η 6 2109G2 五、發明説明() (請先閲讀背而之注意事項孙填寫本頁) 接觸區域,此區域包含一個由撤粒狀之熱塑性彈性塊狀共 聚物所形成之固定床。該熱塑性彈性塊狀共聚物包含一値 線型雙塊狀共聚物、三塊狀共聚物或分支雙塊狀共聚物。 此外,此撤粒狀之熱塑性彈性塊狀共聚物包含一櫥結合於 一値彈性共軛二烯聚合物塊之單乙烯基芳香族聚合物塊、 或一個結合於一値彈性單烯聚合物塊之單乙烯基芳香族聚 合物塊。當溶液通過此微粒狀之塊狀共聚物所形成之固定 床後,可從接觸區域回收大致無污染物之水流。如有需要 ,溶液可經過一次或多次臭氧、紫外線照射及活性磺處理 及/或通過一個空氣汽提塔。 、 該彈性聚合物塊及/或單乙烯基芳番族聚合物塊可以 部份或完全氫化。熱塑性彈性共聚物最好是包含一個聚苯 乙烯-聚丁乙烯-聚苯乙烯塊狀共聚物或是一痼聚苯乙烯-乙烯/ 丁烯共聚物-聚苯乙烯塊狀共聚物。 經濟部中央標準局貝工消赀合作杜印製 此外,已發現從單乙烯基芳香族-共扼二烯塊狀共聚 物、單乙烯基芳香族-單烯塊狀共聚物及此等塊狀共聚物 之氫化衍生物所組成之族群中選出之熱塑性橡膠,若塗上 少量的疏水性矽土,則可大幅減少吸收油溘出物之時^及 所需使用之聚合物量。依據本發明,磺氫化合物溘出物係 與本發明之組合物接觸,而將碩氫化合物包住。若溢出物 是水上的原油或精練石油產品溢出物時,本發明之組合物 會將油包住,然後浮在水面上,它們可Μ很容易地被舀取 及回收。如果溢出物是在固體表面上,譬如修車廠地面, 則本發明之組合物會將溢出液體包住,使它們很容易被埽 本紙張尺度遑用中Β國家標毕(CNS)TM規格(210x297公*) 5 81. 6. 10,〇〇〇張(H) Λ Γ. η 6 210d9j 五、發明説明() 除,而且至多僅會留下少許的溘出液。 本發明亦有關一種自泥土中除去有機液污染物之方法 ,此方法包括將受到有機液污染之泥土與上述熱塑性彈性 塊狀共聚物中之一種結合之步驟。其次,受有機液污染之 泥土及熱塑性彈性共聚物混合形成一個熱塑性彈性共聚物 及受有機液污染的泥土之均質混合物。將此均質混合物再 與水混合後,可自此均質混合物中回收被共聚物包住之有 機污染物,Μ及自剩餘的混合物中回收無污染物之泥土。 本發明的觀點之一,係先將受污染的泥土最好是在壓 力下用水清洗,然後將水萃取物以上述之程序處理,即將 污染液通過一値含有撤粒狀之熱塑性撣性塊狀共聚物所形 成之固定床之接觸區域。 如有需要,可在自均質混合物回收之後,將被共聚物 包住的有機液污染物溶在諸如石油精、汽油、柴油或新原 油等有機溶劑中,形成一棰有機液污染物-彈性聚合物-石 油液組合物,此所得之液體組合物可做爲火爐、引擎等之 燃料。而且通常,係先挖出受有機液污染之泥土,然後再 將此污染泥土與熱塑性撣性塊狀共聚物混合。 ’ 本發明亦有關一種從固體表面回收有機液薄膜之方法 ,其步驟是先將前述之熱塑性彈性塊狀共聚物均勻散布在 該有機液薄膜上,然後從固體表面回收包住有機液之共聚 物。通常每加侖有機液所需使用的塊狀共聚物量約為0.1 磅至1磅,視溢出物的表面積及有機液的黏度及有機液附 在物體表面上的時間長短而定。譬如,表面積愈大、有機 (請先閲讀背而之注意事項再蜞寫本頁) 裝- 線- 經濟部屮央標準局貝工消费合作社印51 本紙張尺度遑用中a Η家《毕(CNS) Τ4規格(210X297公;¢) 6 81. β· 10,000張—(H) 21099^ 五、發明説明() 液黏度愈高、及有機液留在物體表面的時間愈長,則需要 較多的聚合物來包住這些有機液。 本發明的另一値觀點係有關一種使用回收自水中的碩 氫化合物流體的方法;而該碩氫化合物是K前述之一種熱 塑性彈性塊狀共聚物先將其包住,然後再回收得到者。此 方法之步驟包括在諸如石油精、汽油、柴油及原油等之溶 劑中溶解被熱塑性橡膠包住之硝氫化合物流釅,形成一棰 熱塑性橡膠-磺氫化合物滾體-石油液體組合物,此液駸組 合物可做為火鑪、引擎等之燃料。因此,本法亦包括在火 爐中燃燒此熱塑性橡膠-碩氫化合物流髏-石油液體組合物 之步驟。在溶解的步驟當中,最好是能將溶劑加熱,Μ增 進被熱塑性橡膠包住之碳氫化合物流體在溶剤中的溶解。 經濟部屮央檫準局貝工消赀合作杜印¾. 本發明亦係有關一種除去泥土中有機液污染物之方法 ,其中,先將該受有機物污染之泥土與水撤底地混合,Μ 便從泥土中萃取有機液污染物,並得到一種泥土/液體混 合物。然後將此泥土/液體混合物過濾,獲得經清洗之泥 土及一棰包含有機液污染物之濾液。接著,將濾液通過一 値包含由上述之一棰微粒狀熱塑性彈性塊狀共聚物所形成 之一個固定床之接觸區域,再從此接觭區域回收一個大致 無污染物之水流。 本發明亦係有關一種防止地下燃料槽內之有機污染物 漏入槽下之泥土的方法。此方法之步驟包括將第一數量之 泥土與上述之一種熱塑性彈性塊狀共聚物混合,形成一個 泥土/塊狀共聚物混合物,將此泥土/塊狀共聚物混合物 本紙张尺度逍用中ΒΗ家樣準(CNS) Ή規格(2)0X297公;¢) - 1 - 81. 6. 10,000張(H) Λ Γ» It 6 210992 五、發明説明() (請先閲讀背而之注意事項#项寫本頁) 放置在已掘好的泥土洞底,再將地下燃料槽放置在這些泥 土/塊狀共聚物混合物上,然後用第二數量之泥土將洞» 滿。該泥土/塊狀共聚物混合物會吸收任何從燃料槽漏出 而下滲之流體,如此可防止流體滲入土壤中。 本發明亦係有關一種防止自油井井源漏出或溢出之有 機污染物滲入井源附近的泥土中之方法。此方法先將第一 數S之泥土與上述之一種熱塑性彈性塊狀共聚物混合,形 成一傾泥土/塊狀共聚物混合物,然後將此泥土/塊狀共 聚物混合物放置在井源附近的地面上。此泥土/塊狀共聚 物混合物將吸收從井源漏出或溘出之有機污染物,如此可 防止此有機污染物滲入井源周圍的泥土中。 第1圖是一値船腹過濾条統之概圖,此糸統配有並聯 的共聚物處理單元,其內含有依據本發明之熱塑性彈性塊 狀共聚物顆粒,用Μ除去流過其間之水流内所含的碳氫化 合物污染物; 經濟部屮央標準而貝工消货合作杜印51 第2圖是一値組合形態處理糸統的流程圖,此条統包 括一個共聚物處理單元、一値空氣汽提塔單元、一値臭氧 處理單元、一個紫外線照射處理單元及一個活性碳處理單 元; 第3圖是顯示依據本發明用Μ從泥土中回收有機液的 一個方法之諸步驟的流程圖; 第4圖是一個放置於泥土/塊狀共聚物混合物上方之 地下燃料槽之截面圖;Μ及 第5圖是一個被環形泥土/塊狀共聚物混合物包圍的 本紙張尺度边用中ΒΗ家«平(CNS)T4規格(2】0χ297公;ΙΗ 8 81. 6. 10,〇〇〇張(Η) A G It 6 210993 五、發明説明() 產油井之井源的透視圖。 (請先閲讀背而之注意事項孙艰寫木頁) 本發明使用的這些組合物包含一種熱塑性彈性共聚物 。實施本發明時所用的熱塑性彈性共聚物包括具有至少一 種單乙烯基芳香族聚合物塊结合於另一種共轭二烯聚合物 塊之乙烯基芳香族單體及共軛二烯之塊狀共聚物片段,或 具有至少一種單乙烯基芳番族聚合物塊结合於另一種單嫌 聚合物之乙烯基芳香族單體及單烯單體之塊狀聚合物片段 ,及這些塊狀共聚物之氫化衍生物。每一値聚合物塊或塊 狀片段可Μ包含一百値或更多的結合在一起的單獨的單體 〇〇 — 早兀α 經濟部屮央標準而貝工消价合作社印5i 詳言之,本發明所使用的塊狀共聚物是熱塑性彈性線 型二塊狀、三塊狀或分支(放射狀〉二塊狀共聚物,它們包 含結合於彈性共轭二烯或彈性單烯聚合物塊之單乙烯基芳 香族聚合物塊,Μ及包括這些聚合物塊之氫化衍生物。熱 塑性彈性塊狀共聚物的一般結構,可以是線型Α-Β-Α三塊 狀型態、放射狀或分支Α-Β二塊狀型態、及線型Α-Β二塊狀 型態。在這些分子式中,“Α”代表一個單乙烯基芳香族 聚合物塊,它可部份或完全氫化;而“Β”代表一値i性 共軛二烯、氫化二烯、單烯或氫化單烯聚合物塊。 A-B-A三塊狀結構是以彈性聚合物塊B作為一値中間 區塊,而以聚合物塊A作爲終端區塊。而放射狀或分支 A-B二塊狀共聚物包含許多的A聚合物塊,它們分別在各 自的第一端結合在一起,形成一個共同中心。這些A聚合 物塊包括從共同中心Μ不同方向向外放射狀地延伸的各個 本紙尺度逍用中a a家標毕(CNS)T<1規怙(2】0X297公及) 9— 81. 6. ίο,000張(Η) Λ (5 Η 6 2109&2 五、發明説明() 第二端。每一個第二端連结至一掴B聚合物塊,它通常繼 鑛自共同中心Μ放射狀朝外延伸。 單乙烯基芳香族聚合物塊包含單質聚合物或共聚物塊 ,同時,大多是以一種單乙烯基芳香族單鰻作為主要的可 聚合的單元。共軛二烯與氫化二烯聚合物塊及單烯與氫化 單烯聚合物塊可Κ是單質聚合物或共聚物的形式;主要的 特性是它們的構造可Μ使它們具有彈性聚合性質之特性。 這些區塊“ A ”及“ Β ”可以部份或完全氩化。如果 僅爲部份程度的氫化,那麽最好是讓區塊“B” ,即共軛 二烯聚合物塊被氫化,以增進它們的抗氧化性。因此,這 些聚合物可包含未氫化的、部份氫化的、或完全氫化的聚 合物塊。 可用於形成本發明之熱塑性彈性塊狀共聚物的單乙烯 基芳香族單體包括苯乙烯、ct -甲基苯乙烯、及環烷基 苯乙烯。這些單體彼此可採聚合物或共聚物的方式結合 或和少量的共軛二烯形成區塊“A”。而可用於形成區塊 WB”或在區塊“A”中作為次要成份的共軛二烯,最好 是包括每分子含有4至8個硝原子的共軛二烯,特別是丁 二烯及異戊間二烯。至於可用Μ形成區塊“B”的單烯, 最好是含有2至8値磺原子,其中以乙烯、丙烯及丁烯較 適宜。目前,較佳的“Β”區塊包含乙烯/丙烯及乙烯/ 丁烯之共聚物。 代表性的熱塑性彈性塊狀共聚物,其組態為聚苯乙烯 -聚丁二烯-聚苯乙烯、聚苯乙烯-聚異戊二烯-聚苯乙烯、 本紙ffc尺度边用中國國家標準(〇奶)174規格(2】0父297公放) (請先閲請背而之注意事項#堝寫木頁) 裝· 訂 經濟部屮央標準局貝工消坨合作杜印5i 81. 6_ 10,000張(H) Λ 0 Η 6 2109δ2 五、發明説明() 及聚苯乙烯-聚(乙烯/ 丁烯)-聚苯乙烯Α-Β-Α三塊狀共聚 物;聚苯乙烯-聚丁二烯及聚苯乙烯-聚異戊二烯放射狀或 分支Α-Β二塊狀共聚物;Μ及聚苯乙烯-聚丁二烯、聚苯乙 烯-聚(乙烯/丙烯〉及聚苯乙烯-聚(乙烯/ 丁烯)線型Α-Β 二塊狀共聚物。目前較佳的熱塑性彈性塊狀共聚物是聚苯 乙烯-聚丁二烯-聚苯乙烯及聚苯乙烯-聚(乙烯/ 丁烯)-聚 苯乙烯線型Α-Β-Α三塊狀共聚物。 使用於本發明中之最佳的熱塑性橡膠是由密西根州大 急流市的Micro Environmenal公司目前以PS 3200及PS 3400之商檁名供應上市的商品。PS 3200產品包含一種聚 苯乙烯-聚丁二烯-聚苯乙烯塊狀共聚物,而PS 3400產品 包含一種聚苯乙烯-聚(乙烯/ 丁烯)-聚苯乙烯塊狀共聚 物。此製造商所供應的最理想材料是Μ小九狀或粉狀的形 式販售的一種撤粒狀物質。目前,較偏好使用粉狀形式 ,因爲它較小九形式之材料能提供較大的吸收及/或吸附 (“包住” >表面積。這些熱塑性彈性(橡膠 >塊狀共聚物顆 粒的細度模數最好是介於100至300微米之間,其中180至 220撤米是最理想的。 有些情況,需要在熱塑性彈性共聚物顆粒表面均勻地 塗上少量的疏水性矽土,以增加其流動性及吸收碳氫化合 物的能力。專利及技術文獻上均有披露可使用的疏水性矽 土添加劑,這些添加劑也容易自許多廠商處取得。疏水性 矽土大致可包括任何含矽土的化合物,譬如矽土、矽蒲土 、板狀矽藻土及經過處理而具疏水性之其他形式的矽蒲土 本紙張尺度逍用中a Η家標準(CN5) Ή規格(210X297公*) (請先閲讀背而之注意事項4堝寫本頁) 裝. 線< .經濟部屮央標準局员工消赀合作社印製 81. 6. 1〇,〇〇〇張(Η) Λ (ί Η Γ> 2109G3 五、發明説明() 。最佳的矽土爲纽澤西州富田公圔市的Degussa公司以 Aerosil R-972、R-972V、R-974、R-974V及 R-976之商檫 名供應上市的疏水性非晶形燻黑矽土。疏水性矽土的使用 量可為0.1〜2.5値重量百分比(wt%),最好是0·5個重量 百分比,端視熱塑性彈性塊狀共聚物的重量而定。 疏水性矽土可用任何傳統的混合方法很快地和熱塑性 彈性塊狀共聚物結合,使塊狀共聚物的表面得到一層均句 的疏水性矽土覆層。 決定所需使用的處理過之塊狀共聚物量*部份將視所 欲吸收的油膜厚度、經濟回收污染油所需的時間、在處理 水中的油跡時欲除油之水體的攪動情形、以及類似的物理 因素而定。當溢出物包含一層厚度不超過0.5吋的薄膜時 ,對於毎加侖的溢出物,最好使用3至7磅的撤粒狀塊狀 共聚物。塊狀共聚物將油包住所需的時間,將隨溫度、摄 動的程度、液體溘出物與塊狀共聚物的比例、液體的黏度 及所使用的塊狀共聚物的表面而異。 經濟部屮央榣準局貝工消ίϊ·合作社印¾ 本發明之外覆層的塊狀共聚物撤囊劑,在其阐舆液體 溢出物接觸後數秒内,很快地就會將碳氫化合物溘出物包 住。而淸除不超過半吋的溢出物所需的時間,通常是以分 鐘來計算。不過,像油輪撕淺所產生的較大範圍的溢出物 ,清除時較爲費時,因爲新鮮的撤囊劑表面的連續暴露時 間,將視溘出物的體積及其擴展的面積而定。通常Μ本發 明之徹囊劑處理溘出物時,最好是在溘出發生的大約4小 時Μ內開始。不難理解,在使用本發明之組合物處理極大 81. 6. 10,〇〇〇張(H) 本紙»尺度逍用中8 8家標準(〔胳)〒4規格(210父297公*) Λ (i It 6 21099-5 五、發明説明() 之溢出時,需要一次Μ上的溢出物處理。 令人驚奇的是,塊狀共聚物即使在經過少量的疏水性 矽土處理後(譬如0.1〜2.5個體積百分比),也可增加清除 能力,其清除體積的改進,從大約每體積的塊狀共聚物處 理3倍體積的油增加至大約每體積的塊狀共聚物處理4倍 髏積的油。此外,使用處理過的塊狀共聚物包住溘出油的 時間比使用未處理的聚合物吸收溢出油的時間,大約減少 25%。 處理過的塊狀共聚物大致完全將溢出液包入其體内, 而塊狀共聚物撤囊劑的表面大致上保持乾燥及無毒。因此 ,將便於Μ—些方法,譬如用耙子聚攏、移動攔木或網等 ,沿箸水面或類似的表面收集塊狀共聚物及封入其內的液 體。假如溢出物是在諸如鋼甲板、木甲板、水泥地等之固 體表面時,可使用掃帚或類似之物掃除包箸液體的該共聚 物0 有許多方法可完成本發明之組合物在清除液體溢出物 方面之應用。最好是將此組合物較為均勻地散布在受污染 的區域上或是所欲處理的部份區域上。本發明之组合物可 Μ被撤播或Μ別的方法散布在溢出液的表面及/或溢出液 内。這可用多種方式完成之。在水泥地面或類似的表面上 的液體溢出物,可以藉人工撒播或別的散布方法將本發明 之組合物散布其上,Μ回收這些湓出物。而水面上較小的 溘出物可以從小船上噴、吹、或撤出本發明之組合物至溢 出物的表面,而加以處理。對於較大的溢出物,可能需要 本紙》尺度边用中a國家楳準(CN5)甲4規格(210X297公:¢) (請先閱誚背而之注意事項#项筠^-頁) 裝· 線· 經濟部屮央櫺準局Α工消奸合作社印製 81. 6. l〇,〇〇〇ft (Η) Λ Γ. II 6 21090^ 五、發明説明() 使用數艘船隻。在有一大片區域受油污染的情況下,可Μ 傳統的飛機嗅鐳固態物至油跡的表面。這些溢出物會被包 住,因而阻止它們艤續的擴散,然後使用可讓水流通的欄 木,其中在一値多孔的網狀覆蓋物内含有本發明之撤囊劑 ,以防止&出物與海岸線及海灘接觭。這些攔木可讓水通 過其結構,但是會將經過網狀覆蓋物的油包住,使油無法 通過。 本發明之組合物亦可用於清理船腹水槽,可將本發明 之撤囊劑直接撤入船腹水槽中,或是使用一値内含裝滿本 發明之多孔撤囊劑混合物之封閉網狀布之枕頭或船腹袋, 以清除污染。 本發明亦係有關一種去除有機液污染物的處理方法, 特別是諸如化學處理液流之類的水流内所散布或攜帶的碩 氫化合物。在本處理方法中,讓一個受有機液污染的水流 ,直接流經一値由熱塑性彈性共聚物吸收劑顆粒所構成的 固定床。此類所欲處理的水流包含有機液污染物,像燃料 、甲基乙嗣、甲苯、乙苯、二甲苯及苯,Μ及甚至像鐵之 類的金羼。譬如第1圖它是一個去除船腹中所攜帶之有機 液污染物的處理条統,此条統包括一個共聚物處理單元11 ,此單元包括一個位於二個平行共聚物吸收劑床12及14下 游的船腹泵10,其並且以適當的管路與之連接。受污染的 有機液流可自船腹18或其他含有污染液的容器中被泵抽取 ,使其流經一個船腹出口管16,然後由一値三通閥24導引 其流過一値處理單元進入管20或處理單元進入管22。壓力 81. 6. 10,000張(Η) (請先閱讀背而之注意事吩孙堝¾.木頁) 裝. 訂_ 經濟部屮央標準而A工消伢合作社印51 Λ fi ΗΓ) gl〇9i^ 五、發明説明() 表23可測置船腹出口管16中受污染之有機液的壓力。 (請先閲讀背而之注总事項再项寫木頁) 當三通閥24導引污染液流進入處理單元進入管20時, 此汚染液可被船腹泵10抽取流經含有一個由熱塑性彈性塊 狀共聚物顆粒所構成之固定床的共聚物吸收劑床12。從共 聚物吸收劑床12流出之處理遇的水溶液大致上無污染物的 存在,它流經一値處理單元出口管26,然後由一個三通閥 28將其導入容器進入管30。壓力錶32可測量流經容器進入 管30内已處理液之壓力。最後,船腹泵10將容器進入管30 中之處理液抽至一値處理液容器34內或回到船腹18中。 就像包含平行的多値處理單元的液體處理条統傳統作 法一樣,共聚物吸收劑床14保持隨時待命備用的狀態,只 要第一個共聚物吸收劑床12進行其内固定層之共聚物顆粒 再生時,即可上線接替蓮作。各共聚物吸收劑床12及14所 填装的塊狀共聚物撤囊劑顆粒(吸收劑)量,必須足夠包住 大約2 1/2夸特(quarts〉的液體有機污染物。由壓力錶23 及壓力錶32所測得之壓力差,代表通過共聚物吸收劑床12Λ (i 15 6 210992 V. Description of the invention) This invention relates to the technology for recovering organic liquids and petroleum-related products from water bodies, soil, water flow, ship stern, and solid surfaces such as garages and factory floors, sales decks and similar solid surfaces, These petroleum products include crude oil and refined petroleum distillates. Many methods have been proposed for the treatment of petroleum-related pollutants. Many materials have been proposed for use as oil spill absorbers, including a large amount of straw , Clay, silica or Kieselguhr particles. At the same time, it has also been proposed to use foamed polymer materials such as porous polystyrene particles and porous polyethylene wool, or solid inorganic fillers Other additives are used together. US Patent No. 3, 518, 183 discloses the use of a mono-area large-area monovinyl aromatic conjugated diene block copolymer (Monoinyl arene-Conjugated diene block copolymer) and oil traces on the water In contact with oil spills, draw oil into the block copolymer, and then separate the block copolymer filled with oil from the water. The polymer can be combined with the ring-shaped tubular net surrounding the pit platform in the sea; it can also be combined with railings and embankments to prevent oil traces from drifting into the port or along part of the coastline. US Patent No. 4,941,978 discloses the use of a styrene A granular elastic composition of k-shaped copolymer and ethylene / butene copolymer elastomer to treat oil spills on water. The present invention relates to the use of a pelletized thermoplastic elastomer block copolymer to recover from soil and water The technology of oil and other liquid contaminants. One of the concepts of the present invention relates to a method for removing organic liquid contaminants from an aqueous solution mixed with the contaminated particles, which includes passing the solution through a standard paper Happy to use a Η family "Bi (CNS) T4 regulations (2 丨 0X297; ¢)-4-81. 6. 10,000 sheets (H) Please read the back to the urgent matters first, then fill in this page π Line Ministry of Economics Biyang Purification Bureau Beigong Xiaotuo Cooperation Du Yin 3i Λ 6 η 6 2109G2 Fifth, invention description () (please read the precautions Sun fills in this page first) contact area, this area contains a Removal of granular thermoplastic bombs A fixed bed formed by a block copolymer. The thermoplastic elastomer block copolymer includes a linear double block copolymer, a triple block copolymer, or a branched double block copolymer. In addition, the pelletized thermoplastic elastic block The copolymer includes a monovinyl aromatic polymer block bonded to an elastic conjugated diene polymer block, or a monovinyl aromatic polymer block bonded to an elastic monovalent polymer block. After the solution passes through the fixed bed formed by the particulate block copolymer, the water stream can be recovered from the contact area with substantially no contaminants. If necessary, the solution can be subjected to one or more ozone, ultraviolet radiation and active sulfonation treatments and / Or through an air stripping tower. The elastic polymer block and / or monovinyl aromatic polymer block can be partially or completely hydrogenated. The thermoplastic elastic copolymer preferably comprises a polystyrene-polybutylene-polystyrene block copolymer or a polystyrene-ethylene / butylene copolymer-polystyrene block copolymer. The Ministry of Economic Affairs, Central Standards Bureau, Beigong Consumer Co., Ltd. cooperated with Du Printing. In addition, it has been found from monovinyl aromatic-conjugated diene block copolymers, monovinyl aromatic-monoene block copolymers and these blocks If the thermoplastic rubber selected from the group consisting of hydrogenated derivatives of the copolymer is coated with a small amount of hydrophobic silica, it can greatly reduce the amount of oil absorbed and the amount of polymer required. According to the present invention, the sulfohydrogen compound educt is brought into contact with the composition of the present invention to encase the hydrogen compound. If the spillage is crude oil from water or refined petroleum product spillage, the composition of the present invention will entrap the oil and then float on the surface of the water, they can be easily scooped and recovered. If the spillage is on a solid surface, such as a garage floor, the composition of the present invention will cover the spilled liquid so that they can easily be used on paper scales in China National Standard (CNS) TM specifications (210x297 (Public *) 5 81. 6. 10,000 sheets (H) Λ Γ. Η 6 210d9j V. Description of the invention () Except that, at most, only a little effusion will be left. The present invention also relates to a method for removing organic liquid contaminants from mud. The method includes the step of combining soil contaminated with organic liquid with one of the above-mentioned thermoplastic elastic block copolymers. Secondly, the soil contaminated with the organic liquid and the thermoplastic elastic copolymer are mixed to form a homogeneous mixture of the thermoplastic elastic copolymer and the soil contaminated with the organic liquid. After this homogeneous mixture is mixed with water again, organic contaminants encapsulated by the copolymer can be recovered from this homogeneous mixture, and contaminant-free soil can be recovered from the remaining mixture. One of the viewpoints of the present invention is that the contaminated soil is preferably washed with water under pressure, and then the water extract is processed according to the above procedure, that is, the contaminated liquid passes through a thermoplastic dusty block containing granular particles The contact area of the fixed bed formed by the copolymer. If necessary, after recovery from the homogeneous mixture, the organic liquid contaminants encapsulated by the copolymer can be dissolved in organic solvents such as petroleum spirits, gasoline, diesel, or new crude oil to form an organic liquid contaminant-elastic polymerization Oil-petroleum liquid composition, the liquid composition obtained here can be used as fuel for stoves, engines, etc. Moreover, usually, the soil contaminated with organic liquid is excavated first, and then the contaminated soil is mixed with the thermoplastic block copolymer. The present invention also relates to a method for recovering an organic liquid film from a solid surface, the steps of which are to first uniformly spread the aforementioned thermoplastic elastic block copolymer on the organic liquid film, and then recover the copolymer covering the organic liquid from the solid surface . Generally, the amount of block copolymer required per gallon of organic liquid is about 0.1 lb to 1 lb, depending on the surface area of the spill, the viscosity of the organic liquid, and the length of time the organic liquid is attached to the surface of the object. For example, the larger the surface area, the more organic (please read the precautions before writing on this page). Install-Line-51 copies of the paper standard used by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. CNS) Τ4 specifications (210X297; ¢) 6 81. β · 10,000 sheets— (H) 21099 ^ V. Description of invention () The higher the viscosity of the liquid and the longer the organic liquid stays on the surface of the object, the more it needs Polymer to encapsulate these organic liquids. Another aspect of the present invention relates to a method of using a hydrogen compound fluid recovered from water; and the hydrogen compound is a thermoplastic elastomeric block copolymer of K described above, which is first wrapped and then recovered. The steps of this method include dissolving a stream of nitrile compound wrapped in thermoplastic rubber in a solvent such as petroleum spirits, gasoline, diesel oil, crude oil, etc. to form a roll of thermoplastic rubber-sulfohydrogen compound-petroleum liquid composition. The liquid compound can be used as fuel for stoves, engines, etc. Therefore, this method also includes the step of burning the thermoplastic rubber-hydrogen compound-petroleum liquid composition in a furnace. In the dissolving step, it is preferable to heat the solvent to increase the dissolution of the hydrocarbon fluid covered by the thermoplastic rubber in the solvent. The Ministry of Economic Affairs, the Central Bureau of Sassafras and the Bureau of Industry and Fisheries cooperated with Du Yin ¾. The present invention also relates to a method of removing organic liquid contaminants in the soil, in which the soil contaminated with organic matter is first mixed with water to the bottom, M The organic liquid contaminants are extracted from the soil and a soil / liquid mixture is obtained. This mud / liquid mixture is then filtered to obtain cleaned mud and a filtrate containing organic liquid contaminants. Next, the filtrate is passed through a contact area containing a fixed bed formed of one of the above-mentioned particulate thermoplastic elastomeric block copolymers, and a substantially contaminant-free water stream is recovered from this joint area. The invention also relates to a method for preventing organic pollutants in underground fuel tanks from leaking into the soil under the tanks. The steps of this method include mixing the first amount of soil with one of the above-mentioned thermoplastic elastic block copolymers to form a soil / block copolymer mixture. The soil / block copolymer mixture is used in this paper scale. Sample standard (CNS) Ή specification (2) 0X297; ¢)-1-81. 6. 10,000 sheets (H) Λ Γ »It 6 210992 V. Description of invention () (please read the back to the notes # item Write this page) Place at the bottom of the excavated mud cave, and then place the underground fuel tank on these mud / block copolymer mixture, and then fill the cave with the second amount of mud ». The soil / block copolymer mixture will absorb any fluid that leaks out of the fuel tank and infiltrates, thus preventing the fluid from seeping into the soil. The present invention also relates to a method for preventing organic contaminants leaking or overflowing from the well source from penetrating into the soil near the well source. This method first mixes the soil of the first number S with one of the above-mentioned thermoplastic elastic block copolymers to form a tilting soil / block copolymer mixture, and then places the soil / block copolymer mixture on the ground near the well source on. This soil / bulk copolymer mixture will absorb organic contaminants leaking or escaping from the well source, thus preventing the organic contaminants from seeping into the soil around the well source. Figure 1 is an overview of a stern filter system. This system is equipped with a parallel copolymer processing unit, which contains thermoplastic elastomer block copolymer particles according to the present invention, and the water flowing therethrough is removed by Μ Contained hydrocarbon contaminants; the Ministry of Economic Affairs, the central standard and the Beigong Consumer Goods Cooperation Du Yin 51. Figure 2 is a flow chart of a combined morphology processing system, this system includes a copolymer processing unit, a value Air stripping tower unit, an ozone treatment unit, an ultraviolet irradiation treatment unit and an activated carbon treatment unit; Figure 3 is a flow chart showing the steps of a method for recovering organic liquid from mud according to the present invention; Figure 4 is a cross-sectional view of an underground fuel tank placed above the soil / bulk copolymer mixture; Μ and Figure 5 are a paper-scale edge of the paper surrounded by an annular soil / bulk copolymer mixture. Ping (CNS) T4 specifications (2) 0 × 297; ΙΗ 8 81. 6. 10,000 sheets (Η) AG It 6 210993 V. Description of invention () A perspective view of the source of the oil production well. (Please read first Pay attention to Xiang Sunxian wrote a wooden page) The compositions used in the present invention include a thermoplastic elastic copolymer. The thermoplastic elastic copolymer used in the practice of the present invention includes a block having at least one monovinyl aromatic polymer bonded to another conjugated two The vinyl aromatic monomer of the vinylene polymer block and the block copolymer segment of the conjugated diene, or the vinyl aromatic monomer having at least one monovinylaromatic polymer block bonded to another single polymer Block polymer fragments of bulk and monoene monomers, and hydrogenated derivatives of these block copolymers. Each polymer block or block fragment can contain one hundred or more individual Monomer 〇〇— Zaowu α The Ministry of Economic Affairs Standard and the Beigong Pricing Cooperative Printed 5i. In detail, the block copolymer used in the present invention is a thermoplastic elastic linear two-block, three-block or branched (radial > Diblock copolymers, which contain monovinyl aromatic polymer blocks bonded to elastic conjugated diene or elastic monoene polymer blocks, M and hydrogenated derivatives including these polymer blocks. The general structure of the linear block copolymer can be linear A-B-A three-block form, radial or branched A-B two-block form, and linear A-B two-block form. In these molecular formulas Among them, "Α" represents a monovinyl aromatic polymer block, which can be partially or completely hydrogenated; and "Β" represents a univalent conjugated diene, hydrogenated diene, monoene or hydrogenated monoene polymer The three-block structure of ABA uses elastic polymer block B as an intermediate block and polymer block A as a terminal block. Radial or branched AB block copolymer contains many A polymer blocks , They are combined together at their first ends to form a common center. These A polymer blocks include various paper-based Xiaoyaozhongbi (CNS) that extend radially outward from the common center M in different directions. T < 1 regulation (2) 0X297 and 9-81. 6. ίο, 000 sheets (Η) Λ (5 Η 6 2109 & 2 V. Description of the invention) The second end. Each second end is connected to a slap B polymer block, which usually extends radially outward from the common center M. Monovinyl aromatic polymer blocks contain elemental polymer or copolymer blocks. At the same time, most of them contain a monovinyl aromatic monoeel as the main polymerizable unit. Conjugated diene and hydrogenated diene polymer blocks and monoene and hydrogenated monoene polymer blocks can be in the form of elementary polymers or copolymers; the main feature is that their structure can make them have the characteristics of elastic polymerization properties . These blocks "A" and "B" can be partially or completely argonized. If the hydrogenation is only partial, it is best to allow block "B", the conjugated diene polymer block, to be hydrogenated to improve their oxidation resistance. Therefore, these polymers may contain unhydrogenated, partially hydrogenated, or fully hydrogenated polymer blocks. The monovinyl aromatic monomers that can be used to form the thermoplastic elastic block copolymer of the present invention include styrene, ct-methylstyrene, and cycloalkylstyrene. These monomers can be combined with each other in the form of polymers or copolymers or form a block "A" with a small amount of conjugated diene. The conjugated diene that can be used to form block WB "or as a minor component in block" A "preferably includes conjugated diene containing 4 to 8 nitrile atoms per molecule, especially butadiene And isoprene. As for the monoene which can form the block "B" with M, it is best to contain 2 to 8-value sulfon atoms, among which ethylene, propylene and butene are more suitable. At present, the preferred "B" The block contains copolymers of ethylene / propylene and ethylene / butene. Representative thermoplastic elastomer block copolymers with configurations of polystyrene-polybutadiene-polystyrene, polystyrene-polyisoprene Ethylene-polystyrene, ffc scale of this paper, the Chinese national standard (〇 milk) 174 specifications (2) 0 father 297 public release) (please read the back-to-be-attentive matters # 锅 写 木 页) Duyang 5i 81. 6_ 10,000 sheets (H) Λ 0 Η 6 2109δ2 of the Yangtze Standard Bureau Beigong Xiaotuo Co., Ltd. 5. Description of invention () and polystyrene-poly (ethylene / butylene) -polystyrene A-B -A triblock copolymer; polystyrene-polybutadiene and polystyrene-polyisoprene radial or branched A-B diblock copolymer; M and polystyrene -Polybutadiene, polystyrene-poly (ethylene / propylene) and polystyrene-poly (ethylene / butene) linear A-B diblock copolymers. The currently preferred thermoplastic elastic block copolymer is poly Styrene-polybutadiene-polystyrene and polystyrene-poly (ethylene / butene) -polystyrene linear A-B-A triblock copolymer. The best thermoplastic rubber used in the present invention It is currently supplied by Micro Environmenal Corporation of Grand Rapids, Michigan under the trade name of PS 3200 and PS 3400. PS 3200 products include a polystyrene-polybutadiene-polystyrene block copolymer, The PS 3400 product contains a polystyrene-poly (ethylene / butylene) -polystyrene block copolymer. The most ideal material supplied by this manufacturer is a kind of revocation sold in the form of M small nine or powder Particulate matter. Currently, the powder form is preferred because its smaller nine-form material provides greater absorption and / or adsorption ("envelopment" > surface area. These thermoplastic elastomers (rubber > block copolymerization The fineness modulus of the particles is preferably between 100 and 300 microns Among them, 180 to 220 meters is the most ideal. In some cases, it is necessary to uniformly coat a small amount of hydrophobic silica on the surface of the thermoplastic elastomer copolymer particles to increase its fluidity and ability to absorb hydrocarbons. Patent and Technical literature has disclosed hydrophobic silica additives that can be used, and these additives are also readily available from many manufacturers. Hydrophobic silicas can generally include any compound containing silica, such as silica, silica gel, platy silica Algae soil and other forms of hydrophobic silicon pombenite used in paper size for a happy use a Η family standard (CN5) Ή specification (210X297 g *) (please read the precautions 4 before writing this page ) Installed. Line <. Printed by the employee consumption cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 81. 6. 10, 〇〇〇 Zhang (Η) Λ (ί Η Γ > 2109G3 V. Description of the invention). The best silica is the hydrophobic amorphous fumigation marketed by Degussa Company, Futian, New Jersey under the commercial name of Aerosil R-972, R-972V, R-974, R-974V and R-976. Black silica. The amount of hydrophobic silica used may be 0.1 to 2.5 weight percent (wt%), preferably 0.5 weight percent, depending on the weight of the thermoplastic elastic block copolymer. The hydrophobic silica can be quickly combined with the thermoplastic elastomer block copolymer by any conventional mixing method, so that the surface of the block copolymer is provided with a uniform hydrophobic silica coating. The amount of treated block copolymer to be used is determined by the thickness of the oil film to be absorbed, the time required to economically recover the contaminated oil, the agitation of the water body to be degreased when treating the oil trace in the water, and Similar physical factors. When the spill contains a film no thicker than 0.5 inches, it is best to use 3 to 7 pounds of pelletized block copolymer for each gallon of spill. The time required for the block copolymer to entrap the oil will vary with temperature, the degree of perturbation, the ratio of liquid extract to the block copolymer, the viscosity of the liquid, and the surface of the block copolymer used. Printed by Beigongxiao, Co-operative Society, Ministry of Economic Affairs, Ministry of Economic Affairs ¾ The outer layer of the block copolymer of the present invention is a bulk copolymer withdrawal agent, and within a few seconds after the liquid spill is exposed, the hydrocarbon will soon be removed. Compound exudates are covered. The time required to remove spills not exceeding half an inch is usually calculated in minutes. However, the larger range of spills, such as those caused by shallow tearing of oil tankers, is more time-consuming to remove, because the continuous exposure time of the surface of the fresh entrainment agent will depend on the volume of the exudates and their expanded area. In general, when treating the exudate with the capsules of the present invention, it is best to start within about 4 hours of the occurrence of eruption. It is not difficult to understand that when using the composition of the present invention, it is extremely large to handle 81. 610, 000 sheets (H) of this paper »Standards and Standards (88) 〒 4 specifications (210 father 297 g *) Λ (i It 6 21099-5 Fifth, the description of the invention), the overflow of the M needs to be treated once. Surprisingly, the block copolymer even after a small amount of hydrophobic silica treatment (such as 0.1 ~ 2.5 volume percent), can also increase the removal capacity, its removal volume improvement, from about 3 times the volume of the bulk copolymer processing oil to increase to about 4 times the volume of the bulk copolymer processing volume In addition, the time for using the treated block copolymer to entrap the spilled oil is about 25% less than the time for using the untreated polymer to absorb the spilled oil. The treated block copolymer substantially completely removes the spilled liquid. Encased in the body, and the surface of the block copolymer sachet is generally kept dry and non-toxic. Therefore, it will be convenient for some methods, such as gathering with a rake, moving a bar or net, etc., along the surface of the choppy water or similar Collect and seal block copolymer on the surface Liquid. If the spillage is on a solid surface such as a steel deck, wooden deck, concrete floor, etc., you can use a broom or similar to remove the copolymer containing the liquid. There are many ways to complete the removal of the composition of the present invention. The application of liquid spillage. It is better to spread the composition more evenly on the contaminated area or on the part of the area to be treated. The composition of the present invention can be removed or other methods Spread on the surface of the spilled liquid and / or in the spilled liquid. This can be done in a variety of ways. Liquid spills on concrete floors or similar surfaces can be spread by manual spreading or other methods of spreading the composition of the invention On the other hand, M recovers these debris. The smaller debris on the water surface can be sprayed, blown, or withdrawn from the boat to the surface of the spill and treated. For larger spills, This paper may be required "for standard use in the national aqua standard (CN5) Grade 4 (210X297): (please read the back and forth precautions # 项 筠 ^ -page) installation · line · Ministry of Economic Affairs Quasi-bureaucrat Printed by Zuoshe 81. 6. l〇, 〇〇〇ft (Η) Λ Γ. II 6 21090 ^ 5. Description of the invention () Several ships are used. In the case of a large area contaminated by oil, it can be traditional The aircraft smells radium solids to the surface of the oil traces. These spills will be trapped, thus preventing their continued diffusion, and then use a fence that allows water to flow, which is contained in a porous mesh cover The decapsulation agent of the present invention prevents & outgoing objects from reaching the coastline and beaches. These barriers allow water to pass through its structure, but it will entrap the oil passing through the mesh covering, making it impossible for the oil to pass. The composition can also be used to clean the abdomen water tank. The decapsulation agent of the invention can be directly withdrawn into the abdomen water tank, or a pillow with a closed mesh cloth filled with the porous aeration agent mixture of the invention or Stern bag to remove pollution. The present invention also relates to a treatment method for removing contaminants in organic liquids, in particular, hydrogen compounds dispersed or carried in water streams such as chemical treatment liquid streams. In this treatment method, a stream of water contaminated with organic liquid is allowed to flow directly through a fixed bed of thermoplastic elastomer copolymer absorbent particles. This type of water stream to be treated contains organic liquid contaminants such as fuel, methyl ethyl ether, toluene, ethylbenzene, xylene and benzene, M and even Jinlong like iron. For example, in Figure 1, it is a treatment system for removing organic liquid contaminants carried in the stern of the ship. This system includes a copolymer processing unit 11 which includes a downstream of two parallel copolymer absorbent beds 12 and 14 The stern pump 10 is connected to it by an appropriate pipeline. The contaminated organic liquid flow can be pumped from the stern 18 or other container containing the sloping liquid to make it flow through a stern outlet pipe 16, and then guided by a three-way valve 24 to flow through a value treatment unit The tube 20 or the processing unit enters the tube 22. Pressure 81. 6. 10,000 sheets (Η) (please read the cautionary notes of the Sun Sun crucible ¾. Wood pages). Binding. Order _ The Ministry of Economic Affairs Standards and the A Industrial Consumer Cooperation Cooperative Print 51 Λ fi ΗΓ) gl. 9i ^ V. Description of the invention () Table 23 can measure the pressure of the contaminated organic liquid in the outlet pipe 16 of the stern. (Please read the general notes first and then write the wooden page) When the three-way valve 24 directs the contaminated fluid into the treatment unit and enters the pipe 20, this contaminated fluid can be drawn by the stern pump 10 A fixed-bed copolymer absorbent bed 12 composed of massive copolymer particles. The treated aqueous solution flowing out from the copolymer absorbent bed 12 is substantially free of contaminants, it flows through the outlet pipe 26 of a unit, and then is introduced into the container inlet pipe 30 by a three-way valve 28. The pressure gauge 32 can measure the pressure of the treated liquid flowing into the tube 30 through the container. Finally, the abdomen pump 10 pumps the treatment liquid from the container into the tube 30 into a treatment liquid container 34 or back into the abdomen 18. Just like the conventional practice of liquid treatment systems including parallel multi-value processing units, the copolymer absorbent bed 14 remains ready for use as long as the first copolymer absorbent bed 12 carries the copolymer particles in its fixed layer When regenerating, you can go online to replace the lotus. The amount of bulk copolymer bladder particles (absorbent) filled in each of the copolymer absorbent beds 12 and 14 must be sufficient to enclose about 2 1/2 quarts of liquid organic contaminants. By pressure gauge 23 and the pressure difference measured by the pressure gauge 32 represent the bed 12 through the copolymer absorbent

I 經濟部屮央標準而A工消"合作社印製 之壓力降。當通過共聚物吸收劑床12之壓力降相當於包住 大約2夸特的污染物時,即會產生一個適當的警示,此時 操作員可讓第二値共聚物吸收劑床14接替蓮作,而將第一 値共聚物吸收劑床12中之固定床顆粒再生。只需轉動三通 閥24即可使第二個共聚物吸收劑床14上線蓮作,此後受污 染之有機液將流經處理單元進入管22,而非處理單元進入 管20。從共聚物吸收劑床14流出之已處理液將進入出口管 36。三通閥28應被轉成可使流經出口管36的處理液被導入 81. 6. 10,〇〇〇張(H) 本紙張尺度遑用中BB家樣毕(CNS)T4規怙(210x297公龙) 210902_Λβ_ 五、發明説明() 容器進入管30内。 此船腹過濾条統如此浬作幾館月後,環境中大致將無 污染物留存。但是,若所用共聚物吸收劑床中之固定床顆 粒未適時再生,則固定床僅将鐵續作用到容器進入管30中 之已處理液壓力,無法維持船腹泵10之適當蓮作時爲止。 此時將導致船腹泵10產生大幅氣蝕的現象。 經济部屮央標準^ΕΞζ工消仲合作社印製 最初的測試數據指示,數値像第1圖所示者之共聚物 處理單元11,可採串聯的方式安置,將可得到連續性的高 度污染物去除效果。或者參見第2圖,則可見另一種組合 条統,此条統包含一個或多個共聚物處理單元11、一個或 多値空氣汽提塔單元40、一個或多値臭氧處理單元42、一 個或多値紫外線照射處理單元44M及一傭或多値活性硪處 理單元46,它們Μ串聯的方式安置,用Μ除去進入水流48 之污染物,並產生一個無污染之出口水流50。當然,一値 組合条統不一定要包括所有的這些單元,它可Μ是這些單 元的任意组合。譬如,臭氧處理單元42較宜於在欲殺死進 入水流48中的細菌或去除水流中之金羼時使用。紫外線 照射處理單元44亦適於殺死細菌。決定使用一連串的聚合 物吸收劑單元或是某種形式的组合条統,將視污染物的性 質、所需去除的程度、及相鼷成本而定。譬如,處理一個 主要受到像二甲苯之類的較低揮發性化合物所污染的水流 ,從技術及經濟的觀點,僅以聚合物處理的方法是很不錯 的。 若使用組合型糸統處理受汽油污染的水流,那麽在使 81. 6. 10,000ft (Η) (請先閲讀背而之注意事項#艰寫本页) 本紙張尺度边用中ΒΒ家標準(CNS)〒4規怙(210x297公货) Λ ίϊ Π 6 經濟部屮央櫺準局A工消货合作社印製 五、發明説明() 用一値空氣汽提塔單元前,先用一痼共聚物處理單元預先 處理該水流,則可能除去大量的苯及甲苯、以及大致上所 有像二甲苯之類的較低揮發性化合物。如此將減輕含活性碩 之處理塔的A擔,而增加活性碳的赛命。如此由於活性磺 費用可大幅降低,此組合處理方法可獲致較低的整體處理 成本。 此外,在目前商業上使用的處理糸統中,通常都使用 活性碳處理單元。因為活性硪處理單元構成被認可的過濾 介質。不過,活性碩床幾乎每天都必須再生,增加相當可 觀的成本。當一個共聚物處理單元與一値活性磺處理單元 串聯在一起,同時置於活性硝處理單元前,則活性碩處理 單元中之活性硪大約每隔1至2週才需再生。使用這棰组 合處理条統,共聚物處理單元中之共聚物大约每3至4天 才需再生,而再生的費用比活性碳床的再生費用為低。 本發明亦係有關一棰使用被包在熱塑性橡膠塊狀共聚 物之內而由水中回收的磺氫化合物流體的方法。本法是將 被熱塑性橡膠包住之硪氳化合物流體在諸如石油精、汽油 、柴油及原油之類的溶剤中溶解,形成一棰適合用作火爐 、引擎等之燃料的熱塑性橡膠-硪氫化合物流體-石油液組 合物。換言之,在此溶解步驟中,熱塑性橡膠亦會被溶劑 溶解。然後這種熱塑性橡膠-碩氫化合物流體-石油液組合 物可在火瀘中燃燒或作為引擎的燃料。在溶解的過程,最 好能加熱溶劑以促進被熱塑性橡膠包住之磺氫化合物流體 在溶劑中之溶解。 (請先閲請背而之注意事項孙项寫本頁) 裝· 訂 線- 本紙尺度逍用中a Η家樣準(CHS) 規格(210X297公;¢) _ _ 81. 6. 10,000張(H) Λ ίί Η 6 2109^2 五、發明説明() 本發明亦係有關二種回收滲入土中的有機液特別是硪 氫化合物的方法。請參考第3圖,在其中第1種方法中, 先掘出受溘出物所污染的泥土,將之放入一値諸如帶式混 合器的混合器内。其次,將前述之一種塊狀共聚物撤囊劑 Μ與混合物内之污染泥土成大約1:10至1:1最好是1:1 的重量比例加入混合器内。此外,宜再加入一些新鮮的碩 氫化合物至混合器內的泥土及撤囊劑中Μ活化有機液污染 物。 第三,在混合器中將污染泥土及塊狀共聚物徹囊劑以 足以讓塊狀共聚物吸附及/或吸收污染物的時間周期徹底 加以混合。混合的時間可從30秒至2小時或更長,目前較 佳的是1至10分鐘;混合時間的長短將視污染物的性質及 污染物在泥土內的時間而定。然後將此泥土及被污染物包 住之共聚物之均質混合物放至一値存儲槽中,被污染物包 住的共聚物變成粉狀或大的聚塊,此將視所使用的塊狀共 聚物而定。 第四,再將均質混合物與水混合,使被共聚物包住之 污染物及水份自土中瀝濾出來。成塊的被包住的污染物將 浮至水面上,並Μ掬取方式除去這些污染物塊,剩下的水 及泥土大致已無有機液污染物之存在。從水中回收這些污 染塊時,最好使用1/8吋至1时的網。然後再過濾水及泥 土,可得到大致上乾的泥土及分離水,而二者皆不含有機 污染物。 這些被共聚物包住的有機液污染物,在隨後的步驟中 (請先閲讀背而之法意'"項#堝"本頁) 裝- 線- 經濟部屮央標準局β工消价合作社印製 本紙張尺度逍用中®ffl家標準(CNS)T4規格(210X297公徒) 18 81. 6. 10,000張 〇〇 Λ 6 Η 6 2l〇9G^ 五、發明説明() 有再予經濟利用的價值。轚如,被塊狀共聚物包住污染物 塊可在諸如石油精、汽油、柴油或原油之類的溶劑中液化 。溶解後所產生之有機污染物-彈性聚合物-有機溶劑液 組合物則可做為工業火壚、引擎等之燃料來源。或者,此 棰包住污染物之共聚物固體亦可做為固體燃料。 在第二種回收滲入土中之有機液的方法中,係先掘出 受溢出物所污染之泥土,然後在混合器中或其他混合裝置 中與水撤底地混合,Μ便從泥土中瀝濾出污染物。其次, 過濾此混合物,可得到洗土及一種播帶或散布有機液之濾 液。然後將濾液送經諸如第1圔中所示之共聚物處理單元 11的一値熱塑性彈性共聚物吸收劑顆粒所形成之固定床 ,而將水流中的有機污染物去除。如有需要,可依據前述 之第一棰方法,對該洗土加Μ再處理,Μ除去土中之污染 物。 本發明亦係有關一棰將該熱塑性彈性塊狀共聚物處理 諸如網甲板、木甲板、水泥地之類的固體表面上之液鰻溢 出物之應用。處理的方式是Μ人工撤播或其它方法將塊狀 共聚物撤囊劑均勻的散布在溘出物之表面上。 至於決定塊狀共聚物所需之使用量,部份將視所欲吸 收及/或吸附之有機液薄膜厚度及經濟收集該液體所需的 時間而定。當此液體溢出物包含一層厚度不超過約0.5吋 的薄膜時,對於每一加侖的溢出物,塊狀共聚物的使用量 最好是介於0.1至1磅之間。塊狀共聚物包住有機液所需 的時間將隨溫度、有機液與塊狀共聚物的比例、有機液的 本紙张尺度逍用中困國家楳毕(CNS) ΤΜ規格(2】〇x297公:Ϊ) (請先閲讀背而之注意事項#填寫本頁) 裝- 經濟部屮央標準局貞工消费合作社印51 81. 6. 10,000張(Η) 2109^-3 Λ G Η 6 五、發明説明() 黏度、所使用的塊狀共聚物的表面積、及有機液留在土中 或甲板表面上的時間而異。 塊狀共聚物撒囊劑在與液齷溢出物接觸後,很快在數 秒内就開始包住液態碳氫化合物溢出物。清理厚度不超過 半时的湓出物所需的時間;,通常是Μ分鐘來計算。這些溘 出的有機液或石油有關液體,係大致完全被塊狀共聚物包 住,而使塊狀共聚物徹囊劑之表面大致保持乾燥(無油性) 、無黏性及無毒性。這有助於使用諸如用耙聚攏、掃帚掃 除等方法收集被包住的有機液與塊狀共聚物。 請參考第4圖,本發明亦係有關一種防止有機污染物 從一個地下燃料槽滲入其下之泥土的方法。在此方法中* 一値泥土 /塊狀共聚物混合物60是由第一種數量之泥土與 前述之一種塊狀共聚物徹底地混合所產生。其次,將此泥 土 /塊狀共聚物混合物60放置於土 63中所挖掘的洞62之底 部。然後,將一痼地下燃料槽64適切地放置在該泥土 /塊 狀共聚物混合物60上,再用第二種數量之泥土 66填入洞62 內。 經濟部屮央榣準而员工消费合作社印製 (請先間讀背而之:¾¾事項再项寫本頁) 如果有機流體68從地下燃料槽64漏出,它們可能往下 滲透通過第二棰數量之泥土 66,即被泥土 /塊狀共聚物混 合物60中之塊狀共聚物吸收及/或吸附。如有需要,可將 泥土 /塊狀共聚物混合物60直接放在楢64底下,則自槽64 漏出之任何有機液將直接摻入泥土 /塊狀共聚物混合物60 内。因此,本法可防止地下燃料槽64內之有機液68,滲入 其下之泥土 63內。 本紙張尺度遑用中困囷家樣iMCNS)甲4規怙(2〗0χ2ί)7公«) - 20 - 81. 6. 1〇,〇〇〇張(Η) Λ 6 η 6 2109^2 五、發明説明() (請先閲讀背而之注意事項孙项寫本頁) 同樣地,謓參考第5圖,本發明亦係有關一種防止從 一値油井70的井源72處漏出或溘出之有機污染物滲入井源 72周圍泥土之方法。在此方法中,井源72是被前述之泥土 /塊狀共聚物混合物構成之環狀體74所包圍。而從油井70 的井源72處所漏出或溢出之油及其它有機污染物可被回牧 ,因為該泥土/塊狀共聚物混合物中之塊狀共聚物會在它 們自井源72漏出或溢出時吸收及/或吸附諸污染物。如此 乃防止任何此類污染物滲入井源72附近的泥土中。如有需 要,可在井源72附近的區域挖堀至所需之深度,然後填入 該泥土/塊狀共聚物混合物。換言之,由泥土/塊狀共聚 物混合物所形成之環狀體74可爲任何需要之深度。 現Μ下列實例對本發明做進一步的說明: 奮例1 : 經濟部屮央標準局β工消"合作杜印製 將直徑0.5时之單一固定床吸收塔,《入體積約100毫 升的粉狀PS 3200吸收劑(美國密西根州大急流市的Micro Environmental公司所出售的一種塊狀共聚物)至約30吋 之深度。然後將受汽油污染的水(每升溶液中,大約含有 0.6克的AM0C0銀级無鉛汽油)Μ每小時12床體積(bed volumes,BV)的速率通過該吸收塔,其中,床體積的定義 是一個與吸收塔中之塊狀共聚物體積相等之體積(亦即, 100毫升)。因此,進给速率是1.2升/小時。 依據EPA方法602(V0A),测量吸收塔在經過1 2/3、 3 1/3、6 2/3、10及13 1/3小時的作用後,其流出的污 水流中,成份移除之百分比(柑對於未處理之水流),並將 81. 6. 10.000張(Η) 本紙張尺度边用中a Η家揉準(CNS)T4規格(210X297公;ft) 2i〇9^^ 五、發明説明() 結果列於下表: Λ 6 Π 6 %成份移除 污染物 1 2/3 小時 3 1/3 小時 6 2/3 小時 10 小時 13 1/3 小時 ΜΤΒΕ(甲基· 3 31.6 59.6 33.0 41.6 13.4 级丁基醚) 苯 99.4 93.1 76.9 81.4 79.0 甲苯 100.0 100.0 99.5 96.6 91.7 乙苯 100.0 100.0 100.0 100.0 100.0 二甲苯 100.0 100.0 100.0 100.0 100.0 (請先閲讀背而之注意事項再蜞寫本頁) 經濟部屮央櫺準局员工消奸合作社印製 如預期所料,像苯及甲苯之類揮發性較高的成份,較 快通過吸收塔。在測試時,未曾顯示任何通過吸收塔之壓 降有增加的情形。此外,也未發現塊狀共聚物有熔融或 “融化”的現象(汽油與塊狀共聚物之間起作用,不同於 吸收及/或吸附)。因此,該吸收劑之物理反應情形與在 其它吸附型之吸收塔条統所觀察到的情形類似。 奮俐2 : 重複實例1的處理過程,不過M PS 3400吸收劑(美國 密西根州大急流市的Micro Environment公司所出售的一 種塊狀共聚物 >替代PS 3200吸收劑裝入吸收塔内。然而, 本紙張尺度逍用中租B家標準(CNS)甲4規格(210x297公;ft) 81. 6. )0,000張(Η) Λ 6 Η 6 五、發明説明() 流出污水的初步測試顯示,由於揮發性的有機化合物(苯 、甲苯、乙苯、及二甲苯)與實例1使用PS 3200的實驗比 較起來,相當快就通過吸收塔,所Μ测試在3 3/1小時後 即結束。 吸收塔在作用1 2/3及3 1/3小時後,测得之流出污水 內之成份移除百分比(相對於未處理水流)列於下表。由結 果可看出,在實例1中使用的吸收劑PS 3200較PS 3400效 果爲佳。 (請先閲讀背而之注意事項#堝寫本頁) 經濟部屮央標準局貝工消赀合作社印3i 污染物 %成份移除 1 2/3小時 3 1/3小時 ΜΤΒΕ 19.0 78.8 苯 84.5 83.6 甲苯 93.8 94.0 乙苯 97.1 97.5 二甲苯 96.7 97.1 音例3 : 爲決定PS 3200及PS 3400在一個單階段分組接觸糸統 中,自水中移除汽油的效率,乃先決定每一値塊狀共聚物 之極限吸附及/或吸收性能。由於發現這些塊狀共聚物在 與濃縮之汽油溶液接觭後,會有熔融或融化之趨向,所以 裝- 訂- 線· 本紙51c尺度边用中國Η家樣準(CNS)T4規格(210x297公:B:) 81. 6. 10,000張(Η) fj Λ (5 Π 6 五、發明説明( 使用下列的程序來決定極限性能: U)將一特定量的汽油加入過量的聚合物中,使其能作用 數小時; (b) 移去和汽油起反應而熔融或融化之塊狀共聚物,然後 將未反應之塊狀共聚物稱重;及 (c) 將塊狀共聚物之總重量減去未反應之塊狀共聚物之重 量,即可確定起反應之(熔融或融化)塊狀共聚物的重 量0 性能測試的結果如下: 材料 汽油 起反應之聚 性能(汽油(公克) (公克)合物(公克〉/聚合物(公克>) (請先閲讀背而之注意事項一φ堝寫本頁) 裝- PS 3200 PS 3400 5. 5. 4 4, 1.04 1.25 線- 經濟部屮央標準局β工消赀合作杜印製 對於某一特定的吸收劑量,PS 3400材料所吸收的汽 油量較PS 3200材料為多。在測試時,發現PS 3400材料似 乎比PS 3200材料有較大之"熔融”程度。這對於在吸收 塔型的方法中,PS 3200優異的表現,提供了一些解釋; 在此型方式中,吸收劑未被移動,且希望熔融的情形能減 至最低,以避免產生可能的吸收床阻塞或液體通道。 決定了吸收劑的極限性能後,在吸收劑及污染水之間 ,施行一餹單階段、分組等溫、接觸之處理過程,其步驟 匕紙張尺度边用中8 8家楳準(〇肊)肀4規格(2丨0><297公龙) 81. 6. 10,000張(H) Λ 6 Η 6 五、發明説明() 如下:首先,M Amoco銀级無鉛汽油污染蒸餾水,將產生 之污染水溶液各二公升分別放入二個容器中;在每一艏容 器裡,其濃度為每公升溶液含有0.6公克汽油。其次,將 第一種劑量的吸收劑(粉狀 >,它相當於Μ 100%吸附效率 回收所有汽油所需之量(對於PS 3200吸收劑,所計算出之 量為0.6公克/公升),加入第一個二公升溶液中,再將等 於第一種劑量的二倍的第二種劑量之吸收劑加入第二値二 公升溶液中。 然後將每一個試樣在旋轉滾筒中混合約16小時,混合 完畢後,分別從每値容器中取出試樣水,然後以ΕΡΑ方法 602 (V0A)分析“ΒΕΤΧ”(“苯、甲苯、乙苯、二甲苯”)污 染物。其成份移除之百分比顯示如下: %成份移除 (請先閲讀背而之注意事項#填寫本頁) 裝. 訂· 線< 經濟部屮央標準局员工消枰合作社印製 污染物 聚合物第1種劑量 (0.6公克/公升) 聚合物第2種劑量 (1_2公克/公升) 苯 27.8 33.6 甲苯 46.5 50.4 乙苯 62.8 66.4 二甲苯 65.5 68.5 本紙張尺度边用中國國家標準(CNS)Ή規格(210x297公龙) 81. 6. 10,〇〇〇張(Η) 經濟部中央標準局员工消"合作社印製 2l〇9^^; 五、發明説明() 奮例4·: 重複實例3的處理過程,但是以PS 3400吸收劑取代 PS 3200吸收劑。同時,將相當於M100%吸附效率回收所 有汽油所需之量的第一種劑量之吸收劑(對於PS 3400吸收 劑,所計算出之量為0.5克/升),加入第一値受汽油污染 的二公升水溶液中。再將等於第一種劑量的二倍的第二種 劑量之吸收劑加入第二値受汽油污染的二公升水溶液中。 在試樣混合完畢後,將容器從混合滾筒中移出,然後分析 污染物之去除情形。其成份移除之百分比顯示如下: A 6 Π 6 (請先間讀背而之注意事項典项寫本頁) %成份移除 裝- 污染物 聚合物第1種劑量 (0.5公克/公升) 聚合物第2種劑量 (1.0公克/公升) 苯 20.8 24.2 甲苯 37.4 43.2 乙苯 54.9 60.7 二甲苯 58.2 63.4 在檢査實例3及實例4中之單階段分組接觸方法中吸 收劑之有效性時,可以發現PS 3200及PS 3400二種吸收劑 均除去一部份之汽油成份,其中PS 3200較為有效。其次 ,實驗結果顯示將吸收劑的劑量增加一倍時,並未顯著增 本紙张尺度逍用中租困家樣毕(CNS)T4規格(210X297公A) 26 81. 6·〗0,000張(H) Λ 6 η 6 21090^ 五、發明説明() (請先閲讀背而之注意事項再碣寫本頁) 加汽油污染物之移除效果。第三,顯而易見的,實例3及 實例4的單階段分組接觭方法,移除水溶液中汽油成份的 效果比不上實例1及實例2的吸收塔接觸方法。 奮例Η : Μ—値改良的具有進水及拂水分布幹管的55加侖圓筒 擴大實例1之處理過程。吸收塔內可填入大約50加侖的PS 3200吸收劑(約140磅)。而擴大的流動速率(根據實例1中 所測試之12 BV/hr的速率來換算)約為10加侖/分鐘。通 過吸收塔之預期壓降將小於3 psig。 謇俐: 將半杯無鉛汽油溢灑在修車廠的地上,再將一種塊狀 共聚物微囊劑(PS 3400)撤在溘出物的表面。在大約15秒 内,這些溘出汽油卽被共聚物包住。 謇例7 : 重複實例6的處理過程,但是使用10-W30機油代替無 鉛汽油,獲得大致類似的實驗結果。 啻例8 : 經濟部屮央標準^β工消赀合作社印51 將100公克未被污染的泥土(IR認可)與10公克的2號 柴油混合,產生一値污染泥土試樣。然後將10公克的PS 3200吸收劑與被污染的泥土試樣混合30分鐘,產生一値均 質組合物。再將此均質組合物與1公升去離子水混合二痼 小時,使此均質組合物在水中瀝濾。在瀝濾的步驟完成時 ,被包住的污染物塊會上升至水面,可用網在水面撇取, 去除這些污染物塊。然後將剩餘的試樣過濾,再使用配有 81. 6.队000張⑻ 本紙张尺度逍用中囲國家標準(CNS) Τ4規格(210X297公逄) u- Λ 6 H6 經濟部中央櫺準局员工消设合作社印製 五、發明説明( 一値fid偵測器的氣體色譜儀適度分析過濾液中之揮發性 有機污染物(苯、甲苯、乙苯、及二甲苯)。分析結果顯示 此過濾液不含任何可測出之揮發性有機污染物。因此,揮 發性有機污染物的含量不雇過lOppb (十億分之十)。 奮例9 : 重複實例8的處理過程,但是受污染的泥土試樣與吸 收劑混合的時間由30分鐘延長至二小時,獲得相同的結果 〇 審'例1 0 : 將受2加侖無鉛汽油污染的20加侖表土送入一個帶式 混合器中,再將實例1使用的撒囊劑約3加侖與受污染表 土一起混合,產生一個大致上均質的组合物,將此均質組 合物放入一個100加侖的存儲槽內。再用50加侖的自來水 與此均質組合物混合。當被包住的污染物塊浮至存儲槽的 水面上時*使用樹葉耙將它們撇除,然後测試留在榷中的 水和泥土,發現大致上它們將不含無鉛汽油。 啻例11 : 在本實驗中,將海水置於玻璃容器内,然後將數量足 以在水面上形成半吋厚薄膜的科威待原油倒在該海水上。 將經過固體疏水性矽土(Aerosil R 974)處理過的塊狀共 聚物(Kraton G-1650)散布在原油的表面,形成大約1/8吋 的厚度,然後攪動使其進入原油薄膜内。在不到1分鐘的 時間内,本發明之塊狀共聚物組合物即把原油完全包住, 形成一値乾燥固體浮在海水面上。由於這種乾燥固體外表 各紙张尺度逍用中國B家標毕(CNS) T4規怙(210X297公龙) 81. 6. 10,〇〇〇張(H) (請先閲讀背而之注意事項再填窍本頁) 裝· 經濟部中央標準而貝工消费合作杜印製 Λ 6 Π 6 五、發明説明() 不含油漬,所Μ很容易自海水面上去除。海水在除去乾燥 固體後,變得清澈而無原油殘留。使用未經處理的Kraton G-1650塊狀共聚物處理上述之科威特原油薄膜,則需要大 約1-1/2分鐘的時間包住原油湓出物。 審例1 2 : 重複實例Π的處理過程,不過使用淡水代替海水,獲 得大致相同的結果。 音俐1 3 : 重複實例12的處理過程,不過使用無鉛汽油代替科威 特原油,獲得大致相同的結果。 審例U : 再重複實例12的處理過程,不過使用一種10-W-30潤 滑油代替科威特原油,實驗結果大致相同,且用本發明之 撒囊劑處理過的水中完全不含污染物。 窗例1 5 : 再重複實例12的處理過程,但分別使用下列污染物代 替科威特原油:柴油、庚烷、密封用油、變壓器油、JP-5 噴射發動機燃料、液壓油及變速器油。而每一種實驗,都 獲得大致相同的結果,且水中也大致不含磺氫化合物污染 物。在所有的實驗中,使用本發明之組合物包住碩氫化合 物所需的時間要比使用未經處理的組合物快25%。 啻例1 fi : 一條全長32呎裝配二個船内柴油引擎且有20〜30加侖 的船腹槽之船,以周長約4时及長度約48吋而內裝實例11 本紙张尺度逍用中國Η家標毕(CN5}f4規格(2】0X297公龙) 81. 6· 10,〇〇〇張(H) (請先閲讀背而之注意事項#填寫本頁) 裝· 線. Λ 6 Β 6 經濟部屮央標準屌貝工消奸合作社印製 幺1〇分- 五、發明説明() 中使用之本發明组合物的船腹袋處理污染。該船腹袋在需 要替換Μ前,共可有效的移去2夸特的污染油。而在使用 當中,船腹袋可使船腹內之水大致不含油污染物。 窗例1 7 : 一痼小內陸湖的湖面被大約1/4吋厚的柴油油跡覆蓋 了 1/4畝的區域,爲保護湖岸免受油跡污染,使用一艏可 讓水通過的欄木,其中各傾拥木構件填滿實例11中使用的 本發明組合物,並将櫊木置於湖岸及油跡之間。首先用小 船在朝向湖岸的油跡邊緣上,噴漏實例11中所使用的本發 明之組合物,然後繞著油跡,從油跡邊緣朝向中心繼續噴 灑本發明之組合物。處理污染所使用的組合物量,大約是 根據所計算之溢出物重量的20%。在四小時內,油污大致 完全被包住。然後使用一個1/8吋的網撈取水中的這些包 住油污的碎塊。回收的碎塊在石油精中溶解,形成一種液 態柴油-橡膠石油精組合物。然後將此組合物裝入55加侖 的網筒中,可供做為工業熱水爐的燃料。 奮例1 8 : 在本例中,一個裝配平行過濾器筒及適當的管路與閥 的船腹泵,先利用其中一値過濾器去除船腹水中的污染物 ,而第二値過濾器則在隨時待命的狀態,當第1値過濾器 在整修時,它即可替補上線蓮作。每一個過濾器筒所裝填 的實例11中使用的本發明之撤囊劑之量,足夠包住大約2 - 1/2夸特的碳氫化合物污染物。當通過過濾器的壓降相 當於包住大約2夸待的污染物時,条統會產生一値適當的 (請先閲讀背而之注意事項再埸寫本頁) 裝- 訂- 本紙張尺度边用中曲Η家標华(CNS) Ή規格(210x297公 81. 6. 10,〇〇〇張(Η) 經濟部屮央榣準釣C5工消奸合作社印製 五、發明説明() 警示,此時,便可用第二個過濾器替換,然後清洗第1個 過濾器。如果不及時替換過濾器,過濾器將繼續作用,直 到壓降使船腹泵自動停止不再工作為止。此船腹泵過逋条 統如此蓮作約6値月,可使環境中的污染物大致均無法倖 免。 因此,本發明提供從泥土、水流及固體表面回收有機 液或石油有鼷液體的高效率方法。在此等方法中所使用的 塊狀共聚物可迅速地吸收及/或吸附湓出之有機液或石油 有關液體。在這些有機液或石油有關液體被吸收及/或吸 附後,此包住有機液之塊狀共聚物可Μ很容易地被回收, 至多留下撤量的溘出有機液或石油有關液體。含有被回收 之有機液的回收共聚物可再被用作為固作燃料,或將其溶 解在各棰液體燃料中,形成一種燃料油,如此更可避免昂 貴的掩埋或清理之問題。此外,由於有機液被共聚物包住 ,會提高有機液的燃燒溫度(降低其燃點〉。 構件表 10. 船腹泵 11. 共聚物處理單元 12. 共聚物吸收劑床 14.共聚物吸收劑床 16.船腹出口管 18.船腹 20.處理單元進入管 22.處理單元進入管 (請先閲讀背而之注意事項洱硝寫本頁) 裝- 本紙張尺度逍用中a S家樣準(CNS) Τ4規格(210X297公放) 81. 6. 10,000張(H) A 6 Π 6 五、發明説明() 23 ·壓力表 24.三通閥 26.處理單元出口管 28.三通閥 30.容器進入管 32.壓力表 34.處理液容器 36.筒出口管 40.空氣汽提塔 42.臭氧處理單元 44.紫外線照射處理單元 46.活性碩處理單元 48.進入水流 50.出口水流 60.泥土 /塊狀共聚物混合物 62. 所挖掘之洞 63. 周圍泥土 64. 地下燃料槽 經济部中央榣準局貝工消"合作社印製 (請先閱讀背而之注意事項#塡寫本頁) 66.第二種數量之泥土 68.有機流體 70.油井 72.井源 74.環狀體 本紙张尺度逍用中國B家標準(CNS)T4規格(210X25)7公;«:) 81. 6. 10,000張(H)I The pressure from the Ministry of Economic Affairs and the standard printed by the A Co-operative Cooperative Society has been reduced. When the pressure drop across the copolymer absorbent bed 12 is equivalent to entrapment of approximately 2 quarts of contaminants, an appropriate warning is generated, at which point the operator can allow the second copolymer absorbent bed 14 to replace the lotus. , And the fixed bed particles in the first value copolymer absorbent bed 12 are regenerated. By turning the three-way valve 24, the second copolymer absorbent bed 14 can be used as a clematis. After that, the contaminated organic liquid will flow through the treatment unit into the pipe 22 instead of the treatment unit into the pipe 20. The treated liquid flowing out of the copolymer absorbent bed 14 will enter the outlet pipe 36. The three-way valve 28 should be converted to allow the treatment liquid flowing through the outlet pipe 36 to be introduced to 81. 6. 10, 000 sheets (H). This paper size is used in the BB Home Sample (CNS) T4 regulation ( (210x297 male dragon) 210902_Λβ_ V. Description of the invention () The container enters the tube 30. After several months of construction of this aft filter system, no pollutants will remain in the environment. However, if the fixed bed particles in the copolymer absorbent bed used are not regenerated in a timely manner, the fixed bed will only continue to apply iron to the pressure of the treated fluid in the vessel inlet pipe 30, and cannot maintain the proper pumping time of the stern pump 10. At this time, the cavitation pump 10 will cause a large cavitation phenomenon. The Ministry of Economic Affairs Standard ^ ΕΞζ Gongxiaozhong Cooperative printed the first test data to indicate that the value of the copolymer processing unit 11 as shown in Figure 1 can be arranged in series, which will result in continuous high pollution Removal effect. Alternatively, referring to FIG. 2, another combination can be seen, which includes one or more copolymer processing units 11, one or more air stripping unit 40, one or more ozone treatment units 42, one or The multi-value ultraviolet irradiation treatment unit 44M and the one- or multi-value active treatment unit 46, which are arranged in series with M, use M to remove pollutants entering the water stream 48 and produce a non-polluting outlet water stream 50. Of course, a combination rule does not necessarily include all these units, it can be any combination of these units. For example, the ozone treatment unit 42 is more suitable for use when killing bacteria entering the water stream 48 or removing gold jelly in the water stream. The ultraviolet irradiation treatment unit 44 is also suitable for killing bacteria. The decision to use a series of polymer absorbent units or some form of combination system will depend on the nature of the pollutants, the degree of removal required, and the cost of the associated components. For example, to treat a water stream that is mainly contaminated with lower volatile compounds such as xylene, from a technical and economic point of view, polymer treatment alone is good. If you use a combination type system to deal with gasoline-contaminated water flow, then use 81. 6. 10,000ft (Η) (please read the back to the precautions # hard to write this page) This paper scale is used in the BB family standard ( CNS) 〒4 gauge (210x297 public goods) Λ ίϊ Π 6 Printed by the Ministry of Economic Affairs, Central Bureau of Industry and Commerce, A Industrial and Consumer Goods Cooperative V. Description of the invention () Before using a unit of air stripping tower, firstly copolymerize The material treatment unit pre-treating the water stream may remove a large amount of benzene and toluene, as well as substantially all lower volatile compounds such as xylene. This will reduce the A load of the processing tower containing the active master and increase the life of the activated carbon. In this way, since the cost of active sulphur can be greatly reduced, this combined treatment method can result in a lower overall treatment cost. In addition, in the treatment systems currently used commercially, activated carbon treatment units are generally used. Because the active processing unit constitutes an approved filter medium. However, the active bed must be regenerated almost every day, adding considerable cost. When a copolymer treatment unit and an active sulfonation treatment unit are connected in series and placed in front of the active nitrate treatment unit, the active base in the active master treatment unit needs to be regenerated approximately every 1 to 2 weeks. Using this combination treatment system, the copolymer in the copolymer processing unit needs to be regenerated approximately every 3 to 4 days, and the cost of regeneration is lower than that of the activated carbon bed. The present invention also relates to a method of using a sulfohydrogen compound fluid that is encapsulated in a thermoplastic rubber block copolymer and recovered from water. This method is to dissolve the fluid of the compound of haze which is covered by thermoplastic rubber in a solvent such as petroleum spirit, gasoline, diesel oil and crude oil, to form a thermoplastic rubber-hydrogen compound suitable for use as fuel for furnaces, engines, etc. Fluid-petroleum liquid composition. In other words, in this dissolution step, the thermoplastic rubber will also be dissolved by the solvent. This thermoplastic rubber-hydrogen compound fluid-petroleum liquid composition can then be burned in a fire or used as a fuel in an engine. In the process of dissolution, it is best to heat the solvent to promote the dissolution of the sulfohydrogen compound fluid covered by the thermoplastic rubber in the solvent. (Please read the back-to-back precautions for Sun Xiang to write this page) Binding and Strapping-This paper standard is used in a Η family sample standard (CHS) specifications (210X297 public; ¢) _ _ 81. 6. 10,000 sheets ( H) Λ ίί Η 6 2109 ^ 2 V. Description of the invention () The present invention also relates to two methods for recovering organic liquid, especially hydrogen compounds, that have penetrated into the soil. Please refer to Figure 3. In the first method, the soil contaminated by the debris is first excavated and put into a mixer such as a belt mixer. Secondly, one of the aforementioned bulk copolymer decapsulation agents M and the contaminated soil in the mixture is added to the mixer in a weight ratio of approximately 1:10 to 1: 1, preferably 1: 1. In addition, it is advisable to add some fresh hydrogen compounds to the soil in the mixer and the decontamination agent to activate the pollutants of the organic liquid. Third, the contaminated soil and the block copolymer are encapsulated in the mixer for a time period sufficient for the block copolymer to adsorb and / or absorb the contaminants. The mixing time can be from 30 seconds to 2 hours or longer, currently preferably 1 to 10 minutes; the length of the mixing time will depend on the nature of the pollutant and the time the pollutant is in the soil. Then the homogeneous mixture of the soil and the copolymer coated with contaminants is put into a storage tank, and the copolymer covered with contaminants becomes powdery or large agglomerates, which will be copolymerized depending on the block used It depends on the thing. Fourthly, the homogeneous mixture is mixed with water to leaching the pollutants and water enclosed by the copolymer from the soil. The clumps of encapsulated pollutants will float to the surface of the water, and these pollutant blocks will be removed by M grabbing. The remaining water and soil are almost free of organic liquid pollutants. When recovering these contaminated blocks from the water, it is best to use a net from 1/8 inch to 1 hour. Then the water and mud are filtered to obtain substantially dry mud and separation water, both of which do not contain organic pollutants. These organic liquid contaminants encapsulated by the copolymer will be installed in the subsequent steps (please read the counter-product's "#quotation" page #) at this time. Printed by the price cooperative, the paper standard is used in the FFL family standard (CNS) T4 specification (210X297) 18 81. 6. 10,000 sheets 〇〇Λ 6 Η 6 2l〇9G ^ V. Invention description () The value of economic use. For example, the contaminant mass surrounded by the block copolymer can be liquefied in solvents such as petroleum spirits, gasoline, diesel, or crude oil. The organic pollutant-elastic polymer-organic solvent liquid composition produced after dissolution can be used as a fuel source for industrial fire engines and engines. Alternatively, the copolymer solids that enclose the pollutants can also be used as solid fuels. In the second method of recovering the organic liquid infiltrated into the soil, the soil contaminated by the spillage is first excavated, and then mixed with the water in the mixer or other mixing device, and then Μ is leached from the soil Filter out contaminants. Secondly, the mixture is filtered to obtain washing soil and a filter solution for spreading or spreading organic liquid. The filtrate is then passed through a fixed bed of thermoplastic elastomeric copolymer absorbent particles such as the copolymer processing unit 11 shown in the first section to remove organic contaminants from the water stream. If necessary, according to the first method described above, the washed soil can be treated with M to remove contaminants in the soil. The present invention also relates to the use of the thermoplastic elastomer block copolymer to treat liquid eel spills on solid surfaces such as net decks, wooden decks, and concrete floors. The treatment method is to manually disperse the bulk copolymer decapsulation agent on the surface of the exudate by manual withdrawal or other methods. As for determining the amount of the block copolymer required, it will depend in part on the thickness of the organic liquid film to be absorbed and / or absorbed and the time required for economical collection of the liquid. When the liquid spill contains a film no thicker than about 0.5 inches, the amount of block copolymer used is preferably between 0.1 and 1 pound for each gallon of spill. The time required for the block copolymer to encase the organic liquid will vary with temperature, the ratio of the organic liquid to the block copolymer, and the size of the organic liquid on this paper. The CNS TM specifications (2). : Ϊ) (please read the back-end precautions # fill out this page) installed-printed by the Zhenyang Consumer Cooperative Society, Bureau of Standards, Ministry of Economic Affairs 51 81. 6. 10,000 sheets (Η) 2109 ^ -3 Λ G Η 6 5. Description of the invention () The viscosity, the surface area of the block copolymer used, and the time the organic liquid remains in the soil or on the deck surface vary. The block copolymer encapsulant comes into contact with liquid spills and soon begins to contain liquid hydrocarbon spills within seconds. The time required to clean the decanter with a thickness not more than half a hour; usually calculated in M minutes. These organic liquids or petroleum-related liquids are almost completely covered by the block copolymer, and the surface of the block copolymer capsules is kept almost dry (non-oily), non-sticky and non-toxic. This helps collect organic liquid and block copolymers, such as gathering with a rake and sweeping with a broom. Referring to FIG. 4, the present invention also relates to a method for preventing organic pollutants from seeping into the soil underneath an underground fuel tank. In this method, a soil / block copolymer mixture 60 is produced by thoroughly mixing the first amount of soil with the aforementioned block copolymer. Next, this soil / block copolymer mixture 60 is placed at the bottom of the hole 62 excavated in the soil 63. Then, a subterranean fuel tank 64 is properly placed on the earth / block copolymer mixture 60, and then the second amount of earth 66 is filled into the hole 62. Printed by the Ministry of Economic Affairs and printed by the Employee Consumer Cooperative (please read back and forth: ¾¾ Matters and then write this page) If the organic fluid 68 leaks from the underground fuel tank 64, they may penetrate down through the second volume The soil 66 is absorbed and / or adsorbed by the block copolymer in the soil / block copolymer mixture 60. If necessary, the soil / block copolymer mixture 60 can be placed directly under the sill 64, and any organic liquid leaking from the tank 64 will be directly incorporated into the soil / block copolymer mixture 60. Therefore, this method can prevent the organic liquid 68 in the underground fuel tank 64 from seeping into the soil 63 underneath. The size of this paper is not the same as the iMCNS (4〗 0χ2ί) 7 Gong «)-20-81. 6. 1〇, 〇〇〇 sheets (Η) Λ 6 η 6 2109 ^ 2 5 2. Description of the invention () (Please read the notes on the contrary to Sun Xiang to write this page) Similarly, referring to FIG. 5, the present invention also relates to a method for preventing leakage or leakage from the wellhead 72 of Yiyou oil well 70 The method of infiltrating the organic pollutants into the soil around the well source 72. In this method, the well source 72 is surrounded by the ring 74 composed of the aforementioned soil / bulk copolymer mixture. The oil and other organic contaminants leaked or spilled from the wellhead 72 of the oil well 70 can be returned to the pasture, because the bulk copolymer in the soil / bulk copolymer mixture will leak out or overflow from the wellhead 72 Absorb and / or adsorb pollutants. This is to prevent any such contaminants from seeping into the soil near the well source 72. If necessary, the area near the wellhead 72 can be dug to the desired depth and then filled with the soil / block copolymer mixture. In other words, the ring 74 formed from the soil / bulk copolymer mixture can be any desired depth. Now the following examples will further illustrate the present invention: Example 1: Pingyang Standard Bureau, Ministry of Economic Affairs β Gongxiao " Cooperative Du Printing Co., Ltd., a single fixed bed absorption tower with a diameter of 0.5, into a powder with a volume of about 100 ml PS 3200 absorbent (a block copolymer sold by Micro Environmental Corporation of Grand Rapids, Michigan, USA) to a depth of about 30 inches. Then the water contaminated with gasoline (containing about 0.6 grams of AM0C0 silver grade unleaded gasoline per liter of solution) Μ 12 bed volumes (BV) per hour through the absorption tower, where the bed volume is defined A volume equal to the volume of the block copolymer in the absorption tower (ie, 100 ml). Therefore, the feed rate is 1.2 liters / hour. According to EPA method 602 (V0A), after measuring the absorption tower after 1 2/3, 3 1/3, 6 2/3, 10 and 13 1/3 hours, the components in the sewage stream flowing out of it are removed. Percentage (for oranges for untreated water flow), and use 81. 6. 10.000 sheets (Η) of the size of this paper in the standard a Η home rubbing (CNS) T4 specification (210X297; ft) 2i〇9 ^^ V. Description of the invention () The results are listed in the table below: Λ 6 Π 6% ingredients remove contaminants 1 2/3 hours 3 1/3 hours 6 2/3 hours 10 hours 13 1/3 hours MTB (Methyl 3 31.6 59.6 33.0 41.6 13.4 grade butyl ether) Benzene 99.4 93.1 76.9 81.4 79.0 Toluene 100.0 100.0 99.5 96.6 91.7 Ethylbenzene 100.0 100.0 100.0 100.0 100.0 Xylene 100.0 100.0 100.0 100.0 100.0 (Please read the precautions before writing this page) Economy The Ministry of Health, People's Liberation, and Employee Counsel Cooperatives printed as expected, and the more volatile components like benzene and toluene passed through the absorption tower faster. During the test, there was no indication of any increase in pressure drop across the absorption tower. In addition, no melting or “melting” of the block copolymer was found (the interaction between gasoline and the block copolymer is different from absorption and / or adsorption). Therefore, the physical reaction of the absorbent is similar to that observed in other absorption-type absorption tower systems. Fenli 2: The process of Example 1 was repeated, but M PS 3400 absorbent (a block copolymer sold by Micro Environment Corporation of Grand Rapids, Michigan, USA) replaced the PS 3200 absorbent in the absorption tower. However, the standard of this paper is to use the China Rent B Standard (CNS) Grade A specification (210x297 g; ft) 81. 6.) 0,000 sheets (Η) Λ 6 Η 6 5. Description of the invention () Preliminary test of the outflow of sewage Since the volatile organic compounds (benzene, toluene, ethylbenzene, and xylene) were compared with the experiment using PS 3200 in Example 1, they passed the absorption tower quite quickly, and the M test ended after 3 3/1 hours . After 1 2/3 and 3 1/3 hours of the absorption tower, the measured percentage removal of components in the outflow sewage (relative to the untreated water flow) are listed in the table below. From the results, it can be seen that the PS 3200 absorbent used in Example 1 is more effective than the PS 3400. (Please read the back and the precautions ## to write this page) The Ministry of Economic Affairs, Bureau of Standards, Beigong Consumer Cooperatives Cooperative 3i Contaminant% component removal 1 2/3 hours 3 1/3 hours MTBE 19.0 78.8 Benzene 84.5 83.6 Toluene 93.8 94.0 Ethylbenzene 97.1 97.5 Xylene 96.7 97.1 Example 3: To determine the efficiency of PS 3200 and PS 3400 in a single-stage group contact system to remove gasoline from water, each block copolymer was determined first The ultimate adsorption and / or absorption performance. Since it is found that these block copolymers will tend to melt or melt after being exposed to the concentrated gasoline solution, so the binding-binding-line · 51c scale of this paper uses the Chinese HJ standard (CNS) T4 specification (210x297 : B :) 81. 6. 10,000 sheets (Η) fj Λ (5 Π 6 V. Description of the invention (use the following procedure to determine the ultimate performance: U) Add a specific amount of gasoline to the excess polymer to make it Can act for several hours; (b) Remove the block copolymer that reacts with gasoline to melt or melt, and then weigh the unreacted block copolymer; and (c) Subtract the total weight of the block copolymer The weight of the unreacted block copolymer can determine the weight of the reacted (melted or melted) block copolymer. The results of the performance test are as follows: The polymerization performance of the material gasoline (gasoline (gram) (gram)) Objects (grams> / polymers (grams>) (please read the precautions on the first page to write this page) Pack-PS 3200 PS 3400 5. 5. 4 4, 1.04 1.25 Line-Ministry of Economic Affairs Standard The Bureau of β-Work Consumer Cooperation cooperates to print the PS 3400 material for a specific absorbed dose The amount of gasoline absorbed is more than the PS 3200 material. During the test, it was found that the PS 3400 material seems to have a greater "melting" degree than the PS 3200 material. This is for the excellent performance of the PS 3200 in the absorption tower type method. Some explanations are provided; in this type of method, the absorbent is not moved, and it is hoped that the melting will be minimized to avoid possible absorption bed blockage or liquid passage. After determining the ultimate performance of the absorbent, after absorption Between the agent and the contaminated water, a single-stage, grouped isothermal, contact treatment process is carried out. The steps are as follows: the paper scale is used in 8 or 8 揳 樳 計 (〇 肊) 言 4 specifications (2 丨 0> < 297 Male dragon) 81. 6. 10,000 sheets (H) Λ 6 Η 6 V. Description of invention () The following are: First, M Amoco silver-grade unleaded gasoline contaminates the distilled water, placing two liters of the resulting contaminated aqueous solution in two containers respectively ; In each bow container, the concentration is 0.6 grams of gasoline per liter of solution. Second, the first dose of absorbent (powder>, which is equivalent to the amount of 100% adsorption efficiency required to recover all gasoline (For PS 320 0 absorbent, the calculated amount is 0.6 g / L), add to the first two liter solution, and then add the second dose of absorbent equal to twice the first dose to the second two liter solution Then each sample is mixed in a rotating drum for about 16 hours. After the mixing is completed, the sample water is taken out from each container separately, and then the "BETX" ("benzene, toluene, Ethylbenzene, xylene ") pollutants. The percentage of its component removal is shown as follows:% component removal (please read the back-end notes # fill out this page) to install. Order · Line < Ministry of Economic Affairs, Bureau of Standards, Employee Consumer Cooperative Printed Pollutant Polymer The first dose (0.6 g / L) The second dose of polymer (1_2 g / L) Benzene 27.8 33.6 Toluene 46.5 50.4 Ethylbenzene 62.8 66.4 Xylene 65.5 68.5 This paper uses the Chinese National Standard (CNS) Ή specifications ( (210x297 male dragon) 81. 6. 10,000 sheets (Η) Printed by the Central Bureau of Economic Affairs of the Ministry of Economic Affairs " Cooperative printed 2l099 ^^; Fifth, the invention description () Endeavour Example 4: Repeat Example 3 Treatment process, but replace the PS 3200 absorbent with PS 3400 absorbent. At the same time, add the first dose of absorbent equivalent to the amount required for M100% adsorption efficiency to recover all gasoline (for PS 3400 absorbent, the calculated amount is 0.5 g / L), add the first value to gasoline contamination In two liters of aqueous solution. A second dose of absorbent equal to twice the first dose was added to the second two-liter aqueous solution contaminated with gasoline. After the sample is mixed, remove the container from the mixing drum and analyze the removal of contaminants. The percentage of its component removal is shown as follows: A 6 Π 6 (please read back to the precautions before writing this page)% component removal equipment-the first dose of pollutant polymer (0.5 g / L) Polymerization The second dose of the substance (1.0 g / L) Benzene 20.8 24.2 Toluene 37.4 43.2 Ethylbenzene 54.9 60.7 Xylene 58.2 63.4 When checking the effectiveness of the absorbent in the single-stage group contact method in Examples 3 and 4, PS can be found Both the 3200 and PS 3400 absorbents remove part of the gasoline component, of which PS 3200 is more effective. Secondly, the experimental results show that doubling the dose of the absorbent does not significantly increase the size of the paper. The use of the rent-free home-like standard (CNS) T4 specification (210X297 public A) 26 81. 6 ·〗 0,000 sheets (H ) Λ 6 η 6 21090 ^ V. Description of invention () (Please read the precautions before writing this page) Add the removal effect of gasoline pollutants. Third, it is obvious that the single-stage grouping method of Example 3 and Example 4 can not remove the gasoline component in the aqueous solution as well as the absorption tower contact method of Example 1 and Example 2. Example H: Μ-a modified 55-gallon cylinder with inlet and whisker distribution mains Expand the process of Example 1. The absorption tower can be filled with approximately 50 gallons of PS 3200 absorbent (about 140 pounds). The expanded flow rate (based on the 12 BV / hr rate tested in Example 1) is approximately 10 gallons / minute. The expected pressure drop through the absorption tower will be less than 3 psig. Jian Li: Spill half a cup of unleaded gasoline on the ground of the garage, and then remove a block copolymer microcapsule (PS 3400) on the surface of the extract. In about 15 seconds, the leached gasoline was enveloped by the copolymer. Example 7: The process of Example 6 was repeated, but 10-W30 engine oil was used instead of unleaded gasoline, and roughly similar experimental results were obtained. Example 8: The Ministry of Economic Affairs Standard ^ β 工 消 貀 Cooperative Seal 51 Mix 100 g of uncontaminated soil (IR approved) with 10 g of No. 2 diesel oil to produce a sample of contaminated soil. Then 10 grams of PS 3200 absorbent was mixed with the contaminated soil sample for 30 minutes to produce a homogeneous composition. The homogenized composition was mixed with 1 liter of deionized water for two hours, and the homogenized composition was leached in water. When the leaching step is completed, the enclosed pollutant blocks will rise to the surface of the water, which can be skimmed on the surface with a net to remove these pollutant blocks. Then filter the remaining samples, and then use 81,000 sheets of paper. ⑻ The standard size of the Chinese paper (CNS) Τ4 specifications (210X297) is used for the standard paper size u- Λ 6 H6 Central Bureau of Economic Development The employee ’s cooperative prints 5. The description of the invention (a gas chromatograph with a fid detector properly analyzes the volatile organic pollutants (benzene, toluene, ethylbenzene, and xylene) in the filter fluid. The liquid does not contain any measurable volatile organic pollutants. Therefore, the content of volatile organic pollutants has not been employed lOppb (10 parts per billion). Example 9: Repeat the process of Example 8, but the polluted The mixing time of the soil sample and the absorbent was extended from 30 minutes to two hours, and the same results were obtained. Example 1 0: 20 gallons of topsoil contaminated with 2 gallons of unleaded gasoline were sent to a belt mixer, and then Approximately 3 gallons of the encapsulating agent used in Example 1 were mixed with contaminated topsoil to produce a substantially homogeneous composition, which was placed in a 100-gallon storage tank. An additional 50-gallon tap water was used to homogenize this Composition mix When the enclosed contaminants float to the surface of the storage tank * Use a leaf rake to skim them off, and then test the water and soil left in question and find that they will generally be free of unleaded gasoline. Example 11: In this experiment, seawater was placed in a glass container, and then a sufficient amount of Kuwait to form a half-inch thick film on the surface of the water was poured onto the seawater. The solid hydrophobic silica (Aerosil R 974 ) The treated block copolymer (Kraton G-1650) is spread on the surface of the crude oil, forming a thickness of about 1/8 inch, and then stirred to make it into the crude oil film. In less than 1 minute, the present invention The block copolymer composition completely encapsulates the crude oil, forming a dry solid floating on the surface of the seawater. Because of the appearance of this dry solid, all paper sizes are freely used by China B Jiabiao (CNS) T4 regulation (210X297 male dragon) ) 81. 6. 10, 000 sheets (H) (please read the precautions before filling in this page) installed · Central Standard of the Ministry of Economic Affairs and printed by Beigong Consumer Cooperation Λ 6 Π 6 V. Inventions Description () does not contain oil stains, so it is easy to go from the sea surface After removing dry solids, seawater becomes clear without crude oil remaining. Using the untreated Kraton G-1650 block copolymer to process the above-mentioned Kuwait crude oil film, it takes about 1-1 / 2 minutes to wrap up the crude oil Scrap. Case 1 2: Repeat the process of Example Π, but use fresh water instead of seawater to obtain approximately the same results. Yin Li 1 3: Repeat the process of Example 12, but use unleaded gasoline instead of Kuwaiti crude oil to obtain roughly The same result. Case U: Repeat the process of Example 12, but using a 10-W-30 lubricant instead of Kuwait crude oil, the experimental results are roughly the same, and the water treated with the encapsulating agent of the present invention is completely free of Pollutants. Example 15: Repeat the process of Example 12, but replace the Kuwait crude oil with the following pollutants: diesel, heptane, sealing oil, transformer oil, JP-5 jet engine fuel, hydraulic oil, and transmission oil. In each experiment, roughly the same results were obtained, and the water was also substantially free of sulfohydrogen compound contaminants. In all experiments, the time required to encase the hydrogenated compound with the composition of the present invention was 25% faster than with the untreated composition. Example 1 fi: A 32-foot-long ship equipped with two inboard diesel engines and having 20 to 30 gallons of stern slots, with a circumference of about 4 hours and a length of about 48 inches, and built example 11 This paper size is used in China. Home standard (CN5) f4 specifications (2) 0X297 male dragon) 81. 6 · 10, 000 sheets (H) (please read back to the precautions # fill out this page) installation · line. Λ 6 Β 6 Printed by the Ministry of Economic Affairs, Standards of the Ministry of Economic Affairs, Co., Ltd., Pyongyang Co., Ltd. 10 points-V. Invention description () The stern pouch of the composition of the present invention used in pollution treatment. The stern pouch is effective before replacing Μ Remove 2 quarts of contaminated oil. In use, the stern bag can make the water in the stern substantially free of oil contaminants. Window Example 17: The surface of a small inland lake is covered with diesel oil traces about 1/4 inch thick Covering an area of 1/4 acres, in order to protect the lake shore from oil pollution, a barrage that allows water to pass through was used, in which each leaning wooden member filled the composition of the present invention used in Example 11, and the The wood is placed between the lake shore and the oil track. First, use a small boat to spray the book used in Example 11 on the edge of the oil track towards the lake shore The composition of the invention is then sprayed around the oil trace from the edge of the oil trace towards the center. The amount of the composition used to treat the pollution is approximately 20% of the calculated overflow weight. Within four hours The oil pollution is almost completely covered. Then use a 1 / 8-inch net to catch the oil-encrusted fragments in the water. The recovered fragments are dissolved in petroleum spirit to form a liquid diesel-rubber petroleum essence composition. Then This composition is filled into a 55-gallon mesh cylinder, which can be used as fuel for industrial water heaters. Example 18: In this example, a stern pump equipped with a parallel filter cylinder and appropriate piping and valves, First use one of the filters to remove pollutants in the abdomen water, and the second filter is on standby at any time. When the first filter is being renovated, it can replace the clematis. Each filter cartridge The amount of the decapsulation agent of the present invention used in the filled example 11 is sufficient to enclose about 2-1/2 quart of hydrocarbon contaminants. When the pressure drop through the filter is equivalent to entrap about 2 quarts Of contaminants The system will produce an appropriate value (please read the precautions before writing this page). Binding-Order-This paper is used in the middle of the paper (CNS) Ή specifications (210x297 public 81. 6. 10, 〇〇〇 Zhang (Η) The Ministry of Economic Affairs of the Central Committee of the Ministry of Economics and Fisheries C5 Workers' Co-op Cooperative Printing V. Description of Invention () Warning, at this time, you can use the second filter to replace, and then clean the first filter If the filter is not replaced in time, the filter will continue to function until the pressure drop makes the stern pump stop automatically and stop working. This stern pump has passed the system for about 6 months, so that the pollutants in the environment can be roughly Therefore, the present invention provides a high-efficiency method for recovering organic liquid or petroleum liquid from mud, water flow and solid surfaces. The block copolymers used in these methods can quickly absorb and / or adsorb the decanted organic liquid or petroleum-related liquid. After these organic liquids or petroleum-related liquids have been absorbed and / or adsorbed, the block copolymers encapsulating the organic liquids can be easily recovered, leaving at most the amount of decanted organic liquids or petroleum-related liquids. The recovered copolymer containing the recovered organic liquid can be used as solid fuel again, or it can be dissolved in each liquid fuel to form a fuel oil, which can avoid expensive landfill or cleaning problems. In addition, because the organic liquid is surrounded by the copolymer, it will increase the combustion temperature of the organic liquid (lower its ignition point). Table 10. Stern pump 11. Copolymer processing unit 12. Copolymer absorbent bed 14. Copolymer absorbent bed 16. Vessel outlet tube 18. Vessel 20. Handling unit inlet tube 22. Handling unit inlet tube (please read the precautions first and write this page) Packing-This paper standard is easy to use in a S family sample (CNS ) Τ4 specifications (210X297 public) 81. 6. 10,000 sheets (H) A 6 Π 6 5. Description of the invention () 23 · Pressure gauge 24. Three-way valve 26. Processing unit outlet pipe 28. Three-way valve 30. Container Inlet pipe 32. Pressure gauge 34. Treatment liquid container 36. Barrel outlet pipe 40. Air stripping tower 42. Ozone treatment unit 44. Ultraviolet radiation treatment unit 46. Active master treatment unit 48. Inlet water flow 50. Outlet water flow 60. Soil / Block copolymer mixture 62. Excavated hole 63. Surrounding soil 64. Underground fuel tank Printed by the Central Bureau of Economics, Ministry of Economic Affairs, Beigong & Cooperative (please read the back-end notes # 塡 写 此 页) 66. The second amount of soil 68. Organic fluid 70. Oil well 72. Well source 74. Ring body The paper size is easy to use China B standard (CNS) T4 specification (210X25) 7 male; «:) 81. 6. 10,000 sheets (H)

Claims (1)

I修補j HG 109 2I patch j HG 109 2 7 7 7 7 A B c D 經濟部中央標準局R工消費合作社印製 六、申請專利範困 第81104607號專利申請案申請專利範圍修正本 修正日期:82年6月 1. 一種除去水溶液中所攜帶之有機液污染物的方法,包 含將該水溶液通過一個接觭區域,此接觸區域含有至 少由一種撤粒狀熱塑性撣性線型雙塊狀共聚物、三塊 狀共聚物或分支雙塊狀共聚物所形成之固定床,而此 撤粒狀熱塑性彈性塊狀共聚物至少包含一種與撣性共 轭二烯聚合物塊结合之單乙烯基芳番族聚合物塊、或 一種與彈性單烯聚合物塊結合之單乙烯基芳香族聚合 物塊;Μ及由該接觸區域回收大致無污染物之水流。 2. —種從泥土中除去有機液污染物之方法*包含: 將受有機液污染之泥土至少與一種撤粒狀熱塑性彈性 線型雙塊狀共聚物、三塊狀共聚物、或分支二塊狀共 聚物结合,而此撤粒狀熱塑性彈性塊狀共聚物包含一 種與彈性共軛二烯聚合物塊結合之單乙烯基芳香族聚 合物塊、或一種與彈性單烯聚合物塊结合之單乙烯基 芳香族聚合物塊; 將該受有機液污染之泥土與該熱塑性彈性塊狀共聚物 混合,形成該熱塑性彈性塊狀共聚物及該受有機液污 染之泥土的一種均質混合物; 將該均質混合物與水混合; 從該均質混合物中回收被塊狀共聚物包住之有機液Β 染物;以及 本紙張又度適用中國國家標準(CNS)甲4规格(210 X 297公釐> — — — 1J *-1—— !* 裝— 11 — I 訂-----^" (請先閲讀背面之注項再塡寫本頁) 7 7 7 7 A B c D 、申請專利範困 從剩餘的混合物中回牧無污染之泥土。 3. —種從一艏液體或固體表面回收有機液薄膜之方法, 包含: 將包含一種線型雙塊狀共聚物、三塊狀共聚物、或分 支雙塊狀共聚物之細分微粒狀熱塑性彈性塊狀共聚物 均匀地散布在該有機液薄膜上,該撤粒狀熱塑性彈性 塊狀共聚物包含一種與撣性共轆二烯聚合物塊結合之 單乙烯基芳香族聚合物塊、或一種與彈性單烯聚合物 塊結合之單乙烯基芳香族聚合物塊;其中該塊狀共聚 物被均勻地塗上一層疏水性矽土,使用之矽土量在該 熱塑性塊狀共聚物重量的0.1至2. 5重量百分比範圍内 t 讓塊狀共聚物包住污染油;Μ及 從該液體或固體表面回收包住有機液之塊狀共聚物。 4. 一棰從泥土中除去有機掖污染物之方法,包含: 將該受有機物污染之泥土與水混合,Μ便從泥土中瀝 漉出該有機液污染物,並得到一種泥土/液體混合物 « » 將該泥土/液體混合物過濾,得到洗土及一種包含該 有機液污染物之濾液; 將該濾液通過一個含有至少由一種撤粒狀熱塑性彈性 線型雙塊狀共聚物、三塊狀共聚物、或分支雙塊狀共 聚物所形成之一個固定床之接觸區域,該撤粒狀熱塑 本紙張尺度適用中國國家標準(CNS)甲4规格(210 X 297公釐> {請先閲讀背面之注意事項再埔寫本頁) 裝· 訂 垤濟部中央標準局貝工消費合作社印製 六、申請專利範团 A7 B7 C7 D7 性撣性塊狀共聚物至少包含一锺與彈性共轭二烯聚合 物塊結合之單乙烯基芳香族聚合物塊、或一種與彈 性單烯聚合物塊结合之單乙烯基芳香族聚合物塊;Μ 及 從該接觸區域回收一個大致無污染之水流。 5. —種防止有機污染物從一痼含污染物之棺或管中滲漏 至該槽或管之下或周圍的泥土中之方法,包含: 將某一數量之泥土與一種撤粒狀熱塑性撣性線型雙塊 狀共聚物、三塊狀共聚物、或分支雙塊狀共聚物混合 ,形成一個泥土/塊狀共聚物混合物,該微粒狀熱塑 性彈性塊狀共聚物至少包含一種與彈性共轭二烯聚合 物塊結合之單乙烯基芳香族聚合物塊、或一棰與彈 性單烯聚合物塊結合之單乙烯基芳香族聚合物塊;Μ 及 將該泥土/塊狀共聚物混合物放置在位於地下的該槽 或管之週園或底下。 6. 依據申請專利範圍第5項所述之方法,尚包含從受到 有機物汚染的地下,回收泥土及共聚物之該混合物的 步驟; 閲 面 之 注 再 頁 煙 濟 部 中 央 標 準 局 Ά X 消 合 社 印 製 W及從土中分離出含有污染物之共聚物的步驟。 7. 依據申請專利範圍第1至6項中之任一項所述之方法 ,其中,該彈性聚合物塊至少部份氫化。 8. 浓據申請專利範圍第1至6項中之任一項所述之方法 本紙張又度適用中國Κ家標準(CNS)甲4规格(210 X 297公货) 35 A7 B7 C7 D7 經濟部中央標準局8工消费合作社印製 、申請專利範囲 ,其中,該單乙烯基芳香族聚合物塊至少部份氫化。 9.依據申請專利範圍第1至6項中之任一項所述之方法 ,其中,該熱塑性彈性塊狀共聚物包含一種聚苯乙烯 -聚丁二烯-聚苯乙烯塊狀共聚物。 1〇·依據申請專利範圍第1至6項中之任一項所述之方法 ,其中,該熱塑性彈性塊狀共聚物包含一種聚苯乙烯 -乙烯/ 丁烯共聚物-聚苯乙烯塊狀共聚物。 11·依據申請專利範圍第1至6項中之任一項所述之方法 ,尚包括在一値有機溶劑中溶解該被塊狀共聚物包住 之有機液污染物,形成一種有機液污染物-共聚物液 髏組合物,可做爲火爐、引擎等之燃料。 12.依據申請專利範圍第11項所述之方法,其中,該有機 溶劑係選自包含石油精、柴油、原油及汽油之組群 中。 13·依據申請專利範圍第3項所述之方法,其中,對於每 一加侖的有機液,該塊狀共聚物的使用量大约在0.1 至1磅的範圍内。 14. 依據申請專利範圍第1項所述之方法,尚包括使用臭 氧處理該溶液之步驟。 15. 依據申請專利範圍第1項所述之方法,尚包括使用紫 外線輻射處理該溶液之步驟。 16. 依據申諳專利範圍第1項所述之方法,尚包括使用话 性碳處理該溶液之步驟。 (請先面之注意事項再墻寫本頁) -装· 訂. 7.4. 本紙張尺度適用中國B家標準(CNS>甲4规格(210 X 297公® > A7 B7 C7 D7_ 六、申請專利範園 17.依據申請專利範圍第1項所逑之方法,尚包括將溶液 通過一値空氣汽提塔之步驟。 ----------------1-·1-----裝------#(泉 (請先閲讀背面之注意事項再堉寫本頁) 經濟部中央標準局貝工消费合作社印製 本紙張尺度適用中國國家標準(CNS)甲4規格(210 X 297公釐>7 7 7 7 AB c D Printed by R Industry and Consumer Cooperatives, Central Bureau of Standards, Ministry of Economic Affairs VI. Patent Application No. 81104607 Patent Application Amendment of Patent Scope Amendment Date: June 82, 1 A method of contaminating organic liquids, comprising passing the aqueous solution through a contact area, the contact area containing at least one of a thermoplastic thermoplastic linear bi-block copolymer, a tri-block copolymer or a branched bi-block copolymer The formed fixed bed, and the pelletized thermoplastic elastomeric block copolymer contains at least one monovinylarene polymer block combined with an extruded conjugated diene polymer block, or one with an elastic monoene polymer Block-bonded monovinyl aromatic polymer block; M and a substantially contaminant-free water stream recovered from the contact area. 2. A method for removing contaminants of organic liquid from the soil * includes: at least one type of thermoplastic elastomer linear bi-block copolymer, tri-block copolymer, or branched two-block copolymer in the soil contaminated with organic liquid The copolymer is combined, and the pelletized thermoplastic elastic block copolymer contains a monovinyl aromatic polymer block combined with an elastic conjugated diene polymer block, or a monoethylene combined with an elastic monoene polymer block Based aromatic polymer block; mixing the soil contaminated with organic liquid with the thermoplastic elastic block copolymer to form a homogeneous mixture of the thermoplastic elastic block copolymer and the soil contaminated with organic liquid; mixing the homogeneous mixture Mix with water; recover the organic liquid B dyestuff enclosed by the block copolymer from the homogeneous mixture; and this paper is again applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm> — — 1J * -1——! * Pack — 11 — I order ----- ^ " (please read the notes on the back and then write this page) 7 7 7 7 AB c D 、 Patent application difficulties from the rest In the mixture Grazing non-polluting soil 3. A method for recovering organic liquid film from a bow liquid or solid surface, which includes: will include a linear bi-block copolymer, tri-block copolymer, or branched bi-block copolymer The finely divided particulate thermoplastic elastomeric block copolymer is evenly dispersed on the organic liquid film, and the withdrawn thermoplastic elastomeric block copolymer contains a monovinyl aromatic polymer combined with a block copolymer of a co-coated diene diene Block, or a monovinyl aromatic polymer block combined with an elastic monoene polymer block; wherein the block copolymer is evenly coated with a layer of hydrophobic silica, and the amount of silica used is copolymerized in the thermoplastic block Within the range of 0.1 to 2.5 weight percent of the weight of the substance t Let the block copolymer encapsulate the contaminated oil; Μ and recover the block copolymer encapsulating the organic liquid from the surface of the liquid or solid. 4. Remove from the soil in a row The method for organic pollutants includes: mixing the soil contaminated with organic matter with water, and then leaching the organic liquid contaminants from the soil and obtaining a soil / liquid mixture « Filtering the soil / liquid mixture to obtain washed soil and a filtrate containing the contaminants of the organic liquid; passing the filtrate through a copolymer containing at least one thermoplastic elastomer linear bi-block copolymer, tri-block copolymer, or The contact area of a fixed bed formed by the branched double block copolymer, the size of the thermoplastic paper withdrawn from this sheet is in accordance with the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm> {Please read the note on the back Matters will be written on this page.) Installation and printing. Printed by the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy. 6. Patent Application Group A7 B7 C7 D7 A block copolymer of at least one polyimide and elastic conjugated diene. A monovinyl aromatic polymer block combined with a mass, or a monovinyl aromatic polymer block combined with an elastic monoene polymer block; M and a substantially pollution-free water stream recovered from the contact area. 5. A method to prevent organic pollutants from leaking from a coffin or pipe containing contaminants into the soil under or around the tank or pipe, including: mixing a certain amount of soil with a granular thermoplastic Dust linear bi-block copolymers, tri-block copolymers, or branched bi-block copolymers are mixed to form a soil / block copolymer mixture. The particulate thermoplastic elastomer block copolymer contains at least one conjugate with elasticity Monovinyl aromatic polymer blocks combined with diene polymer blocks, or monovinyl aromatic polymer blocks combined with elastic monoene polymer blocks; M and the earth / block copolymer mixture is placed in The perimeter or underneath of the tank or tube is underground. 6. According to the method described in item 5 of the patent application scope, it also includes the step of recovering the mixture of soil and copolymer from the ground contaminated with organic matter; The steps of printing and separating the copolymer containing contaminants from the soil. 7. The method according to any one of claims 1 to 6, wherein the elastic polymer block is at least partially hydrogenated. 8. According to the method described in any one of the items 1 to 6 of the patent application scope, this paper is again applicable to the Chinese Kjia Standard (CNS) A 4 specifications (210 X 297 public goods) 35 A7 B7 C7 D7 Ministry of Economic Affairs Printed and patented by the 8th Industrial Cooperative Cooperative of the Central Bureau of Standards, where the monovinyl aromatic polymer block is at least partially hydrogenated. 9. The method according to any one of claims 1 to 6, wherein the thermoplastic elastic block copolymer comprises a polystyrene-polybutadiene-polystyrene block copolymer. 10. The method according to any one of claims 1 to 6, wherein the thermoplastic elastomer block copolymer comprises a polystyrene-ethylene / butylene copolymer-polystyrene block copolymer Thing. 11. The method according to any one of items 1 to 6 of the patent application scope, further comprising dissolving the organic liquid pollutant enclosed by the block copolymer in an organic solvent to form an organic liquid pollutant -The copolymer liquid skull composition can be used as fuel for stoves, engines, etc. 12. The method according to item 11 of the patent application scope, wherein the organic solvent is selected from the group consisting of petroleum spirits, diesel oil, crude oil, and gasoline. 13. The method according to item 3 of the patent application scope, wherein the amount of the block copolymer used is approximately in the range of 0.1 to 1 pound for each gallon of organic liquid. 14. According to the method described in item 1 of the patent application scope, it also includes the step of treating the solution with ozone. 15. According to the method described in item 1 of the patent application scope, it also includes the step of treating the solution with ultraviolet radiation. 16. According to the method described in item 1 of the patent scope of application, the step of treating the solution with speech carbon is also included. (Please follow the precautions before writing this page on the wall)-Binding · Ordering. 7.4. This paper scale is applicable to China's B standard (CNS > A 4 specifications (210 X 297 Gong ®> A7 B7 C7 D7_ Sixth, apply for a patent Fan Yuan 17. According to the method described in item 1 of the scope of patent application, it also includes the step of passing the solution through an air stripper. ---------------- 1- · 1 ----- 装 ------ # (泉 (Please read the precautions on the back before writing this page) The paper standard printed by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs is applicable to the Chinese National Standard (CNS) A 4 specifications (210 X 297 mm >
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI468424B (en) * 2009-04-17 2015-01-11 Lanxess Deutschland Gmbh Process for producing a polymer dispersion based on polychloroprene and plant for producing a polymer dispersion based on polychloroprene

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI468424B (en) * 2009-04-17 2015-01-11 Lanxess Deutschland Gmbh Process for producing a polymer dispersion based on polychloroprene and plant for producing a polymer dispersion based on polychloroprene

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