TWI252841B - A system and method for delivering electron acceptors and/or electron donors to contaminated aquifer - Google Patents

A system and method for delivering electron acceptors and/or electron donors to contaminated aquifer Download PDF

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TWI252841B
TWI252841B TW91137257A TW91137257A TWI252841B TW I252841 B TWI252841 B TW I252841B TW 91137257 A TW91137257 A TW 91137257A TW 91137257 A TW91137257 A TW 91137257A TW I252841 B TWI252841 B TW I252841B
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electron
gas injection
injecting
gas
pipe
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TW91137257A
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TW200410910A (en
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Kan-Fu Liang
Ming-Jin Guo
Chih-Jen Lu
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Ming-Jin Guo
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Abstract

A system and method for delivering electron acceptors and/or electron donors to contaminated aquifer. The invention contains a main line of a large diameter and numerous reduced-diameter lines branching from the main lines in parallel array. The method is to inject electron acceptors and/or electron donors in gas or vapor state pneumatically through the system into contaminated aquifer. Delivering electron acceptors and/or electron donors in gas or vapor state provides effective mixing with microorganisms and the contaminants in aquifer. This invention is capable to deliver electron acceptors and donors to contaminated aquifer with radius of influence greater than vertical and horizontal wells. Also, by delivering electron acceptors and/or electron donors in gas or vapor state avoids potential clogging near the injection points due to excessive microbial growth.

Description

1252841 玖、發明說明: 【發明所屬之技術領域】 石油碳氫化合物及有機化合物是地下水及土壤最 常見的有機污染物。這些化合物常溶在飲用水源引起嚴 重國民健康問題。因為地下水是世界上多地使用的飲用 水源,發展經濟及有效的整治方法是非常重要且有意義 的。 已知的整治方法包括抽出處理,氣提法及土壤氣體 抽出法等。自然降解也被證實能降解土壤及地下水有機 污染物的濃度。但自然降解通常速度緩慢。現地生物整 治常用來整治受石油碳氳化合物及含氣有機物污染之 土壤及地下水。 現地生物整治技術大部分的研就發展及現場應用 都專注在現場調查,菌種篩選馴養,或營養鹽、電子接 受者及(或)電子供給者的應用。很少研究發展注意到 將電子接受者及(或)電子供給者注入系統之改良及電 子接受者及(或)電子供給者在地下與污染物的混合接 觸效率之提升。 現地生物整治隶重要的工程瓶頸在缺少已證實可 行的方法將電子接受者及(或)電子供給者注入地下並 有效與污染物及微生物充分混合接觸。現地生物整治技 術現%應用之成效未如貫驗室理想。這顯示改良電子接 受者及(或)電子供給者注入系統的重要性。 【先前技術】 1252841 氣提法以空氣為電子接受者,注入飽和層。根據3 I個模廠數據,Mariey等人(1995)報告氣 提法有效半徑約3至8米。A c omb等人(1 9 9 5 ) 根據現場試驗,報告在注氣速率4 5 〇公升/分穩 疋流狀態下’氣提法最大整治半徑約4 · 5米。L u η d e g a r d等人(2 〇 〇 1 )由現場試驗報告水平注 氣井之注氣有效距離可達15米。 Η 〇 p k i n s 及M cCarty(1995)報 告以盼及甲苯為主要基質好氧共代謝三氯乙烯及含氯 烯類。McCarty等人(1998)以氧氣及過氧 化氳為電子接受者,曱苯為主要基質整治受三氯乙烯污 染之場址。以上電子接受者及主要基質皆在地表與水混 合後由注入井擠注進入地下含水層。M c c a r t y等 人(1 9 9 8 )報告注入井現場操作發現之問題包括注 入含水層之電子接受者及主要基質與污染物未能充分 混合;在注入井附近微生物過度生長造成井篩堵塞。Μ cCarty等人(1998)用脈衝注入方式幫助甲 苯更均勻分布在含水層,但有效半徑也在1〇米以内。 【發明内容】 習用垂直井或水平井將電子接受者及(或)電子供 給者注入受污染含水層降解有機污染物。以上習用方法 有困難將電子接受者及(或)電子供給者有效分布在含 水層中,並且大部分侷限在注入井附近。 本發明係提供一種將電子接受者及(或)電子供給 者注入受污染含水層之方法及系統。該方法能將電子接 1252841 受者及(或)電子供給者有效均勻分布在含水層中,並 且有效注入半徑大於習用的垂直井或水平井。本發明之 /主入系統首先由大口徑之注氣主管出發,再經由注氣主 管並聯式分支出多個小口徑之注氣支管,最後進入含水 層。大口從之注入糸統能將電子接受者及(或)電子供 給者在不需過度壓降下注到遠距離。並聯式注氣支管各 配有流量控制裝置及多孔限流出氣管能有效控制電子 接受者及(或)電子供給者在含水層的分布。 本發明使用氣動方式將電子接受者及(或)電子供 給者以氣態注入受污染含水層。將電子接受者及(或) 電子供給者以氣態注入可提供其與含水層中微生物及 污染物充分有效之混合。本發明將電子接受者及(或) 電子供給者注入含水層之有效範圍大於習用之垂直井 及水平井方法。另外,本發明將電子接受者及(或)電 子供給者以氣態注入含水層能有效避免習用方法常見 在注入井附近微生物堵塞井篩的問題。 【實施方式】 為使本發明使用之技術手段、發明特徵、達成目的 與功能易於明白了解,以具體實施例配合圖式及圖號詳 細說明如下: 第一較佳具體實施例的詳細說明(以空氣為電子接 受者注入含水層的一個例子): 圖一為本發明並聯式空氣注入方法及系統示意 圖,其具有一於入口可配合注氣機(5)將空氣(5 1 ) 注入之大口徑注氣主管(1 ),且注氣主管(1)分別 1252841 並聯式多數支小口徑之注氣支管(2),注氣支管(2 ) 各組裝有流量控制裝置(4)及限流出氣管(3)。本 :明2氣:管(2)及各限流出氣管(3)並聯式排 另卜圖一為各限流出氣管(3)以注氣管(丄工) 連接串聯式排列之示意圖。圖三比較本發明並聯式空氣 =^統壓力分佈與㈣式域注人力分佈,該 i力為主人屋力扣除水柱靜壓。圖四比較本發明並聯式 空氣注入系統流量分佈與串聯式空氣注入系統流量分 佈。由圖三可見本發明並聯式线注人系統之注入距離 至少可達2 Q米’遠大於串聯式空氣注人系統,也遠大 於習用之垂直或水平注人井。由圖四可見本發明並聯式 空氣注入系統比串聯式更能將空氣均勻注人含水層。 其中,本發明之注氣主管(i )人口可供注入曰電子 接受者及(或)電子供給者,電子接受者可為氧氣,電 子供給者可為氣態甲苯等。 第二較佳具體實施例的詳細說明(以空氣為電子接 受者通過文氏管攜帶甲苯蒸氣(電子供給者)注入含水 層的一個例子): 圖五為本發明空氣通過文氏管攜帶甲苯蒸氣並聯 式注入方法及系統示意圖。首先配合注氣機(5 )將空 氣(5 1 )注入文氏管(6 ),將一與文氏管(6)連 ^容器(7)内的甲苯溶液(71)氣化,並攜帶甲 苯蒸氣(72)進入大口徑注氣主管(1),再由注氣 主管(1 )並聯式分別進入小口徑之注氣支管(2); 注氣支官(2)各配有流量控制裝置(4)及限流出氣 1252841 二未二Τί進入含水層(8) ’含水層(8)上方 η 圖六為本發…苯蒸汽並聯式注入 dtrj濃度分布圖。由圖六甲苯濃度之分布可 迅實本發明以空氣(電子接受者)攜㈣苯 =者之綠歸許縣者均勻 含水層。 另外’針㈣五之實施例,於下制其操作條件與 少驟·1252841 玖, invention description: [Technical field of invention] Petroleum hydrocarbons and organic compounds are the most common organic pollutants in groundwater and soil. These compounds are often dissolved in drinking water sources causing serious national health problems. Because groundwater is a drinking water source used in many parts of the world, it is very important and meaningful to develop economic and effective remediation methods. Known remediation methods include extraction, stripping, and soil gas extraction. Natural degradation has also been shown to degrade the concentration of organic pollutants in soil and groundwater. But natural degradation is usually slow. Local bioremediation is often used to remediate soils and groundwater contaminated with petroleum carbonaceous compounds and gas-containing organic matter. Most of the research and development and on-site applications of local bioremediation technologies focus on on-site investigations, strain screening domestication, or application of nutrients, electronic recipients, and/or electron suppliers. Few research developments have noted improvements in the injection of electronic receivers and/or electron suppliers into the system and the increased efficiency of hybrid contact between the electron receiver and/or the electron supplier in the subsurface. Local bioremediation is an important engineering bottleneck in the absence of proven methods to inject electron recipients and/or electron donors into the ground and effectively mix with contaminants and microorganisms. The effectiveness of local bioremediation technology is not as good as that of the laboratory. This shows the importance of improving the electronic recipient and/or electron supplier injection system. [Prior Art] 1252841 Stripping method uses air as an electron acceptor to inject a saturated layer. Based on 3 I mold data, Mariey et al. (1995) reported that the effective radius of the stripping process is about 3 to 8 meters. A c omb et al. (1 9 9 5 ) reported a maximum remediation radius of about 4 · 5 m at the gas injection rate of 4 5 〇 liters per minute under steady turbulent flow according to field tests. L u η d e g a r d et al. (2 〇 〇 1 ) reported by the field test that the gas injection effective distance of the gas injection well can reach 15 meters. Η 〇 p k i n s and M cCarty (1995) report aspiration and toluene as the main matrix for aerobic co-metabolism of trichloroethylene and chloroolefins. McCarty et al. (1998) used oxygen and barium peroxide as electron acceptors, and benzene as the main substrate to remediate sites contaminated with trichloroethylene. The above electron acceptors and main substrates are injected into the underground aquifer by the injection well after mixing with the surface and water. M c c a r t y et al. (1 9 9 8 ) reported that the in-situ operation of the injection well found that the electron acceptor and the main substrate injected into the aquifer did not mix well with the contaminant; the microbial overgrowth near the injection well caused the well screen to clog. Μ cCarty et al. (1998) used pulse injection to help more uniform distribution of toluene in the aquifer, but the effective radius was also within 1 metre. SUMMARY OF THE INVENTION A vertical or horizontal well is used to inject an electron acceptor and/or an electron donor into a contaminated aquifer to degrade organic contaminants. The above conventional methods have difficulty in effectively distributing electron acceptors and/or electron donors in the aquifer, and most of them are confined to the vicinity of the injection well. SUMMARY OF THE INVENTION The present invention provides a method and system for injecting an electron acceptor and/or an electron supplier into a contaminated aquifer. The method can effectively and evenly distribute the electronic 1252841 recipient and/or electron supplier in the aquifer, and the effective injection radius is larger than the conventional vertical or horizontal well. The /introgress system of the present invention is first started by a large-caliber gas injection main pipe, and then a plurality of small-diameter gas injection branch pipes are branched in parallel through the gas injection main pipe, and finally enter the aquifer. The large mouth from which the system can inject electron receivers and/or electron donors to a long distance without excessive pressure drop. The parallel gas injection manifolds are each equipped with a flow control device and a porous limited outflow gas pipe to effectively control the distribution of electron acceptors and/or electron suppliers in the aquifer. The present invention pneumatically injects an electron acceptor and/or an electron donor into a contaminated aquifer in a gaseous state. Injecting an electron acceptor and/or an electron supplier in a gaseous state provides a sufficiently effective mixing with microorganisms and contaminants in the aquifer. The present invention has an effective range for injecting an electron acceptor and/or an electron supplier into an aquifer greater than conventional vertical and horizontal well methods. In addition, the present invention effectively injects the electron acceptor and/or the electron supplier into the aquifer in a gaseous state, thereby effectively avoiding the problem that the microorganisms in the vicinity of the injection well block the well screen. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In order to make the technical means, the features of the invention, the objects, and the functions of the present invention are readily understood, the detailed description of the specific embodiments, the drawings and the drawings are as follows: An example of air injected into an aquifer for an electron receiver): Figure 1 is a schematic diagram of a parallel air injection method and system of the present invention having a large diameter for injecting air (5 1 ) into the inlet (3) at the inlet. Injecting main pipe (1), and gas injecting main pipe (1) respectively, 1252841 parallel type of small-diameter gas injection pipe branch (2), gas injection pipe branch (2) each equipped with flow control device (4) and limited outflow pipe ( 3). Ben: Ming 2 gas: tube (2) and each outflow trachea (3) parallel row. Fig. 1 is a schematic diagram of the series of outflow trachea (3) connected by gas injection pipe (complex). Figure 3 compares the parallel air distribution of the present invention with the pressure distribution of the (4) type field, and the i-force is the main house force minus the static pressure of the water column. Figure 4 compares the flow distribution of the parallel air injection system of the present invention with the flow distribution of the series air injection system. It can be seen from Fig. 3 that the injection distance of the parallel line injection system of the present invention is at least 2 Q meters, which is much larger than the tandem air injection system, and is also much larger than the conventional vertical or horizontal injection wells. It can be seen from Fig. 4 that the parallel air injection system of the present invention can uniformly inject air into the aquifer more than the series type. Among them, the gas injection main pipe (i) of the present invention can be injected into the electron acceptor and/or the electron supplier, the electron acceptor can be oxygen, and the electron donor can be gaseous toluene or the like. DETAILED DESCRIPTION OF THE SECOND PREFERRED EMBODIMENT (An example of injecting toluene vapor (electron supplier) by air as an electron acceptor through a venturi): Figure 5 is an air carrying toluene vapor through the venturi of the present invention. Parallel injection method and system schematic. First, inject air (5 1 ) into the venturi (6) with a gas injector (5), vaporize a toluene solution (71) in the vessel (7) with the venturi (6), and carry toluene. The steam (72) enters the large-diameter gas injection main pipe (1), and then the gas injection main pipe (1) enters the small-diameter gas injection branch pipe (2) in parallel; the gas injection support (2) is equipped with a flow control device ( 4) and limited effluent gas 1252841 two untwisted ί into the aquifer (8) 'the upper layer of the aquifer (8) η Figure 6 is the benzene vapor parallel injection dtrj concentration distribution map. The distribution of the hexamethylbenzene concentration can be quickly obtained by the present invention with air (electron acceptor) carrying (four) benzene = the green of the county is a uniform aquifer. In addition, the embodiment of the needle (four) five, under the operating conditions and less

A 於注氣主官(1)入口連接文氏管(㈠,文氏管 (6)入口連接注氣機(5),文氏管(6)底側 連?一裝有甲苯溶液(71)之容器(7);注氣 主管(1 )另端密閉,其上並聯諸多注氣支管(2 ), 各注氣支管(2)之進氣端與上述注氣主管(工) 間連結一流量控制裝置(4),注氣支管(2)之 曝氣端連結一限流出氣管(3);限流出氣管(3) 可為不鏽鋼材質之多孔隙管;其中,注氣支管(2 ) 係延伸至污染含水層(8),限流出氣管(3)則 亦延伸於污染含水層(8)。 、 B·利用注氣機將空氣(5 1)注入文氏管(6),以 將谷二、(7 )内之甲笨溶液(7 1 )藉由低壓效應 揮發成曱笨蒸氣(7 2),並吸入文氏管(6)而 與注氣機(5)擠注之空氣混合;繼之,混合氣體 會進入注氣主管(1),並依序進入各注氣支管 (2),其中,利用流量控制裝置(4)控制注氣 主管(1)與注氣支管(2)之開口面積,使各注 1252841 氣支管(2)之壓力與流量相近;該注氣支管(2 ) 可將曱苯蒸氣(7 2 )導引,並經由限流出氣管(3 ) 將其釋放進入污染含水層(8)。 藉此,攜帶混合氣體因質能轉換,平均分布至污 染含水層(8),以被微生物利用。 綜上所述,本發明實施例確能達到所預期之使用 功效,又其所揭露之具體構造,不僅未曾見諸於同類 產品中,亦未曾公開於申請前,誠已完全符合專利法 之規定與要求,爰依法提出發明專利之申請,懇請惠 予審查,並賜准專利,則實感德便。 10 1252841 【圖式簡單說明】 圖一本發明並聯式空氣注入方法及系統示意圖 圖-串&式式空氣注人方法及系統示意圖 圖三本發明並聯式空氣注人系統壓力分佈 式空 氣注入系統壓力分佈之比較圖 圖四本發明並聯式空氣注入系統流量分佈與串聯 式空 氣注入系統流量分佈之比較圖 圖五本發明空氣通過文氏管攜帶甲苯蒸氣並聯式 注入方法及系統示意圖 圖六本發明曱苯蒸氣並聯式注入系統含水層曱苯 濃度分布圖 【主要元件符號說明】 (1 ) 注氣主管 (2 ) 注氣支管 (3 ) 限流出氣管 (4 ) 流量控制裝置 (5 ) 注氣機 (51) 空氣 (6 ) 文氏管 (7 ) 容器 (71) 甲苯溶液 (72) 甲苯蒸氣 (8 ) 含水層 (9 ) 未飽和層 (11) 注氣管A is connected to the venturi (1) at the inlet of the gas injection (1), the inlet (6) is connected to the inlet of the venturi (6), and the bottom side of the venturi (6) is connected with a toluene solution (71). The container (7); the gas injection main pipe (1) is sealed at the other end, and a plurality of gas injection pipe branches (2) are connected in parallel, and a flow rate is connected between the inlet end of each gas injection branch pipe (2) and the gas injection main pipe (work) The control device (4), the aeration end of the gas injection branch pipe (2) is connected to a limited outflow gas pipe (3); the limited outlet gas pipe (3) may be a porous pipe made of stainless steel; wherein the gas injection branch pipe (2) is extended To the polluted aquifer (8), the restricted outflow pipe (3) also extends to the polluted aquifer (8). B. Inject air (5 1) into the venturi (6) by means of a gas injection machine to (7) The solution of the stupid solution (7 1 ) is volatilized into a stupid vapor (72) by a low pressure effect, and is drawn into the venturi (6) and mixed with the air squeezed by the gas injection machine (5); Then, the mixed gas enters the gas injection main pipe (1), and sequentially enters each gas injection branch pipe (2), wherein the flow control device (4) is used to control the opening of the gas injection main pipe (1) and the gas injection branch pipe (2). Area Note 1252841 The pressure of the gas branch pipe (2) is similar to the flow rate; the gas injection branch pipe (2) can guide the benzene vapor (7 2 ) and release it into the polluted aquifer via the restricted gas pipe (3) (8) Thereby, the carried mixed gas is evenly distributed to the polluted aquifer (8) due to mass conversion, and is utilized by the microorganism. In summary, the embodiment of the present invention can achieve the intended use effect, and the disclosed The specific structure has not only been seen in similar products, nor has it been disclosed before the application. Cheng has fully complied with the requirements and requirements of the Patent Law, and has filed an application for invention patents according to law, so please review the application and grant the patent. 10 1252841 [Simple diagram of the diagram] Figure 1 Schematic diagram of the parallel air injection method and system of the present invention - string & type air injection method and system diagram FIG. 3 pressure distribution of the parallel air injection system of the invention Comparison of pressure distribution of air injection systemFig.4 Comparison of flow distribution of parallel air injection system and flow distribution of series air injection system of the present invention Schematic diagram of system and system for parallel injection of gas carrying toluene vapor through venturi tubeFig. 6 Distribution of benzene concentration in aquifer of benzene-benzene vapor parallel injection system of the present invention [Description of main components] (1) Gas injection supervisor (2) Gas injection Branch pipe (3) Outflow pipe (4) Flow control device (5) Gas injection machine (51) Air (6) Venturi tube (7) Container (71) Toluene solution (72) Toluene vapor (8) Aquifer (9 Unsaturated layer (11) gas injection pipe

Claims (1)

翁輕月/ί /J252841 拾、申請專利範圍: 1. 一種將電子供給者注入受污染含水層之系統,係包 含大口徑之注氣主管,再由注氣主管並聯式分支出 多個小口徑之注氣支管,大口徑之注入系統能將電 子供給者在不需過度壓降下擠注到遠距離,並聯式 注氣支管各組裝一可控制注氣主管與注氣支管開口 面積之流量控制裝置及一多孔限流出氣管以控制電 子供給者在含水層的分布。 2. 如申請專利範圍第1項所述將電子供給者注入受污 染含水層之系統,該注氣主管入口供注入之電子供 給者,係氣態甲苯。 3. 如申請專利範圍第1項所述將電子供給者注入受污 染含水層之系統,該限流出氣管係多孔隙管。 4. 如申請專利範圍第1項所述將電子供給者注入受污 染含水層之系統,該注氣主管入口連接注氣機以便 注氣。 5. 如申請專利範圍第1項所述將電子供給者注入受污 染含水層之系統,該注氣主管入口連接文氏管,文 氏管底側連通一容器,容器内裝液態電子供給者。 6. 如申請專利範圍第5項所述將電子供給者注入受污 染含水層之系統,該文氏管入口連接注氣機。 7. 如申請專利範圍第5項所述將電子供給者注入受污 染含水層之系統,該液態電子供給者,係為曱苯溶 液。 8. —種將電子接受者注入受污染含水層之系統,係包 12 1252841Weng Guangyue / ί /J252841 Picking up, applying for patent scope: 1. A system for injecting electron donors into a contaminated aquifer, which consists of a large-caliber gas injection supervisor, and then a plurality of small calibers are branched by the gas injection supervisor in parallel. The gas injection branch pipe, the large diameter injection system can squeeze the electron supplier to a long distance without excessive pressure drop, and the parallel gas injection branch pipe can be assembled to control the flow area of the gas injection pipe and the gas injection pipe opening area. The device and a porous outlet flow out of the gas tube to control the distribution of the electron supplier in the aquifer. 2. Inject the electron supplier into the system of the contaminated aquifer as described in item 1 of the scope of the patent application, the injecting main inlet for the injected electron donor, which is gaseous toluene. 3. Inject the electron supplier into the system of contaminated aquifer as described in item 1 of the scope of the patent application, which limits the flow of the trachea to the porous tube. 4. Inject the electron supplier into the system of the contaminated aquifer as described in item 1 of the patent application, the gas injection main inlet being connected to the gas injection machine for gas injection. 5. A system for injecting an electron supplier into a contaminated aquifer as described in claim 1 of the patent application, wherein the gas injection main inlet is connected to a venturi, and the bottom side of the venturi is connected to a container containing a liquid electron supplier. 6. Inject the electron supplier into the system of contaminated aquifer as described in item 5 of the patent application, the venturi inlet being connected to the gas injector. 7. A system for injecting an electron supplier into a contaminated aquifer as described in item 5 of the scope of the patent application, the liquid electron supplier being a terpene solution. 8. A system for injecting electron donors into contaminated aquifers, 12 1252841 含大口徑之注氣主管,再由注氣主管並聯式分支出 多個小口徑之注氣支管,大口徑之注入系統能將電 子接受者在不需過度壓降下擠注到遠距離,並聯式 注氣支管各組裝一可控制注氣主管與注氣支管開 口面積之流量控制裝置及一多孔限流出氣管以控 制電子接受者在含水層的分布。 9.如申請專利範圍第8項所述將電子接受者注入受污 染含水層之系統,該注氣主管入口供注入之電子接The large-caliber gas injection main pipe is connected in parallel by the gas injection main pipe to a plurality of small-diameter gas injection branch pipes. The large-diameter injection system can push the electron receiver to a long distance without excessive pressure drop. The gas injection branch pipes are respectively assembled with a flow control device for controlling the opening area of the gas injection pipe and the gas injection pipe branch and a porous limit outlet gas pipe to control the distribution of the electron acceptor in the aquifer. 9. A system for injecting an electron acceptor into a contaminated aquifer as described in claim 8 of the scope of the patent application, the gas inlet main inlet for the electronic connection of the injection 者為氧氣。 10. 如申請專利範圍第8項所述將電子接受者注入受污 染含水層之系統,該限流出氣管係多孔隙管。 11. 如申請專利範圍第8項所述將電子接受者注入受污 染含水層之系統,該注氣主管入口連接注氣機以便 注氣。 12. —種將電子接受者及電子供給者注入受污染含水 層之系統,係包含大口徑之注氣主管,再由注氣主 管並聯式分支出多個小口徑之注氣支管,大口徑之g 注入系統能將電子揍受者及電子供給者在不需過® 度壓降下擠注到遠距離,並聯式注氣支管各組裝一 可控制注氣主管與注氣支管開口面積之流量控制 裝置及一多孔限流出氣管以控制電子接受者及電 子供給者在含水層的分布。 13. 如申請專利範圍第12項所述將電子接受者及電子 供給者注入受污染含水層之系統,該注氣主管入口 供注入之電子供給者,係氣態甲苯。 13 1252841 14. 如申請專利範圍第12項所述將電子接受者及電子 供給者注入受污染含水層之系統,該注氣主管入口 供注入之電子接者為氧氣。 15. 如申請專利範圍第12項所述將電子接受者及電子 供給者注入受污染含水層之系統,該限流出氣管係 多孔隙管。 16. 如申請專利範圍第12項所述將電子接受者及電子 供給者注入受污染含水層之系統,該注氣主管入口 連接注氣機以便注氣。 17. 如申請專利範圍第12項所述將電子接受者及電子 供給者注入受污染含水層之系統,該注氣主管入口 連接文氏管,文氏管底侧連通一容器,容器内裝液 態電子供給者。 18. 如申請專利範圍第16項所述將電子接受者及電子 供給者注入受污染含水層之系統,該文氏管入口連 接注氣機。 19. 如申請專利範圍第16項所述將電子接受者及電子 供給者注入受污染含水層之系統,該液態電子供給 者,係為甲苯溶液。 20· —種將電子供給者注入受污染含水層之方法,其步 驟為: A ·於一端為密閉之注氣主管上並聯諸多注氣支 管,各注氣支管之進氣端與注氣主管間連結一 流量控制裝置,注氣支管之曝氣端連結一限流 出氣管;其中,注氣支管係延伸至污染含水層, 14 1252841 限流出氣管則亦延伸於污染含水層; B .將電子供給者注入注氣主管,使其依序進入各注 氣支管;其中,利用流量控制裝置控制注氣主 管與注氣支管之開口面積,使各注氣支管之壓 力與流量相近;該注氣支管可將電子供給者導 引,並經由限流出氣管將其平均釋放進入污染 含水層,以被微生物利用。 21. 如申請專利範圍第20項所述將電子供給者注入受 污染含水層之方法,該注氣主管入口供注入之電子 供給者,係氣態曱苯。 22. 如申請專利範圍第20項所述將電子供給者注入受 污染含水層之方法,該限流出氣管係多孔隙管。 23. 如申請專利範圍第20項所述將電子供給者注入受 污染含水層之方法,該注氣主管入口連接注氣機以 便注氣。 24. 如申請專利範圍第20項所述將電子供給者注入受 污染含水層之方法,該注氣主管入口連接文氏管, 文氏管底侧連通一容器,容器内裝液態電子供給 者。 25. 如申請專利範圍第24項所述將電子供給者注入受 污染含水層之方法,該文氏管入口連接注氣機。 26. 如申請專利範圍第24項所述將電子供給者注入受 污染含水層之方法,該液態電子供給者,係為甲苯 溶液。 27· —種將電子接受者注入受污染含水層之方法,其步 15 1252841 輝為·· A.二:端:密閉之注氣主管上並聯諸多注氣支 ;二支!,進氣端與注氣主管間連結-流 总.置乳支管之曝氣端連結一限流出氣 出弟二目丨注軋支管係延伸至污染含水層,限流 B 出乳g則亦延伸於污染含水層; 將電子接受者、、+人、士 > + ^ /入注軋主官,使其依序進入各注 n: 1二中’利用流量控制裝置控制注氣主管 二=支管之開口面積’使各注氣支管之塵力與 二里相近;該注氣支管可將電子供給者導引並 f由限流出氣管將其平均釋放進人污染含水 層,以被微生物利用。 、-Γϋ專利範圍第27項所述將電子接受者注入受 水層之方法’該注氣主管入口供注入之電子 接者為氧氣。 29.如申請專利範圍第27項所述將電子接受者注入受 30 水層之方法,該限流域㈣多孔隙管。 .、、- =凊專利範圍第27項所述將電子接受者注入受 二木:水層之方法’該注氣主管入口連接注氣機以 1更〉主氣。 31.種將電子接受者及t子供給者注人受污染含水 層之方法,其步驟為: Ί端為密閉之注氣主管上並聯諸多注氣支 各注氣支管之進氣端與注氣主管間連結一流 置控制裝置,注氣支管之曝氣端連結一限流出氣 16 1252841 管;其中,注氣支管係延伸至污染含水層,限流 出氣管則亦延伸於污染含水層; B .將電子接受者及電子供給者注入注氣主管,使其 依序進入各注氣支管;其中,利用流量控制裝置 控制注氣主管與注氣支管之開口面積,使各注氣 支管之壓力與流量相近;該注氣支管可將電子供 給者導引,並經由限流出氣管將其平均釋放進入 污染含水層,以被微生物利用。 32. 如申請專利範圍第31項所述將電子接受者注入受 φ 污染含水層之方法,該注氣主管入口供注入之電子 供給者,係氣態甲苯。 33. 如申請專利範圍第31項所述將電子接受者注入受 污染含水層之方法,該注氣主管入口供注入之電子 -接者為氧氣。 34. 如申請專利範圍第31項所述將電子接受者注入受 污染含水層之方法,該限流出氣管係多孔隙管。 35. 如申請專利範圍第31項所述將電子接受者注入受 φ 污染含水層之方法,該注氣主管入口連接文氏管, 文氏管底侧連通一容器,容器内裝液態電子供給 者。 3G.如申請專利範圍第35項所述將電子接受者注入受 污染含水層之方法,該文氏管入口連接注氣機。 , 37.如申請專利範圍第35項所述將電子接受者注入受 污染含水層之方法,該液態電子供給者,係為曱苯 溶液。 17It is oxygen. 10. A system for injecting an electron acceptor into a contaminated aquifer as described in Section 8 of the patent application, which exits the tracheal system. 11. Inject the electron acceptor into the system of contaminated aquifer as described in item 8 of the patent application, the gas injection main inlet being connected to the gas injection machine for gas injection. 12. A system for injecting electron acceptors and electron suppliers into a contaminated aquifer, comprising a large-caliber gas injection main pipe, and then a plurality of small-diameter gas injection branch pipes are branched in parallel by the gas injection mains, and a large diameter g The injection system can push the electronic receiver and the electron supplier to a long distance without the need of a pressure drop. The parallel gas injection branch is assembled to control the flow area of the gas injection main pipe and the gas injection branch opening area. The device and a porous outlet flow out of the trachea to control the distribution of electron acceptors and electron donors in the aquifer. 13. A system for injecting an electron acceptor and an electron supplier into a contaminated aquifer as described in claim 12, the gas supply mains inlet for injecting electrons, which is gaseous toluene. 13 1252841 14. Injecting an electronic receiver and an electron supplier into a system of contaminated aquifers as described in claim 12, the injecting mains inlet is oxygen for injection. 15. A system for injecting an electron acceptor and an electron supplier into a contaminated aquifer as described in claim 12, which limits the flow of the trachea to the porous tube. 16. A system for injecting an electronic recipient and an electronic supplier into a contaminated aquifer as described in claim 12, the gas injection main inlet being connected to a gas injection device for gas injection. 17. A system for injecting an electron acceptor and an electron supplier into a contaminated aquifer as described in claim 12, wherein the gas injection main inlet is connected to the venturi, and the bottom side of the venturi is connected to a container, the liquid is filled in the container Electronic supplier. 18. A system for injecting an electronic receiver and an electronic supplier into a contaminated aquifer as described in claim 16 of the patent application, the venturi inlet being connected to the gas injector. 19. A system for injecting an electron acceptor and an electron supplier into a contaminated aquifer as described in claim 16 of the patent application, the liquid electron supplier being a toluene solution. 20· A method for injecting an electron supplier into a contaminated aquifer, the steps of which are as follows: A. A plurality of gas injection branches are connected in parallel with a gas injection main pipe at one end, and an inlet end of each gas injection branch pipe and a gas injection main pipe Connected to a flow control device, the aeration end of the gas injection branch is connected to a limited outlet gas pipe; wherein, the gas injection branch pipe extends to the polluted aquifer, and the 14 1252841 restricted gas flow pipe also extends to the polluted aquifer; B. The electron supplier Injecting the gas injecting main pipe, and sequentially entering each gas injecting branch pipe; wherein, the flow control device is used to control the opening area of the gas injecting main pipe and the gas injecting pipe branch, so that the pressure and the flow rate of each gas injecting pipe branch are similar; the gas injecting pipe branch can be The electron supplier directs and releases it evenly into the contaminated aquifer via a restricted outflow tube for use by the microorganism. 21. A method of injecting an electron supplier into a contaminated aquifer as described in claim 20, the gas supply mains inlet for injecting an electron donor, gaseous toluene. 22. A method of injecting an electron supplier into a contaminated aquifer as described in claim 20, which exits the trachea porous tube. 23. A method of injecting an electron supplier into a contaminated aquifer as described in claim 20, wherein the gas injection main inlet is connected to the gas injection device for gas injection. 24. A method of injecting an electron supplier into a contaminated aquifer as described in claim 20, wherein the gas injection main inlet is connected to a venturi, and the bottom side of the venturi is connected to a container containing a liquid electron supplier. 25. A method of injecting an electron supplier into a contaminated aquifer as described in claim 24, the venturi inlet being connected to the gas injector. 26. A method of injecting an electron donor into a contaminated aquifer as described in claim 24, the liquid electron supplier being a toluene solution. 27·—A method of injecting an electron acceptor into a contaminated aquifer, the step 15 1252841 is a · A. 2: end: a closed gas injection main pipe is connected in parallel with a plurality of gas injection branches; two! Injecting main pipe connection-flow total. The aeration end of the milking branch pipe is connected to a limited outflow gas. The second leg of the pipe is extended to the polluted aquifer, and the restricted flow B is also extended to the polluted aquifer; The electronic receiver, + person, 士> + ^ / into the main officer, so that they enter each note n: 1 2 'using the flow control device to control the gas injection pipe 2 = the opening area of the branch pipe' The dusting force of each gas injection branch pipe is similar to that of the second gas; the gas injection branch pipe can guide the electron supplier and release it into the polluted aquifer by the outflow gas pipe to be utilized by the microorganism. - The method of injecting an electron acceptor into a water receiving layer as described in item 27 of the patent scope'. The electron injector for the injection main inlet is oxygen. 29. A method of injecting an electron acceptor into a layer of 30 water as described in claim 27, the restricted watershed (iv) porous tube. ., , - = 凊 凊 凊 凊 将 将 将 将 将 将 将 将 将 将 将 将 将 将 将 将 将 将 将 将 电子 电子 电子 电子 电子 电子 电子 电子 电子 电子 电子 电子 电子 电子 电子31. A method for injecting an electron acceptor and a t-supplier into a contaminated aquifer, the steps of which are: the end of the gas injection pipe is connected to the gas inlet pipe of the gas injection pipe and the gas injection pipe The main pipe is connected to the first-class control device, and the aeration end of the gas injection pipe is connected with a limited flow of gas 16 1252841; wherein the gas injection branch pipe extends to the polluted aquifer, and the outflow gas pipe extends to the polluted aquifer; The electron receiver and the electron supplier inject the gas injection main pipe into the gas injection branch pipes in sequence; wherein the flow control device is used to control the opening area of the gas injection main pipe and the gas injection branch pipe, so that the pressure of each gas injection branch pipe is close to the flow rate The gas injection branch can guide the electron supplier and release it evenly into the polluted aquifer via the outflow pipe to be utilized by the microorganism. 32. A method of injecting an electron acceptor into a φ contaminated aquifer as described in claim 31, wherein the gas injection main inlet is supplied to the electron donor, which is gaseous toluene. 33. In the method of injecting an electron acceptor into a contaminated aquifer as described in claim 31, the electron injecting port of the gas injection main inlet is oxygen. 34. A method of injecting an electron acceptor into a contaminated aquifer as described in claim 31, which exits the tracheal porous tube. 35. A method of injecting an electron acceptor into a φ contaminated aquifer as described in claim 31, the gas injection main inlet is connected to a venturi, and the bottom side of the venturi is connected to a container containing a liquid electron supplier . 3G. A method of injecting an electron acceptor into a contaminated aquifer as described in claim 35, the venturi inlet being connected to the gas injector. 37. A method of injecting an electron acceptor into a contaminated aquifer as described in claim 35, the liquid electron supplier being a toluene solution. 17 12528411252841 1252841 i· 91 Π . 9「ΙΊΊΊΙΊΙ I ΤΙ TnHLI Ί Γ OOVO 寸 CNr"H〇〇Vs〇 寸 CN,.〇〇〇〇 • «攀 擊 j « · · · oooo oooo (疆鮮)謂 12528411252841 i· 91 Π . 9 "ΙΊΊΊΙΊΙ I ΤΙ TnHLI Ί OO OOVO inch CNr"H〇〇Vs〇 inch CN,.〇〇〇〇 • «攀击 j « · · · oooo oooo (疆鲜) 1252841 91 采)歷wnYfti皿 II91 mining) calendar wnYfti dish II Ό 1 1 Ο 1252841Ό 1 1 Ο 1252841 1252841 mm 顆 IgSSYtti皿 CNI IIOI 6COA 910寸 He® mmm 〇〇〇〇〇〇〇 ο ο ο ο ο ο ο ο ο ο ο ο Ό 寸 CO CN r-H1252841 mm IgSSYtti dish CNI IIOI 6COA 910 inch He® mmm 〇〇〇〇〇〇〇 ο ο ο ο ο ο ο ο ο ο ο ο ο ο ο CO CO CO CO CN r-H
TW91137257A 2002-12-25 2002-12-25 A system and method for delivering electron acceptors and/or electron donors to contaminated aquifer TWI252841B (en)

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