TW436335B - An effective treatment method for washing the soil contaminated by heavy metals - Google Patents

An effective treatment method for washing the soil contaminated by heavy metals Download PDF

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TW436335B
TW436335B TW88107180A TW88107180A TW436335B TW 436335 B TW436335 B TW 436335B TW 88107180 A TW88107180 A TW 88107180A TW 88107180 A TW88107180 A TW 88107180A TW 436335 B TW436335 B TW 436335B
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Taiwan
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soil
cleaning
cleaning agent
decontamination
item
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TW88107180A
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Chinese (zh)
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Ren-Jie Jung
Ming-Shing Wu
Lu-Hua Hung
Rung-Chuen Shie
Yu-Liang Chen
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Inst Of Nuclear Energy Res Roc
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Abstract

This invention discloses an effective treatment method for washing the soil contaminated by heavy metals. Under the optimum operating conditions, the contaminated soil is leached by mixing with washing solutions which are prepared from phosphoric species and other additives. Experimental results show that the method is very effective for soil decontamination, and the residual concentration of heavy metals in soil can be as low as the environmental background after decontamination. In addition, the washing agents used for the decontamination can be reused with the same decontamination efficiency after electrolytic treatment. The soil after decontamination can be used for agriculture purpose again.

Description

43633S 五、發明說明(1) t發明乃關於重金屬污染土壤之處理方 劑與清洗劑回收方法。 β用m /先 L :染ΐ ?主ί可分成二大·,第-類為有機污染,、 上 乐一類為無機金屬污毕, 包ί重金屬污染及放射性元素之污染,其中第:類有關重 金屬污染土壤之產生主要臾自协 有關重 此類重金屬包含有鎘、銅,、鋅、、鎳、鉛、:廢水等所造成’ 目:台灣本土所存在受鎘污染之土壤面積相當大,如 桃園的中帛、觀音地區和彰化的和美地區等,造成廣大農 地休耕及農作物收成受影響。根據環保法規之規定,、任何 受π染之土壤移作它種用途之前必須先將土壤中之污染物 質去除至合乎管制標準,因此發展—種能#效解決此一重 金屬污染土壤之方法是相當迫切需要的,且為使污染‘土壤 能再度被有效使用,必須進行土壤除污使土壤中重^屬含 量降至環境之背景值及環保法規管制值以下。目前已知被 使用來處理污染土壤之方法,包含有土壤清洗(S〇il washing)、電動力處理(Electrokinetic treatment)、 玻璃化(Vitrification)、生物處理(Bi〇remediati〇n)、 植物吸收(Vegetative absorption)、固化 (Solidification)及焚化(incineration)等法。 比較土壤清洗及電動力處理,二者最大之差異在於前 者利用所添加之各種化學試劑將土壤中的重金屬浸潰或萃 取出來,而後者主要藉由外加電場之作用使重金屬自土壤_ 中分離’再經由電場之作用於陰極收集。由於電動力處理43633S V. Description of the invention (1) The invention relates to a method for treating heavy metal contaminated soil and a method for recovering cleaning agents. β used m / first L: dyeing? The main ί can be divided into two major categories, the first type is organic pollution, the upper one is inorganic metal pollution, including heavy metal pollution and radioactive element pollution, of which the first: category related The production of heavy metal contaminated soil is mainly related to the self-association of heavy heavy metals including cadmium, copper, zinc, nickel, lead, and waste water. 'Project: The area of soil contaminated with cadmium existing in Taiwan is quite large, such as Zhongyuan, Guanyin, and Hemei districts in Changhua, Taoyuan, affected the vast agricultural land fallow and crop yields. According to the environmental protection regulations, before any π-contaminated soil can be used for other purposes, the pollutants in the soil must be removed to meet the control standards. Therefore, the development of a kind of energy-efficient solution to this heavy metal contaminated soil is quite equivalent. It is urgently needed, and in order for the contaminated soil to be used again effectively, soil decontamination must be carried out to reduce the content of heavy metals in the soil to below the environmental background value and the value regulated by environmental laws and regulations. Methods currently known to be used to treat contaminated soil include soil washing, electrokinetic treatment, vitrification, biological treatment, and plant absorption ( Vegetative absorption), solidification and incineration. Comparing soil cleaning and electrodynamic treatment, the biggest difference between the two is that the former uses various added chemical reagents to immerse or extract the heavy metals in the soil, while the latter mainly separates heavy metals from soil_ by the action of an external electric field ' Collected by the action of the electric field on the cathode. Due to electric power handling

436335 五、發明說明(2) 牽涉到電泳(Electrophoresis)、電透析 (Electro-osmosis)及電解(Electrolysis)三種因素之影 響,使得重金屬元素於土壌中之遷移速度緩慢,處理時匈 較長,因此清洗法成為此類污染土壤較常使用的有效方 =。在過去許多文獻中曾報導使用土壤清洗法處理鋼、-汞、鉛等之污染’雖有相當程度之效果,但亦隨不同清洗 劑配方及土壤本身特性,而有不同之處理效果,例如砂土 中之污染較易去除,反之黏土在清洗效果上常大打折扣’ 因此如何發展出一種效果好且適用於各種重金屬元素及土 壤特性之清洗劑是目前各方著重之努力方向。 土壤清洗法是一種結合物理及化學達到污染物去除和 減廢目的之除污方法,有關土壤清洗的原理主要利用加入 的各種試劑與污染土壤充分混合後,將土壤中之污染,物進 行取代、脫附或離子交換等反應而達到除污之效果。影響 土壤清洗效果的因素相當多,包括有(1)津洗劑的種類, (2)清洗劑濃度,(3)清洗方式,(4)清洗時間,(5)pH值’ (^)清洗溫度及(7)其他外加試劑及條件的影響等,常用的 β洗劑可分成三大類:(丨)酸、鹼及一般化學試劑,例如 Ma'酸硝酸、醋酸、過氧化氫、氣化鐵、氣化約…·等, (2)螯合劑,如EDTA、草酸銨及檸檬 酸鹽(Cltrate),(3)界面活性劑,如清潔劑、SDS、CTAB 等。通常土壤除污之效果,除了與所使用的清潔劑有關 $ ’亦與土壤的特性、操作條件及污染元素之種類有關, 一般存在於土壤中之無機污染元素可經由離子交換、化學436335 V. Description of the invention (2) It involves the influence of three factors, electrophoresis, electro-osmosis and electrolysis, which makes the migration speed of heavy metal elements in the soil slow. The cleaning method has become an effective method for such contaminated soils. In the past many literatures have reported that the use of soil cleaning methods to treat the pollution of steel, -mercury, lead, etc. has a certain degree of effect, but also has different treatment effects with different cleaning agent formulations and the characteristics of the soil itself, such as sand Contamination in the soil is relatively easy to remove. Conversely, the cleaning effect of clay is often greatly reduced. Therefore, how to develop a cleaning agent that is effective and suitable for various heavy metal elements and soil characteristics is the current focus of efforts of all parties. Soil cleaning method is a kind of decontamination method that combines physical and chemical to achieve the purpose of pollutant removal and waste reduction. The principle of soil cleaning mainly uses various reagents added to mix thoroughly with the contaminated soil, and then replaces the contaminated soil in the soil. Desorption or ion exchange and other reactions to achieve the effect of decontamination. There are quite a few factors that affect the soil cleaning effect, including (1) the type of Tianjin detergent, (2) the concentration of cleaning agent, (3) the cleaning method, (4) the cleaning time, (5) the pH value, (^) the cleaning temperature And (7) the effects of other external reagents and conditions, etc., commonly used beta lotions can be divided into three categories: (丨) acids, alkalis and general chemical reagents, such as Ma 'acid nitric acid, acetic acid, hydrogen peroxide, gasified iron, Gasification is about ... etc., (2) chelating agents, such as EDTA, ammonium oxalate and citrate (Cltrate), (3) surfactants, such as cleaning agents, SDS, CTAB, etc. In general, the effect of soil decontamination is not only related to the cleaning agent used, and it is also related to the characteristics of the soil, operating conditions, and the type of pollution elements. The inorganic pollution elements generally existing in the soil can be ion exchanged, chemically

4 3 633 5 五、發明說明(3) 和物理吸附、沉澱、取代及凝集(agglomeration)等方式 與土壤相結合,結合方式的不同會使得清洗的效果亦不— 樣。另外,不同種類的金屬亦會有不同之清洗效果,如多 金屬與土壌間的污染僅在於土壤之表面則此類污染較易去 除,但來自於環境中土壌之重金屬污染均是由於廢水中'重 金屬長時間沉積於土壤中所造成,通常與土壤之結合相當 緊密,甚至進入土壤的晶格層中,因此去除比較困難。 雖然已有文獻(S. V. Kruglov; Radiochemistry,4 3 633 5 V. Description of the invention (3) Combined with soil by physical adsorption, precipitation, substitution and agglomeration. The combination of different methods will make the cleaning effect different. In addition, different types of metals also have different cleaning effects. For example, the pollution between polymetals and soil scum is only on the surface of the soil. Such pollution is easier to remove, but the heavy metal pollution from soil scum in the environment is due to the waste water. It is caused by heavy metals deposited in the soil for a long time, and it is usually very tightly combined with the soil, and even enters the crystal layer of the soil, so it is difficult to remove. Although the literature (S. V. Kruglov; Radiochemistry,

Vol. 36,No. 6,1 994)揭示6M鹽酸及7M硝酸於沸騰時對 於土壌中某些活性元素的清洗效果可得到改善,這種土壌 清洗方式並不能真正解決存在於環境中之污染土壤問題, 因為(1)對於高濃度之污染土壤不適用,因為其最大除污 率僅約89%,尚有10%左右之污染存在於土壤中,在高,濃度 污染物之情況下,清洗後殘留在土壌中的污染物濃度將仍 大於環保法規所管制之標準;(2)HC1和HN〇3中含有ci和 子,會造成廢水處理上的困難;⑻此法處理須於濟 業=作時間較長—壤不。 雖然目前文獻資料顯示酸洗對於污染土 匕方法具有更好的效果,伸伪Λ断机"银(去π較其 通级也 不1一仍受限於土壤之特性,污毕金 屬種類和與;亏染土壌結合 π杂金 可摇_ 心万式等因素’使得除污效率雖 洗劑n °么通無法符合環保法規之需纟。以酸性清 先劑進行重金屬土壤除污的方法,例如美國專# *Vol. 36, No. 6, 1 994) reveals that 6M hydrochloric acid and 7M nitric acid can improve the cleaning effect of some active elements in soils when boiling, and this soil cleaning method cannot really solve the polluted soil existing in the environment. The problem is because (1) it is not applicable to polluted soil with high concentration, because its maximum decontamination rate is only about 89%, and about 10% of the pollution exists in the soil. In the case of high concentration pollutants, after cleaning The concentration of pollutants remaining in the soil will still be higher than the standard regulated by environmental protection regulations; (2) HC1 and HN03 contain ci and ions, which will cause difficulties in wastewater treatment; Longer-not soil. Although the current literature shows that pickling has a better effect on the method of contaminated soil, the extension of the pseudo-cutting machine " silver (removal of π is less than its general grade) is still limited by the characteristics of the soil, the type of metal and The combination of π miscellaneous gold can be combined with deficient soil 壌 and other factors' make the decontamination efficiency of the lotion n ° Mo Tong can not meet the requirements of environmental protection regulations. The method of decontamination of heavy metal soil with acid detergent, For example U.S. special # *

436335 五,發明說明(4) 5,466,426(1995)、5,505,925(1996)和5,660,806(1997) 等’使用含5% HOAC + 2,5% NH40AC之清洗液對發生於砂土 (sand)及黏土(clay)上之鉛污染,以清洗劑250 ml/50g味 壌之比例進行清洗,當浸潰萃取的時間達66小時後,顯示 對鉛污染砂土之除污率為94%,而對於鉛污染黏土的除^ 率則僅1 9〜21 %。在此法中主要以醋酸(h〇AC )作為清洗劑 之主成份’再添加其它物質作為清洗劑,此類清洗劑包括436335 V. Description of the invention (4) 5,466,426 (1995), 5,505,925 (1996), 5,660,806 (1997), etc. 'The use of a cleaning solution containing 5% HOAC + 2,5% NH40AC on sand and clay (clay) The lead pollution on) was cleaned at the ratio of 250 ml / 50g miso detergent. When the extraction time reached 66 hours, the decontamination rate for lead contaminated sand was 94%, and for lead contaminated clay The division rate is only 19 ~ 21%. In this method, acetic acid (h0AC) is mainly used as the main component of the cleaning agent, and other substances are added as the cleaning agent. Such cleaning agents include

有 5% HOAC、5% HOAC + 5% HC1、10% HOAC + 5% NH4 OAC 5% HOAC + 2.5% NaOAC 和 5% HOAC + 2.5% NH40AC。上述 各項清洗劑中除了 5% H0AC + 2. 5% NH40AC外,其餘清洗 劑的除污效果均不甚理想,然而雖然使用5% H0AC + 2. 5%NH40AC清洗劑可去除砂土中94%之鉛污染,但對於黏 土中鉛污染只能去除1 9〜2 1 % ’此乃因為砂土中鉛污染的 形態主要是以吸附之形式附著在土壤之表面,因此清洗上 較為容易,反之在黏土上之鉛因被包覆於黏土内層之中, 處理亦就相當不易。一般污染土壌之發生通常來自於長時 間所形成,且土壌的特性決非單純的屬於砂土種類,例如 一般農地的土質通常均非砂土,因此應用此法於非砂土之 金屬污染,除污效果將大打折扣,在實際應用上有其困難 存在。 另外一種常被應用的土壌除污方法,則利用土壤中由 於細小顆粒的表面積較大,吸附污染元素之機率増加的原 理,利用篩選的方式先將各種不同顆粒大小之土壌進行筛 分,再將含鎘污染金屬較多之土壤分離並清洗,如美國專There are 5% HOAC, 5% HOAC + 5% HC1, 10% HOAC + 5% NH4 OAC 5% HOAC + 2.5% NaOAC, and 5% HOAC + 2.5% NH40AC. With the exception of the above cleaning agents, except for 5% H0AC + 2. 5% NH40AC, the decontamination effect of the other cleaning agents is not satisfactory. However, although 5% H0AC + 2. 5% NH40AC cleaning agent can be used to remove sand from the soil 94 % Of lead pollution, but can only remove 19 ~ 2 1% of lead pollution in clay. This is because the form of lead pollution in sand is mainly attached to the surface of the soil by adsorption, so it is easier to clean, otherwise Because the lead on the clay is coated in the inner layer of the clay, it is not easy to handle. The occurrence of general contaminated soil moth usually comes from long-term formation, and the characteristics of soil moth are by no means purely sandy soil types. For example, the soil quality of general agricultural land is usually not sandy soil. The pollution effect will be greatly reduced, and there are difficulties in practical application. Another commonly used soil decontamination method uses the principle of increasing the probability of adsorption of contaminating elements due to the large surface area of fine particles in the soil. Using screening methods, various soil particles of different particle sizes are first screened, and then Separate and clean soils containing more cadmium-contaminated metals, such as the United States

436335 五、發明說明(5) 利5’ 342, 449(1 994)即採用此種結合物理和化古 處理受污染之土壤。此法首先利用物理 ' $ 的顆軔八M,甘士卞 將不同粒輕 的土壤顆粒为開,其中不同顆粒大小的土壤中 度的污染元素,然後再利用有機酸清洗劑將污染程鲛大 的土壌部份進行清洗除污。該專利所使用之清洗劑包含* 機酸、礦酸及少許氧化劑(如HA、〇3等)之組合,主 以單、雙、參(mono-、di:、和tri_)取代的羧酸 (carboxylic acids)作為主要成份,其中單羰酸包含萨 酸、乳酸、甲酸和苯甲酸,二羰酸包含草酸、琥珀酸和 戊二酸,三羰酸則有檸檬酸。又儘管所使用之試劑雖如 此多,但以H20 + 1% 醋酸 + 1% (w/v) Naci + 1% (w/v) NH4N〇3所組成之清洗劑效果最佳。清洗12小時後對Zn、436335 V. Description of the invention (5) Li 5 ’342, 449 (1 994) This kind of combination of physics and paleontology is used to treat contaminated soil. This method first uses the physical size of the particles, Gan Shifang to open different light soil particles, among which soils with different particle sizes are moderately polluting elements, and then use organic acid cleaning agents to increase the pollution process. The soil part is cleaned and decontaminated. The cleaning agent used in this patent contains a combination of organic acids, mineral acids, and a few oxidants (such as HA, 〇3, etc.), mainly carboxylic acids (mono-, di :, and tri_) substituted with mono, di, and ginseng (mono-, di :, and tri_). carboxylic acids) as the main ingredients, of which mono-carboxylic acid contains sarnic acid, lactic acid, formic acid and benzoic acid, di-carboxylic acid contains oxalic acid, succinic acid and glutaric acid, and tri-carboxylic acid contains citric acid. Although there are so many reagents, the cleaning agent composed of H20 + 1% acetic acid + 1% (w / v) Naci + 1% (w / v) NH4N03 is the best. After cleaning for 12 hours,

Cu、Pb有不錯的清洗效果,平均效率約〜93%,但對於 ,它的重金屬例如Cd、Ni則效果不佳,此法先利用篩選法 为出不同粒徑的土壤,藉此將高污染(粒徑小)的土壤與低 污染C粒徑大)的土壤區分離,再針對高污染的土壌作處 理’理論上似乎可行’但實際上由於土質之特性、污染元 素種類等的不同’並無一定的規律性,因此細分不同粒徑 大丨、並無多大意義’且為了能準碟筛選出不同粒徑之土 壤,少量在實驗室規模也許可行’大規模應用之設備不容 易設計,對於廠型設備則非易事。另外在此法中使用醋酸 作為清洗劑雖對Zn、Cu、Pb有不錯之清洗效果,但實際留 存於土壌中之金屬濃度仍超出環保法規值,且對其它金屬 元素之清洗效果並不明顯,而清洗時間須1 2小時,對於實Cu and Pb have a good cleaning effect, with an average efficiency of ~ 93%, but for its heavy metals such as Cd and Ni, the effect is not good. This method first uses the screening method to produce soils with different particle sizes, thereby reducing high pollution. (Small particle size) The soil is separated from the low-pollution C soil area, and then treated for the high-contamination soil moth 'theoretically feasible', but in fact due to the differences in soil properties and types of pollution elements, etc. There is no certain regularity, so it does n’t make much sense to subdivide different particle sizes. Also, in order to screen different soils with different particle sizes, a small amount may be feasible in the laboratory scale. 'Large-scale application equipment is not easy to design. Factory-type equipment is not easy. In addition, although the use of acetic acid as a cleaning agent in this method has a good cleaning effect on Zn, Cu, and Pb, the actual metal concentration in the soil still exceeds environmental protection regulations and the cleaning effect on other metal elements is not obvious. The cleaning time should be 12 hours.

第10頁 43633 6 五、發明說明(6) , 際之應用效果上亦嫌太長。 除了使用酸作為清洗劑外,亦有使用鹼作為清洗劑, 例如美國專利5, 516,968(1996)用於處理由汞與多氣聯笨 或放射性元素之混合廢料所產生的污染土壤之除污,主、要 利用鹼性無水氨液作為清洗劑,在此法中藉由液體氨溶液 與含汞之污染土壤在反應器中相互混合,形成一個氨化的 液汞(ammoniacal liquid-mercury)污泥,再利用加熱及 氣泡擾拌方式自污泥中分開與液體氨結合,且汞含量較高 7細顆粒土壤分散液,靜置後將此一上層之液-固相土壤 分散液取出’氨液經由蒸發方式回收使用,而剩餘細顆粒 土壤部份則儲存或靜候進一步處理,藉此可達到減廢目 的。但此法仍存在與美國專利5, 342, 449(1 994)相同之問 =二依土壤特性及土質的不同並非大部份的污染物均,存 顆粒土壤中,因此並不適用於所有的例子,過程中 液固的:J亦須進一步固化處理,且需隔夜靜置使上層之 Ϊ:二之土 土壤分數液沉澱出來頗為費時,僅適用於 壤’對於其它重金屬污染較不適用。 5 i述專利相類似的為另—美國專利 染土壤進行係利用其所發明的清洗分離設備將污 態,再si加將污染土壤與水混合成泥浆 熱至沸騰狀態,電流通過泥漿’將此-泥漿加 帶出,經由離心過请2之氣泡會將含於土壤中的污染物. 過4將土壞與清洗刺分開。此法之先Page 10 43633 6 V. The description of the invention (6) is too long for the application effect. In addition to using acids as cleaning agents, there are also alkalis used as cleaning agents. For example, U.S. Patent No. 5,516,968 (1996) is used for the decontamination of contaminated soils produced by the mixed waste of mercury and gaseous or radioactive elements. Mainly, use alkaline anhydrous ammonia as a cleaning agent. In this method, liquid ammonia solution and mercury-contaminated soil are mixed with each other in the reactor to form an ammoniacal liquid-mercury sludge. , And then use heating and bubble agitation to separate from the sludge and combine with liquid ammonia, and have a high mercury content of 7 fine-grained soil dispersions. After standing, take out this upper liquid-solid phase soil dispersion to take out the ammonia solution. Recycling is performed by evaporation, and the remaining fine-grained soil is stored or awaited for further processing, thereby reducing waste. However, this method still has the same problem as U.S. Patent No. 5,342,449 (1 994) = the difference between soil properties and soil quality is not that most of the pollutants are stored in granular soil, so it is not applicable to all For example, the liquid-solid: J must be further solidified during the process, and it needs to be left to stand overnight to make the upper part of the soil: the second soil soil fractions precipitate out. It is quite time-consuming, and it is only applicable to soil. The above patent is similar to the other one—U.S. Patents for soil staining use the cleaning and separation equipment invented by the invention to contaminate the soil, and then add the contaminated soil and water to form a slurry and heat it to a boiling state. -The mud is brought out, and the bubbles contained in the soil will be contaminated by centrifugation. The soil will be separated from the cleaning thorns after passing 4. Before this law

第11頁 43633 b 五、發明說明(7) 件=假没大部份的污染物存在於顆粒較細的土壤中’因此 仍子在與美國專利5, 342’44 9(1994)及5,516, 968(1996)同 問題’亦就是仍有部份污染物質存在於較大顆粒的^ ,中必須清洗’且長時間利用電場加熱生成氣泡去除泥土 中的巧·染物亦頗為耗費能源。 、一九本發明針對上述各項缺點加以改進,而提供一種用於 污染土壤的新穎獨特之清诜劑配方及清洗除污方法,除了 對於土壌的除污率大於99%之外,清洗後殘留於土壌内之 金屬濃度亦合乎環保法規值,另附帶提供一種清洗劑回收 處。理程序,可將清洗劑回收使用’且清洗效果仍可維持在 99% ’除可避免產生大量廢水外’亦可節省清洗葯劑之成 本支出。 本發明中所提的方法除可在低於彿騰的溫度下處‘理且 除污的效果高於9 9%外,實驗結果顯示留存於土壤中之重 金屬濃度’以鎘污染土壤為例,可降至約〇. 2ρριη或更低, 符合環保署暫定台灣地區土壤重金屬標準與等級區分之第 二級環境背景值要求(0. 39ppm以下);另外清洗後之清洗 劑亦可經由回收裝備進行清洗劑回收’.回收後之試劑再度 使用於污染土壤之清洗時’其除污率仍維持在99?6。如此 不但清洗劑可重覆循環使用,減少廢水量之產生及降低操 作的成本,而且經植物之栽種測試,本法除污後之土壤可 再作為農業使用;此外,處理速度快亦為本發明方法的另 一特點,平均約每3小時可清洗一批次之污染土壤。 本發明的應用範圍包含所有重金屬污染土壤之處理/Page 11 43633 b V. Description of the invention (7) Item = Most of the pollutants are present in the fine-grained soil 'so they are still in contact with U.S. Patents 5,342'44 9 (1994) and 5,516, 968 (1996) The same problem, that is, there are still some pollutants in the larger particles, must be cleaned, and the use of electric field heating for a long time to generate air bubbles to remove clutter and dyes in the soil is also quite energy-consuming. 19. The present invention improves the above disadvantages, and provides a new and unique formulation of detergent and cleaning and decontamination method for contaminated soil. In addition to the soil decontamination rate greater than 99%, it remains after cleaning. The metal concentration in the soil is also in compliance with environmental protection regulations, and a cleaning agent recovery place is also provided. The cleaning process can be recycled, and the cleaning effect can still be maintained at 99%. In addition to avoiding the generation of a large amount of waste water, the cost of cleaning chemicals can also be saved. In addition to the method mentioned in the present invention, in addition to being able to be treated at a temperature lower than Foten and the effect of decontamination is higher than 99%, the experimental results show that the concentration of heavy metals remaining in the soil is exemplified by cadmium contaminated soil It can be reduced to about 0.2ρριη or lower, which meets the second-level environmental background value requirements of the EPA ’s provisional soil heavy metal standards and classifications in Taiwan (below 0.39ppm); in addition, the cleaning agent after cleaning can also be performed through recycling equipment. Cleaning agent recovery '. When the recovered reagent is reused in the cleaning of contaminated soil, its decontamination rate remains at 99-6. In this way, not only the cleaning agent can be reused repeatedly to reduce the amount of waste water and reduce the cost of operation, but also the soil after decontamination by this method can be used for agriculture after planting tests. In addition, the fast processing speed is also the invention Another feature of the method is that one batch of contaminated soil can be cleaned approximately every 3 hours on average. The scope of application of the present invention includes the treatment of all heavy metal contaminated soil /

第12頁 4 3 6336 五、發明說明(8) ~—~ 主要的清洗除污原理乃利用以磷酸為主劑的清洗劑本身之 特性與土壌表面或吸附於土壤且形成鍵結之金屬離子進行 化學反應,使得金屬離子能由土瓖中被清洗出來,同時.,亦 藉由某些化學添加劑的加入,使得被清洗出來之金屬離 子,避免再度被吸附於土壌中。由於土壤之成份中混合*著 許多有機物質,例如腐質酸(Humic acid)和褐菌酸 (Fulvic acid)等,此類有機物通常包圍於土壌顆粒之表 面上,而許多污染元素會與此類有機物形成鍵結,因此若 要將污染源去除則需破壞此類元素與有機物間之鍵結但 有些污染金屬經由一段長時間與土壤作用後,會進入土壤 顆粒之晶格層間,若欲將其除去則於清洗劑之選擇及操作 上均需費較大之功夫^ , 本發明中所發展出來的清洗劑是以磷酸為主要架‘構的 混合劑’由於磷酸具有較強氧化能力,對大多數的物質均 能產生氧化作用,為使除污效率能達到完全的效果(符合 ^法規要求)’少量的添加劑有加強清洗之作用。根據 :驗的結果顯示Μ吏用本研究中所開發的扎❿配方清洗 劑,對於由一般重金屬元素例如鎘、 鎳、鉛、 2….所造成之污染土壤,經由本發明之清洗劑的處理 f ’脫除效果可達99%,殘留在土壤中之重金屬含量已符 :環保署所暫訂之第三級環境背景值的㈣,以鎘為例, 按^染土壌中鎘含量為73. 2ppm,經本試劑清洗後殘留土 壤中鎬含量為0‘37PPm,除污率高達99 5%,其它如銅、 鉛、鋅、鉻、鎳,亦都在三級標準内,由此可見本法對於Page 12 4 3 6336 V. Description of the invention (8) ~~~ The main principle of cleaning and decontamination is to use the characteristics of the cleaning agent with phosphoric acid as the main agent and the surface of the soil or the metal ions adsorbed on the soil and form bonds. The chemical reaction allows the metal ions to be washed out of the soil, and at the same time, the added metal ions are prevented from being adsorbed in the soil again by the addition of certain chemical additives. Because soil ingredients are mixed with many organic substances, such as humic acid and fulvic acid, these organic substances are usually surrounded on the surface of soil particles, and many pollution elements are associated with this kind of soil. Organic matter forms a bond, so if you want to remove the pollution source, you need to destroy the bond between these elements and organic matter. However, some contaminated metals will enter the interstitial layer of the soil particles after interacting with the soil for a long time. If you want to remove it, It takes a lot of effort in the selection and operation of the cleaning agent ^, the cleaning agent developed in the present invention is based on phosphoric acid as the main structure 'mixture' Because phosphoric acid has a strong oxidizing capacity, All substances can produce oxidation, in order to achieve the full effect of decontamination efficiency (in compliance with ^ regulations) 'a small amount of additives have the effect of strengthening cleaning. According to the test results, it is shown that the cleaning agent developed by this researcher uses the cleaning agent formulated in this study to treat the contaminated soil caused by general heavy metal elements such as cadmium, nickel, lead, 2 ..., through the cleaning agent of the present invention. f 'Removal effect can reach 99%, the content of heavy metals remaining in the soil has already met: the third level of environmental background value ㈣ temporarily set by the Environmental Protection Agency, taking cadmium as an example, the cadmium content in 壌 dyed soil 壌 is 73. 2ppm, the content of pickaxes in the residual soil after washing with this reagent is 0'37PPm, and the decontamination rate is as high as 99 5%. Others such as copper, lead, zinc, chromium, and nickel are also within the third-level standard.

4 3 633b 五、發明說明(9) 重金屬污染土壌之除污效果相當優異。 本研究過程中亦發現若於清洗劑中加入適當的添加 h 劑,對於土壤中重金屬之清洗有加強之作用。根據實驗結 果顯示添加各種氣化物、硫化物和硝化物於磷酸配方清诜 液中’對於土壌之除污效果有很好的幫助,其中尤以硝化 物及硫化物之效果最佳,平均可使得土壤中金屬離子之去 除效率增加5〜10%。影響土壌除污效率的主要因素包括有 清洗劑配方’添加劑及清洗條件,例如清洗溫度、土壤/ 清洗劑比例、濃度…·等。在本研究中顯示清洗系統中清 洗劑的濃度愈高,反應速率愈快,但為節省操作成本,清 洗劑濃度仍不宜太高,而土壤(g)/清洗劑(mI)以1/3〜1/4 例混合.,添加少量硫化物於清洗劑中,控制操作溫度 以上:以下皮而最好在70〜80。。,若溫度在‘沸點 以上則浪費熱能、溫度過低則反應時間太長 益,開始進行清洗,反應時間為2 °^ 3小時’對於土壤中之污染金屬元素=二般 99%。 〜际巧效率最咼可達 此外對於清洗程序上,為考慮各 =性,清洗效果及清洗劑之用與2吸 程序及逆向交又清洗操作程序,前者二一出一-人清洗 能達到完全清除的目的,此 人凊洗程序在於為 太降又操作流程採逆向交又清唼古斗 / π冼兀 清洗的程序得以連續方式進行。二」、’使整個土壤 清洗操作程序如圖丨.所示 ::Ί及逆向交又, P用清洗液人將污染之土壤B先 第14頁 α363354 3 633b V. Description of the invention (9) The decontamination effect of soil contaminated by heavy metals is quite excellent. In the course of this study, it was also found that if an appropriate h-agent was added to the cleaning agent, it would strengthen the cleaning of heavy metals in the soil. According to the experimental results, it is shown that adding various kinds of gaseous, sulfide and nitrate to the phosphoric acid formula cleaning solution is very helpful for the soil decontamination effect. Among them, the effect of nitrate and sulfide is the best. The removal efficiency of metal ions in the soil is increased by 5-10%. The main factors that affect the soil decontamination efficiency include cleaning agent formula ’additives and cleaning conditions, such as cleaning temperature, soil / cleaning agent ratio, concentration, etc. In this study, it was shown that the higher the concentration of the cleaning agent in the cleaning system, the faster the reaction rate, but in order to save operating costs, the concentration of the cleaning agent should not be too high, and the soil (g) / cleaning agent (mI) should be 1/3 ~ 1/4 case mix. Add a small amount of sulfide to the cleaning agent, and control the operating temperature above: preferably 70 ~ 80. . If the temperature is ‘above the boiling point, heat energy is wasted. If the temperature is too low, the reaction time is too long. Start cleaning. The reaction time is 2 ° ^ 3 hours.’ For the contaminated metal elements in the soil = 99%. ~ The best efficiency can be achieved. In addition, in the cleaning program, in order to consider various properties, cleaning effects and the use of cleaning agents and 2 suction program and reverse intersecting and cleaning operation program, the former two one out-one person can achieve complete For the purpose of cleaning, this person's cleaning procedure is to carry out the continuous cleaning of the ancient combat / π 冼 cleaning procedure for the descending operation process and the reverse flow. Second "and‘ make the entire soil cleaning operation procedure as shown in Figure 丨. :: Ί and reverse crossing, P will use the cleaning solution to contaminate the soil B first Page 14 α36335

436335 五、發明說明(11) 難,通常以每公斤溶液中含〇. 1〜〇. 7公斤之間的清洗劑為 宜。至於添加劑的最佳濃度則以每公斤溶液含〇. 〇1〜〇. ;! 公斤為宜。 * 以下發明人將以實驗舉例說明本發明的土壤清洗方-法、流程及清洗劑配製,且以受重金屬如鎘、銅、鉛、 鋅、鉻、鎳….等元素實際污染的土壤,說明利用本發明 之清洗劑及清洗除污程序的效果。為註明本發明之實用 性’將採用彰化及桃園地區實際重金屬污染之土壌進行各 種實驗’除污後土壤中重金屬含量將以環保署所暫訂第3 級環境背景值作為依據,以鎘為例第三級之環境背景濃度 為0.05ppm〜〇.39ppm,詳細的步驟及結果說明如下。 這些實驗僅是本發明之部份實施例,並不代表本發明 的全部使用範圍,因此不能成為對本發明使用範圍之> 限 制。 實施例一: 取來自桃·園區實際鎘污染之土壤若干量,首先經初步 筛選去除大石塊、樹枝等雜物,且以研磨機將硬塊土壤先 行打碎、混合’於32 溫度下將土壌烘乾,去除含於土壤 表面之水份,如此可確實獲知反應土壤之重量,再將此一 洪乾之土壤進行篩選’去除大於36 mesh之小石塊和雜 物’取樣分析土壤中所含重金屬離子濃度’作為實驗土壌 之進料。 磷酸配方清洗劑的配製,取一般工業用磷酸於其中加 水及少量無機酸使其充分混合,再加入硫酸鹽於常溫下攪436335 V. Description of the invention (11) Difficult, usually a cleaning agent containing between 0.1 to 0.7 kg per kg of solution is suitable. As for the optimal concentration of the additive, it contains 0.001 ~ 〇. Per kg of solution;! Kg is appropriate. * The following inventors will use experimental examples to illustrate the soil cleaning method, process and cleaning agent preparation of the present invention, and use soils that are actually polluted by heavy metals such as cadmium, copper, lead, zinc, chromium, nickel ... Utilize the effect of the cleaning agent and cleaning decontamination procedure of the present invention. To indicate the practicability of the present invention, 'Experiments with actual heavy metal pollution in Changhua and Taoyuan areas will be used for various experiments.' The heavy metal content in the soil after decontamination will be based on the level 3 environmental background value temporarily set by the Environmental Protection Agency as an example. The environmental background concentration of the third stage is 0.05 ppm to 0.39 ppm. The detailed steps and results are explained below. These experiments are only a part of the embodiments of the present invention, and do not represent the full range of use of the present invention, and therefore cannot be > limits to the use range of the present invention. Example 1: Take a certain amount of soil that is actually polluted by cadmium from the Tao · Park. Firstly, remove large stones, branches and other debris through preliminary screening, and use a grinder to break and mix the hard soil first. The soil is dried to remove the water contained on the soil surface, so that the weight of the reaction soil can be accurately known, and then this flooded soil is screened to 'remove small stones and debris larger than 36 mesh'. Concentration of heavy metal ions was used as the feed for the test soil. For the preparation of phosphoric acid formula cleaning agent, take general industrial phosphoric acid, add water and a small amount of inorganic acid to make it fully mixed, then add sulfate to stir at room temperature

436335 五、發明說明(12) 拌均勻,使製成之溶液含P04=/H20/S04=之比例為6/38/1 (莫 耳),此製備好之溶液儲存備用。將上述準備好之土壌樣 品1 000份(重量)與磷酸混合清洗劑380 0份(體積)混合,吏 土壌重量(g ) /清洗劑體積(m 1)比=1 / 4,將此混合物置於.反 應槽内授拌均勻,一面加熱此反應槽升溫至80 t:,在此溫 度下清洗3小時,為防止過程中清洗液之損失,須加裝冷 凝裝置,反應完後利用抽.氣過濾將土壤與清洗劑分離,用 過之清洗劑開始進行電解回收,操作電壓9 V、電流密度: 0. 23 A/cm2、操作時間72小時,而土壤部份經水洗過濾後 將此一 土壤於32 °C下烘乾後取樣分析土壤中重金屬濃度及 除污效率,清洗結果如表1.所示。此為污染土壌一次清洗 之效果,顯示土壤中重金屬濃度以鎘為例由原有之 73_ 2ppm降至小於〇. 3ppm,平均土壌中重金屬之除污奉為 99.5%,符合環保署所暫訂土壤中鎘金屬含量第三級環境 背景值標準:0.05〜0.39ppm。 實施例二: 取實際重金屬污染之土壤(包含鎘、銅、鉛、鋅、 鉻、錄、….等元素)若干量,使用如實施例一之處理方法 將土壤進行前處理’清洗劑之配製方法亦如實施例一,再 使用與實施例一相同之方法進行土壤清洗,不同之處在於 本實施例中所用之土壤除鎘污染外尚含有其它重金屬之污 染’結果如表2·所示》經清洗後鎘由4· 1 7ppm降至 0.25ppm ’ 銅由 61.5ppm 降至 6.93ppm,錯由 26.1ppm 降至 8 66ppm,鋅由 42.4ppm 降至 23ppm ,鎳由 34.8ppm 降至436335 V. Description of the invention (12) Mix well, so that the prepared solution contains P04 = / H20 / S04 = at a ratio of 6/38/1 (mol). The prepared solution is stored for future use. 1 000 parts by weight of the soil sample prepared above was mixed with 3800 parts by volume of phosphoric acid mixed cleaning agent, and the ratio of the weight (g) / cleaning agent volume (m 1) of the soil preparation was set to 1/4. Stir in the reaction tank evenly, and heat the reaction tank to 80 t while heating: Wash at this temperature for 3 hours. In order to prevent the loss of cleaning liquid during the process, a condensation device must be installed. The filtration separates the soil from the cleaning agent, and the used cleaning agent starts electrolytic recovery. The operating voltage is 9 V, the current density is 0.23 A / cm2, and the operation time is 72 hours. The soil part is washed and filtered to filter the soil. After drying at 32 ° C, samples were taken to analyze the concentration of heavy metals in the soil and the decontamination efficiency. The cleaning results are shown in Table 1. This is the effect of one-time cleaning of contaminated soil, showing that the concentration of heavy metals in the soil, taking cadmium as an example, has decreased from 73_ 2ppm to less than 0.3 ppm. The average decontamination of heavy metals in soil is 99.5%, which is in line with the EPA ’s provisional soil The third level environmental background value standard for the content of cadmium metal: 0.05 ~ 0.39ppm. Example Two: Take the actual heavy metal contaminated soil (including cadmium, copper, lead, zinc, chromium, chromium, ..., etc.), and use the treatment method of Example 1 to prepare the soil for cleaning. The method is the same as in Example 1, and the same method as in Example 1 is used for soil cleaning, except that the soil used in this example contains other heavy metals in addition to cadmium pollution. The results are shown in Table 2 · " After cleaning, the cadmium was reduced from 4.17ppm to 0.25ppm. The copper was reduced from 61.5ppm to 6.93ppm, the error was reduced from 26.1ppm to 866ppm, the zinc was reduced from 42.4ppm to 23ppm, and the nickel was reduced from 34.8ppm.

4363 3 b 五、發明說明(13) 2,38ppm ’處理後之濃度均在環保署所暫訂三級環境背景 標準值以内。 實施例三: r 取實際重金屬污染之土壤,如實施例一之方法進行.實 驗’不同之處在於本例中所用之土壤來自於彰化地區之重 金屬污染土壤,清洗之結果如表3.所示。鎘由2.98ppm, 至 〇·2ρριπ,銅由 l〇,7ppm 降至 3.i8ppm,鉛由 23.8ppm 降至 8.79ppm ’ 鋅由I9.6ppm 降至4.27ppm,鉻由2· 34ρρπι 降至〇. 89ppm,鎳由5.28ppm降至1.59ppm,處理後之濃度符合環 保署所暫訂的環境背景標準值以内。 實施例四: 取鎘污染之土壤’利用實施例一之方法,進行土壤 處理及清洗劑之配製,且依實施例一之步驟進行土壤‘除污 工作’與實施例-不同之處在於對污染土壤清洗之時間為 變數,藉此觀察在不同清洗時間内所得效果的差異為 此共進行五批實驗,反應時間分別為1、2、3、4、5、小 時,反應後個別取樣分析殘留於土壤中鑛之濃度,結 示如表4.,隨著反應時間之增加 * * 遂漸減少,當反應時間二二加制殘/Λ二 濃度 町闲两d小砰,剩餘在土壤中之鎘含 。 f0.38ppm已達環保署所訂環境背景值之第三級桿準,决 =反應時間若再增加,則土壌中锡含量可更為減不準/月 實施例五· 利用如實施例一之方法 依實施例一之步驟進行 取含不同濃度之鎘污染土壤, 進行土壤前處理及清洗劑配製,且4363 3 b V. Description of the invention (13) 2,38ppm ′ The concentration after treatment is within the third-level environmental background standard set by the Environmental Protection Agency. Example 3: r Take the actual heavy metal contaminated soil, and carry it out as in the method of Example 1. The experiment is different in that the soil used in this example comes from the heavy metal contaminated soil in the Changhua area. The cleaning results are shown in Table 3. . Cadmium was reduced from 2.98ppm to 0.2pρ, copper was reduced from 10.7ppm to 3.i8ppm, lead was reduced from 23.8ppm to 8.79ppm 'zinc was reduced from I9.6ppm to 4.27ppm, and chromium was reduced from 2.34ρρπ to 0. 89ppm, nickel decreased from 5.28ppm to 1.59ppm, and the concentration after treatment was within the environmental background standard set by the Environmental Protection Agency. Example 4: Take the soil contaminated with cadmium 'Use the method of Example 1 to prepare soil treatment and cleaning agent, and perform the soil' decontamination work 'according to the steps of Example 1 and the example-the difference lies in the pollution The soil cleaning time is variable, so as to observe the difference in the effect obtained in different cleaning times. Five batches of experiments were performed for this purpose. The reaction time was 1, 2, 3, 4, 5, and hours. The concentration of minerals in the soil is shown in Table 4. As the reaction time increases, * * gradually decreases. When the reaction time is 22, the residue / Λ 二 concentration is dangling, and the remaining cadmium in the soil With. f0.38ppm has reached the third level of the environmental background value set by the Environmental Protection Agency. If the reaction time is further increased, the tin content in the soil can be further reduced. Example 5 · Use as in Example 1 Method According to the steps of Example 1, soils containing cadmium contaminated with different concentrations were taken, soil pretreatment and cleaning agent preparation were performed, and

43 63 3 5 五、發明說明(14) 土壤除污工作,與實施例一不同之處在於進料之污染土壌 i農度不同’在本實施例中共進行五批實驗,每批土壤中錦 含量依序為 73_2ppm、65.6ppm、11.8ppm、4.1 7ρρι〇 和 2. 9 6ppm,經處理後分析土壤中鎘含量如表5.所示,不巧 濃度之鎘污染土壤經過清洗除污後殘留於土壤中之鎘含量 介於0· 25〜0· 38ppm之間,均小於環保署所訂環境背景值 第三級樣準。 實施例六: 使用如實施例一相同之方法配製清洗劑及相同的方式 進行實際重金屬污染土壤之清洗,此一使用過之清洗劑作 為本實施例中有關清洗劑電解回收所需之原料。將此用過 之清洗劑置於陽極電解槽中,另使用〇·1Ν H2S04溶液作為 陰極電解液’分別使用白金鈦網及不銹鋼作為陽極與.陰極 材料’外加10V電壓與電流28. 7Α進行電解,反應23小時後 結果如表6.所示’ Pb、Cr·去除效率約70〜8〇%,而cd、43 63 3 5 V. Description of the invention (14) The soil decontamination work differs from the first embodiment in that the contaminated soil of the feed is different in fertility. In this embodiment, five batches of experiments were performed, and the content of brocade in each batch of soil The order is 73_2ppm, 65.6ppm, 11.8ppm, 4.17ρριο and 2.96ppm. The analysis of the cadmium content in the soil after treatment is shown in Table 5. The cadmium contaminated soil with unfortunate concentrations remained in the soil after cleaning and decontamination. The cadmium content in this range is between 0.25 to 0.38 ppm, which is less than the third level of environmental background value set by the Environmental Protection Agency. Example 6: The same method as in Example 1 was used to prepare a cleaning agent and the same method was used to clean the actual heavy metal contaminated soil. This used cleaning agent was used as the raw material required for the electrolytic recovery of the cleaning agent in this example. This used cleaning agent was placed in an anode electrolytic cell, and a 〇 · 1Ν H2S04 solution was used as the catholyte 'using platinum titanium mesh and stainless steel as the anode and the cathode material' plus 10V voltage and current 28. 7Α for electrolysis The results after 23 hours of reaction are shown in Table 6. 'The removal efficiency of Pb, Cr · is about 70 ~ 80%, and cd,

Ni、Zn和Cu之去除效果為92〜99%。 實施例七: 取含鎘、銅、鋅、鉻及鎳等實際污染之土壤,使用如 實施例一相同之方法進行土壌前處理,且依實施例一之步 驟進行土壤除污工作,與實施例一不同之處在於本實施例 中所用之清洗劑乃使用後再經由回收程序處理過之清洗 劑,目的在於証明本發明之清洗劑經電解回收後仍可再次 使用於土壞之清洗。在此清洗劑之回收乃利用電解槽,以 電解的方式在操作電壓3V〜10V且電流密度〇·23 A/cm2的 436335 五、發明說明(15) 條件下,將清洗劑中重金屬及有機質電解去除。經由此方 法回收處理後之清洗劑儲存作為本實驗所需的清洗劑,如 實施例一將污染土壤重量(g )與上述處理後之清洗劑體積 (m 1)比以1 / 4之比例混合於清洗槽中進行清洗等步驟,然 後分析土壤中重金屬剩餘含量及除污效率,結果如表7所 示’殘存於土壤中之重金屬均小於環保署所訂環境背景值 之第三級標準β 圖面之簡單說明 第一圖表示本發明處理方法之逆向交又清洗操作流程 圖。 符號說明: Α 清洗劑 Β 污染土壌 C,C,第一道清洗 D 第二道清洗 A,,A” 用過之清洗劑 、 B1誕第一道清洗後之土壤 M 乾淨土壌 E 再生處理槽The removal effect of Ni, Zn and Cu is 92 ~ 99%. Embodiment 7: Take soils containing actual pollution such as cadmium, copper, zinc, chromium, and nickel, use the same method as in Example 1 to perform soil pretreatment, and perform soil decontamination according to the steps of Example 1. One difference is that the cleaning agent used in this embodiment is a cleaning agent that is processed after being used and then processed through a recovery program, and the purpose is to prove that the cleaning agent of the present invention can be reused for cleaning the soil after being recovered by electrolysis. Here, the cleaning agent is recovered by using an electrolytic cell in an electrolytic manner at an operating voltage of 3V to 10V and a current density of 236335 A / cm2. 436335 V. Description of the invention (15) The heavy metals and organic matter in the cleaning agent are electrolyzed Remove. The cleaning agent recovered and processed by this method is stored as the cleaning agent required for this experiment. As in Example 1, the weight of the contaminated soil (g) and the volume (m 1) of the cleaning agent after the above treatment are mixed at a ratio of 1/4. Perform cleaning and other steps in the cleaning tank, and then analyze the remaining content of heavy metals in the soil and the decontamination efficiency. The results are shown in Table 7. 'The heavy metals remaining in the soil are less than the third-level standard β chart of the environmental background value set by the Environmental Protection Agency. The brief description of the first figure shows the flow chart of the reverse and cleaning operation of the processing method of the present invention. Explanation of symbols: Α cleaning agent Β contaminated soil C, C, first cleaning D second cleaning A ,, A "used cleaning agent, B1 soil after the first cleaning M clean soil 壌 E regeneration treatment tank

436335 五'發明說明(16) 表1.鎘污染土壌除污效率 原土鎘濃度(ppm) 清洗後土壤鎘濃度(ppm) 除污率 73.2 0.30 99.5% 65.6 0.38 99.4% 11.8 0.38 96. 8%' 4.2 0.25 94.0% 3.0 0.37 87.5% 1.0 0.20 79.3% 0.3 <0.1 >70.6% 台灣地區土壤重金屬含量標準與等級區分表中鎘金屬第三級標 準值:0.05〜0.39ppm uni 第21頁 43 633 5 五、發明說明(17) 表2.重金屬污染土壤除污結果 桃 困 中 福 區 元素 原土壤金屬漢度(ppm) 土壤清洗後金眉濃度(ppm) 除污率 第三級標準 Cd 4.2 0.25 94.0% 0‘05 〜0.39 Cu 61.5 6.93 88.7% 12 〜20 Pb 26.1 8.66 66.8% 1〜15 Zn 42.4 23.00 45.8% 11 〜25 Ni 34.8 2.38 93.2% 2〜10436335 Five 'invention description (16) Table 1. Decontamination efficiency of cadmium-contaminated soil. Decontamination efficiency of raw soil. Cadmium concentration (ppm). Soil cadmium concentration (ppm) after decontamination. 73.2 0.30 99.5% 65.6 0.38 99.4% 11.8 0.38 96.8%' 4.2 0.25 94.0% 3.0 0.37 87.5% 1.0 0.20 79.3% 0.3 < 0.1 > 70.6% Taiwan's soil heavy metal content standards and grades in the table for the classification of cadmium metal in the third grade standard value: 0.05 ~ 0.39ppm uni Page 21 43 633 5 V. Explanation of the invention (17) Table 2. Results of decontamination of soil contaminated by heavy metals Contamination of elemental original soil metal content (ppm) in Zhongfu District, Taojin, Jinmei concentration after soil cleaning (ppm) Decontamination rate third-level standard Cd 4.2 0.25 94.0 % 0'05 to 0.39 Cu 61.5 6.93 88.7% 12 to 20 Pb 26.1 8.66 66.8% 1 to 15 Zn 42.4 23.00 45.8% 11 to 25 Ni 34.8 2.38 93.2% 2 to 10

HI 第22頁 436335 五、發明說明(18) 表3.重金屬污染土壤除污結果 元素 原土壤金屬濃度(ppm) 土壤清洗後金屬濃度(ppm) 除污率 第三級標準 彰 Cd 3.3 0.21 93.9% 0.05 〜0.39 化 Cu 4.6 3.17 31.1% 12 〜20 和 Pb 40.6 13.00 67.9% 1〜15 美 Zn 11.7 3.96 66.2% 11 〜25 區 Cr 15.0 0.89 94.1% 〇h 〜10 Ni 1.9 1.58 16.8% 2〜10 mill 第23頁 4363i 五、發明說明(19) C-4-1 m K) -ω tJi | 時間(Hr) S 固(g)/液(ml) 3.49 3.49 3.49 3.49 3.49 土壌錢濃度(ppm) 0.61 0.51 0.38 0.37 0.25 j 清洗後土壤鎘濃度(ppm) >4‘縳睁鉍钸港iifelr鎵(眾S瘅左)HI Page 22 436335 V. Description of the invention (18) Table 3. Results of decontamination of heavy metal contaminated soil Elemental soil metal concentration (ppm) Metal concentration after soil cleaning (ppm) Decontamination rate third level standard Cd 3.3 0.21 93.9% 0.05 to 0.39 Cu 4.6 3.17 31.1% 12 to 20 and Pb 40.6 13.00 67.9% 1 to 15 US Zn 11.7 3.96 66.2% 11 to 25 Zone Cr 15.0 0.89 94.1% 〇h to 10 Ni 1.9 1.58 16.8% 2 to 10 mill No. Page 23, 4363i V. Description of the invention (19) C-4-1 m K) -ω tJi | Time (Hr) S Solid (g) / Liquid (ml) 3.49 3.49 3.49 3.49 3.49 Local money concentration (ppm) 0.61 0.51 0.38 0.37 0.25 j cadmium concentration in soil after cleaning (ppm) > 4 'bismuth port iifelr gallium (Zhong S 瘅 left)

第24頁 43 63 五、發明說明(20) C-6-4 C-6-3 C-6-5 I C-6-2 C-6-1 OJ U) U> 時間(Hr) mrnt 5: 5 1—i 1—k 固(g),液㈣ 2.96 4.17 11.81 65.62 73.21 原土壤錄濃度(ppm) 0.37 0.25 0.38 0.38 0.37 | 清洗後土壤鎘濃度(ppm) ; 87.5% 94.0% 96.8% 99.4% 99.5% 除污率Page 24 43 63 V. Description of the invention (20) C-6-4 C-6-3 C-6-5 I C-6-2 C-6-1 OJ U) U > Time (Hr) mrnt 5: 5 1-i 1-k solid (g), liquid radon 2.96 4.17 11.81 65.62 73.21 Original recorded soil concentration (ppm) 0.37 0.25 0.38 0.38 0.37 | Soil cadmium concentration (ppm) after cleaning; 87.5% 94.0% 96.8% 99.4% 99.5 Decontamination rate

第25頁 436335 五、發明說明(21) 表6.用過清洗劑電解回收結果(操作電壓:10V,電流:28.7A,時間:23小哼) 元素 條件 Pb Cd Cu Zn Cr Ni 處理前(ppm) 22 3 227 174 25 87 處理後(ppm) 5 0.2 3 6 7 3 去除率(%) 78 93 99 97 72 96 ·.» 第26頁 43 63 3 S 五、發明說明(22) 表7.經回收後之清洗劑再使用於污染土壤之清洗效杲 彰化和美土壌 元素 原土壌金屬濃度(ppm) 土壤清洗後金屬濃度(ppm) 除污率 Cd 3.9 0.1 97.4% Cu 467 15 96.8% Zn 355 3.8 98.9% Cr 77 9.5 87.8% Ni 170 2.2 98.7%Page 25 436335 V. Description of the invention (21) Table 6. Electrolytic recovery results of used cleaning agent (operating voltage: 10V, current: 28.7A, time: 23 hum) Elemental conditions Pb Cd Cu Zn Cr Ni Before treatment (ppm ) 22 3 227 174 25 87 After treatment (ppm) 5 0.2 3 6 7 3 Removal rate (%) 78 93 99 97 72 96 ·. »Page 26 43 63 3 S V. Description of the invention (22) Table 7. The recovered cleaning agent is reused for the cleaning effect of contaminated soil. Changhua and the beautiful soil element. Raw metal concentration (ppm). Metal concentration (ppm) after soil cleaning. Decontamination rate Cd 3.9 0.1 97.4% Cu 467 15 96.8% Zn 355 3.8 98.9 % Cr 77 9.5 87.8% Ni 170 2.2 98.7%

1HHI 第27頁1HHI Page 27

Claims (1)

43633s 、申婧專利範圍 1 * ~™·.十 穩重金 壤使用以 量垵類化 凊洗處理 2.如申請專 壤之成份 1 β、EB .如申請專 鱗鳆濃度 4,如中請專 ,冷染土 使用 傳%至陰 總有機碳 •如申請專 與第1、3 .如申請專 採用電解 ;•如申請專 卷,係將 由3V-10V 解而達成 氧化的方式β — 利範圍第7項所述之歡收每 待處理清洗劑露於陽極槽於操作範圍 0.6 A/cm2之條件下,施以電 屬污染土壤之處理大 磷酸或磷酸鹽溶液為主劑;2重金屬污染土 合物均勺人而士 “劑並可添加無機酸及少 而去除所含重金屬成份之方法、劑加:以 利範圍第1項所述之方.、各,f i 〈万去其中重金屬污染土 I含鎘、銅、鋅、鎳.、鉛、鉻等週期表上 、VIB、硼B及IVA族等金屬元素之一部份。 利範圍第1項所述之方法,其中清洗劑主劑之 範圍以趙積比而言在50%以下。 利Ιε圍第1項所述之方法,其中所用清洗劑 壌混合後開始清洗之溫度為沸點以下(;Α 於重金屬污染土壤除污用之清洗劑的 電解及氧化破壞的方式將置於陽極槽中亦青 之金屬藉由電場之作用’使其透過離子交換膜 極,同時藉由外加電壓之作用將陽極清洗劑中 含量降低,經處青洗劑則再回收使用。 利範圍第5項所述其中清洗劑的成份 或4項中所界定的之成份相同。 利範圍第5項所述其中清洗劑回收係 奮. 電流密度〇. 243633s, Shen Jing's patent scope 1 * ~ ™ ·. Ten stable gold soils are used for quantification and rinsing treatment. 2. If you apply for the special ingredient 1 β, EB. If you apply for the special scale 鳆 concentration 4, please refer to the special The use of cold-stained soil passes to the total organic carbon of the anion. • If you apply for the first and third. If you apply for electrolysis; • If you apply for a special volume, the oxidation will be achieved by 3V-10V solution. The cleansing agents to be treated as described in item 7 are exposed to the anode tank under the operating range of 0.6 A / cm2, and treated with electro-polluted soil as the main agent; 2 heavy metal contaminated soil compounds "Every spoon" can be added with inorganic acid and a method for removing heavy metal components, and the method of adding the agent: the method described in item 1 of the range of benefits, each, fi <10,000, where the heavy metal contaminated soil I contains Cadmium, copper, zinc, nickel, lead, chromium and other periodic elements of the periodic table, VIB, boron B and IVA and other metal elements. The method described in item 1, the range of the main agent of the cleaning agent is For Zhao Ji ratio, it is less than 50%. The method described in item 1 of Li Yi ε, in which the clear The temperature at which the cleaning agent starts to be mixed after boiling is below the boiling point (A) The electrolytic and oxidative destruction methods of the cleaning agent used for decontamination of heavy metal contaminated soil will be placed in the anode tank and the green metal will be allowed to pass through the action of the electric field Ion-exchange membrane electrode, at the same time, the content of the anode cleaning agent is reduced by the application of voltage, and the green cleaning agent is recycled for reuse. The component of the cleaning agent described in item 5 or the one defined in 4 The composition is the same. The cleaning agent recovery system described in Item 5 of the beneficial range. Current density 0.2
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106734179A (en) * 2017-03-08 2017-05-31 祝凤娟 A kind of soil restoring device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106734179A (en) * 2017-03-08 2017-05-31 祝凤娟 A kind of soil restoring device

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