TWI443069B - Process for the preparation of six-valent iron - Google Patents
Process for the preparation of six-valent iron Download PDFInfo
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- TWI443069B TWI443069B TW99145289A TW99145289A TWI443069B TW I443069 B TWI443069 B TW I443069B TW 99145289 A TW99145289 A TW 99145289A TW 99145289 A TW99145289 A TW 99145289A TW I443069 B TWI443069 B TW I443069B
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本發明是有關於一種六價鐵之製備方法,特別是有關於一種利用含鐵汙泥來製備六價鐵之方法。The invention relates to a preparation method of hexavalent iron, in particular to a method for preparing hexavalent iron by using iron-containing sludge.
伴隨印刷電路板製造業、金屬表面處理業及電鍍業在台灣的發展,大量的重金屬廢液也隨之產生。重金屬廢液與廢水如沒有經適當處理,任意排放,將對生態環境造成極為嚴重的破壞。因此,含重金屬廢棄物與廢水的回收與處理一直受到主管機關與環保團體相當的關注。Along with the development of printed circuit board manufacturing, metal surface treatment industry and electroplating industry in Taiwan, a large amount of heavy metal waste liquid has also been produced. If heavy metal waste liquid and wastewater are not properly treated and discharged, it will cause extremely serious damage to the ecological environment. Therefore, the recycling and treatment of heavy metal-containing wastes and wastewater has been receiving considerable attention from the competent authorities and environmental groups.
混凝是一種常用在重金屬廢水處理的方法。目前混凝劑種類眾多,可分為鋁鹽與鐵鹽,主要常見的無機混凝劑如:硫酸鋁、聚合氯化鋁、氯化鐵、硫酸亞鐵等,一般使用混凝劑以鋁鹽作為混凝劑較鐵鹽來的普遍,主要是因為鋁鹽混凝劑不會造成處理水酸鹼值(PH)的劇烈變化,且不會增加水中色度。然而,使用混凝法來處理重金屬廢水會產生大量的有害污泥,造成嚴重的污泥處置問題。因此有人提出以六價鐵來處理重金屬廢水。Coagulation is a method commonly used in the treatment of heavy metal wastewater. At present, there are many kinds of coagulants, which can be divided into aluminum salt and iron salt. The main common inorganic coagulants are: aluminum sulfate, polyaluminum chloride, ferric chloride, ferrous sulfate, etc., generally using a coagulant to aluminum salt. The prevalence of coagulants as iron salts is mainly due to the fact that the aluminum salt coagulant does not cause drastic changes in the pH of the treated water and does not increase the color of the water. However, the use of coagulation to treat heavy metal wastewater produces large amounts of harmful sludge, causing serious sludge disposal problems. Therefore, it has been proposed to treat heavy metal wastewater with hexavalent iron.
六價鐵是具有氧化功能與混凝功能的水質處理藥劑,能有效地去除水中的懸浮物、重金屬、及多中水中污染物。六價鐵反應後的最終產物不會對環境產生不良影響,所以被稱為綠色氧化劑。六價鐵可水解成高電荷產物及Fe(OH)3 ,其有良好的混凝及吸附作用,對水中重金屬,例如Mn2 + 、Cu2 + 、Pb2 + 、Cd2 + 、Cr3 + 和Hg2 + ,皆有良好的去除效果,對同濃度的重金屬可完全氧化。Hexavalent iron is a water treatment agent with oxidation function and coagulation function, which can effectively remove suspended solids, heavy metals, and many water pollutants in water. The final product after the hexavalent iron reaction does not adversely affect the environment, so it is called a green oxidant. Hexavalent iron can be hydrolyzed into a highly charged product and Fe(OH) 3 , which has good coagulation and adsorption, and heavy metals in water, such as Mn 2 + , Cu 2 + , Pb 2 + , Cd 2 + , Cr 3 + and Hg 2 +, there are good removal effect of the same concentration of heavy metals may be completely oxidized.
由於六價鐵對於水體中的重金屬離子有強力的去除能力,因此極需一種低成本的六價鐵製備方法。Since hexavalent iron has a strong ability to remove heavy metal ions in water, a low-cost preparation method of hexavalent iron is highly desirable.
本發明之一方面是在提供一種六價鐵之製備方法,以利用含鐵汙泥來製備六價鐵。One aspect of the present invention is to provide a method for preparing hexavalent iron to prepare hexavalent iron using iron-containing sludge.
根據本發明之一實施例,在此六價鐵之製備方法中,首先根據預設值來調整含鐵汙泥的含水率。接著,對含鐵汙泥進行酸處理步驟,以將酸洗液與含鐵汙泥均勻混合,使含鐵汙泥中的鐵溶解至酸洗液中。然後,進行固液分離步驟,以將酸洗液與含鐵污泥分開。接著,進行濕式氧化步驟,以利用氧化劑來於強鹼環境下氧化酸洗液中的鐵離子,以產生六價鐵離子。然後,進行沉澱步驟,以利用鹽類來與六價鐵離子形成高鐵酸鹽。According to an embodiment of the present invention, in the preparation method of the hexavalent iron, the moisture content of the iron-containing sludge is first adjusted according to a preset value. Next, the iron-containing sludge is subjected to an acid treatment step to uniformly mix the pickling liquid with the iron-containing sludge to dissolve the iron in the iron-containing sludge into the pickling liquid. Then, a solid-liquid separation step is performed to separate the pickling liquid from the iron-containing sludge. Next, a wet oxidation step is performed to oxidize iron ions in the acid wash solution with a oxidizing agent in a strong alkali environment to produce hexavalent iron ions. Then, a precipitation step is performed to form a ferrate salt with hexavalent iron ions using a salt.
請同時參照第1圖和第2圖,第1圖係繪示根據本發明一實施例之六價鐵製備系統100的設備示意圖,第2圖係繪示應用六價鐵製備系統100之六價鐵製備方法200的流程示意圖。本實施例之六價鐵製備方法200可將含鐵汙泥中的鐵成分提取出來並製成六價鐵,如此不但可獲得具有高度利用價值的六價鐵,亦可同時可減少汙泥的重金屬含量。Please refer to FIG. 1 and FIG. 2 simultaneously. FIG. 1 is a schematic diagram showing the apparatus of the hexavalent iron preparation system 100 according to an embodiment of the present invention, and FIG. 2 is a diagram showing the hexavalent value of the hexavalent iron preparation system 100. Schematic diagram of the process of the iron preparation method 200. The hexavalent iron preparation method 200 of the present embodiment can extract the iron component in the iron-containing sludge and prepare the hexavalent iron, so that not only the hexavalent iron having high utilization value can be obtained, but also the heavy metal of the sludge can be reduced at the same time. content.
本實施例之六價鐵製備系統100包含震盪裝置110、固液分離裝置120、反應槽130、攪拌裝置140和乾燥裝置150,以下將詳細介紹六價鐵製備系統100與六價鐵製備方法200的操作機制。The hexavalent iron preparation system 100 of the present embodiment includes an oscillating device 110, a solid-liquid separation device 120, a reaction tank 130, a stirring device 140, and a drying device 150. The hexavalent iron preparation system 100 and the hexavalent iron preparation method 200 will be described in detail below. Operating mechanism.
在本實施例之六價鐵製備方法200中,首先進行含水率調整步驟210,以根據一預設值來調整含鐵汙泥的含水率。在本實施例中,含鐵汙泥的含水率被調整為10~20%。然後,進行酸洗步驟220。在酸洗步驟220中,從汙泥回收槽160所取出之待處理污泥係與酸洗液一同置入震盪裝置110來進行酸洗,以使汙泥中的鐵溶解至酸洗液中。本實施例係採用震盪的方式來進行酸洗,而酸洗液則是使用硝酸,但本發明之實施例並不受限於此。In the hexavalent iron preparation method 200 of the present embodiment, the moisture content adjustment step 210 is first performed to adjust the moisture content of the iron-containing sludge according to a predetermined value. In the present embodiment, the moisture content of the iron-containing sludge is adjusted to 10 to 20%. Then, a pickling step 220 is performed. In the pickling step 220, the sludge to be treated taken out from the sludge recovery tank 160 is placed in the oscillating device 110 together with the pickling liquid to be pickled to dissolve the iron in the sludge into the pickling liquid. In the present embodiment, pickling is carried out in an oscillating manner, and in the pickling liquid, nitric acid is used, but the embodiment of the present invention is not limited thereto.
接著,進行固液分離步驟230。在固液分離步驟230中,固液分離裝置120係從步驟220之汙泥與酸洗液的混合物中,將含有鐵的酸洗液分離出來。本實施例所採用的固液分離裝置包含有過濾篩網,此篩網可過濾出固體汙泥,以將液體和固體分離,但本發明實施例之固液分離裝置並不受限於此。Next, a solid-liquid separation step 230 is performed. In the solid-liquid separation step 230, the solid-liquid separation device 120 separates the acid-containing washing liquid containing iron from the mixture of the sludge and the pickling liquid in the step 220. The solid-liquid separation device used in the present embodiment includes a filter screen which can filter solid sludge to separate the liquid and the solid, but the solid-liquid separation device of the embodiment of the present invention is not limited thereto.
然後,進行濕式氧化步驟240。在濕式氧化步驟240中,含有鐵之酸洗液、氧化劑、鹼劑和鹽類被加入至反應槽130中,並配合攪拌裝置140來將其均勻混合,以產生高鐵酸鹽。Then, a wet oxidation step 240 is performed. In the wet oxidation step 240, an acid-containing pickling solution, an oxidizing agent, an alkali agent, and a salt are added to the reaction tank 130, and uniformly mixed with the stirring device 140 to produce ferrate.
本實施例之氧化劑、鹼劑和鹽類係分別選用次氯酸鈉、氫氧化鈉和氫氧化鉀。在濕式氧化步驟240中,首先將次氯酸鈉與酸洗液一同置入反應槽130中,以利用次氯酸根來氧化酸洗液中的鐵,使酸洗液中的三價鐵變成六價鐵。接著,再將氫氧化鈉加入反應槽130中,以提供鹼性的反應環境來促進次氯酸根的氧化作用。雖然,加入氫氧化鈉後,即可得到具有六價鐵的高鐵酸鈉,但由於高鐵酸鈉為不穩定的化合物,因此在濕式氧化步驟240後,再進行沉澱步驟250,以利用一鹽類來與六價鐵離子形成高鐵酸鹽,而沉澱出來。在本實施例中,係加入氫氧化鉀至反應槽130中,以沉澱出較為穩定的高鐵酸鉀。The oxidizing agent, the alkali agent and the salt of the present embodiment are selected from sodium hypochlorite, sodium hydroxide and potassium hydroxide, respectively. In the wet oxidation step 240, sodium hypochlorite is first placed in the reaction tank 130 together with the acid washing liquid to oxidize the iron in the acid washing liquid by using hypochlorite to change the ferric iron in the acid washing liquid into hexavalent iron. . Next, sodium hydroxide is added to the reaction tank 130 to provide an alkaline reaction environment to promote the oxidation of hypochlorite. Although sodium ferrate having hexavalent iron is obtained after the addition of sodium hydroxide, since sodium ferrate is an unstable compound, after the wet oxidation step 240, a precipitation step 250 is further performed to utilize a salt. It forms a ferrate with hexavalent iron ions and precipitates. In this embodiment, potassium hydroxide is added to the reaction tank 130 to precipitate a relatively stable potassium ferrate.
然後,進行乾燥步驟260,以利用乾燥裝置150來乾燥高鐵酸鉀上的水分。在本實施例中,乾燥裝置150係利用熱風來乾燥高鐵酸鉀上的水分,但本發明之實施例並不受限於此。Then, a drying step 260 is performed to dry the moisture on the potassium ferrate using the drying device 150. In the present embodiment, the drying device 150 uses hot air to dry the moisture on the potassium ferrate, but the embodiment of the present invention is not limited thereto.
由以上實施例可知,本發明實施例之六價鐵製備方法200係使用廢棄的含鐵汙泥作為原料,因此本發明實施例之六價鐵的製備成本相當低廉。It can be seen from the above examples that the hexavalent iron preparation method 200 of the embodiment of the present invention uses waste iron-containing sludge as a raw material, and therefore the preparation cost of the hexavalent iron of the embodiment of the present invention is relatively low.
另外,值得一提的是,在本發明其他實施例中,六價鐵製備可更包含溫度控制步驟和酸液回收步驟。在濕式氧化步驟240中,當氫氧化鈉加入反應槽130時,會釋放出很高的熱能,並使反應槽130中的溫度大幅上升,如此將不利後續化學反應的進行。因此,在進行濕式氧化步驟240時,同時進行溫度控制步驟來將反應槽130的溫度維持在攝氏25度至30度之間,如此可避免高溫帶來不利的影響。在酸液回收步驟中,係根據一預設回收率來將從固液分離步驟230所得到的含鐵酸洗液分為兩部份,其中一部分係作為六價鐵生成的原料,而另一部份可回收作為酸洗步驟中的酸洗液,如此可減少酸洗液的消耗。In addition, it is worth mentioning that in other embodiments of the invention, the hexavalent iron preparation may further comprise a temperature control step and an acid recovery step. In the wet oxidation step 240, when sodium hydroxide is added to the reaction tank 130, high heat energy is released and the temperature in the reaction tank 130 is greatly increased, which may adversely affect the subsequent chemical reaction. Therefore, when the wet oxidation step 240 is performed, the temperature control step is simultaneously performed to maintain the temperature of the reaction tank 130 between 25 and 30 degrees Celsius, so that adverse effects of high temperature can be avoided. In the acid recovery step, the ferric acid-containing washing liquid obtained from the solid-liquid separation step 230 is divided into two parts according to a predetermined recovery rate, one of which is used as a raw material for the formation of hexavalent iron, and the other is Partially recoverable as an acid wash in the pickling step, which reduces the consumption of pickling solution.
雖然本發明已以數個實施例揭露如上,然其並非用以 限定本發明,在本發明所屬技術領域中任何具有通常知識者,在不脫離本發明之精神和範圍內,當可作各種之更動與潤飾,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。Although the invention has been disclosed above in several embodiments, it is not intended to The invention is defined by the general knowledge of the present invention, and various modifications and refinements can be made without departing from the spirit and scope of the invention. The scope is defined.
100‧‧‧六價鐵製備系統100‧‧‧ hexavalent iron preparation system
110‧‧‧震盪裝置110‧‧‧ oscillating device
120‧‧‧液分離裝置120‧‧‧Liquid separation device
130‧‧‧反應槽130‧‧‧Reaction tank
140‧‧‧攪拌裝置140‧‧‧Agitator
150‧‧‧乾燥裝置150‧‧‧Drying device
160‧‧‧汙泥回收槽160‧‧‧Sludge recovery tank
200‧‧‧六價鐵製備方法200‧‧‧ hexavalent iron preparation method
210‧‧‧含水率調整步驟210‧‧‧Water content adjustment steps
220‧‧‧酸洗步驟220‧‧‧ pickling step
230‧‧‧固液分離步驟230‧‧‧ Solid-liquid separation steps
240‧‧‧濕式氧化步驟240‧‧‧ Wet oxidation step
250‧‧‧沉澱步驟250‧‧‧Precipitation step
260‧‧‧乾燥步驟260‧‧‧ drying step
為讓本發明之上述和其他目的、特徵、和優點能更明顯易懂,上文特舉一較佳實施例,並配合所附圖式,作詳細說明如下:第1圖係繪示根據本發明一實施例之六價鐵製備系統的設備示意圖。The above and other objects, features and advantages of the present invention will become more <RTIgt; A schematic diagram of an apparatus for a hexavalent iron preparation system according to an embodiment of the invention.
第2圖係繪示根據本發明一實施例之六價鐵製備方法的流程示意圖。2 is a schematic flow chart showing a method for preparing hexavalent iron according to an embodiment of the present invention.
200...六價鐵製備方法200. . . Hexavalent iron preparation method
210...含水率調整步驟210. . . Moisture rate adjustment step
220...酸洗步驟220. . . Pickling step
230...固液分離步驟230. . . Solid-liquid separation step
240...濕式氧化步驟240. . . Wet oxidation step
250...沉澱步驟250. . . Precipitation step
260...乾燥步驟260. . . Drying step
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