TWI627137B - Method for recycling waste to produce aluminum sulfate - Google Patents
Method for recycling waste to produce aluminum sulfate Download PDFInfo
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- TWI627137B TWI627137B TW106101165A TW106101165A TWI627137B TW I627137 B TWI627137 B TW I627137B TW 106101165 A TW106101165 A TW 106101165A TW 106101165 A TW106101165 A TW 106101165A TW I627137 B TWI627137 B TW I627137B
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Abstract
本發明係有關一種回收廢棄物製造硫酸鋁之方法,其包括下列步驟:a.在反應槽內混合含鋁汙泥與含鋁廢液,反應形成氫氧化鋁;b.在反應槽內混合含硫酸廢液,讓氫氧化鋁與硫酸反應形成硫酸鋁;以及c.進行固液分離,分離出硫酸鋁溶液與汙泥;其中,含鋁汙泥為環保署廢棄物代碼為D-0902的含鋁汙泥,含鋁廢液為環保署廢棄物代碼為C-0201的含鋁廢液,含硫酸廢液為環保署廢棄物代碼為C-0202的含硫酸廢液。藉此,用以提供一種回收廢棄物製造硫酸鋁之方法,而具有處理廢棄物且資源回收再利用之功效。 The invention relates to a method for producing aluminum sulfate by recycling waste, which comprises the following steps: a. mixing aluminum-containing sludge and aluminum-containing waste liquid in a reaction tank to react to form aluminum hydroxide; b. mixing in the reaction tank Sulfuric acid waste liquid, allowing aluminum hydroxide to react with sulfuric acid to form aluminum sulfate; and c. performing solid-liquid separation to separate aluminum sulfate solution and sludge; wherein the aluminum-containing sludge is contained in the environmental protection department waste code D-0902 The aluminum sludge and aluminum-containing waste liquid are the aluminum-containing waste liquid of the Environmental Protection Agency's waste code C-0201, and the sulfuric acid waste liquid is the sulfuric acid waste liquid of the Environmental Protection Agency's waste code C-0202. Thereby, it is used to provide a method for recycling waste to produce aluminum sulfate, and has the effect of treating waste and recycling resources.
Description
本發明係有關一種回收廢棄物製造硫酸鋁之方法,尤指一種先將含鋁汙泥與含鋁廢液混合反應形成氫氧化鋁,再混合含硫酸廢液,並在適當的pH值與溫度的條件下,讓氫氧化鋁與硫酸反應形成硫酸鋁之設計者。 The invention relates to a method for producing aluminum sulfate by recycling waste, in particular to first mixing an aluminum-containing sludge with an aluminum-containing waste liquid to form aluminum hydroxide, and then mixing the sulfuric acid-containing waste liquid at an appropriate pH and temperature. Under the conditions, the aluminum hydroxide is reacted with sulfuric acid to form a designer of aluminum sulfate.
按,鋁擠型產品之製造過程乃將鋁錠及合金金屬經熔解、澆注、鑄造、中和切削及鹼洗等程序;其中,汙水程序產生含鋁汙泥(環保署廢棄物代碼為D-0902),鹼洗程序產生含鋁廢液(pH值大(等)於12.5,環保署廢棄物代碼為C-0201),清洗或蝕刻程序產生含硫酸廢液(pH值小(等)於2,環保署廢棄物代碼為C-0202)。然而,由於前述之廢棄物若施以適當的處理,不但可避免造成環境的污染,尚具有資源回收再利用的價值。 According to the manufacturing process of aluminum extrusion products, the aluminum ingots and alloy metals are melted, cast, cast, neutralized and alkali washed; among them, the sewage program produces aluminum sludge (the EPA waste code is D) -0902), the alkaline washing process produces aluminum-containing waste liquid (pH value (equal) at 12.5, EPA waste code is C-0201), cleaning or etching process produces sulfuric acid-containing waste liquid (pH value is small (etc.)) 2. The EPA waste code is C-0202). However, if the aforementioned waste is properly treated, it not only avoids environmental pollution, but also has the value of recycling and recycling of resources.
本發明之主要目的,係欲提供一種回收廢棄物製造硫酸鋁之方法,而具有處理廢棄物且資源回收再利用之功效。 The main object of the present invention is to provide a method for recycling waste to produce aluminum sulfate, which has the effect of treating waste and recycling resources.
為達上述功效,本發明之技術特徵,係包括下列步驟:a.在反應槽內混合含鋁汙泥與含鋁廢液,反應形成氫氧化鋁;b.在反應槽內混合含硫酸廢液,讓氫氧化鋁與硫酸反應形成硫酸鋁;以及c.進行固液分離,分離出硫酸鋁溶液與汙泥;其中,含鋁汙泥為環保署廢棄物代碼為D-0902的含鋁汙泥,含鋁廢液為環保署廢棄物代碼為C-0201的含鋁廢液,含硫酸廢液為環保署廢棄物代碼為C-0202的含硫酸廢液。 In order to achieve the above effects, the technical features of the present invention include the following steps: a. mixing the aluminum-containing sludge and the aluminum-containing waste liquid in the reaction tank to form aluminum hydroxide; b. mixing the sulfuric acid-containing waste liquid in the reaction tank , allowing aluminum hydroxide to react with sulfuric acid to form aluminum sulfate; and c. performing solid-liquid separation to separate aluminum sulfate solution and sludge; wherein the aluminum-containing sludge is an aluminum-containing sludge of the Environmental Protection Agency's waste code D-0902 The aluminum-containing waste liquid is the aluminum-containing waste liquid of the Environmental Protection Agency's waste code C-0201, and the sulfuric acid waste liquid is the sulfuric acid waste liquid of the Environmental Protection Agency's waste code C-0202.
此外,步驟b係控制在低pH值的條件下進行反應,其中,pH值3-5為佳;再者,步驟b進一步添加硫酸控制反應溫度,其中,步驟b分為兩階段反應,第一階段的反應溫度控制在70-90℃,第二階段的反應溫度控制在100℃;又,步驟a進一步添加過量鋁原料進行反應,其中,進一步添加之鋁原料為鋁錠或氫氧化鋁;另,步驟c以板壓機進行固液分離。 In addition, step b is controlled to carry out the reaction under conditions of low pH, wherein pH 3-5 is preferred; further, step b further adds sulfuric acid to control the reaction temperature, wherein step b is divided into two-stage reaction, first The reaction temperature of the stage is controlled at 70-90 ° C, and the reaction temperature of the second stage is controlled at 100 ° C; in addition, step a further adds excess aluminum raw material to carry out the reaction, wherein the further added aluminum raw material is aluminum ingot or aluminum hydroxide; Step c is subjected to solid-liquid separation by a plate press.
藉此,先將含鋁汙泥與含鋁廢液混合反應形成氫氧化鋁,再混合含硫酸廢液,並在適當的pH值與溫度的條件下,讓氫氧化鋁與硫酸反應形成硫酸鋁,而硫酸鋁產品可提供廢水處理混凝程序之混凝藥劑使用,不但處理了多種廢棄物且回收了可再利用的資源, Thereby, the aluminum-containing sludge is mixed with the aluminum-containing waste liquid to form aluminum hydroxide, and then the sulfuric acid-containing waste liquid is mixed, and the aluminum hydroxide and sulfuric acid are reacted to form aluminum sulfate under appropriate pH and temperature conditions. And the aluminum sulfate product can be used as a coagulating agent for the wastewater treatment coagulation process, which not only processes a variety of wastes but also recycles reusable resources.
〔圖1〕係本發明之製造流程圖。 [Fig. 1] is a manufacturing flow chart of the present invention.
首先,請參閱〔圖1〕所示,本發明係包括下列步驟:a.在反應槽內混合環保署廢棄物代碼為D-0902的含鋁汙泥與環保署廢棄物代碼為C-0201的含鋁廢液,反應形成氫氧化鋁,反應式:Al3++3OH-→Al(OH)3,且為了確保具有足夠的鋁原料參與反應,乃可進一步添加過量鋁原料進行反應,而添加之鋁原料為鋁錠或氫氧化鋁;b.在反應槽內混合環保署廢棄物代碼為C-0202的含硫酸廢液,讓氫氧化鋁與硫酸反應形成硫酸鋁,反應式:2Al(OH)3+3H2SO4→Al2(SO4)3+6H2O,並利用鋁於低pH值具有高溶解度的特性,而將pH值控制在3-5的低pH值條件下進行反應,另可進 一步添加硫酸控制反應溫度,且分為兩階段反應,第一階段的反應溫度控制在70-90℃,第二階段的反應溫度控制在100℃;以及c.以板壓機進行固液分離,分離出硫酸鋁溶液與汙泥。 First, please refer to [Fig. 1], the present invention includes the following steps: a. mixing the EPA waste code D-0902 containing aluminum sludge and the EPA waste code C-0201 in the reaction tank. The aluminum-containing waste liquid reacts to form aluminum hydroxide, and the reaction formula: Al 3+ +3OH - → Al(OH) 3 , and in order to ensure that sufficient aluminum raw material participates in the reaction, an excess of aluminum raw material may be further added for reaction, and added The aluminum raw material is aluminum ingot or aluminum hydroxide; b. mixed with the effluent containing sulfuric acid waste code C-0202 in the reaction tank, and reacting aluminum hydroxide with sulfuric acid to form aluminum sulfate, reaction formula: 2Al(OH 3 +3H 2 SO 4 →Al 2 (SO 4 ) 3 +6H 2 O, and use aluminum to have high solubility at low pH, and control the pH at a low pH of 3-5 Further, sulfuric acid may be further added to control the reaction temperature, and is divided into two-stage reaction, the reaction temperature of the first stage is controlled at 70-90 ° C, the reaction temperature of the second stage is controlled at 100 ° C; and c. is solidified by a plate press. The liquid is separated, and the aluminum sulfate solution and the sludge are separated.
基於如是之方法,本發明先將環保署廢棄物代碼為D-0902的含鋁汙泥與環保署廢棄物代碼為C-0201的含鋁廢液,混合反應形成氫氧化鋁,再混合環保署廢棄物代碼為C-0202的含硫酸廢液,並在適當的pH值與溫度的條件下,讓氫氧化鋁與硫酸反應形成硫酸鋁,而硫酸鋁產品可提供廢水處理混凝程序之混凝藥劑使用,不但處理了多種廢棄物且回收了可再利用的資源,而具有處理廢棄物且資源回收再利用之功效。 Based on the method of the present invention, the invention firstly combines the aluminum-containing sludge of the EPA waste code D-0902 with the aluminum-containing waste liquid of the Environmental Protection Agency waste code C-0201, and reacts to form aluminum hydroxide, and then mixes with the EPA. The waste code is C-0202 containing sulfuric acid waste liquid, and under the appropriate pH and temperature conditions, the aluminum hydroxide reacts with sulfuric acid to form aluminum sulfate, and the aluminum sulfate product can provide the coagulation process of the wastewater treatment coagulation process. The use of the chemical agent not only treats a variety of wastes but also recycles the reusable resources, and has the effect of treating the waste and recycling the resources.
綜上所述,本發明所揭示之技術手段,確具「新穎性」、「進步性」及「可供產業利用」等發明專利要件,祈請 鈞局惠賜專利,以勵發明,無任德感。 To sum up, the technical means disclosed in the present invention have the invention patents such as "novelty", "progressiveness" and "available for industrial use", and pray for the patent to be invented by the bureau. German sense.
惟,上述所揭露之圖式、說明,僅為本發明之較佳實施例,大凡熟悉此項技藝人士,依本案精神範疇所作之修飾或等效變化,仍應包括在本案申請專利範圍內。 The drawings and the descriptions of the present invention are merely preferred embodiments of the present invention, and those skilled in the art, which are subject to the spirit of the present invention, should be included in the scope of the patent application.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1350065A (en) * | 2000-10-19 | 2002-05-22 | 中国科学院福建物质结构研究所 | Comprehensive utilization of waste from aluminium smeltery |
CN101070176A (en) * | 2007-06-07 | 2007-11-14 | 童益 | Method for producing aluminium sulfate using aluminium hydroxide mud |
CN101254934A (en) * | 2007-02-26 | 2008-09-03 | 苏宗裕 | Method for manufacturing aluminum sulfate |
CN101746802A (en) * | 2010-01-24 | 2010-06-23 | 徐州浩通新材料科技股份有限公司 | Method for manufacturing aluminum sulfate |
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CN1350065A (en) * | 2000-10-19 | 2002-05-22 | 中国科学院福建物质结构研究所 | Comprehensive utilization of waste from aluminium smeltery |
CN101254934A (en) * | 2007-02-26 | 2008-09-03 | 苏宗裕 | Method for manufacturing aluminum sulfate |
CN101070176A (en) * | 2007-06-07 | 2007-11-14 | 童益 | Method for producing aluminium sulfate using aluminium hydroxide mud |
CN101746802A (en) * | 2010-01-24 | 2010-06-23 | 徐州浩通新材料科技股份有限公司 | Method for manufacturing aluminum sulfate |
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