TW202308948A - Method for treating fluorine-containing water - Google Patents
Method for treating fluorine-containing water Download PDFInfo
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- TW202308948A TW202308948A TW111124801A TW111124801A TW202308948A TW 202308948 A TW202308948 A TW 202308948A TW 111124801 A TW111124801 A TW 111124801A TW 111124801 A TW111124801 A TW 111124801A TW 202308948 A TW202308948 A TW 202308948A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
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Abstract
Description
本發明是有關於一種用於自含氟水中除去氟的含氟水的處理方法。The present invention relates to a method for treating fluorine-containing water for removing fluorine from fluorine-containing water.
作為自含氟水中除去氟的方法,施行了如下方法:在反應槽中向含氟水添加消石灰、氯化鈣等鈣化合物而調整成pH值6~10,使包含氟化鈣的析出物析出,在凝集槽中添加高分子凝集劑進行凝集反應,並在沈澱槽中進行沈澱分離。As a method for removing fluorine from fluorine-containing water, a method of adding calcium compounds such as hydrated lime and calcium chloride to fluorine-containing water in a reaction tank to adjust the pH to 6 to 10, and to precipitate precipitates including calcium fluoride , adding a polymer coagulant in the coagulation tank for coagulation reaction, and carrying out precipitation and separation in the precipitation tank.
但是,在此種處理方法中,由於生成的絮凝物是包含大量水的凝膠狀的氫氧化物,因此沈降性差。另外,所生成的污泥的脫水性差,其處理不容易。另外,無法充分降低處理水的氟濃度。However, in this treatment method, since the generated flocs are gel-like hydroxides containing a large amount of water, the settleability is poor. In addition, the generated sludge has poor dehydration properties, and its treatment is not easy. In addition, the fluorine concentration of the treated water cannot be sufficiently reduced.
作為改善所述方面的方法,在專利文獻1中記載了如下的氟除去方法:使用使含氟水與鈣化合物反應的反應槽、向該反應槽導入含氟水的原水通路、自反應槽移送反應液並添加高分子凝集劑來進行凝集的凝集裝置、以及導入在凝集裝置中形成的包含絮凝物的混合液來進行固液分離的固液分離槽,將在固液分離槽中分離出的污泥的一部分導入改質槽,並添加鈣化合物後使其循環至反應槽。As a method for improving the above-mentioned aspects,
專利文獻2、專利文獻3中亦記載了同樣的含氟水的處理方法。
[現有技術文獻]
[專利文獻]
[專利文獻1]日本專利特開平10-479號公報 [專利文獻2]日本專利特開2007-190517號公報 [專利文獻3]日本專利特開2009-233568號公報 [Patent Document 1] Japanese Patent Laid-Open No. 10-479 [Patent Document 2] Japanese Patent Laid-Open No. 2007-190517 [Patent Document 3] Japanese Patent Laid-Open No. 2009-233568
[發明所欲解決之課題] 關於鈣化合物向所述污泥改質槽的添加量,對原水的流量及氟濃度進行測定,基於其結果進行控制。 [Problem to be Solved by the Invention] The amount of the calcium compound to be added to the sludge reforming tank was measured by measuring the flow rate and the fluorine concentration of the raw water, and controlling based on the results.
然而,在鈣化合物如消石灰(氫氧化鈣)、碳酸鈣等般為難溶性的情況下,鈣化合物水溶液的濃度無法達到設定值,鈣化合物的添加量有時偏離目標值。However, when the calcium compound is poorly soluble such as slaked lime (calcium hydroxide), calcium carbonate, etc., the concentration of the calcium compound aqueous solution cannot reach the set value, and the added amount of the calcium compound may deviate from the target value.
在鈣化合物向污泥改質槽的添加不足的情況下,氟自含氟水的除去變得不充分。相反,在鈣化合物的添加過剩的情況下,不僅藥品成本高,而且在對處理水進行再利用的情況下,需要用於降低處理水中的鈣濃度的處理。When the addition of the calcium compound to the sludge reforming tank is insufficient, the removal of fluorine from the fluorine-containing water becomes insufficient. Conversely, when the calcium compound is added excessively, not only the chemical cost is high, but also when the treated water is reused, treatment for reducing the calcium concentration in the treated water is required.
本發明的課題在於提供一種含氟水的處理方法,其將在固液分離槽中分離出的污泥的一部分導入至污泥改質槽,並在添加鈣化合物後使其循環至反應槽,且所述含氟水的處理方法中,可以鈣化合物向污泥改質槽的添加量成為適當量的方式進行控制。 [解決課題之手段] The object of the present invention is to provide a method for treating fluorine-containing water, which introduces a part of the sludge separated in the solid-liquid separation tank to the sludge reforming tank, and circulates it to the reaction tank after adding a calcium compound, In addition, in the treatment method of the above-mentioned fluorine-containing water, the addition amount of the calcium compound to the sludge reforming tank can be controlled so that it becomes an appropriate amount. [Means to solve the problem]
本發明的含氟水的處理方法使用了含氟水的處理裝置,所述含氟水的處理裝置包括:反應槽,使包含含氟水的原水與鈣化合物反應而生成反應液;原水通路,向所述反應槽導入原水;凝集裝置,自反應槽移送反應液,並添加高分子凝集劑進行凝集;固液分離槽,導入在凝集裝置中形成的包含絮凝物的混合液並進行固液分離;以及循環通路,將在固液分離槽中分離出的污泥的一部分導入至污泥改質槽,並藉由鈣化合物添加部件添加鈣化合物,使其循環至反應槽,且所述含氟水的處理方法的特徵在於,基於原水的氟濃度及原水流量、以及所述反應液中的鈣濃度來控制鈣化合物向所述污泥改質槽的添加量。The treatment method of fluorine-containing water of the present invention uses a treatment device for fluorine-containing water, and the treatment device for said fluorine-containing water includes: a reaction tank, which reacts raw water containing fluorine-containing water and a calcium compound to generate a reaction liquid; a raw water passage, Introduce raw water into the reaction tank; coagulation device, transfer the reaction liquid from the reaction tank, and add a polymer coagulant for coagulation; solid-liquid separation tank, introduce the mixed liquid containing flocs formed in the coagulation device and perform solid-liquid separation and a circulation path for introducing a part of the sludge separated in the solid-liquid separation tank to the sludge reforming tank, and adding a calcium compound through the calcium compound adding part to circulate it to the reaction tank, and the fluorine-containing The water treatment method is characterized in that the addition amount of the calcium compound to the sludge reforming tank is controlled based on the fluorine concentration of raw water, the flow rate of raw water, and the calcium concentration in the reaction liquid.
在本發明的一形態中,作為所述反應槽,設有:第一反應槽,於其中導入原水及來自所述污泥改質槽的污泥;以及第二反應槽,於其中導入所述第一反應槽的流出液且添加pH值調整劑,且所述形態中,基於原水的氟濃度及原水流量、以及所述第二反應槽內或自所述第二反應槽流出的反應液中的鈣濃度,來控制鈣化合物向所述污泥改質槽的添加量。In one aspect of the present invention, as the reaction tank, there are provided: a first reaction tank into which raw water and sludge from the sludge reforming tank are introduced; and a second reaction tank into which the The effluent of the first reaction tank is added with a pH adjuster, and in the form, based on the fluorine concentration of the raw water and the flow rate of the raw water, and the reaction liquid in or out of the second reaction tank Calcium concentration to control the amount of calcium compound added to the sludge reforming tank.
在本發明的一形態中,以與向所述第一反應槽的氟導入量為當量的方式決定基準添加量,並基於所述第二反應槽內或自所述第二反應槽流出的反應液中的檢測鈣濃度來修正所述基準添加量。In one aspect of the present invention, the standard addition amount is determined so as to be equivalent to the amount of fluorine introduced into the first reaction tank, and is based on the reaction in the second reaction tank or outflow from the second reaction tank. The detected calcium concentration in the solution is used to correct the base addition amount.
在本發明的一形態中,關於所述修正,當所述反應液中的鈣濃度低於預先設定的鈣濃度目標值時,根據鈣濃度目標值與檢測鈣濃度之差,增加鈣化合物的添加量,當所述反應液中的檢測鈣濃度高於預先設定的鈣濃度目標值時,根據檢測鈣濃度與鈣濃度目標值之差,減少鈣化合物的添加量。In one aspect of the present invention, regarding the correction, when the calcium concentration in the reaction solution is lower than a preset calcium concentration target value, the addition of the calcium compound is increased according to the difference between the calcium concentration target value and the detected calcium concentration. When the detected calcium concentration in the reaction solution is higher than the preset calcium concentration target value, the added amount of the calcium compound is reduced according to the difference between the detected calcium concentration and the calcium concentration target value.
在本發明的一形態中,添加氫氧化鈣漿液(slurry)作為所述鈣化合物。 [發明的效果] In one aspect of the present invention, calcium hydroxide slurry (slurry) is added as the calcium compound. [Effect of the invention]
在本發明的含氟水的處理方法中,不僅基於原水中的氟濃度,亦基於反應液中的鈣濃度來控制鈣化合物向污泥改質槽的添加量,因此可適當地控制鈣化合物的添加量。藉此,處理水的水質亦提高。另外,由於處理水中的鈣濃度低,鈣水垢(scale)得到抑制,因此能夠在本處理的後段應用生物處理。In the method for treating fluorine-containing water of the present invention, the addition amount of the calcium compound to the sludge reforming tank is controlled based not only on the fluorine concentration in the raw water but also on the calcium concentration in the reaction solution, so the concentration of the calcium compound can be appropriately controlled. Add amount. Thereby, the water quality of the treated water is also improved. In addition, since calcium scale in the treated water is low and calcium scale is suppressed, biological treatment can be applied in the latter stage of this treatment.
以下,參照圖1對實施方式進行說明。Hereinafter, an embodiment will be described with reference to FIG. 1 .
圖1是表示用於進行本發明方法的含氟水的處理裝置的實施方式的系統圖,圖1中,1表示於其中經由原水配管1a而導入原水的第一反應槽,2表示第二反應槽,3表示凝集槽,4表示沈澱槽,5表示污泥改質槽。在原水配管1a設有原水流量計21、以及包括用於檢測原水的氟濃度的氟離子電極等的氟感測器16。Fig. 1 is a system diagram showing an embodiment of a fluorine-containing water treatment device for carrying out the method of the present invention. In Fig. 1, 1 represents a first reaction tank into which raw water is introduced via a
圖1中,原水與鈣化合物的反應在呈兩段串聯配置的第一反應槽1與第二反應槽2中進行。即,向第一反應槽1添加來自污泥改質槽5的改質污泥,同時視需要添加鈣化合物及pH值調整劑,在較佳為pH值4~10,更佳為pH值6~6.5下使原水中的氟幾乎不溶化。將第一反應槽1的流出液導入至第二反應槽2,視需要添加pH值調整劑,較佳為在pH值4~10,更佳為pH值6~6.5下使殘留的氟不溶化。再者,為了在第二反應槽2中進一步使氟不溶化,除了添加pH值調整劑以外,有時亦添加鈣化合物。In FIG. 1 , the reaction between raw water and calcium compounds is carried out in a
在所述第二反應槽2設有用於檢測鈣離子濃度的鈣離子感測器等鈣感測器9。再者,鈣感測器9除了設於第二反應槽2以外,亦可設於第二反應槽2與凝集槽3之間的配管2a、或者沈澱槽4的處理水通過後的配管4a。A
所述第二反應槽2的流出液被導入至凝集槽3,添加高分子凝集劑而進行凝集處理。作為所述高分子凝集劑,只要是用於懸濁排水的凝集處理者,則並無特別限制,例如使用聚丙烯醯胺系高分子凝集劑等。另外,為了提高凝集效果,亦能夠在添加聚氯化鋁(Poly aluminum chloride,PAC)或硫酸鋁等無機凝集劑後,添加高分子凝集劑。The effluent from the
凝集槽3的凝集處理水繼而經由配管3a而導入至沈澱槽4並經固液分離,分離水作為處理水排出至系統外。分離污泥的一部分作為回流污泥輸送至污泥改質槽5,殘留部分作為剩餘污泥排出至系統外。The coagulation-treated water in the
在污泥改質槽5中添加鈣化合物進行混合,藉此鈣化合物的至少一部分藉由吸附等附著在污泥的表面而對污泥進行改質。當將所述改質污泥導入至第一反應槽1時,污泥表面的鈣化合物與原水中的氟反應,污泥粒子成長。如此進行了晶粒生長的污泥由於沈降性良好,因此在沈澱槽4中效率良好地沈澱。By adding and mixing a calcium compound in the
鈣化合物以含鈣化合物的液體(例如,消石灰(氫氧化鈣)或碳酸鈣的水性漿液、氯化鈣水溶液)的形態添加至污泥改質槽5。含鈣化合物的液體較佳為消石灰漿液,其濃度為20 wt%以下,理想為10 wt%。氯化鈣水溶液以標準濃度(例如35 wt%)使用。The calcium compound is added to the
含鈣化合物的液體藉由泵等經由配管10、開閉閥11、配管12、控制閥13、配管14而添加至污泥改質槽5。The calcium compound-containing liquid is added to the
控制閥13構成為可連續地改變開度(即鈣化合物供給量),由控制器15控制開度。控制器15基於鈣感測器9、包括用於檢測原水的氟濃度的氟離子電極等的氟感測器16的檢測訊號、原水配管的原水流量計21的檢測訊號、以及設於配管12的流量計17的檢測訊號,來控制控制閥13的開度。The
關於鈣化合物的添加量,基本上以與向第一反應槽1的氟導入量(由原水的流量與原水的氟濃度的積求出)為當量的方式決定基準添加量,並基於鈣感測器9的檢測鈣濃度對所述基準添加量進行修正來決定。在所述修正的一例中,當鈣感測器9的檢測鈣濃度低於預先設定的鈣濃度目標值時,根據鈣濃度目標值與檢測鈣濃度之差,增加鈣化合物的添加量。相反,當鈣感測器9的檢測鈣濃度高於預先設定的鈣濃度目標值時,根據檢測鈣濃度與鈣濃度目標值之差,減少鈣化合物的添加量。The amount of calcium compound to be added is basically determined so that it is equivalent to the amount of fluorine introduced into the first reaction tank 1 (obtained from the product of the flow rate of raw water and the fluorine concentration of raw water). The calcium concentration detected by the
再者,在所述實施方式中,為了防止控制閥13的堵塞,能夠經由具有閥18的配管19對配管12供給洗淨水。藉由將閥11關閉,將閥18打開,向控制閥13通入洗淨水,利用該洗淨水將控制閥13洗淨,而防止堵塞。利用所述洗淨水的控制閥13的洗淨較佳為利用計時器而定期地進行,例如以5分鐘~24小時1次、特別是1小時1次左右的頻率、並且以1次的洗淨水的通水時間為1分鐘~10分鐘,特別是2分30秒左右來進行,但並不限定於此。作為洗淨水,可使用自來水、工業用水等。Furthermore, in the above-described embodiment, in order to prevent clogging of the
如此,在本實施方式中,由於利用鈣感測器9的檢測值對鈣化合物的添加量進行修正,因此即使鈣化合物溶液的鈣化合物濃度有變動,亦進行適當的鈣化合物添加控制。藉此,能夠獲得水質良好的處理水,例如可降低處理水中的氟濃度或鈣濃度。另外,藉此,容易對處理水進行再利用。Thus, in this embodiment, since the calcium compound addition amount is corrected using the detection value of the
在所述實施方式中,由於利用洗淨水將控制閥13洗淨,因此防止控制閥13堵塞,而能夠進行穩定的處理。In the above-described embodiment, since the
利用特定的形態對本揭示進行了詳細說明,但所屬技術領域具有通常知識者當知,在不脫離本揭示的意圖及範圍的情況下能夠進行各種變更。 本申請案是基於2021年8月23日提出申請的日本專利申請案2021-135698,藉由引用而援引其全文。 Although this indication was demonstrated in detail using the specific form, it is clear to those skilled in the art that various changes can be made without deviating from the intention and range of this indication. This application is based on Japanese Patent Application No. 2021-135698 filed on August 23, 2021, the entirety of which is incorporated by reference.
1:第一反應槽
1a:原水配管
2:第二反應槽
2a、3a、4a、10、12、14、19:配管
3:凝集槽
4:沈澱槽
5:污泥改質槽
9:鈣感測器
11:開閉閥
13:控制閥
15:控制器
16:氟感測器
17、21:流量計
18:閥
1: The
圖1是實施方式的含氟水的處理裝置的構成圖。FIG. 1 is a configuration diagram of a treatment apparatus for fluorine-containing water according to an embodiment.
1:第一反應槽 1: The first reaction tank
1a:原水配管 1a: Raw water piping
2:第二反應槽 2: The second reaction tank
2a、3a、4a、10、12、14、19:配管 2a, 3a, 4a, 10, 12, 14, 19: Piping
3:凝集槽 3: Agglutination tank
4:沈澱槽 4: Sedimentation tank
5:污泥改質槽 5: Sludge reforming tank
9:鈣感測器 9: Calcium sensor
11:開閉閥 11: On-off valve
13:控制閥 13: Control valve
15:控制器 15: Controller
16:氟感測器 16: Fluorine sensor
17、21:流量計 17, 21: flow meter
18:閥 18: valve
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