200808661 九、發明說明： 【發明所屬之技#r領域】 • 本發明係有關於處理高濁度水，且特別有關於生物性 ‘凝聚劑及處理高濁度水之方法。 【先前技彳标】 . < 傳統上淨水場處理流程多為混凝:、沉降處理每序，其 餐 中混滅 >儿降單元之设計標準’係以原水濁度兩千度以内， 可以出水百分之百，若濁度達五千度，則需加強藥劑、，出 水量只有八成五左右；濁度達五千至一萬度，則出水量下降 至八成，而一萬度左右，只能出水五成，一萬五以上則只 有一成，且當出水量只有七成五至八成五時，便需分區:供 水，即對民生或工業產生相當大的影響。 目前淨水處理常用的化學凝聚劑包括硫搜.銘 (Al2(S〇4)3)、氯化鐵(FeCl3)、聚氯化銘（PAC1)、聚丙烯醯 馨胺（polyacrylamide, PAM)、聚氯化己二烯二曱基腺 .- . . 一 .· (poly(diallyldimethyl ammonium chloride)5 poly (DADMAC) :及氯曱基一氧三—環二甲基胺聚合物Epi-DMA polyamines(epichlorohydrill dimethylamine polymer)，例 如，以PAC1處理時，先加入液鹼提升pH約至8〜9之間:， 再加入PAC1進行混凝動作，使混凝時控制於pH中牲混凝 範圍，其成本較高且處理後水質導電度及總解解性固形物 (tds)值較高，並因ΡΑα(ια%)混凝劑本身電荷密度為 1，375,000 meq/g，.易因高濁度水懸浮固體物多，加.藥量的 .' ‘ · · . , .〆 ' ' · . ' ' . ’ 、0296-A21698TWF(N2);358;kai , -200808661 IX. INSTRUCTIONS: [Technical Fields of the Invention] The present invention relates to the treatment of high turbidity water, and more particularly to biological 'coagulating agents and methods for treating high turbidity water. [Previous technical standards] . < Traditionally, the clean water treatment process is mostly coagulation: and the settlement process is used for each sequence, and the design standard of the child drop unit is based on the original water turbidity of two thousand degrees. Within 100% of the water, if the turbidity reaches 5,000 kWh, it is necessary to strengthen the pharmacy. The amount of water is only about 85 percent. When the turbidity is 5,000 to 10,000 kWh, the amount of water is reduced to 80%, and about 10,000 degrees. Only 50% of the water can be discharged, and only 10% of the 15,000 or more, and when the water output is only 75% to 85%, the partition is required: water supply, which has a considerable impact on people's livelihood or industry. The current chemical coagulants commonly used in water purification include sulfur search. (Al2(S〇4)3), ferric chloride (FeCl3), polychlorinated (PAC1), polyacrylamide (PAM), Poly(diallyldimethyl ammonium chloride) 5 poly (DADMAC): and chloromercapto-oxo-trimethylamine polymer Epi-DMA polyamines (poly(diallyldimethyl ammonium chloride)) Epichlorohydrill dimethylamine polymer), for example, when treated with PAC1, first add liquid alkali to raise the pH to about 8~9:, then add PAC1 for coagulation, so that the coagulation is controlled in the pH range of coagulation, the cost Higher and higher water conductivity and total decomposed solids (tds) after treatment, and because ΡΑα(ια%) coagulant itself has a charge density of 1,375,000 meq/g, which is easy to be due to high turbidity water. Suspended solids, plus the amount of drug. ' ' · · , .〆 ' ' · . ' ' . ' , 0296-A21698TWF (N2); 358; kai, -
- L 200808661 增加，至使不易達到電 & π τ性，產生水質反濁現象，當濁度 大於2000NTU時，盔法去 豕田满反 、有致率的混凝及快速沉降，造成缺 水問題。此外，在以ΡΑρι 士 · θ + ^ 1處理時’谷易造成處理德水含 殘鋁致癌性的問題。 .人处埋俊冬3 【發明内容】 本發明的目的為提供一 ^ tL· ^ LA k夕古本你考柿i，種生物性婕名劑及處理高濁度 水之方法’使處理後水濁度降至5NTU以下、絲量在 O.hng/L以下，且不會發生上清液反濁的現象。 為達成上述目的：，本發明提供一種生物性劑，並 適用於處理高濁度水，其中該生物+ 丫巧生物性攱聚劑的導電度介於 2.13mS/cm與16.171^化111之間，且带；^_由入 rt/ Ί且包何密度介於12〇meq/g 與 3055meq/g。 \ ^ ^ ^ ^ ^ H 5 為達成上述目的，本發明另接供— 攸仏~種處理高濁唐太之 方法，包括加入一生物性凝聚劑至言 门/蜀I水之 . 呵/司度水中，且姆搞一 混凝及一沉降步驟.，其中該生物性 .. 2. i 3泰與i 6_ i 7mS/cm之間，且j :劑的導電度介於 與3055meq/g。更包括在該沉降步^您度介於12011^ ^ 1庚力σ入化學凝聚密》1， 且再經過一混凝及一、沉降步驟。·、子疋來d 為了讓本發明之上述和其他目的、 胡顯易懂，下文特舉較佳實施例，f特徵v和優點能更 細說明如r .配合所附圖示，作詳 - v · ， . 【實施方式】 -. - . . 本發明主要係利用導電声人' 电度介於2.13mS/cm 0296-A21698TWF(N2)；358；kai 200808661 16.17mS/cm之間，且電荷密度介於120meq/g與3055meq/g 之間的生物性凝聚劑來處理高濁度水。在本發明中，所甩 之生物性凝聚劑可為幾丁聚醣水溶液或以其為組成之複合 • 配方溶液。 • 本發明中，處理高濁度水的方法可為單階段處理或雙 P身段處理，參照第1圖，單階段處理係將專電度介於 2.13mS/cm 與 16.17mS/cm 之間，電荷密度介於 i2〇meq/g 與3055meq/g之間，pH值介於1〜5.0及濃度介於〇·1〜5% 的生物性凝聚劑加入高獨度水中，此生物性凝聚劑的添加 置在5ppm至5000ppm之間’較佳在500ppm至3000ppm 之間，依序進行混凝（快混、慢混）及沉降等步驟。參照第2 圖，其中慢混步驟可使用多檟串聯之操作模式，以多個慢 混槽201及多個攪拌器203，來增加去除濁度之效果。在 -> * -一較佳實施例中，生物性凝聚劑的'導電度約為2.37 . . · * · mS/cm，電荷密度約為1015.6 meq/g，pH·值約為4，濃度 ⑩約為1 %。其中混旋步驟包括快混及慢混，快混的轉速杳 180至200rpm之間，時間在20秒至60秒之間，速度坡降 (G)在200 s 1至400 s 1之間，慢混的轉速在至75rpm之 間，時間在3分至30分之間，速度坡降(G)在2〇 s-i至75 s_1 之間，Gt值在2x104-2x105。沉降的時間在}至12〇分鐘， 較佳在'10分鐘。本發明生物丨生凝聚劑:對導電度的影響很 低’處理後所獲得之膠沉水無銘殘留、濁度去除率在9〇% 以上「且不會有、劑量過多（overdose)產生反濁問題.。 芩照篇.3圖，雙階段處理包括第一階段的預處理及第 0296-A21698TWF(N2);358;kai 200808661 '二階段的化混處理，在第一階段，加入本發明之生物性凝 聚劑至高濁度水中，經過第一混凝及第一沉降步驟後，濁 度一般可由27072NTU降至2000NTU。生物性凝聚劑的添 ‘ 加量在lOppm至200ppm，較佳30ppm至40ppm之間。第 • 一混凝步驟包括快混及慢混9其中快混的轉速在18〇至 200rpm之間，時間在20秒至60秒之間，速度坡降(G)在 200 s·1至400 S·1之間，慢混的轉速在55至75rpm之間， 時間在3/分至30分之間，速度坡降(G)在40 s-1至70 S·1之 間，Gt值在104-105。沉降的時間可從1至12〇分鐘，較佳 10分鐘左右。其中慢混步驟包括多槽串聯之操作模式，如 第2圖所示。 ' * ， . 接著，於第二階段中加入化學凝聚劑，再進·行第二鹿 -凝及第二沉降，以將濁度由2000NTU降至5NTU.以下。化’ 學凝聚劑可為Al2(S〇4)3、FeCl3、聚两烯醯胺、聚氯化己二 烯二曱基胺、氯曱基一氧三環二甲基胺聚合物或聚氯化 φ 銘’其中又以聚氯化銘較佳。一般而言，化學凝聚劑的添 加量在lOppm至350ppm之間，較佳在lOOppm至200ppm 、之間。弟二混凝亦可包括快混及慢混二階段，其中快混的. 參數可與第一階段相同，慢混的轉速在55至75rpm之間， , 、 - · - · - 時間在3分至30分之間，速度坡降(G)在20 s-1至75 s:1之 間」Gt值在2χ104-2χ105。·第二沉降的參數可與第一階段的 _ >儿降相同。 '纟 1雙階段處理後，含銘量測試可低於〇1 mg/L，、表未 雙階段處理可有效降低聚氣化銘的添加劑量，故大幅縮減 0296-A21698TWF(N2)；358；kai 200808661 殘銘的生成可能。 【實施例】 * 實施例1 :單階段處理方式 將1%，ρΗ4,導電度2.37 ms/cm，電荷密度上㈣啊^ 之幾丁聚醣凝聚劑溶液加至.1000 ml的高濁度水中，原水 濁度為27072 NTU ’原水混凝機為Jar Test式，其+各參 • 數如表一所示。在添加幾丁聚·凝聚劑後經過19〇 rpK 30秒的快混，65 rpm，558秒的慢混，及_秒的沉降以 去除原水中的懸浮粒子。此外，以添加聚氯化銘的高濁度 水作為對照組。由第4圖可知，嘰丁聚醣凝聚劑沉降速度 較聚氯化紹快約5-10.倍，由第5a_5d圖可知，幾丁聚釀凝 聚劑不會影響原水的pH值及導電度，且濁度去除率可達 9〇%以上，但聚氯化㈣導致原水導電度增加(較本發明凝 聚：劑高5-H)倍）、PH下降’耗驗度較高，且會發生上清液 φ反濁的現象。參照表二’聚氯化叙劑量在6〇 〇 ppm時，立 濁度可降至6NTU，幾丁聚醣凝聚劑量在15〇〇ppm時，^ 度'可降至5 NTU。… ：… 、- L 200808661 increase, so that it is not easy to reach electric & π τ, resulting in anti-turbidity of water quality, when the turbidity is greater than 2000 NTU, the helmet method to go to the field full of reverse, the rate of coagulation and rapid settlement, resulting in water shortage . In addition, when treated with ΡΑρι士 · θ + ^ 1 , the glutinous rice has a problem of treating the carcinogenicity of the residual aluminum with residual aluminum. [Inventive] The object of the present invention is to provide a method for treating water after treatment, such as a bio-anonymous agent and a method for treating high turbidity water. The turbidity is reduced to below 5 NTU, the amount of silk is below O.hng/L, and the supernatant is not turbid. To achieve the above object, the present invention provides a biological agent suitable for treating high turbidity water, wherein the conductivity of the biological + smart biological polymerization agent is between 2.13 mS/cm and 16.171 ^111 And with; ^_ from rt / Ί and the density of the package is between 12〇meq/g and 3055meq/g. \ ^ ^ ^ ^ ^ H 5 In order to achieve the above purpose, the present invention further provides a method for treating high turbidity Tangtai, including adding a biological coagulant to the door/蜀I water. And a coagulation and a settling step, wherein the biologicality: 2. i 3 Thai and i 6_ i 7mS / cm, and j: the conductivity of the agent is between 3055 meq / g. It is also included in the sedimentation step ^ you degree is between 12011 ^ ^ 1 Geng force σ into the chemical condensation dense 1 , and then through a coagulation and a settling step. In order to make the above and other objects of the present invention easy to understand, the following preferred embodiments, f features v and advantages can be described in more detail, such as r. [Embodiment] -. - . . The present invention mainly utilizes a conductive sounder's electric power between 2.13mS/cm 0296-A21698TWF(N2); 358; kai 200808661 16.17mS/cm, and the charge density is High turbidity water is treated with a biocoagulant between 120 meq/g and 3055 meq/g. In the present invention, the biological coagulant may be an aqueous solution of chitosan or a composite solution of the composition. • In the present invention, the method for treating high turbidity water may be a single-stage treatment or a double-P body treatment. Referring to Figure 1, the single-stage treatment system has a specific electric power between 2.13 mS/cm and 16.17 mS/cm. a biocoagulant with a density between i2〇meq/g and 3055meq/g, a pH between 1 and 5.0 and a concentration of between 1 and 5%, added to high-independence water, the addition of this biocoagulant It is placed between 5 ppm and 5000 ppm, preferably between 500 ppm and 3000 ppm, and the steps of coagulation (fast mixing, slow mixing) and sedimentation are sequentially performed. Referring to Fig. 2, wherein the slow mixing step can use a multi-turn series operation mode, the plurality of slow mixing tanks 201 and the plurality of agitators 203 are used to increase the effect of removing turbidity. In a preferred embodiment, the biocoagulant has a 'electric conductivity of about 2.37. · · · mS/cm, a charge density of about 1015.6 meq/g, a pH of about 4, and a concentration. 10 is about 1%. The mixing step includes fast mixing and slow mixing, the speed of the fast mixing is between 180 and 200 rpm, the time is between 20 seconds and 60 seconds, and the speed gradient (G) is between 200 s 1 and 400 s 1 , which is slow. The mixing speed is between 75 rpm and the time is between 3 and 30 minutes, the speed gradient (G) is between 2 〇si and 75 s_1, and the Gt value is between 2x104 and 2x105. The settling time is from { to 12 minutes, preferably at '10 minutes. The bio-coagulation coagulant of the invention has the effect of low conductivity. The residue of the glue obtained after the treatment has no residual residue and the turbidity removal rate is above 9〇%. “There is no over-dose and anti-turbidity. Problem: The three-stage process includes the first stage of pretreatment and the 0296-A21698TWF (N2); 358; kai 200808661 'two-stage chemical mixing process. In the first stage, the invention is added. The biological coagulant to high turbidity water, after the first coagulation and the first sedimentation step, the turbidity can generally be reduced from 27072 NTU to 2000 NTU. The addition amount of the biological coagulant is from 10 ppm to 200 ppm, preferably from 30 ppm to 40 ppm. The first coagulation step includes fast mixing and slow mixing. The speed of the fast mixing is between 18 〇 and 200 rpm, the time is between 20 seconds and 60 seconds, and the speed gradient (G) is between 200 s·1. Between 400 S·1, the speed of slow mixing is between 55 and 75 rpm, the time is between 3/min and 30 minutes, and the speed gradient (G) is between 40 s-1 and 70 S·1, Gt value At 104-105, the settling time can be from 1 to 12 minutes, preferably about 10 minutes. The slow mixing step includes a multi-tank series operation mode. As shown in Figure 2. '*, . Next, add the chemical coagulant in the second stage, and then proceed to the second deer-coagulation and the second sedimentation to reduce the turbidity from 2000 NTU to 5 NTU. ' The learning coagulant can be Al2(S〇4)3, FeCl3, polydiene decylamine, polychlorinated hexadienyldiamine, chlorodecyloxytrimethylamine polymer or polychlorinated φ 铭 ' is also preferred by polychlorination. In general, the amount of chemical coagulant added is between 10 ppm and 350 ppm, preferably between 100 ppm and 200 ppm. The second coagulation can also include fast mixing. Slow mixing two stages, in which the fast mixing. The parameters can be the same as the first stage, the slow mixing speed is between 55 and 75 rpm, , - - - - - - the time is between 3 and 30 minutes, the speed ramp ( G) Between 20 s-1 and 75 s:1" Gt values are between 2χ104-2χ105. • The parameters of the second settling can be the same as the _ > drop of the first stage. After the two-stage treatment of 纟1, the test containing the amount can be less than 〇1 mg/L, and the two-stage treatment can effectively reduce the amount of additive in the gasification, so it is greatly reduced by 0296-A21698TWF(N2);358; Kai 200808661 The generation of the remnant may be. [Examples] * Example 1: Single-stage treatment method: 1%, ρΗ4, conductivity 2.37 ms/cm, and a charge density (four) s of chitosan coagulant solution was added to .1000 ml of high turbidity water. The raw water turbidity is 27072 NTU 'The raw water coagulation machine is Jar Test type, and its + parameters are shown in Table 1. After adding a chitosan coagulant, a 19 rpm RPK 30 sec. fast mixing, 65 rpm, 558 sec slow mixing, and _ second settling were performed to remove suspended particles in the raw water. In addition, high turbidity water of polychlorinated rice was added as a control group. It can be seen from Fig. 4 that the sedimentation rate of the ketobutyl coagulant is about 5-10 times faster than that of polychlorinated chlorin. It can be seen from the 5a-5d chart that the chitosan coagulant does not affect the pH and conductivity of the raw water. And the turbidity removal rate can reach more than 9〇%, but the polychlorination (4) leads to an increase in the conductivity of the raw water (5-H times higher than the agglomeration of the present invention), and the pH decreases, and the consumption degree is high, and it occurs. The phenomenon of anti-turbidity of clear liquid φ. Referring to Table 2, when the polychlorinated dose is 6 〇 〇 ppm, the turbidity can be reduced to 6 NTU, and the chitosan condensing dose can be reduced to 5 NTU at 15 〇〇 ppm. ... :... ,
0296-A21698TWF(N2)；358；kai 200808661 角速度 19.89 rad/s 6.28 rad/s 速度 0.44745 m/s … 0.1413 m/s 輪入功率 0.0919 kg/m2/s2 0.0029 kg/m2/s2 速度坡降 303 s'1 60s'1 1 Gt 9000 33850 表二、比較聚氯化鋁與幾丁聚醣處理後之水質0296-A21698TWF(N2);358;kai 200808661 Angular velocity 19.89 rad/s 6.28 rad/s Speed 0.44745 m/s ... 0.1413 m/s Wheeling power 0.0919 kg/m2/s2 0.0029 kg/m2/s2 Speed ramp 303 s '1 60s'1 1 Gt 9000 33850 Table 2, comparing the water quality of polyaluminium chloride and chitosan
原水 聚氯化鋁（600 幾丁聚醣（1500 ' - Ppm) ppm) pH值 7.23 6.77 7:14 混凝劑量 0 600 1500 (PPm) 殘留濁度 27072 6 5 (NTU) 界達電位 -19.3 0.4 0.191 (mV) 導電度 0.188 0.293 0.191 (mS/cm) 殘留驗度 .84,5- 73.9 80.6 (mg/L) 殘鋁（mg/L) ND 0.12 ND 實施例2:雙階段處理方式. ： 首先，.第一階段將1%，pH4，導電度2.37 ms/cm，電^ 0296-A21698TWF(N2)；358；kai πRaw water polyaluminium chloride (600 chitosan (1500 ' - Ppm) ppm) pH 7.23 6.77 7:14 Coagulant dose 0 600 1500 (PPm) Residual turbidity 27072 6 5 (NTU) Bound potential -19.3 0.4 0.191 (mV) Conductivity 0.188 0.293 0.191 (mS/cm) Residual test. 84,5-73.9 80.6 (mg/L) Residual aluminum (mg/L) ND 0.12 ND Example 2: Two-stage treatment. : First , the first stage will be 1%, pH4, conductivity 2.37 ms / cm, electricity ^ 0296-A21698TWF (N2); 358; kai π
' 1 I 200808661 荷密度l，〇16 meq/g之幾丁聚醣凝聚劑溶液加至1000 ml的 高濁度水中，原水濁度為27Q72 NTU，幾丁聚醣的添加量 為 35 ppm，經過 190 rpm，30 秒的快混，65 rpm，558 秒 的慢混，及600秒的沉降後，加入50 ppm至200 ppm之聚 氯化銘’再經過19〇 rpm，3〇秒的快混，65 jrpm，558秒白勺 慢混，及600秒的沉降以去除懸浮粒子。此外，以二階段 皆添加聚氯化鋁作為對照組，對照組之第一階段加入5 ppm之聚氣化链’弟二階段加入加入5〇 ppm至200 ppm之 聚氯化鋁。油第6、7圖可知，對照組會產生上清液反濁的 現象，而添加本發明之幾丁聚醣凝聚劑則無反濁‘現象，且 由表三、四可知，對照組最後的原水殘留濁度在10〜20 NTU，而本發明的殘留濁度則可降至5 NTU以下。. 表三、以幾丁聚醣+ !氯化鋁處多後之永質 窠一階段 - · - _ . · 、 · 幾丁聚 醣的添 加 量 (ppm) 濁度 (NTU) 界達電位 (mV) pH值 導電度 (yS/cm) 殘留鹼度 (mg/L)： 紹含量 35 1，914 -9.2 807 87.5. ND - 第二階段 、 ' / 聚氯化 在呂的添 加 量 濁度 (NTU) 界達電位 (mV) pH值 導電、度 (/xS/crn) 殘留鹼度 (mg/L) 鋁含量 0296-A21698TWF(N2)；358；kai 12 200808661' 1 I 200808661 The density of l, 〇16 meq / g of chitosan coagulant solution was added to 1000 ml of high turbidity water, the raw water turbidity was 27Q72 NTU, the addition of chitosan was 35 ppm, after 190 rpm, 30 seconds of fast mixing, 65 rpm, 558 seconds of slow mixing, and 600 seconds of settling, adding 50 ppm to 200 ppm of polychlorinated 'after another 19 rpm, 3 sec. 65 jrpm, 558 seconds of slow mixing, and 600 seconds of settling to remove suspended particles. In addition, polyaluminum chloride was added as a control group in two stages, and a 5 ppm polygasification chain was added in the first stage of the control group, and 5 〇 ppm to 200 ppm of polyaluminum chloride was added in the second stage. Oil figures 6 and 7 show that the control group will produce the phenomenon of anti-turbidity of the supernatant, while the addition of the chitosan agglutinating agent of the present invention has no anti-turbidity phenomenon, and it can be seen from Tables 3 and 4, and the last of the control group. The residual water turbidity is 10-20 NTU, and the residual turbidity of the present invention can be reduced to below 5 NTU. Table 3. The stage of permanent bismuth after the addition of chitosan + ! aluminum chloride - · - _ . · · · The amount of chitosan added (ppm) turbidity (NTU) mV) pH conductivity (yS/cm) Residual alkalinity (mg/L): The content of 35,914 -9.2 807 87.5. ND - The second stage, ' / polychlorination in Lu added turbidity ( NTU) Boundary potential (mV) pH conductivity, degree (/xS/crn) residual alkalinity (mg/L) aluminum content 0296-A21698TWF(N2);358;kai 12 200808661
(ppm) - 一 50 8.63 0.6 7.37 822 74 ND 75 5.57 0.8 7.19 833 71.8 ND 100 3.36 0.8 7.1 846 69.6 ND 125 3.05 0.9 6.96 852 64.8 ND 150 2.83 ,0 6.89 866 56.6 ND 200 4.25/ 1.2 6.78 888 55.9 ND(ppm) - a 50 8.63 0.6 7.37 822 74 ND 75 5.57 0.8 7.19 833 71.8 ND 100 3.36 0.8 7.1 846 69.6 ND 125 3.05 0.9 6.96 852 64.8 ND 150 2.83 ,0 6.89 866 56.6 ND 200 4.25/ 1.2 6.78 888 55.9 ND
表四、皆以聚氯化銘處理後之水質 第一階段 ，： 聚氯化 銘的添 '加 量 (PPm) 濁度 (NTU) 界達電位 (mV) pH值 導電度 (jicS/cm) 殘留鹼度 (mg/L) 銘含量 5 2,508 -10.6 7.68 816 88.0 ND 第二階段 …’ .：^ ^ ^ \ 入 聚氯化 銘.的添 加、量/ (ppm) 濁度 (NTU) j達電位 (mV) pH值 .導電度 (ptS/cm) 殘留鹼度 (mg/L) 鋁含量 50 8.63 0.6 7.40 832 76,4 ND 75 10.52 0.7 7.23 . 842 ' 74.5 ND 100 12.72 . 0.8 7.09 855 68.8 ND 125 14.06 0.8 7.00 863 64.2 ND \ 0296-Α2Ί 698TWF(N2)；358；kai 200808661 150 19 0.8 6.88 876 60.9 ND ^ 200 22.6 0.9 6.75 888 53.0 •ND ' 雖然本發明已以較佳實施例揭露如土，然其並非用以. 限定本發明，任何熟習此技藝者，在不脫離本發明之精神 和範圍内，當可作些許之更動與潤飾，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。/Table 4, the first stage of water quality after treatment with polychlorination: Adding amount of polychlorinated (PPm) turbidity (NTU) boundary potential (mV) pH conductivity (jicS/cm) Residual alkalinity (mg/L) Ming content 5 2,508 -10.6 7.68 816 88.0 ND Second stage...' .:^ ^ ^ \ Addition of polychlorination. Addition, quantity / (ppm) Turbidity (NTU) j Potential (mV) pH value. Conductivity (ptS/cm) Residual alkalinity (mg/L) Aluminum content 50 8.63 0.6 7.40 832 76,4 ND 75 10.52 0.7 7.23 . 842 ' 74.5 ND 100 12.72 . 0.8 7.09 855 68.8 ND 126 。 。 。 。 。 However, it is not intended to limit the invention, and any person skilled in the art can make some modifications and refinements without departing from the spirit and scope of the invention, and therefore the scope of protection of the present invention is as follows. The scope defined by the patent scope shall prevail. /
0296-A21698TWF(N2)；358；kai .， ]4 200808661 【圖式簡單說明】 第1圖顯示本發明之單階段處理方式。 .第2圖顯示本發明之多槽慢混處理單元。 第3圖顯示本發明之雙.階段處理方式。、 第4圖顯示比較本發明凝聚劑與聚氯化鋁的沉降速 度。 、 第5a-5d圖顯示比較本發明凝聚劑與聚氣化銘的濁 馨 度、去除率、pH值及導電度。： ： 第6圖顯示雙藥劑雙階段處理方式的殘留濁度。： 第7圖顯示、單藥劑雙階段處理方式的殘留濁度。 【主要元件符號說明】 201〜慢混槽； 2〇3〜攪拌器。’ 0296-A21698TWF(N2)；358；kai0296-A21698TWF(N2);358;kai ., ]4 200808661 [Simplified Schematic] FIG. 1 shows a single-stage processing method of the present invention. Figure 2 shows the multi-slot slow mixing processing unit of the present invention. Figure 3 shows the dual stage processing of the present invention. Fig. 4 shows a comparison of the sedimentation speed of the coagulant of the present invention and polyaluminum chloride. Fig. 5a-5d shows the comparison of the cloudiness, removal rate, pH value and conductivity of the coagulant and polygasification of the present invention. : : Figure 6 shows the residual turbidity of the two-agent two-stage treatment. : Figure 7 shows the residual turbidity of the single-agent two-stage treatment. [Main component symbol description] 201~ slow mixing tank; 2〇3~ stirrer. ’ 0296-A21698TWF(N2);358;kai