CN105174663A - 染料废水的处理方法 - Google Patents
染料废水的处理方法 Download PDFInfo
- Publication number
- CN105174663A CN105174663A CN201510728894.0A CN201510728894A CN105174663A CN 105174663 A CN105174663 A CN 105174663A CN 201510728894 A CN201510728894 A CN 201510728894A CN 105174663 A CN105174663 A CN 105174663A
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- China
- Prior art keywords
- waste water
- treatment
- water
- dyestuff
- anaerobic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- YPLPZEKZDGQOOQ-UHFFFAOYSA-M Iron oxychloride Chemical compound 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[O][Fe]Cl YPLPZEKZDGQOOQ-UHFFFAOYSA-M 0.000 claims 1
- 241000276438 Gadus morhua Species 0.000 abstract description 16
- 235000019516 cod Nutrition 0.000 abstract description 16
- 239000011780 sodium chloride Substances 0.000 abstract description 13
- 150000003839 salts Chemical class 0.000 abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- 230000005501 phase interface Effects 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 1
Abstract
本发明提供了一种染料废水的处理方法,将经过预先催化氧化的染料废水进行厌氧好氧处理;再将厌氧好氧处理后的废水进行活性炭吸附处理后排出。本发明针对染料废水含盐量高、COD浓度高的特点,前端通过预先催化氧化处理降低部分COD负荷,中间经生活污水稀释催化氧化处理后废水使COD降低,同时盐含量降低,使厌氧好氧生化过程得以进行,并经过活性炭吸附,完成污水的处理。本发明的方法简单、反应条件温、速度快、操作容易,预处理时采用的催化剂可以回收,循环使用;反应时不需要酸性条件不需要调节pH值,避免了大量酸的消耗;处理过程短,处理效率高。
Description
技术领域
[0001] 本发明属于废水处理技术领域,特别是涉及一种染料废水的处理方法。
背景技术
[0002] 由于染料废水具有高C0D、高色度、高含盐量,有机物难生化降解,水质和水量随时 间变化较大(废水间接性排放)等特点,染料废水成为工业废水治理领域的难点。从二十世 纪七十年代起,发达国家开始投入大量的资金进行环境治理,一方面改进生产工艺,实行源 头控制,尽量减少生产中的废水排放量,另一方面又探索各种方法对染料废水进行净化处 理。染料废水的处理包括各种方法,按照处理原理不同,可以将处理方法主要分为物理法、 化学法和生物法。在实际应用中,单一的处理手段往往无法使染料废水达标排放,一般是几 种方式联合处理。
[0003] 1、物理法处理染料废水
[0004] 用于染料废水处理的物理法通常包括萃取、吸附、离子交换、结晶、渗析、膜分离技 术、混凝等方法,主要去除大砂粒、固体物和纤维肩等。
[0005] 吸附法是应用具有较强吸附能力的吸附剂,使废水中的一种或者数种成分吸附于 固体表面,这种过程发生在固液两相界面上,是流体混合物中的一种或数种在相界面上浓 集的过程,包括物理吸附和化学吸附。在染料废水处理中,吸附法主要用在预处理(减少水 处理主体装置的负荷,回收有用物质)和深度处理(提高水处理质量,满足回用水水质的要 求),不同的吸附剂对染料吸附具有不同的选择性,活性炭吸附效果好,但费用较高。
[0006] 混凝法是染料废水经常采用的物化处理法之一。在染料工业废水中,常含有不同 数量的悬浮体和溶胶,大小在10 3~10 9m范围内,这些物质自动凝聚成大颗粒并从分散介 质中沉淀出来的速度很慢,对于这类废水的处理,一般要先进行悬浮体及溶胶的脱稳,投加 一定量的混凝剂,悬浮性或胶体状态的污染物形成絮凝物沉淀析出,从而达到去除污染物 质的目的。絮凝处理方法主要去除水体中的溶胶和悬浮体,同时也可以去除部分溶解性的 杂质,并且絮凝处理可以改善污泥的脱水性能。混凝法的关键在于混凝剂的选择,投加量 少,管理方便,并能取得最佳经济效果的混凝剂是最有生命力的。
[0007] 2、化学法处理染料废水
[0008] 化学法是通过氧化还原反应,将废水中的有机物分解为小分子有机物以及无机 物,通常包括臭氧氧化、加氯氧化、射线氧化、光氧化、湿式空气氧化、电解氧化、燃烧等方 法,主要用于调节pH值、脱色、降低COD、BOD等。
[0009] 化学氧化法所指的范围很广,是直接用氧化剂(包括高锰酸钾、臭氧、次氯酸、双 氧水、Fenton试剂等)进行氧化分解有机物的方法。它一般具有反应速度快,降解副产物 少,广谱性好等优点。氧化剂不同,其投资和运行费用差异较大,但总的来说费用较高。因 此,目前化学氧化法仅用于饮用水处理、特种工业用水处理、有毒工业废水处理和以回用为 目的的废水深度处理等有限的场合。
[0010] 电解法是一种传统的电化学技术,采用石墨、铁板、钛板等作极板,还可以加入 NaCl、NaSO4S以水中原有盐份作导电介质,对染料废水通电电解,阳极产生O2或Cl2,阴极 产生H2,新生态氧或NaClO的氧化作用及H2的还原作用破坏了染料分子结构而脱色。此类 方法尤其适合于预处理生化难降解的有机污染物。
[0011] 微电解法是将铸铁肩作为滤料,使染料废水浸没或通过,利用Fe和C与溶液的电 位差,产生电极效应。电极反应产物新生态H有较高的化学活性,能与染料废水中的多种组 分发生氧化还原反应,破坏染料的发色结构。微电池中阳极产生新生态Fe2+,其水解产物的 凝絮体具有较强的吸附能力。
[0012] 3、生物法处理染料废水
[0013] 生物处理技术是利用微生物将废水中的有机物分解除去,各种好氧和厌氧生物处 理技术在染料废水处理中得到了一定的应用。调查发现,印染废水中虽然不可生化有机物 含量较大,但是其中相当数量的无机还原物质可被氧化,不可降解物质通过物理或生物吸 附聚于活性污泥或生物膜上即得到去除。
[0014] 好氧法处理是生物处理主要的方法,在有氧的情况下,废水中的有机物通过活性 污泥吸附、氧化、还原、合成过程,把有机物氧化成为简单无机物,好氧法处理的效率高,速 度快,比较经济。
[0015] 废水的厌氧生物处理是指在没有游离氧的情况下,厌氧微生物对有机物进行降解 的稳定无害化处理过程。在厌氧生物处理过程中,复杂的有机化合物被降解,转换为简单、 稳定的化合物,同时释放能量。目前,比较先进且应用日趋广泛的是UASB反应器。
[0016] 现在的处理工艺已经逐渐转向以厌氧一好氧联合处理为轴心与物化或化学方法 结合的混合多级处理工艺,以期达到最佳处理效果。厌氧一好氧联合处理法的微生物对营 养物质、温度、PH值有一定要求,虽然占地面积较大,管理复杂,但其对C0D、B0D和色度去除 率高,效果稳定的优点仍然使其在处理染料废水中占有重要的地位。
[0017] 然而,虽然染料废水可以采用上述方法或者几种方式联合的方法进行处理,但是 目前染料废水的处理仍不理想。主要原因如下:由于采用盐析方式生产染料的废水含盐量 过高,盐含量高达8% -10%,高盐量无法完成厌氧一好氧的生化过程,虽然可以采用稀释 的方法降低盐含量,但大量的染料废水需要数倍的清水稀释才能达到生化处理所能承受的 盐含量要求,因此稀释的方法并不现实。另一方面,如果采用活性炭吸附方法,虽然此方法 对盐含量无要求,但是废水中的高浓度使活性炭很快达到饱和状态,成本高,因此活性炭吸 附法不能应用在主处理过程中。
[0018] CN102260009B公开了一种染料废水的处理方法,将经过预先处理的染料废水送 入纳滤进水罐进行纳滤,形成体积较小的纳滤浓缩液和体积较大的纳滤透析液;所述纳滤 浓缩液经过稀释降低盐含量,然后进行厌氧好氧处理;所述纳滤透析液进行活性炭吸附处 理。但是该方法预处理过程复杂,处理过程中多次使用滤膜,提高了处理废水的成本,不利 于该方法的推广。
发明内容
[0019] 本发明的目的在于提供一种染料废水的处理方法,该方法针对含盐量高的染料废 水也可以有效去除COD、BOD和色度,且效果稳定。
[0020] 为实现上述目的,本发明的技术解决方案是:
[0021] -种染料废水的处理方法,将经过预先催化氧化的染料废水进行厌氧好氧处理, 再将厌氧好氧处理后的废水进行活性炭吸附处理后排出。
[0022] 所述预先催化氧化处理包括以下步骤:
[0023] (1)预处理:染料废水经排水管网收集后首先经过格栅格网,去除水中所含的大 颗粒悬浮物,然后流入带有搅拌装置的废水池;
[0024] (2)投加催化氧化剂和过氧化氢溶液:向废水池加入催化氧化剂和过氧化氢,并 开启搅拌装置,进行搅拌;
[0025] (3)砂滤和纳滤处理:将经过催化氧化处理后的废水送入砂滤器中,经过砂滤后 的废水的出水流量的大部分进入纳滤进水罐进行纳滤,小部分用于砂滤反冲洗,反冲洗水 返回步骤(1)中所述的均质废水池。
[0026] 步骤(2)所述的过氧化氢加入量为:2. 2~6. 8kg/吨废水,过氧化氢溶液的浓度 为 30%。
[0027] 步骤(2)所述的催化氧化剂的加入量为0. 5~2. 5kg/吨废水。
[0028] 步骤(3)中经过砂滤后的废水的出水流量的95%进入纳滤进水罐进行纳滤;经过 砂滤后的废水的出水流量的5%用于砂滤反冲洗。所述的活性炭吸附处理为:采用三级活 性炭吸附,活性炭吸附饱和后,进行生物再生,反复利用。
[0029] 所述的催化氧化处理后的废水与生活污水混合进行稀释。
[0030] 所述厌氧好氧处理具体为:
[0031] (4)生活污水预处理:生活污水首先经过格栅格网,去除水中所含的大颗粒悬浮 物,然后流入生活污水均质调节池,催化氧化处理后的废水直接进入生活污水均质调节池, 催化氧化处理后的废水与生活污水混合的废水在生活污水均质调节池内停留一般时间,再 由提升栗将水送到厌氧生化反应器;
[0032] (5)厌氧处理:纳滤池出水进入厌氧生化反应器进行高效厌氧生物处理;
[0033] (6)好氧处理:经厌氧生化反应器处理后的出水进入好氧生物反应器进一步降解 有机物;经好氧处理后的污水可以达到排放要求。
[0034] 经好氧处理后,还可再经混凝沉淀处理:混凝处理,向经好氧生物反应器处理后的 废水中投加入聚合硫酸铁,使其终浓度达到l〇〇mg/L,通过混凝使废水中的胶体物质聚集成 较大絮粒,通过沉淀从废水中去除,而混凝的颗粒经沉淀去除后,即可达标排放。
[0035] 经过混凝沉淀处理后,还可再进行砂滤处理和回用步骤:经过混凝处理后的废水 再经砂滤处理,生成水质达标的达标水,再进行过反渗透膜处理,用于生产产品的回用,其 余浓缩液达标排放。
[0036] 所述方法进一步包括污泥处理步骤:将染料废水处理部分产生的污泥,由螺杆栗 输送至污泥浓缩池,再抽升至污泥浓缩脱水一体化机械设备进行脱水,污泥上清液回流至 步骤(4)重新处理,泥饼外运。
[0037] 采用上述方案后,本发明针对染料废水含盐量高(盐含量高达8% -10% )、C0D浓 度高的特点,前端先进行预先催化氧化处理降低部分COD负荷,后端采用厌氧-好氧生化过 程进一步降低污水中的C0D,从而完成污水的处理。
[0038] 与现有技术相比,本发明的有益效果为:
[0039] 本发明的方法简单、反应条件温、速度快、操作容易,预处理时采用的催化剂可以 回收,循环使用;反应时不需要酸性条件不需要调节pH值,避免了大量酸的消耗;处理过程 短,处理效率高。
具体实施方式
[0040] 下面通过具体实施方式来进一步说明本发明的技术方案。
[0041] 本发明是一种染料废水的处理方法,它包括以下步骤:
[0042] (1)预处理:废水经排水管网收集,进入本污水处理系统。废水首先经过格栅格 网,去除水中所含的大颗粒悬浮物,然后流入带有搅拌装置的废水池。
[0043] 传统的机械格栅和筛网分离效率很低,本设计选用机械旋转格栅,可去除固体物 质,以保证后续工艺的顺利运行。
[0044] (2)投加催化氧化剂和过氧化氢溶液:向废水池加入催化氧化剂和过氧化氢,并 开启搅拌装置,进行搅拌。
[0045] (3)砂滤和纳滤处理:经过砂滤后的废水的出水流量的95%进入纳滤进水罐,;经 过砂滤后的废水的出水流量的5%用于砂滤反冲洗,反冲洗水返回步骤(1)中所述的废水 池。
[0046] (4)生活污水的预处理:生活污水经排水管网收集,进入本污水处理系统,污水首 先经过格栅格网,去除水中所含的大颗粒悬浮物,然后流入生活污水均质调节池。步骤(5) 中的纳滤浓缩液直接进入生活污水均质调节池。生活污水均质调节池内设水下搅拌机,为 了使水均质,停留时间设计为24小时,再由提升栗将水送到厌氧生化反应器进行厌氧处 理。
[0047] (5)厌氧处理:纳滤池出水经过水栗提升后进入厌氧生化反应器,进行高效厌氧 生物处理。废水经过厌氧降解以后可以去除大部分有机物,同时对较难降解的物质可以经 过厌氧酸化分解为小分子有机物,有利于后续好氧生物处理。
[0048] (6)好氧处理:经厌氧生化反应器处理后的出水进入好氧生物反应器进一步降解 有机物。好氧生物反应器是在好氧条件下利用好氧微生物使有机物分解成二氧化碳和水。 经好氧处理后的污水可以达到排放要求。
[0049] (7)活性炭吸附处理:由于纳滤透析液的COD较高,为保证出水质量,纳滤透析液 采用三级活性炭吸附,活性炭吸附饱和后,进行生物再生,反复利用。(8)混凝沉淀处理:废 水经过生化处理后,还有磷、部分难以降解的有机物、色度、SS等污染物,这些污染物通过后 续物化处理进行去除,物化处理采用网格混凝沉淀池。进入混凝前,向经好氧生物反应器处 理后的废水中投加一定剂量的聚合硫酸铁,使其终浓度达到l〇〇mg/L,通过混凝使废水中的 胶体物质聚集成较大絮粒,通过沉淀从废水中去除,而混凝的颗粒经沉淀去除后,即可达标 排放。
[0050] (9)砂滤处理和回用:经过混凝处理后的废水再经砂滤处理,生成水质达标的达 标水,再将经砂滤处理处理后的达标水进行反渗透膜处理,用于生产产品的回用,设计回收 率50 %,其余浓缩液达标排放。
[0051] (10)污泥处理:将染料废水处理部分产生的污泥,由螺杆栗输送至污泥浓缩池, 再抽升至污泥浓缩脱水一体化机械设备进行脱水,污泥上清液回流至步骤(4)重新处理, 泥饼外运。
[0052] 本发明废水处理实例如下:
[0053] 染料废水原水:处理量300m3/d,COD约为6000~7000mg/L,盐含量5~8% ;
[0054] 生活污水原水:生活污水处理量1500m3/d,COD为200~300mg/L。综合处理原水: 染料废水经过预催化氧化处理后,得到COD约为1000~2000mg/L,含盐量5~8 %的生化处 理原水;将该废水与1500m3/d的生活污水混合后将盐含量降到1 %以下,COD约为1000~ 1500mg/L,经过厌氧好氧处理后的废水其COD值为70-90mg/L。
[0055] 表1所列为本发明各工艺步骤会对上述实例的处理效率表。
[0056] 表 1
[0057]
[0058] 申请人声明,本发明通过上述实施例来说明本发明的详细方法,但本发明并不局 限于上述详细方法,即不意味着本发明必须依赖上述详细方法才能实施。所属技术领域的 技术人员应该明了,对本发明的任何改进,对本发明产品各原料的等效替换及辅助成分的 添加、具体方式的选择等,均落在本发明的保护范围和公开范围之内。
Claims (10)
1. 一种染料废水的处理方法,其特征在于:将经过预先催化氧化的染料废水进行厌氧 好氧处理;再将厌氧好氧处理后的废水进行活性炭吸附处理后排出。
2. 根据权利要求1所述染料废水的处理方法,其特征在于:所述预先催化氧化包括以 下步骤: (1) 预处理:染料废水经排水管网收集后首先经过格栅格网,去除水中所含的大颗粒 悬浮物,然后流入带有搅拌装置的废水池; (2) 投加催化氧化剂和过氧化氢溶液:向废水池加入催化氧化剂和过氧化氢,并开启 搅拌装置,进行搅拌; (3) 砂滤和纳滤处理:将经过催化氧化处理后的废水送入砂滤器中,经过砂滤后的废 水的出水流量的大部分进入纳滤进水罐进行纳滤,小部分用于砂滤反冲洗,反冲洗水返回 步骤(1)中所述的废水池。
3. 根据权利要求2所述染料废水的处理方法,其特征在于:步骤(2)所述的过氧化氢 加入量为:2. 2~6. 8kg/吨废水,过氧化氢溶液的浓度为30%。
4. 根据权利要求2或3所述染料废水的处理方法,其特征在于:步骤(2)所述的催化 氧化剂的加入量为0. 5~2. 5kg/吨废水。
5. 根据权利要求2-4之一所述染料废水的处理方法,其特征在于:步骤(3)中经过砂 滤后的废水的出水流量的95%进入纳滤进水罐进行纳滤;经过砂滤后的废水的出水流量 的5%用于砂滤反冲洗。
6. 根据权利要求1-5之一所述染料废水的处理方法,其特征在于:所述的催化氧化处 理使用的催化剂为氯氧化铁。
7. 根据权利要求1-6之一所述染料废水的处理方法,其特征在于:所述的处理方法还 包括催化氧化处理后的废水与生活污水混合进行稀释; 优选地,所述活性炭吸附处理为采用三级活性炭吸附,活性炭吸附饱和后,进行生物再 生,反复利用。
8. 根据权利要求7所述染料废水的处理方法,其特征在于:所述厌氧好氧处理具体 为: (4) 生活污水预处理:生活污水首先经过格栅格网,去除水中所含的大颗粒悬浮物,然 后流入生活污水均质调节池,催化氧化处理后的废水直接进入生活污水均质调节池,催化 氧化处理后的废水与生活污水混合的废水在生活污水均质调节池内停留一般时间,再由提 升栗将水送到厌氧生化反应器; (5) 厌氧处理:均质调节池出水进入厌氧生化反应器进行高效厌氧生物处理; (6) 好氧处理:经厌氧生化反应器处理后的出水进入好氧生物反应器进一步降解有机 物。
9. 根据权利要求1-8之一所述染料废水的处理方法,其特征在于:经好氧处理后,还可 再经混凝沉淀处理:混凝处理,向经好氧生物反应器处理后的废水中投加入聚合硫酸铁,使 其终浓度达到l〇〇mg/L,通过混凝使废水中的胶体物质聚集成较大絮粒,通过沉淀从废水中 去除,而混凝的颗粒经沉淀去除后,即可达标排放。
10. 根据权利要求1-9之一所述染料废水的处理方法,其特征在于:经过混凝沉淀处理 后,还可再进行砂滤处理和回用步骤:经过混凝处理后的废水再经砂滤处理,生成水质达标 的达标水,再进行过反渗透膜处理,用于生产产品的回用,其余浓缩液达标排放。 优选地,所述染料废水的处理方法还包括污泥处理步骤:将染料废水处理部分产生的 污泥,由螺杆栗输送至污泥浓缩池,再抽升至污泥浓缩脱水一体化机械设备进行脱水,污泥 上清液回流至步骤(4)重新处理,泥饼外运。
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