CN101941749B - Method for treating high-concentration copper-containing antibiotic wastewater and recovering copper by iron-carbon micro-electrolysis - Google Patents
Method for treating high-concentration copper-containing antibiotic wastewater and recovering copper by iron-carbon micro-electrolysis Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 59
- 239000010949 copper Substances 0.000 title claims abstract description 44
- 239000002351 wastewater Substances 0.000 title claims abstract description 44
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 26
- 230000003115 biocidal effect Effects 0.000 title claims abstract description 13
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 7
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 title claims abstract description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 34
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims abstract description 11
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims abstract description 11
- YBHILYKTIRIUTE-UHFFFAOYSA-N berberine Chemical compound C1=C2CC[N+]3=CC4=C(OC)C(OC)=CC=C4C=C3C2=CC2=C1OCO2 YBHILYKTIRIUTE-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000004519 manufacturing process Methods 0.000 claims abstract description 9
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 239000007791 liquid phase Substances 0.000 claims abstract description 4
- 239000007790 solid phase Substances 0.000 claims abstract description 3
- 229910052742 iron Inorganic materials 0.000 claims description 12
- 229910052799 carbon Inorganic materials 0.000 claims description 10
- 239000000047 product Substances 0.000 claims description 6
- 239000010865 sewage Substances 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 239000003610 charcoal Substances 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 238000001465 metallisation Methods 0.000 claims 3
- 238000001914 filtration Methods 0.000 claims 2
- 230000002829 reductive effect Effects 0.000 claims 2
- ZRBGFWOXAQPDTH-UHFFFAOYSA-N umbellatine Natural products C1=C2C3=CC4=CC=C(OC)C(OC)=C4C(O)N3CCC2=CC2=C1OCO2 ZRBGFWOXAQPDTH-UHFFFAOYSA-N 0.000 claims 2
- 230000001112 coagulating effect Effects 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 239000006228 supernatant Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 229940093265 berberine Drugs 0.000 abstract description 8
- QISXPYZVZJBNDM-UHFFFAOYSA-N berberine Natural products COc1ccc2C=C3N(Cc2c1OC)C=Cc4cc5OCOc5cc34 QISXPYZVZJBNDM-UHFFFAOYSA-N 0.000 abstract description 8
- 239000003242 anti bacterial agent Substances 0.000 abstract description 7
- 229940088710 antibiotic agent Drugs 0.000 abstract description 7
- 238000004064 recycling Methods 0.000 abstract description 5
- 239000005416 organic matter Substances 0.000 abstract description 4
- 238000002306 biochemical method Methods 0.000 abstract description 2
- 239000003054 catalyst Substances 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 description 5
- 238000004065 wastewater treatment Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 230000002195 synergetic effect Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000020477 pH reduction Effects 0.000 description 2
- 238000011085 pressure filtration Methods 0.000 description 2
- 229910021592 Copper(II) chloride Inorganic materials 0.000 description 1
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
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Abstract
本发明涉及一种铁碳微电解处理高浓度含铜抗生素废水及回收铜的方法,属于水处理应用及资源化领域。该方法以高浓度的含铜抗生素废水为处理对象,主要采用廉价的铁粉和炭粉为原料,利用过程中炭的吸附作用、铁的还原作用以及Fe/C微电池的氧化还原作用等,一方面消减废水中有机物负荷与抗生素的浓度,另一方面还原废水中的Cu2+,使其从液相转化到固相之中,进而提高了废水的可生化性,是生化方法强有力的补充。同时对反应后的残渣进行压滤,对滤渣进行焚烧,并进一步提纯、酸化得到CuCl2成品。CuCl2是生产抗生素黄连素生产过程中的必不可少的一种催化剂原料,进而实现铜的循环利用。
The invention relates to a method for treating high-concentration copper-containing antibiotic waste water and recovering copper by iron-carbon micro-electrolysis, which belongs to the field of water treatment application and resource utilization. This method takes high-concentration copper-containing antibiotic wastewater as the treatment object, and mainly uses cheap iron powder and carbon powder as raw materials. On the one hand, it reduces the organic matter load and the concentration of antibiotics in the wastewater, and on the other hand, it reduces the Cu 2+ in the wastewater to transform it from the liquid phase to the solid phase, thereby improving the biodegradability of the wastewater, which is a powerful biochemical method. Replenish. At the same time, press filter the residue after the reaction, incinerate the filter residue, and further purify and acidify to obtain CuCl 2 finished product. CuCl 2 is an indispensable catalyst raw material in the production process of the antibiotic berberine, thereby realizing the recycling of copper.
Description
技术领域 technical field
本发明技术属于环境保护领域,特别涉及一种高效的废水处理与资源化技术,该方法能提高废水的可生化性,与生化处理方法相结合,能弥补生化处理方法中的不足之处,同时该方法作为高浓度含铜抗生素废水处理工艺中一个重要环节,能实现废水中铜的资源化回收,从而大大降低废水的处理成本。The technology of the present invention belongs to the field of environmental protection, and in particular relates to a high-efficiency waste water treatment and recycling technology. The method can improve the biodegradability of waste water. Combining with the biochemical treatment method, it can make up for the deficiencies in the biochemical treatment method, and at the same time As an important link in the treatment process of high-concentration copper-containing antibiotic wastewater, the method can realize resource recovery of copper in wastewater, thereby greatly reducing the cost of wastewater treatment.
背景技术 Background technique
含铜黄连素生产废水属于化学合成类药物生产中较为典型的一种难降解废水,其含有高浓度的Cu2+、有机物和悬浮物质量浓度高、pH值波动较大、成份复杂等特点,其中废水中含有高浓度的Cu2+和黄连素等对微生物活性具有较强的抑制作用,很难直接进行生化处理,必须采取合适的物化方法对其进行预处理。因而,寻找一种实际操作可行、成本相对较低廉且能同时削减黄连素及Cu2+浓度的工艺方法势在必行。Copper-containing berberine production wastewater is a typical refractory wastewater in the production of chemical synthesis drugs. It contains high concentrations of Cu 2+ , high concentrations of organic matter and suspended matter, large pH fluctuations, and complex components. The wastewater contains high concentrations of Cu 2+ and berberine, etc., which have a strong inhibitory effect on microbial activity, and it is difficult to directly carry out biochemical treatment. Appropriate physical and chemical methods must be adopted for pretreatment. Therefore, it is imperative to find a process method that is feasible in practice, relatively low in cost, and can simultaneously reduce the concentration of berberine and Cu 2+ .
近年来,关于铁碳微电解法处理各种废水的研究报道很多。铁碳微电解技术是利用具有不同电极电位的铁和碳作为电极形成无数个微小原电池,发生电极反应,进而产生电化学效应而去除废水中的污染物。本发明工艺方法采用廉价的铁粉与炭粉,通过铁的还原、碳的吸附以及Fe/C原电池的氧化还原等的协同作用,同时消除废水中高浓度的抗生素及Cu2+的含量,有利于废水的进一步生化处理。另外,产生的废渣通过焚烧、提纯和酸化处理得到CuCl2成品,而该产品是生产黄连素必不可少的原料,实现了铜的循环利用,且大大降低了废水的处理成本。In recent years, there have been many research reports on the treatment of various wastewater by iron-carbon micro-electrolysis. The iron-carbon micro-electrolysis technology uses iron and carbon with different electrode potentials as electrodes to form countless tiny primary batteries, and electrode reactions occur, thereby producing electrochemical effects to remove pollutants in wastewater. The process of the present invention adopts cheap iron powder and carbon powder, through the synergistic effect of reduction of iron, adsorption of carbon and redox of Fe/C primary battery, etc., simultaneously eliminates high-concentration antibiotics and Cu 2+ content in waste water, has It is beneficial to the further biochemical treatment of wastewater. In addition, the generated waste residue is incinerated, purified and acidified to obtain CuCl 2 finished product, which is an indispensable raw material for the production of berberine, realizes the recycling of copper, and greatly reduces the cost of wastewater treatment.
发明内容 Contents of the invention
本发明的目的在于提出一种简单可行、成本相对低廉、能同时削减废水中高浓度抗生素及Cu2+且能实现铜的资源化回收的处理方法。The purpose of the present invention is to propose a treatment method that is simple, feasible, relatively low in cost, can simultaneously reduce high-concentration antibiotics and Cu 2+ in wastewater, and can realize resource recovery of copper.
本发明提出的高浓度含铜抗生素废水的处理方法,是一种基于“铁碳微电解”的物化处理方法。该方法采用廉价的铁粉及炭粉为原料,利用处理过程中炭的吸附、铁的还原以及Fe/C微电池的氧化还原等协同作用,一方面消减废水中有机物负荷与抗生素的浓度,另一方面通过还原废水中的Cu2+,使其从液相转化到固相之中,从而实现废水中Cu2+的去除。同时对反应后的残渣进行压滤,滤液与生活污水混合后进入后续生化处理工艺,而对滤渣进行焚烧,并进一步提纯、酸化得到CuCl2成品,CuCl2是生产黄连素生产过程中的必不可少的一种催化剂原料,进而实现铜的循环利用。The method for treating high-concentration copper-containing antibiotic wastewater proposed by the present invention is a physicochemical treatment method based on "iron-carbon micro-electrolysis". This method uses cheap iron powder and carbon powder as raw materials, and utilizes the synergistic effects of carbon adsorption, iron reduction, and Fe/C micro-battery redox during the treatment process. On the one hand, it reduces the organic matter load and the concentration of antibiotics in wastewater. On the one hand, the Cu 2+ in the wastewater can be removed by reducing the Cu 2+ in the wastewater to make it transform from the liquid phase to the solid phase. At the same time, press filter the residue after the reaction, mix the filtrate with domestic sewage and enter the subsequent biochemical treatment process, and incinerate the filter residue, and further purify and acidify to obtain CuCl 2 finished product, CuCl 2 is essential in the production process of berberine A less catalyst raw material, and then realize the recycling of copper.
本发明的反应装置如附图所示。本发明的具体方法如下:The reaction device of the present invention is as shown in the accompanying drawing. Concrete method of the present invention is as follows:
该方法采用间歇式的方式对废水进行处理。储水槽1中的含铜抗生素废水通过水泵2经由进水口5进入反应器主体3,投加一定量的铁粉与炭粉,通过电动搅拌器4对体系进行充分搅拌,反应完毕后静置沉淀,打开出水口阀门6,排放处理出水并通过与生活污水混合的方式进入进一步的生化处理单元,最后打开排泥口阀门7,对过程中产生的废渣进行压滤、焚烧、提纯、酸化等工艺实现铜的资源化利用。The method adopts an intermittent method to treat wastewater. The copper-containing antibiotic wastewater in the water storage tank 1 enters the reactor main body 3 through the
本发明的特点如下:Features of the present invention are as follows:
1.该方法将铁的还原与碳的吸附过程综合,使铁碳的协同作用在一个体系中集成。1. This method integrates the reduction of iron and the adsorption process of carbon, so that the synergistic effect of iron and carbon is integrated in one system.
2.该方法采用廉价的铁和炭为原料,通过回收废水中高浓度的铜,从而大大降低废水的处理成本。2. The method uses cheap iron and charcoal as raw materials, and recycles high-concentration copper in wastewater, thereby greatly reducing the cost of wastewater treatment.
3.该方法采用间歇式的方式对高浓度含铜废水进行处理,使得体系更容易控制。3. The method adopts an intermittent method to treat high-concentration copper-containing wastewater, which makes the system easier to control.
4.该方法能大大削减废水中抗生素及Cu2+的含量,有利于提高废水的可生化性,是生化方法强有力的补充。4. The method can greatly reduce the content of antibiotics and Cu 2+ in the wastewater, which is beneficial to improve the biodegradability of the wastewater, and is a powerful supplement to the biochemical method.
5.该方法采用原料均为粉末态,一方面防止了生成的铜包裹于铁的表面,使得铁反应更充分,提高了铁的利用率,另一方面有利用碳对废水中有机物尤其是抗生素的吸附。5. This method uses raw materials that are all in powder state. On the one hand, it prevents the generated copper from being wrapped on the surface of the iron, so that the iron reacts more fully and improves the utilization rate of iron. On the other hand, it can use carbon to treat organic matter in wastewater, especially antibiotics. of adsorption.
6.该方法通过搅拌器实现废水与铁、炭粉的混合均匀,促进了反应的进行,提高了反应速度与处理效率。6. The method uses a stirrer to realize uniform mixing of waste water, iron and carbon powder, which promotes the reaction and improves the reaction speed and treatment efficiency.
7.该方法通过对产生的废渣进行压滤、焚烧、提纯或酸化,可实现CuCl2的资源化回收。7. The method realizes resource recovery of CuCl 2 by performing pressure filtration, incineration, purification or acidification on the generated waste residue.
8.该方法通过把回收的CuCl2应用于抗生素的生产过程,进而实现了铜的循环利用。8. The method realizes the recycling of copper by applying the recovered CuCl 2 to the production process of antibiotics.
9.该方法操作简单,设备紧凑,易于操作,切实可行。9. The method is simple in operation, compact in equipment, easy to operate, and practical.
本发明方法可用于高浓度含铜抗生素废水的处理,也可以用于其它高浓度含铜废水的处理及铜的资源化回收利用。The method of the invention can be used for the treatment of high-concentration copper-containing antibiotic wastewater, and can also be used for the treatment of other high-concentration copper-containing wastewater and the resource recovery and utilization of copper.
附图说明 Description of drawings
1.储水槽 2.水泵 3.反应器主体 4.电动搅拌器1.
5.进水口 6.出水口及阀门 7.排泥口及阀门5. Water inlet 6. Water outlet and valve 7. Mud discharge port and valve
具体实施方式 Detailed ways
实施例1:Example 1:
某制药厂生产过程中产生的含铜抗生素废水,该废水的水质为:废水COD约为80000mg/L,Cu2+浓度约为20000mg/L,抗生素黄连素浓度为1700~1900mg/L。当废水pH值为2.0-3.0,铁炭投加量分别为25g/L和30g/L,反应90min条件后,废水中黄连素的去除率可达70%以上,Cu2+的去除率高达99.9%以上。对滤渣进行焚烧、提纯、酸化后得到CuCl2成品,该方法工艺可实现处理吨水回收铜18-19kg(以Cu计)。Copper-containing antibiotic wastewater produced in the production process of a pharmaceutical factory. The water quality of the wastewater is: wastewater COD is about 80,000mg/L, Cu 2+ concentration is about 20,000mg/L, and antibiotic berberine concentration is 1700-1900mg/L. When the pH value of the wastewater is 2.0-3.0, the dosage of iron and carbon is 25g/L and 30g/L respectively, and after 90 minutes of reaction, the removal rate of berberine in the wastewater can reach more than 70%, and the removal rate of Cu 2+ can reach as high as 99.9% %above. The filter residue is incinerated, purified, and acidified to obtain the CuCl2 finished product. This method and process can realize the recovery of copper 18-19kg (calculated as Cu) per ton of water.
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