CN106734046A - A kind of coking sludge method for innocent treatment - Google Patents
A kind of coking sludge method for innocent treatment Download PDFInfo
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- CN106734046A CN106734046A CN201510815834.2A CN201510815834A CN106734046A CN 106734046 A CN106734046 A CN 106734046A CN 201510815834 A CN201510815834 A CN 201510815834A CN 106734046 A CN106734046 A CN 106734046A
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- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/10—Destroying solid waste or transforming solid waste into something useful or harmless involving an adsorption step
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Abstract
本发明公开了一种焦化污泥无害化处理方法。这种方法具体工艺如下:将焦化污泥放置于容器内,功能材料改性环糊精包于滤网内,放于焦化污泥的中,通过对焦化污泥进行搅拌,使二者接触,达到无害化处理的目的。本发明首次使用改性环糊精处理焦化污泥,经过改性环糊精处理后的焦化污泥,其有机污染物如苯类和酚类有机污染物浓度从50000mg/L降低到20mg/L;重金属离子(Cr,Ni等离子)的含量,从10000mg/L降低到10mg/L;有效去除焦化污泥的臭味;此种改性环糊精还可以进行再生处理,能够将焦化污泥处理成本降低,从0.5-2万元/吨污泥,降低到小于0.5万元/吨污泥;经无害化处理的焦化污泥可以进行资源再利用;减少和降低了焦化污泥对环境的污染,避免在处理过程中产生的二次污染。
The invention discloses a harmless treatment method for coking sludge. The specific process of this method is as follows: the coking sludge is placed in a container, the functional material modified cyclodextrin is wrapped in a filter screen, placed in the coking sludge, and the coking sludge is stirred to make the two contact, To achieve the purpose of harmless treatment. The present invention uses modified cyclodextrin to treat coking sludge for the first time, and the concentration of organic pollutants such as benzene and phenol organic pollutants in the coking sludge treated by modified cyclodextrin is reduced from 50000mg/L to 20mg/L ; The content of heavy metal ions (Cr, Ni plasma) is reduced from 10000mg/L to 10mg/L; effectively removes the odor of coking sludge; this kind of modified cyclodextrin can also be regenerated, and can treat coking sludge The cost is reduced from 0.5-20,000 yuan/ton of sludge to less than 0.5 million yuan/ton of sludge; the harmless treated coking sludge can be reused as resources; the impact of coking sludge on the environment is reduced and reduced Pollution, to avoid secondary pollution in the process of processing.
Description
技术领域technical field
本发明属于环境化工领域,特别涉及一种焦化污泥无害化处理方法。The invention belongs to the field of environmental chemical industry, in particular to a harmless treatment method of coking sludge.
背景技术Background technique
焦化废水处理是焦化行业难题,焦化废水的成分复杂,能够被测出的有害物质就有100多种,经过工艺处理的焦化废水外排,剩余的污泥还没有处理措施。经过分析发现焦化污泥中含有苯类、酚类、以及多环芳烃等污染物,还含有多种重金属离子以及金属氧化物,所以无论将焦化污泥进行何种后续处理,都应该首先要对其进行无害化处理,降低或除去其污染物。目前,焦化污泥常不经过任何无害化处理后,送入煤场,用于燃烧或炼焦等。这样污染物继续留在污泥中,造成二次污染,对环境有很大的污染。周玉青等(化学反应工程与工艺,2011,27(5):477-480)在“用新型交联β-环糊精处理苯酚废水”一文中提到交联环糊精的再生吸附率达到88%以上,这一再生吸附是在不断补充损失量的情况下,文章没有提及交联β-环糊精在吸附和再生过程损失,以及如何解决这种损失。王海军等(生物加工过程,2013,11(6):82-85)在“HDI改性β-环糊精及其焦化废水处理”中发现,HDI-β-CD的吸附性能可以再生,重复再生10次后吸附率仍在58.1%,没有研究HDI-β-CD在使用过程中的质量损耗问题。李仲谨等(精细化工,2010,27(7):692-695)在“β-环糊精聚合物微球的合成与表征”中使用环氧氯丙烷为交联剂,用反相乳液法合成了β-环糊精聚合物微球,微球粒径为10μm,没有研究其应用和再生问题。Coking wastewater treatment is a difficult problem in the coking industry. The composition of coking wastewater is complex, and there are more than 100 harmful substances that can be detected. The treated coking wastewater is discharged, and the remaining sludge has no treatment measures. After analysis, it is found that the coking sludge contains pollutants such as benzene, phenols, and polycyclic aromatic hydrocarbons, as well as a variety of heavy metal ions and metal oxides. It undergoes harmless treatment to reduce or remove its pollutants. At present, coking sludge is often sent to coal yards for combustion or coking without any harmless treatment. In this way, the pollutants continue to remain in the sludge, causing secondary pollution and causing great pollution to the environment. Zhou Yuqing et al. (Chemical Reaction Engineering and Technology, 2011, 27(5):477-480) mentioned in the article "Treatment of Phenol Wastewater with New Cross-linked β-cyclodextrin" that the regeneration adsorption rate of cross-linked cyclodextrin reached More than 88%, this regenerative adsorption is under the condition that the loss amount is constantly replenished. The article does not mention the loss of cross-linked β-cyclodextrin in the adsorption and regeneration process, and how to solve this loss. Wang Haijun et al. (Bioprocessing, 2013, 11(6): 82-85) found in "HDI-modified β-cyclodextrin and its coking wastewater treatment" that the adsorption performance of HDI-β-CD can be regenerated and regenerated The adsorption rate was still 58.1% after 10 times, and the mass loss of HDI-β-CD during use was not studied. Li Zhongjin et al. (Fine Chemical Industry, 2010, 27(7): 692-695) used epichlorohydrin as a crosslinking agent in "Synthesis and Characterization of β-cyclodextrin Polymer Microspheres" and synthesized by inverse emulsion method β-cyclodextrin polymer microspheres with a particle size of 10 μm were studied, but their application and regeneration were not studied.
发明内容Contents of the invention
为解决焦化污泥的无害化问题,本发明的提供了一种焦化污泥无害化处理方法,具体是使用自制的改性环糊精(具体制备方法见专利CN 201410639016.7),让其与焦化污泥充分混合后,进行无害化处理。以减少焦化污泥对环境的污染,并将焦化污泥进行无害化处理后进行再利用。In order to solve the harmless treatment of coking sludge, the present invention provides a method for harmless treatment of coking sludge, specifically using self-made modified cyclodextrin (see patent CN 201410639016.7 for the specific preparation method), allowing it to be compared with After the coking sludge is fully mixed, it will be treated innocuously. In order to reduce the pollution of coking sludge to the environment, the coking sludge will be reused after harmless treatment.
为实现上述目的,本发明采用以下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
焦化污泥放置于容器内,功能材料改性环糊精包于滤网内,放于焦化污泥的中,通过对焦化污泥进行搅拌,使二者接触,达到无害化处理的目的。The coking sludge is placed in the container, and the functional material modified cyclodextrin is wrapped in the filter screen, placed in the coking sludge, and the coking sludge is stirred to make the two contact to achieve the purpose of harmless treatment.
具体步骤如下:Specific steps are as follows:
A 将制备的改性环糊精在50℃以上真空干燥中干燥24~32h;A Dry the prepared modified cyclodextrin in vacuum drying above 50°C for 24-32 hours;
B 向容器中加入一定量的焦化污泥;B Add a certain amount of coking sludge into the container;
C 将改性环糊精包于滤网内;C Wrap the modified cyclodextrin in the filter screen;
D 将滤网内改性环糊精放置于焦化污泥中;D Place the modified cyclodextrin in the filter in the coking sludge;
E 对焦化污泥进行搅拌。E Stir the coking sludge.
优选的,步骤B中,污泥可以是焦化污泥,也可以是其它工业废水处理后的污泥。Preferably, in step B, the sludge may be coking sludge, or sludge after treatment of other industrial wastewater.
本发明所述改性环糊精不仅对污泥中的苯类、酚类有机污染物有吸附作用,对重金属离子也有较好的去除作用。The modified cyclodextrin of the invention not only has adsorption effect on benzene and phenol organic pollutants in sludge, but also has better removal effect on heavy metal ions.
本发明的有益效果是:The beneficial effects of the present invention are:
1、本发明首次使用改性环糊精处理焦化污泥,经过改性环糊精处理后的焦化污泥,其有机污染物如苯类和酚类有机污染物浓度从50000mg/L降低到20mg/L;1. The present invention uses modified cyclodextrin to treat coking sludge for the first time, and the concentration of organic pollutants such as benzene and phenol organic pollutants in the coking sludge treated by modified cyclodextrin is reduced from 50000mg/L to 20mg /L;
2、重金属离子(Cr,Ni等离子)的含量,从10000mg/L降低到10mg/L;2. The content of heavy metal ions (Cr, Ni plasma) is reduced from 10000mg/L to 10mg/L;
3、有效去除焦化污泥的臭味;3. Effectively remove the odor of coking sludge;
4、此种改性环糊精还可以进行再生处理,能够将焦化污泥处理成本降低,从0.5-2万元/吨污泥,降低到小于0.5万元/吨污泥;4. This kind of modified cyclodextrin can also be regenerated, which can reduce the cost of coking sludge treatment from 5,000-20,000 yuan/ton of sludge to less than 5,000 yuan/ton of sludge;
5、经无害化处理的焦化污泥可以进行资源再利用;5. The harmless treated coking sludge can be reused as resources;
6、减少和降低了焦化污泥对环境的污染,避免在处理过程中产生的二次污染。6. Reduce and reduce the pollution of coking sludge to the environment, and avoid secondary pollution during the treatment process.
附图说明Description of drawings
图1是未处理的焦化污泥。Figure 1 is untreated coking sludge.
图2经本发明处理后的焦化污泥。Fig. 2 is coking sludge treated by the present invention.
具体实施方式detailed description
下面结合附图和实施例对本发明作进一步阐述,本领域技术人员应当理解,所述实施例仅用于示例,而不对本发明构成任何限制。The present invention will be further described below in conjunction with the accompanying drawings and embodiments, and those skilled in the art should understand that the embodiments are only for illustration and do not constitute any limitation to the present invention.
实施例1Example 1
取含有机污染物浓度为50000mg/L,重金属离子为1%的未脱水焦化污泥1000ml放于烧杯中,再称量20g的改性环糊精置于滤网,将滤网放置于焦化污泥中,使用磁力搅拌器搅拌2h,取出来后的污泥进行离心分离,取上层清液,测定其浓度为500mg/L,下层的污泥分析重金属离子为100mg/L,改性环糊精再生,焦化污泥进行离心分离后,废水送废水处理厂,污泥风干后作为回填土。Take 1000ml of non-dehydrated coking sludge containing 50000mg/L of organic pollutants and 1% of heavy metal ions in a beaker, weigh 20g of modified cyclodextrin and place it in the filter screen, and place the filter screen in the coking sludge In the mud, use a magnetic stirrer to stir for 2 hours, take out the sludge for centrifugation, take the supernatant, measure its concentration as 500mg/L, and analyze the heavy metal ion of the lower layer of sludge as 100mg/L, modified cyclodextrin Regeneration, after coking sludge is centrifuged, the wastewater is sent to the wastewater treatment plant, and the sludge is air-dried and used as backfill.
实施例2Example 2
取含有机污染物浓度为25000mg/L,重金属离子为0.5%的未脱水焦化污泥1000ml放于烧杯中,再称量15g的改性环糊精置于滤网,将滤网放置于焦化污泥中,使用磁力搅拌器搅拌2h,取出来后的污泥进行离心分离,取上层清液,测定其浓度为100mg/L,下层的污泥分析重金属离子为40mg/L,改性环糊精再生,焦化污泥进行离心分离后,废水送废水处理厂,污泥风干后作为回填土。Take 1000ml of undehydrated coking sludge containing 25000mg/L of organic pollutants and 0.5% of heavy metal ions in a beaker, then weigh 15g of modified cyclodextrin and place it on the filter screen, and place the filter screen on the coking sludge. In the mud, use a magnetic stirrer to stir for 2 hours, take out the sludge for centrifugation, take the supernatant, measure its concentration as 100mg/L, and analyze the heavy metal ion of the lower layer of sludge as 40mg/L, modified cyclodextrin Regeneration, after coking sludge is centrifuged, the wastewater is sent to the wastewater treatment plant, and the sludge is air-dried and used as backfill.
实施例3Example 3
取含有机污染物浓度为1000mg/L,重金属离子为100mg/L的未脱水焦化污泥1000ml放于烧杯中,再称量15g的改性环糊精置于滤网,将滤网放置于焦化污泥中,使用磁力搅拌器搅拌2h,取出来后的污泥进行离心分离,取上层清液,测定其浓度为20mg/L,下层的污泥分析重金属离子为10mg/L,改性环糊精再生,焦化污泥进行离心分离后,废水送废水处理厂,污泥风干后作为回填土。Take 1000ml of undehydrated coking sludge containing 1000mg/L of organic pollutants and 100mg/L of heavy metal ions and put it in a beaker, then weigh 15g of modified cyclodextrin and put it on the filter screen, and place the filter screen on the coking In the sludge, use a magnetic stirrer to stir for 2 hours, take out the sludge for centrifugation, take the supernatant, measure its concentration as 20mg/L, and analyze the heavy metal ion of the lower layer of sludge as 10mg/L, modified cyclopaste Fine regeneration, coking sludge is centrifuged, the waste water is sent to the wastewater treatment plant, and the sludge is air-dried and used as backfill.
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Application publication date: 20170531 |