CN116002940A - A method for increasing methane production in anaerobic digestion of sludge containing heavy metals - Google Patents
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 122
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 87
- 230000029087 digestion Effects 0.000 title claims abstract description 82
- 238000000034 method Methods 0.000 title claims abstract description 82
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 50
- 229920002401 polyacrylamide Polymers 0.000 claims abstract description 108
- 125000000129 anionic group Chemical group 0.000 claims abstract description 52
- 125000002091 cationic group Chemical group 0.000 claims abstract description 52
- 230000008569 process Effects 0.000 claims abstract description 33
- 229910052793 cadmium Inorganic materials 0.000 claims description 20
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 4
- 229910052804 chromium Inorganic materials 0.000 claims description 4
- 239000011651 chromium Substances 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 239000010949 copper Substances 0.000 claims description 4
- 239000011133 lead Substances 0.000 claims description 4
- 239000011701 zinc Substances 0.000 claims description 4
- 229910052725 zinc Inorganic materials 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 150000001450 anions Chemical class 0.000 claims description 2
- 244000005700 microbiome Species 0.000 abstract description 24
- 238000005189 flocculation Methods 0.000 abstract description 9
- 230000016615 flocculation Effects 0.000 abstract description 9
- 238000001179 sorption measurement Methods 0.000 abstract description 7
- 208000010501 heavy metal poisoning Diseases 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 12
- 239000007787 solid Substances 0.000 description 7
- WLZRMCYVCSSEQC-UHFFFAOYSA-N cadmium(2+) Chemical compound [Cd+2] WLZRMCYVCSSEQC-UHFFFAOYSA-N 0.000 description 6
- 231100000419 toxicity Toxicity 0.000 description 5
- 230000001988 toxicity Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 230000006641 stabilisation Effects 0.000 description 4
- 238000011105 stabilization Methods 0.000 description 4
- 231100000331 toxic Toxicity 0.000 description 4
- 230000002588 toxic effect Effects 0.000 description 4
- 230000002411 adverse Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 210000002249 digestive system Anatomy 0.000 description 2
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000020477 pH reduction Effects 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
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- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 239000004343 Calcium peroxide Substances 0.000 description 1
- 239000004155 Chlorine dioxide Substances 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 239000006172 buffering agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- LHJQIRIGXXHNLA-UHFFFAOYSA-N calcium peroxide Chemical compound [Ca+2].[O-][O-] LHJQIRIGXXHNLA-UHFFFAOYSA-N 0.000 description 1
- 235000019402 calcium peroxide Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
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- 230000007246 mechanism Effects 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000004792 oxidative damage Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- PFUVRDFDKPNGAV-UHFFFAOYSA-N sodium peroxide Chemical compound [Na+].[Na+].[O-][O-] PFUVRDFDKPNGAV-UHFFFAOYSA-N 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
本发明公开了一种提升含重金属污泥厌氧消化甲烷产量的方法,该方法是利用阳离子聚丙烯酰胺或阴离子聚丙烯酰胺提升含重金属污泥厌氧消化过程中的甲烷产量。本发明方法中,首次将阳离子聚丙烯酰胺/阴离子聚丙烯酰胺引入污泥消化系统当中,通过利用阳离子聚丙烯酰胺/阴离子聚丙烯酰胺对重金属的吸附架桥作用、絮凝作用、静电吸附作用实现对污泥流动性的限制,减少重金属和微生物的直接接触,进而减缓重金属对微生物的毒害作用,从而提升厌氧消化过程中相关微生物的丰度,并提高厌氧消化系统甲烷的产量,具有工艺简单、操作方便、成本低廉、性价比高、效率高等优点,在提升污泥厌氧消化产甲烷方面,有着很高的使用价值和很好的应用前景。The invention discloses a method for increasing the methane output of anaerobic digestion of sludge containing heavy metals. The method utilizes cationic polyacrylamide or anionic polyacrylamide to increase the methane output in the process of anaerobic digestion of sludge containing heavy metals. In the method of the present invention, the cationic polyacrylamide/anionic polyacrylamide is introduced into the sludge digestion system for the first time, and the adsorption and bridging, flocculation and electrostatic adsorption of heavy metals by the cationic polyacrylamide/anionic polyacrylamide are used to realize the The limitation of sludge fluidity reduces the direct contact between heavy metals and microorganisms, thereby slowing down the toxic effect of heavy metals on microorganisms, thereby increasing the abundance of related microorganisms in the anaerobic digestion process and increasing the methane production of the anaerobic digestion system. The process is simple , convenient operation, low cost, high cost performance, high efficiency and other advantages, it has high use value and good application prospect in improving methane production by anaerobic digestion of sludge.
Description
技术领域technical field
本发明属于环保技术领域,涉及一种提升含重金属污泥厌氧消化甲烷产量的方法。The invention belongs to the technical field of environmental protection and relates to a method for increasing the methane output of anaerobic digestion of sludge containing heavy metals.
背景技术Background technique
剩余活性污泥是污水处理厂常规活性污泥处理的主要副产物,大量的污泥如果不能被很好地处理处置就直接排放则会对地面和地下水体、土壤和空气造成严重的二次污染,同时也会危害人体健康。污泥的厌氧消化是在厌氧微生物的参与下,污泥依次经历溶解、水解、酸化和产甲烷的生化过程,是最常见的污泥稳定化和资源化的手段之一。由于污泥对大多数污染物具有极强的吸附能力,因而污泥中通常会富集大量的外源污染物,例如重金属,这些重金属包括镉、铬、铜、铅、锌等。以重金属镉为例,若污泥中含有镉,则镉的富集会对污泥厌氧消化系统甲烷的产生造成不良影响。因此,如何有效降低重金属对厌氧消化系统的毒性作用,这对于有效提高厌氧消化甲烷产能具有十分重要的意义。Excess activated sludge is the main by-product of conventional activated sludge treatment in sewage treatment plants. If a large amount of sludge is not properly treated and disposed of, it will cause serious secondary pollution to surface and groundwater, soil and air. , but also endanger human health. Anaerobic digestion of sludge is a biochemical process in which sludge undergoes dissolution, hydrolysis, acidification, and methane production in sequence with the participation of anaerobic microorganisms. Because sludge has a strong adsorption capacity for most pollutants, a large amount of exogenous pollutants, such as heavy metals, including cadmium, chromium, copper, lead, zinc, etc., are usually enriched in sludge. Taking heavy metal cadmium as an example, if the sludge contains cadmium, the enrichment of cadmium will have adverse effects on the methane production in the sludge anaerobic digestion system. Therefore, how to effectively reduce the toxic effect of heavy metals on the anaerobic digestion system is of great significance for effectively increasing the methane production capacity of anaerobic digestion.
迄今为止,已经有部分研究人员做了相关尝试。例如,有研究人员提出了一种增强厌氧消化污泥重金属稳定化过程的方法,通过在污泥厌氧消化产酸阶段添加适量的改性污泥生物炭,可以明显吸附、捕获反应器中游离态重金属,从而能够增强污泥重金属的稳定化效果,然而,该方法中改性污泥生物炭的添加对污泥产甲烷和稳定化过程没有明显影响,而且改性生物炭的制备和合成较为复杂耗时,操作不便,性价比低。另外,也有研究人员提出了一种污泥厌氧消化中重金属稳定的调理剂,通过向污泥厌氧消化系统中引入氧化剂(过氧化钠、过氧化钙和二氧化氯中的至少一种)和缓冲剂(碳酸钠和碳酸氢钠混合物),减少重金属对厌氧消化的影响,可以提升污泥的水解速率,然而,此方法所采用的调理剂具有强氧化性和弱腐蚀性,因而该调理剂的购置和运输,均需要大量的人力、物力和财力,存在成本过高的问题,与此同时,该方法中采用的调理剂,对微生物的毒害作用较强,因而导致厌氧消化过程中相关微生物的丰度较差,容易抑制这些微生物的活性,从而使得厌氧消化过程中甲烷的产量仍然偏低。因此,寻求一种廉价、简捷、有效的方法,用于缓解重金属对厌氧消化系统的毒性已经成为当务之急。So far, some researchers have made related attempts. For example, some researchers have proposed a method to enhance the stabilization process of heavy metals in anaerobic digestion sludge. By adding an appropriate amount of modified sludge biochar in the acid production stage of anaerobic digestion of sludge, it can be obviously adsorbed and captured in the reactor. free heavy metals, which can enhance the stabilization effect of heavy metals in sludge. However, the addition of modified sludge biochar in this method has no obvious effect on sludge methane production and stabilization process, and the preparation and synthesis of modified biochar are comparatively Complicated and time-consuming, inconvenient to operate, and low cost performance. In addition, some researchers have proposed a conditioner for the stabilization of heavy metals in sludge anaerobic digestion, by introducing oxidants (at least one of sodium peroxide, calcium peroxide and chlorine dioxide) into the sludge anaerobic digestion system And buffering agent (sodium carbonate and sodium bicarbonate mixture), reduce the impact of heavy metals on anaerobic digestion, can increase the hydrolysis rate of sludge, however, the conditioner used in this method has strong oxidizing and weak corrosive, so this method The purchase and transportation of the conditioner requires a lot of manpower, material and financial resources, and there is a problem of high cost. At the same time, the conditioner used in this method has a strong toxic effect on microorganisms, which leads to the anaerobic digestion process. The abundance of related microorganisms in the anaerobic digestion process is relatively low, and the activity of these microorganisms is easily inhibited, so that the methane production in the anaerobic digestion process is still low. Therefore, finding a cheap, simple and effective method to alleviate the toxicity of heavy metals to the anaerobic digestive system has become a top priority.
聚丙烯酰胺是水处理领域的常用药剂,通常是用于增强固液分离和强化污泥脱水,但是,至今为止,尚未见到将聚丙烯酰胺添加到污泥的厌氧消化过程中用于调理污泥中重金属毒性的相关报道。Polyacrylamide is a commonly used agent in the field of water treatment, and is usually used to enhance solid-liquid separation and sludge dewatering. However, so far, it has not been seen that polyacrylamide is added to the anaerobic digestion process of sludge for conditioning Related reports on the toxicity of heavy metals in sludge.
发明内容Contents of the invention
本发明要解决的技术问题是克服现有技术的不足,提供一种工艺简单、操作方便、成本低廉的提升含重金属污泥厌氧消化甲烷产量的方法。The technical problem to be solved by the present invention is to overcome the deficiencies of the prior art and provide a method for increasing the methane output of anaerobic digestion of heavy metal-containing sludge with simple process, convenient operation and low cost.
为解决上述技术问题,本发明采用的技术方案是:In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:
一种提升含重金属污泥厌氧消化甲烷产量的方法,所述方法是利用阳离子聚丙烯酰胺或阴离子聚丙烯酰胺提升含重金属污泥厌氧消化过程中的甲烷产量。The invention discloses a method for increasing the methane output of anaerobic digestion of heavy metal-containing sludge, the method is to use cationic polyacrylamide or anionic polyacrylamide to increase the methane output in the process of anaerobic digestion of heavy metal-containing sludge.
上述的方法,进一步改进的,利用阳离子聚丙烯酰胺提升含重金属污泥厌氧消化过程中的甲烷产量时,所述阳离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.001~0.004∶1。The above method is further improved. When cationic polyacrylamide is used to increase the methane production in the anaerobic digestion process of sludge containing heavy metals, the mass ratio of the cationic polyacrylamide to the volatile suspended matter in sludge containing heavy metals is 0.001 ~0.004:1.
上述的方法,进一步改进的,所述阳离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.0015~0.0035∶1。The above method is further improved, the mass ratio of the cationic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.0015-0.0035:1.
上述的方法,进一步改进的,所述阳离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.0015~0.003∶1。The above method is further improved, the mass ratio of the cationic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.0015-0.003:1.
上述的方法,进一步改进的,所述阳离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.002∶1。The above method is further improved, the mass ratio of the cationic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.002:1.
上述的方法,进一步改进的,利用阴离子聚丙烯酰胺提升含重金属污泥厌氧消化过程中的甲烷产量时,所述阴离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.0005~0.003∶1。The above method is further improved. When using anionic polyacrylamide to increase the methane production in the anaerobic digestion process of heavy metal-containing sludge, the mass ratio of the anionic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.0005 ~0.003:1.
上述的方法,进一步改进的,所述阴离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.0006~0.002∶1。The above method is further improved, the mass ratio of the anionic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.0006-0.002:1.
上述的方法,进一步改进的,所述阴离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.0007~0.001∶1。The above method is further improved, the mass ratio of the anionic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.0007-0.001:1.
上述的方法,进一步改进的,所述阴离子聚丙烯酰胺与含重金属污泥中可挥发性悬浮物的质量比为0.00075∶1。The above method is further improved, the mass ratio of the anionic polyacrylamide to the volatile suspended matter in the heavy metal-containing sludge is 0.00075:1.
上述的方法,进一步改进的,包括以下步骤:The above-mentioned method, further improved, comprises the following steps:
S1、将阳离子聚丙烯酰胺与含重金属污泥混合,得到泥水混合物;S1, mixing cationic polyacrylamide with heavy metal-containing sludge to obtain a mud-water mixture;
S2、将步骤S1中得到的泥水混合物进行厌氧消化,完成对含重金属污泥的处理。S2. Perform anaerobic digestion on the mud-water mixture obtained in step S1 to complete the treatment of heavy metal-containing sludge.
上述的方法,进一步改进的,步骤S1中,所述阳离子聚丙烯酰胺以溶液的形式加入到含重金属污泥中;所述阳离子聚丙烯酰胺溶液中阳离子聚丙烯酰胺的质量体积浓度为0.5%。The above method is further improved. In step S1, the cationic polyacrylamide is added into the heavy metal-containing sludge in the form of a solution; the mass volume concentration of the cationic polyacrylamide in the cationic polyacrylamide solution is 0.5%.
上述的方法,进一步改进的,步骤S1中,所述含重金属污泥中重金属的初始浓度≥2.5mg/g VSS;所述含重金属污泥中的重金属包括镉、铬、铜、铅、锌中的至少一种。The above method is further improved, in step S1, the initial concentration of heavy metals in the heavy metal-containing sludge is ≥ 2.5mg/g VSS; the heavy metals in the heavy metal-containing sludge include cadmium, chromium, copper, lead, and zinc at least one of .
上述的方法,进一步改进的,步骤S1中,所述含重金属污泥中可挥发性悬浮物的初始浓度为29.1g/L。The above method is further improved. In step S1, the initial concentration of volatile suspended matter in the heavy metal-containing sludge is 29.1 g/L.
上述的方法,进一步改进的,步骤S2中,所述厌氧消化过程中控制温度为35℃~37℃;所述厌氧消化的时间为30天~45天。The above method is further improved, in step S2, the temperature is controlled to be 35° C. to 37° C. during the anaerobic digestion process; the time for the anaerobic digestion is 30 days to 45 days.
上述的方法,进一步改进的,包括以下步骤:The above-mentioned method, further improved, comprises the following steps:
S1、将阴离子聚丙烯酰胺与含重金属污泥混合,得到泥水混合物;S1, mixing anionic polyacrylamide with heavy metal-containing sludge to obtain a mud-water mixture;
S2、将步骤S1中得到的泥水混合物进行厌氧消化,完成对含重金属的处理。S2. Perform anaerobic digestion on the mud-water mixture obtained in step S1 to complete the treatment of heavy metals.
上述的方法,进一步改进的,步骤S1中,所述阴离子聚丙烯酰胺以溶液的形式加入到含重金属污泥中;所述阴离子聚丙烯酰胺溶液中阴离子聚丙烯酰胺的质量体积浓度为0.5%。The above method is further improved. In step S1, the anionic polyacrylamide is added to the heavy metal-containing sludge in the form of a solution; the mass volume concentration of the anionic polyacrylamide in the anionic polyacrylamide solution is 0.5%.
上述的方法,进一步改进的,步骤S1中,所述含重金属污泥中重金属的初始浓度≥2.5mg/g VSS;所述含重金属污泥中的重金属包括镉、铬、铜、铅、锌中的至少一种。The above method is further improved, in step S1, the initial concentration of heavy metals in the heavy metal-containing sludge is ≥ 2.5mg/g VSS; the heavy metals in the heavy metal-containing sludge include cadmium, chromium, copper, lead, and zinc at least one of .
上述的方法,进一步改进的,步骤S1中,所述含重金属污泥中可挥发性悬浮物的初始浓度为29.1g/L。The above method is further improved. In step S1, the initial concentration of volatile suspended matter in the heavy metal-containing sludge is 29.1 g/L.
上述的方法,进一步改进的,步骤S2中,所述厌氧消化过程中控制温度为35℃~37℃;所述厌氧消化的时间为30天~45天。The above method is further improved, in step S2, the temperature is controlled to be 35° C. to 37° C. during the anaerobic digestion process; the time for the anaerobic digestion is 30 days to 45 days.
与现有技术相比,本发明的优点在于:Compared with the prior art, the present invention has the advantages of:
(1)本发明提供了一种提升含重金属污泥厌氧消化甲烷产量的方法,首次将阳离子聚丙烯酰胺/阴离子聚丙烯酰胺引入污泥消化系统当中,用于缓解重金属对厌氧消化的不良影响,由此提高厌氧消化过程中的甲烷产量,具体来说,利用阳离子聚丙烯酰胺/阴离子聚丙烯酰胺对重金属的吸附架桥作用、絮凝作用对污泥流动性进行限制,减少重金属和微生物的直接接触,进而减缓重金属对微生物的毒害作用,这有利于提升厌氧消化过程中相关微生物的丰度,并提高厌氧消化系统甲烷的产量。另外,对于阴离子聚丙烯酰胺而言,除对污泥流动性的限制作用外,其还具有用于吸附重金属的静电吸附作用,因而通过上述多种作用方式的协同调控,可以更加有效增加污泥厌氧消化过程中的甲烷产量。相比于常规方法,本发明提升含重金属污泥厌氧消化甲烷产量的方法,具有工艺简单、操作方便、成本低廉、性价比高、效率高等优点,在提升污泥厌氧消化产甲烷方面,有着很高的使用价值和很好的应用前景。(1) The present invention provides a method for improving the methane yield of anaerobic digestion of heavy metal-containing sludge. For the first time, cationic polyacrylamide/anionic polyacrylamide is introduced into the sludge digestion system to alleviate the adverse effects of heavy metals on anaerobic digestion Influence, thereby increasing methane production in the anaerobic digestion process, specifically, using cationic polyacrylamide/anionic polyacrylamide to adsorb and bridging heavy metals, flocculation to limit sludge fluidity, reduce heavy metals and microorganisms The direct contact of heavy metals can slow down the toxic effect of heavy metals on microorganisms, which is beneficial to increase the abundance of related microorganisms in the anaerobic digestion process and increase the methane production of the anaerobic digestion system. In addition, for anionic polyacrylamide, in addition to restricting the fluidity of sludge, it also has an electrostatic adsorption effect for adsorbing heavy metals. Therefore, through the coordinated regulation of the above-mentioned multiple modes of action, sludge can be more effectively increased. Methane production during anaerobic digestion. Compared with the conventional method, the method of the present invention for improving the methane production of anaerobic digestion of heavy metal-containing sludge has the advantages of simple process, convenient operation, low cost, high cost performance, and high efficiency. High use value and good application prospect.
(2)本发明中,通过优化阳离子聚丙烯酰胺和阴离子聚丙烯酰胺的用量,在有效降低重金属毒性的同时,最大限度地保证聚丙烯酰胺本身不会影响厌氧消化系统,从而更加有利于污泥菌胶团的形成和微生物的繁殖扩张,进而更加有效的提升厌氧消化甲烷的产量。(2) In the present invention, by optimizing the dosage of cationic polyacrylamide and anionic polyacrylamide, while effectively reducing the toxicity of heavy metals, it is guaranteed that polyacrylamide itself will not affect the anaerobic digestion system to the greatest extent, thereby more conducive to pollution The formation of slime micelles and the reproduction and expansion of microorganisms can more effectively increase the production of anaerobic digested methane.
(3)本发明中,对阳离子/阴离子聚丙烯酰胺提高含重金属污泥厌氧消化甲烷产量的机制做了相关分析,通过对污泥厌氧消化过程相关步骤的测定分析,发现阳离子聚丙烯酰胺/阴离子聚丙烯酰胺的添加,有效地提升了高镉污泥厌氧消化的溶解、水解和酸化过程,进而有利于增加甲烷的产量。从重金属对微生物的毒性来源角度分析,发现阳离子聚丙烯酰胺/阴离子聚丙烯酰胺的添加,一方面有效地减少了重金属诱导的活性氧物种的产量,使得其对微生物细胞的氧化损伤程度减弱;另一方面使得厌氧消化过程中的关键酶(水解酶、产酸酶和产甲烷酶)活性有所提升,促进了厌氧消化的进程。同时,对厌氧消化过程相关微生物群落的测定分析,表明阳离子聚丙烯酰胺/阴离子聚丙烯酰胺的引入,提升了含重金属污泥厌氧消化过程中相关微生物的丰度。(3) In the present invention, the mechanism of cationic/anionic polyacrylamide improving methane production in anaerobic digestion of sludge containing heavy metals has been analyzed. Through the measurement and analysis of the relevant steps of the sludge anaerobic digestion process, it is found that cationic polyacrylamide The addition of anionic polyacrylamide effectively improves the dissolution, hydrolysis and acidification process of anaerobic digestion of high-cadmium sludge, which in turn is beneficial to increase the production of methane. From the perspective of the toxicity source of heavy metals to microorganisms, it was found that the addition of cationic polyacrylamide/anionic polyacrylamide, on the one hand, effectively reduced the production of active oxygen species induced by heavy metals, and weakened the degree of oxidative damage to microbial cells; On the one hand, the activity of key enzymes (hydrolase, acid-producing enzyme and methanase) in the process of anaerobic digestion has been improved, and the process of anaerobic digestion has been promoted. At the same time, the determination and analysis of the microbial community related to the anaerobic digestion process showed that the introduction of cationic polyacrylamide/anionic polyacrylamide increased the abundance of related microorganisms in the anaerobic digestion process of heavy metal-containing sludge.
具体实施方式Detailed ways
以下结合具体优选的实施例对本发明作进一步描述,但并不因此而限制本发明的保护范围。The present invention will be further described below in conjunction with specific preferred embodiments, but the protection scope of the present invention is not limited thereby.
以下实施例中所采用的原料和仪器均为市售;所采用的设备和制备工艺若无特别说明均为常规设备和常规工艺。The raw materials and instruments used in the following examples are all commercially available; the equipment and preparation processes used are conventional equipment and conventional processes unless otherwise specified.
实施例1Example 1
一种提升含重金属污泥厌氧消化甲烷产量的方法,具体是利用阳离子聚丙烯酰胺提升含镉污泥厌氧消化过程中的甲烷产量,包括以下步骤:A method for increasing methane production in anaerobic digestion of sludge containing heavy metals, specifically using cationic polyacrylamide to increase methane production in anaerobic digestion of sludge containing cadmium, comprising the following steps:
(1)取含镉污泥,该污泥中镉离子的初始浓度为2.5mg/g VSS,即污泥中镉离子与可挥发性悬浮物(VSS)的质量比为0.0025∶1,且该污泥中可挥发性悬浮物(VSS)的初始浓度为29.1g/L。(1) Take cadmium-containing sludge, the initial concentration of cadmium ions in the sludge is 2.5 mg/g VSS, that is, the mass ratio of cadmium ions in the sludge to volatile suspended solids (VSS) is 0.0025:1, and the The initial concentration of volatile suspended solids (VSS) in the sludge was 29.1g/L.
(2)取阳离子聚丙酰胺,配置成阳离子聚丙酰胺溶液,该阳离子聚丙酰胺溶液中阳离子聚丙烯酰胺的浓度为0.5%(w/v),将上述的阳离子聚丙酰胺溶液加入到含镉污泥中,控制阳离子聚丙烯酰胺的含量与污泥的可挥发性悬浮物(VSS)质量比为0.002∶1,混合均匀,得到泥水混合物,该泥水混合物中阳离子聚丙烯酰胺的含量为2mg/g VSS。(2) Get cationic polyacrylamide, configure cationic polyacrylamide solution, the concentration of cationic polyacrylamide in this cationic polyacrylamide solution is 0.5% (w/v), join above-mentioned cationic polyacrylamide solution in the cadmium-containing sludge , control the mass ratio of the content of cationic polyacrylamide to the volatile suspended solids (VSS) of the sludge to be 0.002:1, mix evenly to obtain a mud-water mixture, the content of cationic polyacrylamide in the mud-water mixture is 2mg/g VSS.
(3)往泥水混合物中充入氮气,排除各污泥系统中的氧气,控制污泥系统为厌氧条件,于35℃~37℃下进行厌氧消化,时间为40天。(3) Fill nitrogen into the mud-water mixture, remove oxygen in each sludge system, control the sludge system to anaerobic conditions, and carry out anaerobic digestion at 35°C to 37°C for 40 days.
空白组:对不含有镉离子和阳离子聚丙烯酰胺的污泥进行厌氧消化,其他条件均与实施例1相同。Blank group: Anaerobic digestion was performed on sludge without cadmium ions and cationic polyacrylamide, and other conditions were the same as in Example 1.
对照组:利用等量的水代替阳离子聚丙烯酰胺溶液,其他条件均与实施例1相同。Control group: an equal amount of water was used to replace the cationic polyacrylamide solution, and other conditions were the same as in Example 1.
同时,还考察了阳离子聚丙烯酰胺与污泥中的可挥发性悬浮物(VSS)的质量比分别为0.001∶1、0.004∶1时对厌氧消化甲烷产量的影响,其他条件与实施例1相同。Simultaneously, the mass ratio of cationic polyacrylamide and volatile suspended solids (VSS) in the sludge was also investigated when the mass ratio was 0.001: 1 and 0.004: 1, respectively. same.
经测试,不同泥水混合物甲烷产量如表1所示。After testing, the methane production of different mud-water mixtures is shown in Table 1.
表1不同泥水混合物对应的甲烷产量Table 1 Methane production corresponding to different mud-water mixtures
表1中,甲烷产量为与空白组相比甲烷的相对含量。按照空白组的甲烷产量为100%,则对照组、阳离子聚丙烯酰胺与可挥发性悬浮物VSS的质量比0.001∶1、0.002∶1、0.004∶1时,对应的甲烷产量分别为:68%、79%、90%和83%。由表1可知,与对照组相比,阳离子聚丙烯酰胺的加入有效恢复了甲烷产量,这是因为本发明中通过向高浓度含镉污泥的系统中加入阳离子聚丙烯酰胺,通过利用阳离子聚丙烯酰胺的絮凝作用,减少镉和微生物的直接接触,有效降低了镉对微生物的毒害作用,提升了厌氧消化过程中相关微生物的丰度,促进了厌氧消化系统甲烷的产量。需要注意的是,相比对照组,本发明中,阳离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比为0.001~0.004∶1时,均能提升厌氧消化甲烷产量。特别的,当阳离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比小于0.001∶1时,阳离子聚丙烯酰胺用量过低,其对污泥基本没有絮凝作用,不会限制重金属的流动,不利于提升厌氧消化系统甲烷产量。而阳离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比大于0.004∶1时,絮凝作用过于强烈,污泥絮体过度团聚,不利于污泥的溶解,阻碍厌氧消化的进程;其次,高浓度的阳离子聚丙烯酰胺本身对厌氧微生物具有一定的毒害作用,更不利于甲烷产量的恢复。因此,通过优化阳离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比,更有利于提升厌氧消化甲烷产量。In Table 1, methane production is the relative content of methane compared with the blank group. According to the methane production of the blank group is 100%, then when the mass ratio of the control group, cationic polyacrylamide and volatile suspended matter VSS is 0.001:1, 0.002:1, 0.004:1, the corresponding methane production is respectively: 68% , 79%, 90% and 83%. It can be seen from Table 1 that compared with the control group, the addition of cationic polyacrylamide effectively restored the methane production. This is because in the present invention, by adding cationic polyacrylamide to the system with high concentration The flocculation of acrylamide reduces the direct contact between cadmium and microorganisms, effectively reduces the toxic effect of cadmium on microorganisms, increases the abundance of related microorganisms in the anaerobic digestion process, and promotes the production of methane in the anaerobic digestion system. It should be noted that compared with the control group, in the present invention, when the mass ratio of cationic polyacrylamide to volatile suspended matter in the sludge is 0.001-0.004:1, the anaerobic digestion methane production can be increased. In particular, when the mass ratio of cationic polyacrylamide to volatile suspended matter in the sludge is less than 0.001:1, the amount of cationic polyacrylamide is too low, it has basically no flocculation effect on sludge, and will not restrict the flow of heavy metals , which is not conducive to increasing the methane production of the anaerobic digestion system. However, when the mass ratio of cationic polyacrylamide to volatile suspended matter in the sludge is greater than 0.004:1, the flocculation effect is too strong, and the sludge flocs are excessively agglomerated, which is not conducive to the dissolution of sludge and hinders the process of anaerobic digestion; Secondly, the high concentration of cationic polyacrylamide itself has a certain toxic effect on anaerobic microorganisms, which is not conducive to the recovery of methane production. Therefore, by optimizing the mass ratio of cationic polyacrylamide to volatile suspended matter in sludge, it is more beneficial to increase the methane production of anaerobic digestion.
实施例2:Example 2:
一种提升含重金属污泥厌氧消化甲烷产量的方法,具体是利用阴离子聚丙烯酰胺提升含镉污泥厌氧消化的甲烷产量,包括以下步骤:A method for increasing the methane output of anaerobic digestion of heavy metal-containing sludge, specifically using anionic polyacrylamide to increase the methane output of anaerobic digestion of cadmium-containing sludge, comprising the following steps:
(1)取含镉污泥,该污泥中镉离子的初始浓度为2.5mg/g VSS,即污泥中镉离子与可挥发性悬浮物(VSS)的质量比为0.0025∶1,且该污泥中可挥发性悬浮物(VSS)的初始浓度为29.1g/L。(1) Take cadmium-containing sludge, the initial concentration of cadmium ions in the sludge is 2.5 mg/g VSS, that is, the mass ratio of cadmium ions in the sludge to volatile suspended solids (VSS) is 0.0025:1, and the The initial concentration of volatile suspended solids (VSS) in the sludge was 29.1g/L.
(2)取阴离子聚丙烯酰胺,配置成阴离子聚丙烯酰胺溶液,该阴离子聚丙烯酰胺溶液中阴离子聚丙烯酰胺的浓度为0.5%(w/v),将上述的阴离子聚丙烯酰胺溶液加入到含镉污泥中,控制阴离子聚丙烯酰胺的含量与污泥的可挥发性悬浮物(VSS)质量比为0.0015∶1,混合均匀,得到泥水混合物,该泥水混合物中阴离子聚丙烯酰胺的含量为1.5mg/g VSS。(2) Take anionic polyacrylamide and configure it into an anionic polyacrylamide solution. The concentration of anionic polyacrylamide in this anionic polyacrylamide solution is 0.5% (w/v), and the above-mentioned anionic polyacrylamide solution is added to the solution containing In the cadmium sludge, control the mass ratio of the content of anionic polyacrylamide to the volatile suspended solids (VSS) of the sludge to be 0.0015:1, and mix evenly to obtain a mud-water mixture, the content of anion polyacrylamide in the mud-water mixture is 1.5 mg/g VSS.
(3)往泥水混合物中充入氮气,排除各污泥系统中的氧气,控制污泥系统为厌氧条件,于35℃~37℃下进行厌氧消化,时间为40天。(3) Fill nitrogen into the mud-water mixture, remove oxygen in each sludge system, control the sludge system to anaerobic conditions, and carry out anaerobic digestion at 35°C to 37°C for 40 days.
空白组:对不含有镉离子和阴离子聚丙烯酰胺的污泥进行厌氧消化,其他条件均与实施例2相同。Blank group: Anaerobic digestion was performed on the sludge not containing cadmium ions and anionic polyacrylamide, and other conditions were the same as in Example 2.
对照组:利用等量的水代替阴离子聚丙烯酰胺溶液,其他条件均与实施例2相同。Control group: an equivalent amount of water was used to replace the anionic polyacrylamide solution, and other conditions were the same as in Example 2.
同时,还考察了阴离子聚丙烯酰胺与污泥中的可挥发性悬浮物(VSS)的质量比分别为0.00075∶1、0.003∶1时对厌氧消化甲烷产量的影响,其他条件与实施例2相同。Simultaneously, the mass ratio of the volatile suspended matter (VSS) in the anionic polyacrylamide and the sludge was also investigated when the mass ratio was respectively 0.00075: 1, 0.003: 1. The impact on the output of anaerobic digestion methane, other conditions and embodiment 2 same.
经测试,不同泥水混合物甲烷产量如表2所示。After testing, the methane production of different mud-water mixtures is shown in Table 2.
表2不同泥水混合物对应的甲烷产量Table 2 Methane production corresponding to different mud-water mixtures
表2中,甲烷产量为与空白组相比甲烷的相对含量。当空白组的甲烷产量为100%时,对照组、阴离子聚丙烯酰胺与可挥发性悬浮物VSS的质量比0.00075∶1、0.0015∶1、0.003∶1时,对应的甲烷产量分别为:68%,93%,86%和79%。由表2可知,与对照组相比,阴离子聚丙烯酰胺的加入有效恢复了甲烷产量,这是因为本发明通过向含高镉污泥的系统中加入阴离子聚丙烯酰胺,通过阴离子聚丙烯酰胺的吸附架桥作用、絮凝作用和对镉的静电吸附作用,减少镉和微生物的直接接触,有效降低了镉对微生物的毒害作用,提升了厌氧消化过程中相关微生物的丰度,促进了厌氧消化系统甲烷的产量。需要注意的是,相比对照组,本发明中,阴离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比为0.00075~0.003∶1,均能提升厌氧消化甲烷产量。特别的,当阴离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比小于0.00075∶1时,阴离子聚丙烯酰胺用量过低,其对污泥基本没有絮凝作用,不会限制重金属的流动,不会提升厌氧消化系统甲烷产量;而当阴离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比大于0.003∶1时,絮凝作用过于强烈,污泥絮体过度团聚,不利于污泥的溶解,阻碍厌氧消化的进程;其次,高浓度的阴离子聚丙烯酰胺本身对厌氧微生物具有一定的毒害作用,更不利于甲烷产量的恢复。因此,通过优化阴离子聚丙烯酰胺与污泥中的可挥发性悬浮物的质量比,更有利于提升厌氧消化甲烷产量。此外,相比阳离子聚丙烯酰胺,阴离子聚丙烯酰胺的加入量更小,因而能够在更低成本条件下提高甲烷产量。In Table 2, methane production is the relative content of methane compared with the blank group. When the methane production of the blank group is 100%, when the mass ratios of the control group, anionic polyacrylamide and volatile suspended matter VSS are 0.00075:1, 0.0015:1, and 0.003:1, the corresponding methane production is respectively: 68% , 93%, 86% and 79%. As can be seen from Table 2, compared with the control group, the addition of anionic polyacrylamide effectively restored the methane production, this is because the present invention adds anionic polyacrylamide to the system containing high cadmium sludge, through Adsorption bridging, flocculation and electrostatic adsorption of cadmium reduce the direct contact between cadmium and microorganisms, effectively reduce the toxicity of cadmium to microorganisms, increase the abundance of related microorganisms in the anaerobic digestion process, and promote anaerobic digestion. Digestive system methane production. It should be noted that, compared with the control group, in the present invention, the mass ratio of anionic polyacrylamide to volatile suspended matter in the sludge is 0.00075-0.003:1, both of which can increase the methane production of anaerobic digestion. In particular, when the mass ratio of anionic polyacrylamide to volatile suspended matter in sludge is less than 0.00075:1, the amount of anionic polyacrylamide is too low, and it has basically no flocculation effect on sludge and will not restrict the flow of heavy metals , will not increase the methane production of the anaerobic digestion system; and when the mass ratio of anionic polyacrylamide to volatile suspended matter in the sludge is greater than 0.003:1, the flocculation is too strong, and the sludge flocs are excessively agglomerated, which is not conducive to The dissolution of sludge hinders the process of anaerobic digestion; secondly, the high concentration of anionic polyacrylamide itself has a certain toxic effect on anaerobic microorganisms, which is not conducive to the recovery of methane production. Therefore, by optimizing the mass ratio of anionic polyacrylamide to volatile suspended matter in sludge, it is more conducive to improving the methane production of anaerobic digestion. In addition, compared with cationic polyacrylamide, the addition amount of anionic polyacrylamide is smaller, so methane production can be increased at a lower cost.
综上可知,本发明提升含重金属污泥厌氧消化甲烷产量的方法,首次将阳离子聚丙烯酰胺/阴离子聚丙烯酰胺引入污泥消化系统当中,用于缓解重金属对厌氧消化的不良影响,由此提高厌氧消化过程中的甲烷产量,具体来说,利用阳离子聚丙烯酰胺/阴离子聚丙烯酰胺对重金属的吸附架桥作用、絮凝作用对污泥流动性进行限制,减少重金属和微生物的直接接触,进而减缓重金属对微生物的毒害作用,这有利于提升厌氧消化过程中相关微生物的丰度,并提高厌氧消化系统甲烷的产量。另外,对于阴离子聚丙烯酰胺而言,除对污泥流动性的限制作用外,其还具有用于重金属的静电吸附作用,因而通过上述多种作用方式的协同调控,可以更加有效增加污泥厌氧消化过程中的甲烷产量。相比于常规方法,本发明提升含重金属污泥厌氧消化甲烷产量的方法,具有工艺简单、操作方便、成本低廉、性价比高、效率较高等优点,在提升污泥厌氧消化产甲烷方面,有着很高的使用价值和很好的应用前景。In conclusion, the present invention improves the methane yield of anaerobic digestion of sludge containing heavy metals. For the first time, cationic polyacrylamide/anionic polyacrylamide is introduced into the sludge digestion system to alleviate the adverse effects of heavy metals on anaerobic digestion. This improves the methane production in the anaerobic digestion process. Specifically, the use of cationic polyacrylamide/anionic polyacrylamide to adsorb and bridge heavy metals, and flocculation to limit the fluidity of sludge and reduce direct contact between heavy metals and microorganisms , and then slow down the toxic effect of heavy metals on microorganisms, which is conducive to increasing the abundance of related microorganisms in the anaerobic digestion process and increasing the methane production of the anaerobic digestion system. In addition, for anionic polyacrylamide, in addition to restricting the fluidity of sludge, it also has an electrostatic adsorption effect on heavy metals. Therefore, through the coordinated regulation of the above-mentioned multiple modes of action, it can more effectively increase sludge repellency. Methane production during oxygen digestion. Compared with the conventional method, the method of the present invention for improving the methane production of anaerobic digestion of heavy metal-containing sludge has the advantages of simple process, convenient operation, low cost, high cost performance, and high efficiency. It has high use value and good application prospect.
以上实施例仅是本发明的优选实施方式,本发明的保护范围并不仅局限于上述实施例。凡属于本发明思路下的技术方案均属于本发明的保护范围。应该指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下的改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above examples are only preferred implementations of the present invention, and the scope of protection of the present invention is not limited to the above examples. All technical solutions under the idea of the present invention belong to the protection scope of the present invention. It should be pointed out that for those skilled in the art, improvements and modifications without departing from the principle of the present invention should also be regarded as the protection scope of the present invention.
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