[go: up one dir, main page]

CN205436606U - Reaction bed of microbiological treatment oiliness waste residue - Google Patents

Reaction bed of microbiological treatment oiliness waste residue Download PDF

Info

Publication number
CN205436606U
CN205436606U CN201620231998.0U CN201620231998U CN205436606U CN 205436606 U CN205436606 U CN 205436606U CN 201620231998 U CN201620231998 U CN 201620231998U CN 205436606 U CN205436606 U CN 205436606U
Authority
CN
China
Prior art keywords
waste residue
reaction bed
oily waste
microbial
aeration
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.)
Expired - Fee Related
Application number
CN201620231998.0U
Other languages
Chinese (zh)
Inventor
卞卫国
张洁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Karamay Zhongke Oilfield Services New Tech Co ltd
Xinjiang Institute of Ecology and Geography of CAS
Original Assignee
Karamay Zhongke Oilfield Services New Tech Co ltd
Xinjiang Institute of Ecology and Geography of CAS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Karamay Zhongke Oilfield Services New Tech Co ltd, Xinjiang Institute of Ecology and Geography of CAS filed Critical Karamay Zhongke Oilfield Services New Tech Co ltd
Priority to CN201620231998.0U priority Critical patent/CN205436606U/en
Application granted granted Critical
Publication of CN205436606U publication Critical patent/CN205436606U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

本实用新型涉及一种微生物处理含油废渣的反应床,该反应床是由电动卷帘、喷头、给水管、含油废渣、曝气头、曝气支管、曝气干管、集滤液管、固定座组成,该反应床结合了微生物修复技术中的堆肥法、预制床法和生物反应器法的优点,能够通过供气系统调节反应槽中的含氧量,通过供水系统调节反应槽中的含水率、pH、营养物等,保温和遮阳系统调节反应器内的温度,为微生物在反应床内的生长繁殖提供了良好的生长环境,大大提高微生物降解石油烃类污染物的效率。本实用新型与现有土耕法、堆肥法和预制床法相比效率更高,与生物反应器相比,有可以大规模处理含油废渣的优势。解决了现有在实际应用中的微生物适应性较差、微生物活性低、处理效率低、处理效果不彻底等问题。

The utility model relates to a reaction bed for microbial treatment of oily waste residue. The reaction bed is composed of an electric roller shutter, a nozzle, a water supply pipe, an oily waste residue, an aeration head, an aeration branch pipe, an aeration main pipe, a filtrate collection pipe, and a fixing seat. Composition, the reaction bed combines the advantages of composting method, prefabricated bed method and bioreactor method in microbial remediation technology, and can adjust the oxygen content in the reaction tank through the air supply system, and adjust the water content in the reaction tank through the water supply system , pH, nutrients, etc., the heat preservation and shading system regulates the temperature in the reactor, which provides a good growth environment for the growth and reproduction of microorganisms in the reaction bed, and greatly improves the efficiency of microorganisms in degrading petroleum hydrocarbon pollutants. Compared with the existing soil tillage method, composting method and prefabricated bed method, the utility model has higher efficiency, and compared with the bioreactor, the utility model has the advantage of large-scale treatment of oily waste residue. The present invention solves the existing problems of poor microbial adaptability, low microbial activity, low treatment efficiency, and incomplete treatment effect in practical applications.

Description

一种微生物处理含油废渣的反应床A reaction bed for microbial treatment of oily waste residue

技术领域technical field

本实用新型涉及一种微生物处理含油废渣的反应床。The utility model relates to a reaction bed for microbial treatment of oily waste residue.

背景技术Background technique

目前涉及微生物修复技术有:Currently involved in microbial remediation technologies are:

(1)原位生物修复技术(1) In situ bioremediation technology

微生物原位修复技术即向污染的土壤直接投放化学物质,如:N、P等营养物质或供养,促进微生物的生长、繁殖或接种经驯化培养的高效微生物等,利用微生物的代谢来达到分解石油烃的目的。原位处理方法是将受污染土壤在原地处理,处理期间土壤基本不需移动。由于这项技术不需要挖掘污染土壤,因此是一种比较经济的修复手段。此法包括:投菌法、生物培养法、生物通气法、土耕法、生物堆放。Microbial in-situ remediation technology is to directly put chemical substances into the polluted soil, such as: N, P and other nutrients or support, to promote the growth and reproduction of microorganisms, or to inoculate highly efficient microorganisms that have been domesticated and cultivated, and to use the metabolism of microorganisms to decompose oil. purpose of hydrocarbons. The in-situ treatment method is to treat the contaminated soil in situ, and the soil basically does not need to be moved during the treatment. Since this technique does not require excavation of contaminated soil, it is a relatively economical means of remediation. This method includes: bacterial injection method, biological culture method, biological aeration method, soil tillage method, and biological stacking.

①投菌法① Bacteria injection method

直接向污染的土壤接入污染降解菌,同时提供这些降解菌生长、繁殖所必须的N、P等营养元素和微量元素。Directly insert pollution-degrading bacteria into the polluted soil, and at the same time provide the nutrients and trace elements such as N and P necessary for the growth and reproduction of these degrading bacteria.

②生物培养法②Biological culture method

定期地向污染土壤中投加营养物质和双氧水,并且供氧。双氧水在微生物代谢过程中作为电子受体,将污染物彻底氧化为CO2和水。Regularly add nutrients and hydrogen peroxide to the polluted soil, and supply oxygen. Hydrogen peroxide acts as an electron acceptor in the process of microbial metabolism, completely oxidizing pollutants into CO2 and water.

③生物通气法③ Biological ventilation method

生物通气法是一种强迫氧化的生物降解方法,在污染土壤区域上打至少两口井,并且安装鼓风机和抽气机,将空气强制鼓入土壤中,然后抽走,土壤中挥发性和半挥发性的有毒物质将随之出去。此方法只适合有多孔的土壤结构。The biological aeration method is a biodegradation method of forced oxidation. At least two wells are drilled in the contaminated soil area, and blowers and air extractors are installed to force the air into the soil and then pump it away. Volatile and semi-volatile in the soil Sexual toxic substances will go out with it. This method is only suitable for porous soil structures.

④土耕法④ Soil tillage

土耕法是把污染土壤盖在土地上,然后对土壤进行耕耙处理,使污染土壤充分与降解微生物混合,利用土壤中微生物将污染物彻底分解。The soil tillage method is to cover the polluted soil on the land, and then plow the soil to make the polluted soil fully mix with the degrading microorganisms, and use the microorganisms in the soil to completely decompose the pollutants.

⑤生物堆法⑤ biopile method

生物堆法是土耕法的一种改进形式,生物堆放通常包括一个打了孔的暗渠用来收集沥出物和回收生物堆中的空气。在暗渠的一端连接一个真空泵,向生物堆鼓气,以促进微生物的生长。生物堆还包括一个喷灌和滴灌系统,来调节湿度,为微生物的生长提供一个良好的环境,以便提高处理效率。A modified form of soil farming, biopiles usually include a perforated underdrain to collect leachate and recycle the air in the biopiles. Attached to one end of the underdrain is a vacuum pump that blows air into the biopile to encourage microbial growth. The biopile also includes a sprinkler and drip irrigation system to regulate the humidity and provide a good environment for the growth of microorganisms in order to improve the treatment efficiency.

(2)微生物异位修复技术(2) Microbial ectopic repair technology

异位生物修复是将石油污染的土壤移到别的地点或生物反应器内再进行修复。异位修复通常具有可以节省修复时间、修复效果易控制等优点。但投资成本较原位修复大。异位生物修复包括:土地耕作法、预制床法、堆置处理法、生物反应器和厌氧生物处理法。Ex situ bioremediation is to move oil-contaminated soil to another site or bioreactor for remediation. Heterotopic repair usually has the advantages of saving repair time and easy control of the repair effect. But the investment cost is larger than in-situ restoration. Ex situ bioremediation includes: land cultivation method, prefabricated bed method, stacking treatment method, bioreactor and anaerobic biological treatment method.

①堆置处理法即堆肥法(Composting)总体上堆置处理法可分为4种堆制方法,即堤形堆肥法、静态堆肥法、封闭堆肥法和容器堆肥法。堆肥法是在污染土壤中加入土壤调理剂以提供促进微生物生长和石油生物降解的营养元素,使天然微生物降解石油烃类,从而达到生物修复的目的。这个过程对去除高浓度石油类污染物是最有效的。加入的物质或调理剂可以是干草、刈割草、树叶、木屑、麦秆、锯屑或肥料。加入土壤调理剂的目的是为了提高土壤的渗透性、增加氧的传输、改善土壤质地以及为快速建立一个大的微生物种群提供能源。① Composting method, that is, composting method (Composting) Generally, the composting method can be divided into four composting methods, namely embankment composting method, static composting method, closed composting method and container composting method. The composting method is to add soil conditioner to the contaminated soil to provide nutrients that promote microbial growth and petroleum biodegradation, so that natural microorganisms can degrade petroleum hydrocarbons, thereby achieving the purpose of bioremediation. This process is most effective for removing high concentrations of petroleum-based contaminants. The added substance or conditioner may be hay, mowed grass, leaves, wood chips, straw, sawdust or manure. The purpose of adding soil conditioners is to increase soil permeability, increase oxygen transport, improve soil texture, and provide energy for the rapid establishment of a large microbial population.

②预制床法(Preparedbedbioremediation)预制床具有滤液收集和控制排放系统,底面为渗透性低的物质,如高密度的聚乙烯、黏土或混凝土。将含油污泥转移到预制床上,通过施肥、灌溉、调节pH,有时还加入微生物和表面活性剂,使其最适合污染物的降解。与同一区域的原位处理技术相比,预制床处理对3环和3环以上的多环芳烃的降解率明显提高。②Prefabricated bed method (Preparedbed bioremediation) The prefabricated bed has a filtrate collection and control discharge system, and the bottom surface is a material with low permeability, such as high-density polyethylene, clay or concrete. The oily sludge is transferred to a prefabricated bed that is optimally suited for the degradation of the pollutants by fertilization, irrigation, pH adjustment, and sometimes addition of microorganisms and surfactants. Compared with the in-situ treatment technology in the same area, the degradation rate of PAHs with 3 rings and more than 3 rings was significantly improved by the prefabricated bed treatment.

③生物反应器法(Slurry-phasebioremediation)也称泥浆法,是将污染土壤置于一专门的反应器中处理的方法。生物反应器处理的过程为:将挖出的石油污染土壤移到反应器内,加水混合,使其呈泥浆状,同时加入适量的营养物质、表面活性剂,并鼓入空气、剧烈搅拌使微生物与污染物充分接触和增加氧气浓度。为了提高降解速率,常在反应器先前处理的土壤中分离出已被驯化的微生物,加入到准备处理的土壤中。含油土壤经处理后,液体部分可排入处置井(坑、池)或另作他用(如回用),固体部分可施用于农田。生物反应器法也可用于石油工业废弃物的预处理,以减少烃类含量,然后进行其他处理。处理后的土壤与水分离后,经脱水处理再运回原地。处理后的出水视视水质情况,直接排放或送入污水处理厂继续处理。反应装置不仅包括各种可以拖动的小型反应器,也可以是经过防渗处理的池塘。③ Bioreactor method (Slurry-phase bioremediation), also known as mud method, is a method of placing contaminated soil in a special reactor for treatment. The process of bioreactor treatment is as follows: move the excavated oil-contaminated soil into the reactor, add water to mix it to make it muddy, and at the same time add appropriate amount of nutrients and surfactants, blow in air, and vigorously stir to make the microorganisms Adequate contact with pollutants and increased oxygen concentration. In order to increase the degradation rate, domesticated microorganisms are often isolated from the previously treated soil in the reactor and added to the soil to be treated. After the oily soil is treated, the liquid part can be discharged into the disposal well (pit, pond) or used for other purposes (such as reuse), and the solid part can be applied to the farmland. The bioreactor method can also be used in the pretreatment of petroleum industry wastes to reduce the hydrocarbon content, followed by other treatments. After the treated soil is separated from the water, it is dehydrated and transported back to the original site. The treated effluent will be discharged directly or sent to the sewage treatment plant for further treatment depending on the water quality. The reaction device not only includes various small reactors that can be dragged, but also a pond that has been treated with anti-seepage.

3.影响微生物处理技术的因素3. Factors affecting microbial treatment technology

在所有的微生物处理方法和技术中,关键是解决影响微生物降解石油类和有机物的环境因素,其影响因素见下表。通过设施设备的科学设计,调整好微生物生长环境是提高生物修复效率的关键。Among all microbial treatment methods and technologies, the key is to solve the environmental factors that affect microbial degradation of petroleum and organic matter. The influencing factors are shown in the table below. Through the scientific design of facilities and equipment, adjusting the microbial growth environment is the key to improving the efficiency of bioremediation.

土壤微生物降解环境因素Soil microorganisms degrade environmental factors

(1)含氧量控制(1) Oxygen content control

在自然环境中,大多数的石油烃类物质是在好氧的条件下被降解的,这是因为许多烃类物质的降解过程实质上是烃类物质的氧化过程,需要有加氧酶和分子氧的参与,因此环境中的氧气对微生物而言是一个及其重要的限制因子。氧气的含量决定微生物群落的结构,在缺氧或无氧的条件下,是以厌氧微生物为主的群落结构,而在好氧条件下,则是好氧微生物为主的群落结构。厌氧降解速率比好氧降解的速率慢。In the natural environment, most petroleum hydrocarbons are degraded under aerobic conditions, because the degradation process of many hydrocarbons is essentially the oxidation process of hydrocarbons, which requires oxygenase and molecular The participation of oxygen, so the oxygen in the environment is an extremely important limiting factor for microorganisms. The content of oxygen determines the structure of the microbial community. Under anoxic or anaerobic conditions, the community structure is dominated by anaerobic microorganisms, while under aerobic conditions, the community structure is dominated by aerobic microorganisms. The rate of anaerobic degradation is slower than that of aerobic degradation.

(2)温度控制(2) Temperature control

温度是影响微生物生长、繁殖和新陈代谢的一个重要因素。微生物对石油烃的降解借助于酶的催化作用,而酶的活性只有在一定的温度范围内才能得以发挥。温度过低会使酶活性受到抑制,细胞和新陈代谢活动减弱。温度上升,使微生物的酶活性加强,细胞生长速率加快。但是超过最适宜温度后,一方面,酶的活性下降,甚至有的酶失活,另一方面,培养液中溶解氧浓度降低也会导致生长速率减慢。每种微生物只能在一定的范围内生长,并有其生长、繁殖最快的最适生长温度。因此,选择合适的温度对微生物的生长繁殖及其污染物的降解能力的提高至关重要。Temperature is an important factor affecting the growth, reproduction and metabolism of microorganisms. The degradation of petroleum hydrocarbons by microorganisms relies on the catalysis of enzymes, and the activity of enzymes can only be exerted within a certain temperature range. If the temperature is too low, the activity of enzymes will be inhibited, and the activity of cells and metabolism will be weakened. As the temperature rises, the enzyme activity of microorganisms is strengthened, and the cell growth rate is accelerated. However, when the optimum temperature is exceeded, on the one hand, the activity of enzymes decreases, and some enzymes are even inactivated; Each microorganism can only grow within a certain range, and has the optimum growth temperature for its fastest growth and reproduction. Therefore, choosing an appropriate temperature is crucial to the growth and reproduction of microorganisms and the improvement of the degradation ability of pollutants.

(3)含水率控制(3) Moisture content control

土壤中含水量过低,微生物得不到充分的水分供应,细胞活性受到抑制,代谢速率降低;水分过高,有效毛细空隙空间被水分充满,妨碍空气的流通和氧的供应。土壤中含水率为30%~90%时,微生物对石油烃了有机物的降解率较高。If the water content in the soil is too low, microorganisms cannot get sufficient water supply, the cell activity is inhibited, and the metabolic rate is reduced; if the water content is too high, the effective capillary space is filled with water, which hinders the circulation of air and the supply of oxygen. When the water content in the soil is 30% to 90%, the degradation rate of microorganisms to petroleum hydrocarbons and organic matter is relatively high.

(4)酸碱度调节(4) pH adjustment

土壤中pH值变化范围大,为2.5~11.0,大多数异氧菌和真菌洗好中性范围的环境,pH值对微生物生长的影响主要是影响细胞内的酶活性,甚至可以影响到DNA、RNA、ATP的稳定性与合成,pH值太高或太低都会影响微生物的降解能力,所以在实际工程运用当中,为了给微生物提供良好的生长环境,提高微生物对石油烃类物质的降解效率,需要向废渣添加pH缓冲剂,调节微生物PAH降解最适值为7.5~7.8。处理过程根据pH值变化,需要适当调节土壤pH。The pH value in the soil varies widely, ranging from 2.5 to 11.0. Most heterotrophic bacteria and fungi are in a neutral environment. The effect of pH on the growth of microorganisms is mainly to affect the enzyme activity in the cell, and can even affect DNA, The stability and synthesis of RNA and ATP, if the pH value is too high or too low will affect the degradation ability of microorganisms, so in practical engineering applications, in order to provide a good growth environment for microorganisms and improve the degradation efficiency of microorganisms on petroleum hydrocarbons, It is necessary to add a pH buffer to the waste residue to adjust the optimal value of microbial PAH degradation to 7.5-7.8. The treatment process varies according to the pH value, and the soil pH needs to be adjusted properly.

(5)营养液、肥料(5) Nutrient solution, fertilizer

在油污土壤中,氮源和磷源经常成为微生物降解石油烃类物质的限制因子。因为在石油烃类物质中含有大量的碳和氢,则氮和磷元素是影响细菌生长繁殖的主要因素,石油中碳完全转化是所需要的N、P量可以根据细胞质材料中C:N:P比例计算,土壤中C:N:P比例达不到细菌代谢所需的比例,则会限制细菌的代谢速度,从而制约油泥污染的降解。In oily soils, nitrogen and phosphorus sources often become limiting factors for microbial degradation of petroleum hydrocarbons. Because petroleum hydrocarbons contain a large amount of carbon and hydrogen, nitrogen and phosphorus elements are the main factors that affect the growth and reproduction of bacteria. The complete conversion of carbon in petroleum is the required N and P amounts. According to the C:N: Calculating the P ratio, if the C:N:P ratio in the soil does not reach the ratio required for bacterial metabolism, it will limit the metabolic rate of bacteria, thereby restricting the degradation of sludge pollution.

发明内容Contents of the invention

本实用新型目的在于,针对现有影响微生物处理技术的相关因素,提供一种微生物处理含油废渣的反应床,该反应床是由反应槽、遮阳帘、喷头、给水管、含油废渣、曝气头、曝气支管、曝气干管、集滤液管、固定座组成,该反应床结合了微生物修复技术中的堆肥法、预制床法和生物反应器法的优点,能够通过供气系统调节反应槽中的含氧量,通过供水系统调节反应槽中的含水率、pH、营养物等,保温和遮阳系统调节反应器内的温度,为微生物在反应床内的生长繁殖提供了良好的生长环境,大大提高微生物降解石油烃类污染物的效率。本实用新型与现有土耕法、堆肥法和预制床法相比效率更高,与生物反应器相比,可以大规模处理含油废渣的优势。The purpose of the utility model is to provide a reaction bed for microbial treatment of oily waste residues in view of the relevant factors affecting the existing microbial treatment technology. , aeration branch pipe, aeration main pipe, filtrate collection pipe, and fixed seat. The reaction bed combines the advantages of composting method, prefabricated bed method and bioreactor method in microbial remediation technology, and can adjust the reaction tank through the gas supply system. The oxygen content in the reaction tank is adjusted through the water supply system to adjust the water content, pH, nutrients, etc. in the reaction tank, and the heat preservation and shading system adjusts the temperature in the reactor to provide a good growth environment for the growth and reproduction of microorganisms in the reaction bed. Greatly improve the efficiency of microbial degradation of petroleum hydrocarbon pollutants. Compared with the existing soil tillage method, composting method and prefabricated bed method, the utility model has higher efficiency, and compared with the bioreactor, the utility model has the advantage of large-scale treatment of oily waste residue.

本实用新型所述的一种微生物处理含油废渣的反应床,该反应床是由反应槽、遮阳帘、喷头、给水管、含油废渣、曝气头、曝气支管、曝气干管、集滤液管、固定座组成,在反应床两端的固定座(9)上分别固定遮阳帘(1)、喷头(2)和给水管(3),在反应床中部为反应槽(10),在反应槽(10)的底部分别固定曝气干管(7)和集滤液管(8),在曝气干管(7)上连接曝气支管(6),在曝气支管(6)上设有曝气头(5)。The utility model relates to a reaction bed for microbial treatment of oily waste residue. The reaction bed is composed of a reaction tank, a sunshade curtain, a nozzle, a water supply pipe, an oily waste residue, an aeration head, an aeration branch pipe, an aeration dry pipe, and a filtrate collector. tube and fixing seat, the sunshade curtain (1), nozzle (2) and water supply pipe (3) are respectively fixed on the fixing seats (9) at both ends of the reaction bed, and the reaction tank (10) is in the middle of the reaction bed. The bottom of (10) fixes the main aeration pipe (7) and the filtrate collection pipe (8) respectively, connects the branch aeration pipe (6) on the main aeration pipe (7), and is provided with an aeration pipe (6) on the branch aeration pipe (6). Angry head (5).

在反应槽(10)内堆放含油废渣(4)。The oily waste residue (4) is piled up in the reaction tank (10).

该反应床为混凝土预制结构。The reaction bed is a prefabricated concrete structure.

本实用新型所述的一种微生物处理含油废渣的反应床,该反应床中所述的微生物菌种可以是各种高效降解石油烃类的微生物菌种。MicrobeLiftIND和MicrobeLiftHydro是从美国生态实验室公司购买的可高效降解石油烃类物质的微生物菌种,购买时间2015年3月。The utility model relates to a reaction bed for microbial treatment of oily waste residues. The microbial strains in the reaction bed can be various microbial strains that efficiently degrade petroleum hydrocarbons. MicrobeLiftIND and MicrobeLiftHydro are microbial strains that can efficiently degrade petroleum hydrocarbons purchased from American Ecolabs in March 2015.

本实用新型所述的一种微生物处理含油废渣的反应床,该反应床能够通过曝气管调节含油废渣中的含氧量,通过给水管调节反应床内的含水率、pH值、营养物含量等,能够通过遮阳帘调节反应槽内温度等,为微生物在反应床内的生长繁殖提供了良好的生长环境,大大提高微生物降解石油烃类污染物的效率。The utility model relates to a reaction bed for microbial treatment of oily waste residue. The reaction bed can adjust the oxygen content in the oily waste residue through the aeration pipe, and adjust the water content, pH value and nutrient content in the reaction bed through the water supply pipe. etc., the temperature in the reaction tank can be adjusted through the sunshade curtain, which provides a good growth environment for the growth and reproduction of microorganisms in the reaction bed, and greatly improves the efficiency of microorganisms in degrading petroleum hydrocarbon pollutants.

附图说明Description of drawings

图1为本实用新型结构示意图。Fig. 1 is the structural representation of the utility model.

具体实施方式detailed description

以下结合附图进一步描述并给出实施例。Embodiments are further described and given below in conjunction with the accompanying drawings.

含油废渣取自吐哈油田温米南山废渣场,废渣成分多为落地原油、罐底油泥等。The oily waste residue was taken from the Wenmi Nanshan waste residue yard in Tuha Oilfield, and the waste residue components were mostly ground crude oil, tank bottom sludge, etc.

本实用新型所述的一种微生物处理含油废渣的反应床,该反应床是由反应槽、遮阳帘、喷头、给水管、含油废渣、曝气头、曝气支管、曝气干管、集滤液管、固定座组成,在反应床两端的固定座9上分别固定遮阳帘1、喷头2和给水管3,每2m布置一个喷头2,在反应床两端的固定座9上分别固定遮阳帘1、喷头2和给水管3,在反应床的中部为反应槽10,在反应槽10的底部分别固定曝气干管7和集滤液管8,在曝气干管7上连接曝气支管6,在曝气支管6上设有曝气头5;在反应槽10内堆放含油废渣4;该反应床为混凝土预制结构,反应床一次性规模为250×2.4×0.3×100=18000m3,每个反应槽10长250m,宽2.4m,深度为0.4m,含油废渣堆放深度为0.3m,反应槽共100具平行并联布置;The utility model relates to a reaction bed for microbial treatment of oily waste residue, which is composed of a reaction tank, a sunshade curtain, a nozzle, a water supply pipe, an oily waste residue, an aeration head, an aeration branch pipe, an aeration main pipe, and a filtrate collection The sunshade curtain 1, the nozzle 2 and the water supply pipe 3 are respectively fixed on the fixing seats 9 at both ends of the reaction bed, and a nozzle 2 is arranged every 2m, and the sunshade curtain 1 and 1 are respectively fixed on the fixing seats 9 at both ends of the reaction bed. Nozzle 2 and water supply pipe 3 are reaction tank 10 in the middle of the reaction bed, fixed aeration main pipe 7 and filtrate collection pipe 8 at the bottom of reaction tank 10 respectively, connected aeration branch pipe 6 on aeration main pipe 7, and An aeration head 5 is provided on the aeration branch pipe 6; oily waste residue 4 is piled up in the reaction tank 10; The tank 10 is 250m long, 2.4m wide, and 0.4m deep, and the oily waste residue is stacked at a depth of 0.3m. A total of 100 reaction tanks are arranged in parallel;

在使用时,将含油废渣4使用铲车送入反应床中部的反应槽10内,平铺厚度30cm,通过给水3和喷头2先将水喷洒到反应槽内,使含油废渣4含水率达到30%,再将微生物菌种MicrobeLiftIND和MicrobeLiftHydro喷洒在含油废渣4上,每次每平米投加量为30gMicrobeLiftHydro+140mLMicrobeLiftIND,每6天投加一次,处理周期为2-4个月,在每次喷洒完微生物菌种后,使用拖拉机翻耕,使微生物菌种与含油废渣充分混合,并由此改善了含油废渣内部的空气含量,然后使用给水管3每三天向反应槽10内部喷水,补充反应槽10内部的含水率,补充水后使用拖拉机翻耕;每过9天检测预处理含油废渣4中的C、N、P含量,最适宜微生物的C:N:P为100:10:1,在反应床旁配有压差式施肥罐,当含油废渣4中营养物质不足时,将营养物质为尿素、磷酸二氢钾投加到施肥罐中,由水压带进喷灌系统,向含油废渣4中投加;为了给含油废渣4提供充足的氧气,每天打开反应槽10底部的曝气干管7,通过曝气干管7上曝气支管6和曝气头5定期曝气充氧2小时;由于本反应床建设在室外,在夏季时,室外温度较高,将遮阳帘1打开,覆盖在反应槽10上,避免阳光直射,防止反应槽10内温度过高,影响微生物活性,同时也可以减小水分蒸发;当温度过高时,适当喷水降温;当室外温度低时,打开遮阳帘1,覆盖在反应槽10上,可以保温,微生物菌种生长适宜温度为30℃-45℃;酸碱度调节:根据微生物菌种的生长特性,含油废渣4的酸碱性对微生物菌种活性同样有很大的影响,特别是当含油废渣4的pH值呈酸性时,需要向反应槽10内撒生石灰,或通过给水管3和喷头2喷洒碱液,而含油废渣呈碱性时,通过给水管3喷洒酸性缓冲剂,喷洒完后需使用拖拉机翻耕,处理过程根据pH值变化,适当调节土壤pH。When in use, use a forklift to send the oily waste residue 4 into the reaction tank 10 in the middle of the reaction bed, spread it with a thickness of 30cm, and spray water into the reaction tank through the water supply 3 and the nozzle 2, so that the water content of the oily waste residue 4 reaches 30 %, and then spray the microbial strains MicrobeLiftIND and MicrobeLiftHydro on the oily waste residue 4, the dosage per square meter is 30gMicrobeLiftHydro+140mLMicrobeLiftIND, once every 6 days, the treatment cycle is 2-4 months, after each spraying After microbial strains, use a tractor to plow to fully mix the microbial strains with the oily waste residue, thereby improving the air content inside the oily waste residue, and then use the water supply pipe 3 to spray water into the reaction tank 10 every three days to supplement the reaction. The water content inside the tank 10 is plowed with a tractor after replenishing water; the C, N, and P contents in the pretreated oily waste residue 4 are detected every 9 days, and the most suitable C:N:P for microorganisms is 100:10:1. A pressure differential fertilization tank is equipped next to the reaction bed. When the nutrients in the oily waste residue 4 are insufficient, the nutrients such as urea and potassium dihydrogen phosphate are added to the fertilization tank, and are brought into the sprinkler irrigation system by water pressure to feed the oily waste residue. Add in 4; in order to provide sufficient oxygen for the oily waste residue 4, open the aeration main pipe 7 at the bottom of the reaction tank 10 every day, and regularly aerate and oxygenate through the aeration main pipe 7 on the aeration branch pipe 6 and the aeration head 5 hours; because this reaction bed is built outdoors, in summer, the outdoor temperature is higher, the sunshade curtain 1 is opened, covers on the reaction tank 10, avoids direct sunlight, prevents that the temperature in the reaction tank 10 is too high, affects microbial activity, simultaneously It can also reduce water evaporation; when the temperature is too high, spray water appropriately to cool down; when the outdoor temperature is low, open the sunshade 1 and cover it on the reaction tank 10 to keep warm, and the suitable temperature for the growth of microorganisms is 30°C-45°C ℃; pH adjustment: According to the growth characteristics of the microbial strains, the acidity and alkalinity of the oily waste residue 4 also has a great influence on the activity of the microbial strains, especially when the pH value of the oily waste residue 4 is acidic, it needs to be added to the reaction tank 10 Sprinkle quicklime inside, or spray lye through water supply pipe 3 and nozzle 2, and when the oily waste residue is alkaline, spray acid buffer through water supply pipe 3, and use a tractor to plow after spraying. The treatment process depends on the change of pH value. Regulates soil pH.

Claims (3)

1. the reaction bed of a microbial treatments oily waste residue, it is characterized in that this reaction bed is by reactive tank, abat vent, shower nozzle, feed pipe, oily waste residue, aeration head, aeration branch pipe, aeration main, collection filtrate pipe, fixing seat composition, the upper fixed shading curtain (1) respectively of fixing seat (9) at reaction bed two ends, shower nozzle (2) and feed pipe (3), it it is reactive tank (10) in the middle part of reaction bed, at the bottom of reactive tank (10) difference immobilized film main (7) and collection filtrate pipe (8), aeration main (7) connects aeration branch pipe (6), aeration branch pipe (6) is provided with aeration head (5).
The reaction bed of microbial treatments oily waste residue the most according to claim 1, it is characterised in that stack oily waste residue (4) in reactive tank (10).
The reaction bed of microbial treatments oily waste residue the most according to claim 1, it is characterised in that this reaction bed is concrete prefabricated structure.
CN201620231998.0U 2016-03-24 2016-03-24 Reaction bed of microbiological treatment oiliness waste residue Expired - Fee Related CN205436606U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620231998.0U CN205436606U (en) 2016-03-24 2016-03-24 Reaction bed of microbiological treatment oiliness waste residue

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620231998.0U CN205436606U (en) 2016-03-24 2016-03-24 Reaction bed of microbiological treatment oiliness waste residue

Publications (1)

Publication Number Publication Date
CN205436606U true CN205436606U (en) 2016-08-10

Family

ID=56574976

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620231998.0U Expired - Fee Related CN205436606U (en) 2016-03-24 2016-03-24 Reaction bed of microbiological treatment oiliness waste residue

Country Status (1)

Country Link
CN (1) CN205436606U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107803400A (en) * 2017-10-31 2018-03-16 中国环境科学研究院 The compost method of petroleum hydrocarbon contaminated soil is repaired using biogas slurry
CN109365523A (en) * 2018-12-10 2019-02-22 北京博诚立新环境科技股份有限公司 A kind of bioreactor and its application method for contaminated soil remediation
CN110627227A (en) * 2019-11-04 2019-12-31 蒋俊连 High-temperature self-protection type microorganism treatment pool
CN114472503A (en) * 2020-11-13 2022-05-13 新疆大学 A composite remediation method for leaky oil-contaminated soil

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107803400A (en) * 2017-10-31 2018-03-16 中国环境科学研究院 The compost method of petroleum hydrocarbon contaminated soil is repaired using biogas slurry
CN107803400B (en) * 2017-10-31 2020-12-08 中国环境科学研究院 Composting method of using biogas slurry to remediate petroleum hydrocarbon polluted soil
CN109365523A (en) * 2018-12-10 2019-02-22 北京博诚立新环境科技股份有限公司 A kind of bioreactor and its application method for contaminated soil remediation
CN110627227A (en) * 2019-11-04 2019-12-31 蒋俊连 High-temperature self-protection type microorganism treatment pool
CN110627227B (en) * 2019-11-04 2021-12-24 南京康旭科技有限公司 High-temperature self-protection type microorganism treatment pool
CN114472503A (en) * 2020-11-13 2022-05-13 新疆大学 A composite remediation method for leaky oil-contaminated soil

Similar Documents

Publication Publication Date Title
CN105598161A (en) Method for processing oil-containing waste residues by virtue of microorganisms
CN205436606U (en) Reaction bed of microbiological treatment oiliness waste residue
CN108911158B (en) A kind of rural domestic sewage treatment system based on small watershed form
US7422393B2 (en) Aerobic and anaerobic waste management systems and methods for landfills
CN107008723B (en) method for treating and sealing open type refuse landfill
CN101445297B (en) Method for deeply treating papermaking wastewater
CN108841392A (en) Utilize the conditioner of microorganism remediation organic polluted soil
US7168888B2 (en) Aerobic and anaerobic waste management systems and methods for landfills
CN104803721A (en) Biological composting treatment method of oil-based drilling waste
CN1173835A (en) Anaerobic/aerobic decontamination of DDT contaminated soil by repeated anaerobic/aerobic treatments
Husain et al. Microorganisms: An eco-friendly tools for the waste management and environmental safety
US20130023037A1 (en) Compost organic-matter accelerated bioremediation
CN105777258A (en) Method for making sludge into nutrient soil through anaerobic fermentation
CN109607988A (en) A kind of ecology pit black and odorous water processing method
CN111250537A (en) A bioremediation system for organically polluted sites
JP5968180B2 (en) Underground fermentation equipment
CN102513345B (en) Method for treating organic polluted soil
CN1293952C (en) Biological restoring method for contaminative soil and equipment therefor
CN112551824B (en) Vertical subsurface flow type constructed wetland device and method for sludge treatment
CN109734263A (en) A method of domestic sludge is quickly repaired using CPPM collaboration recovery scenario
CN201077820Y (en) Pit type high-temperature aerobic biofermentation deodorizer degrading organic fetor wastes compost
CN111922057A (en) In-situ remediation method for petroleum-polluted soil
CN209065779U (en) A kind of small-sized simulation installation for fermenting for Composting treatment garden wastes
Eleshmawiy et al. ECONOMIC VALUATION OF IRRIGATING TOMATO PLANTS WITH AGRICULTURAL DRAINAGE WATER REMEDIATED WITH DHS TECHNOLOGY.
CN112570447A (en) Composite remediation method for petroleum hydrocarbon contaminated soil

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160810

Termination date: 20190324

CF01 Termination of patent right due to non-payment of annual fee