CN110698025A - A kind of domestic sludge slurrying method and application of sludge after slurrying - Google Patents
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Abstract
Description
技术领域technical field
本发明属于污泥浆化领域,具体涉及一种生活污泥浆化方法及浆化后污泥的应用。The invention belongs to the field of sludge slurrying, and particularly relates to a domestic sludge slurrying method and application of the slurry after slurrying.
背景技术Background technique
随着城市的发展,城市污水处理量的提高和处理程度的深化,污泥的产生量一直是较大的增长。到2018年,我国污泥产生量高达7436万吨,其中生活污泥产生量3658万吨,呈逐年上升趋势。生活污泥含水量高、易腐烂,有强烈的臭味,并且含有寄生虫卵、病原微生物等,如不加以妥善处理,任意排放,将会造成二次污染。我国现有的污泥处理方法主要是脱水后堆放或填埋,处理费用昂贵,一般一个污水处理厂的污泥处理费约占总运行费用的15-30%,占总投资10-25%,由于处理污泥花费巨大,致使一些污水处理厂将污泥直接排放,给环境造成严重破坏,污泥已成为困扰污水处理厂和全社会的重大问题。With the development of the city, the increase in the amount of urban sewage treatment and the deepening of the treatment degree, the amount of sludge generated has been increasing greatly. By 2018, the amount of sludge produced in my country was as high as 74.36 million tons, of which the amount of domestic sludge was 36.58 million tons, showing an upward trend year by year. Domestic sludge has a high water content, is perishable, has a strong odor, and contains parasite eggs, pathogenic microorganisms, etc. If it is not properly treated and discharged arbitrarily, it will cause secondary pollution. The existing sludge treatment methods in my country are mainly dehydration and then stacking or landfilling, and the treatment cost is expensive. Generally, the sludge treatment cost of a sewage treatment plant accounts for about 15-30% of the total operating cost and 10-25% of the total investment. Due to the huge cost of sludge treatment, some sewage treatment plants directly discharge sludge, causing serious damage to the environment. Sludge has become a major problem that plagues sewage treatment plants and the whole society.
近年来,我国的环保工作取得很大进展,国家投入了大量资金进行污水处理,但如果对污水处理的伴生物—污泥不进行合理处理的话,又将会形成一个巨大的污染源,危害生态环境,在污泥处理中,堆放和填埋并不是好办法,不仅浪费钱财,而且浪费土地,这就需要一种污泥无害化处理和利用的技术。In recent years, my country's environmental protection work has made great progress, and the state has invested a lot of money in sewage treatment. However, if the sludge, the accompanying organism of sewage treatment, is not properly treated, it will form a huge source of pollution and endanger the ecological environment. , In the sludge treatment, stacking and landfill is not a good way, not only waste of money, but also waste of land, which requires a technology for the harmless treatment and utilization of sludge.
为解决这一问题,利用污泥堆肥技术将污泥制成肥料,很好的解决了污泥对环境的污染问题。原因有下:一是污泥堆肥与其他处理方法,如填埋、焚烧相比,具有建设投资少、运行费用低等优点,适合我国的国情。二是污泥中养分丰富。含有较高的有机质和丰富的氮磷等矿质营养元素,是实现污泥的资源化和循环利用的有效途径。In order to solve this problem, sludge composting technology is used to make sludge into fertilizer, which solves the problem of sludge pollution to the environment. The reasons are as follows: First, compared with other treatment methods, such as landfill and incineration, sludge composting has the advantages of less construction investment and lower operating costs, which is suitable for my country's national conditions. Second, the sludge is rich in nutrients. It contains high organic matter and abundant mineral nutrients such as nitrogen and phosphorus, which is an effective way to realize the resource utilization and recycling of sludge.
要实现生活污泥能更好的利用于绿化或农业,首先需要对污泥进行浆化处理,现有的处理污泥肥熟的浆化技术一是采用浆化池形式达到接收、混合、浆化目的,调节后的污泥含水率在90-92%,通过污泥泵打入后续处理单元。浆化池的顶部设置竖轴搅拌机进行搅拌,一侧为敞口设计,用于脱水污泥车倾倒污泥,补水管通过顶部接入。正常运行时竖轴搅拌机连续搅拌,当污泥倾倒如浆化池后,打开加水开关进行调节。In order to realize that the domestic sludge can be better used in greening or agriculture, the sludge needs to be pulped first. The existing pulping technology for sludge processing is to use the form of pulping tank to receive, mix, and pulp. For chemical purposes, the moisture content of the adjusted sludge is 90-92%, and it is pumped into the subsequent treatment unit through the sludge pump. The top of the slurry tank is equipped with a vertical shaft mixer for stirring, and one side is designed to be open, which is used for dewatering sludge trucks to dump sludge, and the water supply pipe is connected through the top. During normal operation, the vertical shaft mixer continuously stirs, and when the sludge is dumped like a slurry tank, the water addition switch is turned on for adjustment.
采用浆化池的形式进行污泥的混合、调质、浆化虽然可以达到效果,但是有一定的问题:进泥侧敞口设计,当污泥车倾倒污泥时,会造成很大的喷溅,影响现场卫生。由于计量问题,污泥量和加水量不容易进行精确匹配,很难调整到合适的含水率,难以达到工艺要求。Although the mixing, conditioning and pulping of sludge in the form of a slurry tank can achieve the effect, there are certain problems: the design of the open side of the sludge inlet, when the sludge truck dumps the sludge, it will cause a lot of spray splash, affecting the site hygiene. Due to the measurement problem, it is not easy to precisely match the amount of sludge and the amount of water added, it is difficult to adjust to the appropriate moisture content, and it is difficult to meet the process requirements.
发明内容SUMMARY OF THE INVENTION
为解决上述技术问题,提供一种生活污泥浆化方法及浆化后污泥的应用。In order to solve the above-mentioned technical problems, a method for slurrying domestic sludge and application of sludge after slurrying are provided.
具体技术方案如下:The specific technical solutions are as follows:
一种生活污泥浆化方法,其不同之处在于,所述生活污泥浆化的方法包括以下步骤:A method for slurrying domestic sludge, which is different in that the method for slurrying domestic sludge comprises the following steps:
步骤S1:将生活污泥进行沉降处理,得到预处理污泥;Step S1: carry out sedimentation treatment with domestic sludge to obtain pretreated sludge;
步骤S2:将匀浆剂加入预处理污泥中混合均匀,并静置得到稳定污泥;Step S2: adding the homogenizer to the pretreated sludge to mix evenly, and standing to obtain stable sludge;
步骤S3:将所述稳定污泥进行高压喷射。Step S3: spraying the stabilized sludge with high pressure.
进一步,所述步骤S1中,所述预处理污泥的含水率为90%~95%。Further, in the step S1, the moisture content of the pretreated sludge is 90% to 95%.
进一步,所述步骤S2中,所述匀浆剂剂包括膨润土及β-萘磺酸甲醛缩合物,搅拌2min~4min后混合均匀。Further, in the step S2, the homogenizing agent includes bentonite and β-naphthalenesulfonic acid formaldehyde condensate, and the mixture is uniformly mixed after stirring for 2 to 4 minutes.
进一步,所述步骤S2中,静置时间为3天。Further, in the step S2, the standing time is 3 days.
进一步,所述步骤S3中,将所述稳定污泥通过直径为0.6~0.8mm的微孔在文丘里喷射器中喷出。Further, in the step S3, the stabilized sludge is ejected in a venturi injector through micro-holes with a diameter of 0.6-0.8 mm.
进一步,所述匀浆剂与预处理污泥的重量比为:(0.1~0.15):1。Further, the weight ratio of the homogenizer to the pretreated sludge is: (0.1-0.15):1.
一种经上述方法处理后的生活污泥的应用,其不同之处在于,所述经浆化方法处理后的污泥在污泥肥熟中的应用。An application of the domestic sludge treated by the above method, the difference lies in the application of the sludge treated by the pulping method in the sludge fattening.
进一步,将所述稳定污泥造成球型后进行污泥肥熟。Further, after the stabilized sludge is formed into a spherical shape, the sludge is fattened.
与现有技术相比,本发明的有益效果在于:(1)匀浆剂可降低生活污泥中的含水率小于75%;(2)可建立新的平衡,使污泥处于稳定匀浆状态,污泥颗粒4小时的沉降速率不能超过1%的要求;(3)降低污泥的粘度,便于后续处理;(4)经文丘里喷射是污泥状态更加均匀,且占地面积小缩短匀浆时间;(5)经本发明浆化处理后的污泥分散均匀,污泥肥熟更加快速;(5)经本发明的浆化方法处理的污泥可直接作为堆肥球的原料使用,无需脱水,无需再增加其他材料原料。Compared with the prior art, the beneficial effects of the present invention are: (1) the homogenizer can reduce the water content in the domestic sludge to less than 75%; (2) a new balance can be established to keep the sludge in a stable homogenized state , the sedimentation rate of the sludge particles in 4 hours cannot exceed the requirement of 1%; (3) reduce the viscosity of the sludge to facilitate subsequent treatment; (4) Venturi jetting makes the sludge state more uniform, and the footprint is small and shortened evenly (5) The sludge after the slurry treatment of the present invention is evenly dispersed, and the sludge is cooked more quickly; (5) The sludge treated by the slurry method of the present invention can be directly used as the raw material of the compost ball, without the need for Dehydration, no need to add other raw materials.
具体实施方式Detailed ways
以下结合实施例对本发明的原理和特征进行描述,所举实例只用于解释本发明,并非用于限定本发明的范围。The principles and features of the present invention will be described below with reference to the embodiments. The examples are only used to explain the present invention, but not to limit the scope of the present invention.
污泥的含水率一般很高,在传统工艺中,为了使污泥便于输送、处理和处置,一般需要对污泥进行脱水处理,但不同性质污泥的脱水性能差别很大,脱水的难度也很大。通常用污泥比阻来衡量污泥的脱水性能,它反映水分通过污泥颗粒时,所受阻力的大小,由此可知,污泥比阻与过滤压力及过滤面积的平方成正比,而与滤液的动力黏度及滤饼的干固体重量成反比,并取决于污泥的性质。The moisture content of sludge is generally high. In the traditional process, in order to facilitate the transportation, treatment and disposal of sludge, it is generally necessary to dewater the sludge. very large. The sludge specific resistance is usually used to measure the dewatering performance of the sludge, which reflects the resistance of water passing through the sludge particles. It can be seen that the sludge specific resistance is proportional to the filtration pressure and the square of the filtration area, and is proportional to the square of the filtration pressure and the filtration area. The kinematic viscosity of the filtrate is inversely proportional to the dry solids weight of the filter cake and depends on the nature of the sludge.
由于污泥比阻、比表面积、毛细吸水及粘结力较大,在浆化过程中污泥分散性较差,易于分层离析,处于固液分离状态,不利于污泥浆化过程,同时离子的核电性能较大,污泥颗粒与溶剂的分散性系数较大,污泥颗粒与水溶液较难混为一体。而所达到的匀质浆体是将污泥颗粒与污水充分混合,即需增大污泥比阻来实现。如果仅仅使用浆化设备借助物理作用来对污泥进行处理,虽可增大过滤压力及过滤面积,达到一定的固液混合效果,但很难调整到合适的含水率,且作用时间较长,对于设备利用效率低下,难以达到工艺要求,且经过处理后期,污泥颗粒也会因重力原因下沉,保存时间不持久且状态不稳固。Due to the large specific resistance, specific surface area, capillary water absorption and cohesion of the sludge, the dispersibility of the sludge during the slurrying process is poor, and it is easy to be separated into layers. The nuclear power performance of ions is large, the dispersibility coefficient of sludge particles and solvent is large, and it is difficult for sludge particles to mix with aqueous solution. The homogeneous slurry achieved is to fully mix the sludge particles with the sewage, that is, to increase the specific resistance of the sludge to achieve. If only pulping equipment is used to treat sludge by physical action, although the filtration pressure and filtration area can be increased to achieve a certain solid-liquid mixing effect, it is difficult to adjust the appropriate moisture content and the action time is long. For the low utilization efficiency of the equipment, it is difficult to meet the process requirements, and after the late treatment, the sludge particles will also sink due to gravity, the storage time is not long and the state is unstable.
快速肥熟工艺:当前对于污泥的堆肥工艺主要是基于微生物对有机物的分解过程。其中污泥堆肥过程可分为条垛堆肥系统、强制通风静态垛堆肥系统以及工厂中筒仓式肥熟,其中这些堆肥技术有占地面积大,对气候条件的要求较高,堆肥周期长,且需要大量的人力翻堆等不足之处,不仅不可大规模的处理污泥而且很难满足当下社会的需求。而通过液态化混匀的浆化技术,可简化污泥处理步骤,降低处理成本,以期达到快速肥熟效果。Rapid composting process: The current composting process for sludge is mainly based on the decomposition process of organic matter by microorganisms. Among them, the sludge composting process can be divided into strip composting system, forced ventilation static stacking composting system and silo-type composting in the factory. These composting technologies have large area, high requirements on climatic conditions, and long composting cycle. In addition, it requires a lot of manpower to turn the heap and other shortcomings, not only can not deal with sludge on a large scale, but also difficult to meet the needs of the current society. And through the slurry technology of liquefaction and mixing, the sludge treatment steps can be simplified, the treatment cost can be reduced, and the effect of fast fattening can be achieved.
实施例一Example 1
一种生活污泥浆化方法,所述生活污泥浆化的方法包括以下步骤:A method for slurrying domestic sludge, the method for slurrying domestic sludge comprises the following steps:
步骤S1:将生活污泥进行沉降处理,得到预处理污泥,所述预处理污泥的含水率为90%~95%。Step S1 : performing sedimentation treatment on the domestic sludge to obtain pretreated sludge, wherein the moisture content of the pretreated sludge is 90% to 95%.
步骤S2:将匀浆剂加入预处理污泥中混合均匀,并静置3天得到稳定污泥;所述匀浆剂包括膨润土及β-萘磺酸甲醛缩合物(FDN),搅拌2min~4min后混合均匀,所述匀浆剂与预处理污泥的重量比为:(0.1~0.15):1。Step S2: adding a homogenizer to the pretreated sludge and mixing evenly, and standing for 3 days to obtain a stable sludge; the homogenizer includes bentonite and β-naphthalenesulfonic acid formaldehyde condensate (FDN), and stirs for 2 to 4 minutes After mixing evenly, the weight ratio of the homogenizer to the pretreated sludge is: (0.1-0.15):1.
步骤S3:将所述稳定污泥通过直径为0.6~0.8mm的微孔在文丘里喷射器中高压喷出。Step S3: The stabilized sludge is ejected at high pressure in a venturi injector through micropores with a diameter of 0.6-0.8 mm.
实施例二Embodiment 2
步骤S3中,将所述稳定污泥通过直径为0.6~0.8mm的微孔在文丘里喷射器中高压喷出至造粒设备,将稳定污泥造成圆球后进行污泥肥熟,污泥以球体为单位进行厌氧发酵,成为缓释肥供作物使用。In step S3, the stabilized sludge is ejected to the granulation equipment at high pressure in a venturi ejector through micro-holes with a diameter of 0.6-0.8 mm, and the stabilized sludge is formed into a ball, and then the sludge is fattened and cooked. Anaerobic fermentation is carried out in units of spheres to become slow-release fertilizer for crops.
以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the protection of the present invention. within the range.
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