CN104163491A - Petrochemical sewage treatment system by pulse water-distribution hydrolysis and acidification and application method thereof - Google Patents
Petrochemical sewage treatment system by pulse water-distribution hydrolysis and acidification and application method thereof Download PDFInfo
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Abstract
Description
技术领域technical field
本发明属于水处理技术领域,特别涉及一种脉冲布水水解酸化石化污水处理系统及其应用方法。The invention belongs to the technical field of water treatment, in particular to a pulse water distribution hydrolysis acidification petrochemical sewage treatment system and an application method thereof.
背景技术Background technique
石化污水具有废水量大、水质复杂、毒害性大、水质波动大、浓度高、难生物降解等特点,属于较难处理的工业废水。因此,有必要对石化废水进行适当的预处理技术,以改变其污染物结构,降低毒物浓度,提高其可生化性。水解酸化是一种厌氧处理工艺(丁雷,祁佩时,赵一先.2012.水解酸化工艺效果评价体系研究.环境工程,30(6):65-68)。它能够将废水中的悬浮性固体和大分子难降解物质水解为溶解性有机物和易生物降解的小分子物质及挥发性脂肪酸,提高废水可生化性,从而提高后续生物处理工艺的运行效果;同时具有负荷高、产泥少、能耗低、营养物需求量小、抗冲击负荷能力强、对水温和pH变化不敏感、易于控制等特点。因此,水解酸化工艺被广泛应用于处理难降解的石化废水。Petrochemical wastewater has the characteristics of large wastewater volume, complex water quality, high toxicity, large water quality fluctuations, high concentration, and difficult biodegradation. It is a relatively difficult industrial wastewater to treat. Therefore, it is necessary to carry out appropriate pretreatment technology for petrochemical wastewater to change its pollutant structure, reduce the concentration of poisonous substances, and improve its biodegradability. Hydrolytic acidification is an anaerobic treatment process (Ding Lei, Qi Peishi, Zhao Yixian. 2012. Research on the evaluation system of hydrolytic acidification process. Environmental Engineering, 30(6):65-68). It can hydrolyze suspended solids and macromolecular refractory substances in wastewater into dissolved organic matter, easily biodegradable small molecule substances and volatile fatty acids, improve the biodegradability of wastewater, and thus improve the operation effect of subsequent biological treatment processes; at the same time It has the characteristics of high load, less mud production, low energy consumption, small nutrient demand, strong impact load resistance, insensitive to water temperature and pH changes, and easy to control. Therefore, the hydrolytic acidification process is widely used in the treatment of refractory petrochemical wastewater.
为了保证水解酸化池内污泥和废水的充分接触,一般多采用机械搅拌、水力搅拌等方式加强泥水混合效果,实际应用中存在污泥沉积、动力消耗、设备腐蚀等缺点。In order to ensure sufficient contact between sludge and wastewater in the hydrolytic acidification tank, mechanical agitation and hydraulic agitation are generally used to enhance the mud-water mixing effect. In practical applications, there are disadvantages such as sludge deposition, power consumption, and equipment corrosion.
水解酸化池的进水方式分为连续进水和间歇脉冲进水。连续流进水能够实现较均匀的布水,但是存在水头损失大、出水口容易堵塞的问题。脉冲式进水能够形成高速流体冲击池内底层污泥,使污泥与污水充分混合,且无需消耗动力,是比较好的进水方式。The water intake mode of the hydrolytic acidification tank is divided into continuous water intake and intermittent pulse water intake. The continuous flow of water can achieve relatively uniform water distribution, but there are problems of large head loss and easy blockage of the water outlet. The pulsed water inlet can form a high-speed fluid to impact the bottom sludge in the tank, so that the sludge and sewage can be fully mixed without consuming power, so it is a better water inlet method.
脉冲布水器一般可分为电门式和虹吸式。电门式通过自动控制装置根据工况和工艺要求,控制电磁阀或者电动阀,形成脉冲。电门式脉冲布水器控制精确,但是设备成本和运行成本都比较高,而且长时间运行,容易出现故障。Pulse water distributors can generally be divided into switch type and siphon type. The switch type uses the automatic control device to control the solenoid valve or electric valve according to the working conditions and process requirements to form pulses. The switch-type pulse water distributor is precise in control, but the equipment cost and operating cost are relatively high, and it is prone to failure due to long-term operation.
虹吸式脉冲布水器是利用虹吸管中快速流动的水流将主管道中的空气带走,使主管道内形成一定的真空度,在管道内外大气压的作用下容器中的水进入主管道后排入池中。由于水流速度很快,布水能在短时间内完成,达到脉冲的效果,搅起池底的污泥,使其与池内废水不断充分混合,污泥与污水中的有机物得到充分的接触反应。从而提高水解酸化池的泥水混合效果,提高处理效率。The siphon pulse water distributor uses the fast-flowing water in the siphon to take away the air in the main pipe, so that a certain degree of vacuum is formed in the main pipe, and the water in the container enters the main pipe and is discharged into the pool under the action of the atmospheric pressure inside and outside the pipe. . Due to the fast water flow, the water distribution can be completed in a short time, achieving the effect of pulse, stirring up the sludge at the bottom of the pool, so that it can be continuously and fully mixed with the wastewater in the pool, and the organic matter in the sludge and sewage can be fully contacted and reacted. Thereby, the mud-water mixing effect of the hydrolytic acidification tank is improved, and the treatment efficiency is improved.
发明内容Contents of the invention
针对现有技术不足,本发明提供了一套水解酸化设备,包括脉冲布水器和水解酸化池。其中,脉冲布水器提供了高效节能、性能稳定可靠的脉冲效果,并可在不同流量条件下,实现单次脉冲体积、脉冲时间和脉冲周期均可调,中心出水管和钟罩气隙可调。可研究在不同条件下适用于石化废水的脉冲条件,能够适应多种工况下对脉冲布水要求。水解酸化池通过数值模拟计算优化各布水管径及出水孔的大小和位置,配合脉冲器,可实现布水均匀,防止管孔堵塞,强化泥水混合效果,增强生物活性和传质。Aiming at the deficiencies of the prior art, the invention provides a set of hydrolytic acidification equipment, including a pulse water distributor and a hydrolysis acidification tank. Among them, the pulse water distributor provides high-efficiency energy-saving, stable and reliable pulse effects, and can realize single pulse volume, pulse time and pulse period under different flow conditions. The center outlet pipe and the air gap of the bell can be adjusted Tune. It can study the pulse conditions suitable for petrochemical wastewater under different conditions, and can adapt to the requirements of pulse water distribution under various working conditions. The hydrolytic acidification tank optimizes the diameter of each water distribution pipe and the size and position of the outlet hole through numerical simulation calculations. With the pulser, it can achieve uniform water distribution, prevent pipe hole blockage, strengthen the mixing effect of mud and water, and enhance biological activity and mass transfer.
一种脉冲布水水解酸化石化污水处理系统,该系统由脉冲布水器和水解酸化池构成,其中,脉冲布水器由筒体、伸缩式钟罩、支架、中心出水管、辅助虹吸管、大气连通管、进水管、放空管和筒盖构成;水解酸化池由池体、一级布水管、二级布水管、出水孔、溢流堰、集水槽、溢流管、沿程取样口和放空排泥口构成;A pulse water distribution hydrolysis acidification petrochemical sewage treatment system, the system is composed of a pulse water distributor and a hydrolysis acidification tank, wherein the pulse water distributor consists of a cylinder, a telescopic bell, a bracket, a central outlet pipe, an auxiliary siphon, an atmospheric The connecting pipe, water inlet pipe, emptying pipe and cylinder cover; the hydrolysis acidification tank is composed of the tank body, the first-level water distribution pipe, the second-level water distribution pipe, the outlet hole, the overflow weir, the sump, the overflow pipe, the sampling port along the process and the Empty sludge discharge port configuration;
在筒体中设置支架,在支架上设置伸缩式钟罩,所述伸缩式钟罩由公扣段和母扣段相连构成,其中公扣段的一端与支架固定相连(焊接),母扣段的另一端由盲堵封口;所述筒体顶端设置筒盖,筒体下部设置进水管;辅助虹吸管的顶端与筒体的底部固定相连,底端与一级布水管的顶端相连;筒体的底部通过放空管与辅助虹吸管相连;放空管上设置阀门(球阀);辅助虹吸管与大气连通管相连;在辅助虹吸管内设置可调节固定位置的中心出水管,中心出水管的顶端位于伸缩式钟罩,底端位于一级布水管;A bracket is set in the cylinder, and a telescopic bell jar is arranged on the bracket. The telescopic bell jar is composed of a male buckle section and a female buckle section, wherein one end of the male buckle section is fixedly connected (welded) to the bracket, and the female buckle section The other end of the cylinder is sealed by a blind plug; the top of the cylinder is provided with a cylinder cover, and the bottom of the cylinder is provided with a water inlet pipe; the top of the auxiliary siphon is fixedly connected with the bottom of the cylinder, and the bottom is connected with the top of the primary water distribution pipe; The bottom is connected to the auxiliary siphon pipe through the vent pipe; a valve (ball valve) is set on the vent pipe; the auxiliary siphon pipe is connected to the atmospheric communication pipe; a central water outlet pipe with an adjustable fixed position is set in the auxiliary siphon pipe, and the top of the central water outlet pipe is located at the telescopic The bell jar, the bottom end is located in the first-level water distribution pipe;
在筒体下方设置池体,在池体内水平设置二级布水管,二级布水管上设置出水口;垂直于二级布水管设置一级布水管,一级布水管的底端与二级布水管相连;池体顶部设置溢流堰,溢流堰顶部设置集水槽,集水槽底部设置溢流管;池体底部设置放空排泥口;池体上设置沿程取样口;沿程取样口和放空排泥口上分别设置阀门(球阀)。A pool body is set under the cylinder body, a secondary water distribution pipe is arranged horizontally in the pool body, and a water outlet is set on the secondary water distribution pipe; a primary water distribution pipe is arranged perpendicular to the secondary water distribution pipe, and the bottom end of the primary water distribution pipe The water pipes are connected; the top of the pool is provided with an overflow weir, the top of the overflow weir is provided with a sump, and the bottom of the sump is provided with an overflow pipe; the bottom of the pool is provided with an emptying and mud discharge port; Valves (ball valves) are respectively arranged on the venting mud outlets.
所述进水管上设置阀门(球阀)。A valve (ball valve) is arranged on the water inlet pipe.
所述中心出水管为顶端具有一定长度公扣的管体。The central water outlet pipe is a pipe body with a male buckle of a certain length at the top.
所述中心出水管与筒体和支架之间分别通过丝扣相连。The central water outlet pipe is connected with the barrel body and the bracket through threaded buckles respectively.
所述二级布水管以一级布水管底端为中心,呈“米”字型均匀分布。The secondary water distribution pipes are centered on the bottom end of the primary water distribution pipes and are evenly distributed in the shape of a "meter".
一种脉冲布水水解酸化石化污水处理系统的应用方法,其脉冲过程如下:An application method of a pulsed water distribution hydrolysis acidification petrochemical sewage treatment system, the pulse process is as follows:
污水由进水管通过提升泵流入脉冲器筒体内;当筒体内液位达到伸缩式钟罩底端时,伸缩式钟罩内、中心出水管内以及辅助虹吸管内的空气被密封,随着筒体内液位的继续升高,上述密封空气由于水压经大气连通管被排出;当伸缩式钟罩内液位升高至中心出水管顶端后,中心出水管开始有污水溢流,并进一步排出被密封的空气,同时会使中心出水管内的液位比一级布水管的液位高,这个液位差促使中心出水管内液位降低,造成中心出水管内的空气压力小于一个大气压,呈负压状态,进而形成虹吸,将筒体内的污水通过伸缩式钟罩、中心出水管、一级布水管、二级布水管以及出水孔以高速注入池体中;当筒体内的液位降至伸缩式钟罩底端时,空气进入伸缩式钟罩内,破坏原来的负压状态,虹吸停止。Sewage flows into the cylinder of the pulsator from the water inlet pipe through the lifting pump; when the liquid level in the cylinder reaches the bottom of the telescopic bell, the air in the telescopic bell, the central outlet pipe and the auxiliary siphon is sealed, and the liquid in the cylinder As the level continues to rise, the above-mentioned sealed air is discharged through the atmospheric communication pipe due to water pressure; when the liquid level in the telescopic bell rises to the top of the central outlet pipe, the central outlet pipe begins to overflow with sewage, and further discharge is sealed At the same time, the liquid level in the center outlet pipe will be higher than the liquid level in the first-level water distribution pipe. This liquid level difference will cause the liquid level in the center outlet pipe to decrease, causing the air pressure in the center outlet pipe to be less than one atmospheric pressure, which is in a negative pressure state. Then a siphon is formed, and the sewage in the cylinder is injected into the pool at high speed through the telescopic bell jar, the central outlet pipe, the primary water distribution pipe, the secondary water distribution pipe and the water outlet hole; when the liquid level in the cylinder drops to the telescopic bell jar At the bottom, air enters the retractable bell jar, destroys the original negative pressure state, and the siphon stops.
上述脉冲布水器可由有机玻璃、不锈钢等材料制成。The above-mentioned pulse water distributor can be made of organic glass, stainless steel and other materials.
本发明的有益效果为:The beneficial effects of the present invention are:
本发明系统中高速污水对水解酸化池底部污泥有较好的搅拌作用。污泥实现了周期性的膨胀、压缩。整套系统除了提升泵,无需其他动力,易于维护,性能稳定,并且布水均匀,泥水混合效果好。The high-speed sewage in the system of the present invention has better stirring effect on the sludge at the bottom of the hydrolysis acidification tank. Sludge realizes periodic expansion and compression. The whole system does not need other power except the lifting pump, easy to maintain, stable performance, uniform water distribution, and good mud-water mixing effect.
附图说明Description of drawings
图1为本发明脉冲布水水解酸化石化污水处理系统的装置结构示意图;Fig. 1 is the schematic diagram of the device structure of the pulse water distribution hydrolysis acidification petrochemical sewage treatment system of the present invention;
图2为本发明可伸缩式钟罩的装置结构示意图;Fig. 2 is the device structural representation of retractable bell jar of the present invention;
图3为本发明二级布水管的装置结构示意图;Fig. 3 is a schematic diagram of the device structure of the secondary water distribution pipe of the present invention;
图中标号:11-筒体、12-伸缩式钟罩、12A-公扣段、12B-母扣段、13-支架、14-中心出水管、15-辅助虹吸管、16-大气连通管、17-进水管、18-放空管、19-筒盖、21-池体、22-一级布水管、23-二级布水管、24-出水孔、25-溢流堰、26-集水槽、27-溢流管、28-沿程取样口、29-放空排泥口。Numbers in the figure: 11-Cylinder body, 12-Telescopic bell jar, 12A-Male buckle section, 12B-Female buckle section, 13-Bracket, 14-Central water outlet pipe, 15-Auxiliary siphon pipe, 16-Atmospheric communication pipe, 17 -Inlet pipe, 18-Empty pipe, 19-Cylinder cover, 21-Pool body, 22-First-level water distribution pipe, 23-Secondary water distribution pipe, 24-Water outlet, 25-Overflow weir, 26-Sink, 27-Overflow pipe, 28-Sampling port along the way, 29-Empty mud discharge port.
具体实施方式Detailed ways
本发明提供了一种脉冲布水水解酸化石化污水处理系统及其应用方法,下面结合附图和具体实施方式对本发明做进一步说明。The present invention provides a pulsed water distribution hydrolysis acidification petrochemical sewage treatment system and its application method. The present invention will be further described below in conjunction with the accompanying drawings and specific implementation methods.
一种脉冲布水水解酸化石化污水处理系统,该系统由脉冲布水器和水解酸化池构成,其中,脉冲布水器由筒体11、伸缩式钟罩12、支架13、中心出水管14、辅助虹吸管15、大气连通管16、进水管17、放空管18和筒盖19构成;水解酸化池由池体21、一级布水管22、二级布水管23、出水孔24、溢流堰25、集水槽26、溢流管27、沿程取样口28和放空排泥口29构成;A pulse water distribution hydrolysis acidification petrochemical sewage treatment system, the system is composed of a pulse water distributor and a hydrolysis acidification tank, wherein the pulse water distributor consists of a cylinder 11, a telescopic bell 12, a bracket 13, a central outlet pipe 14, Auxiliary siphon pipe 15, atmospheric communication pipe 16, water inlet pipe 17, vent pipe 18 and cylinder cover 19; the hydrolysis acidification tank is composed of pool body 21, primary water distribution pipe 22, secondary water distribution pipe 23, water outlet hole 24, overflow weir 25. It is composed of a water collection tank 26, an overflow pipe 27, a sampling port 28 along the way, and a mud discharge port 29;
在筒体11中设置支架13,在支架13上设置伸缩式钟罩12,所述伸缩式钟罩12由公扣段12A和母扣段12B相连构成,其中公扣段12A的一端与支架13固定相连(焊接),母扣段12B的另一端由盲堵封口;所述筒体11顶端设置筒盖19,筒体11下部设置进水管17;辅助虹吸管15的顶端与筒体11的底部固定相连,底端与一级布水管22的顶端相连;筒体11的底部通过放空管18与辅助虹吸管15相连;放空管18上设置阀门(球阀);辅助虹吸管15与大气连通管16相连;在辅助虹吸管15内设置可调节固定位置的中心出水管14,中心出水管14的顶端位于伸缩式钟罩12,底端位于一级布水管22;A support 13 is arranged in the cylinder body 11, and a telescopic bell case 12 is arranged on the support 13. The telescopic bell case 12 is formed by connecting a male buckle section 12A and a female buckle section 12B, wherein one end of the male buckle section 12A is connected to the support 13 Fixedly connected (welded), the other end of the female buckle section 12B is sealed by a blind plug; the top of the cylinder 11 is provided with a cylinder cover 19, and the bottom of the cylinder 11 is provided with a water inlet pipe 17; the top of the auxiliary siphon 15 is fixed to the bottom of the cylinder 11 The bottom end is connected to the top of the primary water distribution pipe 22; the bottom of the cylinder body 11 is connected to the auxiliary siphon pipe 15 through the vent pipe 18; a valve (ball valve) is set on the vent pipe 18; the auxiliary siphon pipe 15 is connected to the atmospheric communication pipe 16 ;In the auxiliary siphon 15, a central water outlet pipe 14 with an adjustable fixed position is set, the top of the central water outlet pipe 14 is located at the telescopic bell jar 12, and the bottom end is located at the primary water distribution pipe 22;
在筒体11下方设置池体21,在池体21内水平设置二级布水管23,二级布水管23上设置出水口24;垂直于二级布水管23设置一级布水管22,一级布水管22的底端与二级布水管23相连;池体21顶部设置溢流堰25,溢流堰25顶部设置集水槽26,集水槽26底部设置溢流管27;池体21底部设置放空排泥口29;池体21上设置沿程取样口28;沿程取样口28和放空排泥口29上分别设置阀门(球阀)。A pool body 21 is arranged below the cylinder body 11, a secondary water distribution pipe 23 is horizontally arranged in the pool body 21, and a water outlet 24 is arranged on the secondary water distribution pipe 23; a primary water distribution pipe 22 is arranged perpendicular to the secondary water distribution pipe 23, and a primary The bottom of the water distribution pipe 22 is connected to the secondary water distribution pipe 23; the top of the pool body 21 is provided with an overflow weir 25, the top of the overflow weir 25 is provided with a sump 26, and the bottom of the sump 26 is provided with an overflow pipe 27; the bottom of the pool body 21 is provided with a vent Mud outlet 29; pool body 21 is provided with sampling port 28 along the way; valves (ball valves) are respectively set on the sampling port 28 and the venting mud outlet 29.
所述进水管17上设置阀门(球阀)。A valve (ball valve) is set on the water inlet pipe 17 .
所述中心出水管14为顶端具有一定长度公扣的管体。The central water outlet pipe 14 is a pipe body with a male buckle of a certain length at the top.
所述中心出水管14与筒体11和支架13之间分别通过丝扣相连。The central water outlet pipe 14 is connected with the cylinder body 11 and the bracket 13 respectively through threaded fasteners.
所述二级布水管23以一级布水管22底端为中心,呈“米”字型均匀分布。The secondary water distribution pipe 23 is centered on the bottom end of the primary water distribution pipe 22 and is evenly distributed in the shape of a "rice".
实施例1Example 1
本实施例所采用的脉冲布水水解酸化石化污水处理系统结构如图1~图3所示,其中,可通过调节伸缩式钟罩12的长度实现调节单次脉冲体积,并可通过丝扣调节中心出水管14与伸缩式钟罩12顶端的相对距离。The structure of the pulsed water distribution hydrolysis acidification petrochemical sewage treatment system adopted in this embodiment is shown in Figures 1 to 3, wherein the volume of a single pulse can be adjusted by adjusting the length of the telescopic bell 12, and can be adjusted by a threaded button The relative distance between the center outlet pipe 14 and the telescopic bell 12 top.
实验采用的脉冲布水器有效体积可调节范围为1L~5L,脉冲水头为1m,水解酸化池为直径为300mm、高为2500mm的有机玻璃柱,有效体积为150L。The effective volume of the pulse water distributor used in the experiment can be adjusted from 1L to 5L, and the pulse water head is 1m. The hydrolytic acidification tank is a plexiglass column with a diameter of 300mm and a height of 2500mm, and the effective volume is 150L.
以某石化工业园区内排放的实际污水(水质指标如表1所示)为处理对象,在进水化学需氧量(COD)为400mg/L~600mg/L,水力停留时间为20h,脉冲频次为10次/h,水温25~28度,采用上述脉冲水解酸化反应器的运行结果表明:COD的去除率为15%~20%,出水挥发酸所占的比例由进水的18%~24%增加到32%~45%,泥水混合良好,无污泥淤积现象。Taking the actual sewage discharged in a petrochemical industrial park (water quality indicators are shown in Table 1) as the treatment object, the influent chemical oxygen demand (COD) is 400mg/L-600mg/L, the hydraulic retention time is 20h, and the pulse frequency 10 times/h, water temperature 25-28 degrees, using the above-mentioned pulse hydrolysis acidification reactor operation results show that: COD removal rate is 15%-20%, the proportion of volatile acid in the effluent is from 18%-24% of the influent water % increased to 32% to 45%, the mud and water are well mixed, and there is no sludge deposition.
表1 石化废水的水质指标(mg/L,挥发酸以乙酸计)数据表Table 1 Water quality index of petrochemical wastewater (mg/L, volatile acid is calculated as acetic acid) data table
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104724822A (en) * | 2015-04-15 | 2015-06-24 | 铁道第三勘察设计院集团有限公司 | Pulse water distributor |
CN105481088A (en) * | 2015-12-16 | 2016-04-13 | 浙江省环境保护科学设计研究院 | Pulse water distribution generating device and pulse water distribution control method thereof |
CN108821432A (en) * | 2018-08-06 | 2018-11-16 | 广州博环保科技有限公司 | One kind can promote water distribution system reactor for hydrolysis and acidification |
CN110723811A (en) * | 2019-11-11 | 2020-01-24 | 博天环境集团股份有限公司 | Pulse water distributor |
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CN201077803Y (en) * | 2007-08-21 | 2008-06-25 | 四川立新瑞德环保科技发展有限责任公司 | Pulse water distributing device |
CN201082875Y (en) * | 2007-08-24 | 2008-07-09 | 宜兴市清涵环保工程有限公司 | Energy-saving impulse anaerobic reactor |
CN201704125U (en) * | 2010-04-30 | 2011-01-12 | 青岛银河环保股份有限公司 | Siphon type pulse water distributor and sewage treatment pool with the same |
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SU1722306A1 (en) * | 1990-05-17 | 1992-03-30 | Всесоюзное Научно-Производственное Объединение По Механизации Орошения "Радуга" | Device for irrigation |
CN201077803Y (en) * | 2007-08-21 | 2008-06-25 | 四川立新瑞德环保科技发展有限责任公司 | Pulse water distributing device |
CN201082875Y (en) * | 2007-08-24 | 2008-07-09 | 宜兴市清涵环保工程有限公司 | Energy-saving impulse anaerobic reactor |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104724822A (en) * | 2015-04-15 | 2015-06-24 | 铁道第三勘察设计院集团有限公司 | Pulse water distributor |
CN105481088A (en) * | 2015-12-16 | 2016-04-13 | 浙江省环境保护科学设计研究院 | Pulse water distribution generating device and pulse water distribution control method thereof |
CN105481088B (en) * | 2015-12-16 | 2017-10-20 | 浙江省环境保护科学设计研究院 | Pulse water distribution generating means and its pulse water distribution control method |
CN108821432A (en) * | 2018-08-06 | 2018-11-16 | 广州博环保科技有限公司 | One kind can promote water distribution system reactor for hydrolysis and acidification |
CN110723811A (en) * | 2019-11-11 | 2020-01-24 | 博天环境集团股份有限公司 | Pulse water distributor |
CN110723811B (en) * | 2019-11-11 | 2022-04-05 | 博天环境集团股份有限公司 | Pulse water distributor |
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