WO2017096657A1 - 一种脱水污泥厌氧干发酵的装置 - Google Patents

一种脱水污泥厌氧干发酵的装置 Download PDF

Info

Publication number
WO2017096657A1
WO2017096657A1 PCT/CN2015/099494 CN2015099494W WO2017096657A1 WO 2017096657 A1 WO2017096657 A1 WO 2017096657A1 CN 2015099494 W CN2015099494 W CN 2015099494W WO 2017096657 A1 WO2017096657 A1 WO 2017096657A1
Authority
WO
WIPO (PCT)
Prior art keywords
sludge
mud
tank
liquid
fermentation
Prior art date
Application number
PCT/CN2015/099494
Other languages
English (en)
French (fr)
Inventor
李欢
司丹丹
张玉瑶
陈成
Original Assignee
清华大学深圳研究生院
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 清华大学深圳研究生院 filed Critical 清华大学深圳研究生院
Publication of WO2017096657A1 publication Critical patent/WO2017096657A1/zh

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/02—Biological treatment
    • C02F11/04—Anaerobic treatment; Production of methane by such processes
    • 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/20—Sludge processing

Definitions

  • the invention relates to the field of sludge treatment, in particular to a device for anaerobic dry fermentation of dewatered sludge.
  • the anaerobic digestion of sludge is divided into wet fermentation and dry fermentation according to the solid content of sludge.
  • Dry fermentation refers to an operation mode in which the total solid content accounts for 15% to 20% of the total amount of the substance in the reactor.
  • dry fermentation has the advantages of high organic loading rate, high methane yield per unit effective volume, low energy consumption and low waste generation.
  • more than 80% of the sludge in China has been dehydrated before subsequent treatment and disposal. Therefore, the intensive treatment of dewatered sludge by dry fermentation technology has great development potential in China and is receiving increasing attention.
  • the invention provides a device for anaerobic dry fermentation of dewatered sludge, which has the disadvantages of large volume of the existing low-solids sludge anaerobic digestion facility, difficulty in stirring, difficulty in heat and mass transfer, and low gas production per unit volume. In order to effectively and directly dry the dewatered sludge, the gas production efficiency is significantly improved.
  • An apparatus for anaerobic dry fermentation of dewatered sludge comprises: a fermenting tank body, a double ribbon agitator and a spiral auger, wherein the upper and lower portions of the fermenting tank body are respectively provided with a mud inlet and a mud outlet, a double spiral belt agitator traversing the fermentor body and adjacent to the mud inlet, the spiral auger traversing the fermentor body and close to the mud outlet, the double spiral belt agitator is in the spiral strand Above the dragon, the double ribbon agitator is used to promote heat and mass transfer of the sludge and accelerate the escape of gas in the fermenter.
  • the spiral auger is used to agitate the sludge in the lower part of the fermenter and in the fermenter body. When the sludge is discharged, the sludge is pushed toward the mud outlet.
  • the double spiral belt agitator and the auger have the same agitation frequency.
  • a can insulation layer disposed on an outer surface of the fermentor body.
  • a heating layer is also included, the heating layer being disposed on an inner surface of the fermentor body.
  • a liquid tank a liquid pump, and a heater
  • the heating layer is for flowing a liquid
  • the heating layer includes a liquid inlet and a liquid outlet
  • the heater is disposed in the liquid tank
  • the liquid pump is used for The heated liquid in the tank is pumped into the liquid inlet from which the liquid flows from the liquid inlet and exits from the liquid outlet back to the tank.
  • a gas outlet disposed above the double helix belt agitator and a gas flow meter in communication with the gas outlet.
  • a mud hopper Also included is a mud hopper, a mud pump for receiving mud, and the mud snail
  • the rod pump is used to pump sludge from the mud into the ferment tank from the inlet.
  • a plurality of temperature detectors are also included, the plurality of temperature detectors being evenly distributed inside the fermentor body.
  • the upper part of the fermenter body is provided with a gas safety valve and a barometer.
  • a gas safety valve When the gas pressure in the fermenter exceeds a set pressure threshold, the gas is discharged through the gas safety valve to the outside of the fermenter.
  • the upper portion of the fermentor body is provided with a cleaning liquid inlet.
  • a mud screw pump and a ball valve are also included, and the mud screw pump is coupled to the mud outlet through the ball valve.
  • the invention can effectively and directly dry the dewatered sludge, and significantly improve the gas production efficiency.
  • a composite of a double ribbon agitator, a screw auger, and a screw pump is used. System to achieve agitation and discharge of sludge.
  • FIG. 1 is a schematic view of an apparatus for anaerobic dry fermentation of dewatered sludge according to an embodiment of the present invention
  • Figure 2 is a side view (partial structure) of Figure 1;
  • Figure 3 is a cross-sectional view along line A-A of the apparatus for anaerobic dry fermentation of the dewatered sludge of Figure 1.
  • Inlet screw pump 1 inlet mud 2, pressure gauge 3, safety valve 4, pressure inlet hole 5, cleaning port 6, exhaust port 7, gas flow meter 8, tank insulation layer 9, water bath heating layer 10, fermentation Tank 11, double ribbon stirrer 12, stirring shaft 13, motor 14, temperature control and electric control box 15, spiral auger 16, ball Valve 17, discharge screw pump 18, heating water tank 19, electric heater 20, water pump 21, bracket 22, water outlet 23, water inlet 24, temperature detector 25
  • an apparatus for anaerobic dry fermentation of dewatered sludge comprises: a fermentor body 11, a double ribbon agitator 12, and a screw auger 16, the upper part of which is the fermenter body 11.
  • the double spiral belt agitator 12 traversing the fermentation tank body 1 and adjacent to the mud inlet, the spiral auger 16 traversing the fermentation tank body 1 and Close to the mud outlet, the double spiral belt agitator 12 is above the spiral auger 16 , and the double ribbon agitator 12 is used for uniformly mixing sludge, promoting heat and mass transfer of sludge, and accelerating
  • the sludge in the fermentor body 1 is fermented to generate gas, and the gas in the fermenting tank body 1 can be accelerated, and the screw auger 16 is used to agitate the sludge in the lower part of the fermenting tank body 1 and in the fermenting tank body.
  • the agitator frequency of the double spiral belt agitator 12 and the screw auger 16 are the same, and the sludge is prevented from accumulating at the bottom corner of the fermentation tank body 1 to form a sludge. Stir the dead zone.
  • the double helix agitator 12 and the auger 16 can each be driven by a corresponding motor 14.
  • the apparatus for dehydrated sludge anaerobic dry fermentation may further include a tank insulation layer 9 disposed on an outer surface of the fermentor body 1 to perform the fermentation tank body 1 Insulation to promote the fermentation of sludge.
  • the apparatus for anaerobic dry fermentation of dewatered sludge may further include a heating layer 10 disposed on an inner surface of the fermentor body 1 to provide a continuously stable heat source to the fermentor body 1.
  • the heating layer 10 may be a liquid source for providing a heat source.
  • the dehydrated sludge anaerobic dry fermentation apparatus may further include a tank 19, a liquid pump 21, and a heater 20, the heating layer 10 including a liquid An inlet 24 and a liquid outlet 23 (both may be located at an upper portion and a lower portion of a side of the fermentor body 1, respectively), the heater 20 being disposed in the tank 19, and the liquid pump 21 for The heated liquid in the tank 19 is pumped into the liquid inlet 24 from which the liquid The inlet 24 flows through the heating layer 10 and flows out of the liquid outlet 23 back into the tank 19.
  • the dehydrated sludge anaerobic dry fermentation apparatus may further include a gas outlet 7 and a gas flow meter 8 disposed above the double spiral belt agitator 12, the gas flow meter 8 is in communication with the gas outlet 7 for measuring gas produced by sludge fermentation.
  • the apparatus for anaerobic dry fermentation of dewatered sludge may further include a mud hopper 2 for receiving sludge, and a mud screw pump 1 for The sludge in the mud hopper 2 is pumped from the mud inlet into the fermentor body 11.
  • the apparatus for dehydrated sludge anaerobic dry fermentation may further include a plurality of temperature detectors 25 uniformly distributed inside the fermentor body 1 to monitor the fermentor body 1 The temperature inside changes.
  • the upper portion of the fermentor body is provided with a gas safety valve 4, a barometer 3, a cleaning liquid inlet 6 and a pressure inlet hole 5, when the gas pressure in the fermentation tank body 11 exceeds a set pressure threshold
  • the gas is discharged from the outside of the fermenter through the gas safety valve 4, and the pressure inlet hole 5 is used to facilitate the installation and disassembly of the double spiral belt agitator 12 and the screw auger 16 inside the fermentation tank body 11.
  • the apparatus for anaerobic dry fermentation of dewatered sludge further includes a mud screw pump 18 and a ball valve 17, through which the sludge pump 18 is coupled to the sludge outlet.
  • the fermentor body 11 operates in a semi-continuous manner with an effective volumetric coefficient of the fermentor body 11 of 0.8-0.9. Regularly enter and discharge a certain amount of dewatered sludge with a water content of 20%.
  • the mud screw pump 1 is started, and after the mud is completed, the feed screw pump 1 and the ball valve are closed.
  • the double ribbon agitator 12 starts to agitate before entering the mud, and continues the whole mud entering process.
  • the motor 14 is turned off, the agitator is suspended, and then the stirring frequency is set according to the setting. And time will re-rotate.
  • the main function of the lower spiral auger 16 is to promote the discharge of sludge in the tank.
  • the discharge ball valve 17 is opened, the spiral auger motor 14 is turned on and rotated in the direction of the mud, thereby the tank
  • the sludge in the lower part of the body is transported to the discharge port, and after a short period of time, the discharge screw pump 18 is opened to complete the quantitative discharge process.
  • the ball valve 17, the screw pump 18, and the motor 14 are closed, and then the auger 16 is simultaneously agitated with the double ribbon agitator 12 according to the set stirring frequency and time.
  • the biogas generated by the sludge fermentation is discharged through the exhaust port 7 at the upper portion of the tank, and the gas production amount is recorded by the gas flow meter 8, and then collected or transported for other uses.
  • the pressure gauge 3 on the upper part of the tank will show the internal pressure of the tank. When the pressure is too high, the safety valve 4 will automatically open for deflation.
  • a water bath heating layer 10 is disposed outside the tank body, and the heating water is supplied from the heating water tank, and flows from the lower water inlet 24 on the tank side under the action of the water pump 21, and the water cooled in the heating layer 10 is from the same side of the tank body.
  • the upper water outlet 23 flows out.
  • the water in the heating water tank is heated by the electric heater 20 at its lower portion.
  • a plurality of temperature detectors 25 are provided in the fermenter tank, which are connected to the temperature control and electric control box 15 through a pipeline for detecting changes in the temperature inside the tank, for example, whether it reaches or exceeds 35 °C.

Abstract

一种脱水污泥厌氧干发酵的装置，包括：发酵罐体(11)、双螺带搅拌器(12)和螺旋绞龙(16)，所述发酵罐体(11)的上部和下部分别设有进泥口和出泥口，所述双螺旋带搅拌器(12)横贯所述发酵罐体(11)且靠近所述进泥口，所述螺旋绞龙(16)横贯所述发酵罐体(11)且靠近所述出泥口，所述双螺旋带搅拌器(12)在所述螺旋绞龙(16)上方，所述双螺带搅拌器(12)用于促进污泥的传热传质，加快发酵罐体内气体的逸出，所述螺旋绞龙(16)用于搅动发酵罐体(11)下部的污泥，并在发酵罐体(11)排污泥时把污泥推向所述出泥口，本装置可以对脱水污泥进行有效直接干发酵，显著提高产气效率。

Description

一种脱水污泥厌氧干发酵的装置 【技术领域】
本发明涉及污泥处理领域，具体涉及一种脱水污泥厌氧干发酵的装置。
【背景技术】
目前，我国的污水处理能力逐年提高，截止2014年底，污水处理能力已达到1.57亿m3/d，然而污水处理量的增加导致了大量污泥的产生，估计今年污泥产量将突破3500万t。目前，污泥的处置方法包括卫生填埋、堆肥、焚烧和厌氧消化。相较而言，污泥厌氧消化更好的实现了污泥的减量化、稳定化和资源化，现在在国内外已得到了普遍应用。
污泥的厌氧消化按照污泥含固率又分为湿发酵和干发酵。干发酵是指总固体含量占反应器中物质总量的15％-20％以上的运行方式。相对于湿发酵，干发酵具有有机负荷率高、单位有效容积甲烷产量高、能耗低和产生废物少等优点。目前，我国超过80％的污泥在进行后续的处理处置之前都已经过脱水处理，所以干发酵技术集约处理脱水污泥在我国具有很大的开发潜力，也正日益受到广泛的关注。
然而，由于脱水污泥的粘度较大，呈半固体状，脱水污泥干发酵仍存在搅拌困难，发酵过程传质传热不均一，易造成有机酸、氨氮等物质积累，消化周期延长及抑制厌氧微生物活性等缺点，这都可能导致脱水污泥发酵性能的显著下降。目前国内外有关污泥厌氧消化产沼气的研究大多围绕传统的低固体浓度消化工艺(3％-5％)展开，还没有将含固率高达20％的脱水污泥直接用于厌氧消化的工程实例，主要是因为缺乏直接用于脱水污泥厌氧干发酵的装置。
【发明内容】
针对现有低固体污泥厌氧消化设施存在的容器体积太大、不易搅拌、传热传质困难及单位容积产气量少等缺点，本发明提供了一种脱水污泥厌氧干发酵的装置，以对脱水污泥进行有效直接干发酵，显著提高产气效率。
一种脱水污泥厌氧干发酵的装置，包括：发酵罐体、双螺带搅拌器和螺旋绞龙，所述发酵罐体的上部和下部分别设有进泥口和出泥口，所述双螺旋带搅拌器横贯所述发酵罐体且靠近所述进泥口，所述螺旋绞龙横贯所述发酵罐体且靠近所述出泥口，所述双螺旋带搅拌器在所述螺旋绞龙上方，所述双螺带搅拌器用于促进污泥的传热传质，加快发酵罐体内气体的逸出，所述螺旋绞龙用于搅动发酵罐体下部的污泥，并在发酵罐体排污泥时把污泥推向所述出泥口。
在一个实施例中，
所述双螺旋带搅拌器和所述螺旋绞龙的搅动频率相同。
在一个实施例中，
还包括罐体保温层，所述罐体保温层设置在所述发酵罐体的外表面。
在一个实施例中，
还包括加热层，所述加热层设置在所述发酵罐体的内表面。
在一个实施例中，
还包括液箱、液泵和加热器，所述加热层用于流动液体，所述加热层包括液体入口和液体出口，所述加热器设置在所述液箱内，所述液泵用于将所述液箱内经过加热的液体泵入液体入口，液体从所述液体入口流经所述加热层后从液体出口流出回到所述液箱。
在一个实施例中，
还包括气体出口和气体流量计，所述气体出口设置在所述双螺旋带搅拌器的上方，所述气体流量计与所述气体出口连通。
在一个实施例中，
还包括进泥斗、进泥螺杆泵，所述进泥斗用于接收污泥，所述进泥螺 杆泵用于将进泥斗内的污泥从进泥口泵入发酵罐体。
在一个实施例中，
还包括多个温度探测器，所述多个温度探测器均匀分布在所述发酵罐体内部。
在一个实施例中，
所述发酵罐体的上部设有气体安全阀和气压计，当所述发酵罐体内的气压超过设定气压阈值时，气体通过所述气体安全阀排出发酵罐体外。
在一个实施例中，
所述发酵罐体的上部设有清洗液体入口。
在一个实施例中，
还包括出泥螺杆泵和球阀，所述出泥螺杆泵通过所述球阀与所述出泥口连接。
本发明可以对脱水污泥进行有效直接干发酵，显著提高产气效率。
由于脱水污泥的粘度较高，且呈半固体状，造成密封条件下操作时搅拌和出料困难，因而，在一些实施例中采用了双螺带搅拌器、螺旋绞龙、螺杆泵的复合系统，以实现对污泥的搅拌和排出。
【附图说明】
图1是本发明一种实施例的脱水污泥厌氧干发酵的装置的示意图；
图2是图1的侧视示意图(部分结构)；
图3是图1的脱水污泥厌氧干发酵的装置的A-A剖视图。
进泥螺杆泵1、进泥斗2、压力表3、安全阀4、压力入孔5、清洗口6、排气口7、气体流量计8、罐体保温层9、水浴加热层10、发酵罐体11、双螺带搅拌器12、搅拌轴13、电机14、温控和电控箱15、螺旋绞龙16、球 阀17、出料螺杆泵18、加热水箱19、电加热器20、水泵21、支架22、出水口23、进水口24、温度探测器25
【具体实施方式】
以下对发明的较佳实施例作进一步详细说明。
如图1至3所示，一种实施例的脱水污泥厌氧干发酵的装置，包括：发酵罐体11、双螺带搅拌器12和螺旋绞龙16，所述发酵罐体11的上部和下部分别设有进泥口和出泥口，所述双螺旋带搅拌器12横贯所述发酵罐体1且靠近所述进泥口，所述螺旋绞龙16横贯所述发酵罐体1且靠近所述出泥口，所述双螺旋带搅拌器12在所述螺旋绞龙16上方，所述双螺带搅拌器12用于使污泥混合均匀，促进污泥的传热传质，加快发酵罐体1内的污泥发酵而产生气体，并可以加快发酵罐体1内的气体的逸出，所述螺旋绞龙16用于搅动发酵罐体1下部的污泥，并在发酵罐体1排污泥时把污泥推向所述出泥口，所述双螺旋带搅拌器12和所述螺旋绞龙16的搅动频率相同，并防止污泥在发酵罐体1底部角堆积而形成搅拌死区。双螺旋带搅拌器12和螺旋绞龙16分别可以通过对应的电机14驱动。
在一个实施例中，脱水污泥厌氧干发酵的装置还可以包括罐体保温层9，所述罐体保温层9设置在所述发酵罐体1的外表面，以对发酵罐体1进行保温，促进污泥的发酵。
脱水污泥厌氧干发酵的装置还可以包括加热层10，所述加热层10设置在所述发酵罐体1的内表面，以对发酵罐体1提供持续稳定的热源。
加热层10可以是供液体流动而提供热源的，在这种情形下，脱水污泥厌氧干发酵的装置还可以包括液箱19、液泵21和加热器20，所述加热层10包括液体入口24和液体出口23(两者可以分别位于所述发酵罐体1的侧面的上部和下部)，所述加热器20设置在所述液箱19内，所述液泵21用于将所述液箱19内经过加热的液体泵入液体入口24，液体从所述液体 入口24流经所述加热层10后从液体出口23流出回到所述液箱19内。
在一个实施例中，脱水污泥厌氧干发酵的装置还可以包括气体出口7和气体流量计8，所述气体出口7设置在所述双螺旋带搅拌器12的上方，所述气体流量计8与所述气体出口7连通，用于测量污泥发酵产生的气体。
在一个实施例中，脱水污泥厌氧干发酵的装置还可以包括进泥斗2、进泥螺杆泵1，所述进泥斗2用于接收污泥，所述进泥螺杆泵1用于将进泥斗2内的污泥从进泥口泵入发酵罐体11。
在一个实施例中，脱水污泥厌氧干发酵的装置还可以包括多个温度探测器25，所述多个温度探测器25均匀分布在所述发酵罐体1内部，以监控发酵罐体1内的温度变化。
在一个实施例中，所述发酵罐体的上部设有气体安全阀4、气压计3、清洗液体入口6和压力入孔5，当所述发酵罐体11内的气压超过设定气压阈值时，气体通过所述气体安全阀4排出发酵罐体外，压力入孔5用于方便安装和拆卸发酵罐体11内部的双螺旋带搅拌器12和螺旋绞龙16。
在一个实施例中，脱水污泥厌氧干发酵的装置还包括出泥螺杆泵18和球阀17，所述出泥螺杆泵18通过所述球阀17与所述出泥口连接。
在一个实施例中，发酵罐体11采用半连续方式运行，发酵罐体11的有效容积系数为0.8-0.9。每天定时进、排一定量含水率为20％的脱水污泥，先将定量的泥加入进泥斗2中，然后打开进料球阀进泥(设置在螺杆泵1与进泥口之间)，并启动进泥螺杆泵1，待进泥完成后，关闭进料螺杆泵1和球阀。双螺带搅拌器12在进泥前即开启搅动，并持续整个进泥过程，进泥完成且待罐内泥全部搅拌均匀后，电机14关闭，搅拌器暂停搅动，之后根据设定的搅拌频率和时间会重新转动。下部的螺旋绞龙16的主要作用是促进罐体内污泥的排出，当需要排泥时，出料球阀17打开，开启螺旋绞龙电机14并使其顺着出泥的方向转动，从而将罐体下部的污泥向出料口输送，一小段时间后打开出料螺杆泵18完成定量的出料过程。出料完成后， 关闭球阀17、螺杆泵18以及电机14，之后螺旋绞龙16会根据设定的搅拌频率和时间与双螺带搅拌器12进行同时搅动。污泥发酵产生的沼气通过罐体上部的排气口7排出并由气体流量计8记录产气量，之后进行收集或输送以进行其他的使用。罐体上部的压力表3会显示罐体内部压力，当压力过大时，安全阀4会自动开启进行放气。在罐体外面设置有水浴加热层10，加热用水由加热水箱提供，并在水泵21的作用下从罐体一侧的下部进水口24流入，加热层10内冷却下来的水从罐体同侧上部的出水口23流出。加热水箱内的水由其下部的电加热器20进行加热。发酵罐体内设有多个温度探测器25，其与温控和电控箱15通过管线相连接，用于检测罐体内温度的变化，例如是否达到或超过35℃。
以上内容是结合具体的优选实施方式对本发明所作的进一步详细说明，不能认定本发明的具体实施只局限于这些说明。对于本发明所属技术领域的普通技术人员来说，在不脱离本发明构思的前提下，还可以做出若干简单推演或替换，都应当视为属于本发明由所提交的权利要求书确定的专利保护范围。

Claims (10)

  1. 一种脱水污泥厌氧干发酵的装置，其特征是，包括：发酵罐体、双螺带搅拌器和螺旋绞龙，所述发酵罐体的上部和下部分别设有进泥口和出泥口，所述双螺旋带搅拌器横贯所述发酵罐体且靠近所述进泥口，所述螺旋绞龙横贯所述发酵罐体且靠近所述出泥口，所述双螺旋带搅拌器在所述螺旋绞龙上方，所述双螺带搅拌器用于促进污泥的传热传质，加快发酵罐体内气体的逸出，所述螺旋绞龙用于搅动发酵罐体下部的污泥，并在发酵罐体排污泥时把污泥推向所述出泥口。
  2. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：所述双螺旋带搅拌器和所述螺旋绞龙的搅动频率相同。
  3. 如权利要求1或2所述的脱水污泥厌氧干发酵的装置，其特征是：还包括加热层、罐体保温层，所述加热层设置在所述发酵罐体的内表面，所述罐体保温层设置在所述发酵罐体的外表面。
  4. 如权利要求3所述的脱水污泥厌氧干发酵的装置，其特征是：还包括液箱、液泵和加热器，所述加热层用于流动液体，所述加热层包括液体入口和液体出口，所述加热器设置在所述液箱内，所述液泵用于将所述液箱内经过加热的液体泵入液体入口，液体从所述液体入口流经所述加热层后从液体出口流出回到所述液箱。
  5. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：还包括气体出口和气体流量计，所述气体出口设置在所述双螺旋带搅拌器的上方，所述气体流量计与所述气体出口连通。
  6. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：还包括进泥斗、进泥螺杆泵，所述进泥斗用于接收污泥，所述进泥螺杆泵用于将进泥斗内的污泥从进泥口泵入发酵罐体。
  7. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：还包括多个温度探测器，所述多个温度探测器均匀分布在所述发酵罐体内部。
  8. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：所述发酵罐体的上部设有气体安全阀和气压计，当所述发酵罐体内的气压超过设定气压阈值时，气体通过所述气体安全阀排出发酵罐体外。
  9. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：所述发酵罐体的上部设有清洗液体入口。
  10. 如权利要求1所述的脱水污泥厌氧干发酵的装置，其特征是：还包括出泥螺杆泵和球阀，所述出泥螺杆泵通过所述球阀与所述出泥口连接。
PCT/CN2015/099494 2015-12-10 2015-12-29 一种脱水污泥厌氧干发酵的装置 WO2017096657A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201510916620.4A CN105417912B (zh) 2015-12-10 2015-12-10 一种脱水污泥厌氧干发酵的装置
CN201510916620.4 2015-12-10

Publications (1)

Publication Number Publication Date
WO2017096657A1 true WO2017096657A1 (zh) 2017-06-15

Family

ID=55496531

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2015/099494 WO2017096657A1 (zh) 2015-12-10 2015-12-29 一种脱水污泥厌氧干发酵的装置

Country Status (2)

Country Link
CN (1) CN105417912B (zh)
WO (1) WO2017096657A1 (zh)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107935345A (zh) * 2017-12-28 2018-04-20 杨建� 一种生活污泥厌氧消化处理培育有机营养土的方法及系统
CN108441414A (zh) * 2018-06-21 2018-08-24 农业部规划设计研究院 一种厌氧干发酵渗滤液流动特性测试装置及测试方法
CN108641941A (zh) * 2018-06-04 2018-10-12 榆林学院 一种用于发酵腐殖酸的装置
CN109182120A (zh) * 2018-10-22 2019-01-11 中霖华夏农业科技发展有限公司 一种发酵装置
CN110437985A (zh) * 2019-07-17 2019-11-12 光大环保技术研究院（南京）有限公司 一种干式厌氧反应器
CN113414225A (zh) * 2021-06-30 2021-09-21 重庆市环卫集团有限公司 干式厌氧消化及罐底除砂系统
CN113956930A (zh) * 2021-11-30 2022-01-21 宁波沪港食品机械制造有限公司 一种啤酒发酵罐
CN114988655A (zh) * 2022-05-16 2022-09-02 福建源固节能环保科技有限公司 污泥可降解金属离子处置方法

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106830606B (zh) * 2017-03-30 2023-12-05 四川高博环投科技有限公司 一种污泥水解、腐植、催化、干燥综合处理设备
CN107032844A (zh) * 2017-06-19 2017-08-11 盐城市剑峰机械有限公司 畜禽粪便卧式发酵机结构
CN107698122A (zh) * 2017-10-13 2018-02-16 朱平 一种双螺旋污泥脱水机
CN109046148A (zh) * 2018-07-27 2018-12-21 长沙市凤英机械科技有限公司 一种建材加工用污泥搅拌装置
WO2021114111A1 (zh) * 2019-12-10 2021-06-17 深圳市合众清洁能源研究院 一种深度脱水污泥的输送系统
CN112624814A (zh) * 2021-01-20 2021-04-09 浙江春绿生态环保科技有限公司 一种垃圾制肥料设备
CN112777898A (zh) * 2021-01-26 2021-05-11 云南炳森环境工程有限公司 一种便于清理沉积物的玻璃钢化粪池

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6673247B2 (en) * 2000-10-13 2004-01-06 Fkc Co., Ltd. Sludge dewatering and pasteurization process
CN201074232Y (zh) * 2007-08-11 2008-06-18 谷宗华 移动式沼气发生器
CN101921049A (zh) * 2010-09-21 2010-12-22 同济大学 一种城市污泥及有机质干法厌氧发酵产沼气的方法及装置
CN104150726A (zh) * 2014-07-25 2014-11-19 中国环境科学研究院 一种减量化的污泥处理装置及污泥干化方法
CN204550355U (zh) * 2015-03-30 2015-08-12 中和利华投资管理（北京）有限公司 一种污泥高负荷厌氧消化备料调节系统
CN105036505A (zh) * 2015-09-06 2015-11-11 中国农业大学 一种处理脱水污泥的干发酵装置

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003039099A (ja) * 2001-07-27 2003-02-12 Mitsubishi Heavy Ind Ltd メタン発酵槽
CN102242052B (zh) * 2011-02-25 2016-06-08 上海济兴能源环保技术有限公司 水平折流式干法厌氧发酵反应装置
CN103243019A (zh) * 2012-02-03 2013-08-14 彭世英 生活有机垃圾和污泥生产生物能源的装置及工艺
CN104326636B (zh) * 2014-09-22 2016-08-24 同济大学 一种能控制氧化还原电位促进污泥干法厌氧发酵的装置及方法
CN104276737B (zh) * 2014-10-13 2016-07-06 南京国能环保工程有限公司 一种能源输出型污水污泥处理方法
CN104402182B (zh) * 2014-11-18 2017-01-11 泰州明锋资源再生科技有限公司 用于污泥处理的厌氧发酵池

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6673247B2 (en) * 2000-10-13 2004-01-06 Fkc Co., Ltd. Sludge dewatering and pasteurization process
CN201074232Y (zh) * 2007-08-11 2008-06-18 谷宗华 移动式沼气发生器
CN101921049A (zh) * 2010-09-21 2010-12-22 同济大学 一种城市污泥及有机质干法厌氧发酵产沼气的方法及装置
CN104150726A (zh) * 2014-07-25 2014-11-19 中国环境科学研究院 一种减量化的污泥处理装置及污泥干化方法
CN204550355U (zh) * 2015-03-30 2015-08-12 中和利华投资管理（北京）有限公司 一种污泥高负荷厌氧消化备料调节系统
CN105036505A (zh) * 2015-09-06 2015-11-11 中国农业大学 一种处理脱水污泥的干发酵装置

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107935345A (zh) * 2017-12-28 2018-04-20 杨建� 一种生活污泥厌氧消化处理培育有机营养土的方法及系统
CN108641941A (zh) * 2018-06-04 2018-10-12 榆林学院 一种用于发酵腐殖酸的装置
CN108441414A (zh) * 2018-06-21 2018-08-24 农业部规划设计研究院 一种厌氧干发酵渗滤液流动特性测试装置及测试方法
CN108441414B (zh) * 2018-06-21 2023-11-17 农业部规划设计研究院 一种厌氧干发酵渗滤液流动特性测试装置及测试方法
CN109182120A (zh) * 2018-10-22 2019-01-11 中霖华夏农业科技发展有限公司 一种发酵装置
CN110437985A (zh) * 2019-07-17 2019-11-12 光大环保技术研究院（南京）有限公司 一种干式厌氧反应器
CN113414225A (zh) * 2021-06-30 2021-09-21 重庆市环卫集团有限公司 干式厌氧消化及罐底除砂系统
CN113956930A (zh) * 2021-11-30 2022-01-21 宁波沪港食品机械制造有限公司 一种啤酒发酵罐
CN114988655A (zh) * 2022-05-16 2022-09-02 福建源固节能环保科技有限公司 污泥可降解金属离子处置方法
CN114988655B (zh) * 2022-05-16 2023-12-08 福建源固节能环保科技有限公司 污泥可降解金属离子处置方法

Also Published As

Publication number Publication date
CN105417912A (zh) 2016-03-23
CN105417912B (zh) 2018-07-27

Similar Documents

Publication Publication Date Title
WO2017096657A1 (zh) 一种脱水污泥厌氧干发酵的装置
CN103627621B (zh) 固态立式发酵、自循环冷却、蒸馏一体化装置及方法
CN103624066B (zh) 一种半干式餐厨垃圾连续处理系统及其处理方法
CN108456633B (zh) 一种高固含有机废弃物序进式厌氧发酵装置
CN206244781U (zh) 一种餐厨垃圾高温厌氧发酵装置
CN107815409A (zh) 一种太阳能辅助沼气发酵装置
CN102604816B (zh) 一种一体化固体物料两相沼气发酵反应器及其制备沼气的方法
CN208883890U (zh) 一体化三相干式厌氧发酵自适应设备
CN205528747U (zh) 一种实验室用发酵装置
CN108753609A (zh) 一体化三相干式厌氧发酵自适应设备及其产沼气方法
CN104109632B (zh) 一种大型外驱动整体卧式旋转连续沼气干式发酵装置及方法
WO2017152476A1 (zh) 大型自旋式夹层加温充气发酵罐
CN103387932B (zh) 干式厌氧反应处理装置
CN205576158U (zh) 一种固液两阶段厌氧发酵装置
CN112209500A (zh) 一种垃圾与污水联合发酵处理沼气池
CN105624033A (zh) 一种有机垃圾干式厌氧发酵装置
CN201062264Y (zh) 立式机械搅拌沼气装置
CN219079369U (zh) 一种鸡粪堆肥发酵搅拌装置
CN106190811A (zh) 一种两相厌氧发酵自搅拌反应装置
CN2923711Y (zh) 卧式机械搅拌沼气装置
CN105985902A (zh) 一种内循环式干式厌氧反应装置
CN106883984B (zh) 一种木质纤维素物料高效产甲烷装置及方法
CN214327584U (zh) 利用粪便无害化生产有机肥设备
CN102060425B (zh) 一种高固体含量干清猪粪的酸化设备及方法
CN205990394U (zh) 一种卧式沼气发酵装置

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15910131

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

32PN Ep: public notification in the ep bulletin as address of the adressee cannot be established

Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC (EPO FORM 1205 DATED 01/10/2018)

122 Ep: pct application non-entry in european phase

Ref document number: 15910131

Country of ref document: EP

Kind code of ref document: A1