CN104492331A - Activated carbon feeding device and activated carbon feeding method - Google Patents
Activated carbon feeding device and activated carbon feeding method Download PDFInfo
- Publication number
- CN104492331A CN104492331A CN201410805316.8A CN201410805316A CN104492331A CN 104492331 A CN104492331 A CN 104492331A CN 201410805316 A CN201410805316 A CN 201410805316A CN 104492331 A CN104492331 A CN 104492331A
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid separator
- charcoal
- jet pump
- tank
- 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.)
- Granted
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明公开了一种活性炭投加装置及方法,包括一个浆液罐、射流泵和气液分离器,在所述的浆液罐的外部设有与其内部相连通的料仓,所述的射流泵的吸气口通过抽气管与炭浆罐的顶部相连通,所述射流泵的出水管插入到气液分离器中,且出水管延伸到气液分离器的下部,所述气液分离器固定在炭浆罐上,气液分离器的底部位于炭浆罐内液面之下,气液分离器的顶部位于炭浆罐顶盖之上,其与大气连通。
The invention discloses an activated carbon dosing device and method, comprising a slurry tank, a jet pump and a gas-liquid separator, a silo connected to the inside of the slurry tank is provided outside the slurry tank, and the suction pump of the jet pump The air port is connected to the top of the carbon slurry tank through the air extraction pipe, the outlet pipe of the jet pump is inserted into the gas-liquid separator, and the outlet pipe extends to the lower part of the gas-liquid separator, and the gas-liquid separator is fixed on the carbon On the slurry tank, the bottom of the gas-liquid separator is located below the liquid level in the slurry tank, and the top of the gas-liquid separator is located above the top cover of the slurry tank, which communicates with the atmosphere.
Description
技术领域technical field
本发明涉及一种活性炭投加装置,特别涉及粉末活性炭的活性炭投加装置。The invention relates to an activated carbon dosing device, in particular to an activated carbon dosing device for powdered activated carbon.
背景技术Background technique
为改善水质口感,目前我国自来水已陆续采用活性炭吸附工艺来去除季节性产生的霉味等异臭、异味,以及去除水中的有机物、表面活性剂、农药中的微污染物、水藻、工业重金属污染等。采用活性炭吸附工艺处理自来水主要有两种方式,一是自来水经过颗粒状活性炭吸附池,这种方式的缺点是颗粒状活性炭随时间加长吸附能力下降,需要定期更换;一种是根据水量的变化向活性炭吸附池中连续投加相应数量的粉末状活性炭粉,这种方式的好处是能根据水量和水质的变化随时来改变活性炭的投加量,处理水质效果好,其缺点是粉末活性炭在投加过程中容易有扬尘而影响现场操作人员身体健康和环境污染的问题。In order to improve the taste of water quality, at present, my country's tap water has successively adopted activated carbon adsorption technology to remove seasonal musty and other odors and odors, as well as to remove organic matter, surfactants, micro-pollutants in pesticides, algae, and industrial heavy metal pollution in water. wait. There are two main ways to treat tap water with activated carbon adsorption process. One is that tap water passes through the granular activated carbon adsorption pool. The disadvantage of this method is that the adsorption capacity of granular activated carbon decreases with time and needs to be replaced regularly; The corresponding amount of powdered activated carbon powder is continuously added to the activated carbon adsorption tank. The advantage of this method is that the dosage of activated carbon can be changed at any time according to the change of water quantity and water quality, and the effect of treating water quality is good. The disadvantage is that the powdered activated carbon is added. During the process, it is easy to raise dust and affect the health of on-site operators and environmental pollution.
粉末状活性炭投加装置一般由活性炭料仓、螺旋输送机、炭浆罐、给水管、搅拌器、输送泵组成。其工作流程一般为:炭粉首先通过螺旋输送机由料仓计量后输送至炭浆罐,炭粉输入与进水同步,在炭粉进入炭浆罐的同时给水管向炭浆罐内输入相应量的清水用于溶解炭粉,在搅拌器的作用下,炭粉溶在水中承悬浮状态,输送泵由炭浆罐中将活性炭悬浮液输送到活性炭吸附池中。在炭粉和水同时进入炭浆罐的时候,由于粉末活性炭颗粒微小,极其产生扬尘,造成炭粉从炭浆罐的搅拌轴、炭粉投加口等处溢出,造成环境污染。The powdered activated carbon dosing device is generally composed of activated carbon silo, screw conveyor, carbon slurry tank, water supply pipe, agitator, and delivery pump. The working process is generally as follows: the carbon powder is firstly measured by the screw conveyor from the silo and then transported to the carbon slurry tank. The input of the carbon powder is synchronized with the water intake. A large amount of clean water is used to dissolve the carbon powder. Under the action of the agitator, the carbon powder is dissolved in the water and suspended. The delivery pump transports the activated carbon suspension from the carbon slurry tank to the activated carbon adsorption tank. When the carbon powder and water enter the carbon slurry tank at the same time, due to the tiny particles of powdered activated carbon, dust is extremely generated, causing the carbon powder to overflow from the stirring shaft of the carbon slurry tank, the carbon powder feeding port, etc., causing environmental pollution.
为了解决炭粉外溢问题,现有技术采取的措施主要有如下几种:In order to solve the problem of carbon powder spillage, the measures taken in the prior art mainly contain the following:
一种方式是在炭浆罐上设置填料吸收器,吸收器上方喷自来水润湿填料,炭粉在溢出时被填料部分吸收;一种方式是螺旋输送机将炭粉直接输送到炭浆罐内的液面以下,减少炭粉在液面上方的扩散;还有一种方式是在炭浆罐上设置粉尘过滤器。由于炭粉和溶解水进入炭浆罐时,罐内空间急剧减小,罐内空气需要快速排出,悬浮在炭浆罐内空气中的炭粉就会随排出气流流出关外,这个原因造成现有这些方式都未能彻底解决炭粉在投加过程中的外溢污染问题。One way is to install a filler absorber on the carbon slurry tank, spray tap water above the absorber to wet the filler, and the carbon powder will be absorbed by the filler when it overflows; one way is to directly transport the carbon powder into the carbon slurry tank by the screw conveyor Below the liquid level, reduce the diffusion of carbon powder above the liquid level; Another way is to install a dust filter on the carbon slurry tank. When the carbon powder and dissolved water enter the carbon slurry tank, the space in the tank decreases sharply, and the air in the tank needs to be discharged quickly, and the carbon powder suspended in the air in the carbon slurry tank will flow out of the customs with the exhaust air flow. This reason causes the existing These methods have failed to completely solve the problem of overflow pollution of carbon powder during the dosing process.
为了解决炭粉的外溢问题,也有在炭浆罐上设置布袋除尘器的,其工作原理是布袋除尘器一端连接炭浆罐,另一端连接抽气风机,工作时,风机启动抽气,炭浆罐内含有活性炭粉尘颗粒的空气在风机的抽吸作用下沿布袋除尘器进入风机中,气体在经过布袋除尘器时,细颗粒粉尘经滤袋过滤后,吸咐在滤袋的内壁上,净化后的气体经袋滤,吸入风机内,再经排气筒排入大气中。布袋除尘器在工业上大多应用在去除锅炉烟气中的粉煤灰等干燥气体中的细颗粒粉尘,当滤袋附尘不断增加,阻力上升到一定值时,可以通过吹风、震动等方式清除吸附在滤袋上的灰尘,使滤袋恢复正常使用状态。将布袋除尘器应用在活性炭投加装置上的一个非常大的弊端是,风机从炭浆罐抽出的气体中含有大量水分,使活性炭颗粒变潮湿后粘附在滤袋上不容易被清除下来,滤袋气体阻力越来越大,必须频繁更换滤袋,这种方式一方面需要风机引风,一方面需要频繁更换滤袋,在实际使用中运行成本高,不切实际。In order to solve the overflow problem of carbon powder, there is also a bag filter installed on the carbon slurry tank. Its working principle is that one end of the bag filter is connected to the carbon slurry tank, and the other end is connected to the exhaust fan. The air containing activated carbon dust particles in the tank enters the fan along the bag filter under the suction of the fan. When the gas passes through the bag filter, the fine particle dust is filtered by the filter bag and adsorbed on the inner wall of the filter bag for purification. The final gas is filtered by the bag, sucked into the fan, and then discharged into the atmosphere through the exhaust tube. Bag dust collectors are mostly used in industry to remove fine particles of dust in dry gases such as fly ash in boiler flue gas. When the dust attached to the filter bag continues to increase and the resistance rises to a certain value, it can be removed by blowing, shaking, etc. The dust adsorbed on the filter bag restores the filter bag to normal use. A very big disadvantage of applying the bag filter to the activated carbon dosing device is that the gas drawn by the fan from the carbon slurry tank contains a lot of water, which makes the activated carbon particles stick to the filter bag after becoming wet and is not easy to be removed. The gas resistance of the filter bag is getting bigger and bigger, and the filter bag must be replaced frequently. On the one hand, this method requires a fan to induce air, and on the other hand, it requires frequent replacement of the filter bag. In actual use, the operating cost is high and it is impractical.
发明内容Contents of the invention
针对现有技术中存在的上述缺陷,本发明提供了一种结构更加简单、可彻底解决炭粉外溢的活性炭投加装置。In view of the above-mentioned defects in the prior art, the present invention provides an activated carbon dosing device with a simpler structure, which can completely solve the overflow of carbon powder.
本发明采用的技术方案如下:The technical scheme that the present invention adopts is as follows:
一种活性炭投加装置,包括一个浆液罐、射流泵和气液分离器,在所述的浆液罐的外部设有与其内部相连通的料仓,所述的射流泵的吸气口通过抽气管与炭浆罐的顶部相连通,所述射流泵的出水管插入到气液分离器中,使炭浆罐内形成负压,所述气液分离器固定在炭浆罐上,气液分离器的底部位于炭浆罐内液面之下,气液分离器的顶部位于炭浆罐顶盖之上,其与大气连通。An activated carbon dosing device, comprising a slurry tank, a jet pump and a gas-liquid separator, a hopper connected to the inside of the slurry tank is provided outside the slurry tank, and the suction port of the jet pump connects with the suction port through a suction pipe. The top of the carbon slurry tank is connected, and the outlet pipe of the jet pump is inserted into the gas-liquid separator to form a negative pressure in the carbon slurry tank. The gas-liquid separator is fixed on the carbon slurry tank, and the gas-liquid separator The bottom is located below the liquid level in the carbon slurry tank, and the top of the gas-liquid separator is located on the top cover of the carbon slurry tank, which communicates with the atmosphere.
一种活性炭投加装置,包括一个浆液罐、射流泵和气液分离器,在所述的浆液罐的外部设有与其内部相连通的料仓,所述的射流泵的吸气口通过抽气管与炭浆罐的顶部相连通,使炭浆罐内形成负压,所述射流泵的出水管插入到气液分离器中,所述气液分离器位于炭浆罐外部,气液分离器与炭浆罐通过连通管相连通,气液分离器的底部位于炭浆罐内液面之下,气液分离器的顶部位于炭浆罐顶盖之上,其与大气连通。An activated carbon dosing device, comprising a slurry tank, a jet pump and a gas-liquid separator, a hopper connected to the inside of the slurry tank is provided outside the slurry tank, and the suction port of the jet pump connects with the suction port through a suction pipe. The top of the carbon slurry tank is connected to form a negative pressure in the carbon slurry tank, and the outlet pipe of the jet pump is inserted into the gas-liquid separator, which is located outside the carbon slurry tank. The slurry tanks are connected through communication pipes, the bottom of the gas-liquid separator is located below the liquid level in the slurry tank, and the top of the gas-liquid separator is located on the top cover of the slurry tank, which communicates with the atmosphere.
所述的气液分离器内部有填料。There is packing inside the gas-liquid separator.
所述的浆液罐内设有对其内部液体进行搅拌的搅拌装置。The slurry tank is provided with a stirring device for stirring the liquid inside.
所述的射流泵的进水管设有一个控制进水量的阀门。The water inlet pipe of the jet pump is provided with a valve for controlling the water inlet.
所述的活性炭投加装置进行活性炭投加的方法,如下:The method for adding activated carbon to the activated carbon dosing device is as follows:
炭粉通过螺旋输送机由料仓计量后输送至炭浆罐,进水依次经射流泵、气液分离器、气液分离器与炭浆罐的连通管后进入炭浆罐,炭粉输入与进水同步,在进水流经射流泵时,射流泵进口吸气,炭浆罐内的空气被吸进射流泵中,炭浆罐内部处于微负压状态,悬浮在空气中的炭粉连同空气一同被吸入射流泵中与水充分混合后进入气液分离器,空气在气液分离器中实现与水的分离后排出,与水充分混合后的炭粉随水流经气液分离器与炭浆罐的连通管后进入炭浆罐。The carbon powder is metered from the silo by the screw conveyor and then transported to the carbon slurry tank. The water enters the carbon slurry tank through the jet pump, gas-liquid separator, gas-liquid separator and the connecting pipe of the carbon slurry tank in turn. The carbon powder input and The water inlet is synchronized. When the water flows through the jet pump, the inlet of the jet pump sucks air, and the air in the carbon slurry tank is sucked into the jet pump. The inside of the carbon slurry tank is in a state of slight negative pressure. They are sucked into the jet pump and fully mixed with water and then enter the gas-liquid separator. The air is separated from the water in the gas-liquid separator and then discharged. The carbon powder mixed with water flows through the gas-liquid separator and carbon slurry with the water. The connecting pipe of the tank enters the carbon slurry tank.
本发明的有益效果是:The beneficial effects of the present invention are:
本发明中,由于射流泵吸气口与炭浆罐相连通,射流泵出口与气液分离器相连通,炭浆罐和气液分离器相连通,此结构改变了现有活性炭投加装置的工作流程。一方面本发明通过射流泵的抽吸作用使炭浆罐内形成微负压,解决了炭浆罐内的炭粉通过搅拌杆、炭粉投加口等处外溢的问题;另一方面由于射流泵具有抽吸和混合双重作用,使进入射流泵内的炭粉与水流激烈碰撞混合,水分子快速浸湿活性炭颗粒,形成稳定的活性炭悬浮液,解决了从炭浆罐抽出的微量炭粉的再次扬尘问题;In the present invention, since the suction port of the jet pump is connected with the carbon slurry tank, the outlet of the jet pump is connected with the gas-liquid separator, and the carbon slurry tank is connected with the gas-liquid separator, this structure changes the work of the existing activated carbon dosing device. process. On the one hand, the present invention forms a slight negative pressure in the carbon slurry tank through the suction of the jet pump, which solves the problem that the carbon powder in the carbon slurry tank overflows through the stirring rod, the carbon powder feeding port, etc.; The pump has dual functions of suction and mixing, so that the carbon powder entering the jet pump collides and mixes violently with the water flow, and the water molecules quickly soak the activated carbon particles to form a stable activated carbon suspension, which solves the problem of a small amount of carbon powder drawn from the carbon slurry tank. Dust problem again;
其次,进入射流泵使其实现抽气作用所需要的水,利用的是进入炭浆罐内溶解活性炭的溶解水,无需消耗额外的能源和水源,解决了现有处理方式需要风机抽吸消耗能源或喷淋水消耗水源的问题;Secondly, the water needed to enter the jet pump to achieve the pumping effect is to use the dissolved water that enters the carbon slurry tank to dissolve the activated carbon, without consuming additional energy and water sources, which solves the need for fan suction to consume energy in the existing treatment methods Or the problem of water consumption by spraying water;
另外,通过射流泵出水管插入到气液分离器中、气液分离器的上口与大气连通和气液分离器的下排放口位于碳浆罐内液面之下这种结构设计,使射流泵出水管中的混合液首先流入气液分离器中,在气液分离器中实现气液分离,混合液中的气体上浮,经气液分离器的上口排入大气中;混合液中含有碳粉颗粒的水向下流动,经气液分离器的下排放口流入碳浆罐内。解决了从炭浆罐抽出的空气的洁净排空问题,同时使被吸入射流泵的炭粉重新进入炭浆罐中。In addition, the outlet pipe of the jet pump is inserted into the gas-liquid separator, the upper port of the gas-liquid separator communicates with the atmosphere, and the lower discharge port of the gas-liquid separator is located below the liquid level in the carbon slurry tank. This structural design makes the jet pump The mixed liquid in the outlet pipe first flows into the gas-liquid separator, and the gas-liquid separation is realized in the gas-liquid separator. The gas in the mixed liquid floats up and is discharged into the atmosphere through the upper port of the gas-liquid separator; the mixed liquid contains carbon The water of the powder particles flows downward, and flows into the carbon slurry tank through the lower discharge port of the gas-liquid separator. The problem of clean emptying of the air extracted from the carbon slurry tank is solved, and at the same time, the carbon powder sucked into the jet pump re-enters the carbon slurry tank.
与现有技术相比,本发明结构更加简单,操作也更加简单,制造成本低,有利于该装置的推广应用。Compared with the prior art, the present invention has simpler structure, simpler operation and lower manufacturing cost, which is beneficial to popularization and application of the device.
本发明除适用于活性炭外,也可以适用于石灰粉等粉末性物质的浆液制备。In addition to being applicable to activated carbon, the present invention can also be applied to slurry preparation of powdery substances such as lime powder.
附图说明Description of drawings
图1是本发明实施例1的结构示意图;Fig. 1 is the structural representation of embodiment 1 of the present invention;
图2是本发明实施例2的结构示意图;Fig. 2 is the structural representation of embodiment 2 of the present invention;
图中,1、料仓,2、输送机,3、炭浆罐,4、输送泵,5、搅拌器,6、抽气管,7、进水阀,8、进水管,9、射流泵,10、出水管,11、气液分离器,12、连通管。In the figure, 1. feed bin, 2. conveyor, 3. carbon slurry tank, 4. transfer pump, 5. agitator, 6. exhaust pipe, 7. water inlet valve, 8. water inlet pipe, 9. jet pump, 10. Outlet pipe, 11. Gas-liquid separator, 12. Connecting pipe.
具体实施方式detailed description
下面通过具体实施例并结合附图对本发明作进一步的说明:Below by specific embodiment and in conjunction with accompanying drawing, the present invention will be further described:
实施例1Example 1
如附图1所示,一种活性炭投加装置,其包带有抽气管6的炭浆罐3、射流泵8和气液分离器11,射流泵吸气口通过抽气管6与炭浆罐3相连通,射流泵出水管9插入到气液分离器11中,气液分离器11固定在炭浆罐3上,气液分离器11的底部位于炭浆罐3内液面之下,气液分离器11的顶部位于炭浆罐3顶盖之上。As shown in accompanying drawing 1, a kind of activated carbon dosing device, it packs the charcoal slurry tank 3, jet pump 8 and gas-liquid separator 11 with exhaust pipe 6, and jet pump suction port passes through exhaust tube 6 and carbon slurry tank 3 Connected, the jet pump outlet pipe 9 is inserted into the gas-liquid separator 11, the gas-liquid separator 11 is fixed on the carbon slurry tank 3, the bottom of the gas-liquid separator 11 is located below the liquid level in the carbon slurry tank 3, and the gas-liquid The top of the separator 11 is located on the top cover of the carbon slurry tank 3 .
本实施例的工作过程是:The working process of this embodiment is:
当炭浆罐3内的液位达到一定位置需要进料时,输送机3和进水阀7同时打开,炭粉通过螺旋输送机3由料仓1计量后输送至炭浆罐3,清水由进水阀7、进水管8依次通过射流泵9、气液分离器11进入炭浆罐3,在清水流经射流泵9时,射流泵9内部形成射流抽吸作用,将碳浆罐3内的含有悬浮炭粉颗粒的空气经抽气管6抽吸进入射流泵9,在射流泵9内与高速水流激烈混合形成混合液进入到气液分离器11中,在气液分离器11中空气上浮由气液分离器11的顶部排出,混合液中的炭粉随水流进入到炭浆罐3中。当炭浆罐3内的液面达到一定液位时,输送机3关闭,进水阀7延时几分钟后关闭。如此往复循环。在此过程中,炭浆罐3内始终处于微负压状态,没有炭粉颗粒进入空气中。在炭浆罐3内有炭粉混合浆时,输送泵4向外定量输送炭粉混合浆至活性炭吸附池中。When the liquid level in the carbon slurry tank 3 reaches a certain position and needs to be fed, the conveyor 3 and the water inlet valve 7 are opened at the same time, and the carbon powder is transported to the carbon slurry tank 3 after being metered by the silo 1 through the screw conveyor 3, and the clean water is delivered to the carbon slurry tank 3. The water inlet valve 7 and the water inlet pipe 8 enter the carbon slurry tank 3 through the jet pump 9 and the gas-liquid separator 11 in sequence. The air containing suspended carbon powder particles is sucked into the jet pump 9 through the suction pipe 6, and is violently mixed with the high-speed water flow in the jet pump 9 to form a mixed liquid that enters the gas-liquid separator 11, and the air floats in the gas-liquid separator 11 Discharged from the top of the gas-liquid separator 11, the carbon powder in the mixed liquid enters the carbon slurry tank 3 with the water flow. When the liquid level in the carbon slurry tank 3 reached a certain liquid level, the conveyor 3 was closed, and the water inlet valve 7 was closed after a few minutes of delay. And so on and on. During this process, the carbon slurry tank 3 is always in a slight negative pressure state, and no carbon powder particles enter the air. When there is carbon powder mixed slurry in the carbon slurry tank 3, the delivery pump 4 quantitatively transports the carbon powder mixed slurry to the activated carbon adsorption pool.
本发明使炭粉通过输送机进入炭浆罐时,炭浆罐3内始终处于微负压状态,较好地解决了炭粉的外溢问题。In the present invention, when the charcoal powder enters the charcoal pulp tank through the conveyor, the interior of the charcoal pulp tank 3 is always in a state of slight negative pressure, which better solves the problem of charcoal powder overflowing.
本实施例中的其他部分采用现有技术,在此不再赘述。Other parts in this embodiment adopt the prior art, and will not be repeated here.
实施例2Example 2
如附图2所示,本实施例与实施例1基本相同,不同之处是,本实施例中气液分离器11位于炭浆罐3外部,气液分离器11与炭浆罐3通过连通管12相连通。As shown in accompanying drawing 2, present embodiment is basically the same as embodiment 1, and difference is, in the present embodiment, gas-liquid separator 11 is positioned at the outside of carbon slurry tank 3, and gas-liquid separator 11 communicates with carbon slurry tank 3 Tube 12 communicates with each other.
本实施例的工作过程是:当炭浆罐3内的液位达到一定位置需要进料时,输送机3和进水阀7同时打开,炭粉通过螺旋输送机3由料仓1计量后输送至炭浆罐3,清水由进水阀7、进水管8依次通过射流泵9、气液分离器11进入炭浆罐3,在清水流经射流泵9时,射流泵9内部形成射流抽吸作用,将碳浆罐3内的含有悬浮炭粉颗粒的空气经抽气管6抽吸进入射流泵9,在射流泵9内与高速水流激烈混合形成混合液进入到气液分离器11中,在气液分离器11中空气上浮由气液分离器11的顶部排出,混合液中的炭粉随水流通过连通管12进入到炭浆罐3中。The working process of this embodiment is: when the liquid level in the carbon slurry tank 3 reaches a certain position and needs to be fed, the conveyor 3 and the water inlet valve 7 are opened at the same time, and the carbon powder is transported by the screw conveyor 3 after being measured by the silo 1 To the carbon slurry tank 3, the clean water enters the carbon slurry tank 3 through the water inlet valve 7 and the water inlet pipe 8 through the jet pump 9 and the gas-liquid separator 11 in turn. When the clean water flows through the jet pump 9, a jet suction is formed inside the jet pump 9 Function, the air containing suspended carbon powder particles in the carbon slurry tank 3 is sucked into the jet pump 9 through the suction pipe 6, and is violently mixed with the high-speed water flow in the jet pump 9 to form a mixed liquid that enters the gas-liquid separator 11. The air in the gas-liquid separator 11 floats up and is discharged from the top of the gas-liquid separator 11, and the carbon powder in the mixed liquid enters the carbon slurry tank 3 through the connecting pipe 12 along with the water flow.
本实施例中的其他部分与实施例1相同,在此不再赘述。Other parts in this embodiment are the same as those in Embodiment 1, and will not be repeated here.
实施例3Example 3
如附图1或2所示,本实施例与实施例1或2基本相同,不同之处是,本实施例中气液分离器11内部有填料,其可起到平稳排出气流,进一步清洁空气的作用。As shown in Figure 1 or 2, this embodiment is basically the same as Embodiment 1 or 2, the difference is that there is a filler inside the gas-liquid separator 11 in this embodiment, which can play a role in stabilizing the exhaust airflow and further cleaning the air role.
上述虽然结合附图对本发明的具体实施方式进行了描述,但并非对本发明保护范围的限制,所属领域技术人员应该明白,在本发明的技术方案的基础上,本领域技术人员不需要付出创造性劳动即可做出的各种修改或变形仍在本发明的保护范围以内。Although the specific implementation of the present invention has been described above in conjunction with the accompanying drawings, it does not limit the protection scope of the present invention. Those skilled in the art should understand that on the basis of the technical solution of the present invention, those skilled in the art do not need to pay creative work Various modifications or variations that can be made are still within the protection scope of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410805316.8A CN104492331B (en) | 2014-12-22 | 2014-12-22 | Activated carbon feeding device and activated carbon feeding method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410805316.8A CN104492331B (en) | 2014-12-22 | 2014-12-22 | Activated carbon feeding device and activated carbon feeding method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104492331A true CN104492331A (en) | 2015-04-08 |
CN104492331B CN104492331B (en) | 2017-02-22 |
Family
ID=52933834
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410805316.8A Active CN104492331B (en) | 2014-12-22 | 2014-12-22 | Activated carbon feeding device and activated carbon feeding method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104492331B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106693827A (en) * | 2017-03-06 | 2017-05-24 | 上海诺固恩机械设备有限公司 | Activated carbon dosing system |
CN106984203A (en) * | 2017-04-26 | 2017-07-28 | 邯钢集团邯宝钢铁有限公司 | A kind of lime dissolving tank |
CN113209903A (en) * | 2021-04-16 | 2021-08-06 | 合肥楚航环保设备有限公司 | Closed powdered activated carbon feeding device |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5733776A (en) * | 1993-11-09 | 1998-03-31 | Genzyme Corporation | Continuous settling apparatus |
WO2008010721A1 (en) * | 2006-07-04 | 2008-01-24 | Heggset Teknologi As | A method and device for admixture of powder in a liquid |
CN202161928U (en) * | 2011-06-24 | 2012-03-14 | 上虞帝瑞云涛化工有限公司 | Activated carbon wetting device |
CN202460545U (en) * | 2012-02-03 | 2012-10-03 | 上海巴安水务股份有限公司 | Automatic preparing and adding device for powdery powdered activated carbon |
CN103736411A (en) * | 2013-12-06 | 2014-04-23 | 珠海市长陆工业自动控制系统有限公司 | Self-cleaning dust-free powder measurement conveying feeding system |
CN203648480U (en) * | 2013-10-10 | 2014-06-18 | 徐州天正活性炭厂 | Activated carbon homogenizing device |
CN203710962U (en) * | 2014-02-28 | 2014-07-16 | 金川集团股份有限公司 | Aluminum powder suspension preparation device |
CN204352818U (en) * | 2014-12-22 | 2015-05-27 | 山东大学 | A kind of activated charcoal adding apparatus |
-
2014
- 2014-12-22 CN CN201410805316.8A patent/CN104492331B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5733776A (en) * | 1993-11-09 | 1998-03-31 | Genzyme Corporation | Continuous settling apparatus |
WO2008010721A1 (en) * | 2006-07-04 | 2008-01-24 | Heggset Teknologi As | A method and device for admixture of powder in a liquid |
CN202161928U (en) * | 2011-06-24 | 2012-03-14 | 上虞帝瑞云涛化工有限公司 | Activated carbon wetting device |
CN202460545U (en) * | 2012-02-03 | 2012-10-03 | 上海巴安水务股份有限公司 | Automatic preparing and adding device for powdery powdered activated carbon |
CN203648480U (en) * | 2013-10-10 | 2014-06-18 | 徐州天正活性炭厂 | Activated carbon homogenizing device |
CN103736411A (en) * | 2013-12-06 | 2014-04-23 | 珠海市长陆工业自动控制系统有限公司 | Self-cleaning dust-free powder measurement conveying feeding system |
CN203710962U (en) * | 2014-02-28 | 2014-07-16 | 金川集团股份有限公司 | Aluminum powder suspension preparation device |
CN204352818U (en) * | 2014-12-22 | 2015-05-27 | 山东大学 | A kind of activated charcoal adding apparatus |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106693827A (en) * | 2017-03-06 | 2017-05-24 | 上海诺固恩机械设备有限公司 | Activated carbon dosing system |
CN106984203A (en) * | 2017-04-26 | 2017-07-28 | 邯钢集团邯宝钢铁有限公司 | A kind of lime dissolving tank |
CN113209903A (en) * | 2021-04-16 | 2021-08-06 | 合肥楚航环保设备有限公司 | Closed powdered activated carbon feeding device |
Also Published As
Publication number | Publication date |
---|---|
CN104492331B (en) | 2017-02-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN205820929U (en) | A kind of Powdered Activated Carbon wet method automatic dilution adds unit and wet method throwing device | |
CN204602792U (en) | For the drip washing prosthetic device that agriculture heavy-metal contaminated soil is repaired | |
CN103241791B (en) | A kind of with pre-dispersed and Powdered Activated Carbon dosing system that is Weighing mechanism | |
CN207478428U (en) | A kind of traffic water coating processes efficient evenly mixing device | |
CN202460545U (en) | Automatic preparing and adding device for powdery powdered activated carbon | |
CN106178843B (en) | A kind of packed absorber | |
CN104492331B (en) | Activated carbon feeding device and activated carbon feeding method | |
CN204638708U (en) | The drip washing prosthetic device of drum-type contaminated soil | |
CN206937645U (en) | A kind of agitating device of concrete liquid additive | |
CN209491167U (en) | A kind of soil restoring device | |
CN204352818U (en) | A kind of activated charcoal adding apparatus | |
CN108295607A (en) | A kind of mechanical engineering powdery castoff processing system | |
CN105161156B (en) | A method and reactor for treating radioactive wastewater in a mega-kilowatt nuclear power plant | |
CN106693827A (en) | Activated carbon dosing system | |
CN211358569U (en) | A medical nutritional powder mixing machine | |
CN102806029A (en) | Upper and lower double-cycle stirring dispensing process | |
CN204661530U (en) | Mud-water separation tank | |
CN105880154A (en) | Cement unpacking and filtering device | |
CN207509554U (en) | A feeding device for granulator | |
CN207998176U (en) | A kind of activated carbon feeding device | |
CN209900925U (en) | Smoke and dust exhaust gas purification device | |
CN209226986U (en) | Anaerobic reactor feed device | |
CN117046361B (en) | A device for wet dosing of powdered materials and water treatment method thereof | |
CN208839587U (en) | A kind of chlorinated paraffin energy conservation reaction unit | |
CN206297011U (en) | A kind of concrete central mix plant |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |