CN106110735A - A kind of liquid impurity segregation apparatus - Google Patents
A kind of liquid impurity segregation apparatus Download PDFInfo
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- CN106110735A CN106110735A CN201610687712.4A CN201610687712A CN106110735A CN 106110735 A CN106110735 A CN 106110735A CN 201610687712 A CN201610687712 A CN 201610687712A CN 106110735 A CN106110735 A CN 106110735A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/04—Filters with filtering elements which move during the filtering operation with filtering bands or the like supported on cylinders which are impervious for filtering
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/056—Construction of filtering bands or supporting belts, e.g. devices for centering, mounting or sealing the filtering bands or the supporting belts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/46—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element
- B01D33/466—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element scrapers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/48—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/70—Filters with filtering elements which move during the filtering operation having feed or discharge devices
- B01D33/72—Filters with filtering elements which move during the filtering operation having feed or discharge devices for feeding
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Abstract
本发明公开了一种液体杂质分离装置,其包括进液渠、传送轮和滤布清理机构,进液渠的上方设有向该进液渠输送待除杂液体的输入管,进液渠的渠底开口,并且渠底覆有滤布;滤布为环形;上述传送轮撑在环形的上述滤布内,并用于驱动滤布转动,以使滤布不断地沿进液渠的渠底移动;滤布清理结构用于在滤布转动过程中,清理其上未与进液渠槽底对应的部分的杂质。该液体杂质分离装置中,滤布在传动轮的作用下不断转动,使得其上与进液渠对应的部分进行过滤工作,而脱离进液渠的部分在滤布清理机构的作用下进行清洁,实现了过滤和清洁同时进行,无需停机清理滤布,利于液体除杂持续进行,提高效率。
The invention discloses a liquid impurity separation device, which comprises a liquid inlet channel, a transmission wheel and a filter cloth cleaning mechanism. An input pipe for delivering liquid to be removed to the liquid inlet channel is arranged above the liquid inlet channel. The bottom of the canal is open, and the bottom of the canal is covered with filter cloth; the filter cloth is ring-shaped; the above-mentioned transmission wheel is supported in the ring-shaped above-mentioned filter cloth, and is used to drive the filter cloth to rotate, so that the filter cloth is continuously moved along the bottom of the liquid inlet channel ; The filter cloth cleaning structure is used to clean up the impurities on the filter cloth not corresponding to the bottom of the liquid inlet channel during the rotation process of the filter cloth. In the liquid impurity separation device, the filter cloth is continuously rotated under the action of the transmission wheel, so that the part corresponding to the liquid inlet canal is filtered, and the part separated from the liquid inlet canal is cleaned under the action of the filter cloth cleaning mechanism. Filtration and cleaning can be carried out at the same time, and there is no need to stop the machine to clean the filter cloth, which is conducive to continuous liquid removal and improves efficiency.
Description
技术领域technical field
本发明涉及机械工业技术领域,更具体地说,涉及一种液体杂质分离装置。The invention relates to the technical field of machinery industry, more specifically, to a liquid impurity separation device.
背景技术Background technique
现有技术中,如生活废水、工业废水等液体需经过除杂处理才能进行排放或后续利用。In the prior art, liquids such as domestic wastewater and industrial wastewater need to undergo impurity removal treatment before they can be discharged or subsequently utilized.
但是,目前常用的液体除杂装置一般包括滤布,而经过长时间使用后滤布上沾染的杂质多,需使液体除杂装置停机并清洗滤布,影响液体除杂的进程。However, currently commonly used liquid impurity removal devices generally include filter cloth, and after a long period of use, the filter cloth is contaminated with impurities, and the liquid impurity removal device needs to be shut down to clean the filter cloth, which affects the process of liquid impurity removal.
综上所述,如何提供一种用于去除液体中杂质的装置,以避免其停机清洗滤布,是本领域技术人员亟待解决的技术问题。To sum up, how to provide a device for removing impurities in liquid so as to avoid shutting down the device to clean the filter cloth is a technical problem to be solved urgently by those skilled in the art.
发明内容Contents of the invention
有鉴于此,本发明提供一种液体杂质分离装置,其滤布为环形,能够在应用过程中不断转动,实现过滤和清洁同时进行,无需停机清洗滤布,便于液体除杂持续进行,提高效率。In view of this, the present invention provides a liquid impurity separation device. The filter cloth is ring-shaped and can be continuously rotated during the application process to achieve simultaneous filtration and cleaning without stopping the machine to clean the filter cloth, which facilitates continuous liquid impurity removal and improves efficiency. .
为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:
一种液体杂质分离装置,包括:A liquid impurity separation device, comprising:
进液渠,所述进液渠的上方设有向所述进液渠输送待除杂液体的输入管,所述进液渠的渠底开口,并且所述渠底覆有滤布;所述滤布为环形;The liquid inlet channel, the upper part of the liquid inlet channel is provided with an input pipe for transporting the liquid to be removed to the liquid inlet channel, the bottom of the liquid inlet channel is open, and the bottom of the channel is covered with filter cloth; The filter cloth is ring-shaped;
传送轮,所述传送轮撑在环形的所述滤布内,并用于驱动所述滤布转动,以使所述滤布不断地沿所述进液渠的渠底移动;A transmission wheel, the transmission wheel is supported in the ring-shaped filter cloth, and is used to drive the filter cloth to rotate, so that the filter cloth continuously moves along the bottom of the liquid inlet channel;
滤布清理机构,所述滤布清理结构用于在所述滤布转动过程中,清理其上未与所述进液渠槽底对应的部分的杂质。A filter cloth cleaning mechanism, the filter cloth cleaning structure is used to clean the impurities on the part of the filter cloth not corresponding to the bottom of the liquid inlet channel during the rotation process of the filter cloth.
优选的,上述液体杂质分离装置中,还包括多个转轮,所述转轮设置在所述进液渠下方,并且所述转轮与所述滤布相切接触;所述转轮能够在转动过程中产生负压;所述转轮的切线速度范围设置为0.8m/s-8m/s;或者Preferably, the above-mentioned liquid impurity separation device also includes a plurality of runners, the runners are arranged under the liquid inlet channel, and the runners are in tangential contact with the filter cloth; the runners can be Negative pressure is generated during rotation; the tangential speed range of the runner is set to 0.8m/s-8m/s; or
还包括多个静置中空轴,所述静置中空轴设置在所述进液渠下方,并与所述滤布相贴;所述静置中空轴上与滤布的接触面设有开口,其端面设置出口,用于通过所述开口和出口的导通实现抽吸液体,从而形成负压。It also includes a plurality of static hollow shafts, the static hollow shafts are arranged under the liquid inlet channel and attached to the filter cloth; the contact surface of the static hollow shafts with the filter cloth is provided with openings, An outlet is provided on the end surface, and is used for sucking liquid through the conduction between the opening and the outlet, so as to form a negative pressure.
优选的,上述液体杂质分离装置中,所述进液渠中渠底的第一端高于第二端;所述滤布上与所述渠底对应的部分呈倾斜的平板状结构。Preferably, in the above-mentioned liquid impurity separation device, the first end of the bottom of the liquid inlet channel is higher than the second end; the part of the filter cloth corresponding to the bottom of the channel has an inclined flat plate structure.
优选的,上述液体杂质分离装置中,所述滤布上与所述渠底对应的部分同水平方向的夹角为α,α的角度范围为0°-60°。Preferably, in the above liquid impurity separation device, the angle between the part of the filter cloth corresponding to the bottom of the canal and the horizontal direction is α, and the angle range of α is 0°-60°.
优选的,上述液体杂质分离装置中,所述滤布清理机构包括刮渣板、气冲洗系统和水冲洗系统;所述刮渣板与所述滤布的外侧相抵;所述气冲洗系统位于所述滤布的内侧,并用于向所述滤布沿朝向所述滤布外的方向喷射气体;所述水冲洗系统用于向所述滤布喷射水流。Preferably, in the above-mentioned liquid impurity separation device, the filter cloth cleaning mechanism includes a slag scraper, an air flushing system and a water flushing system; the scraper is against the outside of the filter cloth; the air flushing system is located at the The inner side of the filter cloth is used to spray gas to the filter cloth in a direction toward the outside of the filter cloth; the water flushing system is used to spray water to the filter cloth.
优选的,上述液体杂质分离装置中,所述滤布转过所述进液渠后先由所述气冲洗系统进行冲洗,再由所述水冲洗系统进行冲洗。Preferably, in the above-mentioned liquid impurity separation device, after the filter cloth passes through the liquid inlet channel, it is firstly washed by the air flushing system, and then washed by the water flushing system.
优选的,上述液体杂质分离装置中,所述进液渠的两侧分别固定有密封条,所述密封条与所述滤布相抵,并且所述密封条沿所述滤布的传送滤渣的方向布置。Preferably, in the above-mentioned liquid impurity separation device, sealing strips are respectively fixed on both sides of the liquid inlet channel, and the sealing strips are against the filter cloth, and the sealing strips are along the direction of conveying the filter residue of the filter cloth. layout.
优选的,上述液体杂质分离装置中,所述密封条上用于与所述滤布相抵的端面为圆弧面。Preferably, in the above-mentioned liquid impurity separation device, the end surface of the sealing strip for abutting against the filter cloth is an arc surface.
优选的,上述液体杂质分离装置中,所述传送轮包括主动轮和从动轮,并且所述主动轮的切线速度范围为0.01m/s-1.7m/s。Preferably, in the above liquid impurity separation device, the transmission wheel includes a driving wheel and a driven wheel, and the tangential speed of the driving wheel is in the range of 0.01m/s-1.7m/s.
优选的,上述液体杂质分离装置中,还包括滤布张紧装置和滤布纠偏装置,所述滤布张紧装置用于由所述滤布的内侧撑紧所述滤布;所述滤布纠偏装置用于调整所述滤布在所述传送轮上的位置。Preferably, the above-mentioned liquid impurity separation device further includes a filter cloth tensioning device and a filter cloth correction device, the filter cloth tensioning device is used to tighten the filter cloth from the inner side of the filter cloth; the filter cloth The deviation correcting device is used to adjust the position of the filter cloth on the transmission wheel.
优选的,上述液体杂质分离装置中,还包括集液槽和集废槽;所述集液槽设置在所述进液渠下方,用于盛装经所述滤布过滤的液体;所述集废槽用于收集所述滤布清理机构清除的杂质,以及由所述滤布与所述进液渠的渠底之间间隙泄露的液体。Preferably, the above-mentioned liquid impurity separation device further includes a liquid collection tank and a waste collection tank; the liquid collection tank is arranged under the liquid inlet channel, and is used to hold the liquid filtered by the filter cloth; the waste collection tank The groove is used to collect the impurities removed by the filter cloth cleaning mechanism and the liquid leaked from the gap between the filter cloth and the bottom of the liquid inlet channel.
本发明提供一种液体杂质分离装置,其包括进液渠、传送轮和滤布清理机构,进液渠的上方设有向该进液渠输送待除杂液体的输入管,进液渠的渠底开口,并且渠底覆有滤布;滤布为环形;上述传送轮撑在环形的上述滤布内,并用于驱动滤布转动,以使滤布不断地沿进液渠的渠底移动;滤布清理结构用于在滤布转动过程中,清理其上未与进液渠槽底对应的部分的杂质。The invention provides a liquid impurity separation device, which includes a liquid inlet channel, a transmission wheel and a filter cloth cleaning mechanism. An input pipe for transporting liquid to be removed to the liquid inlet channel is provided above the liquid inlet channel. The bottom is open, and the bottom of the canal is covered with filter cloth; the filter cloth is ring-shaped; the above-mentioned transmission wheel is supported in the ring-shaped above-mentioned filter cloth, and is used to drive the filter cloth to rotate, so that the filter cloth continuously moves along the bottom of the liquid inlet channel; The filter cloth cleaning structure is used to clean the impurities on the part of the filter cloth not corresponding to the bottom of the liquid inlet channel during the rotation process of the filter cloth.
上述液体杂质分离装置中,滤布在传动轮的作用下不断转动,使得其上与进液渠对应的部分进行过滤工作,而脱离进液渠的部分在滤布清理机构的作用下进行清洁,实现了过滤和清洁同时进行,无需停机清理滤布,利于液体除杂持续进行,提高效率。In the above-mentioned liquid impurity separation device, the filter cloth is continuously rotated under the action of the transmission wheel, so that the part corresponding to the liquid inlet channel is filtered, and the part separated from the liquid inlet channel is cleaned under the action of the filter cloth cleaning mechanism. Filtration and cleaning can be carried out at the same time, and there is no need to stop the machine to clean the filter cloth, which is conducive to continuous liquid removal and improves efficiency.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention. Those skilled in the art can also obtain other drawings based on these drawings without creative work.
图1为本发明实施例提供的液体杂质分离装置的结构示意图;Fig. 1 is a schematic structural diagram of a liquid impurity separation device provided by an embodiment of the present invention;
图2为本发明实施例提供的进液渠和密封条的装配示意图;Fig. 2 is a schematic diagram of the assembly of the liquid inlet channel and the sealing strip provided by the embodiment of the present invention;
图3为本发明实施例提供的密封条和滤布的装配示意图;Fig. 3 is the assembly diagram of sealing strip and filter cloth provided by the embodiment of the present invention;
图4为本发明实施例提供的静置中空轴的结构示意图;Fig. 4 is a schematic structural diagram of a static hollow shaft provided by an embodiment of the present invention;
图5为本发明实施例提供的滤布张紧装置的结构示意图;Fig. 5 is a structural schematic diagram of a filter cloth tensioning device provided by an embodiment of the present invention;
其中,图1-图5中:Among them, in Figure 1-Figure 5:
主体101;输入管102;进液渠103;密封条104;固定件34;静置中空轴105;开口151;出口152;主动轮106;从动轮162;滤布107;刮渣板181;喷气头182;喷水头183;滤布张紧装置109;张紧杠杆191;滚轮192;稳压气缸193;滤布纠偏装置110;集液槽111;集废槽112。Main body 101; input pipe 102; liquid inlet channel 103; sealing strip 104; fixing member 34; static hollow shaft 105; opening 151; outlet 152; driving wheel 106; driven wheel 162; filter cloth 107; slag scraping plate 181; air jet Head 182; water spray head 183; filter cloth tensioning device 109; tensioning lever 191; roller 192; pressure stabilizing cylinder 193;
具体实施方式detailed description
本发明实施例公开了一种液体杂质分离装置,其滤布为环形,能够在应用过程中不断转动,实现过滤和清洁同时进行,无需停机清洗滤布,便于液体除杂持续进行,提高效率。The embodiment of the invention discloses a liquid impurity separation device. The filter cloth is ring-shaped and can be continuously rotated during the application process to realize simultaneous filtering and cleaning without stopping the machine to clean the filter cloth, which facilitates continuous liquid impurity removal and improves efficiency.
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
请参阅图1-图5,本发明实施例提供一种液体杂质分离装置,其包括进液渠103、传送轮和滤布清理机构,进液渠103的上方设有向该进液渠103输送待除杂液体的输入管102,进液渠103的渠底开口,并且渠底覆有滤布107;滤布107为环形;上述传送轮撑在环形的上述滤布107内(“内”指滤布107组成的环内,相应的“外”表示滤布107组成的环外),并用于驱动滤布107转动,以使滤布107不断地沿进液渠103的渠底移动;滤布清理机构用于在滤布107转动过程中,清理滤布107上未与进液渠103槽底对应的部分的杂质。Please refer to Fig. 1-Fig. 5, the embodiment of the present invention provides a kind of liquid impurity separating device, and it comprises liquid inlet channel 103, transmission wheel and filter cloth cleaning mechanism, and the top of liquid inlet channel 103 is provided with this inlet channel 103 conveying The input pipe 102 of the liquid to be removed, the opening at the bottom of the liquid inlet channel 103, and the bottom of the channel is covered with filter cloth 107; the filter cloth 107 is annular; In the ring formed by the filter cloth 107, the corresponding "outside" means outside the ring formed by the filter cloth 107), and is used to drive the filter cloth 107 to rotate, so that the filter cloth 107 continuously moves along the bottom of the liquid inlet channel 103; The cleaning mechanism is used to clean up impurities on the filter cloth 107 not corresponding to the bottom of the liquid inlet channel 103 during the rotation of the filter cloth 107 .
上述液体杂质分离装置中,滤布107在传动轮的作用下不断转动,使得其上与进液渠103对应的部分进行过滤工作,而脱离进液渠103的部分在滤布清理机构的作用下进行清洁,实现了过滤和清洁同时进行,无需停机清理滤布107,利于液体除杂持续进行,提高效率。In the above-mentioned liquid impurity separation device, the filter cloth 107 is continuously rotated under the action of the transmission wheel, so that the part corresponding to the liquid inlet channel 103 performs filtering work, and the part detached from the liquid inlet channel 103 is under the action of the filter cloth cleaning mechanism. Cleaning realizes filtering and cleaning at the same time, without stopping the machine to clean the filter cloth 107, which is beneficial to continuous liquid removal and improves efficiency.
另外,本发明实施例提供的液体杂质分离装置在应用中,滤布107旋转,使得待除杂液体产生激烈的稳流,促进了待除杂液体与空气的接触和更新,进而使液体中溶解氧的浓度大大提高,可达3mg/L-9mg/L。In addition, in the application of the liquid impurity separation device provided by the embodiment of the present invention, the filter cloth 107 rotates, causing the liquid to be removed to generate a strong steady flow, which promotes the contact and renewal of the liquid to be removed with air, and further dissolves the impurity in the liquid. The concentration of oxygen is greatly increased, up to 3mg/L-9mg/L.
再者,本实施例提供的液体杂质分离装置占地面积小、运行费用低,应用范围广(可以应用于污水厂中原污水固液分离,污水厂中生物池泥水分离,家庭下水道粪便分离,河流湖泊等藻类分离,食品加工厂废水固液分离,采矿废水中矿渣分离等)。Furthermore, the liquid impurity separation device provided by this embodiment has a small footprint, low operating costs, and a wide range of applications (it can be applied to the solid-liquid separation of raw sewage in sewage plants, the separation of mud and water in biological pools in sewage plants, the separation of feces in household sewers, rivers, etc.) Separation of algae in lakes, solid-liquid separation of wastewater in food processing plants, separation of slag in mining wastewater, etc.).
优选的,上述液体杂质分离装置中,还包括多个转轮,转轮设置在进液渠103下方,并且转轮与滤布107相切接触;转轮能够在转动过程中产生负压。应用时,转轮转动并搅动滤布107下方的气体形成负压,便于待除杂液体大量且快速地通过滤布107,既提高过滤液体的量,又提高过滤效率。上述转轮的转动方向可设置为与传送轮的转动方向相同,还可设置为与传送轮的转动方向相反,另外转轮切线速度的范围设置为0.8m/s-8m/s。Preferably, the above-mentioned liquid impurity separation device further includes a plurality of runners, the runners are arranged under the liquid inlet channel 103, and the runners are in tangential contact with the filter cloth 107; the runners can generate negative pressure during rotation. During application, the runner rotates and stirs the gas under the filter cloth 107 to form a negative pressure, which facilitates a large amount of liquid to be removed to pass through the filter cloth 107 quickly, which not only increases the amount of filtered liquid, but also improves the filtration efficiency. The rotation direction of the above-mentioned runner can be set to be the same as the rotation direction of the transmission wheel, and can also be set to be opposite to the rotation direction of the transmission wheel. In addition, the range of the tangential speed of the runner is set to 0.8m/s-8m/s.
除设置转轮形成负压的方式外,上述液体杂质分离装置还可设置为包括多个静置中空轴105,如图4所示,静置中空轴105上与滤布的接触面设有开口151,其端面设置出口152,应用时用于通过开口和出口的导通实现抽吸液体,从而形成负压,便于待除杂液体大量且快速地通过滤布107,既提高过滤液体的量,又提高过滤效率。In addition to the method of setting the runner to form negative pressure, the above-mentioned liquid impurity separation device can also be set to include a plurality of static hollow shafts 105, as shown in Figure 4, the contact surface between the static hollow shafts 105 and the filter cloth is provided with openings 151, an outlet 152 is provided on its end face, and it is used to suck the liquid through the conduction between the opening and the outlet during application, thereby forming a negative pressure, which is convenient for the liquid to be removed to pass through the filter cloth 107 in a large amount and quickly, which not only increases the amount of filtered liquid, And improve the filtration efficiency.
本实施例提供的液体杂质分离装置中滤布下方可形成负压,能够在10s内有效地分离待除杂液体中的泥渣砂油等杂质,效率高。In the liquid impurity separation device provided in this embodiment, a negative pressure can be formed under the filter cloth, which can effectively separate impurities such as sludge, sand, oil, etc. in the liquid to be removed within 10 seconds, with high efficiency.
上述进液渠103中渠底的第一端高于第二端;滤布107上与渠底对应的部分呈倾斜的平板状结构。上述第一端和第二端为进水渠上相对的两部,并且由第一端到第二端的方向与滤布107上同渠底对应的部分的移动方向平行。The first end of the bottom of the above-mentioned liquid inlet channel 103 is higher than the second end; the part of the filter cloth 107 corresponding to the bottom of the channel has an inclined flat plate structure. The above-mentioned first end and second end are two opposite parts on the water inlet ditch, and the direction from the first end to the second end is parallel to the moving direction of the part corresponding to the bottom of the ditch on the filter cloth 107 .
本实施例提供的液体杂质分离装置中,滤布107上与渠底对应的部分倾斜,利于待除杂液体均匀地分布在进液渠103的整个渠底,从而充分地利用滤布107上与渠底对应的部分进行过滤。In the liquid impurity separation device provided in this embodiment, the part corresponding to the bottom of the canal on the filter cloth 107 is inclined, which is beneficial to the liquid to be removed evenly distributed on the whole canal bottom of the liquid inlet canal 103, thereby making full use of the filter cloth 107 and the bottom of the canal. The corresponding part of the bottom of the canal is filtered.
具体的,滤布107上与渠底对应的部分同水平方向的夹角为α,α的角度范围为0°-60°。Specifically, the angle between the part of the filter cloth 107 corresponding to the bottom of the canal and the horizontal direction is α, and the angle range of α is 0°-60°.
上述实施例提供的液体杂质分离装置中,滤布清理机构包括刮渣板181、气冲洗系统和水冲洗系统;刮渣板181与滤布107的外侧相抵;气冲洗系统位于滤布107的内侧,并用于向滤布107沿朝向滤布107外的方向喷射气体;水冲洗系统用于向滤布107喷射水流。优选的,水冲洗系统位于滤布107内,并用于沿朝向滤布107外的方向向滤布喷射水流。In the liquid impurity separation device provided in the above embodiments, the filter cloth cleaning mechanism includes a scraper 181, an air flushing system and a water flushing system; the scraper 181 is against the outside of the filter cloth 107; the air flushing system is located on the inside of the filter cloth 107 , and is used to spray gas to the filter cloth 107 in a direction toward the outside of the filter cloth 107; the water flushing system is used to spray water to the filter cloth 107. Preferably, the water flushing system is located inside the filter cloth 107 and used to spray water toward the filter cloth 107 toward the outside of the filter cloth.
优选的,上述液体杂质分离装置中,滤布107经转动脱离进液渠103后先由气冲洗系统进行冲洗,再由水冲洗系统进行冲洗。Preferably, in the above-mentioned liquid impurity separation device, the filter cloth 107 is rotated and detached from the liquid inlet channel 103, and then washed by the air flushing system, and then flushed by the water flushing system.
具体的,上述气冲洗系统包括至少两个喷气头182,且各喷气头182间隔布置;上述水冲洗系统包括至少两个喷水头183,且各喷水头183间隔布置;上述刮渣板181位于相邻的两个喷气头182之间,如图1所示。Specifically, the above-mentioned air flushing system includes at least two air spray heads 182, and each air spray head 182 is arranged at intervals; the above-mentioned water flushing system includes at least two water spray heads 183, and each water spray head 183 is arranged at intervals; the above-mentioned slag scraper 181 It is located between two adjacent air spray heads 182, as shown in FIG. 1 .
上述液体杂质分离装置中,进液渠103的两侧(该两侧是进液渠103上沿第一方向的两侧,第一方向与进液渠103的第一端到第二端的方向垂直,并且第一方向沿滤布107的输送滤渣的方向垂直)固定有密封条104,密封条104与滤布107相抵,并且密封条104沿滤布107的传送方向(即滤布107输送滤渣的方向)布置。密封条104优选设置为通过固定件34固定在进液渠103上。In the above-mentioned liquid impurity separation device, the two sides of the liquid inlet channel 103 (the two sides are the two sides along the first direction on the liquid inlet channel 103, and the first direction is perpendicular to the direction from the first end to the second end of the liquid inlet channel 103 , and the first direction is vertical along the direction of the conveying filter residue of filter cloth 107) is fixed with sealing strip 104, and sealing strip 104 is offset with filter cloth 107, and sealing strip 104 is along the conveying direction of filter cloth 107 (that is filter cloth 107 transports filter residue direction) layout. The sealing strip 104 is preferably configured to be fixed on the liquid inlet channel 103 by a fixing member 34 .
进一步的,密封条104上用于与滤布107相抵的端面为圆弧面,以避免待除杂液体由进液渠103与滤布107之间的间隙大量泄露,又防止密封条104与滤布107的摩擦过大,避免滤布107受损并使滤布107顺畅转动。上述密封条104是采用耐磨且光滑的材料制成的密封条104,如陶瓷密封条104、不锈钢密封条104或橡胶密封条104等。Further, the end face of the sealing strip 104 that is used to abut against the filter cloth 107 is a circular arc surface, so as to avoid a large amount of leakage of the liquid to be removed from the gap between the liquid inlet channel 103 and the filter cloth 107, and prevent the sealing strip 104 from contacting the filter cloth 107. The friction of the cloth 107 is too large to prevent the filter cloth 107 from being damaged and to make the filter cloth 107 rotate smoothly. The above-mentioned sealing strip 104 is made of wear-resistant and smooth material, such as ceramic sealing strip 104 , stainless steel sealing strip 104 or rubber sealing strip 104 .
具体的,上述液体杂质分离装置中,传送轮包括主动轮106和从动轮162,其中,主动轮106为一个,从动轮162为多个;上述主动轮106的切线速度范围为0.01m/s-1.7m/s。主动轮106设置在进液渠103的第一端处。Specifically, in the above-mentioned liquid impurity separation device, the transmission wheel includes a driving wheel 106 and a driven wheel 162, wherein, there is one driving wheel 106 and a plurality of driven wheels 162; the tangential speed range of the driving wheel 106 is 0.01m/s- 1.7m/s. The driving wheel 106 is arranged at the first end of the liquid inlet channel 103 .
优选的,上述液体杂质分离装置还包括滤布张紧装置109和滤布纠偏装置110,滤布张紧装置109用于由滤布107的内侧撑紧滤布107;滤布纠偏装置110用于调整滤布107在传送轮上的位置,确保滤布107能够准确可靠地覆在进液渠103的渠底。Preferably, the above-mentioned liquid impurity separation device also includes a filter cloth tensioning device 109 and a filter cloth correction device 110, the filter cloth tensioning device 109 is used to tighten the filter cloth 107 from the inner side of the filter cloth 107; the filter cloth correction device 110 is used to Adjust the position of the filter cloth 107 on the transmission wheel to ensure that the filter cloth 107 can cover the bottom of the liquid inlet channel 103 accurately and reliably.
上述滤布张紧装置109包括张紧杠杆191,张紧杠杆191的中部设有铰接安装点,张紧杠杆191的第一端设有能够绕自身轴向转动的滚轮192,该滚轮192与滤布107相抵;张紧杠杆191的另一端与稳压气缸193的活塞杆相连;稳压气缸193的活塞杆做伸缩运动时驱动张紧杠杆191绕其铰接安装点转动,从而调节滚轮192抵紧滤布107的程度,使滤布107张紧或松弛。上述滤布纠偏装置110是采用现有的纠偏装置。The above-mentioned filter cloth tensioning device 109 includes a tensioning lever 191, the middle part of the tensioning lever 191 is provided with a hinged installation point, and the first end of the tensioning lever 191 is provided with a roller 192 that can rotate around its own axis, and the roller 192 is connected to the filter cloth. The cloth 107 offsets; the other end of the tensioning lever 191 is connected with the piston rod of the pressure stabilizing cylinder 193; when the piston rod of the stabilizing cylinder 193 is doing telescopic movement, the tensioning lever 191 is driven to rotate around its hinged mounting point, thereby adjusting the roller 192 against the tension The extent of the filter cloth 107 makes the filter cloth 107 tense or loose. The above-mentioned filter cloth deviation correcting device 110 adopts an existing deviation correcting device.
上述液体杂质分离装置还包括集液槽111和集废槽112;集液槽111设置在进液渠103下方,用于盛装经滤布107过滤的液体;集废槽112用于收集滤布清理机构清除的杂质,以及由滤布107和进液渠103的渠底之间间隙泄露的液体。由于滤布清理机中各个系统间隔布置,为了便于收集,上述方案中集废槽112包括两个,其中一个用于收集刮渣板181以及第一个喷气头183清理的废渣,另一个设置在集液槽111下方,用于收集剩余喷气头182、水冲洗系统清理的废渣,以及由滤布107与进液渠109的渠底之间间隙泄露的液体。当然上述集废槽112的底部设有排放口,进一步的,为了便于废渣排放,集废槽112的排放口处连接有罗茨风机。另外,上述集液槽111的底部设有排液口。The above-mentioned liquid impurity separation device also includes a liquid collection tank 111 and a waste collection tank 112; the liquid collection tank 111 is arranged below the liquid inlet channel 103, and is used to hold the liquid filtered by the filter cloth 107; the waste collection tank 112 is used to collect the filter cloth for cleaning The impurities removed by the mechanism, and the liquid leaked from the gap between the filter cloth 107 and the bottom of the liquid inlet channel 103. Since each system in the filter cloth cleaning machine is arranged at intervals, in order to facilitate collection, the waste collection tank 112 in the above scheme includes two, one of which is used to collect the waste residue cleaned by the scraper plate 181 and the first air spray head 183, and the other is arranged on the The bottom of the liquid collection tank 111 is used to collect the remaining air nozzles 182 , the waste residue cleaned by the water flushing system, and the liquid leaked from the gap between the filter cloth 107 and the bottom of the liquid inlet channel 109 . Of course, the bottom of the above-mentioned waste collection tank 112 is provided with a discharge port. Furthermore, in order to facilitate the discharge of waste residue, a Roots blower is connected to the discharge port of the waste collection tank 112 . In addition, a liquid discharge port is provided at the bottom of the liquid collection tank 111 .
上述滤布107可设置为单层,优选设置为多层,其中位于外侧,并用于与密封条104直接接触的一层滤网为面层,其余为内层,面层的孔径优选设置为不小于内层的孔径。另外,滤布设置为多层时需使各层固定连接,优选采用聚四氟乙烯线缝接。Above-mentioned filter cloth 107 can be arranged as single layer, preferably is arranged as multi-layer, wherein is positioned at outside, and is used for one deck filter screen that is used for directly contacting with sealing strip 104 as surface layer, and the rest is inner layer, and the aperture of surface layer is preferably set to not smaller than the pore size of the inner layer. In addition, when the filter cloth is arranged in multiple layers, each layer needs to be fixedly connected, preferably sewn with polytetrafluoroethylene thread.
进一步的,上述液体杂质分离装置还包括主体101,上述进液渠103、传送轮、滤布清理机构、转轮或静置中空轴105、滤布张紧装置109、滤布纠偏装置110、集液槽111和集废槽112分别装配在该主体101上。主体101上固定有支撑脚。Further, the above-mentioned liquid impurity separation device also includes a main body 101, the above-mentioned liquid inlet channel 103, a transmission wheel, a filter cloth cleaning mechanism, a runner or a static hollow shaft 105, a filter cloth tensioning device 109, a filter cloth correction device 110, a set The liquid tank 111 and the waste collection tank 112 are respectively assembled on the main body 101 . Support feet are fixed on the main body 101 .
下面以具体实验介绍:The following is a specific experiment introduction:
1、杂质分离装置中,滤布107上与进液渠103的渠底对应的部分的倾斜角α设置为20°;主动轮106的切线速度设置为1m/s;密封条104采用不锈钢密封条104;应用转轮,转轮的切线速度设置为4m/s;滤布107设置为双层,面层孔径为100um,内层孔径分别选取10um,20um,30um,40um,50um,80um进行试验,可知待除杂液体中悬浮物的过滤情况如下表1. In the impurity separation device, the inclination angle α of the part corresponding to the bottom of the liquid inlet channel 103 on the filter cloth 107 is set to 20°; the tangential speed of the driving wheel 106 is set to 1m/s; the sealing strip 104 is made of stainless steel sealing strip 104; the runner is used, and the tangential velocity of the runner is set to 4m/s; the filter cloth 107 is set to a double layer, the surface aperture is 100um, and the inner aperture is selected respectively from 10um, 20um, 30um, 40um, 50um, and 80um to test, It can be seen that the filtration of suspended solids in the liquid to be removed is as follows
2、杂质分离装置中,滤布107上与进液渠103的渠底对应的部分的倾斜角α设置为30°;主动轮106的切线速度设置为1.7m/s;密封条104采用陶瓷密封条104;应用静置中空轴;滤布107设置为三层,面层孔径为150um,最内侧的内层设置为与面层孔径相同,中间的内层孔径分别选取10um,20um,30um,40um,50um,80um进行试验,可知待除杂液体中活性污泥的过滤情况如下表2. In the impurity separation device, the inclination angle α of the part of the filter cloth 107 corresponding to the bottom of the liquid inlet channel 103 is set to 30°; the tangential speed of the driving wheel 106 is set to 1.7m/s; the sealing strip 104 is sealed with ceramics Article 104: apply static hollow shaft; the filter cloth 107 is set to three layers, the surface layer aperture is 150um, the innermost inner layer is set to be the same as the surface layer aperture, and the middle inner layer aperture is respectively selected as 10um, 20um, 30um, 40um , 50um, 80um to test, it can be seen that the filtration of activated sludge in the liquid to be removed is as follows
3、杂质分离装置中,滤布107上与进液渠103的渠底对应的部分的倾斜角α设置为45°;主动轮106的切线速度设置为0.5m/s;密封条104采用不锈钢密封条104;应用转轮,转轮的转动方向设置为与主动轮106的转动方向相反,切线速度为0.01m/s;滤布107设置为单层,滤布107的孔径分别选取100um,50um和18um进行试验,可知待除杂液体中悬浮颗粒的过滤情况如下表3. In the impurity separation device, the inclination angle α of the part of the filter cloth 107 corresponding to the bottom of the liquid inlet channel 103 is set to 45°; the tangential speed of the driving wheel 106 is set to 0.5m/s; the sealing strip 104 is sealed with stainless steel Bar 104; use the runner, the rotation direction of the runner is set to be opposite to the rotation direction of the driving wheel 106, and the tangential speed is 0.01m/s; the filter cloth 107 is set to a single layer, and the aperture of the filter cloth 107 is selected 100um, 50um and 18um test, it can be seen that the filtration of suspended particles in the liquid to be removed is as follows
4、杂质分离装置中,滤布107上与进液渠103的渠底对应的部分的倾斜角α设置为60°;主动轮106的切线速度设置为1.5m/s;密封条104采用不锈钢密封条104;应用转轮,且转轮的转动方向设置为与主动轮106的转动方向相同,切线速度为8m/s;滤布107设置为单层,滤布107的孔径分别选取100um,800um和1500um进行试验,可知液体过滤前后其绿藻水浓度变化如下表4. In the impurity separation device, the inclination angle α of the part corresponding to the bottom of the liquid inlet channel 103 on the filter cloth 107 is set to 60°; the tangential speed of the driving wheel 106 is set to 1.5m/s; the sealing strip 104 is sealed with stainless steel Bar 104; use the runner, and the rotation direction of the runner is set to be the same as the rotation direction of the driving wheel 106, and the tangential speed is 8m/s; the filter cloth 107 is set to a single layer, and the aperture of the filter cloth 107 is selected 100um, 800um and Tested at 1500um, we can see that the concentration of green algae in the liquid before and after filtration changes as shown in the table below
5、杂质分离装置中,滤布107上与进液渠103的渠底对应的部分的倾斜角α设置为30°;主动轮106的切线速度设置为1.3m/s;密封条104采用橡胶密封条104;采用静置在中空轴;滤布107设置为单层,滤布107的孔径分别选取100um,500um,1000um进行试验,可知液体过滤前后其粪便浓度变化如下表5. In the impurity separation device, the inclination angle α of the part of the filter cloth 107 corresponding to the bottom of the liquid inlet channel 103 is set to 30°; the tangential speed of the driving wheel 106 is set to 1.3m/s; the sealing strip 104 is sealed with rubber Article 104; adopt to stand still on the hollow shaft; the filter cloth 107 is set as a single layer, and the aperture of the filter cloth 107 is respectively selected as 100um, 500um, and 1000um for testing. It can be seen that the concentration of feces before and after liquid filtration changes as shown in the following table
由上述5个试验可以看出,本实施例对液体中各种杂质均具有良好的除杂效果。It can be seen from the above 5 tests that this embodiment has good impurity removal effects on various impurities in the liquid.
本说明书中各个实施例采用递进的方式描述,每个实施例重点说明的都是与其他实施例的不同之处,各个实施例之间相同相似部分互相参见即可。Each embodiment in this specification is described in a progressive manner, each embodiment focuses on the difference from other embodiments, and the same and similar parts of each embodiment can be referred to each other.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
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CN106395994A (en) * | 2016-11-24 | 2017-02-15 | 攀枝花市仁通钒业有限公司 | Sewage filtering apparatus |
CN108144349A (en) * | 2017-12-30 | 2018-06-12 | 深圳市水务(集团)有限公司阀门检测及维修分公司 | Duct type microfroc filter |
CN112058197A (en) * | 2020-08-10 | 2020-12-11 | 宁夏奥斯化工有限公司 | Process and device for producing cyanamide |
CN112999725A (en) * | 2021-03-30 | 2021-06-22 | 宁夏共享机床辅机有限公司 | Liquid tank maintenance equipment |
CN113561554A (en) * | 2020-04-28 | 2021-10-29 | 青岛金玖能源科技有限公司 | Wet pressing plate host |
CN115159597A (en) * | 2021-10-15 | 2022-10-11 | 尚川(北京)水务有限公司 | Filtration equipment for quickly and efficiently removing sludge and sand oil in sewage |
CN115944983A (en) * | 2023-01-09 | 2023-04-11 | 安徽华功信息科技有限公司 | Waste liquid recovery and filtration treatment device and method |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN106395994A (en) * | 2016-11-24 | 2017-02-15 | 攀枝花市仁通钒业有限公司 | Sewage filtering apparatus |
CN108144349A (en) * | 2017-12-30 | 2018-06-12 | 深圳市水务(集团)有限公司阀门检测及维修分公司 | Duct type microfroc filter |
CN113561554A (en) * | 2020-04-28 | 2021-10-29 | 青岛金玖能源科技有限公司 | Wet pressing plate host |
CN112058197A (en) * | 2020-08-10 | 2020-12-11 | 宁夏奥斯化工有限公司 | Process and device for producing cyanamide |
CN112058197B (en) * | 2020-08-10 | 2023-08-08 | 宁夏奥斯化工有限公司 | Process and device for producing cyanamide |
CN112999725A (en) * | 2021-03-30 | 2021-06-22 | 宁夏共享机床辅机有限公司 | Liquid tank maintenance equipment |
CN115159597A (en) * | 2021-10-15 | 2022-10-11 | 尚川(北京)水务有限公司 | Filtration equipment for quickly and efficiently removing sludge and sand oil in sewage |
CN115944983A (en) * | 2023-01-09 | 2023-04-11 | 安徽华功信息科技有限公司 | Waste liquid recovery and filtration treatment device and method |
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