CN2465771Y - Vacuum mud filter without filter cloth - Google Patents
Vacuum mud filter without filter cloth Download PDFInfo
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- CN2465771Y CN2465771Y CN 01212477 CN01212477U CN2465771Y CN 2465771 Y CN2465771 Y CN 2465771Y CN 01212477 CN01212477 CN 01212477 CN 01212477 U CN01212477 U CN 01212477U CN 2465771 Y CN2465771 Y CN 2465771Y
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- 239000004744 fabric Substances 0.000 title claims abstract description 12
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims abstract description 66
- 238000009826 distribution Methods 0.000 claims abstract description 29
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 15
- 239000010935 stainless steel Substances 0.000 claims abstract description 15
- 238000001914 filtration Methods 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 21
- 238000005406 washing Methods 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 238000003828 vacuum filtration Methods 0.000 abstract 1
- 239000010802 sludge Substances 0.000 description 8
- 239000007921 spray Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 230000005540 biological transmission Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000003860 storage Methods 0.000 description 6
- 240000000111 Saccharum officinarum Species 0.000 description 5
- 235000007201 Saccharum officinarum Nutrition 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 238000005352 clarification Methods 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 206010035148 Plague Diseases 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
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- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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Abstract
本实用新型公开了一种无滤布真空过滤装置,它包括设有支承转轴和内侧设有吸汁导管的转鼓圆筒,其特点是转鼓圆筒外表面固定覆盖有网格板和不锈钢微孔过滤网,网格处于该圆筒外表面与过滤网之间;在转鼓圆筒转轴含吸汁导管一端所联接的真空分配头是三功能分区真空分配头。该装置可大大降低糖厂泥汁所排滤泥的转光度,提高滤泥单位过滤面积的处理能力,减轻操作人员的劳动强度,从根本上消除洗滤布的大量用水和造成的污染。
The utility model discloses a vacuum filtration device without filter cloth, which comprises a drum cylinder provided with a supporting rotating shaft and a juice suction conduit provided inside thereof, and is characterized in that the outer surface of the drum cylinder is fixedly covered with a grid plate and a stainless steel microporous filter screen, and the grid is located between the outer surface of the drum cylinder and the filter screen; the vacuum distribution head connected to one end of the rotating shaft of the drum cylinder containing the juice suction conduit is a three-function zoned vacuum distribution head. The device can greatly reduce the light conversion degree of the filter mud discharged by the sugar factory mud juice, improve the processing capacity of the filter mud per unit filtering area, reduce the labor intensity of the operator, and fundamentally eliminate the large amount of water used for washing the filter cloth and the pollution caused.
Description
本实用新型涉及一种将液体从固体中分离的设备,尤其是糖厂所用的泥汁过滤装置。The utility model relates to a device for separating liquid from solid, in particular to a mud filter device used in sugar factories.
蔗汁的澄清过滤作为糖厂重要的工艺过程,它的主要作用是尽可能把混在蔗汁中的夹杂物从蔗汁中分离出来。在澄清过程产生的泥汁中还含有一定份量的糖份,通过过滤的形式,尽可能把残留在泥汁中的糖份收回,使在滤泥中损失的糖份降低到最低限度,提高糖的生产率。The clarification and filtration of sugarcane juice is an important process in sugar factories, and its main function is to separate the inclusions mixed in the sugarcane juice from the sugarcane juice as much as possible. The mud juice produced in the clarification process also contains a certain amount of sugar. Through the form of filtration, the sugar remaining in the mud juice can be recovered as much as possible, so that the sugar lost in the filter mud can be reduced to a minimum, and the sugar content can be improved. productivity.
长期以来,我国几乎所有的糖厂所采用的泥汁过滤设备是传统的有滤布真空吸滤机和板框压滤机,这些设备作为糖厂泥汁过滤设备的标准配备,在我国的糖业生产中使用了相当长的时间,也为我国的糖业生产作出了较大贡献。但这些设备在生产使用过程中存在着以下缺点:其一是设备的泥汁处理能力有限,所需设备台数多,设备投资较大;其二是所产生滤泥的转光度(含糖份)高,糖份损失严重;其三是过滤所用的滤布要经常拆卸清洗,工人劳动强度大,更严重的是洗滤布产生的大量废水外排,严重污染环境,随着近年来国家对环保问题的日益重视,如何在保证企业正常生产的同时,既能保证糖厂的产品质量和数量,又能保证外排污染物达标排放,成为困扰糖厂企业发展的一个难题。For a long time, the sludge filtration equipment used in almost all sugar factories in my country is the traditional vacuum suction filter with filter cloth and plate and frame filter press. These equipment are used as standard equipment for sugar factory sludge filtration equipment. It has been used in industrial production for quite a long time and has also made a great contribution to my country's sugar production. However, these equipments have the following disadvantages in the process of production and use: one is that the sludge processing capacity of the equipment is limited, the number of equipment required is large, and the equipment investment is relatively large; The third is that the filter cloth used for filtering should be disassembled and cleaned frequently, and the labor intensity of the workers is high. What is more serious is that a large amount of waste water generated by washing the filter cloth is discharged, which seriously pollutes the environment. With the increasing attention to the problem, how to ensure the normal production of the enterprise while ensuring the product quality and quantity of the sugar factory and ensuring that the discharged pollutants meet the standards has become a problem that plagues the development of sugar factories.
本实用新型的目的是提供一种无滤布真空泥汁过滤装置,它应能大大降低泥汁过滤所排滤泥的转光度(含糖份),提高滤泥单位过滤面积的处理能力,减轻操作人员的劳动强度,从根本上消除糖厂的洗滤布大量用水,使糖厂减少一个大污染源。The purpose of this utility model is to provide a kind of vacuum mud filter device without filter cloth, it should be able to greatly reduce the degree of light conversion (sugar content) of the discharged filter mud of mud juice filtration, improve the processing capacity of filter mud unit filter area, alleviate The labor intensity of the operators fundamentally eliminates the large amount of water used for washing filter cloths in the sugar factory, reducing a major pollution source in the sugar factory.
本实用新型包括设有支承转轴和内侧设有吸汁导管的转鼓圆筒,其中的吸汁导管,转鼓圆筒外表面和设在支承转轴一端的真空分配头相通,以及转鼓传动装置、泥汁槽、搅拌装置、热水喷淋装置、刮泥板装置和机架,其特点是:The utility model comprises a rotating drum cylinder provided with a supporting rotating shaft and a juice-absorbing conduit inside, wherein the juice-absorbing conduit, the outer surface of the rotating drum cylinder communicates with a vacuum distribution head arranged at one end of the supporting rotating shaft, and a rotating drum transmission device, mud Juice tank, stirring device, hot water spraying device, scraper device and frame, which are characterized by:
(a)在所述转鼓圆筒的外表面固定覆盖有网格和超薄不锈钢微孔过滤网,其中网格处于该圆筒外表面与微孔过滤网之间;(a) the outer surface of the drum cylinder is fixedly covered with a grid and an ultra-thin stainless steel microporous filter, wherein the grid is between the outer surface of the cylinder and the microporous filter;
(b)在所述转鼓圆筒支承转轴含吸汁导管一端所联接的真空分配头是设有低真空区、高真空区和常压区的三功能分区的真空分配头,低真空区和高真空区分别与各自的导管和贮罐相通。(b) The vacuum distribution head connected to one end of the rotating shaft containing the juice suction conduit on the drum cylinder is a vacuum distribution head with three functional zones, the low vacuum zone, the high vacuum zone and the normal pressure zone, the low vacuum zone and the high vacuum zone. The vacuum zones communicate with their respective conduits and storage tanks.
在所述转鼓圆筒的外面上,按圆周分成多等份,在每等份上固定有纵向的U型槽,将超薄不锈钢微孔过滤网的周国用橡胶条压紧固定在各U型槽中。On the outer surface of the drum cylinder, it is divided into multiple equal parts according to the circumference, and a longitudinal U-shaped groove is fixed on each equal part, and the Zhou Guo of the ultra-thin stainless steel microporous filter is pressed and fixed on each In the U-shaped groove.
上述结构的无滤布真空泥汁过滤装置,转鼓圆筒卧在泥汁槽中,两端的转轴由机架上的轴承座支承;转动圆筒的传动装置在机架的一端,将动力传给转鼓圆筒,使其转动;搅拌装置设置在泥汁槽的后侧一端,通过不断摆动设在泥汁槽内、转鼓圆筒下面的搅拌器,防止泥汁沉淀,和泥汁与蔗糠分离,保护泥汁槽中泥汁的浓度稳定;热水喷淋装置设在转鼓圆筒的后方和上方,设有多支喷淋管道与转鼓圆筒表面纵向平行,在每根管道与转鼓圆筒相对的面上,配置有若干个喷水嘴,运行时能把热水形成喷射状,均匀地喷淋到转鼓圆筒表面的滤泥上,溶解滤泥中的残留糖份,以利于转鼓圆筒内吸汁管网的真空吸收;刮泥板装置设在转鼓圆筒的前面,固定在泥汁槽的外侧上边,其作用是把滤泥从转鼓圆筒表面刮落。这样,转鼓圆筒在传动装置的驱动下不断转动,泥汁槽中的滤泥吸附在转鼓圆筒外表面的超薄不锈钢微孔过滤网上,滤泥中的糖份经热水喷淋溶解,被转鼓圆筒内的吸汁管网真空吸收到贮罐中,含糖份已很少的滤泥被刮泥板刮出。如此循环不断将泥汁槽中的滤泥过滤,吸取糖份,排去滤泥。当然,需过滤的滤泥也不断从蔗汁的澄清过程中不断注入到泥汁槽中。整个过程是全自动进行的,免去了人工拆洗滤布的工序,节约了大量洗滤布的用水,消除了污染源,提高了设备滤泥单位过滤面积的处理能力,也提高了糖的生产率。In the vacuum mud filtration device without filter cloth, the drum cylinder lies in the mud tank, and the rotating shafts at both ends are supported by the bearing seats on the frame; the transmission device for rotating the cylinder is at one end of the frame, and the power transmission Give the drum cylinder to make it rotate; the stirring device is set at one end of the rear side of the mud tank, and by constantly swinging the agitator arranged in the mud tank and below the drum cylinder, the mud juice is prevented from settling, and the mud juice and the mud juice are mixed together. Cane chaff is separated to protect the concentration of mud juice in the mud tank; the hot water spray device is installed behind and above the drum cylinder, and there are multiple spray pipes parallel to the surface of the drum cylinder longitudinally. The surface of the pipeline opposite to the drum cylinder is equipped with several water nozzles, which can spray hot water into a spray shape during operation, and spray evenly on the filter mud on the surface of the drum cylinder to dissolve the residue in the filter mud. The sugar is used to facilitate the vacuum absorption of the juice suction pipe network in the drum cylinder; the mud scraper device is located in front of the drum cylinder and fixed on the outer side of the mud juice tank, and its function is to remove the filter mud from the drum cylinder The surface is scratched off. In this way, the drum cylinder rotates continuously under the drive of the transmission device, the filter mud in the mud juice tank is adsorbed on the ultra-thin stainless steel microporous filter net on the outer surface of the drum cylinder, and the sugar in the filter mud is sprayed with hot water Dissolved and vacuum-absorbed into the storage tank by the juice suction pipe network in the drum cylinder, and the filter mud with little sugar content is scraped out by the mud scraper. This cycle continuously filters the filter mud in the mud juice tank, absorbs sugar, and drains the filter mud. Of course, the filter mud that needs to be filtered is also constantly injected into the mud juice tank from the clarification process of sugarcane juice. The whole process is fully automatic, eliminating the need for manual dismantling and washing of the filter cloth, saving a lot of water for washing the filter cloth, eliminating pollution sources, improving the processing capacity of the unit filter area of the equipment filter mud, and improving the sugar production rate.
下面结合附图,对本实用新型作进一步说明。Below in conjunction with accompanying drawing, the utility model is further described.
图1所示,是本实用新型结构主视图。Shown in Fig. 1, is the utility model structure front view.
图2所示,是图1的左视图。Shown in Fig. 2, it is the left side view of Fig. 1.
图3所示,是转鼓圆筒结构主视图。As shown in Fig. 3, it is a front view of the drum cylinder structure.
图4所示,是图3的右视图。Shown in Figure 4 is the right side view of Figure 3.
图5所示,是转鼓圆筒表面结构图。As shown in Fig. 5, it is a diagram of the surface structure of the drum cylinder.
图6所示、是三功能分区真空分配头结构图。As shown in Figure 6, it is a structural diagram of the three-function partition vacuum distribution head.
图7所示,是图6C-C沿线的A-A视图。As shown in Fig. 7, it is a view along the line A-A of Fig. 6C-C.
图8所示,是图6C-C沿线的B-B视图。As shown in FIG. 8, it is a B-B view along the line of FIG. 6C-C.
在图1和图2所示的无滤布真空泥汁装置结构中可知,长方框状的泥汁槽8处于本装置的低部,其底面和四周用板材密封不透水,开口向上。转鼓圆筒1纵卧在泥汁槽8中,其中心的支承转轴5由机架3两端的轴承座4支承。支承转轴5的左端与设在机架3左端外侧上的转鼓驱动装置11联接,该驱动装置11通过驱动支承转轴5旋转而使转鼓圆筒1转动。在转鼓圆筒1的外表面上设置有不锈钢微孔过滤网16,为了简捷,在图1中该过滤网16局部示意只画了几小块,该过滤网16通过固定在转鼓圆筒1外表面的U型槽,用橡胶条17将其固定,关于过滤网16的设置,在图5中还有说明。在泥汁槽8的左端下设有泥汁注入口10,在蔗汁澄清过程中产生的滤泥汁,由此入口10注入到本装置的泥汁槽8中。搅拌驱动装置20设在泥汁槽8后面上,通过摇杆21驱动纵向设在泥汁槽8中及转鼓圆筒1下方的搅拌器9,使该搅拌器9在运行时不断摆动,防止泥汁沉淀,保持泥汁槽8中泥汁的浓度稳定。在转鼓圆筒1的后方和上方通过固定在机架3两端上的管架12,设置有多支纵向的热水管14,各支热水管14纵向与转鼓圆筒的纵向基本平行,各支热水管14均与热水注入口13相通,在与转鼓圆筒1表面相对的各热水管14面上,设有多个喷淋头15,当有热水注入时,各喷淋头15把喷射状的热水均匀喷淋到转鼓圆筒1表面的滤泥上,溶解滤泥中含有的糖份,以利于转鼓圆筒1内吸汁管网的真空吸收。转鼓圆筒1的内部结构在以下图3和图4中还有说明。在图1中转鼓圆筒1的支承轴5的右端,设置有三功能分区真空分配头2,该分配头中设有高真空区、低真空区和常压区,可从与高真空区相通的高真空吸管18及与低真空区相通的低真空吸管19中可吸出从泥汁中分离出来的糖汁。真空分配头2的结构在以下的图6、7、8中有详细说明。在泥汁槽8的正面上边,设置有多处刮板支撑6,支撑着刮板7。刮板7的刮口纵向贴住转鼓圆筒1的外表面,其主要作用是把滤泥从转鼓圆筒1表面剥落。In the structure of the vacuum mud juice device without filter cloth shown in Fig. 1 and Fig. 2, it can be known that the
图3和图4是转鼓圆筒1的结构图。图3是转鼓圆筒1的剖视图,鼓身为不锈钢板卷焊而成的圆筒体28,鼓身内侧焊有用型钢27及钢板26构成的加强架,两端固定有端面板23。在鼓身外侧按圆周均分成多等份,在等份上纵向焊有用不锈钢制成型的U型槽,用于通过橡胶条17把不锈钢微孔过滤网16压固定,这在图3的左下角作局部表示。在转鼓圆筒1的圆筒体上,从内透过圆筒体不锈钢板,在筒体圆周上均匀设置有不锈钢吸汁管网24,各管网24又与各吸汁主导管25分别相通,各吸汁主导管25的另一端通过支承转轴5右端内侧与真空分配头2联接,使转鼓圆筒1的外表面空间与真空分配头2相通,可通过形成真空把从泥汁中分离出来的糖汁引入存贮罐中。在图4的局部剖视中可知,各纵列向的吸汁管网24分别与本列的主导吸汁管25相连通,各主导吸汁管25的另一端穿过支承转轴5右端内与真空分配头2相连通。转鼓支承转轴5左端除支承转鼓外还与传动装置有传动联接,使转鼓圆筒1在动力的作用下转动。图3中的I是转鼓圆筒1表面需放大表示的结构,在图5表出。3 and 4 are structural diagrams of the
在图5中,放大表示了转鼓圆筒1表面结构,在转鼓圆筒体28的外侧表面上,按圆周分成多等份,在各等份上纵向焊固定有U型槽29,各块状超薄不锈钢过滤网16的边通过橡胶条17压固定在U型槽29内。为了形成一个吸汁空间,方便和保证滤汁的流动畅通,在过滤网16和圆筒体28之间设有一层塑料网格板30。各吸汁管网24的管口穿过圆筒体28后,应不超出圆筒体28的外表面,以利于吸汁。In Fig. 5, the surface structure of the
图6、7、8放大表示了三功能分区真空分配头2的结构,该分配头2包括孔板34、分配板33,固定螺杆32,以及高真空吸管18和低真空吸管19。其中,从图6和图8中可知,孔板34通过螺钉与转轴5固定连接,各吸汁主导管25的管口穿过该孔板34,并与外侧平面平齐,孔板34的右侧面中心有一定位凹孔36,该孔板34随转轴5旋转。图7与图8是图6以沿线C-C为分界面,左视得B-B面的视图8;右视得A-A面的视图7。从图6和图7中可知,分配板33通过螺钉与附加件31固定联接,而附加件31又通过螺杆32与轴承座4和机架3固定联接,分配板33不随转轴5转动。高真空吸管18和低真空吸管19都与附加头31固定联接,并分别与分配板33中的高真空区域39和低真空区域38相通。在分配板33的中心有一凸头37与孔板34中心的凹孔相对应。高真空吸管18与高真空抽汁贮罐相通;低真空吸管19与低真空抽计贮罐相通。在分配板33上,常压区域40与大气相通。分配头2的工作原理是以C-C面为分界线,B-B面随转轴5旋转,A-A面不动,转动面的吸汁管口随着转轴5的旋转,分别循环往复地处于低真空区38、高真空区39和常压区40,把从泥汁中分离出来的糖汁用抽真空的方法抽到各贮罐中。因分配头2中设有低真空、高真空和常压三个区,功能各不一样,故称三功能分区真空分配头。Fig. 6, 7, 8 enlarges and represents the structure of three-function zone
无滤面真空泥汁过滤装置的工作原理:从糖厂沉淀池输送过来的泥汁与蔗糠按一定比例在泥汁蔗糠搅拌器内均匀混合后,输送到过滤装置的泥汁槽中;在泥汁槽与转鼓圆筒面之间设置有搅拌装置,在电机及其它减速装置的驱动下,搅拌装置在泥汁槽与转鼓面之间作往复摆动,以保证泥汁的浓度的稳定及防止泥汁中的杂质发生沉淀;通过变频技术控制的电动机可以调节出适当的转鼓旋转速度;与真空泵连接的两个真空抽汁罐通过真空调节阀的调节,使两罐分别产生高、低真空,与转鼓圆筒内的吸汁管网连接的真空分配头把转鼓圆筒表面按工作顺序分成低真空、高真空和常压三个区,使过滤过程的泥汁也按吸附、洗水(包括干燥)和卸泥三个顺序循环进行。低真空区位于转鼓的底部泥汁浸泡部分,此区域为吸附滤泥和杂质的区域,当转鼓进入此区域,由于此时此区域内的吸汁管均与真空分配头的低真空区相通,通过不锈钢吸汁管的连通,使得微孔过滤网与转鼓面间的吸汁空间形成负压,在负压的作用下,糖汁可以穿过不锈钢微孔过滤网上的微孔进入网格吸汁空间并通过吸汁管及真空分配头流到低真空抽汁罐内,而也由于负压的作用,混在泥汁中的滤泥、蔗糠和其他杂质也不断吸附到过滤网面上去,并不断增加、加厚;随着转鼓的旋转,进入高真空区,在此区域的前大半部分,热水喷淋装置将热水喷淋在转鼓面已吸附的滤泥上,以尽可能提取滤泥中的糖份,热水连同洗下的糖份也穿过过滤网的微孔经吸汁管流入高真空抽汁罐内,后小半部分不淋水,为干燥区,在此区域继续保持高真空,以便尽可通吸于滤泥中的水分,进一步吸取滤泥中的糖分,并使排出的滤泥干燥;随后进入常压区,常压区为卸泥区,在该区解除了真空,以便于粘附在滤网面的滤泥脱落。这样按吸附、洗水(包括干燥)和卸泥三个步骤循环进行,使生产连续均衡进行。The working principle of the vacuum mud filtration device without filter surface: the mud juice and cane chaff transported from the sedimentation tank of the sugar factory are uniformly mixed in the mud juice chaff mixer in a certain proportion, and then transported to the mud juice tank of the filter device; A stirring device is installed between the mud tank and the cylindrical surface of the drum. Driven by the motor and other reduction devices, the stirring device swings back and forth between the mud tank and the drum to ensure the stability of the concentration of the mud. and prevent the impurities in the mud juice from settling; the motor controlled by frequency conversion technology can adjust the appropriate drum rotation speed; the two vacuum juice tanks connected with the vacuum pump are adjusted by the vacuum regulating valve, so that the two tanks respectively produce high, Low vacuum, the vacuum distribution head connected with the juice suction pipe network in the drum cylinder divides the surface of the drum cylinder into three areas of low vacuum, high vacuum and normal pressure according to the working order, so that the mud juice in the filtration process can also be absorbed, Washing water (including drying) and mud unloading are carried out in three sequential cycles. The low-vacuum area is located at the bottom mud soaking part of the drum. This area is the area for absorbing filter mud and impurities. When the drum enters this area, the juice suction pipes in this area are all connected to the low-vacuum area of the vacuum distribution head. , through the connection of the stainless steel juice suction tube, the juice suction space between the microporous filter and the drum surface forms a negative pressure. Under the action of negative pressure, the sugar juice can pass through the micropores on the stainless steel microporous filter and enter the grid juice suction space And it flows into the low-vacuum juice tank through the juice suction pipe and the vacuum distribution head, and due to the effect of negative pressure, the filter mud, cane bran and other impurities mixed in the mud juice are also continuously adsorbed to the surface of the filter mesh and increase , thickening; with the rotation of the drum, it enters the high vacuum area. In the first half of this area, the hot water spraying device sprays hot water on the filter mud adsorbed on the drum surface to extract the filter mud as much as possible. The sugar in the mud, the hot water and the washed sugar also pass through the micropores of the filter screen and flow into the high-vacuum juice pumping tank through the juice suction pipe. Vacuum, so as to absorb the water in the filter mud as much as possible, further absorb the sugar in the filter mud, and dry the discharged filter mud; then enter the normal pressure zone, the normal pressure zone is the sludge unloading zone, and the vacuum is released in this zone , so that the filter mud adhering to the surface of the filter screen falls off. In this way, the three steps of adsorption, water washing (including drying) and sludge discharge are cycled, so that the production can be continuously and balanced.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01212477 CN2465771Y (en) | 2001-02-16 | 2001-02-16 | Vacuum mud filter without filter cloth |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01212477 CN2465771Y (en) | 2001-02-16 | 2001-02-16 | Vacuum mud filter without filter cloth |
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| CN2465771Y true CN2465771Y (en) | 2001-12-19 |
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|---|---|---|---|
| CN 01212477 Expired - Fee Related CN2465771Y (en) | 2001-02-16 | 2001-02-16 | Vacuum mud filter without filter cloth |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101998874A (en) * | 2008-04-11 | 2011-03-30 | 奥图泰(滤器)公司 | Liquid extraction filter and cleaning method thereof |
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2001
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101998874A (en) * | 2008-04-11 | 2011-03-30 | 奥图泰(滤器)公司 | Liquid extraction filter and cleaning method thereof |
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