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CN118387986B - Reverse osmosis industrial water purifier with changeable working mode - Google Patents

Reverse osmosis industrial water purifier with changeable working mode Download PDF

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Publication number
CN118387986B
CN118387986B CN202410780658.2A CN202410780658A CN118387986B CN 118387986 B CN118387986 B CN 118387986B CN 202410780658 A CN202410780658 A CN 202410780658A CN 118387986 B CN118387986 B CN 118387986B
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reverse osmosis
pipe
layer
water
stage
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CN118387986A (en
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魏小刚
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Shenzhen Linkesonic Cleaning Equipment Co ltd
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Shenzhen Linkesonic Cleaning Equipment Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • B01D65/04Membrane cleaning or sterilisation ; Membrane regeneration with movable bodies, e.g. foam balls
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/04Backflushing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/30Mechanical cleaning, e.g. with brushes or scrapers
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention belongs to the technical field of reverse osmosis industrial water purifiers, and particularly relates to a reverse osmosis industrial water purifier with a variable working mode, which comprises a raw water tank, a booster pump, a sand filter, a carbon filter, a softener, a precision filter, a high-pressure pump, reverse osmosis equipment and a pure water tank, wherein the sand filter, the carbon filter and the softener have the same structure, and the reverse osmosis equipment consists of a plurality of reverse osmosis components which are connected in parallel. The reverse osmosis layer of the reverse osmosis unit in the reverse osmosis equipment is provided with a two-stage osmosis structure, raw water can be purified more effectively, meanwhile, a first supporting layer between the two-stage osmosis structure in the reverse osmosis layer can be deformed properly under the action of backwash pressure pulsation to scrape and clean crystals attached to the raw water side of the first-stage reverse osmosis membrane, the crystals separated from the first-stage reverse osmosis membrane are discharged under the drive of backwash pure water, the backwash capacity of the reverse osmosis equipment is improved, the service life of the reverse osmosis equipment is prolonged, the replacement period is prolonged, and the equipment maintenance cost is reduced.

Description

一种工作方式可变的反渗透工业纯水机A reverse osmosis industrial pure water machine with variable working mode

技术领域Technical Field

本发明属于反渗透工业纯水机技术领域,尤其涉及一种工作方式可变的反渗透工业纯水机。The invention belongs to the technical field of reverse osmosis industrial pure water machines, and in particular relates to a reverse osmosis industrial pure water machine with a variable working mode.

背景技术Background Art

反渗透工业纯水机是一种利用反渗透技术进行水处理的设备,反渗透是一种物理过程,在浓溶液侧施加一个大于渗透压的压力,使得浓溶液的溶剂(水)向稀溶液侧流动,从而实现水与杂质的分离。Reverse osmosis industrial pure water machine is a device that uses reverse osmosis technology for water treatment. Reverse osmosis is a physical process that applies a pressure greater than the osmotic pressure on the concentrated solution side, causing the solvent (water) of the concentrated solution to flow to the dilute solution side, thereby achieving separation of water and impurities.

反渗透工业纯水机包括水预处理系统(砂滤器、碳滤器和软化器)、高压泵、反渗透设备,预处理系统用于去除原水中的大颗粒杂质和硬质离子等,高压泵用于将预处理的原水进行加压输送至反渗透设备,反渗透设备中的反渗透膜由高分子材料制成,其具有良好的耐化学腐蚀性和机械强度,能有效阻挡大部分的溶解性盐类、有机物及微生物等杂质而对水不形成阻挡。The reverse osmosis industrial pure water machine includes a water pretreatment system (sand filter, carbon filter and softener), a high-pressure pump, and a reverse osmosis device. The pretreatment system is used to remove large particle impurities and hard ions in the raw water. The high-pressure pump is used to pressurize and transport the pretreated raw water to the reverse osmosis device. The reverse osmosis membrane in the reverse osmosis device is made of polymer materials, which has good chemical corrosion resistance and mechanical strength. It can effectively block most of the impurities such as soluble salts, organic matter and microorganisms without forming a barrier to water.

现有的反渗透工业纯水机在使用过程中还存在如下问题需要解决:The existing reverse osmosis industrial pure water machine still has the following problems to be solved during use:

对于反渗透设备,其在使用一段时间后具有一定的反冲洗能力,通过反冲洗延长反渗透膜的使用周期,但是在反渗透膜的原水侧因长时间使用会附着结晶体,这些结晶体无法通过反冲洗进行清理,当结晶体累积达到一定厚度时会影响反渗透膜的纯水产生率,此时就需要更换新的滤芯,使得成本提高,所以如何通过反冲洗去除反渗透膜原水侧附着的结晶体是需要研究解决的。For reverse osmosis equipment, it has a certain backwashing ability after being used for a period of time. The service life of the reverse osmosis membrane is extended by backwashing. However, crystals will be attached to the raw water side of the reverse osmosis membrane due to long-term use. These crystals cannot be cleaned by backwashing. When the crystals accumulate to a certain thickness, it will affect the pure water production rate of the reverse osmosis membrane. At this time, a new filter element needs to be replaced, which increases the cost. Therefore, how to remove the crystals attached to the raw water side of the reverse osmosis membrane through backwashing needs to be studied and solved.

本发明设计一种工作方式可变的反渗透工业纯水机解决如上问题。The present invention designs a reverse osmosis industrial pure water machine with variable working mode to solve the above problems.

发明内容Summary of the invention

基于此,有必要针对目前的反渗透工业纯水机所存在的问题,提供一种工作方式可变的反渗透工业纯水机,本发明的原水预处理系统中的砂滤器、碳滤器和软化器均采用三层小滤罐结构对水进行逐层依次预处理,且三层小滤罐全部参与生产,实际的水预处理过程中,只有上两层的小滤罐对水进行预处理,而到达底层小滤罐的水已经基本达到要求而无需底层小滤罐参与过滤,因此,在更换其中任意一层滤罐时,其他两层滤罐完全可以满足对水的预处理而依然能保持预处理流量不变,进而保证整个设备的生产效率不受影响。Based on this, it is necessary to provide a reverse osmosis industrial pure water machine with a variable working mode to address the problems existing in the current reverse osmosis industrial pure water machine. The sand filter, carbon filter and softener in the raw water pretreatment system of the present invention all adopt a three-layer small filter tank structure to pretreat the water layer by layer, and all three layers of small filter tanks are involved in production. In the actual water pretreatment process, only the small filter tanks on the upper two layers pretreat the water, and the water reaching the small filter tanks on the bottom layer has basically met the requirements without the need for the small filter tanks on the bottom layer to participate in the filtration. Therefore, when replacing any one layer of the filter tanks, the other two layers of filter tanks can fully meet the pretreatment of the water and still maintain the pretreatment flow rate unchanged, thereby ensuring that the production efficiency of the entire equipment is not affected.

反渗透设备中的反渗透单元的反渗透层具有两级渗透结构,可以对原水进行更加有效的纯化,同时,反渗透层中两级渗透结构之间的第一支撑层在反冲洗压力脉动作用下可以进行适当形变而对一级反渗透膜原水侧附着的结晶体进行刮除清理,脱离一级反渗透膜的结晶体在反冲洗纯水的带动下排出,提高反渗透设备的反冲洗能力,延长其使用寿命,延长更换周期,降低设备维护成本。The reverse osmosis layer of the reverse osmosis unit in the reverse osmosis equipment has a two-stage osmosis structure, which can purify the raw water more effectively. At the same time, the first support layer between the two-stage osmosis structure in the reverse osmosis layer can be appropriately deformed under the action of the backwash pressure pulsation to scrape and clean the crystals attached to the raw water side of the first-stage reverse osmosis membrane. The crystals separated from the first-stage reverse osmosis membrane are discharged under the drive of the backwash pure water, thereby improving the backwash capacity of the reverse osmosis equipment, extending its service life, extending the replacement cycle, and reducing the equipment maintenance cost.

上述目的通过下述技术方案实现:The above purpose is achieved through the following technical solutions:

一种工作方式可变的反渗透工业纯水机,包括原水箱、增压泵、砂滤器、碳滤器、软化器、精密过滤器、高压泵、反渗透设备和纯水箱,所述砂滤器、碳滤器和软化器的结构相同,所述反渗透设备由若干并联的反渗透组件组成,所述反渗透组件包括筒体,所述筒体内设置有若干串联的反渗透单元,所述反渗透单元包括内管,所述内管的管壁上开设有第一进水口,所述内管外套装有外管,所述外管的管壁上开设有与第一进水口相对的第二进水口,所述第二进水口的宽度大于第一进水口的宽度,所述第二进水口处设置有反渗透层,所述反渗透层涡卷缠绕于外管上,所述反渗透层外包裹有外包套,所述外包套与筒体内壁紧贴。A reverse osmosis industrial pure water machine with a variable working mode comprises a raw water tank, a booster pump, a sand filter, a carbon filter, a softener, a precision filter, a high-pressure pump, a reverse osmosis device and a pure water tank, wherein the sand filter, the carbon filter and the softener have the same structure, the reverse osmosis device is composed of a plurality of reverse osmosis components connected in parallel, the reverse osmosis component comprises a cylinder, a plurality of reverse osmosis units connected in series are arranged in the cylinder, the reverse osmosis unit comprises an inner tube, a first water inlet is provided on the tube wall of the inner tube, an outer tube is sleeved outside the inner tube, a second water inlet opposite to the first water inlet is provided on the tube wall of the outer tube, the width of the second water inlet is greater than that of the first water inlet, a reverse osmosis layer is arranged at the second water inlet, the reverse osmosis layer is vortexed and wound on the outer tube, the reverse osmosis layer is wrapped with an outer sheath, and the outer sheath is in close contact with the inner wall of the cylinder.

所述反渗透层包括两个一级膜层和两个二级反渗透膜,两个所述一级膜层分别粘接于第二进水口的两个周向边沿处,两个所述二级反渗透膜分别粘接于第一进水口的两个周向边沿处,两个所述二级反渗透膜的轴向两端用胶封密封,所述一级膜层的外侧密封设置有对一级膜层和二级反渗透膜的径向端密封的不透膜,不透膜与一级膜层之间设有第一支撑层,二级反渗透膜与同侧的一级膜层之间设有第二支撑层,第二支撑层的轴向两端密封;The reverse osmosis layer comprises two primary membrane layers and two secondary reverse osmosis membranes, the two primary membrane layers are respectively bonded to the two circumferential edges of the second water inlet, the two secondary reverse osmosis membranes are respectively bonded to the two circumferential edges of the first water inlet, the axial ends of the two secondary reverse osmosis membranes are sealed with glue seals, the outer side of the primary membrane layer is sealed with an impermeable membrane that seals the radial ends of the primary membrane layer and the secondary reverse osmosis membrane, a first supporting layer is provided between the impermeable membrane and the primary membrane layer, a second supporting layer is provided between the secondary reverse osmosis membrane and the primary membrane layer on the same side, and the axial ends of the second supporting layer are sealed;

进水端反渗透单元的内管和外管被端盖封盖。The inner and outer tubes of the reverse osmosis unit at the water inlet end are capped by end caps.

在其中一个实施例中,所述砂滤器具有三层自上而下依次对原水进行预处理的过滤结构,每层所述过滤结构与第一总管并联,所述第一总管上设置有三个使原水在第一总管与每层过滤结构之间切换的第二开关阀,每层所述过滤结构由六个并联的滤罐组成,所述滤罐的两端通过法兰与管路连接,连接所述滤罐两端的管路上均设置有第一开关阀。In one embodiment, the sand filter has three layers of filtering structures for pre-treating raw water from top to bottom, each layer of the filtering structures is connected in parallel with a first main pipe, and the first main pipe is provided with three second switch valves for switching raw water between the first main pipe and each layer of the filtering structures. Each layer of the filtering structure is composed of six parallel filter tanks, and both ends of the filter tanks are connected to the pipeline through flanges, and the pipelines connecting the two ends of the filter tanks are provided with first switch valves.

在其中一个实施例中,所述滤罐外侧安装有箍套,所述箍套上设置有支座,所述支座通过螺栓与第一支架连接。In one of the embodiments, a hoop is installed on the outside of the filter tank, a support is provided on the hoop, and the support is connected to the first bracket by bolts.

在其中一个实施例中,所述筒体的进水端具有第三进水口,所述筒体的出水端设置有废水管和次纯管,所述次纯管端部封闭且位于筒体端面的中心处,所述次纯管的管壁上具有出水口,所述次纯管与出水端反渗透单元的外管连接,所述次纯管内设置有与筒体连通的纯水管,所述纯水管与出水端反渗透单元的内管连接。In one embodiment, the water inlet end of the cylinder has a third water inlet, and the water outlet end of the cylinder is provided with a wastewater pipe and a secondary pure pipe, the end of the secondary pure pipe is closed and located at the center of the end face of the cylinder, and the wall of the secondary pure pipe has a water outlet, the secondary pure pipe is connected to the outer pipe of the reverse osmosis unit at the water outlet end, and a pure water pipe connected to the cylinder is provided inside the secondary pure pipe, and the pure water pipe is connected to the inner pipe of the reverse osmosis unit at the water outlet end.

在其中一个实施例中,所述纯水管通过第三总管与纯水箱连通,所述第三进水口与高压泵连通。In one of the embodiments, the pure water pipe is connected to the pure water tank through a third main pipe, and the third water inlet is connected to a high-pressure pump.

在其中一个实施例中,所述出水口与第四总管连通,所述废水管与第五总管连通。In one embodiment, the water outlet is connected to the fourth main pipe, and the waste water pipe is connected to the fifth main pipe.

在其中一个实施例中,所述一级膜层由若干通过弹性膜连接的一级反渗透膜组成。In one embodiment, the primary membrane layer is composed of a plurality of primary reverse osmosis membranes connected by elastic membranes.

在其中一个实施例中,所述第一支撑层由并排连接的弹性菱形筒组成。In one embodiment, the first supporting layer is composed of elastic rhombus-shaped tubes connected side by side.

在其中一个实施例中,所述外管与内管之间通过支撑板支撑连接。In one embodiment, the outer tube and the inner tube are supported and connected by a support plate.

在其中一个实施例中,所述反渗透设备通过第二支架固定于地面。In one embodiment, the reverse osmosis device is fixed to the ground via a second bracket.

本发明的有益效果如下:反渗透设备中的反渗透单元的反渗透层具有两级渗透结构,可以对原水进行更加有效的纯化,同时,反渗透层中两级渗透结构之间的第一支撑层在反冲洗压力脉动作用下可以进行适当形变而对一级反渗透膜原水侧附着的结晶体进行刮除清理,脱离一级反渗透膜的结晶体在反冲洗纯水的带动下排出,提高反渗透设备的反冲洗能力,延长其使用寿命,延长更换周期,降低设备维护成本。The beneficial effects of the present invention are as follows: the reverse osmosis layer of the reverse osmosis unit in the reverse osmosis equipment has a two-stage osmosis structure, which can purify raw water more effectively. At the same time, the first support layer between the two-stage osmosis structure in the reverse osmosis layer can be appropriately deformed under the action of backwashing pressure pulsation to scrape and clean the crystals attached to the raw water side of the first-stage reverse osmosis membrane, and the crystals separated from the first-stage reverse osmosis membrane are discharged under the drive of backwashing pure water, thereby improving the backwashing capacity of the reverse osmosis equipment, extending its service life, extending the replacement cycle, and reducing the equipment maintenance cost.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

图1是本发明整体示意图;Fig. 1 is an overall schematic diagram of the present invention;

图2是本发明中的砂滤器示意图;Fig. 2 is a schematic diagram of a sand filter in the present invention;

图3是本发明中砂滤器的侧视剖面示意图;FIG3 is a side cross-sectional schematic diagram of a sand filter in the present invention;

图4是本发明中的砂滤器的局部剖面示意图;FIG4 is a partial cross-sectional schematic diagram of the sand filter of the present invention;

图5是本发明中的砂滤器的俯视剖面示意图;FIG5 is a schematic top cross-sectional view of a sand filter according to the present invention;

图6是本发明中的反渗透设备示意图;FIG6 is a schematic diagram of a reverse osmosis device in the present invention;

图7是本发明中反渗透设备的反渗透单元示意图;FIG7 is a schematic diagram of a reverse osmosis unit of a reverse osmosis device in the present invention;

图8是本发明中反渗透设备的反渗透单元横向剖面示意图;8 is a schematic cross-sectional view of a reverse osmosis unit of a reverse osmosis device according to the present invention;

图9是本发明中反渗透设备的反渗透单元展开的横向剖面示意图;9 is a schematic cross-sectional view of the reverse osmosis unit of the reverse osmosis device of the present invention;

图10是本发明中反渗透单元的反渗透层局部剖面示意图;10 is a partial cross-sectional schematic diagram of the reverse osmosis layer of the reverse osmosis unit of the present invention;

图11是本发明中反渗透单元的内管和外管示意图;FIG11 is a schematic diagram of the inner tube and outer tube of the reverse osmosis unit of the present invention;

图12是本发明中的反渗透组件及其剖面示意图;FIG12 is a reverse osmosis assembly and a cross-sectional schematic diagram thereof in the present invention;

图13是本发明中反渗透组件的进水端结构剖面示意图;13 is a schematic cross-sectional view of the water inlet structure of the reverse osmosis assembly of the present invention;

图14是本发明中反渗透组件的出水端结构剖面示意图;14 is a schematic cross-sectional view of the water outlet structure of the reverse osmosis assembly of the present invention;

图15是本发明中反渗透单元中原水运动状态示意图;15 is a schematic diagram of the movement state of raw water in the reverse osmosis unit of the present invention;

图16是本发明中一级膜层结构示意图;FIG16 is a schematic diagram of the primary membrane structure of the present invention;

图中标号名称:Name of the label in the figure:

101、原水箱;102、增压泵;103、精密过滤器;104、高压泵;105、纯水箱;101. Raw water tank; 102. Booster pump; 103. Precision filter; 104. High pressure pump; 105. Pure water tank;

200、砂滤器;201、第一支架;202、滤罐;203、箍套;204、支座;205、螺栓;206、第一开关阀;207、第一总管;208、第二开关阀;200, sand filter; 201, first bracket; 202, filter tank; 203, hoop; 204, support; 205, bolt; 206, first switch valve; 207, first main pipe; 208, second switch valve;

300、碳滤器;400、软化器;300, carbon filter; 400, softener;

500、反渗透设备;501、第二支架;502、反渗透组件;503、筒体;504、第三进水口;505、废水管;506、次纯管;507、出水口;508、纯水管;509、反渗透单元;510、内管;511、第一进水口;512、支撑板;513、外管;514、第二进水口;515、反渗透层;516、不透膜;517、一级膜层;5171、一级反渗透膜;5172、弹性膜;518、二级反渗透膜;519、第一支撑层;520、第二支撑层;521、胶封;522、外包套;523、端盖;524、第二总管;525、第三总管;526、第四总管;527、第五总管;500, reverse osmosis equipment; 501, second bracket; 502, reverse osmosis assembly; 503, cylinder; 504, third water inlet; 505, waste water pipe; 506, sub-pure pipe; 507, water outlet; 508, pure water pipe; 509, reverse osmosis unit; 510, inner pipe; 511, first water inlet; 512, support plate; 513, outer pipe; 514, second water inlet; 515, reverse osmosis layer; 516, impermeable membrane; 517, primary membrane layer; 5171, primary reverse osmosis membrane; 5172, elastic membrane; 518, secondary reverse osmosis membrane; 519, first supporting layer; 520, second supporting layer; 521, glue seal; 522, outer sleeve; 523, end cover; 524, second main pipe; 525, third main pipe; 526, fourth main pipe; 527, fifth main pipe;

600、垫层。600. Cushion layer.

具体实施方式DETAILED DESCRIPTION

为了使本发明的目的、技术方案及优点更加清楚明白,以下通过实施例,并结合附图,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅用以解释本发明,并不用于限定本发明。In order to make the purpose, technical solution and advantages of the present invention more clearly understood, the present invention is further described in detail below through embodiments and in conjunction with the accompanying drawings. It should be understood that the specific embodiments described herein are only used to explain the present invention and are not used to limit the present invention.

如图1-16所示,一种工作方式可变的反渗透工业纯水机,包括原水箱101、增压泵102、砂滤器200、碳滤器300、软化器400、精密过滤器103、高压泵104、反渗透设备500和纯水箱105,所述砂滤器200、碳滤器300和软化器400的结构相同,所述反渗透设备500包括若干并联的反渗透组件502,所述反渗透组件502包括筒体503,所述筒体503内设置有若干串联的反渗透单元509,所述反渗透单元509包括内管510,所述内管510的管壁上开设有第一进水口511,所述内管510外套装有外管513,所述外管513的管壁上开设有与第一进水口511相对的第二进水口514,所述第二进水口514的宽度大于第一进水口511的宽度,所述第二进水口514处设置有反渗透层515,所述反渗透层515涡卷缠绕于外管513上,所述反渗透层515外包裹有外包套522,所述外包套522与筒体503内壁紧贴。As shown in FIG1-16, a reverse osmosis industrial pure water machine with a variable working mode includes a raw water tank 101, a booster pump 102, a sand filter 200, a carbon filter 300, a softener 400, a precision filter 103, a high-pressure pump 104, a reverse osmosis device 500 and a pure water tank 105. The sand filter 200, the carbon filter 300 and the softener 400 have the same structure. The reverse osmosis device 500 includes a plurality of reverse osmosis components 502 connected in parallel. The reverse osmosis component 502 includes a cylinder 503. The cylinder 503 is provided with a plurality of reverse osmosis units 509 connected in series. The permeability unit 509 includes an inner tube 510, a first water inlet 511 is provided on the tube wall of the inner tube 510, an outer tube 513 is mounted outside the inner tube 510, a second water inlet 514 opposite to the first water inlet 511 is provided on the tube wall of the outer tube 513, the width of the second water inlet 514 is greater than the width of the first water inlet 511, a reverse osmosis layer 515 is provided at the second water inlet 514, the reverse osmosis layer 515 is spirally wound around the outer tube 513, the reverse osmosis layer 515 is wrapped with an outer sheath 522, and the outer sheath 522 is in close contact with the inner wall of the cylinder 503.

所述反渗透层515包括两个一级膜层517和两个二级反渗透膜518,两个所述一级膜层517分别粘接于第二进水口514的两个周向边沿处,两个所述二级反渗透膜518分别粘接于第一进水口511的两个周向边沿处,两个所述二级反渗透膜518的轴向两端用胶封521密封,所述一级膜层517的外侧密封设置有对一级膜层517和二级反渗透膜518的径向端密封的不透膜516,所述二级反渗透膜518与同侧一级膜层517之间设置有第二支撑层520,所述第二支撑层520的轴向两端用胶封521密封,所述不透膜516与一级膜层517之间设置有第一支撑层519。The reverse osmosis layer 515 includes two primary membrane layers 517 and two secondary reverse osmosis membranes 518, the two primary membrane layers 517 are respectively bonded to the two circumferential edges of the second water inlet 514, the two secondary reverse osmosis membranes 518 are respectively bonded to the two circumferential edges of the first water inlet 511, the axial ends of the two secondary reverse osmosis membranes 518 are sealed with glue seals 521, the outer side of the primary membrane layer 517 is sealed with an impermeable membrane 516 for sealing the radial ends of the primary membrane layer 517 and the secondary reverse osmosis membrane 518, a second support layer 520 is arranged between the secondary reverse osmosis membrane 518 and the primary membrane layer 517 on the same side, the axial ends of the second support layer 520 are sealed with glue seals 521, and a first support layer 519 is arranged between the impermeable membrane 516 and the primary membrane layer 517.

位于进水端的反渗透单元509的内管510和外管513被端盖523封盖,如图13所示。The inner tube 510 and the outer tube 513 of the reverse osmosis unit 509 at the water inlet end are capped by end caps 523 , as shown in FIG. 13 .

原水预处理系统中的砂滤器200、碳滤器300和软化器400均采用三层过滤结构对水进行逐层依次预处理,且三层过滤结构全部参与生产,实际的水预处理过程中,只有上两层的过滤结构对水进行预处理,而到达底层的过滤结构的水已经基本达到要求而无需底层的过滤结构参与过滤,因此,在更换其中任意一层过滤结构时,其他两层过滤结构完全可以满足对水的预处理而依然能保持预处理流量不变,进而保证整个设备的生产效率不受影响。The sand filter 200, carbon filter 300 and softener 400 in the raw water pretreatment system all adopt a three-layer filter structure to pretreat the water layer by layer, and all three-layer filter structures are involved in the production. In the actual water pretreatment process, only the upper two layers of the filter structure pretreat the water, and the water reaching the bottom filter structure has basically met the requirements without the need for the bottom filter structure to participate in the filtration. Therefore, when any one of the filter structures is replaced, the other two layers of the filter structure can fully meet the water pretreatment requirements while still maintaining the pretreatment flow rate unchanged, thereby ensuring that the production efficiency of the entire equipment is not affected.

反渗透设备500中的反渗透单元509的反渗透层515具有两级渗透结构,可以对原水进行更加有效的纯化,同时,反渗透层515中两级渗透结构之间的第一支撑层519在反冲洗压力脉动作用下可以进行适当形变而对一级反渗透膜5171原水侧附着的结晶体进行刮除清理,脱离一级反渗透膜5171的结晶体在反冲洗纯水的带动下排出,提高反渗透设备500的反冲洗能力,延长其使用寿命,延长更换周期,降低设备维护成本。The reverse osmosis layer 515 of the reverse osmosis unit 509 in the reverse osmosis equipment 500 has a two-stage osmosis structure, which can purify the raw water more effectively. At the same time, the first support layer 519 between the two-stage osmosis structure in the reverse osmosis layer 515 can be appropriately deformed under the action of the backwash pressure pulsation to scrape and clean the crystals attached to the raw water side of the first-stage reverse osmosis membrane 5171. The crystals separated from the first-stage reverse osmosis membrane 5171 are discharged under the drive of the backwash pure water, thereby improving the backwash capacity of the reverse osmosis equipment 500, extending its service life, extending the replacement cycle, and reducing the equipment maintenance cost.

上述反渗透层的厚度极薄,图8、9、10、15中的反渗透层仅是为了突出表述其结构特点的示意。The thickness of the above-mentioned reverse osmosis layer is extremely thin, and the reverse osmosis layer in Figures 8, 9, 10, and 15 is only for highlighting the schematic representation of its structural characteristics.

在进一步实施例中,如图2、3、4所示,所述砂滤器200、碳滤器300和软化器400均具有三层自上而下依次对原水进行预处理的过滤结构,每层所述过滤结构与第一总管207并联,所述第一总管207上设置有三个使原水在第一总管207与每层过滤结构之间切换的第二开关阀208,每层所述过滤结构包括六个并联的滤罐202,所述滤罐202的两端通过法兰与管路连接,连接所述滤罐202两端的管路上均设置有第一开关阀206。In a further embodiment, as shown in Figures 2, 3, and 4, the sand filter 200, the carbon filter 300, and the softener 400 all have three layers of filtering structures for pre-treating raw water from top to bottom, and each layer of the filtering structure is connected in parallel with the first main pipe 207. The first main pipe 207 is provided with three second switch valves 208 for switching raw water between the first main pipe 207 and each layer of the filtering structure. Each layer of the filtering structure includes six parallel filter tanks 202, and both ends of the filter tank 202 are connected to the pipeline through flanges. The pipelines connecting the two ends of the filter tank 202 are provided with first switch valves 206.

在进一步实施例中,如图4、5所示,所述滤罐202外侧安装有箍套203,所述箍套203上设置有支座204,所述支座204通过螺栓205与第一支架201连接。In a further embodiment, as shown in FIGS. 4 and 5 , a hoop 203 is installed on the outside of the filter tank 202 , a support 204 is provided on the hoop 203 , and the support 204 is connected to the first bracket 201 via bolts 205 .

在进一步实施例中,如图12、13、14所示,所述筒体503的进水端具有第三进水口504,所述筒体503的出水端设置有废水管505和次纯管506,所述次纯管506端部封闭且位于筒体503端面的中心处,所述次纯管506的管壁上具有出水口507,所述次纯管506与位于出水端的反渗透单元509的外管513连接,所述次纯管506内设置有与筒体503连通的纯水管508,所述纯水管508与位于出水端的反渗透单元509的内管510连接。In a further embodiment, as shown in Figures 12, 13, and 14, the water inlet end of the cylinder 503 has a third water inlet 504, and the water outlet end of the cylinder 503 is provided with a wastewater pipe 505 and a secondary pure pipe 506, the end of the secondary pure pipe 506 is closed and located at the center of the end face of the cylinder 503, and the tube wall of the secondary pure pipe 506 has a water outlet 507, the secondary pure pipe 506 is connected to the outer tube 513 of the reverse osmosis unit 509 located at the water outlet end, and a pure water pipe 508 connected to the cylinder 503 is provided in the secondary pure pipe 506, and the pure water pipe 508 is connected to the inner tube 510 of the reverse osmosis unit 509 located at the water outlet end.

在进一步实施例中,如图1、6所示,所述纯水管508通过第三总管525与纯水箱105连通,所述第三进水口504与高压泵104连通。In a further embodiment, as shown in FIGS. 1 and 6 , the pure water pipe 508 is connected to the pure water tank 105 through the third main pipe 525 , and the third water inlet 504 is connected to the high-pressure pump 104 .

在进一步实施例中,如图1、6所示,所述出水口507与第四总管526连通,所述废水管505与第五总管527连通。In a further embodiment, as shown in FIGS. 1 and 6 , the water outlet 507 is connected to the fourth main pipe 526 , and the waste water pipe 505 is connected to the fifth main pipe 527 .

在进一步实施例中,如图9所示,所述一级膜层517包括若干通过弹性膜5172连接的一级反渗透膜5171。In a further embodiment, as shown in FIG. 9 , the primary membrane layer 517 includes a plurality of primary reverse osmosis membranes 5171 connected by elastic membranes 5172 .

在进一步实施例中,如图9、10所示,所述第一支撑层519由并排连接的弹性菱形筒组成。In a further embodiment, as shown in FIGS. 9 and 10 , the first supporting layer 519 is composed of elastic rhombus-shaped cylinders connected side by side.

在进一步实施例中,如图8、9所示,所述外管513与内管510之间通过支撑板512支撑连接。图8中具有垫层,在反渗透层515缠绕过程中,需要垫层支撑第一圈缠绕的反渗透层515,让缠绕的第二圈的反渗透层515更加平滑。垫层的材料选用耐腐蚀且设备中可长时间使用的材料即可。In a further embodiment, as shown in Figs. 8 and 9, the outer tube 513 and the inner tube 510 are supported and connected by a support plate 512. Fig. 8 has a cushion layer, and during the winding process of the reverse osmosis layer 515, the cushion layer is required to support the reverse osmosis layer 515 of the first winding circle, so that the reverse osmosis layer 515 of the second winding circle is smoother. The material of the cushion layer can be selected from corrosion-resistant materials that can be used for a long time in the equipment.

在进一步实施例中,如图6所示,所述反渗透设备500通过第二支架501固定于地面。In a further embodiment, as shown in FIG. 6 , the reverse osmosis device 500 is fixed to the ground via a second bracket 501 .

在进一步实施例中,上述一级反渗透膜的膜孔径与二级反渗透膜的膜孔径大小相同,或者一级反渗透膜的膜孔径略大于二级反渗透膜的膜孔径大小。In a further embodiment, the pore size of the primary reverse osmosis membrane is the same as that of the secondary reverse osmosis membrane, or the pore size of the primary reverse osmosis membrane is slightly larger than that of the secondary reverse osmosis membrane.

本发明的运行流程如下:The operation process of the present invention is as follows:

原水预处理系统中的砂滤器200、碳滤器300和软化器400均采用三层过滤结构对水进行逐层依次预处理,且三层过滤结构全部参与生产,在实际的原水预处理过程中,只有上两层的过滤结构对水进行预处理,而到达底层的过滤结构的水已经基本达到要求而无需底层的过滤结构参与过滤,因此,在更换其中任意一层过滤结构时,其他两层过滤结构完全可以满足对水的预处理而依然能保持预处理流量不变,进而保证整个设备的生产效率不受影响。The sand filter 200, carbon filter 300 and softener 400 in the raw water pretreatment system all adopt a three-layer filter structure to pretreat the water layer by layer, and all three layers of the filter structure are involved in the production. In the actual raw water pretreatment process, only the upper two layers of the filter structure pretreat the water, and the water reaching the bottom filter structure has basically met the requirements without the need for the bottom filter structure to participate in the filtration. Therefore, when any one layer of the filter structure is replaced, the other two layers of the filter structure can fully meet the water pretreatment requirements while still maintaining the pretreatment flow rate unchanged, thereby ensuring that the production efficiency of the entire equipment is not affected.

在三层过滤结构同时参与原水的预处理时,第一总管上的三个第二开关阀208均处于关闭状态,每个滤罐202的两端第一开关阀206均处于打开状态,当需要更换任意一层的滤罐202时,先将该层的滤罐202对应的第一总管207上的第二开关阀208打开,在将该层中每个滤罐202两端的第一开关阀206关闭,使得该层的滤罐202与管路之间的连通切断并完成第一总管207与该层滤罐202的切换,然后,将该层的滤罐202拆下并更换新的滤罐202,更换结束后,先将该层的滤罐202两端的第一开关阀206打开,在将该层的滤罐202对应的第二开关阀208关闭,从而完成新的滤罐202的接入。When the three-layer filtration structure participates in the pretreatment of raw water at the same time, the three second switch valves 208 on the first main pipe are all in a closed state, and the first switch valves 206 at both ends of each filter tank 202 are all in an open state. When it is necessary to replace the filter tank 202 of any layer, first open the second switch valve 208 on the first main pipe 207 corresponding to the filter tank 202 of the layer, and then close the first switch valves 206 at both ends of each filter tank 202 in the layer, so that the connection between the filter tank 202 of the layer and the pipeline is cut off and the switching between the first main pipe 207 and the filter tank 202 of the layer is completed. Then, remove the filter tank 202 of the layer and replace it with a new filter tank 202. After the replacement is completed, open the first switch valves 206 at both ends of the filter tank 202 of the layer, and then close the second switch valve 208 corresponding to the filter tank 202 of the layer, so as to complete the connection of the new filter tank 202.

反渗透设备500中的反渗透单元509的反渗透层515具有两级渗透结构,可以对原水进行更加有效的纯化,同时,反渗透层515中两级渗透结构之间的第一支撑层519在反冲洗压力脉动作用下可以进行适当形变而对一级反渗透膜5171原水侧附着的结晶体进行刮除清理,脱离一级反渗透膜5171的结晶体在反冲洗纯水的带动下排出,提高反渗透设备500的反冲洗能力,延长其使用寿命,延长更换周期,降低设备维护成本。The reverse osmosis layer 515 of the reverse osmosis unit 509 in the reverse osmosis equipment 500 has a two-stage osmosis structure, which can purify the raw water more effectively. At the same time, the first support layer 519 between the two-stage osmosis structure in the reverse osmosis layer 515 can be appropriately deformed under the action of the backwash pressure pulsation to scrape and clean the crystals attached to the raw water side of the first-stage reverse osmosis membrane 5171. The crystals separated from the first-stage reverse osmosis membrane 5171 are discharged under the drive of the backwash pure water, thereby improving the backwash capacity of the reverse osmosis equipment 500, extending its service life, extending the replacement cycle, and reducing the equipment maintenance cost.

如图16所示,当来自高压泵104的高压原水从反渗透组件502的第三进水口504进入筒体503后,高压原水进入反渗透单元509的反渗透层515的两层第一支撑层519并沿轴向向出水端运动,经过第一支撑层519的高压原水在压力作用下穿过一级膜层517进入第二支撑层520形成次纯水而完成第一级的纯化,原水中的较大杂质被阻挡在一级膜层517的外侧,进入第二支撑层520的次纯水一部分经第二进水口514进入外管513内流向第四总管526进行回收再处理,一部分经二级反渗透膜518进入两个二级反渗透膜518之间的空间并经第一进水口511进入内管510,从而完成原水的纯化,次纯水中的杂质被阻挡于二级反渗透膜518的外侧,进入内管510的纯水经纯水管508和第三总管525进入纯水箱105。As shown in FIG. 16 , after the high-pressure raw water from the high-pressure pump 104 enters the cylinder 503 from the third water inlet 504 of the reverse osmosis component 502, the high-pressure raw water enters the two first support layers 519 of the reverse osmosis layer 515 of the reverse osmosis unit 509 and moves axially toward the water outlet. The high-pressure raw water passing through the first support layer 519 passes through the primary membrane layer 517 under pressure and enters the second support layer 520 to form sub-pure water and complete the first-stage purification. The larger impurities in the raw water are blocked on the outside of the primary membrane layer 517. Part of the sub-pure water entering the second supporting layer 520 enters the outer tube 513 through the second water inlet 514 and flows to the fourth main pipe 526 for recovery and reprocessing, and part of it enters the space between the two secondary reverse osmosis membranes 518 through the secondary reverse osmosis membrane 518 and enters the inner tube 510 through the first water inlet 511, thereby completing the purification of the raw water. The impurities in the sub-pure water are blocked on the outside of the secondary reverse osmosis membrane 518, and the pure water entering the inner tube 510 enters the pure water tank 105 through the pure water pipe 508 and the third main pipe 525.

一级膜层517外侧会随着时间累积结晶体,结晶体对一级膜层517形成堵塞而影响一级膜层517对水的纯化效率,此时,将第四总管526和第五总管527关闭,通过第三总管525反向向反渗透组件502内加入高压纯水,高压纯水进入反渗透单元509的内管510并在压力作用下反向依次经二级反渗透膜518、第二支撑层520、一级膜层517、第一支撑层519和第三进水口504出去,在纯水经过一级膜层517的过程中,使得为纯水加压的压力进行脉动,由于一级膜层517由若干被弹性膜5172连接的一级反渗透膜5171组成,弹性膜5172的作用是通过弹性膜5172发生形变使得一级膜层517整体可发生形变与第一支撑层519产生相对运动,而一级反渗透膜5171不发生形变并保证自身对水的纯化作用,压力脉动会使得纯水在经过一级膜层517时带动一级膜层517进行往复的膨胀和收缩,一级反渗透膜5171不发生形变而弹性膜5172发生形变,同时,第一支撑层519在一级膜层517的膨胀挤压下也产生适当形变,使得第一支撑层519与一级膜层517产生相对运动,第一支撑层519对一级膜层517外侧附着的结晶体进行刮除清理,脱离一级膜层517的结晶体会随高压纯水反向排出,从而达到反向冲洗结晶体的目的,提高设备利用率,延长反渗透设备500使用周期,降低设备维修成本。As time goes by, crystals will accumulate on the outside of the primary membrane layer 517, which will block the primary membrane layer 517 and affect the water purification efficiency of the primary membrane layer 517. At this time, the fourth main pipe 526 and the fifth main pipe 527 are closed, and high-pressure pure water is added to the reverse osmosis component 502 through the third main pipe 525. The high-pressure pure water enters the inner pipe 510 of the reverse osmosis unit 509 and goes out in reverse order through the secondary reverse osmosis membrane 518, the second support layer 520, the primary membrane layer 517, the first support layer 519 and the third water inlet 504 under the action of pressure. In the process of pure water passing through the primary membrane layer 517, the pressure pressurized for the pure water pulsates. Since the primary membrane layer 517 is composed of a plurality of primary reverse osmosis membranes 5171 connected by elastic membranes 5172, the function of the elastic membranes 5172 is to deform the primary membrane layer 5172 so that the primary membrane layer 5 17 as a whole can be deformed and produce relative movement with the first support layer 519, while the primary reverse osmosis membrane 5171 does not deform and ensures its own purification effect on water. The pressure pulsation will cause the pure water to drive the primary membrane layer 517 to expand and contract reciprocatingly when passing through the primary membrane layer 517. The primary reverse osmosis membrane 5171 does not deform while the elastic membrane 5172 deforms. At the same time, the first support layer 519 also produces appropriate deformation under the expansion and compression of the primary membrane layer 517, so that the first support layer 519 and the primary membrane layer 517 produce relative movement. The first support layer 519 scrapes and cleans the crystals attached to the outside of the primary membrane layer 517, and the crystals separated from the primary membrane layer 517 will be discharged in the reverse direction with the high-pressure pure water, thereby achieving the purpose of reverse flushing the crystals, improving the equipment utilization rate, extending the service life of the reverse osmosis equipment 500, and reducing the equipment maintenance cost.

本发明中采用了两级反渗透膜的设计,有益效果在于,在一级膜层形变过程中,不发生形变的一级反渗透膜虽然不发生形变,但是会受到拉伸力,多次清理结晶体后,可能会出现永久拉伸变形,此时会影响渗透能力。所以设计的二级反渗透膜能够保证即使一级膜层517有渗透问题,内管得到的水依然是纯水,保证了纯水的质量。The present invention adopts a two-stage reverse osmosis membrane design, which has the beneficial effect that, during the deformation process of the primary membrane layer, the primary reverse osmosis membrane that does not deform does not deform, but will be subjected to tensile force. After cleaning the crystals many times, permanent tensile deformation may occur, which will affect the permeability. Therefore, the designed secondary reverse osmosis membrane can ensure that even if the primary membrane layer 517 has a permeation problem, the water obtained by the inner tube is still pure water, thereby ensuring the quality of the pure water.

上述一级反渗透膜的空隙与二级反渗透膜空隙大小相同,或者一级反渗透膜的空隙略大于二级反渗透膜空隙大小。二级反渗透膜空隙与现有纯水反渗透膜空隙大小相同,能够通过反渗透,得到工业使用的纯水。The voids of the primary reverse osmosis membrane are the same as those of the secondary reverse osmosis membrane, or the voids of the primary reverse osmosis membrane are slightly larger than those of the secondary reverse osmosis membrane. The voids of the secondary reverse osmosis membrane are the same as those of the existing pure water reverse osmosis membrane, and pure water for industrial use can be obtained through reverse osmosis.

Claims (8)

1. A reverse osmosis industrial water purifier with a changeable working mode comprises reverse osmosis equipment; the reverse osmosis equipment comprises a plurality of reverse osmosis components which are connected in parallel;
the reverse osmosis component comprises a barrel body, a plurality of reverse osmosis units connected in series are arranged in the barrel body, each reverse osmosis unit comprises an inner pipe, a first water inlet is formed in the pipe wall of the inner pipe, an outer pipe is sleeved outside the inner pipe, a second water inlet with the width larger than that of the first water inlet is formed in the position, corresponding to the first water inlet, of the pipe wall of the outer pipe, an reverse osmosis layer is arranged at the second water inlet, and a scroll of the reverse osmosis layer is wound on the outer pipe;
The reverse osmosis layer comprises two first-stage membrane layers and two second-stage reverse osmosis membranes, the two first-stage membrane layers are respectively adhered to two circumferential edges of the second water inlet, the two second-stage reverse osmosis membranes are respectively adhered to two circumferential edges of the first water inlet, the two second-stage reverse osmosis membranes are sealed at the two axial ends, an impermeable membrane for sealing the radial ends of the first-stage membrane layers and the second-stage reverse osmosis membranes is sealed at the outer side of the first-stage membrane layers, a first supporting layer is arranged between the impermeable membrane and the first-stage membrane layers, a second supporting layer is arranged between the second-stage reverse osmosis membranes and the first-stage membrane layers at the same side, and the two axial ends of the second supporting layer are sealed;
The inner pipe and the outer pipe of the reverse osmosis unit positioned at the water inlet end are sealed and covered by the end cover;
The first-stage membrane layer comprises a plurality of first-stage reverse osmosis membranes connected through elastic membranes; the first supporting layer is composed of elastic diamond cylinders connected side by side.
2. The variable mode of operation reverse osmosis industrial water purifier of claim 1 wherein the reverse osmosis layer is covered by an outer jacket which is in close contact with the inner wall of the cylinder.
3. The variable-working-mode reverse osmosis industrial water purifier according to claim 1, wherein the water inlet end of the cylinder is provided with a third water inlet, the water outlet end of the cylinder is provided with a waste water pipe and a secondary pure pipe, the end of the secondary pure pipe is closed and positioned at the center of the end face of the cylinder, the pipe wall of the secondary pure pipe is provided with a water outlet, the secondary pure pipe is connected with the outer pipe of the reverse osmosis unit positioned at the water outlet end, the secondary pure pipe is internally provided with a pure water pipe communicated with the cylinder, and the pure water pipe is connected with the inner pipe of the reverse osmosis unit positioned at the water outlet end.
4. A variable mode of operation reverse osmosis industrial water purifier according to claim 3, wherein the reverse osmosis industrial water purifier further comprises a raw water tank, a booster pump, a sand filter, a carbon filter, a softener, a precision filter, a high pressure pump and a pure water tank, wherein the sand filter, the carbon filter and the softener are identical in structure, and the reverse osmosis device is connected between the high pressure pump and the pure water tank.
5. The variable-working-mode reverse osmosis industrial water purifier according to claim 4, wherein the sand filter, the carbon filter and the softener are all provided with three layers of filtering structures for sequentially preprocessing raw water from top to bottom, each layer of filtering structure is connected with the first main pipe in parallel, three second switching valves for switching raw water between the first main pipe and each layer of filtering structure are arranged on the first main pipe, each layer of filtering structure comprises six filtering tanks connected in parallel, two ends of each filtering tank are connected with pipelines, and the pipelines connected with two ends of each filtering tank are all provided with the first switching valves.
6. The variable mode of operation reverse osmosis industrial water purifier of claim 5 wherein the canister is provided with a collar having a support attached thereto and coupled to the first support.
7. The variable mode of operation reverse osmosis industrial water purifier of claim 4 wherein the purified water tube is in communication with the purified water tank via a third manifold and the third water inlet is in communication with the high pressure pump;
the water outlet is communicated with the fourth main pipe, and the waste pipe is communicated with the fifth main pipe.
8. The variable mode of operation reverse osmosis industrial water purifier of claim 1 wherein the outer tube is supportably connected to the inner tube by a support plate.
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