WO2022032731A1 - Spiral-wound membrane element having scale inhibition function - Google Patents
Spiral-wound membrane element having scale inhibition function Download PDFInfo
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- WO2022032731A1 WO2022032731A1 PCT/CN2020/111594 CN2020111594W WO2022032731A1 WO 2022032731 A1 WO2022032731 A1 WO 2022032731A1 CN 2020111594 W CN2020111594 W CN 2020111594W WO 2022032731 A1 WO2022032731 A1 WO 2022032731A1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
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- the invention relates to a roll-type membrane element in the field of water treatment membranes.
- Surface modification methods usually include surface coating, surface graft modification and surface chemical synthesis modification.
- the surface coating modification method generally refers to the direct coating of a polymer material or surfactant on the surface of the membrane. During the coating process, new chemical bonds are generally not formed with the surface of the membrane, and the chemical structure of the surface of the membrane is not destroyed. , Mainly through physical action, such as van der Waals force or electrostatic force between molecules, the surface modifier is attached to the membrane surface, thereby forming a protective layer, improving the membrane surface potential, roughness or hydrophilicity.
- the number, length, width of the membrane leaves, the thickness and geometric structure of the raw water and the net water diversion grid have a certain influence on the fouling of the membrane, among which the raw water diversion
- the different designs of the grids have a great influence on the mass transfer behavior and pressure loss of the raw water, and thus have a great influence on the membrane fouling capacity accordingly.
- the purpose of the present invention is to provide a roll-type membrane element and the material and structure of the raw water guide net to improve the anti-scaling performance of the membrane element, which is especially suitable for the application of high-hardness wastewater environment.
- the present invention provides a roll-type membrane element with a scale-inhibiting function, comprising a water-producing central pipe (1) and at least one group of water-purifying membrane sheets wound on the water-producing central pipe;
- the inside and outside sequentially include a produced water diversion net (2), a first separation membrane (3), a raw water diversion net (4), and a second separation membrane (5);
- the raw water diversion net (4) comprises metal The film sheet (6), and the plastic coarse fiber mesh or alloy wire mesh (7) arranged on both surfaces of the metal film sheet;
- the water production center pipe (1) is hollow, one end is open, the other end is closed, and the pipe A group of water passage holes (8) are arranged on the wall, and the water passage holes (8) are communicated with the produced water diversion net (2).
- the plastic coarse fiber mesh or alloy metal wire mesh (7) distributed on both sides of the metal film sheet (6) of the raw water guiding net (4) is distributed at an angle of 20-160 degrees with the central pipe; the plastic coarse fiber The spacing between the mesh or alloy wire mesh (7) is 0.2-5mm.
- the diameter of the plastic coarse fiber mesh or alloy wire mesh (7) is 0.1-0.7 mm, and the thickness of the metal film sheet (6) is 5-200 microns.
- the metal thin film sheet (6) is made of the following parts by weight: 34-70 parts of copper, 2-30 parts of zinc, 10-25 parts of nickel, 2-5 parts of tin, and 3-10 parts of iron .
- the first separation membrane (3) and the second separation membrane (5) are independently reverse osmosis membranes, nanofiltration membranes or ultrafiltration membranes.
- a sealing ring is provided at the contact point between the water passage hole (8) and the produced water diversion net (2).
- the plastic coarse fiber web is a plastic coarse fiber web with a scale-inhibiting alloy coating on the surface
- the coating is prepared by the following method: soak the plastic coarse fiber web with IPA solution for 1 hour and then rinse it repeatedly with IPA Three times, drying; then soaked in an aqueous solution containing 4.0wt% potassium dichromate and 3.0wt% sulfuric acid for 1 hour, rinsed three times with pure water; then soaked in an aqueous solution containing 0.3wt% SnCl2 and 2.5wt% hydrochloric acid for 2min, take out After immersion in an aqueous solution containing 0.1wt% PdCl2 and 1.0wt% hydrochloric acid for 10 minutes, rinsed with pure water three times to complete the surface activation of the fiber web; immerse the activated plastic coarse fiber web into the electroless plating solution for 5-10 minutes, pass Controlling the deposition time, metal Cu of about 0.2-1 micron is uniformly plated on the surface of the PP fiber web; wherein
- the roll-type membrane element provided by the present invention is composed of a scale-inhibiting alloy metal film sheet, and a plastic coarse fiber mesh or alloy wire mesh coated with scale-inhibiting alloy on both surfaces of the metal film sheet.
- the antibacterial function makes the membrane element not easy to scale on the membrane surface when processing raw water with high hardness, which improves the service life of the membrane.
- Figure 1 is a schematic structural diagram of a rolled membrane element with anti-scaling function (partially unfolded);
- Figure 2 is a schematic diagram of the combined structure of the raw water diversion net
- a roll-type membrane element with a scale-inhibiting function comprising a water-producing central pipe (1) and at least one group of water-purifying membrane sheets wound on the water-producing central pipe;
- the raw water diversion net (4) includes a metal film sheet (6), And the plastic thick fiber mesh or alloy metal wire mesh (7) arranged on both surfaces of the metal film sheet;
- the water production center pipe (1) is hollow, one end is open, the other end is closed, and a group of pipes are arranged on the pipe wall.
- the water hole (8) is communicated with the produced water diversion network (2).
- a sealing ring is provided at the contact between the water passage hole (8) and the produced water diversion net (2).
- the first separation membrane (3) and the second separation membrane (5) are both reverse osmosis membranes.
- the plastic thick fiber net is a plastic thick fiber net with a scale-inhibiting alloy coating on the surface, and the coating is prepared by the following method: soak the plastic thick fiber net with IPA solution for 1 hour, then rinse it with IPA repeatedly for three times, and dry it; Soak in an aqueous solution containing 4.0wt% potassium dichromate and 3.0wt% sulfuric acid for 1 hour, rinse with pure water for three times; then infiltrate into an aqueous solution containing 0.3wt% SnCl2 and 2.5wt% hydrochloric acid for 2min, take it out and immerse it in 0.1wt% hydrochloric acid %PdCl2 and 1.0wt% hydrochloric acid solution for 10 minutes, rinsed with pure water three times to complete the surface activation of the fiber web; immerse the activated plastic coarse fiber web into the electroless plating solution for 5-10 minutes, and by controlling the deposition time, about 0.2-1 micron metal Cu is uniformly plated on the surface of the PP fiber
- the plastic coarse fiber mesh or alloy metal wire mesh (7) distributed on both sides of the metal film sheet (6) of the raw water guiding net (4) is distributed at an angle of 20-160 degrees with the central pipe; the plastic coarse fiber mesh or alloy The spacing between the wire meshes (7) is 0.2-5mm.
- the diameter of the plastic coarse fiber mesh or alloy metal wire mesh (7) is 0.1-0.7 mm, and the thickness of the metal film sheet (6) is 5-200 microns.
- the metal thin film sheet (6) is made of the following parts by weight: 34-70 parts of copper, 2-30 parts of zinc, 10-25 parts of nickel, 2-5 parts of tin, and 3-10 parts of iron.
- the first separation membrane (3) and the second separation membrane (5) are independently reverse osmosis membranes, nanofiltration membranes or ultrafiltration membranes.
- Comparative example six pieces of general-purpose PP mesh 32X55cm, diameter 0.5mm, and spacing 0.3mm were selected for the raw water mesh. Six 32cmx106cm reverse osmosis membranes are folded in half, and the six raw water nets are inserted between the folded membranes to make a rolled membrane element. The water flux and desalination rate were tested using the above conditions.
- Test Example 1 The raw water mesh group includes an alloy film sheet with a thickness of about 50 microns and a raw water mesh with a thickness of 0.25 mm on both sides. Similarly, 6 groups of raw water network groups and reverse osmosis membranes of the same area were selected, and the others were the same as those in the comparative example. The test conditions were the same as in the comparative example.
- Embodiment 2-12 select different raw water net groups for use, and concrete raw water net group constitutions and test results are shown in Table 1.
- the raw water reticulation group of the present invention improves the anti-scaling performance of the membrane to varying degrees.
- a proper proportion of alloy metal sheets plays a greater role in the raw water mesh group than the alloy wire mesh itself.
- Table 1 list of comparative examples and examples
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Abstract
A spiral-wound membrane element having a scale inhibition function. The spiral-wound membrane element comprises a water production central tube (1) and at least one water purification membrane group wound around the water production central tube (1). The water purification membrane group sequentially comprises, from inside to outside, a water production flow guide mesh (2), a first separation membrane (3), a raw water flow guide mesh (4) and a second separation membrane (5). The raw water flow guide mesh (4) comprises a metal thin membrane (6), and plastic coarse fiber meshes or alloy metal wire meshes (7) arranged on two surfaces of the metal thin membrane (6). The water production central tube (1) is hollow, one end of the water production central tube being open, the other end of the water production central tube being closed, a group of water-passing holes (8) being provided in a tube wall of the water production central tube, and the water-passing holes (8) being in communication with the water production flow guide mesh (2). The raw water flow guide mesh (4) of the membrane element is composed of the scale inhibition alloy metal thin membrane (6) and the plastic coarse fiber meshes or alloy metal wire meshes (7), which are located on the surfaces of two sides of the metal thin membrane (6) and plated with scale inhibition alloys. Due to the scale inhibition and bacteriostasis functions of alloy metals, scaling on the surface of a membrane does not easily occur when raw water with a high hardness is treated by means of the membrane element, thereby prolonging the service life of the membrane.
Description
本发明涉及一种水处理膜领域的卷式膜元件。The invention relates to a roll-type membrane element in the field of water treatment membranes.
由于水污染的日益加剧,人们对饮水质量的需求提高,目前市场上出现了大量反渗透及纳滤净水设备,然而由于原水中的污染物成分多种多样,有些很容易附着在膜表面,造成膜水通量的衰减,其中水的硬度、微生物及胶体对膜的表面的污染最为常见,因此如何提高耐此类污染性能的反渗透或纳滤膜元件成为业界研发焦点之一。Due to the increasing water pollution, people's demand for drinking water quality has increased, and a large number of reverse osmosis and nanofiltration water purification equipment have appeared on the market. Causes the attenuation of membrane water flux, among which water hardness, microorganisms and colloids pollute the surface of the membrane the most common. Therefore, how to improve the resistance to such pollution of reverse osmosis or nanofiltration membrane elements has become one of the focus of research and development in the industry.
通常,膜表面的改性,及特殊导流设计能提高膜的耐污染能力。Usually, modification of the membrane surface, and special diversion design can improve the fouling resistance of the membrane.
表面改性方法通常包括,表面涂覆,表面接枝改性及表面化学合成改性等。表面涂覆改性法一般是指将一种聚合物材料、或表面活性剂直接涂覆敷到膜表面,涂覆过程中,一般不与膜表面产生新的化学键,不破坏膜表面的化学结构,主要通过物理作用,如分子之间的范德华力或静电作用力,使表面改性剂附着于膜表面上,从而形成一层保护层,改善了膜表面电位、粗糙度或亲水性。Surface modification methods usually include surface coating, surface graft modification and surface chemical synthesis modification. The surface coating modification method generally refers to the direct coating of a polymer material or surfactant on the surface of the membrane. During the coating process, new chemical bonds are generally not formed with the surface of the membrane, and the chemical structure of the surface of the membrane is not destroyed. , Mainly through physical action, such as van der Waals force or electrostatic force between molecules, the surface modifier is attached to the membrane surface, thereby forming a protective layer, improving the membrane surface potential, roughness or hydrophilicity.
在反渗透元件采用的螺旋卷式膜元件中,膜叶的数量、长度、宽度、原水及净水导流格网的厚度及几何结构等对膜的污染都有一定的影响,其中原水导流格网的不同设计对原水传质行为及压力损失等都有很大的影响,因而相应地对膜污染能力有很大的影响。In the spiral wound membrane element used in the reverse osmosis element, the number, length, width of the membrane leaves, the thickness and geometric structure of the raw water and the net water diversion grid have a certain influence on the fouling of the membrane, among which the raw water diversion The different designs of the grids have a great influence on the mass transfer behavior and pressure loss of the raw water, and thus have a great influence on the membrane fouling capacity accordingly.
然而,随着生活水平提高和人们对饮水质量的需求提高,目前水处理膜领域的卷式膜元件的耐污染性能仍然不能满足需求。However, with the improvement of living standards and the improvement of people's demand for drinking water quality, the pollution resistance performance of the current roll membrane elements in the field of water treatment membranes still cannot meet the demand.
发明内容SUMMARY OF THE INVENTION
发明目的:本发明的目的是提供一种卷式膜元件及原水导流网材料及结构,以提高膜元件抗阻垢性能,特别适合于高硬度废水环境的应用。Purpose of the invention: The purpose of the present invention is to provide a roll-type membrane element and the material and structure of the raw water guide net to improve the anti-scaling performance of the membrane element, which is especially suitable for the application of high-hardness wastewater environment.
技术方案:Technical solutions:
本发明提供的一种具有阻垢功能的卷式膜元件,包括产水中心管(1)以及缠绕在产水中心管上的至少一组净水膜片组;所述净水膜片组自内向外依次包括产水导流网(2)、第一分离膜片(3)、原水导流网(4)、第二分离膜片(5);所述原水导流网(4)包括金属薄膜片(6),以及设于金属薄膜片两表面的塑料粗纤维网或合金金属丝网(7);所述产水中心管(1)为中空,其一端开口,另 一端封闭,其管壁上设有一组通水孔(8),通水孔(8)与产水导流网(2)联通。The present invention provides a roll-type membrane element with a scale-inhibiting function, comprising a water-producing central pipe (1) and at least one group of water-purifying membrane sheets wound on the water-producing central pipe; The inside and outside sequentially include a produced water diversion net (2), a first separation membrane (3), a raw water diversion net (4), and a second separation membrane (5); the raw water diversion net (4) comprises metal The film sheet (6), and the plastic coarse fiber mesh or alloy wire mesh (7) arranged on both surfaces of the metal film sheet; the water production center pipe (1) is hollow, one end is open, the other end is closed, and the pipe A group of water passage holes (8) are arranged on the wall, and the water passage holes (8) are communicated with the produced water diversion net (2).
作为改进,所述原水导流网(4)的金属薄膜片(6)两面分布的塑料粗纤维网或合金金属丝网(7)与中心管呈20-160度角分布;所述塑料粗纤维网或合金金属丝网(7)之间间距0.2-5mm。As an improvement, the plastic coarse fiber mesh or alloy metal wire mesh (7) distributed on both sides of the metal film sheet (6) of the raw water guiding net (4) is distributed at an angle of 20-160 degrees with the central pipe; the plastic coarse fiber The spacing between the mesh or alloy wire mesh (7) is 0.2-5mm.
作为另一种改进,所述塑料粗纤维网或合金金属丝网(7)直径0.1-0.7mm,所述金属薄膜片(6)厚度为5-200微米。As another improvement, the diameter of the plastic coarse fiber mesh or alloy wire mesh (7) is 0.1-0.7 mm, and the thickness of the metal film sheet (6) is 5-200 microns.
作为另一种改进,所述金属薄膜片(6)由以下重量份制成:铜34-70份、锌2-30份,镍10-25份、锡2-5份、铁3-10份。As another improvement, the metal thin film sheet (6) is made of the following parts by weight: 34-70 parts of copper, 2-30 parts of zinc, 10-25 parts of nickel, 2-5 parts of tin, and 3-10 parts of iron .
作为另一种改进,所述第一分离膜片(3)和第二分离膜片(5)分别独立的为反渗透膜、纳滤膜或超滤膜。As another improvement, the first separation membrane (3) and the second separation membrane (5) are independently reverse osmosis membranes, nanofiltration membranes or ultrafiltration membranes.
作为另一种改进,所述通水孔(8)与产水导流网(2)接触处设有密封圈。As another improvement, a sealing ring is provided at the contact point between the water passage hole (8) and the produced water diversion net (2).
作为另一种改进,所述塑料粗纤维网为表面具有阻垢合金镀层的塑料粗纤维网,其镀层采用以下方法制得:将塑料粗纤维网用IPA溶液浸泡1小时后再用IPA反复漂洗三次,烘干;再用含4.0wt%重铬酸钾、3.0wt%硫酸的水溶液浸泡1小时,纯水漂洗三次;再浸润到含0.3wt%SnCl2及2.5wt%盐酸的水溶液中2min,取出后浸入到含0.1wt%PdCl2及1.0wt%盐酸的水溶液中10分钟,纯水漂洗三次,完成纤维网表面活化;将活化后的塑料粗纤维网浸入到化学镀溶液中5-10分钟,通过控制沉积时间,将约0.2-1微米的金属Cu被均匀镀到PP纤维网表面;其中,化学镀溶液组成为:0.7wt%CuSO4,2.5wt%的酒石酸钾钠,0.4wt%氢氧化钠及0.4wt%甲醛,余量为水。As another improvement, the plastic coarse fiber web is a plastic coarse fiber web with a scale-inhibiting alloy coating on the surface, and the coating is prepared by the following method: soak the plastic coarse fiber web with IPA solution for 1 hour and then rinse it repeatedly with IPA Three times, drying; then soaked in an aqueous solution containing 4.0wt% potassium dichromate and 3.0wt% sulfuric acid for 1 hour, rinsed three times with pure water; then soaked in an aqueous solution containing 0.3wt% SnCl2 and 2.5wt% hydrochloric acid for 2min, take out After immersion in an aqueous solution containing 0.1wt% PdCl2 and 1.0wt% hydrochloric acid for 10 minutes, rinsed with pure water three times to complete the surface activation of the fiber web; immerse the activated plastic coarse fiber web into the electroless plating solution for 5-10 minutes, pass Controlling the deposition time, metal Cu of about 0.2-1 micron is uniformly plated on the surface of the PP fiber web; wherein, the electroless plating solution is composed of: 0.7wt% CuSO4, 2.5wt% potassium sodium tartrate, 0.4wt% sodium hydroxide and 0.4wt% formaldehyde, the balance is water.
有益效果:本发明提供的卷式膜元件由一片阻垢合金金属薄膜片,及金属薄膜片两面的表面镀有阻垢合金的塑料粗纤维网或合金丝网组成,由于合金金属具有的阻垢和抑菌功能,使得膜元件在处理高硬度的原水时不易在膜表面结垢,提高了膜的使用寿命。Beneficial effect: The roll-type membrane element provided by the present invention is composed of a scale-inhibiting alloy metal film sheet, and a plastic coarse fiber mesh or alloy wire mesh coated with scale-inhibiting alloy on both surfaces of the metal film sheet. And the antibacterial function makes the membrane element not easy to scale on the membrane surface when processing raw water with high hardness, which improves the service life of the membrane.
图1为具有阻垢功能的卷式膜元件的结构示意图(部分展开);Figure 1 is a schematic structural diagram of a rolled membrane element with anti-scaling function (partially unfolded);
图2为原水导流网组合结构示意图;Figure 2 is a schematic diagram of the combined structure of the raw water diversion net;
实施例:Example:
具有阻垢功能的卷式膜元件,包括产水中心管(1)以及缠绕在产水中心管上的至少一组净水膜片组;所述净水膜片组自内向外依次包括产水导流网(2)、第一分离膜片(3)、原水导流网(4)、第二分离膜片(5);所述原水导流网(4)包括金属薄膜片(6),以及设于金属薄膜片两表面的塑料粗纤维网或合金金属丝网(7);所述产水中心管(1)为中空,其一端开口,另一端封闭,其管壁上设有一组通水孔(8),通水孔(8)与产水导流网(2)联通。所述通水孔(8)与产水导流网(2)接触处设有密封圈。A roll-type membrane element with a scale-inhibiting function, comprising a water-producing central pipe (1) and at least one group of water-purifying membrane sheets wound on the water-producing central pipe; A diversion net (2), a first separation membrane (3), a raw water diversion net (4), and a second separation membrane (5); the raw water diversion net (4) includes a metal film sheet (6), And the plastic thick fiber mesh or alloy metal wire mesh (7) arranged on both surfaces of the metal film sheet; the water production center pipe (1) is hollow, one end is open, the other end is closed, and a group of pipes are arranged on the pipe wall. The water hole (8) is communicated with the produced water diversion network (2). A sealing ring is provided at the contact between the water passage hole (8) and the produced water diversion net (2).
所述第一分离膜片(3)和第二分离膜片(5)均为反渗透膜。The first separation membrane (3) and the second separation membrane (5) are both reverse osmosis membranes.
所述塑料粗纤维网为表面具有阻垢合金镀层的塑料粗纤维网,其镀层采用以下方法制得:将塑料粗纤维网用IPA溶液浸泡1小时后再用IPA反复漂洗三次,烘干;再用含4.0wt%重铬酸钾、3.0wt%硫酸的水溶液浸泡1小时,纯水漂洗三次;再浸润到含0.3wt%SnCl2及2.5wt%盐酸的水溶液中2min,取出后浸入到含0.1wt%PdCl2及1.0wt%盐酸的水溶液中10分钟,纯水漂洗三次,完成纤维网表面活化;将活化后的塑料粗纤维网浸入到化学镀溶液中5-10分钟,通过控制沉积时间,将约0.2-1微米的金属Cu被均匀镀到PP纤维网表面;其中,化学镀溶液组成为:0.7wt%CuSO4,2.5wt%的酒石酸钾钠,0.4wt%氢氧化钠及0.4wt%甲醛,余量为水。The plastic thick fiber net is a plastic thick fiber net with a scale-inhibiting alloy coating on the surface, and the coating is prepared by the following method: soak the plastic thick fiber net with IPA solution for 1 hour, then rinse it with IPA repeatedly for three times, and dry it; Soak in an aqueous solution containing 4.0wt% potassium dichromate and 3.0wt% sulfuric acid for 1 hour, rinse with pure water for three times; then infiltrate into an aqueous solution containing 0.3wt% SnCl2 and 2.5wt% hydrochloric acid for 2min, take it out and immerse it in 0.1wt% hydrochloric acid %PdCl2 and 1.0wt% hydrochloric acid solution for 10 minutes, rinsed with pure water three times to complete the surface activation of the fiber web; immerse the activated plastic coarse fiber web into the electroless plating solution for 5-10 minutes, and by controlling the deposition time, about 0.2-1 micron metal Cu is uniformly plated on the surface of the PP fiber mesh; wherein, the electroless plating solution is composed of: 0.7wt% CuSO4, 2.5wt% potassium sodium tartrate, 0.4wt% sodium hydroxide and 0.4wt% formaldehyde, the rest The amount is water.
以下参数均可以实现本发明的目的:The following parameters can all realize the purpose of the present invention:
所述原水导流网(4)的金属薄膜片(6)两面分布的塑料粗纤维网或合金金属丝网(7)与中心管呈20-160度角分布;所述塑料粗纤维网或合金金属丝网(7)之间间距0.2-5mm。The plastic coarse fiber mesh or alloy metal wire mesh (7) distributed on both sides of the metal film sheet (6) of the raw water guiding net (4) is distributed at an angle of 20-160 degrees with the central pipe; the plastic coarse fiber mesh or alloy The spacing between the wire meshes (7) is 0.2-5mm.
所述塑料粗纤维网或合金金属丝网(7)直径0.1-0.7mm,所述金属薄膜片(6)厚度为5-200微米。The diameter of the plastic coarse fiber mesh or alloy metal wire mesh (7) is 0.1-0.7 mm, and the thickness of the metal film sheet (6) is 5-200 microns.
所述金属薄膜片(6)由以下重量份制成:铜34-70份、锌2-30份,镍10-25份、锡2-5份、铁3-10份。The metal thin film sheet (6) is made of the following parts by weight: 34-70 parts of copper, 2-30 parts of zinc, 10-25 parts of nickel, 2-5 parts of tin, and 3-10 parts of iron.
所述第一分离膜片(3)和第二分离膜片(5)分别独立的为反渗透膜、纳滤膜或超滤膜。The first separation membrane (3) and the second separation membrane (5) are independently reverse osmosis membranes, nanofiltration membranes or ultrafiltration membranes.
制得一批具有阻垢功能的卷式膜元件,并测试其性能,具有阻垢功能的卷式膜元件参数见表1:A batch of rolled membrane elements with anti-scaling function were prepared and their performance was tested. The parameters of rolled membrane elements with anti-scaling function are shown in Table 1:
试验条件:Test conditions:
取膜面积32cmx106cm反渗透膜片6片,卷制成标准3013膜元件。测试压力:0.8Mpa;回收率:90%;测试温度:25C。测试所用原水溶液各组分浓度如下:2000ppm CaCl2、2000ppm NaHCO3、10ppm奶粉、1000ppm NaCl的水溶液。每1小时搜集一次水通量和原水及净水TDS值,计算脱盐率及水通量的衰减百分比以表征膜元件的阻垢能力,水通量衰减百分比越小,阻垢能力越强。Take 6 reverse osmosis membranes with a membrane area of 32cmx106cm and roll them into standard 3013 membrane elements. Test pressure: 0.8Mpa; recovery rate: 90%; test temperature: 25C. The concentration of each component of the original aqueous solution used in the test is as follows: 2000ppm CaCl2, 2000ppm NaHCO3, 10ppm milk powder, 1000ppm NaCl aqueous solution. Collect water flux and TDS values of raw water and purified water every 1 hour, and calculate the desalination rate and the attenuation percentage of water flux to characterize the scale inhibition ability of membrane elements. The smaller the water flux attenuation percentage, the stronger the scale inhibition ability.
对比例:原水网选六片通用PP网32X55cm,直径0.5mm,间距0.3mm。六片32cmx106cm反渗透膜片对折,将六片原水网插入对折的膜片之间,制成卷式膜元件。用上述条件测试水通量及脱盐率。Comparative example: six pieces of general-purpose PP mesh 32X55cm, diameter 0.5mm, and spacing 0.3mm were selected for the raw water mesh. Six 32cmx106cm reverse osmosis membranes are folded in half, and the six raw water nets are inserted between the folded membranes to make a rolled membrane element. The water flux and desalination rate were tested using the above conditions.
测试例1:原水网组包括一张厚度约为50微米合金薄膜片和两面各一张厚度0.25mmPP原水网。同样选6组相同面积的原水网组及反渗透膜片,其它与对比例相同。测试条件与对比例相同。Test Example 1: The raw water mesh group includes an alloy film sheet with a thickness of about 50 microns and a raw water mesh with a thickness of 0.25 mm on both sides. Similarly, 6 groups of raw water network groups and reverse osmosis membranes of the same area were selected, and the others were the same as those in the comparative example. The test conditions were the same as in the comparative example.
实施例2-12:选用不同的原水网组,具体原水网组构成及测试结果见表1。Embodiment 2-12: select different raw water net groups for use, and concrete raw water net group constitutions and test results are shown in Table 1.
由实施例及对比例结果可看出,本发明的原水网组均不同程度地提高了膜的耐阻垢性能。适当比例的合金金属片在原水网组中起到比合金丝网本身更大的作用。It can be seen from the results of the examples and comparative examples that the raw water reticulation group of the present invention improves the anti-scaling performance of the membrane to varying degrees. A proper proportion of alloy metal sheets plays a greater role in the raw water mesh group than the alloy wire mesh itself.
表1对比例与实施例列表Table 1 list of comparative examples and examples
以上的具体实施例,对本发明的目的、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上仅为本发明的具体实施例而已,并不用于限制本发明,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above specific embodiments further describe the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above are only specific embodiments of the present invention, and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
Claims (7)
- 一种具有阻垢功能的卷式膜元件,其特征在于:包括产水中心管(1)以及缠绕在产水中心管上的至少一组净水膜片组;所述净水膜片组自内向外依次包括产水导流网(2)、第一分离膜片(3)、原水导流网(4)、第二分离膜片(5);所述原水导流网(4)包括金属薄膜片(6),以及设于金属薄膜片两表面的塑料粗纤维网或合金金属丝网(7);所述产水中心管(1)为中空,其一端开口,另一端封闭,其管壁上设有一组通水孔(8),通水孔(8)与产水导流网(2)联通。A roll-type membrane element with scale-inhibiting function, characterized in that it comprises a water-producing central pipe (1) and at least one group of water-purifying membrane sheets wound on the water-producing central pipe; The inside and outside sequentially include a produced water diversion net (2), a first separation membrane (3), a raw water diversion net (4), and a second separation membrane (5); the raw water diversion net (4) comprises metal The film sheet (6), and the plastic coarse fiber mesh or alloy wire mesh (7) arranged on both surfaces of the metal film sheet; the water production center pipe (1) is hollow, one end is open, the other end is closed, and the pipe A group of water passage holes (8) are arranged on the wall, and the water passage holes (8) are communicated with the produced water diversion net (2).
- 根据权利要求1所述的一种具有阻垢功能的卷式膜元件,其特征在于:所述原水导流网(4)的金属薄膜片(6)两面分布的塑料粗纤维网或合金金属丝网(7)与中心管呈20-160度角分布;所述塑料粗纤维网或合金金属丝网(7)之间间距0.2-5mm。A roll-type membrane element with anti-scaling function according to claim 1, characterized in that: plastic coarse fiber nets or alloy metal wires distributed on both sides of the metal film sheet (6) of the raw water guiding net (4) The net (7) and the central tube are distributed at an angle of 20-160 degrees; the distance between the plastic coarse fiber nets or alloy metal wire nets (7) is 0.2-5mm.
- 根据权利要求1所述的一种具有阻垢功能的卷式膜元件,其特征在于:所述塑料粗纤维网或合金金属丝网(7)直径0.1-0.7mm,所述金属薄膜片(6)厚度为5-200微米。A roll-type membrane element with scale-inhibiting function according to claim 1, characterized in that: the diameter of the plastic coarse fiber mesh or alloy metal wire mesh (7) is 0.1-0.7 mm, and the metal film sheet (6) is 0.1-0.7 mm in diameter. ) thickness is 5-200 microns.
- 根据权利要求1所述的一种具有阻垢功能的卷式膜元件,其特征在于:所述金属薄膜片(6)由以下重量份制成:铜34-70份、锌2-30份,镍10-25份、锡2-5份、铁3-10份。A roll-type membrane element with scale inhibition function according to claim 1, characterized in that: the metal thin film sheet (6) is made of the following parts by weight: 34-70 parts of copper, 2-30 parts of zinc, 10-25 parts of nickel, 2-5 parts of tin, 3-10 parts of iron.
- 根据权利要求1所述的一种具有阻垢功能的卷式膜元件,其特征在于:所述第一分离膜片(3)和第二分离膜片(5)分别独立的为反渗透膜、纳滤膜或超滤膜。A roll-type membrane element with scale inhibition function according to claim 1, characterized in that: the first separation membrane (3) and the second separation membrane (5) are independently reverse osmosis membranes, Nanofiltration or ultrafiltration membranes.
- 根据权利要求1所述的一种具有阻垢功能的卷式膜元件,其特征在于:所述通水孔(8)与产水导流网(2)接触处设有密封圈。A roll-type membrane element with a scale-inhibiting function according to claim 1, characterized in that a sealing ring is provided at the contact point between the water passage hole (8) and the produced water diversion net (2).
- 根据权利要求1所述的一种具有阻垢功能的卷式膜元件,其特征在于:所述塑料粗纤维网为表面具有阻垢合金镀层的塑料粗纤维网,其镀层采用以下方法制得:将塑料粗纤维网用IPA溶液浸泡1小时后再用IPA反复漂洗三次,烘干;再用含4.0wt%重铬酸钾、3.0wt%硫酸的水溶液浸泡1小时,纯水漂洗三次;再浸润到含0.3wt%SnCl2及2.5wt%盐酸的水溶液中2min,取出后浸入到含0.1wt%PdCl2及1.0wt%盐酸的水溶液中10分钟,纯水漂洗三次,完成纤维网表面活化;将活化后的塑料粗纤维网浸入到化学镀溶液中5-10分钟,通过控制沉积时间,将约0.2-1微米的金属Cu被均匀镀到PP纤维网表面;其中,化学镀溶 液组成为:0.7wt%CuSO4,2.5wt%的酒石酸钾钠,0.4wt%氢氧化钠及0.4wt%甲醛,余量为水。A roll-type membrane element with scale-inhibiting function according to claim 1, characterized in that: the plastic coarse fiber net is a plastic coarse fiber net with a scale-inhibiting alloy coating on the surface, and the coating is obtained by the following method: The plastic crude fiber web was soaked in IPA solution for 1 hour, then rinsed three times with IPA, and dried; then soaked in an aqueous solution containing 4.0 wt % potassium dichromate and 3.0 wt % sulfuric acid for 1 hour, and rinsed with pure water three times; Put it into an aqueous solution containing 0.3wt% SnCl2 and 2.5wt% hydrochloric acid for 2 minutes, take it out and immerse it in an aqueous solution containing 0.1wt% PdCl2 and 1.0wt% hydrochloric acid for 10 minutes, rinse with pure water three times to complete the surface activation of the fiber web; The plastic coarse fiber web is immersed in the electroless plating solution for 5-10 minutes, and by controlling the deposition time, metal Cu of about 0.2-1 micron is uniformly plated on the surface of the PP fiber web; wherein, the composition of the electroless plating solution is: 0.7wt% CuSO4, 2.5wt% potassium sodium tartrate, 0.4wt% sodium hydroxide and 0.4wt% formaldehyde, and the balance is water.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114950141A (en) * | 2022-06-08 | 2022-08-30 | 林金龙 | Conductive separation membrane bag and application thereof |
CN115253692A (en) * | 2022-06-22 | 2022-11-01 | 沃顿科技股份有限公司 | Membrane element, production method of membrane element and roll-type membrane module |
WO2023174203A1 (en) * | 2022-03-15 | 2023-09-21 | 佛山市顺德区阿波罗环保器材有限公司 | Reverse osmosis filter element capable of prolonging service life, preparation method therefor and use thereof |
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Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030211791A1 (en) * | 2002-05-08 | 2003-11-13 | Memsfuel International Corporation | Flow guiding structure |
CN202398295U (en) * | 2012-01-11 | 2012-08-29 | 天津大学 | Spiral wound membrane element with electrolytic oxidation |
CN105381719A (en) * | 2014-09-09 | 2016-03-09 | 贵阳时代沃顿科技有限公司 | Spiral-wound membrane element and rolling method thereof |
CN108176235A (en) * | 2018-01-19 | 2018-06-19 | 南京工业大学 | A kind of new configuration filter |
CN108654390A (en) * | 2018-05-16 | 2018-10-16 | 南京帝膜净水材料开发有限公司 | A kind of wound membrane element |
CN208660832U (en) * | 2018-07-27 | 2019-03-29 | 上海凯矜新材料科技有限公司 | A kind of coiled reverse osmosis membrane element |
CN209093129U (en) * | 2018-08-14 | 2019-07-12 | 三达膜科技(厦门)有限公司 | Pollution-resistant rolled film water conservancy diversion filter |
CN211069667U (en) * | 2019-08-02 | 2020-07-24 | 江苏久吾高科技股份有限公司 | Roll type membrane element |
CN212504241U (en) * | 2020-08-12 | 2021-02-09 | 南京水联天下海水淡化技术研究院有限公司 | Roll type membrane element with scale inhibition function |
-
2020
- 2020-08-12 CN CN202010806728.9A patent/CN111825224A/en active Pending
- 2020-08-27 WO PCT/CN2020/111594 patent/WO2022032731A1/en active Application Filing
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030211791A1 (en) * | 2002-05-08 | 2003-11-13 | Memsfuel International Corporation | Flow guiding structure |
CN202398295U (en) * | 2012-01-11 | 2012-08-29 | 天津大学 | Spiral wound membrane element with electrolytic oxidation |
CN105381719A (en) * | 2014-09-09 | 2016-03-09 | 贵阳时代沃顿科技有限公司 | Spiral-wound membrane element and rolling method thereof |
CN108176235A (en) * | 2018-01-19 | 2018-06-19 | 南京工业大学 | A kind of new configuration filter |
CN108654390A (en) * | 2018-05-16 | 2018-10-16 | 南京帝膜净水材料开发有限公司 | A kind of wound membrane element |
CN208660832U (en) * | 2018-07-27 | 2019-03-29 | 上海凯矜新材料科技有限公司 | A kind of coiled reverse osmosis membrane element |
CN209093129U (en) * | 2018-08-14 | 2019-07-12 | 三达膜科技(厦门)有限公司 | Pollution-resistant rolled film water conservancy diversion filter |
CN211069667U (en) * | 2019-08-02 | 2020-07-24 | 江苏久吾高科技股份有限公司 | Roll type membrane element |
CN212504241U (en) * | 2020-08-12 | 2021-02-09 | 南京水联天下海水淡化技术研究院有限公司 | Roll type membrane element with scale inhibition function |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2023174203A1 (en) * | 2022-03-15 | 2023-09-21 | 佛山市顺德区阿波罗环保器材有限公司 | Reverse osmosis filter element capable of prolonging service life, preparation method therefor and use thereof |
CN116789224A (en) * | 2022-03-15 | 2023-09-22 | 佛山市顺德区阿波罗环保器材有限公司 | Reverse osmosis filter element with prolonged service life and preparation method and application thereof |
CN114950141A (en) * | 2022-06-08 | 2022-08-30 | 林金龙 | Conductive separation membrane bag and application thereof |
CN114950141B (en) * | 2022-06-08 | 2024-01-26 | 林金龙 | Conductive separation film bag and application thereof |
CN115253692A (en) * | 2022-06-22 | 2022-11-01 | 沃顿科技股份有限公司 | Membrane element, production method of membrane element and roll-type membrane module |
CN115253692B (en) * | 2022-06-22 | 2023-12-01 | 沃顿科技股份有限公司 | Membrane element, production method of membrane element and rolled membrane assembly |
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