34 results about "Spiral membrane" patented technology

Provided is a method for dehydrating a spiral membrane element, which can effectively remove moisture contained in a used spiral membrane element by a simple method. The method for dehydrating a spiral membrane element according to the present invention is a method for dehydrating a spiral membrane element E that contains moisture, the spiral membrane element E having a winding body and a perforated center tube, the winding body including a plurality of membrane sheets wound on the center tube and having a permeation-side flow path inside. Furthermore, the method for dehydrating a spiral membrane element according to the present invention includes a step of forming an opening (for example, an end face opening formed by a cut surface 16) that communicates the permeation-side flow path with the outside on the plurality of membrane sheets, and a step of applying a centrifugal force to the spiral membrane element on which the opening is formed.

The application discloses a seawater desalination roll type membrane device based on a biomimetic flow guide net. Multilayer hollow cylindrical reverse osmosis membranes are coaxially arranged in the inside of a reverse osmosis membrane assembly, an annular cavity is formed between every two adjacent reverse osmosis membranes, a hollow cylindrical biomimetic flow guide net is arranged in each annular cavity, the biomimetic flow guide net is coaxially arranged with the reverse osmosis membrane and is located on the central ring line of the annular cavity; liquid to be desalinated is flowed into the reverse osmosis membrane assembly from an inlet, is desalinated by the reverse osmosis membrane and the biomimetic flow guide net, and is finally flowed out of the reverse osmosis membrane assembly from an outlet; a plurality of biomimetic flow guide units of the biomimetic flow guide net are arranged in a longitudinal and transverse staggered mode, and each biomimetic flow guide unit is mainly composed of a plurality of flow guide columns in an elliptical cylindrical structure and is sequentially connected. The application has the advantages of simple structure, high reliability, easy manufacturing and good popularization value, and the structure can further improve the water production efficiency of the roll type membrane assembly and reduce the production cost of a water treatment plant.

The invention relates to the technical field of aromatic hydrocarbon separation and purification, in particular to a system and process flow for removing C8 non-aromatic hydrocarbon in xylene through membrane separation, and the system comprises a membrane separation unit, a feeding unit, a permeation side system, an interception side system, an adsorption tower feeding buffer tank outlet line and a crossover line; the membrane separation unit is provided with a membrane feeding pipeline, one end of the membrane separation unit is connected to an outlet of the membrane separation feeding buffer tank, and the other end of the membrane separation unit is connected to an inlet side pipe orifice of the separation pipeline; a membrane feeding booster pump is arranged on the membrane feeding pipeline; a spiral-wound membrane assembly is arranged in the separation pipeline; the feeding unit is provided with a xylene redistillation tower top outlet line which is connected to an inlet of the membrane separation feeding buffer tank from the xylene redistillation tower top. According to the membrane separation process adopted by the method, the non-aromatic hydrocarbon removal rate can be more than 98% under the operation conditions that the feeding pressure is 1.68 MPa, the permeation side is 20 kPa and the interception side is 1.6 MPa, and the method has definite industrial feasibility and technical advantages.

The present invention provides a new spiral membrane element suitable for recovering a permeated fluid efficiently. A spiral membrane element of the present invention includes: a central tube; a separation membrane that is wound around the central tube and separates a feed fluid into a permeated fluid and a non-permeated fluid; and a feed space and a permeation space separated from each other by the separation membrane. The permeation space communicates with an outer space of the spiral membrane element via an outer circumferential surface of the spiral membrane element.

The utility model discloses a water treatment spiral-wound membrane module with self-scale inhibition capability. The water treatment spiral-wound membrane module comprises a spiral-wound membrane unit, an outer protective shell made of a conductive material or a strong magnetic material, an end cover and a central pipe, end covers are mounted at two ends of the outer protective shell; a plurality of radial through holes are uniformly distributed on the circumference of the central tube; the central tube is coaxially positioned in the inner cavity of the outer protective shell; two ends of the central tube are fixedly connected with end covers; two ends of the spiral-wound membrane unit directly face second through holes of the end covers, the outer wall is attached to the outer protective shell, and the inner wall covers the outer wall of the central pipe; when the end cover is made of a conductive material, a plurality of electric contacts are symmetrically mounted on two sides of the end cover, the electric contacts on two sides are electrically connected with an alternating current power supply or a direct current power supply, raw water is continuously concentrated along the radial direction of the spiral-wound membrane unit, and a strong electromagnetic field can activate water molecules and prevent ions from forming crystals, so that scales cannot be attached to the spiral-wound membrane unit. The utility model has the effects of no scaling for a long time, high energy consumption, high operation efficiency and long service life.

The present invention provides a spiral membrane element suitable for suppressing a decrease in a permeation rate (or a permeation flux) of a permeated fluid from a separation membrane. A spiral membrane element of the present invention includes: a central tube; a membrane leaf that has a separation membrane and a permeation spacer and is wound around the central tube; and a flow passage spacer that is connected to the permeation spacer and is wound around the central tube on a side closer to the central tube than the membrane leaf is. A pressure loss of the flow passage spacer measured by a predetermined test is smaller than a pressure loss of the permeation spacer.

A spiral membrane element includes: a plurality of membrane leaves each having a permeation-side spacer interposed between separation membranes facing each other and having both-side sealing parts and a peripheral-side sealing part that seal both-side ends and a peripheral-side end in an axial direction; a supply-side spacer interposed between the membrane leaves; and a perforated central pipe around which the membrane leaves and the supply-side spacers are wound. The permeation-side spacer in the membrane leaves has a tear processing part over the entire width on a peripheral side from the center.

A spiral membrane element includes: a plurality of membrane leaves each having a permeation-side spacer interposed between separation membranes facing each other and having both-side sealing parts and a peripheral-side end that seal both-side ends in an axial direction; a supply-side spacer interposed between the membrane leaves; and a perforated central pipe around which the membrane leaves and the supply-side spacers are wound, wherein a folded part of an inner surface of each of the membrane leaves and a peripheral-side tip of the permeation-side spacer are not fixed to each other in at least one the peripheral-side end.

According to the present invention, a spiral membrane element in which the durability of a bonding part between a membrane leaf and a central pipe is improved, and the central pipe is more easily separated and collected at the time of recycling. The spiral membrane element includes: a plurality of membrane leaves each having a permeation-side flow-channel between separation membranes facing each other; and a perforated central pipe around which the membrane leaves are wound with a supply-side flow-channel interposed between the membrane leaves. The spiral membrane element includes a bonding part in which each of both-side ends in an axial direction among inner peripheral-side ends of the membrane leaves is bonded to the central pipe, and the central pipe includes a tapered part having a peripheral surface whose diameter expands toward a center side in the axial direction in at least a partial area of the bonding part.

A kind of equalizing air intake spiral membrane module box, including air intake pressure structure, channel structure and box structure;The air intake pressure structure includes first shell, with first port and second port;The first port is equipped with first sealing baffle, the top of the first sealing baffle is equipped with rectangular air inlet;The channel structure includes second shell, with third port and fourth port;The third port is equipped with second sealing baffle, the fourth port is equipped with air equalizing block between the second port;Several evenly distributed transverse air passages are arranged in the air equalizing block;Rectangular adjusting plate is arranged in the second shell, the height of the adjusting plate gradually increases from the fourth port to the third port;The top plate of the second shell is equipped with several through holes, the top of each through hole is fixedly provided with spiral membrane module, and each through hole is connected with the air inlet end of corresponding spiral membrane module;The box structure includes third shell opening downward, is fixed to the top of the second shell, and covers each spiral membrane module.

The utility model discloses a spiral membrane vacuum tower of high -efficient removal lubricating oil gas relates to lubricating oil processing technical field, the utility model discloses a base, the top outer wall fixedly connected with support plate of base, the utility model discloses a turbine agitator and spiral flow guide groove are set up, and the contact area of liquid and the inside of flow -through pipe is increased through spiral flow guide groove in the flow -through pipe, and because the turning of turbine agitator and spiral flow guide groove is opposite, the shear force produced when the rotation of two can tear liquid into small pieces, thereby extruding the tiny bubble in liquid, reach the shear force produced when turbine agitator and spiral flow guide groove rotate in the jar extrude the tiny bubble in liquid, prevent the emergence because traditional degassing jar relies on the rotation of stirring part and increase its contact area with liquid, thereby extruding gas, but the extrusion area of stirring part and liquid is limited, lead to the oil gas efficiency of device to liquid is not good, and the problem such as not thorough degassing.

The application discloses a kind of spiral membrane element and its preparation method, the spiral membrane element includes spiral layer structure and water collection center pipe, the spiral layer structure includes water production flow channel cloth, first membrane, concentrated water flow channel cloth and second membrane, the water collection center pipe is placed between the water production flow channel cloth and the first or second membrane, the water collection center pipe is directly contacted with the first or second membrane and is fused;The water production flow channel cloth is placed between the first membrane and the second membrane, the upper and lower surfaces of the water production flow channel cloth respectively include first edge, second edge and third edge not provided with water collection center pipe, the first edge, second edge and third edge of the upper and lower surfaces of the water production flow channel cloth are directly contacted with the first membrane and the second membrane and are fused to form water production membrane bag.The spiral membrane element of the application has narrower connection area than traditional membrane element, and can obtain larger effective membrane use area under fixed shape.

This invention discloses an overflow-proof microbial wastewater treatment tank, comprising a tank body, a corridor, an exhaust mechanism, and a double-layer folded membrane mechanism. The double-layer folded membrane mechanism includes an upper plate and a lower plate, both inclined. The lower plate rotates circumferentially around the center of the tank body, pulling the double-layer folded membrane mechanism to unfold and form an inverted conical spiral membrane that seals the upper part of the tank body. The exhaust mechanism uses wind and water flow to discharge waste gas from the lower part of the double-layer folded membrane mechanism. This invention effectively prevents tank water overflow and reduced microbial activity caused by heavy rain, maintaining continuous wastewater treatment and reducing subsequent treatment and production cost losses due to heavy rain.

By adjusting the amount of residual functional groups on the front and back surfaces of the separation functional layer, we provide a composite semipermeable membrane with further improved alkali resistance, and a spiral-type membrane element using the same. [Solution] A composite semipermeable membrane comprising a separation functional layer, wherein the separation functional layer contains a polyamide resin, the surface functional group ratio A and the back surface functional group ratio B satisfy the relationship A / B ≤ 3.0, and the carboxyl group concentration x and the amino group concentration y satisfy the relationship x + y ≤ 0.015. The surface functional group ratio A is a value calculated as A = x / y, where x is the carboxyl group concentration relative to the total carbon amount and y is the amino group concentration relative to the total carbon amount when the surface of the separation functional layer is measured by the ESCA gas phase modification method, and the back surface functional group ratio B is a value calculated as B = X / Y when the back surface of the separation functional layer is measured in the same manner.

Provided is a novel separation membrane suitable for a membrane separation device (particularly a spiral membrane element). This separation membrane (10) is provided with a separation functional layer (1), a porous support (3) that supports the separation functional layer (1), and an intermediate layer (2) that is arranged between the separation functional layer (1) and the porous support (3). The porous support (3) has a surface (S1) facing the intermediate layer (2). The load area ratio Smr (c1) of the surface S1 as determined by the following test is less than 80%. And a test: performing three-dimensional analysis on the surface S1 of the porous support body 3 to obtain a load curve specified in JIS B0681-2: 2018. In the load curve, a height (c1) at which the difference from the height (c0) when the load area ratio is 0% coincides with the thickness of the intermediate layer (2) is determined. A load area ratio corresponding to the height c1 is read and determined as a load area ratio Smr (c1).

The utility model discloses an end cover for fixing a spiral-wound membrane element. The end cover comprises an inner ring structure and an outer ring structure, wherein the inner ring structure and the outer ring structure are arranged layer by layer from inside to outside and share a circle; the inner ring structure and the outer ring structure are connected through the middle oval ring body and the multiple special-shaped connecting rib plates, one end of each special-shaped connecting rib plate is connected with the inner ring structure, and the other end of each special-shaped connecting rib plate is connected with the intersection point of the middle oval ring body. The end cover structure for fixing the spiral-wound membrane element is optimized, and the elliptical ring body and the special-shaped connecting rib plates are arranged between the inner ring structure and the outer ring structure, so that on one hand, the end cover rib plates are more uniformly distributed on the whole end surface, the stress of the membrane is more uniform, and the risk of deformation of the membrane is reduced; the overall rib plate layout is approximately triangular, so that the overall structure of the end cover is more stable, and the risk of deformation of the end cover is reduced.

The present invention provides: a composite semipermeable membrane with which desired blocking performance is achieved and in which both contamination resistance and high water permeability are exhibited; and a spiral-type membrane element in which the composite semipermeable membrane is used. The present invention is a composite semipermeable membrane comprising a porous support, a separation function layer formed of a polyamide-based resin on the porous support, and a coating layer that covers the separation function layer and contains a cationic polymer, the composite semipermeable membrane being characterized in that: the polyamide-based resin contains a constituent component derived from m-phenylenediamine (MPD) and trimesic acid chloride (TMC), the molar ratio (TMC / MPD) of the TMC to the MPD being within the range of 0.65-1.00; and the separation function layer in a state of being covered by the coating layer has a surface roughness Ra1 of 85-150 nm as measured in a region measuring 5 μm × 5 μm using an atomic force microscope (AFM) in water.

This invention provides a spiral-type membrane element that improves the durability of the bonding joint between the membrane leaf and the central tube, while also facilitating the separation and recovery of the central tube during recycling. [Solution] A spiral membrane element E comprising a plurality of membrane leaves L having permeable channels between opposing separation membranes, and a perforated central tube 5 around which the membrane leaves L are wound with supply channels interposed between the membrane leaves L, wherein both ends of the inner circumference side of the membrane leaves L in the axial direction A1 are bonded to the central tube 5, and in at least a portion of the area of ​​the bonded channel 13, the outer circumference surface of the central tube 5 has a tapered portion 5b that widens toward the center in the axial direction A1.

The present invention provides a membrane separation device suitable for suppressing deterioration of hygienic conditions inside a membrane separation device. The membrane separation device includes a spiral membrane element. The membrane element includes: a central tube having a through hole; and a membrane leaf wound around the central tube and having a pervaporation membrane that separates a fermented liquid containing a volatile organic compound into a permeated fluid and a non-permeated fluid. A flow of the non-permeated fluid into a space adjacent to an outer circumferential surface of the membrane element is blocked during operation of the membrane separation device.

The application provides a water inlet screen for a spiral membrane element and the spiral membrane element, which comprises a plurality of transverse wires (1), a plurality of longitudinal wires (2) and a support part (3), the transverse wires (1) and the longitudinal wires (2) are staggered to form cells, the water inlet screen comprises a plurality of matrix-arranged cells, the support part (3) is arranged at the intersection of the transverse wires (1) and the longitudinal wires (2), the transverse wires (1) and the longitudinal wires (2) are connected to the support part (3), the height of the support part (3) is greater than the thickness of the transverse wires (1) and the longitudinal wires (2) of the cell, the support part (3) is used for contacting a membrane sheet of the spiral membrane element, and the transverse wires (1) and the longitudinal wires (2) are in different planes in the thickness direction of the water inlet screen.

A spiral membrane element includes an element body, an end member, and an exterior material. The end member includes a body portion having a first protrusion, and a skirt portion located between the element body and the exterior material, and satisfies at least one selected from the group consisting of the following requirements (1) to (3): (1) the first protrusion has a cut-in portion and a part of the exterior material is placed into at least a part of the cut-in portion; (2) the skirt portion has at least one of a hole and a through hole, and a part of the exterior material is placed into at least a part of at least one of a hole and a through hole; and (3) the first protrusion has a recess, and a part of the exterior material is placed into at least a part of the recess.

This invention relates to a spiral membrane element and a method for manufacturing the same, providing a spiral membrane element that reduces waste and saves resources by modifying the outer peripheral end of the membrane leaf to an easily disintegratable structure, and allows for easy recycling of the permeate-side spacer. The spiral membrane element comprises: a plurality of membrane leaves; a permeate-side spacer disposed between opposing separation membranes, having two side sealing portions and an outer peripheral end, the two side sealing portions sealing the two axial ends; a supply-side spacer disposed between the membrane leaves; and a perforated central tube wound with the membrane leaves and the supply-side spacer, wherein at at least one of the outer peripheral ends, a folded portion on the inner surface of the membrane leaf is not fixed to the outer peripheral front end of the permeate-side spacer.

This invention relates to the field of filtration device technology, and particularly to a sleeve-type central tube and a composite spiral membrane structure, wherein the sleeve-type central tube consists of a sleeve and end caps. Compared with the prior art, the sleeve-type central tube provided by this invention connects and fixes the end caps and the sleeve through connecting posts on the sleeve, creating a certain gap between the sleeve and the end caps. The first cap wall of the end cap and the tube wall of the sleeve can be sealed to both ends of the RO spiral membrane. After water is filtered by the RO spiral membrane, it enters the sleeve through the gap between the sleeve and the end caps. The space between the sleeve and the end caps can be used to accommodate integrated internal filter media to form a multifunctional filter cartridge. The combination of the sleeve and the end caps facilitates the integration with the outer RO spiral membrane without affecting the internal filter media. It has a relatively stable structure during production, which is beneficial for improving yield and reducing production costs.

The objective is to provide a spiral-type membrane element and a machine suitable for its recovery operation, which does not require altering the basic structure of the spiral-type membrane element to be recycled, reduces waste generated by used membrane elements and saves introduced resources, and allows for easy recovery of the permeable side spacer and central tube. [Solution] The spiral membrane element comprises a plurality of membrane leaves having a permeation-side spacer interposed between opposing separation membranes, with both axial ends and the outer peripheral end sealed, a supply-side spacer interposed between the membrane leaves, and a perforated central tube around which the membrane leaves and the supply-side spacer are wound. The permeation-side spacer within the membrane leaf has a tear-processed portion along its entire width, on the outer peripheral side from the center.

It is an object of the present invention to provide a composite semipermeable membrane capable of improving both rejection performance against organic compounds and a water permeability by controlling the microscopic surface area of a separation functional layer with an index different from the conventional one, and a spiral membrane element using the same. A composite semipermeable membrane 1 of the present invention includes a porous support 1b and a separation functional layer 1a formed of a polyamide-based resin on the porous support 1b, wherein the separation functional layer 1a has a surface roughness Ra1 of 90 to 150 nm when an area of 5 µm × 5 µm is measured in water by an atomic force microscope (AFM).

The objective is to provide a spiral membrane element that reduces waste generated by used spiral membrane elements and saves introduced resources by changing the outer peripheral end of the membrane leaf to a structure that makes it easy to dismantle, while also allowing for easy recovery of the permeation-side spacer. [Solution] The spiral membrane element comprises a plurality of membrane leaves having a permeable side spacer interposed between opposing separation membranes, a double sealing portion that seals both axial ends and an outer peripheral end, a supply side spacer interposed between the membrane leaves, and a perforated central tube around which the membrane leaves and the supply side spacer are wound, wherein at least one of the outer peripheral ends is not fixed to the folded portion on the inner surface of the separation membrane leaf and the outer peripheral tip of the permeable side spacer.

The present invention provides a spiral membrane element that is suited to suppressing reductions in the permeation speed (or the permeation flux) of a permeated fluid from a separation membrane. This spiral membrane element 10 comprises a center tube 21, a membrane leaf 11 that has a separation membrane 12 and a permeation spacer 14 and is wound around the center tube 21, and a channel spacer 15 that is connected to the permeation spacer 14 and is wound around the center tube 21 closer to the center tube 21 side than the membrane leaf 11. The pressure loss P1 of the channel spacer 15 as measured by means of a prescribed test is lower than the pressure loss P2 of the permeation spacer 14.

The present invention provides: a composite semipermeable membrane that makes it possible to obtain desired rejection performance and that achieves both antifouling properties and high water-permeability; and a spiral membrane element using the same. The present invention provides a composite semipermeable membrane comprising a porous support, a separation functional layer that is formed of a polyamide-based resin on the porous support, and a coating layer that coats the separation functional layer and that contains a hydrophilic polymer, said composite semipermeable membrane characterized in that: the polyamide-based resin contains constituent components derived from m-phenylenediamine (MPD) and trimesic acid chloride (TMC); the molar ratio (TMC / MPD) of TMC to MPD is within the range of 0.65-1.00; and the separation functional layer, when in the state of being coated with the coating layer, has a surface roughness Ra1 of not less than 60 nm when a region of 5 μm × 5 μm is measured with an atomic force microscope (AFM) in water, and has a surface zeta potential of not less than -20 mV at a pH of 7.

The present invention provides a spiral membrane element that improves the durability of the bonding portion between the membrane leaf and the central tube and makes the separation and recovery of the central tube easier during recirculation. The spiral membrane element (E) of the present invention comprises: a plurality of membrane leaves (L) having a permeate-side flow path between opposing separation membranes; and a perforated central tube (5) having the membrane leaves (L) wound around it while the supply-side flow path is provided between the membrane leaves (L), wherein the spiral membrane element (E) has a bonding portion (13) formed by bonding the two ends of the inner peripheral side end of the membrane leaves (L) in the axial direction (A1) to the central tube (5), and in at least a portion of the bonding portion (13), there is a tapered portion (5b) of the outer peripheral side of the central tube (5) with an enlarged diameter towards the center side in the axial direction (A1).