EA201900156A2 - FILTER ELEMENT - Google Patents

FILTER ELEMENT

Info

Publication number
EA201900156A2
EA201900156A2 EA201900156A EA201900156A EA201900156A2 EA 201900156 A2 EA201900156 A2 EA 201900156A2 EA 201900156 A EA201900156 A EA 201900156A EA 201900156 A EA201900156 A EA 201900156A EA 201900156 A2 EA201900156 A2 EA 201900156A2
Authority
EA
Eurasian Patent Office
Prior art keywords
plasma
chemical
polymer particles
particles
membrane
Prior art date
Application number
EA201900156A
Other languages
Russian (ru)
Other versions
EA201900156A3 (en
EA036614B1 (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Publication of EA201900156A2 publication Critical patent/EA201900156A2/en
Publication of EA201900156A3 publication Critical patent/EA201900156A3/en
Publication of EA036614B1 publication Critical patent/EA036614B1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D27/00Cartridge filters of the throw-away type
    • B01D27/08Construction of the casing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/18Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06Tubular membrane modules

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

Фильтрующий элемент относится к фильтрационному оборудованию. Фильтрующий элемент содержит пористую трубчатую подложку (5), фильтрующую мембрану (6), крышку (2) с отверстием (3), днище (1), покрытие и подстилающую плазмохимическую мембрану (4). Пористая трубчатая подложка (5) спечена из полимерных частиц. На торцах пористой трубчатой подложки установлены крышка (2) с отверстием (3) и днище (2). Покрытие выполнено на поверхности полимерных частиц. На внешней поверхности пористой трубчатой подложки (5) нанесена подстилающая плазмохимическая мембрана (4), а на ее поверхности расположена фильтрующая мембрана (6). Предложены следующие частные случаи выполнения фильтрующего элемента. Во-первых, размер полимерных частиц соответствует диапазону от 50 до 180 мкм. Во-вторых, отношение эквивалентных диаметров сквозных пор пористой трубчатой подложки (5) и подстилающей плазмохимической мембраны (4), по меньшей мере, равно 10. В-третьих, отношение эквивалентных диаметров сквозных пор подстилающей плазмохимической (4) и фильтрующей (6) мембран, по меньшей мере, равно 50. В-четвертых, покрытие на полимерных частицах имеет температуру плавления больше 1000°C и выполнено из сорбционно-активных плазменных частиц размером в диапазоне от 0,0035 до 0,0070 мкм или сформировано из их плазмохимических нитридных, оксидных или оксинитридных частиц. В-пятых, покрытие на полимерных частицах имеет температуру плавления не более 1100°C и выполнено из каталитически активных плазменных частиц меди, олова или висмута размером в диапазоне от 0,0055 до 0,0085 мкм или сформировано из их плазмохимических оксидов. В-шестых, полимерные частицы с покрытием из сорбционно-активных и каталитически активных плазмохимических частиц смешаны по массе, по меньшей мере, в соотношении 1:1. Технический результат - повышение тонкости очистки жидкости от механических примесей и эффективности очистки жидкости от растворенных примесей.The filter element refers to filtration equipment. The filter element contains a porous tubular substrate (5), a filtering membrane (6), a cover (2) with a hole (3), a bottom (1), a coating and a underlying plasma-chemical membrane (4). The porous tubular support (5) is sintered from polymer particles. At the ends of the porous tubular substrate there is a lid (2) with an opening (3) and a bottom (2). The coating is made on the surface of polymer particles. An underlying plasmochemical membrane (4) is deposited on the outer surface of the porous tubular substrate (5), and a filter membrane (6) is located on its surface. The following particular cases of filter element execution are proposed. Firstly, the size of the polymer particles corresponds to a range from 50 to 180 microns. Secondly, the ratio of the equivalent diameters of the through pores of the porous tubular substrate (5) and the underlying plasma-chemical membrane (4) is at least equal to 10. Thirdly, the ratio of the equivalent diameters of the through pores of the through pore of the underlying plasma-chemical (4) and filtering (6) membranes at least equal to 50. Fourth, the coating on polymer particles has a melting point greater than 1000 ° C and is made of sorption-active plasma particles with a size in the range from 0.0035 to 0.0070 μm or formed from their plasma-chemical nitride, oxide or ksinitridnyh particles. Fifth, the coating on polymer particles has a melting point of not more than 1100 ° C and is made of catalytically active plasma particles of copper, tin or bismuth in the size range from 0.0055 to 0.0085 μm or formed from their plasma-chemical oxides. Sixth, polymer particles coated with sorption-active and catalytically active plasma-chemical particles are mixed by weight, at least in a ratio of 1: 1. EFFECT: increased fineness of liquid purification from mechanical impurities and efficiency of liquid purification from dissolved impurities.

EA201900156A 2017-12-28 2018-12-21 Filtering element EA036614B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2017146401A RU2678016C1 (en) 2017-12-28 2017-12-28 Filtering element

Publications (3)

Publication Number Publication Date
EA201900156A2 true EA201900156A2 (en) 2019-10-31
EA201900156A3 EA201900156A3 (en) 2020-01-31
EA036614B1 EA036614B1 (en) 2020-11-30

Family

ID=65085046

Family Applications (1)

Application Number Title Priority Date Filing Date
EA201900156A EA036614B1 (en) 2017-12-28 2018-12-21 Filtering element

Country Status (2)

Country Link
EA (1) EA036614B1 (en)
RU (1) RU2678016C1 (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994000618A1 (en) * 1992-06-23 1994-01-06 Higher Vacuum Ind Co., Ltd. Process for laminating metal for emi-blocking over plastic
RU2148679C1 (en) * 1999-03-25 2000-05-10 Закрытое акционерное общество "Обнинский центр естественных наук и технологий" Filter member and method of its manufacture
CA2361930A1 (en) * 1999-12-08 2001-06-14 Baxter International Inc. Microporous filter membrane, method of making microporous filter membrane and separator employing microporous filter membranes
EP2696963B1 (en) * 2011-04-13 2021-03-24 3M Innovative Properties Company Macroporous filtration membrane
RU2635617C1 (en) * 2016-12-23 2017-11-14 Федеральное государственное бюджетное образовательное учреждение высшего образования "Российский химико-технологический университет имени Д.И. Менделеева" Method of filtration material production
RU174088U1 (en) * 2016-12-27 2017-10-02 Акционерное Общество "БВТ БАРЬЕР РУС" Filter element for drinking water purification

Also Published As

Publication number Publication date
RU2678016C1 (en) 2019-01-22
EA201900156A3 (en) 2020-01-31
EA036614B1 (en) 2020-11-30

Similar Documents

Publication Publication Date Title
CN103611431B (en) Preparation method of graphene membrane supported by porous ceramic
CN101947415B (en) Combination of electrostatic spinning and electrostatic spraying for preparing nanofibre base composite separation membrane
CN105396466B (en) Cellulose nanofiber-graphene oxide hybrid composite ultrafiltration membrane and preparation method thereof
RU2007138589A (en) COATED FILTER ELEMENT FOR SURFACE FILTRATION
JPWO2008010452A1 (en) Ceramic filter
CN101559327B (en) Nanometre-sized fibre liquid separation composite film and preparation method thereof
CN103551050B (en) A kind of inorganic composite ultra-filtration membrane and preparation method thereof
JP2016515933A (en) Method for producing oil-absorbing hollow fiber porous membrane
RU2010120692A (en) SEPARATING MEMBRANE ELEMENT AND FILTERING MEMBRANE MODULE
KR20160133459A (en) A Filter Structure For Fuel, A Cartridge And A Filter Group
CN108939945A (en) A kind of compound carbon film of stable ceramic base and preparation method thereof
EA201900156A2 (en) FILTER ELEMENT
CN101559329A (en) Metallic fiber sintered felt composite filtering element
CN208356241U (en) A kind of PVDF perfluor skeleton
CN108744996A (en) A kind of water-oil separating filter membrane and preparation method thereof with titanium dioxide surface
CN105774149A (en) Composite filtering material capable of being used for gas-liquid separation
JP5856524B2 (en) Method for producing silica membrane filter
KR101368462B1 (en) Separation Membrane for Water Treatment and Manufacturing Method thereof
JP2015058406A (en) Precious metal supporting device and precious metal supporting method using the same
CN201454427U (en) Non-symmetric metal film filter component
CN207025109U (en) A kind of complex reverse osmosis membrane
PL428273A1 (en) Method of producing polymer membranes having antimicrobial properties by plasma-chemical method
JP2016093794A (en) Ceramic filter
CN209173491U (en) A kind of folding type filter element
CN107849724A (en) Porous material and system and its manufacture method

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM KG TJ TM RU