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MX2019004895A - Metodo para secar membrana de separacion y metodo para producir estructura de membrana de separacion. - Google Patents

Metodo para secar membrana de separacion y metodo para producir estructura de membrana de separacion.

Info

Publication number
MX2019004895A
MX2019004895A MX2019004895A MX2019004895A MX2019004895A MX 2019004895 A MX2019004895 A MX 2019004895A MX 2019004895 A MX2019004895 A MX 2019004895A MX 2019004895 A MX2019004895 A MX 2019004895A MX 2019004895 A MX2019004895 A MX 2019004895A
Authority
MX
Mexico
Prior art keywords
separation membrane
drying
gas
producing
membrane structure
Prior art date
Application number
MX2019004895A
Other languages
English (en)
Inventor
Noda Kenichi
Hagio Takeshi
Original Assignee
Ngk Insulators Ltd
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 by Ngk Insulators Ltd filed Critical Ngk Insulators Ltd
Publication of MX2019004895A publication Critical patent/MX2019004895A/es

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081After-treatment of organic or inorganic membranes
    • B01D67/0095Drying
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/10Supported membranes; Membrane supports
    • B01D69/108Inorganic support material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/04Specific process operations in the feed stream; Feed pretreatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/10Temperature control
    • B01D2311/103Heating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/14Pressure control
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/16Flow or flux control

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

Un método de secado para una membrana de separación (12) incluye un paso en el cual un gas para secado se suministra a la membrana de separación (12) cuando un valor obtenido al dividir la diferencia entre un valor máximo y un valor mínimo de un nivel de flujo del gas para secado en una superficie de membrana de la membrana de separación por el valor mínimo del nivel de flujo es menor o igual a 15%. El gas para secado es menor o igual a 40 grados C y contiene un gas soluble en agua que tiene una solubilidad en 1 cm3 de agua mayor o igual a 0.5 cm3 en condiciones de 40 grados C y 1 atmósfera.
MX2019004895A 2016-11-08 2017-10-03 Metodo para secar membrana de separacion y metodo para producir estructura de membrana de separacion. MX2019004895A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2016218366 2016-11-08
PCT/JP2017/035949 WO2018088064A1 (ja) 2016-11-08 2017-10-03 分離膜の乾燥方法及び分離膜構造体の製造方法

Publications (1)

Publication Number Publication Date
MX2019004895A true MX2019004895A (es) 2019-06-20

Family

ID=62109804

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2019004895A MX2019004895A (es) 2016-11-08 2017-10-03 Metodo para secar membrana de separacion y metodo para producir estructura de membrana de separacion.

Country Status (6)

Country Link
US (2) US11534724B2 (es)
JP (1) JP7096163B2 (es)
CN (1) CN109890489A (es)
DE (1) DE112017005622B4 (es)
MX (1) MX2019004895A (es)
WO (1) WO2018088064A1 (es)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4487938A1 (en) 2022-02-28 2025-01-08 NGK Insulators, Ltd. Membrane module
CN117138535A (zh) * 2023-07-22 2023-12-01 广东集氧科技有限公司 一种变压吸附氧气浓缩器的干燥装置

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JP2008237946A (ja) * 2007-03-23 2008-10-09 Fujifilm Corp セルロースエステル微細多孔質膜の製造方法および製造装置
JP5048371B2 (ja) 2007-03-29 2012-10-17 日本碍子株式会社 セラミック多孔質膜の製造方法及びセラミックフィルタの製造方法
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JP2010089000A (ja) 2008-10-07 2010-04-22 Ngk Insulators Ltd 分離膜の製造方法
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JP6074410B2 (ja) * 2012-03-16 2017-02-01 日本碍子株式会社 分離膜の製造方法、及び分離膜複合体の製造方法
JP5856524B2 (ja) 2012-03-29 2016-02-09 日本碍子株式会社 シリカ膜フィルタの製造方法
JP6056310B2 (ja) 2012-09-19 2017-01-11 三菱化学株式会社 アンモニアの分離方法
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Also Published As

Publication number Publication date
CN109890489A (zh) 2019-06-14
US11534724B2 (en) 2022-12-27
DE112017005622T5 (de) 2019-07-25
US20230078309A1 (en) 2023-03-16
DE112017005622B4 (de) 2026-02-05
JP7096163B2 (ja) 2022-07-05
WO2018088064A1 (ja) 2018-05-17
JPWO2018088064A1 (ja) 2019-09-26
US20190240626A1 (en) 2019-08-08

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