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Membrane device and process for mass exchange, separation, and filtration

A kind of equipment, technology in equipment, applied in the direction of separation method, lighting and heating equipment, chemical instrument and method, etc., can solve the problem that the membrane filter is not suitable, etc.

Active Publication Date: 2015-12-23
BATTELLE MEMORIAL INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Also, membrane filters designed for liquid phase filtration are not suitable for vapor phase separation at low pressure or under vacuum where pressure drop becomes a significant issue

Method used

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  • Membrane device and process for mass exchange, separation, and filtration
  • Membrane device and process for mass exchange, separation, and filtration
  • Membrane device and process for mass exchange, separation, and filtration

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0120] [filter application]

[0121] use Figure 7A membrane module. A cross-flow membrane module is constructed and configured for filtering and harvesting algae. In Table 1 the design parameters for the membrane modules are listed.

[0122] Table 1 lists the dimensions and components of a typical cross-flow membrane module for filtration applications.

[0123] Diaphragm scale

[0124] width

[0125] as reference Figure 4B As described, capsules are stacked on top of each other. Corrugated (wavy) nickel (Ni) mesh was placed between the individual bellows in the stack, and between bellows positioned adjacent the top and bottom cover plates. The membrane module consists of 9 membrane cassettes with 10 feed tanks and 9 permeate tanks. The wavy Ni mesh was used as spacer material and to support the membrane in the bellows during recoil. During normal filtration operation, the pressure on the feed side of the membrane device is greater than the pressure...

Embodiment 2

[0127] [Membrane module for dehumidification]

[0128] use Figure 7A membrane module. Cross-flow membrane modules are constructed and configured for molecular separation and dehumidification. In Table 2 the design parameters for the membrane modules are listed.

[0129] Table 2 lists the dimensions and components of a typical cross-flow membrane module for air dehumidification applications.

[0130] Dimensions of diaphragm used

width

5.25cm

length

11.25cm

Diaphragms exposed to moist air

width

4cm

length

10cm

Number of diaphragms

6

Number of bellows

3

Supply side (film coating)

channel height

0.1cm

Supply channel spacing

4cm

Number of supply slots

4

Permeate side

Polyester base (0.5mm) thickness

0.1cm

open access height

0.1cm

Number of infiltration tanks

3

Calculation results

...

Embodiment 3

[0144] [Membrane modules for humidity exchange and heat exchange]

[0145] A counterflow membrane module was fabricated with a single 50 μm thick zeolite / Ni membrane configured with a 4 cm x 10 cm active area and subjected to air dehumidification and enthalpy exchange measurements. The module has a symmetrical design. The same base material was placed on both sides of the membrane. A 0.5 mm thick sheet of fabric polyester was placed on the rear side of the diaphragm. A 0.5 mm thick sheet of fabric polyester was placed between the diaphragm and cover plate. The feed gas flow is introduced from one side of the membrane. Sweep gas flow is introduced from the other side of the diaphragm. The feed gas flow through the three inlet ports was distributed over a 10 cm wide membrane. The flow of feed gas flows through the membrane in the opposite direction to the flow of sweep gas. The length of the flow path is 4 cm. Humidity exchange was performed at room temperature with const...

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PUM

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Abstract

A membrane device and processes for fabrication and for using are disclosed. The membrane device may include a number of porous metal membranes that provide a high membrane surface area per unit volume. The membrane device provides various operation modes that enhance throughput and selectivity for mass exchange, mass transfer, separation, and / or filtration applications between feed flow streams and permeate flow streams.

Description

[0001] Cross References to Related Applications [0002] This application claims the benefit of U.S. Provisional Application No. 61 / 768,124, filed February 22, 2013, entitled "Membrane Device and Process for Mass Exchange, separation, and Filtration," and filed February 20, 2014, entitled "Membrane Device and Process for Mass Exchange, separation, and Filtration" Priority of U.S. Application No. 14 / 185,706. [0003] Statement of Rights to Inventions Made Under Federally Sponsored Research and Development [0004] This invention was made with Government support under Contract DE-AC05-76RLO1830 awarded by the US Department of Energy. The US Government has certain rights in this invention. Background technique [0005] Low-cost, large-surface-area inorganic membrane modules have long been the subject of industrial research because they possess both the unique performance properties of metallic materials and those of ceramic materials. In order to easily unfold the membrane mod...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D63/08B01D53/02B01D53/22F24F3/14
CPCB01D53/228B01D61/02B01D61/14B01D63/082B01D63/085B01D71/028B01D2311/13B01D2315/10B01D53/268B01D2257/504B01D53/02F24F3/14B01D2253/108B01D71/022Y10T29/49826Y02C20/40B01D63/081B01D63/084B01D65/02B01D63/0822B01D71/0281B01D71/02232
Inventor 刘伟N·L·坎菲尔德
Owner BATTELLE MEMORIAL INST
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