JP2009039654A - Separation membrane module - Google Patents

Abstract

A separation membrane module capable of further improving separation efficiency and separation performance is provided.
An upper tank 22 and a lower tank 24 are provided in a module main body 11. A separated fluid inlet 31 and a separated fluid outlet 32 are provided in the upper tank 22. A plurality of vertical bar-shaped membrane separation members 12 are passed to the upper tank 22 and the lower tank 24. Each membrane separation member 12 includes a tubular separation membrane 41 and an outer tube 42 that surrounds the separation membrane 41 at an interval. The upper end opening of the separation membrane 41 is opened to the outside of the upper tank 22, and the lower end opening thereof is closed. The upper end of the gap between the separation membrane 41 and the outer tube 42 is communicated with the upper tank, and the lower end thereof is communicated with the lower tank 24. A partition 28 is provided in the upper tank 22 so as to partition the separated fluid inlet 31 and the separated fluid outlet 32.
[Selection] Figure 1

Description

  The present invention relates to a separation membrane module for dehydrating a mixed solution containing, for example, water and an organic solvent.

  Zeolite crystals have pores of about the molecular size in the crystals, and have a molecular sieving property that allows molecules to selectively pass through depending on the size and shape of the zeolite molecules. Zeolite is applied to fields such as gas separation membranes, reverse gas permeation separation, reverse osmosis separation, and gas sensors by utilizing the properties of this molecular sieve. In particular, the use of a zeolite membrane as a separation membrane for separating an organic solvent or the like from a mixed solution containing water and an organic solvent or the like is currently attracting attention.

  As a module for separating an organic solvent by a separation membrane using the zeolite, for example, a plurality of tubular separation membranes having a zeolite membrane formed on the surface of a tubular support are installed, and a mixed liquid of water and an organic substance is passed outside. Thus, only water is allowed to permeate through the membrane, and the organic solvent and the like are separated from the mixed solution containing water and the organic solvent.

  Furthermore, an outer tube is provided around the tubular separation membrane so as to surround the tubular separation membrane with an interval, and a mixed solution containing water and an organic solvent is passed between the tubular separation membrane and the outer tube, so that the mixed solution is brought into the vicinity of the tubular separation membrane. A separation membrane module is known that passes at high speed and spreads over the entire tubular separation membrane with turbulent flow to improve separation efficiency (see, for example, Patent Document 1).

In the separation membrane module, an effect of improving a certain separation efficiency is recognized, but there is little opportunity for the mixed liquid to flow between the tubular separation membrane and the outer tube. I couldn't say that.
WO2004 / 035182

  An object of the present invention is to provide a separation membrane module capable of further improving separation efficiency and separation performance.

  In the separation membrane module according to the first aspect of the present invention, an upper tank and a lower tank are provided in the module body, a separated fluid inlet and a separation fluid outlet are provided in the upper tank, and a plurality of the upper tank and the lower tank are provided. The vertical rod-shaped membrane separation members are each composed of a tubular separation membrane and an outer tube surrounding the separation membrane at an interval, and the upper end opening of the separation membrane is located outside the upper tank. The lower end opening is closed, the upper end of the gap between the separation membrane and the outer tube is communicated with the upper tank, the lower end is communicated with the lower tank, and in the upper tank, A partition is provided so as to partition the separated fluid inlet and the separated fluid outlet.

  In the separation membrane module according to the first aspect of the present invention, the fluid to be separated introduced from the fluid inlet to the upper tank is guided from the upper tank to the lower tank through the gap between the separation membrane and the outer pipe. Therefore, the liquid is inverted and guided to the upper tank through the gap between the separation membrane and the outer tube. During this time, the separation fluid that has passed through the membrane separation member is discharged out of the upper tank and the upper tank. The separation fluid led to is led out from the upper tank through the separation fluid outlet. Therefore, the opportunity for a mixed liquid such as water and an organic solvent to pass between the tubular separation membrane and the outer tube can be increased, so that the separation efficiency and the separation performance can be further improved.

  The separation membrane module according to claim 2 of the present invention is provided with an upper tank and a lower tank in the module body, a separation fluid inlet and a separation fluid outlet are provided in the upper tank, and a plurality of the upper tank and the lower tank are provided. The vertical rod-shaped membrane separation members are each composed of a tubular separation membrane and an outer tube surrounding the separation membrane at an interval, and the upper end opening of the separation membrane is located outside the upper tank. The lower end opening is closed, the upper end of the gap between the separation membrane and the outer tube is communicated with the upper tank, the lower end is communicated with the lower tank, and in the upper tank, A plurality of upper partitions are provided from the separated fluid inlet to the separated fluid outlet, and the number of lower partitions obtained by subtracting 1 from the number of upper partitions is provided in the lower tank. , Downwardly between upper two adjacent partition, in which one of the lower partition are then positioned.

  In the separation membrane module according to the second aspect of the present invention, the fluid to be separated introduced from the fluid inlet to the upper tank is passed through the gap between the separation membrane and the outer tube a plurality of times between the upper tank and the lower tank. By reciprocating, the opportunity of passing between the separation membrane and the outer tube can be freely adjusted according to the conditions such as the type of fluid to be separated and the flow velocity.

  The separation membrane module according to claim 3 of the present invention is provided with a heating means for heating each membrane separation member.

  In the separation membrane module according to the third aspect of the present invention, it is possible to prevent the condensation that occurs when steam is introduced into the fluid to be separated while the membrane separation member is at a low temperature, such as during startup.

  In the separation membrane module according to claim 4 of the present invention, the separation membrane is formed by forming a zeolite membrane on the surface of a support made of ceramics.

  According to the present invention, a separation membrane module capable of further improving separation efficiency and separation performance is provided.

  Embodiments of the present invention will be described below with reference to the drawings.

  Referring to FIGS. 1 and 2, the separation membrane module includes a vertical cylindrical module body 11 closed at both ends, and a plurality of vertical bar-shaped membrane separation members 12 arranged in parallel in the module body 11.

  An upper tank 22 defined by a horizontal upper tube plate 21 is provided at the top of the module body 11. A lower tank 24 partitioned by a horizontal lower tube plate 23 is provided at the bottom of the module body 11. A horizontal partition plate 25 is provided in the upper tank 22. A discharge chamber 26 is formed above the horizontal partition plate 25 in the upper tank 22, and a header chamber 27 is formed below it. A vertical partition plate 28 is provided in the header chamber 27.

  A separated fluid inlet 31 is provided so as to communicate with one side of the vertical partition plate 28 of the header chamber 27, and a separated fluid outlet 32 is provided so as to communicate with the other side. Further, another separation fluid outlet 33 is provided so as to communicate with the discharge chamber 26.

  The membrane separation member 12 includes a tubular separation membrane 41 formed by forming a zeolite membrane on the surface of a support made of ceramics, and an outer tube 42 surrounding the separation membrane 41 with an interval.

  The lower end of the vertical connection pipe 43 is connected to the upper end of the separation membrane 41 in a straight line. The upper end opening of the connection pipe 43 is open to the discharge chamber 26. The lower end of the separation membrane 41 is closed by a closing member (not shown). The upper end of the gap between the separation membrane 41 and the outer tube 42 is communicated with the header chamber 27, and the lower end thereof is communicated with the lower tank 24.

  The separated fluid is introduced into the header chamber 27 from the separated fluid inlet 31. The introduced fluid to be separated is guided from the header chamber 27 to the lower tank 24 through a gap between the separation membrane 41 and the outer tube 42 on one side of the vertical partition plate 28. The fluid to be separated guided to the lower tank 24 is reversed in the lower tank 24 and guided to the header chamber 27 through the gap between the separation membrane 41 and the outer tube 42 on the other side of the vertical partition plate 28. While the fluid to be separated is guided from the upper tank 22 to the lower tank 24, where the fluid to be separated is reversed and returned to the upper tank 22 again, the separated fluid that has passed through the separation membrane 41 passes through the discharge chamber 26 to the outside of the upper tank 22. The separation fluid discharged to the header chamber 27 and returned to the header chamber 27 is led out from the header chamber 27 through the separation fluid outlet 32.

  3 and 4 show another embodiment. 3 and FIG. 4, parts corresponding to those in FIG. 1 and FIG. 2 are given the same reference numerals as those in FIG. 1 and FIG. 2, and their detailed description is omitted.

  In the header chamber 27, two vertical upper partition plates 51 are provided. Thus, the inlet side chamber 52, the intermediate chamber 53, and the outlet chamber 54 are formed in the header chamber 27 so as to be aligned in a line from the separated fluid inlet 31 to the separated fluid outlet 32. In the lower tank 24, one vertical lower partition plate 55 is provided. One lower partition plate 55 is positioned below the middle between the two upper partition plates 51.

  All the membrane separation members 12 are divided into three groups at the upper end from the separated fluid inlet 31 to the separation fluid outlet 32, and the gap between the separation membrane 41 and the outer tube 42 of the membrane separation member 12 of each group. The inlet side chamber 52, the intermediate chamber 53, and the outlet chamber 54 are communicated with each other. On the other hand, all the membrane separation members 12 are divided into two groups at the lower end from the separated fluid inlet 31 to the separation fluid outlet 32, and between the separation membrane 41 and the outer tube 42 of the membrane separation member 12 of each group. The gap communicates with both sides of the lower partition plate 55 of the lower tank 24.

  In the example shown in FIG. 1 and FIG. 2, the liquid to be separated can be reciprocated only once between the upper tank 22 and the lower tank 24. However, in the examples shown in FIG. 3 and FIG. Thus, the separation efficiency can be further improved. Further, the number of upper partition plates 51 may be three or more. In this case, the number of the lower partition plates 55 is reduced by 1 from the number of the upper partition plates 51.

  FIG. 5 shows an example in which a heating device 61 for heating the membrane separation member 12 shown in FIGS. 3 and 4 is provided.

  The heating device 61 is an electric heater. Instead of the electric heater, a heating fluid, for example, steam may be introduced into and led out from the space between the upper tank 22 and the lower tank 24 in the module main body 11.

It is a vertical longitudinal cross-sectional view of the separation membrane module by this invention. FIG. 2 is a horizontal cross-sectional view taken along line II-II in FIG. 1. It is a vertical longitudinal cross-sectional view of the separation membrane module by other embodiment of this invention. FIG. 4 is a horizontal cross-sectional view taken along line IV-IV in FIG. 3. It is a vertical longitudinal cross-sectional view of the separation membrane module by further another embodiment of this invention.

Explanation of symbols

11 Module body
12 Membrane separation member
22 Upper tank
23 Lower tank
28 Partition plate
31 Fluid inlet
32 Separation fluid outlet
41 Separation membrane
42 outer cylinder

Claims (4)

  The module body is provided with an upper tank and a lower tank, the upper tank is provided with a separated fluid inlet and a separated fluid outlet, and a plurality of vertical rod-shaped membrane separation members are passed to the upper tank and the lower tank. The separation member is composed of a tubular separation membrane and an outer tube surrounding the separation membrane at an interval, the upper end opening of the separation membrane is opened to the outside of the upper tank, and the lower end opening thereof is closed, The upper end of the gap between the separation membrane and the outer pipe is communicated with the upper tank, and the lower end is communicated with the lower tank. The upper tank is partitioned so as to partition the separated fluid inlet and the separated fluid outlet. Separation membrane module provided with.   The module body is provided with an upper tank and a lower tank, the upper tank is provided with a separated fluid inlet and a separated fluid outlet, and a plurality of vertical rod-shaped membrane separation members are passed to the upper tank and the lower tank. The separation member is composed of a tubular separation membrane and an outer tube surrounding the separation membrane at an interval, the upper end opening of the separation membrane is opened to the outside of the upper tank, and the lower end opening thereof is closed, The upper end of the gap between the separation membrane and the outer pipe communicates with the upper tank, and the lower end communicates with the lower tank. A plurality of upper partitions are formed in the upper tank from the separated fluid inlet to the separated fluid outlet. The lower tank is provided with a number of lower partitions obtained by subtracting 1 from the number of upper partitions, and one lower partition is provided between two adjacent upper partitions. Separation membrane modules that are to location.   The separation membrane module according to claim 1, further comprising heating means for heating each membrane separation member.   The separation membrane module according to any one of claims 1 to 3, wherein the separation membrane is formed by forming a zeolite membrane on the surface of a support made of ceramics.

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