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Novel coupling film separating method and device used in gas separation

A gas separation membrane and gas separation technology, which is applied in the field of coupled membrane separation and devices for gas separation, can solve the problems of complexity, poor chemical stability of olefin carriers, and restrictions on the development of industrialization process, and achieve the effect of promoting the transfer process

Inactive Publication Date: 2009-06-24
TIANBANG NAT ENG RES CENT OF MEMBRANE TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In its U.S. Patent 5670051 (1997), Pinnau et al. put Ag + Embedded in a polymer membrane to form a so-called solid polymer electrolyte membrane, but the poor chemical stability of olefin supports seriously hinders the industrialization of this separation process
At the same time, Nymeijer et al pointed out that Ag + For trace H 2 Gases such as S and acetylene are more sensitive, including Ag + The solid polymer electrolyte membrane regeneration process is also very difficult and complicated, and these factors are urgent problems to be solved in the current industrialization
[0006] To sum up, for the separation of olefins / alkanes, there are serious industrial bottlenecks in the technical routes of gas separation membranes, carrier-facilitated transfer composite membranes, and supported liquid membranes, which restrict the development of the industrialization process.

Method used

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  • Novel coupling film separating method and device used in gas separation
  • Novel coupling film separating method and device used in gas separation
  • Novel coupling film separating method and device used in gas separation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0061] Example 1 Theoretical simulation of the separation performance of ethylene / ethane passing through the separation unit

[0062] The composite gas separation membrane with polyetherimide (PEI) porous membrane as the base membrane and polydimethylsiloxane (PDMS) as the composite separation layer material is used as the gas separation membrane of the gas separation membrane bag. The carrier solution is 4M AgNO 3 solution. The loss and renewal of the carrier solution is not considered in the simulation, and the flow velocity of the carrier solution in the channel of the carrier solution is 0m / s. The raw gas is pure ethylene and ethane. Separation performance of composite gas separation membranes with ethylene and ethane in AgNO 3 The physical properties in the carrier solution are shown in Table 1. The thickness (d) of the carrier solution channel is 300 μm. Ethylene proceeds in the form of dissolution and diffusion in the composite gas separation membrane, in the form o...

Embodiment 2

[0063] Example 2 Sandwich gas separation membrane bag

[0064] In the present invention, the gas separation membrane bag is defined as a basic separation unit, forming a sandwich structure of gas separation membrane-carrier solution-gas separation membrane. Figure 9 A schematic diagram of the structure of a basic gas separation membrane bag is depicted. A carrier solution channel with a certain thin layer thickness (d) is formed between the gas separation membranes 2a and 2b, and the carrier solution flow 5 flows in the channel at a certain speed to replenish and renew the carrier solution. A spacer 3a of a certain thickness may be placed between the gas separation membranes to support the gas separation membranes. At the same time, the thickness of the carrier solution, that is, the distance (d) between the gas separation membranes can be adjusted by the thickness of the spacer 3a between the gas separation membranes. The carrier solution 3 is filled in the space between t...

Embodiment approach 3

[0068] Embodiment 3 Separation device

[0069] Several gas separation membrane bags can be stacked to produce a plate-and-frame membrane separation unit or a roll-type membrane separation unit. A certain distance is maintained between adjacent gas separation membrane bags to form passages for raw gas or permeate gas. Figure 13 Overlay schematic diagram illustrating the membrane elemental separation elements for the preparation of the membrane separation unit. The M th gas separation membrane bag and the M+1 th gas separation membrane bag form a raw gas channel 7 . Its spacing (df) can be adjusted through the net or frame. The M+1th gas separation membrane bag and the M+2th gas separation membrane bag form a permeate gas channel 8 . Its spacing (dp) can also be adjusted through a mesh or frame. The M+2 basic membrane separation element and the M+3 basic membrane separation element form the raw gas channel 7 . Raw material gas channels and permeate gas channels appear alte...

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PUM

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Abstract

The invention relates to a gas separation method and device, a coupling membrane separation method for gas separation, raw material gas is separated through a plurality of separation units, each separation unit raw material gas is first in contact with a gas separation membrane on one side, and can be formed with a carrier solution The ligand is first dissolved and diffused in the gas separation membrane that is in contact with it through the gas component that facilitates the transfer, and then forms a ligand structure with the carrier solution to facilitate the transfer. The dissolution and diffusion in the gas separation membrane is desorbed on the permeation side; the gas components in the raw gas that cannot form ligands with the carrier solution first dissolve and diffuse in the gas separation membrane in contact with it, and then dissolve and diffuse in the thin layer of carrier solution The form is in contact with the gas separation membrane on the other side, and desorbs on the permeation side through dissolution and diffusion in the gas separation membrane to achieve the purpose of separating the raw gas. The separation method of the present invention not only satisfies the requirement of high-pressure gas separation, eliminates plastic effect, but also prevents membrane wetting and leakage, and maintains long-term stability.

Description

Technical field: [0001] The present invention relates to a gas separation method, and also to a gas separation device. Background technique: [0002] Gas separation is a very important processing method in the chemical industry, especially olefin / alkane separation has always occupied a very important position in the chemical industry. Ethylene and propylene are chemical raw materials with the largest and second largest output in petrochemical industry. At present, the separation technologies of olefins / alkanes mainly include cryogenic rectification, pressure swing adsorption, lean oil absorption, extractive distillation, etc. These processes generally have poor selectivity, low separation coefficient and high energy consumption. At present, the raw materials for olefin production mainly come from crude oil (naphtha, diesel, propane, etc.) and natural gas (ethane, propane, etc.). Since olefins / alkanes have very similar boiling points, the distillation column used for separa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/22
Inventor 任吉中王雁北邓麦村
Owner TIANBANG NAT ENG RES CENT OF MEMBRANE TECH