Separation method and separation apparatus

Patent metadata

Field	Value
Publication number	US-10407367-B2
Application number	US-201715463224-A
Country	US
Kind code	B2
Filing date	Mar 20, 2017
Priority date	Sep 29, 2014
Publication date	Sep 10, 2019
Grant date	Sep 10, 2019

Abstract

A separation apparatus 10 includes a pretreatment section 20 that subjects a target fluid containing an olefin compound to at least one or more of a treatment for reducing an acetylene-based compound, a treatment for reducing a sulfur compound, and a treatment for reducing a fine particle component. In the pretreatment section 20, one or more treatments selected from a hydrotreating and an adsorption treatment with an adsorbent may be performed as the treatment for reducing the acetylene-based compound, one or more treatments selected from a washing and absorption treatment, an adsorption treatment with an adsorbent, and a hydrodesulfurization treatment may be performed as the treatment for reducing the sulfur compound, and one or more treatments selected from a liquid absorption treatment, a collection treatment, or a filtration treatment with a filter may be performed as the treatment for reducing the fine particle component.

First claim

What is claimed is:

1. A separation method, comprising:
a pretreatment step of subjecting a target fluid containing an olefin compound to at least one or more of a treatment for reducing an acetylene-based compound, a treatment for reducing a sulfur compound, and a treatment for reducing a fine particle component; and
a separation step of directing the target fluid into an inlet of a separation structure comprising a porous substrate carrying an Ag-containing separation membrane, wherein the olefin compound from the target fluid that has been subjected to the pretreatment step passes through the separation membrane and the remaining portion of the target fluid is exhausted from an outlet of the separation structure without passing through the separation membrane.

2. The separation method according to claim 1 , wherein in the pretreatment step, one or more treatments selected from a hydrotreating and an adsorption treatment with an adsorbent are performed as the treatment for reducing the acetylene-based compound.

3. The separation method according to claim 1 , wherein in the pretreatment step, one or more treatments selected from a washing and absorption treatment, an adsorption treatment with an adsorbent, and a hydrodesulfurization treatment are performed as the treatment for reducing the sulfur compound.

4. The separation method according to claim 1 , wherein in the pretreatment step, one or more treatments selected from a liquid absorption treatment, a collection treatment, and a filtration treatment with a filter are performed as the treatment for reducing the fine particle component.

5. The separation method according to claim 1 , wherein in the pretreatment step, the treatment for reducing the acetylene-based compound and the treatment for reducing the fine particle component are performed, the treatment for reducing the sulfur compound and the treatment for reducing the fine particle component are performed, or the treatment for reducing the acetylene-based compound and the treatment for reducing the sulfur compound are performed.

6. The separation method according to claim 1 , wherein in the separation step, one or more of a Ag-containing zeolite membrane and a Ag-containing organic-inorganic hybrid membrane are used as the separation membrane.

7. The separation method according to claim 1 , wherein in the separation step, one or more of Ag-containing zeolite membranes having LTA-type, LTL-type, MFI-type, MEL-type, MOR-type, MWW-type, FER-type, and BEA-type crystal structures are used as the separation membrane.

8. The separation method according to claim 1 , wherein in the separation step, a Ag-containing zeolite membrane having an MFI-type crystal structure is used as the separation membrane.

Assignees

• Ngk Insulators Ltd

Inventors

• Noda Kenichi

Classifications

• C10G53/02

  plural serial stages only · CPC title

• B01D2252/10

  Inorganic absorbents · CPC title

• C10G67/02

  plural serial stages only · CPC title

• B01D2311/04

  Specific process operations in the feed stream; Feed pretreatment · CPC title

• C07C7/11

  by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids · CPC title