Installation and method for the treatment by membrane permeation of a gas stream with the aspiration pressure of the second permeate adjusted

Patent metadata

Field	Value
Publication number	US-11083991-B2
Application number	US-201916712373-A
Country	US
Kind code	B2
Filing date	Dec 12, 2019
Priority date	Dec 14, 2018
Publication date	Aug 10, 2021
Grant date	Aug 10, 2021

Abstract

Installation for membrane permeation treatment of feed gas containing methane and carbon dioxide that includes first, second, and third membrane separation units. The permeate from the first membrane separation unit is fed to the third membrane separation unit and the retentate from the first membrane separation unit is fed to the second membrane separation unit. The aspiration pressure of the second permeate is adjusted with a compressor according to the aspiration pressure of the second permeate before recycling thereof to the feed gas flow fed to the first membrane separation unit.

First claim

What is claimed is:

1. The method for controlling membrane permeation treatment of a feed gas flow containing at least methane and carbon dioxide, comprising the following steps:
providing an installation that comprises: a compressor A for compressing the combined flows of feed gas and a third retentate, a first membrane separation unit able to receive the compressed combined flow of feed gas and third retentate that is admixed with a second permeate and to supply a first permeate and a first retentate, a second membrane separation unit able to receive the first retentate and to supply the second permeate and a second retentate, a third membrane separation unit able to receive the first permeate and to supply a third permeate and the third retentate, and at least one compressor B for aspirating the second permeate, feeding the aspirated second permeate to the compressed combined flows of the feed gas and the third retentate, and adjusting the aspiration pressure of the second permeate, wherein each membrane separation unit comprises at least one membrane that is more permeable to carbon dioxide than to methane;
measuring the aspiration pressure of the second permeate at a location in between the second membrane separation unit and the compressor B;
comparing the measured aspiration pressure with an associated setpoint value; and
adjusting the aspiration pressure of the second permeate by the compressor B in order to keep the pressure value equal to the setpoint value associated with the aspiration pressure.

2. The method of claim 1 , wherein, in the adjustment step, the compressor B is accelerated or decelerated.

3. The method of claim 1 , wherein the measurement, comparison and adjustment steps are carried out automatically by data transmission means.

4. The method of claim 1 , wherein the feed gas flow is biogas.

Assignees

• Air Liquide

Inventors

• Barraud Francois
• Chareyre Jean-Marc

Classifications

• Y02E50/30

  Fuel from waste, e.g. synthetic alcohol or diesel · CPC title

• Y02C20/40

  of CO2 · CPC title

• B01D53/226 Primary

  in serial connexion · CPC title

• C07C7/144

  using membranes, e.g. selective permeation · CPC title

• C10L3/104 Primary

  Carbon dioxide · CPC title