Method of charging a sorption store with a gas

Patent metadata

Field	Value
Publication number	US-9243754-B2
Application number	US-201314048223-A
Country	US
Kind code	B2
Filing date	Oct 8, 2013
Priority date	Oct 9, 2012
Publication date	Jan 26, 2016
Grant date	Jan 26, 2016

Abstract

Described is a method of charging a sorption store with a gas. The sorption store comprises a closed container which is at least partly filled with an adsorption medium and has an inlet and an outlet which can each be closed by a shut-off element. The method comprises the steps: (a) closing of the outlet shut-off element and opening of the inlet shut-off element, (b) introduction of gas to be stored under a predetermined pressure through the inlet, (c) rapid opening of the outlet shut-off element with the inlet shut-off element open so that a gas flow having a predetermined flow rate is established in the container, (d) reduction of the flow rate as a function of the adsorption rate of the gas adsorbed in the store, and (e) complete closing of the outlet shut-off element.

First claim

What is claimed is:

1. A method of charging a sorption store with a gas, wherein the sorption store comprises a closed container which is at least partly filled with an adsorption medium and has an inlet and an outlet which can each be closed by a shut-off element, the method comprising the steps:
(a) closing of the outlet shut-off element and opening of the inlet shut-off element,
(b) introduction of the gas to be stored under a predetermined pressure through the inlet,
(c) rapid opening of the outlet shut-off element with the inlet shut-off element open so that a gas flow having a predetermined flow rate is established in the container,
(d) reduction of the flow rate as a function of the adsorption rate of the gas adsorbed in the store, and
(e) complete closing of the outlet shut-off element.

2. The method according to claim 1 , wherein the container has at least two parallel, channel-shaped subchambers which are each at least partly filled with the adsorption medium and whose channel walls are cooled in its interior.

3. The method according to claim 2 , wherein the channel walls of the channel-shaped subchambers are configured as double walls and a heat transfer medium flows through them.

4. The method according to claim 2 , wherein the spacing of the channel walls in each channel-shaped subchamber is from 2 cm to 8 cm.

5. The method according to claim 1 , wherein the gas stream flowing into the container or out of the container is measured by means of a flow sensor and the flow rate of the gas in the container is set as a predetermined multiple of the adsorption rate over time.

6. The method according to claim 5 , wherein the predetermined multiple is from 1.5 to 100.

7. The method according to claim 1 , wherein the temperature of the gas stream is measured at at least one point in the interior of the container and is matched to the flow rate of the gas in the container when required in such a way that a predetermined maximum temperature is not exceeded.

8. The method according to claim 1 , wherein the porosity of the adsorption medium is at least 0.2.

9. The method according to claim 1 , wherein the adsorption medium is present as a bed of pellets and the ratio of the permeability of the pellets to the smallest pellet diameter is at least 10 −14 m 2 /m.

10. The method according to claim 1 , wherein the adsorption medium is selected from zeolite, activated carbon, or metal organic frameworks.

11. The method according to claim 5 , wherein the predetermined multiple is from 3 to 40.

12. The method according to claim 1 , wherein the temperature of the gas stream is measured in at least one channel-shaped subchamber and is matched to the flow rate of the gas in the container when required in such a way that a predetermined maximum temperature is not exceeded.

Assignees

• Basf Se

Inventors

• Weickert Mathias
• Marx Stefan
• Müller Ulrich
• Renze Peter
• Winkler Christian-Andreas

Classifications

• F17C11/007

  for hydrocarbon gases, such as methane or natural gas, propane, butane or mixtures thereof [LPG] · CPC title

• F17C11/00 Primary

  Use of gas-solvents or gas-sorbents in vessels {(absorbing compositions for acetylene C10L3/04; absorbing compositions for hydrogen C01B3/0005)} · CPC title

• F17C11/005 Primary

  for hydrogen · CPC title