Device and method for indicating a fill level of a sorption store

Patent metadata

Field	Value
Publication number	US-2016201854-A1
Application number	US-201414911789-A
Country	US
Kind code	A1
Filing date	Aug 11, 2014
Priority date	Aug 15, 2013
Publication date	Jul 14, 2016
Grant date	—

Abstract

A process for indicating a fill level of a sorption store ( 1 ), wherein at least one gas adsorbent medium ( 5 ) is disposed within at least one vessel ( 3 ) and wherein a total amount (n total ) of a gas ( 15 ) stored in the sorption store ( 1 ) is computed based on at least one measured temperature value and at least one measured pressure value.

First claim

1 .- 23 . (canceled)

24 . A process for indicating a fill level of a sorption store, wherein at least one gas adsorbent medium is disposed within at least one vessel and wherein a total amount (n total ) of a gas stored in the sorption store is computed based on at least one measured temperature value and at least one measured pressure value.

25 . The process according to claim 24 , wherein the total amount (n total ) of a gas stored in the sorption store is computed based on an empirical model defining the relation between the total amount of gas stored in the sorption store and the at least one measured temperature value and the at least one measured pressure value and wherein parameters of the empirical model are fitted to experimental data.

26 . The process according to claim 24 , comprising at least two steps, wherein an amount (n g ) of gas present in a gas phase is computed in a first step and an amount of gas adsorbed by the at least one gas adsorbent medium is computed in a second step and wherein the total amount (n total ) of gas stored in the sorption store is the sum of the amounts of gas calculated in the at least two steps.

27 . The process according to claim 26 , wherein the first step comprises a first model (I) describing an amount (n g ) of gas present in a gas phase in dependency of the at least one measured temperature value and the at least one measured pressure value.

28 . The process according to claim 27 , wherein the first model (I) comprises a thermodynamic equation of state based on the real gas behaviour of methane.

29 . The process according to claim 27 , wherein the first model (I) comprises a thermodynamic equation of state selected from the group consisting of the ideal gas law, the Van der Waals equation of state, the Redlich-Kwong equation of state, the Peng-Robinson equitation of state and modifications thereof.

30 . The process according to claim 26 , wherein the second step comprises a second model (II) describing an equilibrium adsorption capacity of the at least one gas adsorbent medium for the gas stored in the sorption store in dependency of at least the amount (n g ) of gas present in the gas phase and wherein the first step optionally comprises a third model (III) describing adsorption kinetics, said adsorption kinetics describing an adsorption rate in dependency of an adsorption capacity of the at least one gas adsorbent medium.

31 . The process according to claim 30 , wherein the second model (II) is based on an adsorption mechanism of micropore filling or based on an adsorption mechanism of a layering process.

32 . The process according to claim 30 , wherein the second model (II) comprises a Dubinin-Astakhov equation and/or a Langmuir equation.

33 . The process according to claim 24 , wherein the at least one gas adsorbent medium is a porous and/or microporous solid.

34 . The process according to claim 24 , wherein the at least one as adsorbent medium is present as a monolith or as a powder or as a bed of pellets and wherein the ratio of the permeability of the pellets to the smallest pellet diameter is between 1*e −11 m 2 /m and 1*e −16 m 2 /m.

35 . The process according to claim 24 , wherein the at least one gas adsorbent medium is selected from the group consisting of activated charcoals, zeolites, activated alumina, silica gels, open-pore polymer foams, metal-organic frameworks, and combinations thereof.

36 . The process according to claim 24 , wherein the stored gas contains hydrocarbons and/or water.

37 . The process according to claim 24 , wherein the stored gas contains gas selected from the group consisting of methane, ethane, butane, hydrogen, propane, propene, ethylene, water, methane, and combinations thereof.

38 . The process according to claim 24 , wherein the stored gas comprises methane as a main component.

39 . The process according to claim 24 , wherein the gas is stored under pressure in the range of 1 bar to 400 bar.

40 . A device for effectuating the process according to claim 24 .

41 . A sorption store comprising the device of claim 40 .

42 . The sorption store of claim 41 , wherein at least one temperature sensor measuring the at least one measured temperature value and at least one pressure sensor measuring the at least one measured pressure value are disposed in the at least one vessel and/or at the inlet of the sorption store and/or in a supply pipe to the sorption store.

43 . The sorption store of claim 42 , wherein the at least one temperature sensor is disposed in the vessel in a position characterized by a temperature from Which the average temperature of the interior of the sorption store is deducable.

44 . The sorption store of claim 42 , wherein the at least one temperature sensor is disposed in the vessel in a position, which is in case of a substantially horizontally mounted vessel located centrally with regard to a vertical extension of the vessel and centrally or further away from an inlet with regard to a horizontal extension of the vessel and which is in case of a substantially vertically mounted vessel located centrally with regard to the horizontal extension of the vessel and centrally with regard to the vertical extension of the vessel.

45 . A vehicle comprising the sorption store of claim 41 .

46 . A vehicle, comprising an engine control unit effectuating the process according to claim 24 . 47 , (New) The process according to claim 24 , wherein the at least one gas adsorbent medium is present as a monolith or as a powder or as a bed of pellets and wherein the ratio of the permeability of the pellets to the smallest pellet diameter is between 1*ê-12 m̂2/m and 1*ê-14 m̂2/m.

48 . The process according to claim 24 , wherein the stored gas contains natural gas.

49 . The process according to claim 24 , wherein the gas is stored under pressure in the range of 1 bar to 250 bar.

Assignees

• Basf Se

Inventors

• Weickert Matthias
• Marx Stefan
• Müller Ulrich
• Renze Peter

Classifications

• F17C11/007 Primary

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

• F17C2250/03

  Control means · CPC title

• F17C2250/043

  Pressure · CPC title

• F17C2250/032

  using computers · CPC title

• F17C2250/0439

  Temperature · CPC title