Fuel conditioning system and method configured to supply an aircraft turbine engine with fuel from a cryogenic tank
US-12162621-B2 · Dec 10, 2024 · US
US9599283B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9599283-B2 |
| Application number | US-201314440287-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 25, 2013 |
| Priority date | Nov 2, 2012 |
| Publication date | Mar 21, 2017 |
| Grant date | Mar 21, 2017 |
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A system for storage and dosing of ammonia includes solid ammonia storage material capable of binding and releasing ammonia reversibly by adsorption/absorption. The system includes a start-up storage unit and a main storage unit, both of which hold ammonia storage material. A start-up heating device is arranged to heat the start-up storage unit to generate gaseous ammonia by thermal desorption from the solid storage material. A main heating device arranged to heat the main storage unit to generate gaseous ammonia by thermal desorption from the solid storage material. A controller modulates operation of the heating devices such that the main and start-up heating devices are not simultaneously activated.
Opening claim text (preview).
The invention claimed is: 1. A system for storage and dosing of ammonia that comprises a solid ammonia storage material capable of binding and releasing ammonia reversibly by adsorption/absorption, the system comprising: a start-up storage unit and a main storage unit, the storage units holding ammonia storage material; a start-up heating device arranged to heat the start-up storage unit to generate gaseous ammonia by thermal desorption from the solid storage material; a main heating device arranged to heat the main storage unit to generate gaseous ammonia by thermal desorption from the solid storage material; a controller configured to monitor and control operation of the main and start-up heating devices, wherein the controller modulates operation of the heating devices such that the main and start-up heating devices are not simultaneously activated; by a) activating the start-up heating unit until the pressure in the start-up storage unit reaches a first pressure threshold; b) thereafter deactivating the start-up heater and activating the main heating unit until either the pressure in the start-up storage unit falls below a second pressure threshold or the pressure in the main storage unit reaches a third pressure threshold; c) if the pressure in the start-up storage unit falls below the second pressure threshold before the pressure in the main storage unit reaches the third pressure threshold, then repeating steps a and b until the pressure in the main storage unit reaches a third pressure threshold; and d) once the pressure in the main storage unit reaches the third pressure threshold, deactivating the start-up heating unit and control the main heating unit to maintain the pressure in the main storage unit between the third pressure threshold and a fourth pressure threshold. 2. The system of claim 1 , further comprising a dosing valve arranged to control ammonia flow from the storage units, and wherein the controller is configured to control operation of the dosing valve according to a demand. 3. The system of claim 1 , further comprising at least one one-way valve interconnecting the main storage unit with the start-up storage unit, the one-way valve preventing any back-flow of ammonia from the start-up storage unit to the main storage unit. 4. A system for storage and dosing of ammonia that comprises a solid ammonia storage material capable of binding and releasing ammonia reversibly by adsorption/absorption, the system comprising: a start-up storage unit and a main storage unit, the storage units holding ammonia storage material; a start-up heating device arranged to heat the start-up storage unit to generate gaseous ammonia by thermal desorption from the solid storage material; a main heating device arranged to heat the main storage unit to generate gaseous ammonia by thermal desorption from the solid storage material; a controller configured to monitor the pressure in the storage units and control operation of the main and start-up heating devices, the controller being configured to a) activate the start-up heating unit until the pressure in the start-up storage unit reaches a first pressure threshold; b) thereafter deactivate the start-up heater and activate the main heating unit until either the pressure in the start-up storage unit falls below a second pressure threshold or the pressure in the main storage unit reaches a third pressure threshold; c) if the pressure in the start-up storage unit falls below the second pressure threshold before the pressure in the main storage unit reaches the third pressure threshold, then repeat steps a and b until the pressure in the main storage unit reaches a third pressure threshold; and d) once the pressure in the main storage unit reaches the third pressure threshold, deactivate the start-up heating unit and control the main heating unit to maintain the pressure in the main storage unit between the third pressure threshold and a fourth pressure threshold. 5. A method for storing and dosing of ammonia from a solid ammonia storage material capable of binding and releasing ammonia reversibly by adsorption/absorption, the method comprising: a) providing a main storage unit and a start-up storage unit, the storage units holding ammonia storage material; b) heating the start-up storage unit until the pressure in the start-up storage unit reaches a first pressure threshold; c) thereafter heating the main storage unit while simultaneously not heating the start-up storage unit until either the pressure in the start-up storage unit falls below a second pressure threshold or the pressure in the main storage unit reaches a third pressure threshold; d) if the pressure in the start-up storage unit falls below the second pressure threshold before the pressure in the main storage unit reaches the third pressure threshold, then repeating steps b and c until the pressure in the main storage unit reaches a third pressure threshold; and e) once the pressure in the main storage unit reaches the third pressure threshold, controlling heating of the main storage unit to maintain the pressure in the main storage unit between the third pressure threshold and a fourth pressure threshold which is lower than the third threshold.
the substance being in the gaseous form · CPC title
Pressure · CPC title
Control thereof · CPC title
with change of state, e.g. vaporisation · CPC title
Use of gas-solvents or gas-sorbents in vessels {(absorbing compositions for acetylene C10L3/04; absorbing compositions for hydrogen C01B3/0005)} · CPC title
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