Heat engine
US-2024200474-A1 · Jun 20, 2024 · US
US12494697B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12494697-B2 |
| Application number | US-202218289474-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 9, 2022 |
| Priority date | May 6, 2021 |
| Publication date | Dec 9, 2025 |
| Grant date | Dec 9, 2025 |
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An energy storage and retrieval system including an air chamber, a first air compressor operating with Heat Transfer Liquid (HTL-compressor) connected to the air chamber, a second turbine, operating with Heat Transfer Liquid (HTL-turbine) connected to the air chamber, accepting compressed air from the air chamber and producing work. Related apparatus and methods are also described.
Opening claim text (preview).
What is claimed is: 1 . A method for converting waste heat of exhaust gas to work while reducing CO 2 emission in the waste heat, comprising: feeding into a direct contact heat exchanger an exhaust gas that comprises CO 2 and a heat transfer liquid (HTL) that comprises molten salt, thereby resulting in mixing the HTL with the exhaust gas and heating of the HTL to obtain heated HTL; wherein the HTL comprises a CO 2 -capturing material to absorb the CO 2 from the exhaust gas, and said mixing resulting in the CO 2 -capturing material capturing the CO 2 from the exhaust gas, thereby reducing an amount of CO 2 in the exhaust gas; operating an HTL-turbine for performing an isothermal or quasi-isothermal expansion with the heated HTL following said mixing; and producing work using the HTL-turbine. 2 . The method of claim 1 , wherein the HTL exits the heat exchanger at a temperature of about the entrance temperature of the exhaust gas, while the exhaust gas exits the heat exchanger at a temperature about the entering temperature of the HTL. 3 . The method of claim 1 , wherein said CO 2 capturing material solidifies upon absorbing CO 2 , and the method further comprising removing the CO 2 capturing material which has absorbed CO 2 from the exhaust gas before reaching the HTL-turbine. 4 . The method according to claim 1 wherein the CO 2 -capturing material comprises a material selected from a group consisting of: CaO; MgO; NaCO 3 (+H 2 O); NaCO 3 ; KCO 3 (+H 2 O); KCO 3 ; and Na 2 O. 5 . The method according to claim 1 , wherein producing work comprises producing electricity. 6 . The method according to claim 1 , wherein CO 2 capturing material which has absorbed CO 2 from the exhaust gas is removed before reaching the HTL-turbine. 7 . The method according to claim 1 , wherein the molten salt is in a molten state in a temperature range of between 140° C.-530° C. 8 . The method according to claim 1 , wherein said heating comprises heating the HTL that comprises molten salt to a temperature above 670K, using a direct heat exchanger and waste heat of exhaust gas. 9 . The method according to claim 1 , wherein interaction of the CO 2 capturing material with the CO 2 produces a new material which is removable from the HTL; wherein the method further comprising removing the new material from the HTL. 10 . A method for converting waste heat of exhaust gas to work while reducing CO 2 emission in the waste heat, comprising: feeding into a direct contact heat exchanger an exhaust gas that comprises CO 2 and a heat transfer liquid (HTL) that comprises molten salt thereby resulting in mixing the HTL with the exhaust gas and heating of the HTL to obtain heated HTL; wherein the HTL comprises a CO 2 capturing material, to absorb CO 2 from the exhaust gas, and said mixing resulting in the CO 2 -capturing material capturing the CO 2 from the exhaust gas, thereby reducing an amount of CO 2 in the exhaust gas; operating an HTL-turbine for performing an isothermal or quasi-isothermal expansion with the heated HTL following said mixing; and producing work using the HTL-turbine; wherein interaction of the CO 2 capturing material with the CO 2 produces a new material which is removable from the HTL; wherein the method further comprises removing the new material from the HTL. 11 . A method for converting waste heat of exhaust gas to work while reducing CO 2 emission in the waste heat, comprising: feeding into a direct contact heat exchanger an exhaust gas that comprises CO 2 and a heat transfer liquid (HTL) that comprises molten salt, thereby resulting in mixing the HTL with the exhaust gas and heating of the HTL to obtain heated HTL; wherein the HTL comprises a CO 2 capturing material to absorb CO 2 from the exhaust gas, and said mixing resulting in the CO 2 -capturing material capturing the CO 2 from the exhaust gas, thereby reducing an amount of CO 2 in the exhaust gas; operating an HTL-turbine for performing an isothermal or quasi-isothermal expansion with the heated HTL following said mixing; and producing work using the HTL-turbine; wherein said CO 2 capturing material solidifies upon absorbing CO 2 , and the method further comprising removing the CO 2 capturing material which has absorbed CO 2 from the exhaust gas before reaching the HTL-turbine.
using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants (using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10) · CPC title
Engine exhaust gases · CPC title
Carbon dioxide · CPC title
Carbonates · CPC title
Oxides · CPC title
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