Furnace with integrated heat recovery utilizing radiative recuperator for preheating combustion reactants using heat from flue gas
US-2019003706-A1 · Jan 3, 2019 · US
US11940228B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11940228-B2 |
| Application number | US-202117555032-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2021 |
| Priority date | Dec 30, 2020 |
| Publication date | Mar 26, 2024 |
| Grant date | Mar 26, 2024 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention discloses a high-temperature fluid transporting pipeline with a heat exchange apparatus installed therein, a suitable heat exchange apparatus and a heat exchange method, wherein heat contained in a high-temperature fluid can be recovered during the transportation thereof. The heat exchange apparatus comprises a heat exchange body inserted into the high-temperature fluid transporting pipeline, and a heat-receiving fluid coil installed therein. The method of heat exchange is that the high-temperature fluid heats an auxiliary fluid in a heat exchange cavity via a heat exchange panel of the heat exchange body in contact therewith, and the heated auxiliary fluid then conducts the heat to a heat-receiving fluid in the heat-receiving fluid coil. As an example, the high-temperature fluid is flue gas generated by combustion, the heat exchange apparatus of the present invention is inserted into a flue gas transporting pipeline, the auxiliary fluid is an inert gas such as air, and the air heated indirectly by the high-temperature flue gas conducts heat to fuel and/or oxygen-enriched gas (serving as an oxidant/combustion aid) flowing in the heat-receiving fluid coil.
Opening claim text (preview).
What is claimed is: 1. A method for using a high-temperature fluid in a transporting pipeline to heat a heat-receiving fluid, comprising: a) providing a heat exchange apparatus, the heat exchange apparatus comprising a heat exchange body located completely within the transporting pipeline, and a heat-receiving fluid inlet pipeline, a heat-receiving fluid outlet pipeline, an auxiliary fluid inlet pipeline and an auxiliary fluid outlet pipeline, which all extend out of a casing of the transporting pipeline; the heat exchange body comprises a heat exchange cavity enclosed by a heat exchange panel, and a heat-receiving fluid coil is installed in the heat exchange cavity; wherein an installation hole is provided in the casing of the transporting pipeline, the heat exchange body of the heat exchange apparatus is inserted into the interior of the transporting pipeline through the installation hole, a gap between the heat exchange apparatus and the installation hole is sealed using a sealing refractory material, and a supporting structure is further included outside the transporting pipeline for the purpose of supporting the heat exchange apparatus, and b) providing a heat-receiving fluid and an auxiliary fluid, wherein the heat-receiving fluid flows in the heat-receiving fluid coil, the auxiliary fluid flows or is stationary in the heat exchange cavity, and the heat-receiving fluid is heated by the high-temperature fluid through heat conduction by the auxiliary fluid and heat radiation by the heat exchange panel. 2. The method according to claim 1 , wherein the high-temperature fluid comprises flue gas generated by combustion and/or thermal cracking. 3. The method according to claim 1 , wherein the auxiliary fluid comprises one of air, N 2 and CO 2 or a combination of more than one thereof, and the heat-receiving fluid comprises O 2 , natural gas or other fuel gases. 4. The method according to claim 2 , wherein the temperature range of the flue gas is 500-1200° C., and the temperature range of the heat-receiving fluid is 300-600° C. 5. The method according to claim 1 , wherein the range of flow rate of the heat-receiving fluid is 5-100 m/s and the range of flow rate of the auxiliary fluid is 0-50 m/s.
Arrangements for using waste heat · CPC title
the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration · CPC title
Mechanical Engineering · mapped topic
the heat being recuperated from waste air or from vapors (for air conditioning F24F12/001) · CPC title
for thermal power plants or industrial processes · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.