Indirect boiling for water treatment
US-2015096754-A1 · Apr 9, 2015 · US
US10464826B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10464826-B2 |
| Application number | US-201615244110-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 23, 2016 |
| Priority date | Aug 26, 2015 |
| Publication date | Nov 5, 2019 |
| Grant date | Nov 5, 2019 |
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Systems and methods utilize heated waste flue gas to treat water. The heated waste flue gas, which may come from a steam generator, bubbles through untreated water to vaporize the untreated water and separate out solids and other contaminants before subsequent condensing. The steam generator may receive resulting treated water to produce steam for injection.
Opening claim text (preview).
The invention claimed is: 1. A method of generating steam for enhanced oil recovery techniques, comprising: a) admitting a batch of untreated water into a contacting vessel, wherein said contacting vessel has a bubble cap tray and a demister; b) bubbling heated waste flue gas from a steam generator through said bubble cap tray and through the batch of untreated water; c) vaporizing the batch of untreated water with the heated waste flue gas to create intermediate steam; d) condensing the intermediate steam mixed with the heated waste flue gas in a condenser to form a gas stream and a treated water stream; e) heating the treated water stream in the steam generator to produce injection steam for enhanced oil recovery and the heated waste flue gas that is bubbled through the batch of untreated water in step b); and f) removing sediments from the contacting vessel; wherein two contacting vessels are operated sequentially, such that one can be in use while the other is being cleaned in step f). 2. The method of claim 1 , wherein the heated waste flue gas has a temperature between 170° C. and 240° C. 3. The method of claim 1 , wherein the steam generator is a once-through steam generator. 4. The method of claim 1 , wherein the enhanced oil recovery technique comprises steam assisted gravity drainage. 5. The method of claim 1 , wherein the untreated water is at least one of feedwater, brackish water and produced water. 6. The method of claim 1 , wherein the untreated water is produced water. 7. A method of treating produced water using waste flue gas comprising: admitting a batch of untreated produced water into a contacting vessel wherein the contacting vessel has a bubble cap tray through which the heated waste flue gas is passed and a demister; bubbling heated waste flue gas from a steam generator through said bubble cap tray and through the batch of untreated produced water; vaporizing the batch of untreated produced water with the heated waste flue gas to create steam; removing solids from the steam with said demister; condensing the steam in a condenser to form a gas stream and a treated water stream; and separating the gas stream and the treated water stream; wherein two contacting vessels are operated sequentially, such that one can be in use while the other is being cleaned of solids in said demister and said contacting vessel. 8. The method of claim 7 , wherein the heated flue gas has a temperature between 170° C. and 240° C. 9. The method of claim 7 , wherein the heated flue gas is generated by a once-through steam generator. 10. The method of claim 7 , wherein all of the steam from the contacting vessel is condensed to form the treated water.
Use of waste energy from other processes or sources, e.g. combustion gas (for water treatment C02F1/16) · CPC title
using waste heat from other processes · CPC title
with heated gases or vapours {or liquids} in contact with the liquid · CPC title
Demister (vapour-liquid separation) · CPC title
Bubble caps · CPC title
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