Volatile content measurement in process streams such as froth treatment tailings

Patent metadata

Field	Value
Publication number	US-11725147-B2
Application number	US-202117559940-A
Country	US
Kind code	B2
Filing date	Dec 22, 2021
Priority date	Dec 22, 2020
Publication date	Aug 15, 2023
Grant date	Aug 15, 2023

Abstract

Methods, processes and devices are described for measuring a volatile content of a process stream that comprises volatile species, such as light hydrocarbons and/or H2S. The method can include introducing a stripping gas into a sample of the process stream to strip the volatiles therefrom and produce a gas phase comprising vaporized volatiles; detecting the vaporized volatiles in the gas phase to obtain a sample volatile content; and determining the volatile content of the process stream based on the sample volatile content. The method and device can be used to measure a light hydrocarbon content of froth treatment tailings in the context of removing such light hydrocarbons prior to flocculating and dewatering the tailings.

First claim

The invention claimed is:

1. A method for measuring a volatile content of a process stream comprising volatiles, the method comprising:
receiving a sample of the process stream into a sample chamber having a chamber volume;
introducing a stripping gas into the sample of the process stream to strip the volatiles therefrom and produce a gas phase comprising vaporized volatiles;
detecting the vaporized volatiles in the gas phase to obtain a sample volatile content; and
determining the volatile content of the process stream based on the sample volatile content.

2. The method of claim 1 , wherein introducing the stripping gas into the sample of the process stream comprises sparging the stripping gas into the sample.

3. The method of claim 1 , wherein receiving the sample of the process stream into the sample chamber comprises flowing the process stream through the sample chamber until a predetermined timepoint is reached, and retaining the sample of the process stream into the sample chamber.

4. The method of claim 1 , wherein the volatiles comprise light hydrocarbons.

5. The method of claim 4 , wherein the light hydrocarbons comprise naphtha, toluene, light aromatic compounds, C3 to C7 aliphatic compounds, natural gas condensate, or a combination thereof.

6. The method of claim 1 , wherein detecting the vaporized volatiles in the gas phase to obtain the sample volatile content comprises measuring the sample volatile content via photoionization.

7. The method of claim 1 , wherein the volatiles comprise H 2 S, and detecting the vaporized volatiles in the gas phase to obtain the sample volatile content comprises measuring the sample volatile content via a H 2 S sensor.

8. The method of claim 1 , further comprising heating the sample of the process stream prior to detecting the vaporized volatiles in the gas phase, to accelerate the stripping of the volatiles therefrom.

9. The method of claim 1 , wherein the process stream comprises a wastewater stream.

10. The method of claim 9 , wherein the wastewater stream comprises refinery wastewater.

11. The method of claim 1 , wherein the process stream comprises a process stream derived from refinery operations.

12. A process for producing a hydrocarbon product, comprising:
treating a feedstock to produce the hydrocarbon product and an associated process stream;
measuring a volatile content of the associated process stream, comprising:
supplying a sample of the associated process stream to a sample chamber having a chamber volume, the sample chamber being configurable to be in fluid communication with the associated process stream;
introducing a stripping gas from a stripping gas supply into the sample of the associated process stream to strip the volatiles therefrom and produce a gas phase comprising vaporized volatiles, the gas phase being receivable in a detection zone in fluid communication with the sample chamber, the detection zone being further configurable to be in fluid communication with the stripping gas supply;
detecting the vaporized volatiles in the gas phase received in the detection zone to obtain a sample volatile content; and
determining the volatile content of the associated process stream based on the sample volatile content.

13. The process of claim 12 , further comprising measuring the volatile content of the hydrocarbon product.

14. The process of claim 13 , wherein treating the feedstock comprises refining and the hydrocarbon product comprises a refinery-derived product.

15. The process of claim 13 , further comprising adjusting the treating of the feedstock based on the volatile content of the hydrocarbon product or of the associated process stream.

16. The process of claim 12 , wherein the associated process stream comprises a wastewater stream.

17. The process of claim 16 , wherein the wastewater stream comprises refinery wastewater and the hydrocarbon product comprises a refinery-derived product.

18. The process of claim 12 , wherein the associated process stream comprises froth treatment tailings, the hydrocarbon product comprises diluted bitumen, and the feedstock comprises oil sands material.

19. The process of claim 13 , wherein the volatiles comprise light hydrocarbons.

20. A device for measuring a volatile content of a process stream comprising volatiles, the device comprising:
a sample chamber having a chamber volume, the sample chamber being configured for receiving a sample of the process stream;
a stripping gas supply for introducing a stripping gas into the sample of the process stream to strip the volatiles therefrom and produce a gas phase comprising vaporized volatiles, the sample chamber being configured to be alternately in fluid communication with the process stream or with the stripping gas supply;
a detection zone in fluid communication with the sample chamber to receive the gas phase comprising the vaporized volatiles; and
a detection device extending within the detection zone to measure a sample volatile content of the sample that is convertible to the volatile content of the process stream.

21. The device of claim 20 , wherein the device is installable on-line to a pipeline through which the process stream flows, to provide live monitoring of the volatile content of the process stream.

22. The device of claim 20 , further comprising a sparger downstream of the stripping gas supply to introduce bubbles of the stripping gas into the sample.

23. The device of claim 20 , further comprising a heater operatively connected to the sample chamber and configured to heat the sample to accelerate the stripping of the volatiles therefrom prior to detecting the vaporized volatiles in the gas phase.

24. The device of claim 20 , wherein the detection device comprises a photoionization system configured to measure the volatile content when the volatiles comprise light hydrocarbons.

Assignees

• Suncor Energy Inc

Inventors

• Derakhshandeh Babak
• Hollander Elco
• Laborde-Boutet Cedric
• Brown Wayne
• Mccaffrey William

Classifications

• C10G1/008 Primary

  Controlling or regulating of liquefaction processes · CPC title

• G01N27/64

  using wave or particle radiation to ionise a gas, e.g. in an ionisation chamber · CPC title

• G01N33/18

  Water · CPC title