System and method to generate steam by mixing a feed water stream with a heating medium

Patent metadata

Field	Value
Publication number	US-10335708-B2
Application number	US-201615193813-A
Country	US
Kind code	B2
Filing date	Jun 27, 2016
Priority date	Jun 27, 2016
Publication date	Jul 2, 2019
Grant date	Jul 2, 2019

Abstract

A system and method to generate steam from a feed water stream does so in a liquid pool zone of a vessel as the stream comes into contact with a heating medium that is less volatile than the feed water stream. To keep the pool hot, the heating medium can be recirculated through a heater of a pump-around loop or a heater can be placed in the liquid pool. As the feed water stream is vaporized or partially vaporized, any solids or unvaporized water present in the feed water stream come out of the stream and move into the heating medium. These solids and the unvaporized water may be further removed from the heating medium in the pool or in the pump-around loop. The heat exchange surface does not contact the feed water to generate steam.

First claim

What is claimed:

1. A method to generate steam from a feed water stream, the method comprising:
routing the feed water stream into a liquid pool zone of a vessel, the liquid pool zone including a heating medium, the heating medium being less volatile than the feed water stream and maintained at an operating temperature determined by vaporization requirements;
pre-mixing the feed water stream and the heating medium outside of the liquid pool zone of the vessel;
vaporizing at least a portion of the feed water stream due to contact with the heating medium in the liquid pool zone;
removing a vaporized portion of the feed water stream from a vapor separation zone of the vessel as steam; and
removing solids from the liquid pool zone of the vessel.

2. A method according to claim 1 wherein during pre-mixing no vaporization of the water components of the feed water stream occurs.

3. A method according to claim 1 wherein during pre-mixing no more than about 90% of the volatile components of the process stream vaporize.

4. A method according to claim 1 further comprising separating and removing at least some of the solids from the vessel directly as blowdown containing the at least some of the solids.

5. A method according to claim 1 further comprising:
removing a portion of the heating medium residing in the liquid pool zone of the vessel;
raising a temperature of the removed portion to produce a heated recycle stream; and
routing the heated recycle stream back to the liquid pool zone.

6. A method according to claim 5 wherein the removed portion of the heating medium is a mixture of heating medium and at least some of the solids of the feed water stream.

7. A method according to claim 5 further comprising separating and removing at least some of the solids from the mixture prior to raising the temperature.

8. A method according to claim 1 wherein a density of the heating medium is greater than that of the feed water stream.

9. A method according to claim 1 wherein the feed water stream is not pre-treated prior to entering the liquid pool zone of the vessel.

10. A method according to claim 1 further comprising filtering the feed water stream by straining prior to the feed water stream entering the liquid pool zone of the vessel.

11. A system to generate steam from a feed water stream, the system comprising:
a vessel arranged to receive a feed water stream into a liquid pool zone of the vessel, the liquid pool zone including a heating medium less volatile than the feed stream and maintained at an operating temperature determined by vaporization requirements;
a mixer located outside of the liquid pool zone of the vessel and arranged to mix the feed water stream and the heating medium; and
a pump-around loop arranged to receive a portion of the heating medium residing in the liquid pool zone and return the portion back to the liquid pool zone;
wherein when the feed water stream is contacted by the heating medium in the liquid pool zone at least a portion of the water of the feed water stream vaporizes and migrates to a vapor separation zone of the vessel for removal and solids form in the liquid pool zone of the vessel for removal.

12. A system according to claim 11 wherein the mixer is arranged so no vaporization of the volatile components of the feed water stream occurs in the mixer.

13. A system according to claim 11 wherein the mixer is arranged so no more than about 90% of the volatile components of the feed water stream vaporize in the mixer.

14. A system according to claim 11 wherein the vessel includes internals arranged to separate at least some of the solids of the feed water stream from the heating medium.

15. A system according to claim 11 further comprising the pump-around loop including a heater.

16. A system according to claim 11 further comprising the pump-around loop including a separation device.

Assignees

• Cameron Solutions Inc

Inventors

• Zheng Z Frank
• King Christopher Stephen
• Nemmara Harihara V

Classifications

• F28D2021/0064

  Vaporizers, e.g. evaporators · CPC title

• F22B1/02

  by exploitation of the heat content of hot heat carriers · CPC title

• F28C3/04 Primary

  the heat-exchange media both being liquids · CPC title

• B01D1/28

  with vapour compression · CPC title

• C02F1/10

  by direct contact with a particulate solid or with a fluid, as a heat transfer medium · CPC title