System and method to vaporize a process stream by mixing the stream with a heating medium

Patent metadata

Field	Value
Publication number	US-10478745-B2
Application number	US-201615193723-A
Country	US
Kind code	B2
Filing date	Jun 27, 2016
Priority date	Jun 27, 2016
Publication date	Nov 19, 2019
Grant date	Nov 19, 2019

Abstract

A system and method to vaporize a process or 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 process 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 process stream is vaporized, any solids present in the process stream come out of the process stream and move into the heating medium. These solids may be further removed from the heating medium in the pool or in the pump-around loop. The vaporized process stream can be further condensed. Any heat recovered can be used to pre-heat the process stream or used in the pump around loop's heater in case of mechanical vapor recovery.

First claim

What is claimed:

1. A method to vaporize a process stream, the method comprising:
routing the process 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 process stream and maintained at an operating temperature determined by vaporization requirements;
pre-mixing the process stream and the heating medium outside of the liquid pool zone of the vessel;
vaporizing volatile components of the process stream due to contact with the heating medium in the liquid pool zone;
removing a vaporized portion of the process stream from a vapor separation zone of the vessel as a vaporized process stream; 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 volatile components of the process 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 solids of the process stream.

7. A method according to claim 6 further comprising separating and removing at least some of the solids prior to raising the temperature.

8. A method according to claim 1 further comprising condensing at least a portion of the vaporized process stream.

9. A method according to claim 1 further comprising compressing at least a portion of the vaporized process stream.

10. A method according to claim 1 further comprising raising a temperature of at least a portion of the process stream prior to the process stream directly entering the liquid pool zone of the vessel.

11. A method according to claim 1 wherein the process stream is homogenously dispersed in the heating medium.

12. A method according to claim 1 wherein a density of the heating medium is greater than that of the process stream.

13. A method according to claim 1 wherein the process stream includes water.

14. A system to vaporize a process stream, the system comprising:
a vessel arranged to contact the process stream and route the process stream into a liquid pool zone of the vessel, the liquid pool zone including a heating medium less volatile than the process 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 process stream and the portion of the heating medium being returned to the vessel; 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 process stream is contacted by the heating medium in the liquid pool zone volatile components of the process stream vaporize and migrate to a vapor separation zone of the vessel for removal and solids form in the liquid pool zone of the vessel for removal.

15. A system according to claim 14 wherein the mixer is arranged so no vaporization of the volatile components of the process stream occurs in the mixer.

16. A system according to claim 14 wherein the mixer is arranged so no more than about 90% of the volatile components of the process stream vaporize in the mixer.

17. A system according to claim 14 wherein the vessel includes internals arranged to separate at least a portion of nonvolatile components of the process stream from the heating medium.

18. A system according to claim 14 further comprising the pump-around loop including a heater.

19. A system according to claim 14 further comprising the pump-around loop including a separation device.

20. A system according to claim 14 further comprising a condenser arranged to receive at least a portion of a vaporized process stream exiting the vapor separation zone of the vessel.

21. A system according to claim 14 further comprising a compressor arranged to receive at least a portion of a vaporized process stream exiting the vapor separation zone of the vessel and produce a pressurized vaporized process stream.

22. A system according to claim 14 further comprising a pre-heater arranged to raise a temperature of the process stream prior to the process stream entering the liquid pool zone of the vessel.

23. A system according to claim 22 wherein the pre-heater is arranged to recover heat from a condenser arranged to receive at least a portion of the vaporized process stream.

Assignees

• Cameron Solutions Inc

Inventors

• Zheng Z Frank
• King Christopher Stephen
• Nemmara Harihara V
• Messenger Brian Edward

Classifications

• B01D1/28

  with vapour compression · CPC title

• B01D1/0041 Primary

  Use of fluids · CPC title

• B01D5/006

  with evaporation or distillation · CPC title

• B01D1/0052

  Use of a liquid transfer medium or intermediate fluid, e.g. bain-marie · CPC title

• B01D1/0064

  Feeding of liquid into an evaporator · CPC title