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

Patent metadata

Field	Value
Publication number	US-10864456-B2
Application number	US-201916413828-A
Country	US
Kind code	B2
Filing date	May 16, 2019
Priority date	Jun 27, 2016
Publication date	Dec 15, 2020
Grant date	Dec 15, 2020

Abstract

A system and method to partially 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 partially vaporized, any solids present in the process stream together with the unvaporized process or feed water stream move into the heating medium. These solids and unvaporized liquids 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 in the pump-around loop's heater in case of mechanical vapor recovery.

First claim

What is claimed:

1. A method to partially vaporize a process stream, the method comprising:
routing the process stream into a liquid zone of a vessel, the liquid zone including a heating medium that is less volatile than the process stream, immiscible with the process stream, and maintained at a vaporization operating temperature;
providing a mixture of the process stream and a portion of the heating medium to the liquid zone of the vessel;
partially vaporizing volatile components of the process stream by thermal exchange with the heating medium in the liquid zone;
removing a vaporized portion of the process stream from a vapor zone of the vessel;
moving solids from the process stream to the heating medium in the liquid zone; and
removing solids from the heating medium.

2. A method according to claim 1 wherein providing the mixture of the process stream and the portion of the heating medium to the liquid zone of the vessel comprises mixing the process stream and the portion of the heating medium wherein no vaporization of the volatile components of the process stream occurs.

3. A method according to claim 1 wherein providing the mixture of the process stream and the portion of the heating medium to the liquid zone of the vessel comprises mixing the process stream and the portion of the heating medium wherein 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 heating medium 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;
raising a temperature of the removed portion to produce a heated recycle stream; and
routing the heated recycle stream back to the liquid 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 process stream.

7. A method according to claim 6 further comprising separating and removing at least some of the solids from the removed portion 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 zone of the vessel.

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

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

13. A system to partially vaporize a process stream, the system comprising:
a vessel arranged to receive the process stream into a liquid zone of the vessel, the liquid zone comprising a heating medium less volatile than the process stream, immiscible with the process stream, and maintained at a vaporization operating temperature;
a pre-mixer fluidly coupled to the liquid zone of the vessel and arranged to mix the process stream and a portion of the heating medium remote from the liquid zone; and
a pump-around loop arranged to remove a portion of the heating medium from the liquid zone and return the portion back to the liquid zone; a separation device disposed within said pump-around loop;
wherein volatile components of the process stream partially vaporize by thermal exchange with the heating medium and migrate to a vapor zone of the vessel for removal, and solids move from the process stream and collect in the heating medium.

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

15. A system according to claim 13 wherein the vessel includes internals arranged to separate at least some of an unvaporized portion of the process stream from the heating medium.

16. A system according to claim 13 wherein the pump-around loop includes a heater.

17. A system according to claim 13 further comprising a condenser arranged to receive at least a portion of a vaporized process stream exiting the vapor zone of the vessel.

18. A system according to claim 13 further comprising a compressor arranged to receive at least a portion of a vaporized process stream exiting the vapor zone of the vessel and produce a pressurized vaporized process stream.

Assignees

• Cameron Solutions Inc

Inventors

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

Classifications

• B01D1/0052

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

• B01D1/2856

  The compressed vapour is used for heating a reboiler or a heat exchanger outside an evaporator · CPC title

• Y02P20/10

  Process efficiency · CPC title

• C02F2103/08

  Seawater, e.g. for desalination · CPC title

• B01D1/0094 Primary

  with forced circulation · CPC title