Immersed plate heater separation system

Patent metadata

Field	Value
Publication number	US-11583786-B2
Application number	US-202016799630-A
Country	US
Kind code	B2
Filing date	Feb 24, 2020
Priority date	Jan 15, 2018
Publication date	Feb 21, 2023
Grant date	Feb 21, 2023

Abstract

A separation system includes an elongated separator vessel having an inlet, a heating section which is located downstream of the inlet, an oil accumulation section which is located downstream of the heating section, and an oil outlet which is connected to the oil accumulation section. The heating section includes an immersed plate heater which is fluidly connected to a heating medium heater that is located externally of the separator vessel. In operation, a heating fluid which is heated in the heating medium heater is circulated through the immersed plate heater to heat the multiphase fluid.

First claim

What is claimed is:

1. A separation system comprising:
an elongated separator vessel which includes an inlet for a multiphase fluid flowstream, an upstream section which is located downstream of the inlet, a heating section which is located downstream of the upstream section, an oil accumulation section which is located downstream of the heating section, and an oil outlet which is connected to the oil accumulation section;
an immersed plate heater which is positioned in the heating section; and
a heating medium heater which is located externally of the separator vessel and is fluidly connected to the immersed plate heater;
wherein a heating fluid which is heated in the heating medium heater is circulated through the immersed plate heater to heat the multiphase fluid;
wherein the immersed plate heater comprises an immersed plate heater bank comprising a plurality of generally rectangular, generally parallel, spaced apart heat exchanger plates;
wherein the heat exchanger plates are oriented generally vertically in the heating section generally parallel with a longitudinal axis of the separator vessel;
wherein the upstream section is located horizontally adjacent to the heating section and is separated from the heating section by at least one partially perforated baffle plate, the partially perforated baffle plate including a solid upper portion and a perforated lower portion which comprises a plurality of through holes; and
wherein a first vertical distance from a bottom of the separator vessel to a top of the immersed plate heater is greater than a second vertical distance from the bottom of the separator vessel to a top of the perforated lower portion of the partially perforated baffle plate;
whereby the multiphase fluid flowstream from the upstream section is directed by the partially perforated baffle plate both horizontally and vertically through the immersed plate heater.

2. The separation system of claim 1 , wherein the heating medium heater comprises a thermal fluid system.

3. The separation system of claim 1 , wherein the separator vessel includes a separation section which is located downstream of the heating section and upstream of the oil accumulation section and a water outlet which is connected to the separation section, and wherein the separation section is separated from the oil accumulation section by an overflow weir.

4. The separation system of claim 3 , wherein the heating section is separated from the separation section by at least one fully perforated baffle plate.

5. The separation system of claim 3 , further comprising a plate pack coalescer which is positioned in the separation section.

6. The separation system of claim 1 , further comprising an inlet device which is positioned between the inlet and the upstream section.

7. The separation system of claim 6 , further comprising a run- off plate which extends from the inlet device to the upstream section.

8. The separation system of claim 7 , wherein the run-off plate is connected to the partially perforated baffle plate.

9. The separation system of claim 1 , wherein the solid upper portion extends vertically from a top edge of the partially perforated baffle plate to approximately a middle of the partially perforated baffle plate.

10. The separation system of claim 1 , wherein the heating medium heater is configured to maintain the temperature of the multiphase fluid in the heating section above the predetermined temperature by increasing at least one of the flow rate and the temperature of the heating fluid in the immersed plate heater.

11. A method for treating a hydrocarbon flowstream, the method comprising:
directing the hydrocarbon flowstream into an elongated separator vessel which includes at least an inlet for a multiphase fluid flowstream, an upstream section which is located downstream of the inlet, a heating section which is located downstream of the upstream section, a separation section which is located downstream of the heating section, an oil accumulation section which is located downstream of the separation section, and an oil outlet which is connected to the oil accumulation section;
directing at least a portion of the hydrocarbon flowstream into the heating section; and
heating said portion of the hydrocarbon flowstream with an immersed plate heater which is positioned in the heating section and is fluidly connected to a heating medium heater which is located externally of the separator vessel;
wherein the immersed plate heater comprises an immersed plate heater bank comprising a plurality of generally rectangular, generally parallel spaced apart heat exchanger plates;
wherein the heat exchanger plates are oriented generally vertically in the heating section generally parallel with a longitudinal axis of the separator vessel;
wherein the upstream section is located horizontally adjacent to the heating section and is separated from the heating section by at least one partially perforated baffle plate, the partially perforated baffle plate including a solid upper portion and perforated lower portion which comprises a plurality of through holes; and
wherein a first vertical distance from a bottom of the separator vessel to a top of the immersed plate heater is greater than a second vertical distance from the bottom of the separator vessel to a top of the perforated lower portion of the partially perforated baffle plate;
whereby the multiphase fluid flow stream from the upstream section is directed by the partially perforated baffle plate both horizontally and vertically through the immersed plate heater.

12. The method of claim 11 , wherein the heating medium heater comprises a thermal fluid system.

13. The method of claim 11 , wherein said portion of the hydrocarbon flowstream includes at least a water fraction and an oil fraction, said oil fraction comprises a number of light end hydrocarbons, and the method further comprises:
directing said portion of the hydrocarbon flowstream from the heating section into the separation section;
wherein the water fraction and/or the light end hydrocarbons separate from the oil fraction in the separation section.

14. The method of claim 13 , wherein the method further comprises:
directing the oil fraction from the separation section into the oil accumulation section.

15. A separation system comprising:
an elongated separator vessel which includes:
an inlet for a multiphase fluid flowstream;
an upstream section which is located downstream of the inlet;
a heating section which is located downstream of and horizontally adjacent to the upstream section;
a separation section which is located downstream of and horizontally adjacent to the heating section;
an oil accumulation section which is located downstream of and horizontally adjacent to the separation section, the oil accumulation section being separated from the separation section by an overflow weir; and
an oil outlet which is connected to the oil accumulation section;

an immersed plate heater which is positioned in the heating section; and
a heating medium heater which is located externally of the separator vessel and is fluidly connected to the immersed plate heater;
wherein a heating fluid which is heated in the heating medium heater is circulated through the immersed plate heater to heat the multiphase fluid;
wherein the immersed plate heater comprises an immersed plate heater bank comprising a plurality of generally rectangular, generally parallel, spaced apart heat exchanger plates;
wherein the heat exchanger plates are oriented generally vertically in the heating section generally parallel with a lon

Assignees

• Fmc Tech Inc

Inventors

• Van Asperen Victor
• Baaren Sander G
• Balk Wouter

Classifications

• E21B43/34

  Arrangements for separating materials produced by the well · CPC title

• B01D17/045

  with coalescers · CPC title

• C02F2101/32

  Hydrocarbons, e.g. oil · CPC title

• B01D19/0409

  compounds containing Si-atoms · CPC title

• C02F2103/365

  from petrochemical industry (e.g. refineries) · CPC title