Low pressure drop advanced swirl technology gas filter

Patent metadata

Field	Value
Publication number	US-10537839-B1
Application number	US-201715825852-A
Country	US
Kind code	B1
Filing date	Nov 29, 2017
Priority date	Nov 29, 2017
Publication date	Jan 21, 2020
Grant date	Jan 21, 2020

Abstract

A media-free filter device for a supercritical fluid process is disclosed. The media-free filter device includes a first pipe section connected in flow communication with a closed-loop system for a supercritical fluid. A y-pipe segment intersects the first pipe section at an intersection joint. The intersection joint intersects at a descending obtuse angle with respect to the first pipe section flow direction. The y-pipe segment is open at the intersection joint and closed opposite the intersection joint, in flow communication with the first pipe section. The y-pipe section induces an eddy current turbulence zone adjacent the intersection joint to remove substantially all contaminants suspended in the supercritical fluid; and the contaminants are deposited in the descending y-pipe segment. An SCO2 process incorporating the media-free filter device is also disclosed.

First claim

What is claimed is:

1. A media-free filter device for a supercritical fluid process comprising:
a first pipe section connected in flow communication with a closed-loop, supercritical fluid system;
a y-pipe segment intersecting the first pipe section at an intersection joint; the intersection joint at a descending obtuse angle with respect to the first pipe section flow direction;
the y-pipe segment open at the intersection joint and closed opposite the intersection joint, in flow communication with the first pipe section;
wherein the y-pipe section inducing an eddy current turbulence zone adjacent the intersection joint to remove substantially all contaminants suspended in the supercritical fluid; and wherein the contaminants are deposited in the descending y-pipe segment.

2. The device of claim 1 , wherein the flow of supercritical fluid acts in a vortex shedding by generating a swirling eddy of the fluid adjacent the intersection joint.

3. The device of claim 1 , wherein the contaminants removed from the supercritical fluid having a density greater than the supercritical fluid are trapped in the eddy current and deposited in the y-pipe segment.

4. The device of claim 1 , wherein the eddy current being generated by contact with an angular edge formed at the intersection joint of the descending y-pipe segment in flow communication with the first pipe section.

5. The device of claim 1 , wherein the supercritical fluid comprises a supercritical carbon dioxide (SCO2) fluid having a density of about 120 kg/m 3 , a dynamic viscosity of about 5.5×10 −5 kg/m-s, a temperature of about 1,000° F., and a pressure of about 1.75×107 Pa flowing through the closed loop in the first pipe section.

6. The device of claim 1 , wherein the first pipe section comprises a 3-inch schedule 160 pipe having an inside diameter of 0.0667 m, and supercritical fluid corresponds with a mass flow rate of 7.0 kilograms per second (kg/s) or 924.7 gallons per minute (gal/min).

7. The device of claim 1 , wherein the supercritical fluid is turbulent, and has a Reynolds number at 2.4×10 6 , and mean turbulence velocity of 16.7 m/s.

8. The device of claim 1 , wherein the first pipe section having a cross-sectional diameter and a length of at least forty times the cross-sectional diameter.

9. The device of claim 1 , wherein the y-pipe segment comprising a 45° y-trap located at approximately 32 pipe diameters from a first pipe section inlet.

10. The device of claim 1 , wherein a low pressure drop associated with Y-pipe provides the filter for a supercritical fluid process to maintain efficiency at an increased level and negligible losses.

11. The device of claim 10 , wherein the y-pipe segment allows a plurality of y-pipe segments throughout the closed loop system with reduced pressure and flow losses associated with conventional in-line filter media.

12. A closed loop SCO2 system independent of a media filter, comprising:
a heater in flow communication with a process SCO2 fluid to heats the fluid to supercritical parameters for input into a turbine; the process SCO2 fluid flowing first through a y-pipe filter;
a recompressor, a main compressor, a high temperature (HT) recuperator and a low temperature (LT) recuperator, connected in a closed process loop;
the SCO2 in flow communication with the turbine flowing from turbine to an input of the recompressor and into the main compressor; and
a gas cooler for feeding cooled gas to the main compressor;
wherein the recompressor recirculates a portion of the process SCO2 fluid to the high temperature (HT) recuperator at a junction, in serial flow communication with the low temperature (LT) recuperator; the main compressor discharges process SCO2 fluid to the LT recuperator; the turbine discharges a portion of SCO2 fluid to HT recuperator in a reverse path to LT recuperator;
the HT recuperator discharge in a forward path to heater inlet and thence to the y-pipe filter at an inlet to turbine; and
wherein the y-pipe filter comprises:
a first pipe section connected in flow communication with the closed loop SCO2 system;
a y-pipe segment intersecting the first pipe section at an intersection joint; the intersection joint at a descending obtuse angle with respect to the first pipe section flow direction;
the y-pipe segment open at the intersection joint and closed opposite the intersection joint, in flow communication with the first pipe section;
wherein the y-pipe section inducing an eddy current turbulence zone adjacent the intersection joint to remove substantially all contaminants suspended in the SCO2 fluid;
and wherein the contaminants are deposited in the descending y-pipe segment.

13. The process of claim 12 , wherein the Y-pipe filter is located at any point in the closed loop.

14. The process of claim 12 , wherein the Y-pipe filter comprises a plurality of Y-pipe filters, wherein the plurality of Y-pipe filters being located in serial flow communication at multiple points in the closed loop, for removal of contaminants.

15. The process of claim 1 , wherein the eddy current being generated by contact with an angular edge formed at the intersection joint of the descending y-pipe segment in flow communication with the first pipe section.

16. The process of claim 1 , wherein the first pipe section having a cross-sectional diameter and a length of at least forty times the cross-sectional diameter.

17. The process of claim 1 , wherein the y-pipe section comprising a 45° y-trap located at approximately 32 pipe diameters from a first pipe section inlet.

18. The device of claim 1 , wherein a low pressure drop associated with Y-pipe provides the filter for a supercritical fluid process to maintain efficiency at an increased level and negligible losses.

Assignees

• Nat Tech & Eng Solutions Sandia Llc

Inventors

• Fleming Darryn
• Rodriguez Salvador B

Classifications

• F02C7/052

  with dust-separation devices · CPC title

• F02C1/105

  construction; details · CPC title

• F02C1/04 Primary

  the working fluid being heated indirectly {(in a fluidised-bed combustor F02C3/205)} · CPC title

• B01D45/04

  by utilising inertia (B01D45/12 takes precedence) · CPC title

• B01D45/02

  by utilising gravity · CPC title