Downhole Diverter Gas Separator

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7 th Annual Sucker Rod Pumping Workshop Renaissance Hotel Oklahoma City, Oklahoma September 27 - 30, 2011 Downhole Diverter Gas Separator Ken Skinner, Lynn Rowlan, Dieter Becker - Echometer Company A. L. Podio - University of Texas - Austin Jim McCoy

Transcript of Downhole Diverter Gas Separator

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7th Annual Sucker Rod Pumping Workshop

Renaissance Hotel Oklahoma City, Oklahoma

September 27 - 30, 2011

Downhole Diverter Gas Separator

Ken Skinner, Lynn Rowlan, Dieter Becker - Echometer Company A. L. Podio - University of Texas - Austin

Jim McCoy

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liquid in anchor

pump

slip

gas in anchor

Basic Principles of Downhole Separator

System Gravity separation is the

governing principle for downhole gas separators.

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GAS BUBBLES FLOW UPWARD IN OIL OR WATER AT A RATE OF APPROXIMATELY 6 INCHES PER SECOND. THUS, GAS BUBBLES WILL BE RELEASED FROM A LIQUID COLUMN IF THE DOWNWARD LIQUID VELOCITY IS LESS THAN 6 INCHES PER SECOND.

A LIQUID COLUMN HAVING AN AREA OF 1 SQUARE INCH TRAVELLING AT A VELOCITY OF 6 INCHES PER SECOND IS A RATE OF APPROXIMATELY 50 BPD.

Gas Rise Velocity is approximately 6 inches per second.

Gas Separation from Liquid

Gas Separator Liquid Capacity is based on the Following Principle:

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Natural Gas Anchor

The most efficient downhole gas separators locate the pump intake below the lowest gas entry point.

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Improved Natural Gas Anchor

Maximum flow area in casing annulus below pump.

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Liquid Capacity for Various Annular Areas

Natural Gas Anchor

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“Poor Boy” Gas Separator above perforations

A small, long dip tube within a small diameter separator.

Very poor design with a small outer tube ID and long flow paths.

Only acceptable for low volume wells.

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“Poor Boy” Gas Separator – Very Common

Seating Nipple

Collar

Perforated Sub

Collar Joint of Tubing

Dip Tube Tubing Collars prevent perforated sub from laying against casing wall where liquid accumulates

Casing

Limited Flow Area and Small 3/8 inch holes in a perforated sub limit liquid entry flow and gas exit flow thus reducing separation efficiency

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“Poor Boy” Gas Separator Liquid Capacity

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Collar-Size Separator Increases Liquid Capacity

A good separator must strike a balance between annular flow area, separator flow area, dip tube diameter and pressure drop. Outer barrel OD same as collar OD. Thin wall outer barrel and dip tube. Short flow conduits. Large inlet ports.

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To get gas capacity of a specific installation multiply the table value by the Pressure at the Pump Intake (psi) and divide by 14.7 11

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Packer Gas Separator

Uses gravity separation like the “Poor Boy” except much more separation area and capacity.

Higher cost and higher risk of mechanical and sand problems.

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Concentric Packer Gas Separator

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A concentric packer type gas separator offers additional liquid and gas capacities.

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Diverter Gas Separator Animation

Pump

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Diverter Gas Separator Animation

Pump

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Pump

Discharge Port Above Diverter for Reservoir Fluid

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Separator Parts

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Separator Parts

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Premium Rubber Diverter Cups The diverter cups are constructed from high temperature, flexible, wear-resistant, premium elastomer.

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316 Stainless Steel

Separator Parts

Premium Rubber Diverter Assembly

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Premium Rubber Diverter Cups Multiple cups can be utilized as desired

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Separator Parts

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Shear Pins

Shear pins are located below the diverter cups. The force required to shear the shear pins is operator selectable. Factory setting is 4000 pounds. If the diverter cups are not retrievable with the gas separator, the cups will be left in the well with the shear pins and shear collar.

Pump

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Sand Accumulation

Sand or debris may deposit above the swab cup flow diverter. If 5 inches of sand accumulates over the diverter between the gas separator and the casing wall, the flow of liquid into the gas separator will cease and production from the tubing will cease. When sand or debris is blocking the gas separator liquid inlet ports, a fluid level test will indicate a high fluid level in the casing annulus and a dynamometer pump card will indicate low or no pump fillage. The well will require servicing.

Pump

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Sand Accumulation When the pump is unseated, liquid in the tubing will flow down the tubing and discharge out of the gas separator through the gas separator liquid inlet ports. The discharging liquid will be at high pressure. This will wash the sand and debris away from above the diverter. The discharging liquid will flow up the casing annulus and carry the sand. Probably ½ of the liquid and sand will flow down through the gas separator into the lower portion of the casing below the diverter. Reseat the pump and pump the well. Perform the liquid level test and dynamometer test to insure the well is operating properly.

Pump

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Sand Accumulation - Shear Pin Sand can accumulate above the gas separator diverter and cause difficulty in removing the gas separator and diverter from the well. Retrieval of the gas separator and diverter may still be a problem even after flushing sand from above the diverter. A shear pin is located at the bottom of the swab cup diverter on the gas separator so that the gas separator can be removed from the diverter and retrieved from the well. The shear pin holds the diverter swab cups to the gas separator. When the shear pin is sheared, the gas separator can be separated from the diverter swab cups and removed from the well. The shear pin will shear at 4000 # (pre-set).

Pump

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Fluid Pressures Surrounding Separator

Pump

58 psi Fluid Discharge Pressure

60.5 psi Liquid Inlet Pressure

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Installation Pump

A tubing anchor is installed 3 joints above the separator to prevent tubing and Diverter Gas Separator movement during pump operation.

Water or liquid lubricant can be added to casing annulus or tubing when the rubber diverters are above the liquid level in the well when running the Diverter Gas Separator into the well.

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Diverter Gas Separator Capacity 2.5 OD Outer Separator Barrel ~ 60 Psig Intake Pressure

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Producing BHP Recommendation A PBHP of 10% of SBHP insures producing 97% of Well’s Max Rate

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Use Efficient Downhole Gas Separators to:

INCREASE OIL AND GAS PRODUCTION

IMPROVE EFFICIENCY OF THE LIFT SYSTEM

CORRECT ARTIFICIAL LIFT PROBLEMS CAUSED BY INCOMPLETE PUMP FILLAGE DUE TO GAS INTERFERENCE

REDUCE OPERATING COST

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Copyright

Rights to this presentation are owned by the company(ies) and/or author(s) listed on the title page. By submitting this presentation to the Sucker Rod Pumping Workshop, they grant to the Workshop, the Artificial Lift Research and Development Council (ALRDC), and the Southwestern Petroleum Short Course (SWPSC), rights to:

– Display the presentation at the Workshop. – Place it on the www.alrdc.com web site, with access to the site to be as

directed by the Workshop Steering Committee. – Place it on a CD for distribution and/or sale as directed by the Workshop

Steering Committee.

Other use of this presentation is prohibited without the expressed written permission of the author(s). The owner company(ies) and/or author(s) may publish this material in other journals or magazines if they refer to the Sucker Rod Pumping Workshop where it was first presented.

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Disclaimer The following disclaimer shall be included as the last page of a Technical Presentation or Continuing Education Course. A similar disclaimer is included on the front page of the Sucker Rod Pumping Web Site. The Artificial Lift Research and Development Council and its officers and trustees, and the Sucker Rod Pumping Workshop Steering Committee members, and their supporting organizations and companies (here-in-after referred to as the Sponsoring Organizations), and the author(s) of this Technical Presentation or Continuing Education Training Course and their company(ies), provide this presentation and/or training material at the Sucker Rod Pumping Workshop "as is" without any warranty of any kind, express or implied, as to the accuracy of the information or the products or services referred to by any presenter (in so far as such warranties may be excluded under any relevant law) and these members and their companies will not be liable for unlawful actions and any losses or damage that may result from use of any presentation as a consequence of any inaccuracies in, or any omission from, the information which therein may be contained. The views, opinions, and conclusions expressed in these presentations and/or training materials are those of the author and not necessarily those of the Sponsoring Organizations. The author is solely responsible for the content of the materials. The Sponsoring Organizations cannot and do not warrant the accuracy of these documents beyond the source documents, although we do make every attempt to work from authoritative sources. The Sponsoring Organizations provide these presentations and/or training materials as a service. The Sponsoring Organizations make no representations or warranties, express or implied, with respect to the presentations and/or training materials, or any part thereof, including any warrantees of title, non-infringement of copyright or patent rights of others, merchantability, or fitness or suitability for any purpose.