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Choosing the Right Level Technology Maximizes Production and Yield in Heater Treaters for Oil Producer

Sometimes the solution to a plant operations challenge isn’t just automating with instrumentation, but rather choosing the right instruments for the job. A major crude oil and natural gas exploration and production company was experiencing problems with their level measurement in heater treaters. The company was unable to optimize their heater treater separators, which were causing gas to be carried over to the tanks, a very costly loss. This was a significant problem for a major production company operating in the Bakken Oil Field located in the U.S. and Canada, producing over 4,800 MBOE.

Previously, the company used mechanical valves for level measurement, but they did not perform well to solve the problem. The customer was looking to replace these traditional mechanical instruments in order to more efficiently operate their heater treaters. Their goals were to improve level measurement, minimize lost production while maximizing production and yield, and reduce emissions. The main concerns were: improving efficiency of the heater treaters; optimizing liquid level control; and reducing gas carryover to the tanks.

dp level with ERS vs. guided wave radar level measurement

Meeting these goals began with an informative false start. Initially, traditional DP level transmitters were fitted to improve liquid level measurement in the heater treaters. However, the traditional DP needed the wet and dry legs to be blown out regularly otherwise the readings could be affected – a historic characteristic of DP transmitters in some applications. The technology was also not easy for the operators to understand – a problem in an industry where many experienced workers are retiring, and new personnel lack the same hands-on expertise with instrumentation.

The customer retrofitted their existing tanks using Rosemount™ Electronic Remote Seals (ERS) on the oil and water legs, replacing the traditional DP transmitters. The ERS system was much easier for operators to understand than the traditional DP. The ERS system also had no wet or dry legs requiring maintenance, thus significantly reducing personnel time. In addition, it provided faster response time than traditional differential pressure transmitters.

The company also wanted to take advantage of the ability of guided wave radar to measure level, and interface with a single device in new separators they were building. Since the new installations were not constrained by the tank configuration, their manufacturer added a 4-in. (101.6 mm) stilling well inside the separator to accommodate a Rosemount 5300 Guided Wave Radar. This simplified installation even further. The installation using the guided wave radar in the stilling well was efficient and cost effective.

Benefits of different level measurement solutions

Results exceeded the company’s requirements. The combined ERS DP measurement and guided wave radar resulted in accurate flow and liquid level measurement and reduced gas carryover, which in turn led to increased efficiency. The company measured a reduction in gas carryover from 140 mcf to 60 mcf. The guided wave radar has a low operating cost because it requires minimum maintenance. Using the Rosemount 5300 to control the oil and water levels in the treaters also eliminated the requirement for piping and additional tanks associated with the test treater, resulting in savings of $30,000 per train. Gas carryover was also significantly reduced, with possible savings of around $100,000.

What type of level measurement do you use? Do you feel it maximizes your efficiency?

10 Replies

  • We have a Heater Treater Separator which has been converted to a simple separator. We use a DLC3010 as an Interface Level Controller and Fisher 2100P connected to Pressure Switch as PLC discreet inputs, for the Level Safety High and Low shut downs. The only issue is having to remove the DLC3010 float from the vessel for routine maintenance, i.e. recalibration. Was thinking of the possibility of a piping configuration that would T off of the Fisher 2100P Chamber connections to the vessel to mount a GWR such as the Rosemount 5300.
  • In reply to SteveWJ:

    Steve,
    I sent you a direct response so we could share more details.
    Thanks for your reply!
    Lydia
  • In reply to SteveWJ:

    Steve,

    Can you share more information on the DLC3010 maintenance required for the separator? I am guessing if it is related to:
    - Build-up on the displacer (or the torque tube) that restrains the movement, resulted in a need for recalibration. Or,
    - Recalibration due to density change.

    If calibration is done with oil/water not at actual heated temperature, the level measurement will have some error when use at actual heated temperature. The reason is because oil/water density changes with temperature (Temperature increases will result in density decreases).

    To get the best measurement result, you can calibrate the DLC3010 with oil/water at the actual heated temperature. Alternatively, you can calibrate the DLC3010 at room temperature. And when the oil/water is heated to operating temperature, change the density setting in the DLC3010 to actual density at that specific temperature, then run Trim Zero to get the DLC3010 to measure at actual operating condition.

    Feel free to contact me at Keechong.lee@emerson.com if you have questions.

    Thank you.
    Kee Chong
  • In reply to SteveWJ:

    As I understand it, the Fisher 2100P is essentially a float switch? Typically, those floats are designed for the application to "float" throughout a range of varying densities. Unless the float was designed for some other S.G. fluid, I'd expect it would never require recalibration. However, because it's a mechanical technology, it's possible that routine maintenance is required to keep the moving parts free of build-up. Also, it's a best practice with floats to routinely verify the integrity of the float and operability of the linkages. I understand that you might consider using a guided wave radar here. But, assuming the 2100P is a float, then your control must already be based on a discrete input rather than a continuous level measurement? While I'm sure that could be changed, you might think instead about using an electronic switch. These have come a long way, and with the recent introduction of the Rosemount 2140 Vibrating Fork Detector, you can actually now have a "smart" switch with the capability to detect fault conditions such as excessive product build-up as well as faults with the switch itself. The discrete functionality is achieved through two discrete set-points over the 4-20 mA range, commonly 8 and 16 mA to indicate the two states. A fault condition is flagged either by the low or high extreme of the 4-20 mA range. Because the device has a HART interface, configuration is very simple, and this also has the benefit of extending the functionality of the device. For example, you could choose to monitor the frequency of the vibrating fork to indicate changes in process conditions, such as a change in product S.G. Or, inserted into the bottom of a vessel, you could use this device to detect the build-up of sand. For more information, check out the product page at www.emerson.com/.../rosemount-2140-detector-vibrating-fork.
  • In reply to Tom Wienke:

    The 2100P is a pneumatic switch with a float. The pneumatics is connected to the Pressure Switch for a discreet input into the PLC. Build up is the major maintenance issue at this point. We would keep the 2100P as hour Level Safety High and Low (LSHL). My thought was going from the 3010 to a GWR. I am still looking into that. The Rosemount 2140 sounds interesting, and worth looking into. The Heater Treater is actually now a simple separator without any heat.
  • In reply to KeeChong:

    Recalibration is due to build up. Calibration is made with the actual Oil/Water in the vessel. It is now a simple separator without any heat at this time. We are using the SG that we get back from our Oil Analysis. After our next calibration I will contact you directly with more details. The recent cold weather has been keeping us quite busy even out in the Gulf of Mexico.
  • In reply to SteveWJ:

    I have a hard back copy of the Engineers Handbook for Level Measurement. It has some valuable information concerning Automatic Overfill Protection Systems that I have shared when working with new Automation Specialist / SCADA Technicians. How would I go about getting 4 more of those hard back editions of Engineers Handbook for Level Measurement.
  • Steve
     
    Please send me your personal details (your location, full address etc.) and I will try to get a few of these to you.
     
    Anshuman Prasad
     
    Anshuman Prasad | T +1-952-204-6220 | M +1-952-221-3832
     

    Anshuman Prasad

    Director of Integrated Marketing, Rosemount Measurement and Analytical

  • In reply to SteveWJ:

    Hello Steve,
    We now have five engineer’s guides available including one specifically on overfill prevention. You can download pdfs for each one here: http://bit.ly/2F0XdiV and you can also request printed copies of the overfill book.
    The Engineer’s guide to level measurement is currently being updated and we have now run out of printed copies, but we should have a new 2018 version available in May.
  • Please send to the following:
     
    Steve Johnson
    3520 S Sam Houston Pkwy E
    #400,
    Houston, TX 77047
     
    Thank you very much.
     
     
    Steve Johnson
    Telecom Scada / Automation Specialist
    Houston, Tx. 77047
    O.  855-639-4482
    C.  979.236.9343  
     
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