Well Control Flashcards

1
Q

List 5 warning signs of kicks while drilling.

A
Flow rate increase, 
well flows with pump off, 
pit gain, 
drilling break, 
lost circulation, 
drilling into a fracture, 
increase in torque and drag, 
increase connection or background gas.
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2
Q

While drilling a horizontal well with water base mud, a kick is taken and the well is shut in immediately without a flow check. How much of a difference would you see between SIDPP and SICP?

A

There should be little or no difference between SIDPP and SICP if the kick is still in the horizontal section. Gas does not migrate horizontally.

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3
Q

What does shut in drill pipe pressure tell you?

A

It is the difference between formation pressure and hydrostatic pressure in the drill pipe.

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4
Q

Have you been in a well control situation before? If so, describe your role and what happened.

A

yes. Do not rig out wire line when stuck in the hole without being shut in. Even if you think you have cemented off all the gas zones.

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5
Q

On a connection you notice that the off bottom circulating pressure has dropped by 1000 kPa. What would you do?

A

Investigate for lost circulation, gas-cut mud in annulus, dump valve stuck open, washout in string pump losing suction, leak on surface, pump washout, motor drive line twist off.

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6
Q

How and when is nitrogen used to unstuck pipe? How would you plan it?

A

when you are diff stuck.

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7
Q

By Directive 36, function testing Class II-VI BOP’s and HCR for an inspector requires the accumulator pumps be shut down for the test. What is the minimum accumulator pressure during the test and what is the minimun time to recharge the accumulator back to operating pressure when the pump is turned back on? What practices have you done to monitor accumulator performance?

A

8400 kPa and 5 minutes

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8
Q

With surface casing run, what should the minimum pressure test values be for high and low pressure tests on the annular, rams and choke manifold for a 21,000 kPa Class IV stack (Alberta) and manifold and what constitutes a valid pressure test?

A

1400 kPa low, 7000 kPa high on the annular, rams and manifold. A 10% bleed off is permitted. A valid pressure test consists of a 0 kPa pressure drop

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9
Q

What are the pressure testing requirements for different class BOP’s and casing strings?

A

Class 1 BOP’s do not require to be pressure tested - only functioned Other classes required all associated components to be tested with a 10 minute low and high test Every casing string requires a low and high pressure test immediately after cementing

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10
Q

Understanding the appropriate BOP’s in different thermal areas - Class 1, 2, 3 or 4?

A

Class 1 can be used for surface hole when hydrocarbon zones may be encountered or high watertables (artesian aquifers).
Class 1 used in low risk areas (Oil Sands Approved areas) - Directive 8, Checklist 3 posted.
Different minimum pressure ratings.
Depth ratings.
BOP Components

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11
Q

What is a well barrier? Give examples

A

Well barriers can be fluid hydrostatic pressure or a mechanical. Purpose of a well barrier is prevent formation fluid from flowing unintentionally to surface or into another formation. Barriers must be independent and tested for verification.
Primary Barrier: drilling fluid Secondary Barriers: BOPs, wellhead, casing, cement, etc.

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12
Q

How would you validate a barrier? Give Examples

A

Drilling Fluid: confirm fluid density provides adequate hystrostatic pressure to contain formation pressures
Mechanical Barrier: pressure test in the direction of flow (if possible), to maximum expected differential pressure or to regulatory requirement, whichever is higher.

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13
Q

What was the barrier policy of your previous employer? Or what is the the barrier policy at Husky?

A

Husky’s barrier policy is to have at least two independent and tested barriers available in order to control the potential flow path during well operations.

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14
Q

What are important considerations for well barriers?

A

Most operations will require 2 barriers in place at all times where potential exists for uncontrolled flow, exceptions to this normally require a risk assessment by the operator (and MOC). Barrier must withstand max pressure differential it is exposed to. Barrier location must be known and must have a positive or negative pressure test to provide verification (if practical test should be in the direction of flow) Barriers must be independent so no single barrier failure will allow flowA failed barrier must be accessible to repair without impacting the 2nd active barrier

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15
Q

Explain some well conditions when drilling fluid would need to be validated as a well barrier?

A

‘Example: 1) Drilling into over-pressure formation usually requires increasing the mud density to control fluid/gas influx. Before drilling ahead, often a short wiper trip and circulating bottoms-up is conducted to confirm drilling fluid has adequate hydrostatic pressure (trip margin) to drill ahead or trip out of hole.
‘Example 2) During MPD operations the well is circulated to kill fluid at the heel, then monitored to ensure mud density is adequate to limit ballooning and still control the well before tripping out of hole.

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16
Q

How do you monitor the condition of well control equipment? How does winter operations affect this? How do you manage it in winter?

A

Properly pressure testing BOPs and manifold. Function testing accumulator and BOPs. Monitoring performance of BOP system and checking for oil leaks. Monitor condition of annular element. In winter ensure bleed-off lines and manifold are displaced to proper glycol/water blend that will not freeze. Ensure BOPs and manifold have adequate heat. Verify accumulator fluid is rated for winter temperature. Monitor BOP function time in cold weather conditions.

17
Q

Explain how you validate function test of ram preventer?

A

WSL must witness the ram closing and ensure ram closing time are compliant with Directive 36.

18
Q

Explain your checks to evaluate if a Rig Manager and Driller are competent in well control?

A

Understanding over-pressure indicators (Drilled gas, BG, connection gas, trip gas, etc.)
Understanding well control procedures and observe reaction to well control situations.
Managing wellbore conditions (ie. Pressure, losses, tight hole, etc.)
Actively trains crew on well control procedures and equipment. Hold crews accountable.
Complies with company policies and industry regulations (mud checks, flow checks, trip margin, etc.)
Closely monitors well control equipment. Immediately report any concerns
Ensures rig inspection and BOP/accumulator function and pressure testing are properly conducted

19
Q

On a SAGD well, 339mm x 346mm surface bowl is installed, 13-5/8” - 3000 psi BOP Class III is nippled up before drilling intermediate section. How are the different elements of BOP stack tested?

A

Run in with cup type tester and DP, set the cup in the 339mm casing, presure test annular and pipe ram; Test blind ram against the surface casing. Some pressure testers have a set up to test blind ram with cup and a ring hanging on the pipe ram. Ensure this tool is not used. NOTE: When the BOP is nippled up on intermediate casing bowl (11”), pressure tester has to ring to land in the casin bowl and test the blind ram against the cup.

20
Q

After pumping and displacing cement on intermediate casing, what well control measure is applied before picking up the BOP to cut the intermediate casing?

A

Slack off the casing weight on bottom with no weight in the rotary slips. Wait on cement for 2 hours and flow check. If well is static, pick up BOP, cut the casing and walk the rig. NOTE: If during pumping/displacing of cement losses are encountered and cement level drops in annulus, install the seal around the casing.

21
Q

Explain welding method for surface casin bowls and intermediate casing bowls.

A

339mm x 346mm, 14 Mpa surface casing bowl supplied by Stream-Flo, weld the casing to bowl from inside and outside. Test the weld with nitrogen to 3500 kPa (Not more than 50% of 339mm casing collapse rating) 279mm x 244.5mm, 14 Mpa casing bowl supplied by Stream-Flo, weld the casing to bowl from inside and outside. Test weld with nitrogen to 7000 kPa.

22
Q

While drilling in an active thermal area, what is the first indication of drilling in a hot zone?

A

Continuous temperature monitoring at scalping tank shaker box is required. During drilling, due to cooling effect of the mud circulation, mud may not see large temperature changes, but a temperature increasing trend is a good indication