api spec 10a n.
Skip this Video
Loading SlideShow in 5 Seconds..
API Spec 10A PowerPoint Presentation
Download Presentation
API Spec 10A

Loading in 2 Seconds...

play fullscreen
1 / 8

API Spec 10A - PowerPoint PPT Presentation

  • Uploaded on

API Spec 10A. June 25, 2013. Changes to API Spec Q1 8 th Edition to 9 th Edition (Effective June 2013). Involves a complete re-write of Q1 No longer a mirror copy of ISO Introduction of major changes will be done by Bill Ulrich. Mineral Oil being used (Jim Davidson).

I am the owner, or an agent authorized to act on behalf of the owner, of the copyrighted work described.
Download Presentation

PowerPoint Slideshow about 'API Spec 10A' - aulii

An Image/Link below is provided (as is) to download presentation

Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author.While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server.

- - - - - - - - - - - - - - - - - - - - - - - - - - E N D - - - - - - - - - - - - - - - - - - - - - - - - - -
Presentation Transcript
changes to api spec q1 8 th edition to 9 th edition effective june 2013
Changes to API Spec Q1 8th Edition to 9th Edition (Effective June 2013)
  • Involves a complete re-write of Q1
  • No longer a mirror copy of ISO
  • Introduction of major changes will be done by Bill Ulrich
mineral oil being used jim davidson
Mineral Oil being used (Jim Davidson)

From API Spec 10A, Sec 10, part 10.1 Apparatus

  • The space between the slurry container and the walls of the pressure vessel shall be completely filled with a hydrocarbon oil. The selected oil shall have the following physical properties:
  • ⎯ viscosity range: 6 mm2/s to 79 mm2/s at 38 °C (100 °F) or 6 cSt to 79 cSt at 38 °C (100 °F); or 45 SSU to 360 SSU at 38 °C(100 °F);
  • ⎯ specific heat: 1,9 kJ/(kg⋅K) to 2,5 kJ/(kg⋅K) (0,45 Btu/lb⋅°F to 0,60 Btu/lb⋅°F);
  • ⎯ thermal conductivity: 0,112 W/(m⋅K) to 0,138 W/(m⋅K) [0,065 Btu/(h⋅ft2⋅°F/ft) to 0,08 Btu/(h⋅ft2⋅°F/ft)];
  • ⎯ specific gravity: 0,83 to 0,93.
annex b change required
Annex B change required
  • Annex B requires that mass be reported in US Customary units (pounds) but is contradictory
  • B.4.2 Units

As a minimum, product should be marked with U.S. customary (USC) units. Use of dual units [metric (SI) units and USC units] is acceptable.

  • B.4.3 Markings

b) net mass (in U.S. customary (USC) units)

  • API does not enforce when auditors note a violation
  • Committee recommends that mass be reported in the local country of origin’s units
  • ANNEX B also is not a part of ISO 10426-1
auditor findings of problems with api 10a
Auditor Findings of Problems with API 10A
  • a) Clause 7.1.4 - the accuracy and calibration frequency of the mixer's time is not included.
  • b) Clause 7.2.2 - the calibration frequency of the temperature measuring device is not included.
  • c) Figure 7 - the sketch shows a type I class 1 narrow-mouth flask instead of a type I class 2 wide-neck flask required by clause 8.1.3.
  • d) Clause 9.3.2 - why measure the dimensions of the test faces of the compressive strength specimens to +/- 1.0 mm to use to calculate the cross sectional area if it will not be different from the 50.0mm x 50.0mm nominal dimensions.  If it's considered good practice to use actual measurements to calculate the cross sectional area then the test faces should be measured to +/- 0.1 mm or +/- 0.01 mm (which most labs are doing anyway).
auditor findings of problems with api 10a1
Auditor Findings of Problems with API 10A
  • e) Clause 9.3.3 - one of the rate of loadings needs to include the strength when it equals 3.4MPa - one is greater than 3.4 MPa and the other is less than 3.4.
  • f) Clause 9.4 - the calculated compressive strengths of test samples and their average are to be rounded to the nearest 50kPa, i.e. 0.05MPa, however, all the acceptance limits have a least significant digit of 0.1MPa. This could lead to actual results being rounded twice to bring them into specification; for example, for a Class G 38C cured specimen with a calculated strength of 2.04234... MPa it will be rounded to 2.05MPa which does not meet the 2.1 MPa minimum value.  However, it is convention practice in the determination of compliance with a specification limiting value to round the observed or calculated value to same number of significant figures as that of the specification, i.e. 2.05MPa can be rounded to 2.1 MPa and now passes.  Note; this could not be done if the MPa compressive strength minimum limits had another zero added to them, i.e. 2.05 MPa should not be rounded to satisfy a 2.10 MPa limit.  I feel that the rounding practice defined by ASTM E29 should used, as applied by ASTM C114.
auditor findings of problems with api 10a2
Auditor Findings of Problems with API 10A
  • g) Clause 10.2.3 - why are temperature calibration requirements for the pressurized consistometer so different from that of the atmospheric consistometer in clause 8.2.1? 
  • h) Clause 10.2.5 - why is the calibration frequency for the pressurized consistometer annual and that of the atmospheric consistometer quarterly?
  • i) Clause B.4.3b - why is the net mass to be in US customary units if the cement is made and sold outside of the US?  This requirement is not being enforced by API anyway as I wrote this one up as a nonconformity a while ago but it was cancelled.
  • j) Clause 10.2.3 requires temperature measurement to be calibrated to ± 2°C, however, clause 10.3.4 requires the temperature to be within ± 1°C 10 minutes after the end of the ramp.
auditor findings of problems with api 10a3
Auditor Findings of Problems with API 10A
  • 10A has no clear requirements for the qualification of 'rapid' chemical analysis methods and analysts when EN standards are only used