GC MERGE OF LIGHT ENDS WITH ASTM D7169 BOILING POINT DISTRIBUTION

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GC MERGE OF LIGHT ENDS WITH ASTM D7169 BOILING POINT DISTRIBUTION Crude Oil Quality Association St. Louis, MO June 8, 2017 Arden Strycker, Ph.D. SGS North America

Providing Solutions Across the Value Chain UPSTREAM DOWNSTREAM EXPLORATION AND APPRAISAL DRILLING PRODUCTION STORAGE AND LOGISTICS REFINING AND PROCESSING LOGISTICS SERVICES Subsurface Consultancy Well Testing Services Cased Hole Services Production Fluids Testing Metering and Measurement Consulting Tools Wellhead Services Rock Properties Testing Trade Related Services Non-Inspection Related Testing Lab Outsourcing Solutions Plant and Terminal Operations Metering and Instrumentation Oil Condition Monitoring Sample Management Services Fuel Integrity Services Cargo Treatment Services 2

Refining & Processing Overview For the refining and processing of crude oil and natural gas, SGS provides the following expertise and services: LABORATORY TESTING, DESIGN AND OUTSOURCING OUTSOURCED PLANT AND TERMINAL OPERATIONS METERING AND CALIBRATION VALUE ADDED BLENDING AND CARGO TREATMENT MEASUREMENT, SAMPLING AND ANALYSIS OUTSOURCING SAMPLE HANDLING AND DISTRIBUTION BIOFUELS BLENDING 3

SGS CRUDE ASSAY LABORATORY Assay : The combination of physical and chemical data that uniquely describe a crude oil. Usually includes TBP distribution of the oil. (ASTM D7169, D7900, D2892, D5236) Each assay is customized to meet the unique requirements of each client. SGS Crude Assay Laboratories, globally distributed. SGS at Deer Park (TX) services predominantly North and South America. Capability to perform full compositional analysis of crude oils and condensates. Full range of testing and analyses covered. Both Haverly and Spiral Crude Assay software suites are supported. SGS analytical support includes 24/7/365 laboratory operations. 4

HIGH TEMPERATURE SIMDIST (ASTM D7169) Contributions of High Temperature SimDist (D7169) to Crude Oil Quality Mini-Assays (crude oil testing), substitute for TBP curve Flash Assays (crude oil testing), update older assays, TBP Curve Extends TBP curves in new assays to C-100 (720 C) Quality Monitoring (existing supply stream) Benefits & Limitations of ASTM D7169 (+) Quicker & cheaper than physical distillation (+) TBP curve smoother, bigger range, better isomer separation (-) GC Technique not actually a distillation (-) IBP to about 260 F is problematic 5

COMBINE D7169 WITH LIGHT ENDS (D7900) Replacing the D7169 front end with a Light Ends Analysis (up to nonane, 300 F) will improve the overall results. Benefits & Limitations of merging D7169 with D7900 (+) Lightest hydrocarbons (C2, C3, C4) missed by D7169 are captured by D7900. (+) Precision of C4 to C8 is improved. D7900 uses internal standard. D7900 eliminates co-elution problem with CS 2. D7900 eliminates FID response quenching. (-) Merge process is not standardized. (-) Accuracy is affected by the merge point. (-) Figure X1.2 illustration in D7169 Appendix is misleading. 6

X1.2 ILLUSTRATION IN D7169 APPENDIX Decreased light ends impacts cumulative recovery; they are not recovered later. Cum. Yield Unchanged? ASTM D7900 stops at 300 F 380 F? 7

PRECISION IMPACT D7169 Reproducibility (R) at 300 F, about 1.8 mass% yield Integration of CS 2 solvent not quantitative! Impact of quenching region can lower cumulative yields. Light gases variable, missing up to 3 mass% for extreme cases Especially true for ethane, propane, and i-butane Other SimDist methods are no better, D2887 (IBP >100 F), D6352 (IBP >345 F) Note that D7169 test method is not ideal for light crude oils. Relative to TBP, deviations from 2 to 5 mass% are possible! 8

LOSSES IN QUENCH REGION 9

MERGE OR COMBINE D7169 & D7900 DATA SET POINT Separation Systems 10

ASTM PROPOSED MERGE PROCESS ASTM Task Group, D02.04L, WK64242 Draft method being balloted, D02.04L subcommittee Currently proposing algorithm for GC processing software Basic Approach Merged curve begins with D7900 data. HTSD data is appended at set point (not to exceed BP of n- nonane) (user determined). Total recoveries 100% are normalized through D7169 data only. Mathematics are described. Additional mathematical smoothing or fitting is left to the individual user s requirements and not included in the draft. 11

SET POINT Where to put the Set Point? (transition from D7900 to D7169) Ideally between C8 and C9 D7169 impact of light ends extends up to C8 (260 F). Maximum coverage of D7900 is to C9 (300 F). GC Software usually has a default set point. My observations comparing against physical TBP curves For lighter samples with observed losses in D7169, a set point of 300 F is often best. Where losses are less significant, a set point of 200 F works better (correcting other deviations with D7169). As with so many situations in the laboratory there are always exceptions! 12

EXAMPLES, EXPLANATION Following examples are provided to illustrate how the light ends merging process might look. The calculation method used is not identical to that being considered by ASTM. Proposed ASTM method is specific for GC processing (e.g., small increments, 0.01 mass% recommended). Proposed method utilizes data arrays to manipulate cumulative mass percent vs. boiling point tables. The following merge examples were generated independently of GC processing. Approach is similar; calculations are different. Examples are actual samples. Data has been altered for effect. 13

TYPICAL CHROMATOGRAMS 14

TYPICAL RESULT, EXAMPLE #1 Merged HTSD #1 600.0 500.0 400.0 300.0 200.0 100.0 0.0 0 5 10 15 20 25 30 35 40 45 50 mass% HTSD GC Merged HTSD TBP 15

SMOOTHED LIGHT ENDS, EXAMPLE 4 Merged HTSD #4 1400 1200 1000 800 600 400 200 0 0 10 20 30 40 50 60 70 80 90 100 mass% HTSD GC Merge HTSD TBP 16

LESS TYPICAL CHROMATOGRAMS (D7169 GETS IT WRONG) 17

HEAVY CRUDE, DILUENT, EXAMPLE #2 Merged HTSD #2 1400.0 1200.0 1000.0 800.0 600.0 400.0 200.0 0.0 0 10 20 30 40 50 60 70 80 90 100 mass% HTSD GC Merged HTSD TBP 18

D7900 IMPROVES HTSD, EXAMPLE 3 Merged HTSD #3 1000 900 800 700 600 500 400 300 200 100 0 0 10 20 30 40 50 60 70 80 90 mass% HTSD GC Merged HTSD TBP 19

VERY LIGHT CRUDE, EXAMPLE #5 Merged HTSD #5 1000.0 800.0 600.0 400.0 200.0 0.0 0 10 20 30 40 50 60 70 80 90-200.0 mass% HTSD GC Merged HTSD TBP 20

SUMMARY High Temperature SimDist analysis of Crude Oil offers quicker estimate of TBP curve. However, losses & deviations in the quenching region (C4 to C8) can be quite significant for D7169. D7900 provides more accurate results in C4 to C8 range. Merging with Light Ends analysis (ASTM D7900) corrects for losses in the quenching region. I recommend that the original D7169 data be separately provided when merged results are offered. Draft standardization of merging process is currently under review at ASTM (D02.04). Proposed merging GC algorithm written by ASTM work group is inballot at sub-committee level. As proposed the algorithm would be inserted in the appendix (nonmandatory) of D7900. D7169 would reference this section. 21

SGS Group Management SA 2016 All rights reserved SGS is a registered trademark of SGS Group Management SA. QUESTIONS & ANSWERS Arden Strycker, Ph.D. Phone: (713) 824-4326 Email Address: arden.strycker@sgs.com www.sgsgroup.us.com/en/oil-gas This presentations is intended for educational purposes only and does not replace independent professional judgment. Statements of fact and opinions expressed are those of the participants individually and, unless expressly stated to the contrary, are not the opinion or position of SGS. SGS does not endorse or approve, and assumes no responsibility for, the content, accuracy or completeness of the information presented. 22