Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various...

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Report No. CDOT·DTD·94·7 Influence of Refining Processes and Crude Oil Sources Used in Colorado On Results from the Hamburg Wheel-Tracking Device Tim Aschenbrener Colorado Department of Transportation 4201 East Arkansas Avenue Denver, Colorado 80222 Final Report April 1994 Prepared in cooperation with the U.S. Department of Transportation Federal Highway Administration

Transcript of Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various...

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Report No. CDOT·DTD·94·7

Influence of Refining Processes and Crude Oil Sources Used in Colorado On Results from the Hamburg Wheel-Tracking Device

Tim Aschenbrener Colorado Department of Transportation 4201 East Arkansas Avenue Denver, Colorado 80222

Final Report April 1994

Prepared in cooperation with the U.S. Department of Transportation Federal Highway Administration

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The contents of this report reflect the views of

the author who is responsible for the' facts and

the accuracy of the data presented herein. The

contents do not necessarily reflect the official

views of the Colorado Department of Transportation

or the Federal Highway Administration. This report

does not constitute a standard, specification, or

regulation.

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Acknowledgements

The refineries that provide asphalt cement to Colorado were very cooperative in their assistance with this research study. Their cooperation was greatly appreciated. The laboratory mixture tests were performed by Kim Gilbert and Nava Far (CDOT). Benja Bemelen (CDOT) performed the asphalt cement tests. .

The CDOT research panel provided many excellent comments and suggestions for the study. It included: Byron Lord and Kevin Stuart (FHWA - Turner Fairbank Highway Research Center). Doyt Bolling (FHWA - Region 8). Jerry Cloud (FHWA - Colorado Division). Steve Horton and Bob LaForce (CDOT - Staff Materials). Ken Wood (CDOT - Region 4 Materials). and Donna Harmelink (CDOT- Research).

Special thanks to the panel of Colorado asphalt paving experts who provided numerous ideas and suggestions which made this study more informational: Bud Brakey (Brakey Consulting Engineers). Jim Fife (Western Colorado Testing) . Joe Proctor (Morton International). Scott Shuler (Colorado Asphalt Pavement Association) and Eric West (Western Mobile).

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Technical Report Documentation Page

1. Repert No. 2. Govcnlmellt Accession No. 3. Recipient's Catnlog No.

CDOT-DTD-R-94-7

4. ntIt Dnd Subtitle 5. Report nate

Influence of Refining Processes and Crude Oil Sources April 1994

Used in Colorado 6. Perfonnlng OrganIzation Code

On Results from the Hambur!! Wheel-Trackin!! Device 7. Author(s) 8. Performing OrganizAtion Rpt.No.

Tim Aschenbrener CDOT-DTD-R-94-7

9. Performing Organization Name and Address 10. Work Unit No. (TRAlS)

Colorado Department of Transportation

4201 E. Arkansas Ave. 11. Contract or Grant No.

Denver, CO. 80222

12. SpmlsOI'ing Agency Nome and Address 13. Type of Rpt. and Period Covered

Colorado Department of Transportation Final Reoort 4201 E. Arkansas Ave. 14. Sponsoring Agency Code

Denver, CO. 80222

15. Supplementary Notes

Prepared in Cooperation with the U.S. Department of Transportation Federal Hiohway Administration

t 6. Ahslrnct

lhe H.,mburg wheel.tracking device is known to be very sensitive to aggregate qual ity. It was considered important

[(1 invc~tigate how the asphalt-aggregate interaction can influence the results.

The purpose of this report is to identify the influence of the aspha1t-aggregate interaction by using results from

til..:.. Hamburg wheel-tracking device. Ten grading AC-lO asphalt cements were used from four refineries who suppJy asphalt

in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources do

inOuence the test results from the Hamburg wheel-tracking device. Each refinery was able Lo produce an asphalt cement

that pa.,sed in the Hamburg whed-tracking device with the better aggregates.

17. Kel Words 18. Distribution Statement

Crude Oil So urce Hamburg Wheel-Tracking No Restrictions: This report is Device available to the public through

Refining Process the National Technical Info. Service. Springfield, VA 22161

t9.s~c\lrjt~· Clnsslf. (I·~port) 20.Securlly ClassiL (page) Z1. No. of Pnges 22. Pl;ce

Unclassified Unclassified 61 ... III

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Table of Contents

1.0 Introduction ... . ...... . ... . . . ..................... . . . . ... . .. . ..... 1

2.0 Experimental Grid . . .. . . ... . . ......... .. .... . . . .. . .. . .. .. .. ........ 2 2.1 Materials.. . . .... . . . .. .. .... ... . .. .. .. ................. .. . .. 2

2.1.1 Asphalt Cements .. .............. . . . . . . . . . . . . . . . . . .. . . . 2 2.1.2 Aggregates .... ... . ... . . ... . .. . ... . •. ..... .... . ..... . 2 2.1.3 Hot Mix Asphalt . . . . . . . . . . . . . . . . . . . . . • . . . . . . . . . . . . . . . .. 3

2.2 Tests .... . .. . ...... .. ...... . . ... ..•..................... . . 3 2.2.1 Hamburg Wheel-Tracking Device .. . . ... .. ... . . . .... ....... 3 2.2.2 Asphalt Cement Tests . . . • . . . . . .. . .. .. ............. . .... 6

2.3 Experimental Grid ..... . .. .. . ....•.•... . .... . . . . . .. . . .. . . ..... 6

3.0 Results and Discussion ...... ....... ...... . .. . . . . . . .. .. . . . . . . ....... 8 3.1 Asphalt Cement Test Results . . . . • . . . . . . . . . . . . . . . • . . . . . . • . . . . . . . . 8 3.2 Hamburg Wheel-Tracking Device Test Results . .. . . ... . . .. . .. .. .... .. 9

3.2.1 Refinery A . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 10 3.2.2 Refinery B . • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 10 3.2.3 Refinery C . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . • . . 10 3.2.4 Refinery D . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . • . .. 10 3.2.5 Venezuelan ...•....•. . . . . .. . . . . ... .. ............. . . " 11 3.2.6 Summary . .. . . . . ............. . . . . .. . . . .. . .. ......... 11

3.3 Correlation of Asphalt Cement and Hamburg Wheel-Tracking Results . .. . . . 11 3.3.1 Refinery A . . . . . . . . __ .... _ . _ . . . . . . . . . . . . . . . . . . . . . . . . . . 11 3.3.2 Refinery B ... . ...... . • .. . . ... . . . ___ ...... . _ . . . . . . . . . . 11 3.3.3 Refinery C _ .. . . .. _ .... . .... .. . ... _ . _ . _ . . . . __ . _ .. _ . __ . 11 3.3.4 Refinery D _ . _ . _ ... . ... _ . .... .. .•..•........ . • . . _ . . . . . 12 3.3.5 Venezuelan . . .. ____ . . . ___ ...• ... _ . . __ .... _ . __ . . . . . . .. 12 3.3.6 Summary . _ ... . . . _ .. . . .. ... . .. . ..... _ . ... ..... . . . ... 12

3.4 Summary . _ . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . • . . . . . • . . • . . .. 16

4.0 Conclusions . . . . . . . . . . . . . . . . . . . . . • • . . . . . . . . . . . . . . . • . . . . . . . . . . . . . .. 18

5.0 Implementation . . .. . ....................... .... .. . ........ • .... . .. 19

6.0 References . .... . . .. . ....•....... . .... .. . .. . •.......... . . ..•... .. 19

IV

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List of Tables

Table 1. Experimental Grid for the Hamburg Wheel-Tracking Device Tests . . ... . .. . " 7 Table 2. Experimental Grid for the Asphalt Cement Tests. . . . . . . . . . . . . . . . . . . . . . . . ·7 Table 3. Results from the Asphalt Cement Testing . ......... . ....... . . . .•. ... .• 8 Table 4. Results from the Hamburg Wheel-Tracking Device - Deformation (mm) After

20,000 Passes. . . . . . ....... . ... . .. . .. ... .. . . .......... ..... ..... 9 Table 5. Comparison of Results By Mixture. ....•... .. .... . ..• . .. .. . . . . .. . ... 16 Table 6. Comparison of Results By Refinery . . .. , . . . .. . . . . .. . . .. •. ..... ... , . .. 17

List of Figures

Fig. 1. The Hamburg Wheel-Tracking Device. ...... • . .. .. . . . . . . ... . ..... .. . . . 4 Fig. 2. Close-Up of the Hamburg Wheel-Tracking Device. . .... ,...... . . . .. . ... .. 4 Fig. 3. Summary of Results from the Hamburg Wheel-Tracking Device. . .. . ..... .. . . 5 Fig. 4. Results from the Hamburg Wheel-Tracking Device as a Function of Asphalt

Cement Stiffness as Measured by Absolute Viscosity. .. . ........ . ....... .. 13 Fig. 5. Results from the Hamburg Wheel-Tracking Device as a Function of Asphalt

Cement Stiffness as Measured by Penetration. ... . ............ . ... . ... .. 14 Fig. 6. Results from the Hamburg Wheel-Tracking Device as a Function of Asphalt

Cement Stiffness as Measured by the Dynamic Shear Rheometer. ...... . . . . . . 15

Appendices

Appendix A: Summary of Asphalt Cement Test Results Appendix B: Summary of Hamburg Wheel-Tracking Results

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Influence of Refining Processes and Crude 011 Sources Used in Colorado

On Results from the Hamburg Wheel-Tracking Device

Tim Aschenbrener

1.0 Introduction

In September 1990, a group of individuals representing AASHTO, FHWA, NAPA, SHRP, AI, and

TRB participated in a 2-week tour of six European countries. Information on this tour has been

published in a "Report on the 1990 European Asphalt Study Tour" (1). Several areas for potential

improvement of hot mix asphalt (HMA) pavements were identified, including the use of

performance-related testing equipment used in several European countries. The Colorado

Department of Transportation (COOT) and the FHWA Tumer-Fairbank Highway Research Center

(TFHRC) were selected to demonstrate this equipment.

The first priority of the demonstration was to verify the predictive capabilities of this equipment

by performing tests on mixtures of known field performance. The Hamburg wheel-tracking device

was compared to several mixtures of known stripping performance (2), both good and bad.

Results from the test correlated very well with field performance.

The next step was to attempt to improve the stripping resistance of the HMA placed in Colorado

by using the Hamburg wheel-tracking device. The test is known to be very sensitive to aggregate

quality (2), and methods to determine potential areas of improvement with the aggregate were

investigated (3). Besides aggregate quality, asphalt-aggregate interaction is also important. On

one project the results were very sensitive to the asphalt-aggregate interaction (4). Since the

asphalt-aggregate interaction could influence the results, it was considered important to

investigate the potential frequency and magnitude of this occurrence in a systematic manner.

The purpose of this report is to identify the influence of the various refining processes and crude

oil sources used in Colorado on the test results from the Hamburg wheel-tracking device. The

results of this study will provide importa:nt guidance to asphalt paving contractors that bid on

future projects that use the Hamburg wheel-tracking device as a specification.

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2.0 Experimental Grid

2.1 Materials

2. 1.1 Asphalt Cements

The fou r refineries that provide most of the asphalt cement used for CDOT projects provided the

asphalt cement in this study. The asphalt cement from each refinery was labeled A, B, C, or D.

The refineries produced different "types" of asphalt cement by changing crude oil sources or

refining processes. Asphalt cements were all grading AC-1 0 (AASHTO M 226, Table 2). For this

study, the refineries produced 1 to 3 different types of AC-1 o.

Additionally, an asphalt cement refined from a Venezuelan crude oil was used. This was used

primarily for information arid labeled ·Vn". There was only one "type".

2.1 .2 Aggregates

Aggregates used for lIlis study came froni a variety of sources willl a variety of performance

hisl-Jries. The aggregate combinations were selected to provide a variety of results, good to poor,

in the Hamburg wheel-tracking device. All mixtures used quarried aggregate. Two different types

of natural sands were added to help vary the performance of each mixture. All aggregates were

treated with 1 % hydrated lime prior to mixing with the asphalt cement.

The aggregates for Mix 1 were entirely from a quarried source that has had a history of good

performance. The aggregates for Mix 2 were primarily from a different quarry with a good history

of performance. However, a poor quality natural sand was added. Although the natural sand is

nor.-plastic, it does have clay present.

The aggregate for Mix 3 was from a quarry with a mixed history of good and marginal

performance. A problematiC natural sand lIlat has been associated with many HMA pavements

tha: have stripped was added. The natural sand does not adhere to asphalt cement very well and

contains clay. The aggregate for Mix 4 was from a quarry with a history of poor performance.

The poor quality natural sand with clay used in Mix 2 was also added to Mix 4.

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2.1.3 Hot Mix Asphalt

The optimum asphalt content for each of the mixtures was determined with the Texas gyratory

in general accordance with ASTM 0 4013. The pre-gyration stress, end point stress and

consolidation stress used were 210. 690, and 17,240 kPa (30, 100, 2500 psi) , respectively.

These stresses simulate the loads applied to the HMA pavements by high levels of traffic in

Colorado. All mixes contained 1% hydrated lime.

2.2 Tests

2.2. 1 Hamburg Wheel-Tracking Device

The Hamburg wheel-tracking device is manufactured by Helmut-Wind Inc. of Hamburg, Germany

as shown in Figs. 1 and 2. A pair of samples are tested simultaneously. A sample is typically

260 mm (10.2 in.) wide, 320 mm (12.6 in.) long, and 40 mm (1 .6 in.) deep. A sample 's mass is

approximately 7.5 kg (16.5 Ibs.), and it is compacted to 6% ± 1% air voids. For this study,

samples were compacted with the linear kneading compactor. The samples are submerged

under water at 50°C (122°F), although the temperature can vary from 25°C to 70°C (7rF to

158'F). For this study, all of the samples were an AC-l0 grading so the test was performed at

45°C (5). A steel wheel, 47 mm (1 .85 in.) wide, loads the samples with 705 N (158 Ibs.) The

wheel makes 50 passes per minute over each sample. The maximum velocity of the wheel is

34 cmlsec (1 .1 ftlsec) in the center of the sample. Each sample is loaded for 20,000 passes or

until 20 mm of deformation occurs. Approximately 6-1/2 hours are required for a test.

The results from the Hamburg wheel-tracking device include the creep slope; stripping slope and

stripping inflection point as shown in Fig. 3. These results have been defined by Hines (6). The

creep slope relates to rutting from plastic flow. It is the inverse of the rate of deformation in the

linear region of the deformation curve, after post compaction effects have ended and before the

onset of stripping. The stripping slope is the inverse of the rate of deformation in the linear region

of the deformation curve, after stripping begins and until the end of the test. It is the number of

passes required to create a 1 mm impression from stripping. The stripping slope is related to the

severity of moisture damage. The stripping inflection point is the number of passes at the

intersection of the creep slope and the stripping slope. It is related to the resistance of the HMA

to moisture damage.

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Fig. 1. The Hamburg Wheel-Tracking Device.

Fig. 2. Close-Up of the Hamburg Wheel-Tracking Device.

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·4

0 1\ IPost Compaction I ~ h+-~ 2'-S I ~ ... I

~ ..... ____ . J __ ._ ' -

IStripping Inflection POint 1 rCreep Slope I '-- --E ~_ . __ . ___ .. __ L.:. -.. I· . ~.~ I

···········-·····-·1···-··---... -· ~--: . r--. L '" .----E ·6 --.---- --...:-~~P\_--.-f-.--.l __ .J lJ~Pin.g-~~ope 1_ )- ._ .... _ .. __ .. ..1____ - I

I

! . ..:...·-·--f·- -- --...,--~- ._--

--~ .. -.-.-... -L. . - -'t.-. . I __ 1 1 ! .... _. __ ._._-+_._._- ----- s., ·1 6 i I

.. -..•.. ----.~.-----.- "'_'0.

I 1..

·1 8

·20 o 2 4 6

I

8 10 12 .

No. of Pa.sses (Thousands)

I

14 16

Fig.3. Summary of Results from the Hamburg Wheel-Tracking Device.

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I .. 18 20

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The City of Hamburg requires less than 4 mm rut depth after 20,000 passes. The COOT has

indicated this specification is very severe (2). A more reasonable specification for the traffic and

environment in Colorado is a deformation less than either 4 mm after 10,000 passes, or 10 mm

after 20,000 passes. A project in Colorado will be using the results from the Hamburg wheel­

tracking device as a specification for incentive payment only. Since that specification requires

less than 10 mm after 20,000 passes, the deformation after 20,000 passes is used in this report.

2.2.2 Asphalt Cement Tests

A series of tests were performed to characterize the asphalt cements used in this study. If results

from the Hamburg wheel-tracking device indicated differences between the asphalt cements, the

asphalt cement tests might potentially explain differences.

The traditional asphalt cement tests specified by COOT were performed: penetration at 25°C

(AASHTO T 49) and absolute viscosity at 60°C (AASHTO T 202). Additionally, the asphalt

cement tests developed by SHRP were also performed. A full series of tests were performed to

determine the high temperature SHRP Performance Grade of each asphalt cement. The testing

device was the Dynamic Shear Rheometer (OSR) and tests were performed on asphalt cements

that were unaged (tank) and Thin Film Oven Test (TFOT) aged (AASHTO T 179).

The DSR is used to measure the ability of the asphalt cement to resist permanent deformation

at high temperatures. Since the Hamburg wheel-tracking device is performed at high

temperatures, results from the OSR may be appropriate to understand differences in test results.

2.3 Experimental Grid

Each of the types of asphalt cement from each refinery were mixed with the four different

aggregates and tested in the Hamburg wheel-tracking device. The experimental grid is shown

in Table 1. All samples were tested at 45"C in the Hamburg wheel-tracking device since each

asphalt cement was an AC-10 grading (5).

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Table 1. Experimental Grid for the Hamburg Wheel-Tracking Device Tests.

Refmei)' .~ A E[@E:tjEB Type 1 2 3

Mix 1 X X X X X X X X X X

Mix 2 X X X X X X X X X X

Mix 3 X X X X X X X X X X

Mix 4 X X X X X X X X X X

X - Replicate samples were mixed with AC-10 grading asphalt cement and tested at 45°C.

For characterization purposes, all of the asphalt cements were tested with the current asphalt

cement tests specified by the CDOT and the high temperature asphalt cement tests developed

by SHRP. If any differences between the asphalt cements were identified by the results from the

Hamburg wheel-tracking device, the tests on the asphalt cement might potentially explain the

differences. The experimental grid of the asphalt cement tests performed is shown in Table 2 .

Table 2. Experimental Grid for the Asphalt Cement Tests.

Refin~ Vn. E[@E[@Et3EB Type 1 123123121

Penetration X X X X X X X X X X and Viscosity

DSR X X X X X X X X X X (tank)

DSR X X X X X X X X X X (TFOT)

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3.0 Results and Discussion

3.1 Asphalt Cement Test Results

Each of the asphalt cements used in this study was tested with the standard asphalt cement tests

specified by the CDOT and the new SHRP binder tests, The results are summarized in Table

3 and all of the tests are reported in Appendix A. The absolute viscosity of all of the asphalt

cements meets the requirement for an AC-10 grading (AASHTO M 226, Table 2). Additionally,

the high temperature properties of the asphalt cements meet the SHRP high temperature

performance grade of 58. In general, a penetration range of 85 to 100 dmm is expected to be

approximately an AC-10. Although most of the penetration results fell within this range, there

were two that were quite a bit softer: particularly Refinery B Type 2 and Vn.

Table 3. Results from the Asphalt Cement Testing.

Refinery Type Pen. Vis. DSR DSR High (25·C) (60·C) (tank) (TFOT) Temp dmm poises ·C@ ·C@ PG

1.0 kPa 2.2 kPa

1 92 1300 58.0 64.1 58

A 2 110 940 61.7 62.1 58

3 100 1060 62.4 62.7 58

1 105 1030 62.1 62.3 58

B 2 128 . 820 60.2 59.8 58

3 103 1060 62.5 62.7 58

C 1 100 1010 61.8 62.6 58

2 90 1000 62.4 . 61.2 58

D 1 87 1100 62.3 60.7 58

Vn. 1 129 1040 61.7 62.1 58 .

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3.2 Hamburg Wheel-Tracking Device Test Results

The test results from each mix tested in the Hamburg wheel-tracking device for each refinery and

tyPE: of asphalt produced from each refinery are shown in Table 4. The results are plotted in

Appendix B. The results shown are the mm of deformation at 20,000 passes. Each test had a

replicate sample, so the left (L), right (R), and average (Avg) are reported in Table 4. In some

instances, the samples in the Hamburg wheel-tracking device had greater than 20 mm of

defcrmation before 20,000 passes. These samples failed dramatically and are reported as ">20"

in Table 4. The test results were considered acceptable when the average of the two samples

had a deformation of less than 10 mm after 20,000 passes. The cells in Table 4 were shaded

to indicate when the average of the two samples were greater than 10 mm after 20,000 passes.

Table 4. Results from the Hamburg Wheel-Tracking Device - Deformation (mm) After

20',0'0'0' Passes.

c::J Refinery A Refinery B Ref. C D

2 Vn

1 3 1 2 3 1 2 1

L lOA 5.1 7.9 9.4 12.3 12.2 9.9 6.9 >20 12.1 1

R 8.1 11 .8 7.8 5.0 17.2 16.3 6.8 1.9 >20 10.8

Avg 9.2 8.5 7.9 7.2 MS' 14.3' 8.4 4.4 )0'2(" lUr

L 6.3 4.8 Hi2 8.4 >00 18.5 6.0 H'l .. l 5.1 11.3 2

R 9.0 8.9 14.3 10.0 >00 14.8 2.0 Hi.3 9.4 9.7 "'

Avg 7.6 6.9 14.tf 9.2 )0'20" t6.7' 4.0 t<2.7 7.3 'ttl.5'

L 14.4 >20 11.6 9.4 >2"0 17.5 9.5 4.9 >20 >20 3 "'

R 2"1..3 1M t2li 20.8 ,,20 15.7 l1H 5.6 >20 )0'20

Avg 17;9' >21f taf t5.f l>o'2Q' t 61l' 14." 5.2 >00' .. >20'

L 3.2 14.6 HtO 9.9 >20 22.S >20 7.0 >00 >20 4

R 5.2 11.l 17.3 21.4 ,,20 lU >20 4.8 >20 >20"

Avg 4.2 15.9' t7.ff 1;5.6~ >20" 17.4' >20" 5.9 >.2(f >all"

Fc.iling test result (shaded) L • Left sample R - Right sample Avg - Average

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3.2. 1 Refinery A

The Types 1 and 2 asphalt cements performed as expected by passing with the better mixes

(Mixes 1 and 2). The Type 2 asphalt cement also performed as expected by failing with the

poorer mixes (Mixes 3 and 4). It was pleasantly surprising that Type 1 passed with one of the

poorer mixes (Mix 4). Only one of the mixes (Mix 1) passed with the Type 3 asphalt cement.

Refinery A's Type 1 asphalt cement would be very desirable to use on projects with these

aggregates.

3.2.2 Refinery B

The Type 1 asphalt cement performed as expected. The better mixes (Mixes 1 and 2) passed,

and the poorer mixes (Mixes 3 and 4) failed. No mixes passed with the Type 2 asphalt cement,

and three failed dramatically. It would be desirable to avoid Refinery B's Type 2 asphalt cement.

Although Types 1 and 2 were supplied by the refinery, the Type 3 asphalt cement was sampled

from an asphalt paving contractor's plant. Based on the asphalt cement tests, Types 1 and 3

appeared identical. Therefore, it might be expected that the results from the Hamburg wheel­

tracking device would also be similar. For the poorer mixes (Mixes 3 and 4), the results were

very similar as expected. However, for the better mixes (Mixes 1 and 2) the Type 3 asphalt

cement had twice the deformation as the Type 1. This difference is perplexing.

3.2.3 Refinery C

The Type 1 asphalt cement performed as expected. The better mixes (Mixes 1 and 2) had

passing results and the poorer mixes (Mixes 3 and 4) had failing results. Only Mix 4 failed

dramatically. The Type 2 asphalt cement is the only asphalt cement that had passing results with

both of the poorer mixes (Mixes 3 and 4). Mix 2 barely failed with the Type 2 asphalt cement.

Refinery C's Type 2 asphalt cement would be very desirable to use on projects with these

aggregates.

3.2.4 Refinery D

Only one type of asphalt cement was provided by Refinery D and it performed miserably. Three

of the mixes (Mixes 1, 3, and 4) failed, and they all failed dramatically. This asphalt cement did

not perform very well with the aggregates used in this study.

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3.2.5 Venezuelan

The crude oil source of the Venezuelan asphalt tested was not known. All four of the mixes failed

the requirement. The two better mixes (Mixes 1 and 2) barely failed, and the two poorer mixes

(Mixes 3 and 4) failed dramatically.

3.2.6 Summary

All of the refineries were able to produce an asphalt cement that performed well in the Hamburg

wheel-tracking device when using the better aggregates, except Refinery D. It appears there may

be a unique asphalt-aggregate interaction that is dependent on each asphalt cement and each

aggregate used in the mixture.

3.3 Correlation of Asphalt Cement and Hamburg Wheel-Tracking Results

3.3. 1 Refinery A

The Type 1 asphalt cement was the stiffest of Refinery A's grading AC-1 0, and it also performed

the best. The Type 1 not only passed with the better aggregates, but it also did exceptionally well

with one of the poorer aggregates (Mix 4). Although the Type 2 asphalt cement was softer than

Type 3, the Type 2 performed better. Type 2 passed with all of the better aggregate, while Type

3 did not.

3.3.2 Refinery B

The Type 2 asphalt cement was an exceptionally soft grading of AC-10, and it performed very

poorly. Types 1 and 3 had virtually identical stiffnesses to each other and were closer to the

middle of the expected ranges for AC-1 0 than Type 2. Despite Types 1 and 3'5 similarity, they

performed dramatically differently. Type 1 passed with the better aggregates; while Type 3 failed

with all aggregates.

3.3.3 Refinery C

The Types 1 and 2 asphalt cements both performed remarkably well in the Hamburg wheel­

tracking device. The stiffnesses were fairly similar to each other and in the middle of the range

normally expected for a typical grading AC-10 asphalt cement.

11

Page 18: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

3.3.4 Refinery 0

With the aggregates used in this study, this was one of the poorest performing asphalt cements.

Although the viscosity was in the middle of the expected range of stiffness; the penetration

indicated a very stiff AC-10; and the DSR indicated one of the softest grading AC-10 asphalt

cements. Although the asphalt cement tests provided conflicting information about the stiffness,

the results in the Hamburg wheel-tracking device clearly indicated this was one of the poorer

asphalt cements with the aggregates used in this study.

3.3.5 Venezuelan ·

The viscosity and DSR of this asphalt cement was in the range of expected values. The

penetration indicated this was a very soft grading AC-10. Although the asphalt cement tests

provided conflicting information about the stiffness, the results in the Hamburg wheel-tracking

device clearly indicated this was one of the poorer asphalt cements with the aggregates used in

this study.

3.3.6 Summary

The deformation recorded in the Hamburg wheel-tracking device is plotted versus the asphalt

cement stiffness as measured by the absolute viscosity (Fig. 4), penetration (Fig. 5), and dynamic

shear rheometer (Fig. 6). In each of the plots, it is not possible to identify a direct correlation

between the asphalt cement stiffness and results in the Hamburg wheel-tracking device.

However, each of the points are labeled with their aggregate mixture. In general, the distinction

between the mixtures with the better aggregates (Mixes 1 and 2) can be made from the mixtures

with the poorer aggregates (Mixes 3 and 4), regardless of asphalt cement stiffness.

Some of the Types of asphalt cement tested indicated the softer grading AC-1 0 asphalt cements

did poorer than the stiffer grading AC-10 asphalt cements. However, there were numerous

samples with very similar stiffnesses that performed dramatically differently in the Hamburg wheel­

tracking device. The variable that influence the results from the Hamburg wheel-tracking device

are a function of: 1) aggregate quality, 2) refining process and crude oil source, and 3) asphalt

cement stiffness.

12

Page 19: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

20.0.------~-____r-----l...,..--__,_£}---,__-_J!II---___,--_,_--,__-__, r --, , j ,

18.0 ····· ··· ·· ·····;····· ····· ·r···········r····· ····t ·······"1"8·· ···r·········:·········· ·I ······ ···+·· ··· ········ ,

! 1 ; * 1 i

_ 16.0 ···~···· · ···r···· ····· ···r····· ····n l·········· ···· ·r~···· ~······ :··~······ ··· I· ···· ··· ·· ··· ·r ·· ········I··· ······ ···· t ··· ·· ·· ······ ·

>< Mix 1

+

Mix2

:>!.:

Mix3

D

Mix4 ~ 14.0 '+ I --tt~--r--rr-· ~ 12.0- ···· ···· ···l ··· ········r·· ·· ·········· I ······· ····+·· ········~ r*······· · +······· ····l· · ········· ·"!" ······ ····+ .. .... ........ . '---------' o l l + i 1 i I .

~ 1 O. 0 _···_-_····t-·_····· __ ··:-······ __ ······:·· __ ···· ·· -t-_····_··1· ········ ···t-······· ··· ·+· ·· ·· ···:··· ··· ····j .. .... .. . c !! ! + i !

•. o- -i - - ·I~I --r:-:X--t-l --!-- +-! : i : :

60r --rt-t-r--lt- i i-r-4.~ ~ • • 1~ 1~ 11~ 11~ 1~ 1~ 1~

Viscosity, poises

Flg.4. Results from the Hamburg Wheel-Tracking Device as a Function of Asphalt Cement

Stiffness as Measured by Absolute Viscosity.

13

Page 20: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

20.0~ ......... ----------s-----------~--~--~----tlh ~----,

,

:::-- -:l-~-r::r::r~T=:-r~l::l--: .- * ' x l 14. O -·· ·· ··-····· ·:··· · ····· ·· -·· ·· ·r· · ·· · · · · ·· ·· j · · · ·· ·· >.<·· ·· t·· ··· · ·· ·· · ···~·· ·· ·· ·· ·····+· ··· ·· ·· ··· ·· ·i ... .... .... .... j. .. ...........

~ 12.0 - .. · .... ··.· ... ··.t ··. ··· ... ,.j.··· ... ·· .··.t .. · .... · ·.· ·+····· ······ · ··I ·· · ··· · · ·· ···t ·· · · ·· ·· · · · · I · ····· - ··-T-··-·· ·~· E ; . ;

~ 1 0.0 - · ······· ··· · ··! · ,·· · ···· · ··J···· · ···· ' T ·········· -·t.·· · ······-+-··· · ··· t ·-·· ·· -·-· · · I ·- ···· · ····· - -/- · ··-·· ··-~ . x + i ;

i 8.0

;

4.01~-----~4*--~D---+I; ~- ----~----~------+-I----~----~~----4-I----~ 85 90 95 100 105 110 115 120 125 130

Penetration

Flg.5. Results from the Hamburg Wheel-Tracking Device as a Function of Asphalt Cement

Stiffness as Measured by Penetration.

14

x Mix 1

+ Mix2

* Mix3

D

Mix4 -

Page 21: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

20.0.-~~~---.~~~----,-----~,--.Br--~----~----~---. r----,

i' ]

16.0

* i E x I , , , 1 1*; , , , _E 14.0 .. , .. .... ,.+ . . '' ...... ,., ... . ... '' .1- .. , .. . -.-+ ..... .... . :·,···· · ·· ·t · ··· ·· · ·i ·,· ·· ·,,· · ·,··t ·· · ,· · ·'t······ ,·· ·,

c o :;

1\'1 E ... ~ C

! :! : 1

i + .!

1 2 -0 . _." .. ".j .. . " .. ... ..... : .. "" , .. " .. ... + .. " .. " .... -+ .. ,, .. · ·"··"I·~···"···+ ·"*·"·· -"l·"·· ··"--·+--"·" -·t·-······-.. j i r +

1 0.0-,, ··· ,, ···· +····· ·"· ···1" ··"· ·,,··+_··· ,,··,,+ ·- ·,-··,, ·i ·-···-··i,, -··· ·,,· ·i ,,-·,,-·" i""···· ··,,··i ,,·· ····,,·· ! + ! j X

, . j ~

•. O-- -+--I-~--+-- I --!= ~-r·-i-i-t-.-6.0- "·-···-"··+-"·-,,·· · i, ··,, ···"····i"·· ~ ······t· ·· " · " · i"·· · ,, · ·,, +··· ··,,· ·· ····i,, · ,,·· · ··'1"···"····1"···"· ' ·

',,' x ' i '0 4.01-----;'----~------r-----r-I----6rI2-----~I----6'r3-----r-I----6~14~--~ 59.5 60 60.5 61 61.5 62.5 63.5 64.5

Dynamic Shear Rheometer,C

FIg. 6. Results from the Hamburg Wheel-Tracking Device as a Function of Asphalt Cement

Stiffness as Measured by the Dynamic Shear Rheometer.

15

x Mix 1

+ Mix2

* Mix3

o Mix4

Page 22: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

3.4 Summary

Results shown in Table 5 indicate that aggregate differences can make a large difference in the

resuits. The better mixes, Mix 1 and Mix 2, had passing test results with many of the asphalt

cements used. For the poorer aggregates, virtually none of the samples tested passed,

regardless of the asphalt cement. However, there were a few asphalt cements that worked well

with the poor aggregates.

When a sample has greater than 20 mm of deformation before the entire 20,000 passes, the

failure is dramatic. This occurred only once each for the better mixes (Mix 1 and 2). For the

poorer aggregate, the dramatic failure occurred for almost half of the asphalt cements tested.

TableS. Comparison of Results By Mixture.

Mix Pass Fail

< 10 mm > 10 mm >20mm

1 6 4 1 .

2 5 5 1

3 1 9 4

4 2 8 4

Results from the Hamburg wheel-tracking device are significantly influenced by the aggregate.

When results from the device are unacceptable, making changes to the aggregate should be

considered. These changes might include limiting the amount of natural sands or using

aggregates without thick dust coatings.

Results in Table 6 indicate that the asphalt-aggregate interaction created because of varying the

refining' process or crude oil source used by the refinery may also influence the results from the

Hamburg wheel-tracking device. Some of the asphalt cements from a specific refinery and

refining process did not work with any of the aggregates (Refinery 8's Types 2 and 3 and Vn.)

while other asphalt cements worked with 3 of the 4 mixtures tested (Refinery A's Type 1 and

Refinery C's Type 2).

16

Page 23: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Table 6. Comparison of Results By Refinery.

I Ref. I T~e I Pass Fail

< 10 mm > 10 mm > 20 mm

A 1 3 1 0

2 2 2 1

3 1 3 0

B 1 2 2 0

2 0 4 3

3 0 4 0

C 1 2 2 1

2 3 1 0

D 1 1 3 3

Vn. 0 4 2

17

Page 24: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

4.0 Conclusions

The results of this study are based on the use of only four aggregates and the ten grading AC-1 0

asphalt cements provided by the refineries. It is known that there are more than four different

types of aggregate in Colorado, and it is likely that different asphalt cements could be used other

than those in this study. However, the conclusions are limited to the materials used.

1) The quality of aggregates have a significant influence on the test results from the Hamburg

wheel-tracking device. When results from the Hamburg wheel-tracking device indicate a mixture

is unacceptable, the aggregate quality should be investigated.

2) All of the refineries were able to produce an asphalt cement that performed well in the

Hamburg wheel-tracking device when using the better aggregates, except Refinery D. It appears

there may be a unique asphalt-aggregate interaction that is dependent on each asphalt cement

and each aggregate used in the mixture. The refining process and/or· crude oil source can

influence the results in the Hamburg wheel-tracking device.

3) Tests on the asphalt cement alone do not fully explain the adhesion between the asphalt

cement and aggregate in the presence of water. Some of the Types of asphalt cement tested

indicated the softer grading AC-10 asphalt cements did poorer than the stiffer grading AC-10

asphalt cements. However, there were numerous samples with very similar stiffnesses that

performed dramatically differently in the Hamburg wheel-tracking device. Although the stiffness

of the grading AC-10 asphalt cement may influence the results, the refining process or crude oil

source may also have a dramatic effect on the results from the Hamburg wheel-tracking device.

4) It is not justifiable to eliminate any refinery from selling asphalt cement in Colorado. Each

refinery (except Refinery D) was capable of producing an asphalt cement that gave acceptable

results on the Hamburg wheel-tracking device with the better aggregates. It should be noted that

Refinery D had one type and only four different aggregates were used in this study.

18

Page 25: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

5.0 Implementation

A repeatability study should be performed with the Hamburg wheel-tracking device. There are

numerous factors that can influence the test results, and we now have a better understanding of

many of the factors that can cause problems with repeatability. A detailed testing procedure

should be written and thEm a within-laboratory and between-laboratory study should be performed.

The completion of the repeatability study is necessary before any statewide implementation plan

for the Hamburg wheel-tracking device is developed.

6.0 References

1. Report on the 1990 European Asphalt Study Tour (June 1991), American Association of State Highway and Transportation Officials, Washington, D.C., 115+ pages.

2. Aschenbrener, T.B., R.L. Terrel, and RA Zamora (1994), "Comparison of the Hamburg Wheel-Tracking Device and the Environmental Conditioning System to Pavements of Known Stripping Performance,· Colorado Department of Transportation, CDOT­DTD-R-94-1,101pages.

3. Aschenbrener, T.B. (1992), "Comparison of Colorado Component Hot Mix Asphalt Materials with Some European Specifications," Colorado Department of Transportation, CDOT-DTD-R-92-14, 65 pages.

4. Aschenbrener, T.B. (1993), "1-70, Silverthorne to Copper Mountain: A Case History of the Use of European Testing Equipment," Colorado Department of Transportation, CDOT­DTD-R-93-19, 52 pages.

5. Aschenbrener, T.B., and Gray Currier (1993), "Influence of Testing Variables on the Results from the Hamburg Wheel-Tracking Device," Colorado Department of Transportation, CDOT-DTD-R-93-22, 116 pages.

6. Hines, Mickey (1991), "The Hamburg Wheel-Tracking Device," Proceedings of the Twenty­Eighth Paving and Transportation Conference, Civil Engineering Department, The University of New Mexico, Albuquerque, New Mexico.

19

Page 26: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Appendix A

Summary of Asphalt Cement Tests

Page 27: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Refinery A .

Aging Test Test Units Type Temp. of

DC Results 1 2 3 58-22 58-22 58-22

Sp.Gr. 25 1.028 1.029 1.024

Tank Flash . DC 230+ 230+ 230+

Ab.Vis. 60 poises 1300 940 1060

Pen 25 dmm 92 110 100

DSR 52 kPa 4.74 .3.34 3.75

58 kPa 2.21 1.54 1.74

64 kPa 1.00 0;67 0.74

LOH 163 % 0.16 0.13 0.10

TFOT Ab.Vis. 60 poises 3270 2180 2660

DSR 52 kPa 11.50 8.26 8.92

58 kPa 5.03 3.53 4.04

64 kPa 2.22 1.60 1.69

DSR 25 kPa 3280 1620

PAY 22 kPa 4620 2280 3540

19 kPa 6370 3224 4940

16 kPa 4450 6890

13 kPa 5950

BBR -12 MPa 159 139 145 Stiffness

(S) -18 MPa 704 673 655

BBR -12 0.33 0.34 0.34 Slope

(m) -18 . 0.22 0.25 0.23 rhe low temperature graolng WOUIO De loentlcal wnemer me lOW temperature stlnness (::i) or slope

(m) were used.

Al

Page 28: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Refinery B

Aging Test Test Units Type Temp. o!

°C Results 1 2 3 58-22 58-22 58-22

Sp.Gr. 25 1.031 1.026 1.035

Tank Flash °C 230+ 230+ 230+

Ab.Vis. 60 poises 1030 820 1060

Pen 25 dmm 105 128 103

DSR 52 kPa 3.43 2.72 3.78

58 kPa 1.57 1.24 1.68

64 kPa 0.73 0.59 0.77

LOH 163 % 0.15 0.16 0.12

TFOT Ab.Vis. 60 poises 2400 1780 2700

DSR 52 kPa 8.24 5.87 8.92

58 kPa 3.68 2.63 4.04

64 kPa 1.63 1.16 1.70

DSR 25 kPa 2560

PAY 22 kPa 3410 2750 3490

19 kPa 4840 4110 5100

16 kPa 6760 6150

13 kPa

BBR -12 MPa 155 149 164 Stiffness

(S) -18 MPa 692 611 738

BBR -12 0.35 0.39 0.36 Slope

(ni) -18 0.22 0.22 0.22

A2

Page 29: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Refinery C

Aging Test Test Units Type Temp. o!

DC Results 1 2 3 58-22 58-22

Sp.Gr. 25 1.027 1.000

Tank Flash DC 305 330

Ab.Vis. 60 poises 101'0 1000

Pen 25 dmm 100 90

DSR 52 kPa 3.50 3.74

58 kPa 1.57 1.73

64 kPa 0.68 0.74

LOH 163 % 0.18 0.01

TFOT Ab.Vis. 60 poises 2580 1940

DSR 52 kPa 8.65 7.42

58 kPa 3.83 3.17

64 kPa 1.69 1.36

DSR 25 kPa 4630 3540

PAY 22 kPa 4670 5150

19 kPa 6570

16 kPa

13 kPa

BBR . -1~ MPa 130 256 Stiffness

(S) -18 MPa 746 908

BBR -12 0.33 0.32 Slope (nil -18 0.23 0.20

A3

Page 30: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Refinery 0

Aging Test Test . Units Type Temp. of

DC Results 1 2 3 58-22

Sp.Gr. 25 0.994

Tank Flash DC 300+

Ab.Vis. 60 poises 1100

Pen 25 dmm 87

DSR 52 kPa 3.38

58 kPa 1.62

64 kPa 0.76

LOH 163 % 0.02

TFOT Ab.Vis. 60 poises 2020

DSR 52 kPa 6.38

58 kPa 2.92

64 kPa 1.34

DSR 25 kPa 2230

PAV 22 kPa 3340

19 kPa 5000

16 kPa 7000

13 kPa

BBR -12 MPa 245 Stiffness

(S) -18 MPa 1020

BBR -12 0.31 Slope (m) -18 0.18

A4

Page 31: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Refinery Vn.

Aging Test Test Units Type Temp. a!

DC Results 1 2 3 58-22

Sp.Gr. 25 1.013

Tank Flash DC 303

Ab.Vis. 60 poises 1040

Pen 25 dmm 129

DSR 52 kPa 3.16

58 kPa 1.49

64 kPa 0.70

LOH 163 % 0.18

TFOT Ab.Vis. 60 poises 2640

DSR 52 kPa 7.47

58 kPa 5.34

64 kPa 1.56

DSR 25 kPa 1480

PAY 22 kPa 2140

19 kPa 3050

16 kPa 4340

13 kPa 6050

BBR -12 MPa 96 Stiffness

(S) -18 MPa 561

BBR -12 0.37 Slope .

(m) -18 0.27

AS

Page 32: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

Appendix B

Summary of Hamburg Wheel-Tracking Results

Page 33: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

E E-" .9 m m !! <l.

.!; E ~

E ·x " ::Ii

E E-" .9 .. m !! <l. .!; E ~

E ·x " ::Ii

0 I'--

·2

·4

• 6'

·8

·10

·12

·14

·16

·18

·20 o

0 r--.. ·2

·4

·6

·8

·10

·12

·14

·16

·18

·20 o

2 4

.

.

2 4

Refinery A· Type 1· Mix 1 Temperature = 50C

........ "--.. ~

6 8 10 12

No. of Passes (Thousand.)

Refinery A· Type 1 • Mix 2 Temperature = 50C

-....-..... ""'-......

......

14

-----------

6 8 10 12

No. of Passes (Thousands)

B1

---

14

......... .............. ~

16 18 20

--..... ~

16 18 20

Page 34: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

E .E-c

.11 .. • !! Q.

S E

" .!; :I ~

E .E-c

.Q co co ! ... S E " E

" • :;

0 r--r--... -2

-4

-6

-8

-10

-12

-14

·16

-18

·20 o

0

·2

-4

·.8

·8

·10

-12

-14

-18

·18

·20 0

2

2

'"'

Refinery A - Type 1 - Mix 3 Temperalure = 50C

"-..

4

.

4

.~

8

~ ""-

. '" 8 10 12

No. of Passes (TlIou •• nda)

Refinery A - Type 1 - Mix 4 Temperalure = 50C .

8 8 10 12

No. of Passes . (Thou.anda)

B2

"'--~

""-14 18 18 20

14 18 18 20

Page 35: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

E .E-c .2 .. .. !! Q.

.E E ::I E ·x II ::;

E

0

-2

-4

-6

-8

-10

-u

-14

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o

-2

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!. ~6

c .Il -8 .. .. !! Q. -10 E

E -12 ::I

.§ :l ::;

-14

-16

-18

-20 o

2 4

2 4

Refinery A· Type 2 - Mix 1 Temperature = 50C

.

I----- r---... "'-

~

6 8 10 12

No. of Passes (Tbo".andB)

Refinery A· Type 2 • Mix 2 Temperature = 50C

14

......... ~

~

6 8 10 12 . 14

No. of Passes (Thousands)

B3

~ --A.. "-

16 18 20

....... ~

'---

16 18 20

Page 36: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

E E-" .!! .. .. ! <l.

E E :l E ~ ::;

E E-" _II .. I! <l.

E E :l E ·x • ::;

0

~ -2

-4

-6

-8

-10

-12

-14

-16

-18

-20 o 2

0

~ ...... -2

:4

-6

-8

-10

-12

-14

-16

-18

-20 o 2

'\t,

4

4

Refinery A - Type 2- Mix 3 Temperature = 50C

\ \

\1 -\

1\

8 8

~ ~

10 12

No. of Passes (Thousands)

RefinerY A - Type 2 - Mix 4 Temperature = 50C

----- r--... '-~

~ "-.....

14

6 8 10 12 14

No. of Passes (Thousande)

B4

16 18 20

~ "- .",

~

16 18 20

Page 37: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

E .s " .S! 0 0

!! Q.

1: E :J E .~

::;

E .s " .S! .. 0

!! Q.

1: E :J

E .~

::;

0

-2

-4

-6

-8

-10

-12

-14

-16

-18

·20 o

0

-2

-4

-6

-8

-10

-12

-14

-16

·18

-20 o

"---

2 4

2 4

Refinery A - Type 3 • Mix 2 Temperature = 50C

........... ~

" ""'~ ~

.~

~

6 8 10 12

No. of P .... e. (Thou •• nd.)

Refinery A· Type 3 • Mix 1 Temperature = 50C

~ I--

~

14

......... ~

6 8 10 12

No.ofP .... e. (Thousands)

85

14

16

16

~"-

r-----. ""

18 20

--............. ...............

18 20

Page 38: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

e: E-c .!I .. .. ! D. .!; E ::I

.~ ::;

e: E-c

.51 " " ! D.

.!; E ::I E ~ ::;

0

·2 I'--..... r--...

-4

·6

·8

·10

·12

·14

·16

·18

·20 o 2 · 4

0 r---. ~ ·2

·4

·6

·8

·10

·12

·14

·16

·18

·20 o 2 4

RefInery A· Type 3 • MIx 3 Temperature = ·50C

.........

----- --... r---... --~

6 8 10 12 14 16

No. ofPa .. e. (Thou.and_)

RefInery A· Type 3 • MIX 4 Temperature = 50C ..

"'-... . -....., G

'" I\., -...... ~

~ ~

18 20

. ~

6 8 10 12

No. of Pss8es (Thou.and_)

B6

14

" ~

'" 16 18 20

Page 39: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

E E. " .2 .. .. I! D.

.E E " E .~

:;

E

0

·2

·4

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·10

·12

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o

·2

-4

E. ·6

" .Q -8

~ a. -10 .E E ·12 " E .~ ·14 ::;

-16

-18

-20 o

2 4

2 4

Refinery B • Type 1 • Mix 1 Temperature = 50C

----~

6 8 10 12

No. of Passes (Thousa,nds)

Refinery B • Type 1 • Mix 2 Temperature = 50C

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Page 40: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 41: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 42: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 43: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 44: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 45: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 46: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 47: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 48: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 49: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 50: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 51: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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Page 52: Influence of Refining Processes and Crude Oil Sources Used ... · in Colorado that used various refining proce.~es and crude oil sources. TIle refining process and crude oil sources

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