Pet 364 Lab Manual (2)

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University of Alberta *

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Dec 6, 2023

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PETE 364 Drilling Engineering Laboratory Manual Course Instructor: Dr. ERGUN KURU Lab Instructors: Dr. Shanshan Yao Mr. John Czuroski School of Mining and Petroleum Engineering Civil and Environmental Engineering Department University of Alberta FALL 2023
PETE 364 Drilling Engineering Safety Manual School of Mining and Petroleum Engineering Civil and Environmental Engineering Department University of Alberta FALL 2021 Sanctioned by Environmental Health and Safety, U of A
Table of Contents 1. General Laboratory Safety Rules ............. cccccoouniinniiniiinicn 3 2. Specific Equipment Safety Information ........... ccccoevirvinne. 4 3:In'Caseof Emergemey. i R s ianiminis S BTN .- ieinoiisivienisdsssiusas snnnsods s R PRI I VIS IR EORIR SO AT NS S5 4N S 32 Eye Imjuries: e R S i s 5 3.3 EMCTEenCYSROWEE. ... ..c - csossouinssysmayssisssseri iionsiarons svsios 6 S RIrst AN o o R T O R R SRR 6 3.5 Campus Emergency Phone Numbers ............... c.ccooevveecninnne. 6 This manual is intended to make the students aware of safety concerns to themselves as well as to the equipment. Before using a certain apparatus the students must read the short section that applies to that apparatus. As well, the instructor will, where possible, demonstrate the equipment and mention the safety precautions. The instructor is to be listened to at all times. Do not undertake something unless the instructor has said it is permitted. Students will be expected to watch the Pet. E. 364 lab safety videos BEFORE attending the lab session. These should be available on eClass.
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General Laboratory Safety Rules 1. Lab coats and safety glasses must be worn and are the responsibility of the student. Hearing protection, gloves, dust masks, etc. (if necessary) will be provided. For hygiene reasons, the instructor will not hand out spare lab coats or safety glasses. No lab coat/safety glasses = no lab. 2. Be prepared. Read carefully and fully comprehend the laboratory manual for each test before beginning any experiment. If you do not understand the procedure, ask your instructor to explain it. 3. Think safety. No practical jokes or fooling around. 4. No food or beverages in the laboratory. 5. Keep noise to a minimum. Be considerate of the others working in your area. 6. Dress appropriately for lab work. No open-toed shoes. No loose fitting clothing. Shorts may not be worn in the labs. 7. Be aware of dangling jewelry or long hair that might get caught in equipment. Long hair should be tied back and jewelry removed. 8. Do not approach or touch any machine operator from behind while any equipment is in operation. 9. Gas cylinders are not to be operated by the student. 10. Materials and equipment may not be removed from the laboratory without proper authorization. 11. If you detect any equipment that appears to not function properly, DO NOT USE IT. Report it to the instructor. 12. Only authorized and trained persons are to use the laboratory equipment. 13. When finished working in the lab make sure that the lab equipment is returned to the proper place. Students must clean up all equipment properly before leaving or risk losing marks. 14. Report all accidents and injuries to the lab instructor, no matter how minor. 15. If you have any medical problems which could be potentially dangerous to yourself and/or others, report these to the laboratory instructor at the start of the lab. 16. Never work alone. All laboratory students must be supervised by the instructor. 17. Anyone under the influence of alcohol or other drugs will not be allowed in the lab. If necessary, this will be enforced with a call to Campus Security. 3
18. Any messes, wet or dry, must be cleaned up immediately, not left until the end of the lab. 19. Stay in the assigned work area. Do not wander around the lab “exploring” to see what is in other areas. 20. Mud/drilling fluid that is thicker than water is to be disposed of in the garbage cans, not the sinks. 1. Specific Equipment Safety Information Bentonite: This is the primary material used in making drilling fluid. Due to its powdery nature, students handling it MUST wear a dust mask (supplied to them) to avoid inhaling the dust that will diffuse into the air. When weighing the bentonite, be as close to the balance as possible and if any is spilled it must be cleaned up immediately. Mud Mixer: Be aware the mud mixer spins at very high RPMs. As such it creates a bit of a “wind” When adding the bentonite, wear the provided dust mask or this “wind” will send the powder into your face/lungs. When mixing the mud, add a bit of water, then a bit of bentonite and continue until done. Do not pour all the water and add all the bentonite at once. Do not go beyond medium speed or the mud will spill out. Fann VG Viscometer: The viscometer can operate at various RPMs, some of which could be considered quite high. Care should be taken in setting the RPMs. Filtration Apparatus: High pressure is required to operate this apparatus. The mud chamber contains a screen, filter paper and an O-ring (which must be put in a certain order) for proper sealing of the apparatus with the lid, which is connected to a gas cylinder. The chamber will be readied for you by the instructor, do not “play” with this and switch the parts around. The instructor will always check to make sure the chamber is OK and do not put mud into the chamber until the instructor has verified this. Once verification is complete, the instructor, and only the instructor, will attach the mud- filled chamber to the rest of the apparatus and tighten the top lid. Only the instructor will turn on the gas tank to activate the experiment. When the experiment is completed, notify the instructor who will then shut off the gas tank and bleed off the pressure safely.
5. Mud Retort: The mud retort is used to boil the mud so that water evaporates and later condenses into a small cylinder. Do not touch the retort while it is warming up or in operation. There is an extremely high risk of being severely burned. Also, take care in handling the glass cylinder, in case it breaks and causes a cut. 6. Chemicals and Other Substances: The following will be used in the lab at some point: Bentonite, Sepiolite, Xanthan gum, NaCl, Quik-Trol (a bio-polymer), Barafos (a polyphosphate), barite, lignite, Calcium oxide, caustic soda, phenolphthalein, sulfuric acid, Bromo Cresol Green Methyl Red. The “potential” harmful effects of each of these are too numerous and varied to mention here. If handled in a proper manner, safety would not be an issue. Any student wanting to know of the “potential” effects of these substances should consult the in-lab MSDS manual, available by asking the instructor. MSDS is an acronym for Material Safety Data Sheet. In Case of Emergency 3.1 Fire Any fire, no matter how small, can be potentially lethal. This is especially true in a laboratory setting, where toxic fumes may accompany smoke. In the event of fire: 1. Do not attempt to put out the fire. 2. Activate the nearest fire alarm. It is beside the double door entrance to 2-052, in the hallway. 3. All building occupants must exit the building when the fire alarm is activated. 4. Evacuate the building by the nearest and safest exit. DO NOT USE ELEVATORS. 5. Close doors to isolate the fire. 3.2 Eye Injuries Chemical spills or burns to the eyes are extremely serious. This lab has two eyewash stations. Their location will be indicated at the start of the term. An individual with an injury to the eyes may require assistance. If so, guide the casualty to the eyewash station and hold their head in position while the water is running. It may be necessary to pry the lids open. The eyes should be 5
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flushed thoroughly for several minutes, and professional medical attention should be provided immediately by proceeding to Campus Health in the Student Union Building, second floor. 3.3 Emergency Shower The lab also has an emergency shower. Its location will be indicated at the start of the term. 3.4 First Aid First aid kits are available in the lab should anyone have need of one. The instructor has taken first aid courses, though there is a limit to what he is capable of doing, physically and legally. If you require first aid, notify the instructor and he will assist to the best of his ability. 3.5 Campus Emergency Phone Numbers There is a phone (492-9207) in the lab, located on a desk by the double door entrance. EMERGENCY: phone: 911 (24 hrs) any life threatening emergency Campus Security: phone: 2-5050 (24 hrs) non-emergency situations Facilities Management: phone: 2-4833 (24 hrs) maintenance/building issues Civil Main Office: 7-207 ICE: phone: 2-4235 (8:30-4:30) general inquiries Environmental Health and Safety: phone: 2-4555 (8:00-5:00) general inquiries Near the in-lab phone is a green sheet of Emergency Information that summarizes much of the above. This sheet is also located beside the single door at the opposite end of the lab.
Guidelines for Petroleum Engineering Laboratory Reports {Revised JULY 2022) A report, especially one produced for a university course, is written for the purpose of conveying information. The information to be presented in these reports is intended to show: * An understanding of the underlying principles behind the experiment, and how the experiment tests them. % An ability to present this information in a manner such that it is clearly understood by the reader. As such, laboratory reports are expected to be written in a professional manner as befits a university student: (1) Text (and equations) must be typed, be in the past tense and be impersonal. That is, no “I’, “we”, “you”, etc. (2) Graphs must be done with software, not by hand, and be neat and large enough to be readable. (3)All information needed to write the report must be included in the report and not referred to as an outside source. Data tables from the lab manual, or the necessary portions of them, should be retyped, not photocopied, but must be included. This is not considered plagiarism. (4) Schematics (diagrams) of equipment must be neatly hand drawn, not photocopied from the lab manual or downloaded from the Internet. (5) Plagiarism, should it occur in any form (Internet, other students), will be dealt with according to its degree of severity. Report writing is an important aspect of the job of any engineer for accurately conveying the findings of a study. The report should read smoothly and in the past tense, as if it was prepared for a client or boss or instructor. Ensure proper spelling and grammar. Pages must be numbered. Title and number the tables/figures/graphs and refer to them in the text, by their titte/number and page number. Students are recommended to use the following section headings, the value of each section is indicated in parentheses. Each section should begin on a separate page.
1. Title Page (5) This page must include all of the following: course name and course number, experiment number and title of experiment, name of student, ID of student, group number (if there is one assigned by the instructor),date of experiment and date of submitted report. 2, Cover Letter (10) This is an executive summary (on the order of 1 page) and as such should summarize the entire experiment. It should be addressed properly (to the Course Instructor, Lab Instructor or Teaching Assistant by name), define briefly but exactly what was performed (do not to repeat the objective of section 3, below) and what was learned from it, include the sample name and the final (not raw, in-lab _data) numerical results. If necessary, these data can be tabuiated. A graph is only a pictorial representation of numerical data and, as such, should not be included in the cover letter. If it is necessary to include a graph for visual emphasis, present the numerical results with it. Be brief but specific, and include numbers where possible. For instance, do not say “high efficiencies were obtained” but “the measured efficiency was 72%”". There is no need for any amount of procedure, theory, etc. here, only to have that repeated later in those sections. That is, don’t write the entire report in the cover letter; avoid repetition. There must be a printed name and signature. This is the most important section. It conditions the attitude of the reader. When you are working for a living this might be the only part of the report which will be read by the people who matter. They do not want to search the entire report for key information, such as final results or the name of the sample. If they are curious and have the time or desire, then they might read further to see how the experiment was done (Procedure), what could have caused problems with the results (Analysis and Discussion), etc. 3. Objectives, Concepts and Theory (10) The Objectives are the intended outcomes of the experiment: what were expected to be achieved or learned and what was required to achieve that outcome. Concepts would include terms, definitions and some general background information necessary for the reader to understand the experiment. Theory describes the underlying science/engineering of the experiment. Equations used in the Results and Calculation section must be introduced and explained here. Define all symbols used and number the equations. The theory of how the equipment works (not how to use the equipment, as_in the Experimental Procedure) must be explained here. 2
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4. Experimental Procedure (10) Explain the experimental procedure to someone who was not in the lab in relatively simple words do not just repeat the steps indicated in the lab manual. The procedure should indicate to the reader the understanding of not only what was done but how and why it was done. Use simple hand drawn schematic diagrams, large enough to be readable and properly labeled, of the experimental apparatus used in the experiment. Do not photocopy the diagrams from the lab manual. A photograph of the equipment is not acceptable by itself but may be used if it complements the hand drawn sketch and must be the same as the apparatus used in the lab. Give such sketches as are necessary to define the experiment or to describe essential features of the apparatus. Do not waste time on artistic flourishes but produce sketches which befit an engineer. If necessary or possible, include significant dimensions, and identify/label the most important items of equipment. Describe the experimental procedure giving due prominence to those aspects which are crucial and omitting reference to those which could be regarded as self-evident to the reader (but do not assume him/her to be a petroleum engineer who has seen the particular equipment being used). 5. Results and Calculations (25) Results refer to the raw data that was acquired in the lab, and Calculations refer to the mathematical processing of these results and the final outcome. In general, it is best to present the results/calculations in tabulated form. As far as possible, present the raw data in addition to derived results; in this way conversion errors will not completely invalidate the report. Experimental accuracy and possible numerical errors should be stated, though not necessarily in a rigorous, mathematical nature. It is not necessary to be concerned with significant figures. Indicate all experimental conditions, tabulate the measured data, perform sample calculations, and plot graphs (if necessary) showing the calculated or interpreted results. Words must be used to explain the calculations so that they are more clearly understood. The reader should be able to “read” the calculations as easily as reading text and should not have to use a calculator to understand them. Ensure that the scale of any graph is such that the data of interest take up the major portion of the graph and that the graph is large enough to properly convey the information. Label each curve or axis on the graphs and include a legend.
6. Analysis and Discussion (25) The title means what it says, that is, Analyze and Discuss. Do not just repeat the numerical results, but they can be casually referred to. Indicate the assumptions made for interpreting the results, explain and justify differences between experimental and simulated results, if any, indicate and explain any data behavior that is expected or not expected, explain errors, limitations of the equipment, and provide advantages/disadvantages of experimental procedures used. Why/why not do the data look the way they do? First, note any interesting observations in the raw results trends, scatter, anomalies, etc. Then analyze the results in terms of the theory previously presented and discuss the outcome. Do not waste many words stating the obvious, but try to account for significant discrepancies. Try to do this specifically, if possible using numbers, and not by fuzzy arguments. Justify the analysis, that is, why was it done and what did it accomplish. 7. Conclusions and Improvements (10) This section should not be a repetition of the cover letter or of the Analysis and Discussion sections, but rather a summary of what was accomplished/learned from the lab (do not give numerical results) text only, no numbers or figures. It should partly be a refiection of the Objectives from part 3 above, that is, were the statements mentioned in the Objectives achieved? Indicate suggestions for improvements. Why are the improvements needed and how would their implementation affect the data taken in the lab or the outcome of the experiment? The conclusions should be numbered and be brief. In general, do not introduce new material in this section, that is, repetition of previous statements is encouraged.
8. References (5) Author’'s name, Title of Publication, Journal Year, Volume, and Page, as applicable. The link to the website if such a reference is used. Any other materials used, such as videos or conversations with other parties. Two final comments. (1) Though he may at times assist in the lab, the instructor is not to be mentioned in the report. Also, no other student in the group should be referred to. In other words, the work and the report was done by only one person. (2) Above all, READ and UNDERSTAND THOROUGHLY all of the information given to you (the Guidelines, lab manual, etc, If there are any questions, or for clarifications, the student should contact the lab instructor.
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Addendum to the Guidelines for Petroleum Engineering Reports Preface This document supplements the Guidelines for Petroleum Engineering Reports by making clearer what is required in each section. The Guidelines must still be followed. Note the following: 1. All of the report, including equations and calculations, must be typed. 2. All graphs must be done with EXCEL or some other graphing software, but not by hand. 3. The graphs and labels must be large enough for the reader to see the information conveyed clearly. A 1.0 mark will be deducted for each graph not deemed large enough. 4. All figures or diagrams of the equipment must be hand drawn, neat, and large enough to be readable. Any figure or diagram copied from the lab manual, or another source will have a 1.0 mark deducted for each infraction. If not neat enough, 0.5 will be deducted each time. 5. Each figure, diagram, table or graph must be labelled with a proper title and number. For example, Figure 1: The Idiosyncratic Discombobulator. Not labelling a figure, diagram, table, or graph will result in a loss of 1.0 mark each time. The label (title) can be either at the top or bottom. 6. These figures, diagrams or graphs must be referred to in the text, or 0.5 will be deducted each time. This is best done before the reader’s attention is drawn to them. The writer should say something like: “Refer to Figure 1 for a depiction of the Idiosyncratic Discombobulator.” Then start talking about the Idiosyncratic Discombobulator. It makes little sense to talk about an apparatus when the reader can’t see a depiction of it. 7. Spelling will be deducted 0.5 marks for each incorrect spelling (the same word misspelled several times, in the same way, is counted only once), up to a total of 5 marks maximum (10 misspellings). The marker will list these on the Title Page with the correct spelling, and this misspelling mark will be deducted from the total mark, not from each section. 8. Itis permissible (and it will be necessary) to take data from tables in the lab manual, but instead of ‘copying’ the entire table, just make a new table in the report with the needed data. 9. The section headings must be as indicated in the Guidelines, or 0.5 marks will be deducted each time. For example, the section is called Analysis and Discussion. There is not a section called Discussion, nor is there a section called Calculations and Analysis. Do not consider the lab report as just an “exercise” to be done as part of a course requirement. The lab report could also be considered as such: - Areport to your boss for a project he has asked you to do. - Areport to someone for whom you are doing a test and from whom you expect payment. In either case, the reader wants to find the proper information in the correct sections. He/she is a busy person who does not have the time to waste searching a multi-page report looking for the results he/she paid good money for you to supply. Neither does he/she want to pull out a calculator and go through the calculations to find the result when it was your job to supply that result. In either case, you would probably find yourself out of a job. It is best to learn and refine the techniques of report writing here. One final note: Students have been told, or should know, that they can always come to the lab instructor for help.
Title Page (5 marks): In the title page, put those items as mentioned in the Guidelines or fose 0.5 for each. For example, if you were taking Basket Weaving 101: Introduction to Making Baskets, Basket Weaving 101 is the course number, and Introduction to Making Baskets is the course name. The group number is that assigned to you (see the lab schedule) when you are in the lab and working with others and not that designated by Bear Tracks. The experiment's name is as in the lab manual, and any variation will have 0.5 marks deducted. Cover Letter (10 marks): If there is no address, 1.0 mark will be deducted. If the salutation or honorific is improper, 0.5 will be deducted. Either “Dear” or “To” is acceptable. Mr. (professor’s name) is not. DO NOT put the objectives (or a version of them) here, only to repeat them in the next section. Just state what was done/accomplished. For example: “In this experiment, three different types of baskets were made, using different materials such as straw, wire and plastic. The wire basket was determined to hold more weight before breaking than the other two types, 60 pounds versus 40 pounds for straw and 48.5 pounds for plastic.” In this case, straw, wire and plastic would be the names of the samples. No sample designation is deducted 1.0 marks. The weights they hold would be the numerical results. All of the final numerical results (as calculated in the Results and Calculations) section must be here. Up to 5.0 marks are given for these, and partial marks are given depending on how many of these results are missing, or if units are missing or wrong, etc. No marks will be deducted for calculation errors; that will be done in the Results and Calculations section. There must be a printed name and signature, or 1.0 mark will be deducted. If one of these is missing, 0.5 will be deducted. Objectives, Concepts, and Theory (10 marks): The objectives, worth 2.0 marks, must be at the start of this section, not elsewhere or lose 0.5 marks. They should be reflected in the Conclusions and Improvements section as having been achieved. Partial marks are awarded depending upon the strength of the objectives. In the basket weaving example, the objectives might be similar to this: “The objectives of this experiment were to learn the art/science of basket weaving and to make baskets out of different materials. Further, students will learn the use of different techniques or equipment to make these baskets and realize that these can make a difference in how the basket can be used and how much they can hold before breaking.” Concepts are worth up to 2.0 marks and are explained in the Guidelines. For the basket weaving example, a definition of what a basket is, what it is used for, and why it is necessary to use different materials would be a good beginning. More could be said, though. Theory is worth up to 6.0 marks and is explained in the Guidelines. Equations must be numbered or fose 1.0 mark total and thoroughly explained here before being used in the Results and Calculations section. Simply listing the equations without explaining what the symbols or equations mean is improper. One aspect of the theory might be that baskets are weaved because doing so makes the basket stronger, and different materials can affect this strength. Theoretical graphs or outcomes should be presented. Also includes the fundamental theory of the equipment. ii
Experimental Procedure (10 marks): A “procedure” that simply lists the steps performed in the lab is not correct and will result in no marks. Explain to the reader the how and why of each step to understand what was done. It will be necessary to use diagrams or figures of the equipment (refer to items 3 through 6 in the Preface section above) as a visual explanation. These diagrams/figures can appear either in the Theory section or the Procedure section since they will probably need to be discussed in both sections. For example, don’t say: “Valve one was opened, then valve 3 was opened.”, but “Valve one was opened so that the flow of gas could enter the Idiosyncratic Discombobulator from the main gas tank, and valve 3 was opened so that the gas could then enter the main chamber of the Discombobulator. Figure 1 shows the location of these valves.” The procedure is worth a maximum of 10 marks, and deductions are based on how complete this procedure is with regard to text and figures. If there are no figures or diagrams of the equipment, then 2.0 marks are deducted. Results and Calculations (25 marks): Present all of the in-lab results first before any calculations are done. These data must be organized in an ordered manner (a table, where convenient) and their meaning clearly explained. The reader must be able to understand what these data show, not have to guess. Up to 5.0 marks are given for this, less if some data are missing or units are not mentioned, etc. Calculations are to be in a logical order. Calculate a value first before using it in another equation. The calculations should be as readable as text, so use words to explain thoroughly what is being done. The reader/marker should not have to do the math to determine what is being calculated. Depending on this “readability,” up to 2.0 marks could be deducted. For example, don’t say: “xy/5x = 2.0” but say: “Since x =5 and y = 10, then from equation (6), xy/5x = (5x10)/(5x5) = 2.0.” A sample calculation must be shown for every unique calculation, or a deduction of 1.0 mark will occur each time. When all calculations are completed, a table should be made to show all the final calculations in one place. In most cases, graphs will be needed to display the calculated data. Failure to include a graph will lead to a deduction of 2.0 marks each time. Refer to steps 3 to 6 in the Preface section as well. Missing calculations will be deducted 1.0 mark each time. Wrong calculations will be deducted up to 2.0 marks each time, depending on their importance or severity, that is, how they impact the other calculations. Analysis and Discussion (25 marks): As it says in the Guidelines: “Analyze and Discuss”. Don’t state the obvious, be meaningful. For an example analysis, do not say: “The graph (see Figurel) of tachyon density is linear with respect to time.” That is obvious from anyone looking at the graph. What must be addressed is, why is it linear? A better analysis is to say: “The graph (see Figure 1) of tachyon density is linear (with negative slope) with time because as time increases, the number of tachyon particles spread further and further apart into larger and larger volumes; hence there are fewer tachyon particles per unit volume, which is the definition of density.” 11
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The discussion could be like: “One reason that the tachyon density is not as high as expected could be that the vacuum in the Idiosyncratic Discombobulator (1.D.) was not as high as it should have been. This may have been caused by a vacuum pump that was not working efficiently since it was noticed that the vacuum reading was only 22.5 inches of mercury and not closer to 29 inches that it should be if working properly. Tachyons need a strong vacuum if they are to form properly. There may have been a loose connection from the pump to the 1.D., thus preventing the vacuum pump from removing all the air, or which caused some of the room air to leak into the [.D..” Since there are essentially two sub-sections here, up to 12.5 marks will be given for the “analysis™ (technical/scientific/engineering explanation of the final results) and up to 12.5 marks will be given for the “discussion”(limitations of the equipment/method, advantages/disadvantages of the equipment/method, sources of potential error, etc.). Conclusions and Improvements (10 marks): Up to 7.0 marks will be given for the conclusions part, and up to 3.0 marks will be given for the improvements part. Referring to the basket weaving experiment, one conclusion might be that several different types of baskets were successfully made. Another could be that students learned how to use the equipment to make these baskets, whereas, before the lab, they had no understanding of this equipment. An improvement could be that different types of straw should have been used, instead of only one kind, to see if different types would hold more weight. Regardless, the improvement must be justified; that is, do not just say: “Different types of straw should have been used.” State why. References (5 marks): When referencing the lab manual. 0.5 marks will be deducted for each bit of missing information. For other references that should be there but are missing, 1.0 mark will be deducted. iv
Reference Material The lab manual should be read before the relevant experiments. Suggested textbook material includes: A- Mitchell, R.F., Miska, S. “Fundamentals of Drilling Engineering”, SPE Textbook Series,Vol 12., 2011 Chapter 3, pp. 87-138. B- American Petroleum Institute (API), “Recommended Practice for Field Testing Water-based Drilling Fluids,” ANSI/API 13B-1, 4™ Ed., March 2009. C- American Petroleum Institute (API), “Recommended Practice for Field Testing Qil-based Drilling Fluids,” ANSI/API 13B-2, 4" Ed., 2005. D- Darley H.C.H, and Gray G.R, “Composition and Properties of Drilling and Completion Fluids,” Gulf Professional Publishing, 5th Edition, 1988. Concept of This Laboratory Course All experiments will be tied together through the use of a single well. Through the use of offset data and knowledge gained in the lab, the students will be able to make recommendations on the mud program as the drilling progresses. These recommendations should include: the mud weight required, drilling precautions, and cost analysis of drilling mud. The well will be divided into three sections: surface, intermediate, and production. The surface section of the hole will deal with mud problems associated with unweighted mud. The determination of rheological properties and treatment of solids in an unweighted system will be addressed. The intermediate section of the hole will deal with problems associated with contaminates and weighted muds. The intrusion of salt and lost circulation will be addressed. The production section of the hole will deal with problems associated with inhibitive muds. Surface Hole In this section of the hole, the most common problems encountered are related to: 1) Highly unconsolidated formations 2) Poor circulation velocity 3) Weak formations 4) Shallow gas 5) Freshwater sands 6) High volume cuttings generation
With the exception of the freshwater sands, all of the areas of concern listed above relate to efficient hole cleaning and a soiids free system. Because of the large size holes, and the restrictive pump capacity, hole cleaning by normal circulation in insufficient. This, together with the limited capacity of the surface solids control system, results in a continuous degeneration of the mud due to solids buildup. Poor hole cleaning usually results in balled bit and assembly and thick, solids filled, wall cake. Both of these problems together cause tight hole, high swab and surge pressure, loss circulation, well kicks and stuck pipe. Stuck pipe is directly related to pressure differential, wall cake thickness and permeability and formation permeability. Because of this and the fact that fresh water sands are usually shallow makes the surface hole more prone to stuck pipe, even with unweighted muds. Water sands are more permeable to water and as such water base drilling fluids with poor filtrate control increase the susceptibility to stuck pipe. This increased permeability also increases the chances of loss circulation and damage to the fresh water sands. In the design of a mud system therefore emphasis must be placed on hole cleaning, solids control, mud weight and filtrate control. Mud System Design Hole Cleaning One of the important functions of the drilling fluid is to lift cuttings from the borehole. Failure to do this usually results in solids buildup, balling, reduced penetration, high torque and drag, stuck pipe, loss circulation, and fill on bottom. In order to effectively clean the hole the relative movement of the cuttings in the annulus must be in the upward direction. Because of the large size holes and limited pump capacity however, annular velocities are very low. In order to achieve a net upward movement, therefore, the slip velocity must be small. y _[33:5x(w,-w)xD*x¥ ] o [665xYPx(D,~D,)+PVxV | V.: Slip velocity, fi/sec W, . Density of cuttings, ppg W . Density of mud, ppg V. Average annular fluid velocity, ft/sec
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D: Average diameter of cuttings, inches YP: Yield point, Ib/100sq.ft PV : Plastic viscosity, cP D, : Bit size, inches D, : Outside diamete, inches From the above equation, slip velocity can be reduced by increasing the yield point or plastic viscosity in a fixed hole configuration where annular velocity, mud weight, cuttings size and density are constant. Increasing the annular velocity will increase the slip velocity because of the change in flow profile from plug to laminar. Figure 1: Effect of plastic viscosity (PV) to yield point (YP) ratio changes in flow profile. As shown in above figure, plug flow is best for cuttings removal. To achieve this however, the yield point must be raised to give a decreased value of PV/YP. Solids Control Solids control can be achieved chemically or mechanically. lonic inhibition, encapsulation inhibition, oil phase inhibition and deflocculation are ail chemical methods of solids control. Chemical control focuses prevention of cuttings dispersion but its physical removal is usually by mechanical means. Mechanical removal of cuttings is achieved by the use of shale shakers, desanders, desilters, centrifuges, settling tanks and water dilution. The efficiency of these methods of control reduces with increased plastic viscosity and gel strength. As such therefore it is advisable to also control both of these rheological properties.
Mud Weight and Filtrate Control With good solids control, and proper maintenance of commercial bentonite, these two properties can be effectively controlled. The maintenance of a proper commercial bentonite concentration can be achieved by performing the methylene blue test. Usually it is more prudent to use a pump and dump technique in the unweighted section of the hole. This usually results in cheaper and less troublesome control of drilled solids and rheological properties. To effectively train and familiarize the student with these problems and the design consideration needed for their alleviation, the following experiments are recommended. EXPERIMENTS No. 1 & 2 + Yield of Bentonite and Sepiolite Clays / Rheological Characterization of Water-based Drilling Fluids % Filtration Properties of Water-based Drilling Fluids Purpose: Experiment No. 1 is meant to familiarize the student with the rheological properties, behavior and application of both gels. Experiment No. 2 investigates the filtrate control properties of a simple gel and water system. Recommendation: A. Recommendation of type of clay and blend to be used for surface hole drilling. The foliowing points should be noted: l. Bentonite gives better filtrate control . Bentonite provide superior quality . Sepiolite is not affected by increase in salinity With reference to the study well, the salt formations are in the lower section of the well. In this case, therefore, it will more beneficial to drill with a bentonite system and achieve better filtrate control and wall cake quality across the shallower and lowered pressured formations. B. Addition of filtration control agent increases the cost but greatly reduces the cake thickness and water loss. Low values of water loss and cake thickness usually result in the following. I Thin cake, of 1/32 and less, constantly erodes under dynamic drilling conditions Il Low water loss associated with polymers results in higher mud viscosities. On completion of these two experiments the student is expected to acquire better understanding of drilling fluid rheology, yield point and fluid loss.
EXPERIMENT ONE PART 1:YIELD OF BENTONITE AND SEPIOLITE CLAYS PART 2: RHEOLOGICAL CHARACTERIZATION OF WATER-BASED DRILLING FLUIDS OBJECTIVES: In this lab session two different groups of experiments will be conducted to achieve the following objectives: 1) Determine the effect of clay concentration on drilling fluid viscosity for the two most common commercially available clays, bentonite and sepiolite. 2) Select the best model describing rheological behavior of water-based drilling fluids. Part 1 Yield of Bentonite and Sepiolite Clays Introduction Clay material is added to the drilling fluid to give certain characteristics that assist the mud to perform the functions described earlier. Generally two types of clay are used, montmorillonite clay used in fresh water, and attapulgite clay used in salt water. Sodium montmorilionite, commonly called bentonite or gel, is capable of swelling to approximately ten times its original volume when mixed with fresh water. Calcium montmorillonite, commonly called sub-bentonite will swell only 2-4 times its original volume when mixed with water. Montmorillonite clay has a mica-type crystal structure made up of a crystal lattice of silica and alumina as shown in the figure 1-a. The lattice is loosely bound with a cation such as sodium or calcium as in figure 1-b. In the presence of water the crystal lattice absorbs water allowing the crystal to swell. The covalent calcium ion holds the crystal lattice together tighter allowing less swelling. In this experiment bentonite and sepiolite will be used primarily to build viscosity. Figure 2 is a typical clay yield curve. The yield of clay in fresh water is defined as the number of barrels of 15 centipoise (cP) mud obtained from one ton of dry clay. The 15 cP is the apparent viscosity measured at 600 rpm (i.e. ©g00/2) using rotational viscometer. Notice that above 15 cP a small change in solids results in a significant change in the apparent viscosity of the mud. 10
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EXPERIMENTAL PROCEDURE 1. Calibrate the mud balance with tap water at room temperature. 2. Measure the viscosity of water at room temperature with the Marsh Funnel. Ideally, the Marsh funnel should require 26 seconds for 946 cc. (1 quart) of water to flow through it. 3. Mix three samples of mud using 4%, 7%, and 10% bentonite by weight in fresh water. Add the bentonite slowly, a_bit at a time, and definitely not all at once. Stir for 10 minutes at medium speed. If the speed is too high, the mud may spill out and result in a loss of sample. NOTE: All mud samples made are based on 350 cc. of water. By convention, the volume of water is to be measured when the bottom of the interface lies on top of the 350 cc. mark. 4. Measure the apparent viscosity of each bentonite sample at 600 rpm. 5. Measure the density of the 10% bentonite sample, ppg to 2 decimals, using the mud balance. Discard the three samples in the garbage cans, not the sink. 6. Mix three samples of drilling fluid using 4%, 7%, and 10% sepiolite by weight in fresh water. Use the same procedure as in step 3 above. 7. Measure the apparent viscosity of each sepiolite sample at 600 rpm. 8. Measure the density of the 10% sepiolite sample using the mud balance, ppg to 2 decimals. 9. Mix 15,000 mg/L NaCl solution by placing 15 grams of NaCl in a 1000 ml. container and filling with water to the 1000 ml. mark. Stir thoroughly. 10.Mix samples of (a) 7% bentonite and (b) 7% sepiolite (by weight) in 350 cc of the salt solution. Mix for 10 minutes at medium speed. 11.Measure the apparent viscosity of each sample in step 10 at 600 rpm. Lab Report and Data Reduction 1. Water properties Water Properties Density, ppg Funnel Viscosity, sec/qt. 1"
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2. Mud viscosities Apparent Viscosity, cP Fresh Water 15000 mg/L Brine CI‘?A,VV?IZ;‘Q":: b Bentonite Sepiolite Bentonite Sepiolite 4 N/A N/A T - ' 10 N/A N/A 3. Mud densities Mud Density, ppg 10 % Bentonite in Fresh water 10 % Sepiolite in Fresh Water 4. Plot apparent viscosity vs. clay content. Discuss swelling properties of bentonite and sepiolite. 5. Compare your results to Fig. 2. What is sepiolite? 6. Compute, mathematically, the yield of bentonite and sepiolite in fresh water (bbl / ton). 7. Graphically illustrate and discuss the effect of water salinity on viscosity and clay yield. AR, P v/ ' A5, 27 ,/////////////// -4 wNA* ,////////////// F1.1 ) Typical Berfonkto Pertite P ///////////// = " S FIG.1 b)Na montmorienite(efy 4 Camontmorerita(ight 4///////////// ,////////I/// Figure-1a, tb: Crystal Structure of Clay Minerals 12
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Weight in Pounds per Cubic Foot 637 675 71.2 750 87 82.5 86.2 Weight in Pounds per Gallon 85 90 95 100 105 1.0 115 12.0 60 l I > kS < £ T el i i z 3] b [¢] 50 o 2 ¢ g 1HEE ] s w = = kS o Q 3 = 3 t3 5] 4 3 2] (D‘Tf <) 'S 3 FH s B Q Q 40 b3 2 o W : I : s/ [ 2 a 3 - . l s / 9 €4 2 / / - ] | 2 / / SRRy / / (1 / /A / 10 / / v4 /’ 4 / L o 5 10 5 20 25 30 35 a0 a5 50 Percent Solids by Weight SPECIFIC GRAVITY OF SOLIOS = 24 200 10075 50 40 0 25 20 18 16 14 12 10 8 Yield (15 Centipoise Mud) in Barrels per Ton H 4 6 8 10 12 14 18 18 20 25 30 Percent Solids by Volume 10 20 30 40 50 75 100 150 200 250 Pounds Solids per Barrel of Mud Figure-2: Typical Clay Yield Curves (Gray and Darley, 1988) 13
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Part 2 Rheological Characterization of Water-based Drilling Fluids Introduction At a given temperature and pressure, fluids are characterized by: A) Their behavior under transient conditions, as manifested by their response time to changed conditions of flow B) Their behavior in laminar flow, characterized by their experimental flow curve or rheogram. The constant coefficients of the equation of flow represented by this curve are rheological parameters, specific to a particular fluid. C) Their behavior at rest, as manifested by gel formation after a certain period of time for thixotropic fluids. A fluid is thixotropic if: i-) It forms a gel after being shaken and left to stand ii-} It returns to its original condition after it has been shaken again. If the flow is laminar, the equation of flow relates the shear stress. t with the shear rate ,y. In laminar flow the fluid is sheared into laminar layers, parallel to the direction of flow, each layer moving at its specific velocity. A shear rate is, then, defined as: _dv_ _Velocity difference between two adjacent layers dY distance between the two layers %) The dimensional equation of y is: 1 L =T @) i.e., the dimension of y is an inverse time ( s1or 1/S) The shear stress is defined as the force per unit area of the laminar layer inducing the shear. The dimensional equation of tis: MLTZ _ pp-1 72 L2 3 14
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The shear stress, T, has the dimension of pressure. |t is often expressed in Ibf/100 ft 2 orin the Sl unit system in pascal (Pa). For a given shear rate, the apparent viscosity, u : is defined as follows: Pa=%‘ @) The dimensional description of pg is: MLIT2_ \p-1p-1 i (5) It is often expressed in centipoise, cP. The rheological models generally used by drilling engineers to approximate fluid behavior are: A. The Newtonian Model B. Non-Newtonian Fluids . The Bingham Plastic Model . The Power Law Model Rheological Models A. Newtonian Model: The shear stress of Newtonian fluids is directly proportional to the shear rate; if one variable is doubled, the other one is doubled also. The rheological equation is: =py (6) Examples of such fluids are water and gasoline. 15
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B. Non-Newtonian Fluids: Most drilling fluids are too complex to be characterized by a single value of viscosity. The apparent viscosity depends on the shear rate at which the measurement is made and the prior shear rate history of the fluid. Three-types of non-Newtonian fluids are most often encountered in drilling fluids and cement slurries: I. Bingham fluids . Power-Law fluids For Bingham plastic type fluids, the shear stress also varies linearly with shear rate but, unlike Newtonian fluids, a minimum force must be applied to impart motion to them. This force is known as the yield-point or yield value. The theoretical equation of flow behavior of such fluids is: T TotHpY ) 1 o = Yield point as yield value, 1bf/100 ft 2 Kp= Plastic Viscosity in cp Power law fluids, like Newtonian fluids, will flow under any applied stress, however small. But as distinct from Newtonian fluids, the shear stress is not proportional to the shear rate, but to its nth power. Therefore, these type of fluids are called as power law fluids. The equation of flow behavior is: Tt =KyN 8) where K = Consistency Index, Ibf-s/100 ft2 n = Flow behavior index, dimensionless T 1 2 3 1. Bingham Plastic Fluid 2. Power Law Fluid 3. Newtonian Fluid 16
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Determination of Flow Behavior Model Parameters Using a Rotational Viscometer: Rotational viscometers are used in the standard API diagnostic tests to determine flow behavior model parameters of drilling fluids. These determinations are carried out in a 6 Speed Fann Viscometer according to APl RP13B. Fann Viscometer readings can be correlated to the shear stress and shear rate as follows. Shear Stress: t =1.0676 9) where 6 : Dial (viscometer) reading corresponding to the applied shear rate (i.e. rotating speed) Shear Rate: y =1.703 N (10) N : Viscometer rotating speed, RPM Flow behavior parameters can be determined by using Fann Viscometer readings as follows ; Plastic Viscosity (PV): L p=9600-9300: cP. (11) 8 o0 = Fann Reading at 600 rpm 8 300 = Fann Reading at 300 rpm Yield-point (YP): To=8a00 - e, Ibf/100 ft 2 (12) [¢] 300 p _ 0 600 Flow Behavior Index (n): n=3.32log —= (13) 300 510 6 Consistency Index (K): K = (51—1),, , equivalent cP. (14) Apparent Viscosity: The apparent viscosity, p 5, of drilling fluids and cement slurries is to be determined, in accordance with APl standard. If u 4 is expressed in centipoises: (15) HéOO o 17
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Gel Strength: Thixotropy (i.e. change in rheological behavior as a function of time) can be estimated by observing the changes in strength taking place in a gel as function of time. According to APl RP 13 B, two values, the 10 second gel-strength and the 10 minute gel-strength, are determined in 6-speed Fann Viscometer. The rotor is run at 600 rpm for 30 sec. then, the motor is stopped for 10 sec., and after 10 sec. have elapsed, the rotor is run at 3 rpm speed and the corresponding scale deflection is noted as 10 sec. gel-strength, in Ibf/100 ft 2. A period of 10 min. is allowed to elapse without disturbing the mud, and the operation is repeated. The maximum scale deflection is equal to the 10 minute gel-strength in Ibf/100 ft 2 Selection of Model The rheological model chosen will be a) Closest to the Bingham model, or b) Closest to the Power-Law model In most cases it is impossible to make this choice on the shape of the curve alone, whether plotted in Cartesian or in Logarithmic Coordinates. A 6 speed Fann Viscometer provides only 4 experimental points because the readings at 3 and 6 rpm cannot be used if the fluid has a yield point (plug flow) or if it is thixotropic. The four experimental points may be used for linear regression, in Cartesian and in logarithmic coordinates corresponding to Bingham Plastic model and Power Law model respectively. The model with correlation coefficient closest to unity will be chosen for subsequent calculation. This correlation coefficient is given by the following equation: = PZxy-Zx Xy Y[pzx2-(zx2][Pzy2-(2y?] (16) where , P is the number of Fann readings made x is the shear rate or its logarithm ( y or logy) y is the shear stress or its logarithm ( z or log ) 18
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EXPERIMENTAL PROCEDURE 1. Calibrate the mud balance with tap water at room temperature. 2. Place 350 mi. of water in the blender can, a little at a time to avoid spillage while mixing. NOTE: All mud samples made are based on 350 cc. of water. By convention, the volume of water is to be measured when the bottom of the interface lies on top of the 350 cc. mark. 3. Add 30 grams of bentonite while mixing. Add the bentonite slowly, a bit at a time, and definitely not all at once. Stir for 5 minutes at medium speed. If the speed is too high, the mud may spill out and result in a loss of sample. 4. Record the mud temperature. 5. Measure the mud density using the mud balance, ppg to 2 decimals, SG {gm/cc) to 3 decimals. 6. Place the mud in a Fann Viscometer, measure and record the 600, 300, 200, 100, and 6 rpm readings. Note that at 6 rpm the reading could be higher than it should be because of the effect of “gelling”, whereby the rpm’s aren't powerful enough to put the mud into a liquid state. Discard this value if the mud appears to gel, use this value only if it enhances the data. 7. Determine the 10 second and 10 minute gel strengths. Remember, gel strength readings are taken at 3 rpm’s. Refer to top of page 18 for information on how to perform a gel strength. 8. Repeat steps 1 to 7 using 3 grams of Xanthan Gum instead of bentonite as a viscosifier. Lab Report and Data Reduction 1) Plot the rheograms of Bentonite and Xanthan Gum solutions (i.e. shear stress vs. shear rate diagrams) 2) Select the model which fits closest to the rheological behaviors of Bentonite and XG solutions 3) Determine the flow behavior parameters of the models selected at step 2. 19
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EXPERIMENT TWO FILTRATION PROPERTIES OF WATER-BASED DRILLING FLUIDS OBJECTIVES: Determine the effect of clay and water soluble polymers on (API) filtration loss characteristics of water- based drilling fluids. INTRODUCTION One of the most important functions of the drilling fluid is to "control filtrate loss into the formation". This is important for several reasons: 1. The Filtrate lost to the formation must be made up at the surface to maintain the desired mud volume. 2. The filtrate lost to the formation will affect the logs obtained after the hole is drilled. For example, the filtrate can flush hydrocarbons from the rock changing the in-situ saturations and changing the resistivity of the formation water near the well bore. 3. The filtrate lost to the formation can react with clays in the formation rock and cause irreversible formation damage near the well bore. This is referred to as "skin effect” when the permeability next to the well bore is reduced to a very low value compared to the rest of the reservoir. 4. The filtrate lost to the formation leaves the solid portion of the mud behind, deposited on the wall of the hole. This deposit can become sufficiently thick to stick the drill string or casing. When the mud system is circulating (dynamic filtration) the mud cake tends to wash away and is not as big a problem as when circulation is stopped (static filtration). In this experiment you will investigate static filtration using a standard API filter press with a filtrate area equal to 45.8 cm”. Specifically you will investigate the effect of time on filtrate loss and filter cake thickness. You will also observe several methods used in the field to control filtrate loss. Consider a unit volume of mud that contains x fraction of filtrate. The volume of non-filtrate that will be deposited against the side of the hole is then equal to (1-x). Therefore if V. is the volume of filter cake and Vi is the volume of filtrate; 2.1) = e 20
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If the filter cake is deposited on a unit area then the thickness of the cake (h) after time period (t) is equal to; 2.2) h = - Vi where V; is the volume of filtrate that is filtered through a unit area. Darcy's law states that; dvi kAP (2.3) e dt uh where: k = permeability in darcies AP = differential pressure in atm n = viscosity of filtrate in cP h = cake thickness in mm Substituting Equation (2.2) into Equation (2.3), separating variables and performing the integration; kAP x 24) = e () t 2 po 1x Solving for the volume of filtrate per unit area as a function of time; (2.5) Vi =B (1)"? 2 kAPx where B=[-meomeeee ]1/2 r(1-x) This states that the filtrate that flows through the filter cake is proportional to the square root of time. You should notice that the terms in (B) are not time dependent. The term k is controlied by the size distribution and type of material in the non filtrate portion of the mud. The relationship between pressure and filtrate volume is not as easily defined as the relationship between filtrate volume and time. However it can be stated that the filtrate volume is proportional to the pressure raised to some power, i.e., 21
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(2.6) Vy is proportional to Notice that y cannot have a value greater than 0.5. For example, if the filter cake is non-compressible, i.e., k remains constant for any pressure, then y is equal to 0.5 as predicted by Equation (3.5). On the other hand, if the filter cake is compressible, which is usually the case, then k will decrease with an increase in P and the final result will be that y is less than 0.5. In a severe case y can have a negative value. AP Filtrate Loss is defined as the volume of filtrate collected in 30 minutes from a standard filter press when a pressure of one hundred psi is applied. Spurt Loss is the amount of filtrate volume at time zero. EXPERIMENTAL PROCEDURE 1. Mix the following samples using tap water and stir for 10 minutes at medium speed. NOTE: All mud samples made are based on 350 cc. of water. By convention, the volume of water is_to be measured when the bottom of the interface lies on top of the 350 cc. mark. Add the bentonite slowly, a bit at a time, and definitely not all at once. 6% bentonite by weight 6% sepiolite by weight 9% bentonite by weight 9% bentonite by weight plus 1 Ibm/bbl bio-polymer (QUIK-TROL) 9% bentonite by weight plus 6 Ibm/bbl polyphosphate (BARAFOS) See step 3 below ~poooow Note that when making 350 cc. of mud, 1 Ibm/bbl is equal to 1 gram. 2. Measure the filtrate volume versus time at 100 psig of the samples (a) to (e) above. After the filtration test, which lasts for 30 minutes, measure the mud cake thickness of these 5 samples. The thickness must be reported as 32nds of an inch. Take more than one reading and average them. 3. Make another sample just like that in (1e) above. Measure the filtrate volume at 50 psig, and the mud cake thickness. 22
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DATA REDUCTION AND LAB REPORT 1. Plot filtrate volume (measured at 100 psi) of all 5 samples on the same graph paper versus time and versus square root of time. Does the theoretical relationship of filtrate volume proportional to the square root of time hold? 2. Calculate spurt foss using 7.5 min. and 30 min. data. Determine AP| water loss and mud cake thickness for each sample and display the results in a table. 3. Discuss the effectiveness of bentonite, sepiolite, bio-polymer and polyphosphate as filtration control additives. Also discuss the type of mud cake observed for each additive. 4. What value of "y" (Equation 2.6) did you obtain for your polyphosphate mud system? Explain how you obtained the value of "y" and what the physical significance of the number is. Time VTime Filtrate Volume, m! 6% 6% 9% 9% 9% 9% i i Bentonite Sepiolite Bentonite | Bentonite + | Bentonite + | Bentonite+ Quik-Trol Barafos Barafos @ 50 psi 0.25 1 2 3 4 5 6 7.5 10 20 30 23
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THE INTERMEDIATE HOLE Experiments 3 and 4 pertain to the drilling fluid design for intermediate hole. In Experiment 3, the student will study preparation and solids analysis of weighted mud systems. In Experiment 4, the students will learn about identification and treatment of salt contaminated muds. WEIGHTING UP MUD: Solids in weighted mud systems When weighting up a drilling fluid one should be able to calculate the following: a-) The volume increase due to barite addition without water addition. b-) The weight of barite necessary for a particular change in weight without water addition. ¢-) The volume to be discarded due to volume increase when adding barite with water. d-) The weight of barite necessary for a particular change in weight with water addition. e-) The volume of water to be added with the barite (0.01 gal/lbm). The equations to be used for these calculations are as follows: Volume Increase Due To Barite Addition Without Water Addition: dV = Vi* [ (35 - Dom) / (35- Dim) -11 (1) Weight of Barite Required For Weighting Up Without Water Addition: Mp=dV * 1470 2 Volume of Mud To Be Discarded Before Weighting Up With Water Addition: Discarded volume = V4 = V; * [1 -(28.0856 -Dpy) / (28.0856 -Dom)] (3) Weight of Barite Required For Weighting With Water Addition: Mpw= Vg * 1088.89 4) Volume of Water to Be Added With Barite Addition: V= Mp* 0.01 (5) dV = Change in volume due to dry barite addition (bbls) Vi = Initial volume (bbls) Dom = Old mud weight (ppg) Dnm = New mud weight (ppg) Mp = Barite required without water Msw = Barite required with water addition Vi = Volume of water required, gal. 24
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Table 1: Barite Required to Raise Weight of 100 Barrels of Mud for Different Mud Weights. BARITE REQUIRED TO RAISE WEIGHT OF 100 BARRELS OF MUD (number of 100 Ib socks) DESIRED MUD WEIGHT (ppg) 8.0 8.5 | 9.0 9.5]10.0}10.5{11.0 | 11.5| 12,0] 12.5{ 13.0] 13.5| 1n.0] 14.5] 15.0 }15.5 }16.0 |16.5 [17.0 7.5 |18.0 35 ) 6u 9 | 125) 1090 1ot 231 ] 271 313] 3577 4os| wssi 509 s67 | 6304 (27 | 720 1 g9 | 93n jozs ii3p Il 7.35 - |28 57 871 120 154 190 | 228] 269] 312| 358| 407{ ue0| S16| 5761 641 | 212 | 788 | 872 | 962 11052 8.0 g 28 S8 90f 123 1584 196] 235| 77| 322| 370 21| 76| 5351 509 | 667 [ 7u2 | 823 | 912 |ioos 8.5 17 4r] 78| 111 w6 ) 183| 222f 26u) 308y 355) 406| w60 | 519 582 | 650 ) 723 | 804 [891 |98 || 87 29) 60| 92| 127 { 163) 202 2u3] 286) 333 383 436 | 49u | 5% | 623 | 696 | 725 [ 861 [ ase || 9.0 30y 621 95| 130; 168; 208) 251| 2964 3u5| 397 | 453 | 513 | 578 | 649 | 226 | 810 | 903 i 9.5 31| 63 98| 34| 173 215} 259 306| 3571 412 [ 420 [ S34 | 603 | 678 | 760 { 850 [10.0 32 65) 101] 139| 19| 222| 268| 317 370 | u2s | wse | 567 [ 629 {708 [ 796 {10.5 330 67 dou| 1u3) 15| 230) 28| 329 | 385 | wes | s10 | 581 {ess {73 [11.0 values not Listed tn the table con be 30 69| 107( 148| 19)| 238 | 288 | 3u2 | uoo { usu | 533 | 608 | 690 |{11. = |2 comouted using the followlng equation: . ¥ 35 72| 111} 153} 198 | 247 299 | 356 | 417 | wau_[ 557 | 637 112.0 ;g_g A = 1099 X MUD WT. [NCREASE se| 2l 11| is9| 206§ 257 | su {3 Juse |sos | smw f1os |E n B 37 77| 118 165 | 2tu [ 267 | 325 | 387 [4s6 | s31 [|13.0 Q = 28.35 - N & EW MUD 4. 38 91 123 | 170 | 222 | 278 | 339 [u0S | 478 |[13.S ’?‘0*5 = AsB uo ) 82 | 128 | 17 | 232 | 291 | 355 | w5 |1w0 ul 86 | 133 | 186 | 242 {304 | 372 [14.5 The above equation and the values In the table are based H 89 | 139 119 1255 |31 fi1b.0 on the ossumption that one gatlon of woter will be odued 4o | 93 | 145 1203 | 265 11155 with each seck (100 Ib) of borite used in welghting up. a6 97 |15 | 212 [16.0 48 1101 | 199 i16.5 Total Mud Volume Increase bbl S1 | 106 11170 (0.091 x Total Sacks of Barite Required) 53 jj1.s _J A common problem with intermediate weight muds, especially in the 12 to 13 ppg range, is differential sticking, lost returns, and high treating costs. Most often these problems can be traced back to excess solids. Solids are difficult to control in intermediate weight muds because of a lack of mechanical equipment. Desanders, desilters and shale shakers are used to remove unwanted drill solids from low weight muds (muds that contain no barite). Solids control in weighted muds is achieved by the use of centrifuges and fine screen shale shakers. There is no mechanical equipment available for removing solids from intermediate muds (10-13 ppg) other than shale shakers. Consequently, the mud used to drill this section of the well is difficult to control and excessive chemicals and/or dilution will be used. In addition, this mud is 25
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usually used as a base for higher weight muds used to drill the remainder of the well after protection pipe is set. Use of a poor base mud to build a weighted system will increase treating costs and may contribute to other problems such as lost returns, stuck pipe, etc. Sand and drill solids greatly affect the lubricity of both the fluid and the wall cake. This in turn seriously affects the torque and drag of the pipe in the hole. The type of solids and the abrasiveness of the solids in the filter cake are also important factors here since the coefficient of friction of the filter cake severely affects the force required to move the pipe on its surface. The overpull required to move the pipe can be calculated with the following equation: Overpull (Ibf) = Differential Pressure (psi)* Area (in2)* Coefficient of Friction 6) F" R R e ) d Wellbore Resenvolt Pressure Figure 1: Differential sticking (Schlumberger Oilfield Glossary Website & Scribd Website) For a fixed differential the over pull required to move the pipe is directly proportional to both the contact area and the coefficient of friction. The contact area increases with an increase in filter cake thickness. The coefficient of friction changes with the lubricity of the fluid and the abrasiveness of the solids making up the wall cake. For example assuming a 400 psi differential pressure across a 10 ft. permeable section in a 9-7/8 inch hole with 7-1/4 inch drill collars the over pull required for different wall cake thickness, using the above equation are: 26
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For a cake thickness of 2/32" The over pull at .2 coefficient of friction = 27,456 Lbs The over pull at .4 coefficient of friction = 54,912 Lbs For a cake thickness of 1/8" The over pull at .2 coefficient of friction = 35,616 Lbs The over pull at .4 coefficient of friction = 71,232 Lbs For a cake thickness of 1/4" The over pull at .2 coefficient of friction = 50,592 Lbs The over pull at .4 coefficient of friction = 101,184 Lbs For a cake thickness of 1/2" The over pull at .2 coefficient of friction = 72,288 Lbs The over pull at .4 coefficient of friction = 144,576 Lbs For a cake thickness of 1" The over pull at .2 coefficient of friction = 104,640 Lbs The over pull at .4 coefficient of friction = 209,280 .Lbs SOLIDS BUILDUP EFFECTS AND ANALYSIS In a mud system there are several different types of solids present. These are salts, commercial clays, weighting material and drill solids. When active clays are drilled they become dispersed in the mud causing an increase in the solids, plastic viscosity, yield point, gels and mud weight. Evaluation of the percent solids in the system can be achieved by performing a retort analysis. Evaluation of the concentration of commercial bentonite can be achieved by performing a methylene blue test. A high MBT can signify a high concentration of active clays. It also can still be associated with other contaminants such as brine, cement or lime, hydrogen sulphide and carbon dioxide. The key however, lies in the fact that other chemical contaminations will not increase the solids content and plastic viscosity. The MBT test is used to confirm that the increase in solids is due to active clays. Inert drill solids cause an increase in plastic viscosity, water loss, total solids and mud weight. An increase in the yield point is associated with either high temperature or chemical action. Based on this any increase in plastic viscosity, mud weight, solids and fluid loss without an increase in yield point can be safely attributed to a buildup of inert drill solids. An accompanying increase in yield point signifies the presence of a chemical or temperature problem. Flow line temperatures are readily available and can be checked at any time. Usually drill solids will cause an increase in the plastic viscosity due to the increased number of free particles. This increase in plastic viscosity 'will result in greater annular pressure losses, greater equivalent circulating densities, loss circulation and decreased drilling rate. For most bit conditions, when all other parameters are held constant, the penetration rate varies to the 0.45 power of the Reynold's Number. This can be stated as follows: 27
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New drilling rate = Old drilling rate * (New Re/Old Re)*** (7) But the Reynold's Number is indirectly proportional to plastic viscosity (PV) resulting in the following: New drilling rate = OId drilling rate * (Old PV/New PV)**° (8) The following graph shows the effect of PV (cp) on the drilling rate (ft/hr). Here we can see the decrease in drilling rate with the increase in PV. Drilling rate vs Plastic viscosity 120 115 110 1 - - - E L . = 105 1 te in Dril w (4] 20 25 30 35 40 Plastic viscosity Figure 2: Drilling rate vs. Plastic Viscosity A buildup of solids in intermediate weight muds is almost unavoidable with the present mechanical equipment and some dilution is necessary. Desanders and desilters generally cannot be used because of the loss of almost all barite. Centrifuges will salvage most of the barite but they have limited capacity and cannot process sufficient volume to keep up. If mud is to be used as a base for building higher weight muds, then reducing drill solids is a must. Do not attempt to treat a solids problem with chemical. Consider the use of two centrifuges if a significant amount of hole is to be drilled with an 11 to 13 Ib/gal mud. Screen all of the returns through an 80 mesh screen. Install two shakers if one will not handle the volume. Use dilution if necessary to keep the drill solids at an acceptable level. Do not build a weighted system on a poor base. 28
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EXPERIMENT THREE MUD WEIGHT - WEIGHT CONTROL - SOLIDS DETERMINATION OBJECTIVES: » Introduce the concept of drilling fluid weight control. » Determine the effect of barite on the rheological properties of water base drilling fluids. » Determine solid content of the drilling fluid using API retort test. INTRODUCTION A primary function of the drilling fluid is to control, or hold back, the formation pressure while you are drilling the wellbore. This is accomplished by adjusting the specific gravity of the drilling fluid so the pressure gradient of the drilling fluid within the wellbore exceeds the pressure gradient of the fluid in the formation. The specific gravity of the drilling fluid is increased by adding solids to the drilling fluid. The rheology of drilling fluid must be such that the solids will be held in suspension. Two major considerations occur as the specific gravity of the drilling fluid is increased. The first consideration is that the pressure gradient in the wellbore not exceeds the fracture gradient of the formation. The second consideration is how the solids added to the drilling fluid effect the rheology and filtrate properties of the drilling fluid. The surface area of the solids in the drilling fluid has a major effect on the viscosity of the drilling fluid. Consequently, when increasing the specific gravity of the drilling fluid, the denser the solids added, the smaller the rheology change observed. For this reason, barite (sp.gr. 4.2) is preferred to increase the specific gravity of drilling fluid instead of the drill cuttings (sp. gr. 2.65). Mud that contains barite is referred to as weighted mud and mud that does not contain barite is referred to as low weight mud. The solids content of low weight mud can be determined directly from the mud weight without using a mud retort provided there is no oil in the mud system. To determine the solids content of weighted mud, a retort analysis is always required unless no low solids are present, which is seldom the case. In figure 1, you will find a nomograph that will assist you in determining the percentage of low solids and the percentage of high solids in a weighted mud. 29
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EXPERIMENTAL PROCEDURE 1. Put 350 cc. of water in your container, a bit at a time. 2. Add bentonite (a bit at a time) to the water according to the values in Table 1, page 33 (a new mud each time) and mix for 7 minutes. Record the 600 RPM and the 300RPM reading until apparent viscosity (Ja which is Qgp0/2), reaches a value between 15 and 20. 3. Only measure the mud weight and 10 second gel strength when Ogg0/2 reaches the above value. 4. The 600 and 300 rpm viscometer readings are needed to calculate PV and YP. 5. Estimate and record the amount of barite (in grams) that should be added to your mud to increase the density to 9.5 ppg. Use the table named “Barite Required to Raise Weight of 100 Barrels of Mud” (page25). In the report, calculate the exact amount from first principles. 6. Add the estimated barite to your mud (an entirely new sample), mix for 10 minutes and measure the mud weight. The mud weight should be very close to 9.5 ppg. 7. Measure the 10 second gel strength. 8. Record the 300 and 600 RPM viscometer readings to calculate PV and YP. 9. Use the mud retort to determine the low solids and high solids concentration. Apply the following procedure: a) Disassemble retort assembly and fill sample cup almost level full of the fluid to be tested. Put sample cup cover in place firmly, squeezing out excess fluid to obtain the exact 10 cc volume required. Clean spill over from cover and threads. (If threads are coated with silicone grease, it will prevent sticking.) b) Lift cover slightly and slide off so that fluid adhering to bottom surface will be scraped back into the sample cup. c) To prevent boil over, fill the expansion chamber with “steel wool". d) Select correct heater assembly for the available voltage and screw into top of expansion chamber. Keep assembly upright so that mud does not slosh into the drain tube. e) Insert drain tube into hole at the end of condenser, seating firmly. Percentage graduated cylinder should be clipped in place to catch condensate. 30
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9 h) ) 10. Plug in the correct connector cord to the power supply and keep power on until distillation stops which should occur in 15 to 25 minutes depending on the characteristics of solids content and the atmosphere around the unit. Read the amount of water directly from the graduated cylinder. At end of test, grasp rubber covered connector just above heater and separate retort assembly from condenser. Handling the hot retort by means of the connector cord, dip in water to cool. (Piug is waterproof and may be immersed completely.) Most of the solids remaining in retort will adhere to the heater where removal is easy. Use spatula to scrape out cup and expansion chamber. Run short length of pipe cleaner through condenser hole and retort drain tube to remove oil residue. The specific gravity of mud solids can be obtained by the following formulas. Sp.Gr.Solids = [ 100*Sp.Gr.Mud - (vol%water) ]/ (vol%solids) Sp.Gr.Mud = MW(ppg)/8.33 or Sp.Gr.Mud = MW(Ibm per cuft)/62.4 All percentages are volume percentages. Enter Fig.1 (page 32) from y axis with Sp.Gr. of Solids and read the weight % of high gravity solids and calculate weight % of low gravity solids (100 Weight % of High Gravity Solids). DATA REDUCTION AND LAB REPORT 1. 2. Discuss the effect of adding barite on drilling fluid properties measured. Discuss your results from retort analysis (i.e.), compare your retort analysis results and recorded barite and bentonite amounts obtained during the preparation of 9.5 ppg mud. Soive the following field problem: Surface casing 13 3/8", 72 Ib/ft (ID: 12.347 in.), set at 3,000’ Open hole 11" at a measured depth 8,000’ Three mud tanks each has 8' depth * 8' width * 10’ length full of mud. The drill string at total depth) DP 4 1/2", 20 Ib/ft, (ID: 3.64”) DC 7" x 3.5", 98 Ib/ft, 500' 31
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Questions: 1. Determine the total volume of mud in the system (i.e., mud in tank + mud in well). 2. How many bbls of fluid must enter the wellbore from the formation to increase the level of fluid in mud tanks (pits) by 2"? 3. You are the engineer in charge of this drilling rig. You have sent the mud engineer to town for a brown pop. He wrecked the pickup so he will not be back to help you. While you were taking your afternoon nap the mud got into the shape found in step 2 above. The tool pusher has just awakened you and informed you the well is kicking and the mud weight should immediately be increased to 10.5 ppg. Calculate the number of sacks of (100 Ibm) barite required to change the mud system. 43 37 v 35 3.3 Mud Solids Specific Gravity 27 " 0 20 40 60 80 100 120 Weight % High Gravity Solids Figure-1: Relative Amount of Barite and Lower Specific Gravity Solids in the Suspended Solids 32
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TABLE-1 Viscometer Reading Clay, grams 300 RPM 600 RPM 5 10 15 20 25 30 35 40 33
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EXPERIMENT FOUR IDENTIFICATION AND TREATMENT OF SALT CONTAMINATED DRILLING FLUIDS OBJECTIVES: Identify and treat salt contaminated drilling fluids. INTRODUCTION This experiment is designed to familiarize the student with the problems associated with different salts and the treatment necessary to alleviate same. Recommendation: The system should be pre-treated with thinner (i.e. lignite, phosphate, etc.) for inhibition against brine intrusion and loss of circulation. Following this pre-treatment, monitor the system for increase in circulating pressure, yield point, funnel viscosity, water loss, chlorides, decrease in pit volume, flow rate, pH, Pm, and Pf. Such monitoring will insure early identification and readiness to combat the effects of mud contamination. A change in any of these parameters must be followed by pilot testing and additional treatment accordingly. The first indication will be an increase in circulating pressure while drilling. As such, the drilling crews should be on the look-out for this sign. Brine intrusion will greatly increase our chances of lost circulation due to annular flocculation. This will cause an increase in water loss, yield point, and gels, but a decrease in plastic viscosity. Successful drilling at this point will depend on successful maintenance of an inhibited mud system. Additional guidelines for safe drilling are as follows: 1. At the first sight of pressure increase, pickup 30 feet and circulate bottoms up. 2. Perform a chloride test at bottoms up, and before drilling ahead treat the mud with a thinner as dictated by your pilot test. If the chloride count increases too high for economic treatment, dump and add new mud such that the total chlorides stay in line with that required for an economically controllable contaminated fresh water system. 3. Always rotate the pipe first to break the gels before putting the pump on. Calculate the surge pressures, based on the actual rheological properties. Use these calculated results to determine the pipe speed necessary to avoid breakdown while running in the hole, during connections, and during trips. Dress the bit with larger nozzles to reduce the surge and swab pressures and also to facilitate spotting of lost circulation material if necessary. Two jets with one blank will satisfy this requirement by affording better cross flow, the required bit hydraulic horsepower, and larger nozzle sizes. 34
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4. At casing point, circulate bottoms up and perform a pilot test on the mud for treating the gels prior to tripping. 5. On all trips in the hole, stop and break circulation at the casing shoe and monitor the return while running in. After leaving the shoe, stop and break circulation whenever necessary. 6. In case of lost circulation pull to the shoe, condition the mud and run back in, circulating and conditioning as many stages as necessary. 7. Condition the mud thoroughly before running casing and adopt the same precautions as stated for tripping into the hole. EXPERIMENTAL PROCEDURE 1. Prepare a sample of base mud by mixing 30 grams of bentonite and 350 cc. of water. Mix for 5 minutes. Perform the following tests: (a) Measure the mud weight, 10 second gel, and the pH of the mud. (b) Record the 300 and 600 RPM viscometer readings to calculate PV and YP. (c) Measure filtration loss. Since neither a filter cake nor spurt loss is being measured, the filtration only needs to be done for 20 minutes, in_order to get a representative and comparative value. It would be a good idea to take readings at 5, 7.5, 10, and 15 minutes as well. Therefore, this is not an actual API filtration loss. Prepare a second mud by mixing 30 grams of bentonite for 5 minutes. At the end of the 5 minutes, add 10 ml. of a 150,000 mg/L Sodium Chloride (NaCl) solution. Mix for 3 minutes. Perform the same tests as in step 2 above. Prepare a third mud by mixing 30 grams of bentonite for 5 minutes, and then adding 10 ml. of a 150,000 mg/L NaCl solution. Mix for 3 minutes. Treat the salt contaminated mud by adding 1.0 gram of lignite and mix for 5 minutes. Perform the same tests as in step 2 above. RESULTS: 1. Discuss the effect of salt contamination on various mud properties. 2. Discuss how salt contaminant could be identified. 3. Discuss the effectiveness of the lignite treatment used. 35
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Base Dirilling Fluid Salt Contaminated Drilling Fluid Treated Drilling Fluid Plastic Viscosity, cp Yield Point, 1b/100 sq.ft 10 second Gel Strength 1b/100 sq.ft Filtration Loss mi pH
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EXPERIMENT FIVE LIME TREATED INHIBITIVE DRILLING FLUIDS OBJECTIVES: Study the preparation, properties, and applications of inhibitive drilling fluids. INTRODUCTION Primary consideration for drilling production holes is to minimize interaction between drilling fluid and formation rock. This is usually accomplished with the use of inhibitive water-based drilling fluid systems or oil-based drilling fluids. The decision which mud system to use is dependent upon sensitivity of drilled rocks to water, cost of mud, and disposal cost (toxicity). Common mud contaminants such as cement, anhydrite, or salt will not normally affect inhibited fluids as dramatically as they do conventional dispersed, non-inhibited fluids. The problems caused by non- pressured heaving shales and tight hole conditions are more easily handled. In general, inhibited systems have lower viscosities (except in the high density ranges) and low gel strengths. The principal areas of use for these fluids are the drilling of shale formations. Formulation: Water (fresh or salty) Sodium bentonite not to exceed 15 Ib/bbl Caustic soda 11.5- 12.0 pH Lignite 2- 6 Ib/bbl used at breakover and not in highly weighted systems Lime High density fluids 2- 3 I/bbl excess Low density fluids 6- 8 Ib/bbl excess Lignosulfonate 1- 10 Ib/bbl Starch or Polymers 0.75- 3.0 Ib/bbl Lime muds perform well up to 350 °F, at which time the fluid loss may become hard to control. This leads to dehydration of the system and solidification can occur. In most cases the calcium inhibited system is made from the native mud used to drill the surface hole. Downhole temperature aids in converting the system to an inhibited (calcium -bentonite) system. This procedure is called a "breakover”. Normally there is a short period of time during the "breakover" where the viscosity may become very high. This is the "Hump", which is caused by the clay flocculating and converting to calcium clay. 37
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The procedures necessary for the conversion and maintenance of a lime based mud are as follows. A mud system having a lime concentration that is numerically equal to its phenolphthalein mud filtrate alkalinity (Py) is the main objective when running a lime based mud. By doing this, the chemical analysis of the methyl orange alkalinity of the mud filtrate, M and Pf can be used to directly calculate the lime concentration and the required treatment. It is very important to perform the conversion in one circulation. To achieve this, the surface system must be first converted fully and displaced down the hole. This procedure is repeated until the hole is completely displaced. It is advisable to commence the conversion by treating the surface system while waiting on cement. The conversion should be started by first diluting the system with fresh water. Caustic soda is then slowly added followed by chrome lignosulfonate. The mud will thicken, after adding the caustic soda, due to the increase in pH, but the chrome lignosulfonate will subsequently reverse this change. Stop all additions and allow the system to properly mix for a while (30 minutes). This mixing will insure an even consistency of the chemical treatment throughout the system. Any addition of lime before the system is thoroughly mixed will cause thickening and difficulty in conversion. Slowly add hydrated lime and again allow the system to mix for a while (30 minutes). If the mud maintains an increased thickness, further addition of chrome lignosulfonate will help. After properly mixing the system, add CMC and again allow the system to mix for a while (30 minutes). The treatment of the surface system is now completed. Pump-this treated volume down the hole and continue to repeat the same procedure, treating and pumping in batches, for one full cycle. Use the procedures described in APl Recommended Practices 13B-1 (RP 13B-1) Section #8 to monitor the lime concentration and the required treatment. It is very important to maintain the required treatment during circulation since the reaction of the lime and active clays take place down the hole. Closely monitor and maintain the pH at 12. Any increase in pH will cause and increase in the amount of lime in solution and will further cause mud thickening. Precede all future additions of lime while drilling with the proportional additions of chrome lignosulfonate and thorough mixing of the system. Always wait for bottoms-up time before adding any lime. Doing this will insure that the lime is added only to the treated mud as it returns to surface. It is for this purpose that a free lime concentration is maintained. As the lime in solution expends downhole, the free lime goes into solution giving time for replenishment of the free lime while drilling. This is a very delicate system to control and require extreme care. 38
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EXPERIMENTAL PROCEDURE 1. N Prepare a sample of base mud by mixing 25 grams of bentonite with 350 cc. of water for 7 minutes. . Perform the following test on the base mud: (a) Measure the mud weight, 10 second gel, and the pH. (b) Carry out the alkalinity tests by determining Pn, Ps ,and M; (see below, Alkalinity Determinations) (c) Record the 300 and 600 RPM viscometer readings in order to calculate PV and YP. (d) Measure the filtration loss. Since neither a filter cake nor spurt loss is being measured, the filtration only needs to be done for 20 minutes, in_order to get a representative and comparative value. It would be a good idea to take readings at 5, 7.5, 10, and 15 minutes as well. Therefore, this is not an actual AP! filtration loss. Prepare a second mud by again mixing 25 grams of bentonite with 350 cc. of water. Dilute 270 ml. of this mud with 80 ml. of water and convert to lime mud as follows: While mixing the mud, add 3 Ib/bbl, i.e. 3 grams, of caustic soda dissolved in ml. of water. Observe the viscosity change. Add 3 Ib/bbl, i.e. 3 grams, of deflocculant (polyphosphate-Barafos). Observe the viscosity change. Mix for 5 minutes at low speed. Add 4 Ib/bbl, i.e. 4 grams, Calcium oxide, commonly known as burnt lime, lime or quicklime (CaO). Mix for 5 minutes at low speed. Add 0.5 gram Ib/bbl, i.e., 0.5 grams, of Quik Gel. Mix for 5 minutes at low speed. 10.Measure the same properties as were measured in step 2 above. Alkalinity Determinations Py, Py, and M;: 1. Mud Alkalinity, Py, : This test measures the alkalinity of the whole mud. When used along with the filtrate alkalinity determination, the amount of excess lime present in lime muds can be determined. 39
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PROCEDURE Py: 1. Using a syringe, measure 1 ml. of a freshly stirred sample of mud into a titration dish. Make sure there are no air bubbles. Dilute the mud with 25-50 ml distilled water. Add no more than 4 or 5 drops of phenolphthalein. If the sample does not change color, report Pm as 0. If the sample turns pink, titrate rapidly with N/50 sulfuric acid until pink color disappears. Use the 1cc pipette for the base mud and the 10 cc pipette for the lime mud. Report the phenolphthalein alkalinity of the mud, Pm, as the number of mis of N/50 sulfuric acid added to discharge the pink color. 2. FILTRATE ALKALINITY P; .and Mg These tests measure the alkalinity of the filtrate or water. PROCEDURE Py 1. 2. 3. 4. Pipette 1 ml. of filtrate into a clean titration dish. Do not dilute with distilled water. Add no more than 2 or 3 drops of phenolphthalein. If no color develops, Py is 0, and the pH is less than 8.3. If a pink color develops, add N/50 sulfuric acid through a pipette until the color changes back to that of the original sample. Use the 1 cc pipette for the base mud and the 10 cc pipette for the lime mud. The Py is the amount of N/50 sulfuric acid required to discharge the pink color. Excess lime content, Ib/bbl = (Pm - Pf)/4. PROCEDURE Mg 1. 2. 3. To the same sample used for the P; determination, add 2 to 3 drops of Bromcresol Green - Methy! Red Indicator. Again add N/50 sulfuric acid until the color changes from a blue-green to a light pink. Use the 1 cc pipette for either mud. Report the M; alkalinity of the filtrate as the total volume of N/50 sulfuric acid required to reach the end point, including the volume required to reach the Ps end point. 40
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Results: 1. Discuss applications of calcium treated muds. 2. Discuss advantages and limitations of calcium treated muds. 3. Based on your observation of viscosity changes, discuss the conversion mechanism of lime mud. Include the effects of adding each component. 4. Compute the amount of free lime. Discuss what it tells you. 5. Based on the results of your lab experiment, write a step-by-step procedure for the derrick hand to convert to lime mud. Include the barrels of water, sacks of caustic soda, polyphosphate, lime, and bio- polymer (Quik-Gel) needed for the conversion of 1500 bbl base mud in tanks and in the hole. Show all calculations. (1 sack = 50 Ibs). Base Drilling Fluid ] Lime Treated Drilling Fluid Plastic Viscosity, (cP) Yield Point, (Ib/100 sq.ft.) 10 second Gel Strength (Ib/100 sq.ft.) Filtration Loss (mi) pH Ps Pm My Please see sections 12, Alkalinity and lime content, and 13, Chloride ion content of the “Recommended Practice for Field Testing Water-based Drilling Fluids” ANSI/API RP 13B-1, 4" Edition, March 2009 - for further information. 41
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