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.r °~ <br />DRILLING MUD REPORT NO. <br />Appendix I <br /> <br />' ~ ~ ~j DATE~~L..Z 19 d-~ DEPTH <br /> <br />NL Baroid/NL Industries, Inc. <br />SPUD DATE PRESENT ACTIVITY <br />OPERATO <br />[~L CONTRACTOR RIG NO <br />REPOR FO <br />2 .e REPORT FOR SECTION. TOWNSHIP. RANGE <br />WELL NAME AND NO FIELD OR BLOCK NO COUNTY. PART H R <br />OFFSHOREA STATE/ OVIN E <br />C/ <br />DRILLING ASSEMBLY CASING MUD VOLUME (BBL) CIRCULATION DATA <br />BIT SIZE TYPE JEi SIZE SURFACE <br />SET 6~ Fi HOLE PITS PUMP SIZE % IN. ANNULAR VEL.IFTIMIN) <br />DP DC <br />DRILL PIPE <br />SIZE TYPE LENGTH INTERMEDIATE <br />SET @ FT TOTAL CIRCULATING VOLUME PUMP MAKE, MODEL ASSUMED <br />EFF % CIRCULATION <br />PRESSURE (PSI) <br />DRILL PIPE <br />SIZE TYPE LENGTH INTERMEDIATE <br />SET@ A IN STORAGE WEIGHT BBL'STK STKMIN BOTTOMS <br />UP IMIH) <br />DRILL COLLAR SIZE LENGTH PRODUCTION OR LINER <br />SET@ R M OTYPE <br />BBIJMIN GALMIN TOTAL CIRC, <br />TIME IMINI <br /> MUD PROPERTIES MUD PROPERTY SPECIFICATIONS <br />Sample From ^ F.L. ^ PIT ~ F.L. ^ PIT WEIGHT VISCOSITY FILTRATE <br />Time Sample Taken BV AUTHORITY OOPERATOR'S WRITTEN ^DRILLING CONTRACTOR <br />R <br />' <br />, <br />° S REPRESENTATIVE ^ OTHE <br />OPERATOR <br />L <br />Flowline Temperature <br />F <br />Deptn fnl RECOMMENDED TOUR TREATMENT <br />Welghl ^(ppg) ^Ilb/cu. h.l ^SP.G ~ U 11 <br />/ <br />Funnel Vlscoslry lsec/q[JAPI@' °F O O { - ~/ <br />~/ L U Q Gy `(/ ~QX~,Q~ <br />+- ~// <br />s ` <br />Plazlic Viscosry cP @ °F - <br />/ /t ~ <br />/ <br />~ <br /> <br />Yield Point (Ib/100 M') ` <br />~-~,-~,,./ <br />f-R <br />~ <br />G <br /> <br />Gel Strength Qb/100 ft') 10 sad 10 mm. <br />0 r c / <br /> <br />~k „ <br />~ -y„ e ~ <br />~,, <br />~- <br />Filtrate APl (cm~/30 mm.) <br />API HTHP FilVale (cm~/30 min.) @ °F ~ ~ ~ ~ <br />L s 5 2 C /~ Gip/p x ~ <br /> <br />Cake Thickness (32nd in API/HTHPI ~ <br />/' <br />Solids Coolant (%by Val.) ^ Wlculaletl ^ retort <br />L'puid Content (Ye W Vol.) Oil/ Water i-h-b/% <br />Send Content (% by Vol.) <br />Methylene Blua Capanry INbbl acmv. <br />cmA'cm mW <br />pH ^ Strip ^ Meter @ °F <br /> <br />Alkalinity Mud (Pm) <br />/ <br />~ <br />~ <br />~ <br /> <br />Nkalinily Fikrete (Pt/Mt ) ~/~ <br />// <br />/ <br />%~/~ <br />/L <br />Allertwte Alkaliniy Filtrate (PJPoI <br />Chblide (myL) <br />ToW Hardness az Calcium (mg/L) <br /> <br /> <br /> <br /> EOUIPMEN7 <br />SIZE HRS/TOUR <br />PRODUCT Centrifuge <br />INVEMORY <br /> <br />STARTING Degasser <br />INVENTORY Desantler <br />RECEIVED DeSlller <br /> <br />USED LAST Shaker <br />I<NR Other <br />CLOSING <br />INVENTORY DAILY COST CUMULATIVE COST <br />cosT usT <br />2t HR <br />d <br />THE RECOMMENDATIONS MADE HEREON SMALL NOT BE CONSTRUED AS AUTHORIZING THE INFRINGEMENT OF ANY VALID PATENT, AND ARE MADE WITHOUT <br />ASSUMPTION OF ANY LIABILITY By N L INDUSTRIES, INC. OR ITS AGENTS. AND ARE STATEMENTS OF OPINION ONLY. <br />HOME <br />.~ Y <br />