The ICS-X1-ST1 well was a sidetrack of the ICS-X1 well to reach the Huamampampa Formation target. The sidetrack encountered the Huamampampa Formation at 4905m and drilled to 5600m total depth. Between 4905-5376m, 471m of quartzitic sandstone and siltstone of the Huamampampa Formation was found, which was very faulted and fractured. A drill stem test between 4905-5150m produced over 1000 thousand cubic meters per day of gas and condensate. The well provided data on the stratigraphy and structure of the Huamampampa Formation in the area.
Tipers sensemaking tasks for introductory physics 1st edition hieggelke solut...Brasehads
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Get the best Auto Tools at a discount from CARQUEST Autoparts. Visit Auto Barn in Essex Ontario for all the best in Auto Tools at the best prices possible!
In order to support information regarding arthritis in examinees in the study, x-rays of the wrists
and hands, and knees will be conducted on all examinees sixty years of age and above. The x-rays will be
taken in the following positions and sequence.
In order to support information regarding arthritis in examinees in the study, x-rays of the wrists
and hands, and knees will be conducted on all examinees sixty years of age and above. The x-rays will be
taken in the following positions and sequence
A comprehensive review on passive heat transfer enhancementsMohamed Fadl
Enhancing heat transfer surface are used in many engineering applications such as heat exchanger, air
conditioning, chemical reactor and refrigeration systems, hence many techniques have been investi-
gated on enhancement of heat transfer rate and decrease the size and cost of the involving equipment
especially in heat exchangers. One of the most important techniques used are passive heat transfer
technique. These techniques when adopted in Heat exchanger proved that the overall thermal
performance improved significantly. This paper reviews experimental and numerical works taken by
researchers on this technique since 2004 such as twisted tape, wire coil, swirl flow generator, y etc. to
enhance the thermal efficiency in heat exchangers and useful to designers implementing passive
augmentation techniques in heat exchange. The authors found that variously developed twisted tape
inserts are popular researched and used to strengthen the heat transfer efficiency for heat exchangers.
The other techniques used for specific work environments are studied in this paper. Twisted tape
inserts perform better in laminar flow than turbulent flow. However, the other several passive
techniques such as ribs, conical nozzle, and conical ring, etc. are generally more efficient in the
turbulent flow than in the laminar flow.
A comprehensive review on passive heat transfer enhancements in pipe exchangersMohamed Fadl
Enhancing heat transfer surface are used in many engineering applications such as heat exchanger, air
conditioning, chemical reactor and refrigeration systems, hence many techniques have been investi-
gated on enhancement of heat transfer rate and decrease the size and cost of the involving equipment
especially in heat exchangers. One of the most important techniques used are passive heat transfer
technique. These techniques when adopted in Heat exchanger proved that the overall thermal
performance improved significantly. This paper reviews experimental and numerical works taken by
researchers on this technique since 2004 such as twisted tape, wire coil, swirl flow generator, y etc. to
enhance the thermal efficiency in heat exchangers and useful to designers implementing passive
augmentation techniques in heat exchange. The authors found that variously developed twisted tape
inserts are popular researched and used to strengthen the heat transfer efficiency for heat exchangers.
The other techniques used for specific work environments are studied in this paper. Twisted tape
inserts perform better in laminar flow than turbulent flow. However, the other several passive
techniques such as ribs, conical nozzle, and conical ring, etc. are generally more efficient in the
turbulent flow than in the laminar flow.
Get the best Auto Tools at a discount from CARQUEST Autoparts. Visit Auto Barn in Essex Ontario for all the best in Auto Tools at the best prices possible!
In order to support information regarding arthritis in examinees in the study, x-rays of the wrists
and hands, and knees will be conducted on all examinees sixty years of age and above. The x-rays will be
taken in the following positions and sequence.
In order to support information regarding arthritis in examinees in the study, x-rays of the wrists
and hands, and knees will be conducted on all examinees sixty years of age and above. The x-rays will be
taken in the following positions and sequence
A comprehensive review on passive heat transfer enhancementsMohamed Fadl
Enhancing heat transfer surface are used in many engineering applications such as heat exchanger, air
conditioning, chemical reactor and refrigeration systems, hence many techniques have been investi-
gated on enhancement of heat transfer rate and decrease the size and cost of the involving equipment
especially in heat exchangers. One of the most important techniques used are passive heat transfer
technique. These techniques when adopted in Heat exchanger proved that the overall thermal
performance improved significantly. This paper reviews experimental and numerical works taken by
researchers on this technique since 2004 such as twisted tape, wire coil, swirl flow generator, y etc. to
enhance the thermal efficiency in heat exchangers and useful to designers implementing passive
augmentation techniques in heat exchange. The authors found that variously developed twisted tape
inserts are popular researched and used to strengthen the heat transfer efficiency for heat exchangers.
The other techniques used for specific work environments are studied in this paper. Twisted tape
inserts perform better in laminar flow than turbulent flow. However, the other several passive
techniques such as ribs, conical nozzle, and conical ring, etc. are generally more efficient in the
turbulent flow than in the laminar flow.
A comprehensive review on passive heat transfer enhancements in pipe exchangersMohamed Fadl
Enhancing heat transfer surface are used in many engineering applications such as heat exchanger, air
conditioning, chemical reactor and refrigeration systems, hence many techniques have been investi-
gated on enhancement of heat transfer rate and decrease the size and cost of the involving equipment
especially in heat exchangers. One of the most important techniques used are passive heat transfer
technique. These techniques when adopted in Heat exchanger proved that the overall thermal
performance improved significantly. This paper reviews experimental and numerical works taken by
researchers on this technique since 2004 such as twisted tape, wire coil, swirl flow generator, y etc. to
enhance the thermal efficiency in heat exchangers and useful to designers implementing passive
augmentation techniques in heat exchange. The authors found that variously developed twisted tape
inserts are popular researched and used to strengthen the heat transfer efficiency for heat exchangers.
The other techniques used for specific work environments are studied in this paper. Twisted tape
inserts perform better in laminar flow than turbulent flow. However, the other several passive
techniques such as ribs, conical nozzle, and conical ring, etc. are generally more efficient in the
turbulent flow than in the laminar flow.
Hướng dẫn sử dụng Testo 320
https://testostore.vn/san-pham/may-do-khi-thai-testo-320-may-in/
https://testostore.vn/danh-muc/may-do-phat-xa/may-phan-tich-khi-cong-nghiep/
Hướng dẫn sử dụng máy đo áp suất và dò rò rỉ khí Testo 324Tenmars Việt Nam
Hướng dẫn sử dụng máy đo áp suất và dò rò rỉ khí Testo 324
https://testostore.vn/san-pham/testo-324/
https://testostore.vn/danh-muc/do-ap-suat/may-do-ro-di/
Cosmetic shop management system project report.pdfKamal Acharya
Buying new cosmetic products is difficult. It can even be scary for those who have sensitive skin and are prone to skin trouble. The information needed to alleviate this problem is on the back of each product, but it's thought to interpret those ingredient lists unless you have a background in chemistry.
Instead of buying and hoping for the best, we can use data science to help us predict which products may be good fits for us. It includes various function programs to do the above mentioned tasks.
Data file handling has been effectively used in the program.
The automated cosmetic shop management system should deal with the automation of general workflow and administration process of the shop. The main processes of the system focus on customer's request where the system is able to search the most appropriate products and deliver it to the customers. It should help the employees to quickly identify the list of cosmetic product that have reached the minimum quantity and also keep a track of expired date for each cosmetic product. It should help the employees to find the rack number in which the product is placed.It is also Faster and more efficient way.
Student information management system project report ii.pdfKamal Acharya
Our project explains about the student management. This project mainly explains the various actions related to student details. This project shows some ease in adding, editing and deleting the student details. It also provides a less time consuming process for viewing, adding, editing and deleting the marks of the students.
Explore the innovative world of trenchless pipe repair with our comprehensive guide, "The Benefits and Techniques of Trenchless Pipe Repair." This document delves into the modern methods of repairing underground pipes without the need for extensive excavation, highlighting the numerous advantages and the latest techniques used in the industry.
Learn about the cost savings, reduced environmental impact, and minimal disruption associated with trenchless technology. Discover detailed explanations of popular techniques such as pipe bursting, cured-in-place pipe (CIPP) lining, and directional drilling. Understand how these methods can be applied to various types of infrastructure, from residential plumbing to large-scale municipal systems.
Ideal for homeowners, contractors, engineers, and anyone interested in modern plumbing solutions, this guide provides valuable insights into why trenchless pipe repair is becoming the preferred choice for pipe rehabilitation. Stay informed about the latest advancements and best practices in the field.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
Saudi Arabia stands as a titan in the global energy landscape, renowned for its abundant oil and gas resources. It's the largest exporter of petroleum and holds some of the world's most significant reserves. Let's delve into the top 10 oil and gas projects shaping Saudi Arabia's energy future in 2024.
8. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 8
1.1. General Summary
1.1.1. General setting
The foothills of Southern Bolivia and Northwestern Argentina are characterized by a succession of sub-parallel
NNW-SSE trending mountain ranges. Each of these ranges corresponds to a tightly folded elongated anticline
structure up to 300km long. The crest of these mountain ranges have an elevation of 1300-2000m while the
synclines separating the mountain ranges have a relief of 600 to 800m.
The Ipati block is located in the Cordillera Province of the Santa Cruz department. The area corresponds to a
morphological unit of the southwestern part of the foothills. Steep ranges cut by rivers running eastwards
characterize this area.
1.1.2. Regional Stratigraphy
Within the South Bolivian foothills, the undeformed stratigraphic section is approximately 10,000 to 12,000 meters
thick, ranging from Silurian to Tertiary (Pliocene). This section consists almost exclusively of clastics with only minor
carbonates and evaporites present.
The stratigraphic section can be separated into three main cycles : Cordilleran, Subandean, and Andean.
During the Cordilleran cycle, of Silurian to Devonian age, 3500m of near shore to shelf, marine clastics units were
deposited. The Devonian section contains the main source rock (Los Monos Shales) and the main reservoirs
(Huamampampa & Santa Rosa Formations) of the area.
The Carboniferous to Triassic section of the Subandean cycle lies unconformably on the Devonian.
The Carboniferous section (1000 to 1500m) is dominated by massive continental sandstones, with good reservoir
quality (Escarpment, Chorro and Tupambi Formations) and peri-glacial diamectites (Taiguati and Tarija Formations).
The Permo-Triassic section (400m) contains very good fluvial and deltaic sandstones (Cangapi Formation) and
silicified carbonates (cherts of Vitiacua Formation).
The Andean cycle is composed of a thick section of Tertiari foreland deposits (up to 6000m) (Chaco group :
Guandacay, Tariquia and Petaca Formations) and fluvial to eolian sandstones of probable Jurassic to Cretaceous
ages with very good reservoir characteristics (Tacuru group : Ichoa Formation).
Due to the large scale of tectonic activity during the later part of the Andean cycle, all the good Tertiary to
Carboniferous reservoirs outcrop at surface.
1.1.3. Exploration History
On the Incahuasi trend three wells have been drilled in the proximity of the well. These wells recognized only the
Carboniferous and the Upper Devonian.
Aquio-X1, drilled in 1962-1963 by YPBF, is located 4km NNW of ICS-X1 and reached a TD of 2209m in the Los
Monos Formation.
Lagunillas-X1 (LGN-X1), drilled by YPBF in 1964, is located 23km to the North and reached a TD of 1817m in the
Jurassic (Tacuru Group).
La Montana-X1001 (LMT-X1001) (drilled in 2000 by Tecpetrol), located 9km to the South, on the same trend,
reached a TD of 2754m in the Iquiri Formation.
On the neighboring trends, the following wells reached the Humampampa Formation:
- Camiri-201 (CAM-201), drilled between 1962 and 1964, is located 28km to the SE. It reached a total depth
of 3677m in the HMP.
9. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 9
- Tatarenda-X27 (TTR-X27) was drilled in 1967 by YPBF. It is located 80km to the NNE and reached a TD of
3030m in the HMP.
- Inau-X2, drilled in 1988-1989 by YPBF, is located 20km to the SW. It reached a TD of 2768m in the HMP.
- Cumandairenda-X1, drilled in 1994-1995 by YPBF on the same trend than Inau-X2, is located 47km to the
SSE. It reached a TD of 3733m in the HMP.
All these wells were dry, except Inau-X2 and Lagunillas-X1. In Inau-X2, 5.5m thick gas-bearing sands were
encountered in the Los Monos section. Nevertheless logs and DST performed show these levels of poor reservoir
characteristics and marginal production (0.282 MMCFD). In Lagunillas-X1, gas with low pressure was tested in a 6m
thick Iquiri sandstone.
1.1.4. Objectives
Well ICS-X1 was drilled deviated to the West from a surface location on the eastern flank of the Incahuasi surface
anticline (SP 2097 of line T03-IP01). The objective was to reach the expected top of Huamampampa Sandstone at
2950mss. After drilling an unexpected reversed flank of the anticline, it was stopped at 5187mMD in a formation
interpreted as the carboniferous Tupambi formation, dipping around 70° toward the East.
Based on this new information, the structural model was reviewed and indicated that the top HMP could be located
eastward to the TD of ICS-X1, almost at the vertical of the surface location.
It was then decide to side track the well (ICS-X1 ST1) in order to reach this new target.
The main objective of the Incahuasi-X1 ST1 well corresponds to the same tight, fractured Devonian sandstones of
the Huamampampa Formation.
1.1.5. Main Results
The well ICS-X1-ST1 encountered the Huamampampa Fm at 4905m (-3352mTVDSS) and was drilled down to
5600mRT (-4019mTVDSS).
A total of 471m of quartzitic Sandstone and hard Siltstone was found (from 4905 to 5376mMD):
• From 4905 to 5246mMD: dipping 50 to 80ºW,
• From 5246 to 5370mMD: dipping alternatively 45°E to 80°W
• From 5370 to 5376mMD, and then in Shale to 5600mMD (TD): dipping 40 to 60°E.
This formation was very faulted and fractured, and represents 252m of true thickness. Below 5376mMD to TD, only
very radioactive shale was found. A total of 329m (true thickness) of HMP Formation were thus investigated.
A bare foot DST was performed between 4905 to 5150mMD; it produced 1093ksm3/d of gas and 119m3/m3 of
condensate with a 44/64” choke.
16. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 16
2.1. Drilling Summary
Abandon of ICS X1 First Hole & Start with ICS X1.ST1 Geological Side Track N° 1
• Phase 12”1/4 : 2406 to 4294m
30/04/04 : RIH with casing cutter at 3806m. Cut 9”5/8 casing @ 3806m. Losses 10 m3. POOH to 3207m, 2° cut
9”5/8 casing @ 3207m. Close pipe rams & attempt to circulate between 9”5/8 and 13”5/8, no success. POOH to
surface. Nipple down flow line. Pick up BOP & remove “C” section, Cameron CANH seal, nipple up spool, tie down
flange & set BOP. Pick up 10”3/4 spear assembly & tools. Engage spear in 10”3/4 casing & pull to 150 tn.
01/05/04 : Pick up BOP. Pull casing to 340 tn. Remove casing 10”3/4 slips. Work casing from 150 to 400 t without
success. Pick up BOP, clean 10”3/4 casing & spool. Redress casing slips, set slips & lower BOP. Lay down casing
fishing tools. Nipple up flow line. Pick up casing cutter BHA & change blades in cutter. Adjust & test cutter. Check
twen stop. RIH to 2974m & cut casing @ 2974m, string plugged when done. POOH 2974/2674m. Pump 4 m3
between 13”5/8 & 9”5/8 casing without returns. POOH to 73m.
02/05/04 : Continue POOH to surface. Make up casing 10”3/4 fishing tool assembly. Nipple down flow line. Pick up
BOP, install new ring gasket. Set casing spear & pull casing to 270 t. Pull 10”3/4 casing slips, pick up first coupling
at rotary table. Rig up casing tongs. Release spear & lay down cut off joint 10”3/4. Rig up casing tools. POOH casing
10”3/4 break out torque: 40000 lbs/feet. Mud level in annulus not visible. Change tools from 10”3/4 to 9”5/8 casing.
Trouble shoot with elevators & tongs. POOH 9”5/8 casing to 1300m.
03/05/04 : POOH 9”5/8 casing to surface. Rig down casing equipment & lay down machine. Rig down floor handling
tools & bails. Pick up test tools & clean BOP. Test lines & BOP:
5”1/2 pipe rams tested to 500 psi low & 8000 psi high, OK.
Variable 4”1/2 to 7” pipe rams tested to 500 psi low & 8000 psi high: leak.
Annular tested to to 500 psi low & 3500 psi high: OK.
Blind rams tested to 500 psi low & 8000 psi high: OK.
Remove lower rams & redress with new inserts. Reinstall same. Pressure test lower rams with 500 & 8000psi, OK.
Hook up flow line. Pull test plug, install wear bushing.Hawk jaw & 3”1/2 tubing tools. Make up mule shoe & pick up
3”1/2 tubing from cat walk.
04/05/04 :RIH to 1500m. Displace well with OBM 1.1 sg. RIH to 3800m. Pump 4m3 Hi-Vis pill 1.3 sg & 26m3 WMB
1.3sg. Displace with 31.5m3 OBM 1.3 sg. POOH to 2974m. Pump 180 m3 OBM 1.1sg & 8 m3 WBM 1.1sg & 14.5m3
WBM 1.12 sg. Cement plug job:
Pump 9.5m3 spacer water.
Pump 16m3 cement.
Displace with 1.4m3 water & 27m3 OBM 1.1sg.
POOH to 2300m. Pump nut pill. Ciculate & condition mud. POOH to 1578m.
05/05/04 : POOH to surface. Pressure test cement plug to 3000psi, OK. Rig up perforate gun. RIH with perforate
gun & perforate 13”5/8 casing @ 2400 – 2401m. Pressure up annulus to 800psi, no bleed off. Re-arm gun. Run N°2
with perforate gun & perforate 13”5/8 casing @ 2354 – 2355m. Perform LOT:
Leak @ 1050psi EMW:1.42 sg.
Tight Formation – Max pressure 1450psi – Slow injection.
Pumped 1.8m3 & inject 0.7 m3.
Run gauge ring & junk basket with wireline. Rig up wireline to run bridge plug. RIH packer with wireline & set bridge
plug @ 2346.10m. POOH with wireline. Rig down wireline. Wait on Whipstock.
06/05/04 : Make up new BHA. Pick up test assembly & test MWD, OK. Pick up Whipstock & orient tool. RIH @
2340m. MWD operators wiring up directional monitor. Circulate to orient Whipstock. RIH tag bridge plug & set
Whipstock @ 2345m (39° right from high side). Mill & start cut window @ 2336.4m.
07/05/04 : Mill & cut window from 2336 to 2340.50m.
08/05/04 : Continue cut window in 13”5/8 casing from 2340.5 to 2340.8m. Pump slug pill & POOH due to ROP
slowing down. POOH BHA, recover 3.5m of Whipstock, lay down mill & MWD. Change out & cut drilling line. Service
Top drive. Test casing with Halliburton to 1500 & 2500 psi, no bleed off. Stand by, waiting on wash over mill tools.
09/05/04 : Stand by, waiting on wash over mill tools. Unload Weatherford tools & start to make BHA. Pick up bit sub,
junk basket, XO, top bushing, wash over shoe. Attempt to screw shoe on bushing: not OK. Lay down both, attempt
17. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 17
to screw shoe & bushing on 1 joint of wash pipe: shoe OK, bushing not OK. Order bushing in town. Stand by, waiting
on wash over mill bushing.
10/05/04 : Wait on wash over mill bushing. Make up bushing, shoe, continue make up BHA & RIH to 2331m. Wash
& ream to bottom from 2331 to 2340.6m. Mill on Whipstock from 2340.6 to 2341.7m (pump 4m3 Hi-Vis pill @
2341m). Pump 6m3 Hi-Vis pill, circulate hole clean with 2330 l/min. POOH from 2341.7 to 101m.
11/05/04 : POOH short mill BHA. Lay down shoe, bushing, bit sub & junk basket (full of metal). Make up Whipstock
fishing BHA & RIH to 2339m. Work over shot & catch fish. Pump slug & POOH with fish. Lay down fishing tools.
Make up drill out bridge plug BHA & RIH to 2326m. Break circulation & wash out from 2326 to 2344.78m (tag bridge
plug). Drill out plug from 2344.78 to 2345.12m.
12/05/04 : Continue to drill out bridge plug from 2345.12 to 2345.44m. RIH to 2550m without circulation. Circulate
out 12m3 WBM. POOH to surface. Prepare tools, make up mule shoe & RIH 3”1/2 tubing and DP to 2547m. Spot 25
bbl of Hi-Vis pill @ 2547m. POOH to 2499m. Pump 72 bbl cement plug and displace with OBM. POOH to 2300m.
Pump 55 bbl nut pill, circulate out & condition mud. Drop 3”1/2 OD rabbit & POOH;
13/05/04 : Continue POOH to surface. Make up new BHA with bit & RIH to 2298m. Wash down 2298 to 2342m. Tag
top of cement. Dril cement 2342 to 2419m. Circulate hole clean and condition mud. Set 35 klbs on bit with 260gpm
flow to check cement condition, OK. Well control drill. Shut in well, perform calculation & circulate trough chocke.
Drop 3”3/4 rabbit and POOH. Lay down BHA.
14/05/04 : Wait on Whipstock for side track.
15/05/04 : Test BOP & chocke manifold.
Test with 4000psi high pressure (3500psi annulus).
Test with 500psi low pressure.
Wait on Whipstock meanwhile:
H&P : Top drive maintenance. Drawworks maintenance. BOP accumulator. Clean all mud system. Service rig
generator. Service rig air compressors.
Geoservices :Cleaning & repairing Flow line sensor. Cleaning 7 pit level sensors. Maintenance and cleaning 2 gas
traps on shakers. Test & cleaning 5 H2S sensors. Calibration & test Reserval & Geofast FID. Test well head
pressure sensor. Cleaning & maintenance DSM 600 (temperature & MW sensor).
16/05/04 : Wait on Whipstock. Unload, check and measure Whipstock tools. Pick up Whipstock assembly and make
up BHA. RIH to 2419m. Orient and set Whipstock, 30° to the right of high side. Mill window from 2408.8 to 2409.6m.
Pick up. Hole packed off. Free packed off. POOH to 2370m. Wash and ream 2370/2398m. Circulate.
17/05/04 : POOH from 2398m to surface. Lay down window master mill, string mill; monel & MWD. Make up new
BHA with tapered mill & RIH to 2391m. Wash from 2391 to 2396.6m. Took weight @ 2396.60m. Attempt to work in
order to pass 2396.6M without success. Mill from 2396.6 to 2400.5m. Pump 40 bbl Hi-Vis pill, circulate hole clean.
POOH from 2400m to surface. Lay down tapered mill, string mill, bit sub, drilling jar.
18/05/04 : Service Top drive. Pick upwhipstock retrieving tool, fishing jar, XO, float sub, monel. Wait on MWD
operator. Prepare MWD tool. Rig up MWD tool, orient MWD & retrieving tool, test MWD. Finish make BHA and RIH
to 2396m. Orient and latch retrieving tool into Whipstock. Take orientation 96° left of high side (Orientation of side-
track = 183.5°E). POOH to surface and lay down BHA. Make up new milling BHA and RIH to 2118m.
19/05/04 : RIH - Mill Window - FIT (EMW = 1.45) - POOH - Make up new BHA.
20/05/04 : RIH bit - Attempt to pass window - POOH - RIH mill - Milling window.
21/05/04 : POOH - RIH new BHA - Drilling from 2406 to 2418m.
22/05/04 : Drilling f/2418 to 2436m - Circulate - Reaming and mill window area - POOH - Pick up Vertitrack and test
assy.
23/05/04 : M/u new BHA (Vertitrack) - RIH - Drilling from 2436 to 2464m (Sliding from 2436 to 2450m).
24/05/04 : Drilling (Sliding) from 2464 to 2496m - Run Single Shot Survey.
25/05/04 : Drilling (Sliding from 2496 to 2515m - Circulate - Drop single shot - POOH to window - Retrieve single
shot - RIH - Drilling (Sliding) to 2524m.
18. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 18
26/05/04 : Drilling (Sliding from 2524 to 2545m - Circulate - Drop single shot - POOH to window - Retrieve single
shot - POOH to surface.
27/05/04 : Change and test Vertitrack - M/u new BHA - RIH - Drilling (Sliding) from 2545 to 2572m.
28/05/04 : Drilling (Sliding) from 2572 to 2575m - Circulate and drop Single Shot - POOH to 2167m - Test Vertitrack
Survey tool - RIH - Sliding to 2589m - Circulate – POOH.
29/05/04 : Test BOP - RIH with Junk basket - Take MWD surveys from 2408 to 2583m - Drilling from 2589 to 2590 -
Circ – POOH.
30/05/04 : POOH - Test and RIH motor - Drilling from 2590 to 2614m (Sliding : 2590-2610, 2610.5-2611).
31/05/04 : Drilling (Rotary and Sliding) and Surveys from 2614 to 2652m.
01/06/04 : Drilling (Rotary and Sliding) and Surveys from 2652 to 2668m - POOH - Change motor and bit - RIH BHA.
02/04/04 : RIH - Drilling (Rotary and Sliding) and Surveys from 2668 to 2694m.
03/06/04 : Drilling (Rotary and Sliding) and Survey from 2694 to 2731m.
04/06/04 : Drilling (Rotary and Sliding) and Survey from 2731 to 2766m.
05/06/04 : Drilling (Rotary and Sliding) and Survey from 2766 to 2796m.
06/06/04 : Drilling (Rotary and Sliding) and Survey from 2796 to 2831m.
07/06/04 : Drilling (Rotary and Sliding) and Survey from 2831 to 2841m - Circ. - POOH to shoe - FITs (#1 :
Deq=1.31, #2 : Deq=1.19) - POOH - RIH cement string.
08/06/04 : RIH to 2840M - Circ. - Set cement plug - POOH to 2548m - Squeeze cement - POOH - RIH with RR bit.
09/06/04 : Wash and ream to 2689m (tag cement) - Circ. - Perform FIT (EMW=1.35@shoe, inject 500l) - Drill out
cement to 2841m - Circ. – POOH.
10/06/04 : POOH to shoe - FIT (EMW=1.33) - POOH - M/u Vertitrack BHA - RIH - Sliding f/ 2841 to 2845m.
11/06/04 : Drilling (Sliding) &nd Surveys from 2845 to 2905m
12/06/04 : Drilling (Sliding), Reaming and Surveys from 2905 to 2972m
13/06/04 : Drilling (Sliding), Reaming and Surveys from 2972 to 3001m - Circ - POOH to window - FIT#6
(EMW=1.29@shoe - Inject: 500l) - RIH - Sliding to 3023 (Loss MWD signal @3005)
14/06/04 : Drilling (Sliding), Reaming and Surveys from 3023 to 3077m (Regain MWD signal @3037m).
15/06/04 : Drilling (Sliding), Reaming and Surveys from 3077 to 3100m – Circ . – POOH.
16/06/04 : Test BOP: 5000psi High pressure (3500psi annulus) – 500 psi Low pressure.
Pick up vertitrack, inspect float & test vertitrack, make up bit. RIH to 2860m (tag @2860m).
Wash & ream 2860/2867m. RIH 2867/3073m. Wash & ream 3070/3100m. Slide drilling from 3100 to 3114m.
17/06/04 : Drilling (Sliding), Reaming and Surveys from 3114 to 3180m.
18/06/04 : Drilling (Sliding), Reaming and Surveys from 3180 to 3225m. Circulate hole clean for wiper trip (2.5
bottom up). POOH from 3225 to 3185m. Tight hole @ 3185m, max over pull 35 t. Connect Top drive & work pipe @
3185m (hole pack off). Work pipe, pipe free. Back ream from 3185 to 3161m.
19/06/04 : Pump 9m3 low viscosity + 6m3 hi-density pill. Back ream 3161/3060m. Pump out of hole from 3060 to
2948m. Hole packed off after connection @ 2948m. Max over pull 40 t & weight down 50 t. No rotation, no returns.
Drop ball to open circulating sub. Circulate & work pipe. Pump & circulate out 9m3 low viscosity + 6m3 hi-density pill.
Jar down with 60 t max, while pumping with 900 l/m. Pipe free. Drop ball to close circulation sub & work pipe.
Establish full returns, free rotation. Wiper trip, back ream from 2948 to 2875m. Pump 9m3 low viscosity + 7m3 hi-
density pill. Continue back ream from 2875 to 2818m.
19. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 19
20/06/04 : Pump out from 2818 to 2365m. Service top drive. RIH from 2365 to 2992m. Wash down from 2992 to
3181m. Ream from 3181 to 3218m, pump 9m3 low-viscosity + 7m3 hi-density pill. Ream from 3218 to 3225m. Slide
drilling from 3225 to 3243m.
21/06/04 : Slide drilling 3243/3277m. Pump low-vis + hi-dens pill, small increase of cutting over shackers. Drilling
3277/3281m with Vertitrack (120rpm) & TDS (35rpm). Slide drilling 3281/3298m.
22/06/04 : Slide drilling and perform surveys from 3298 to 3359m.
23/06/04 : Slide drilling and perform surveys from 3359 to 3367m. Pump & circulate out 9m3 low-viscosity & 7m3 hi-
density pill. Pump out of hole from 3367 to 3244m. Hole packed of @ 3244m. Recover circulation. Back ream and
wash from 3244 to 3130m. Pump & circulate out 9m3 low-viscosity & 7m3 hi-density pill, small increase of cuttings in
shackers. Back ream and wash from 3130 to 3102m. POOH from 3102 to 2425m. Circulate hole clean. POOH from
2425 to 255m (top of BHA). POOH with BHA.
24/06/04 : POOH with BHA & lay down sock sub, Nortrack & Vertitrack & bit. Test circulation sub, not ok, lay down
same. Recover DC slips dies from BOPs with magnet: los 8, recover 7. Pick up BHA with new: Vertitrack, float sub,
Nortrack, circulation sub (without shock sub). Test Vertitrack, ok. Make up bit #59 PDC. RIH to 1722m. Set traction
motor on drawworks skid. RIH from 1722 to 2367m. Install traction motors on drawworks. Service TDS & drawworks.
RIH 2367/2433m. Test Vertitrack, ok. RIH 2433/3159m (tag). Wash & ream from 3159 to 3220m (tight spot @
3159/3186m). Pump 9m3 low-viscosity + 6m3 hi-density pill to clean the well.
25/06/04 : Wash from 3220 to 3367m. Circulate hole clean. Slide drilling from 3367 to 3375m. Attempt to recover
MWD signal from Vertitrack, not ok. Slide drilling from 3375 to 3420m (no MWD signal).
26/06/04 : Slide drilling from 3420 to 4324m. Torque test Vertitrack, not ok. Pump 9m3 low-viscosity + 6m3 hi-
density pill to clean the well. POOH from 3424 to 3367m. Tight spot @ 3367m. Back ream 3367/3279m. POOH to
surface. Lay down Vertitrack & pick up new one. Surface test Vertitrack, ok. RIH to 2339m. Service TDS &
drawworks.
27/06/04 : RIH from 2339 to 2427m. Torque test Vertitrack, ok. RIH from 2427 to 2836m. Test MWD & Vertitrack, ok.
RIH from 2836 to 3367m. Test MWD & Vertitrack, ok. Wash & down from 3367 to 3396m. Check surveys @ 3365,
3375, 3385m. Ream from 3396 to 3423m. Survey @ 2413m. Ream from 3423 to 3424m. Slide drilling 3424 to
3439m. Rotary drilling from 3439 to 3445m. Slide drilling from 3445 to 3453m.
28/06/04 : Slide drilling 3453/3494m.Attempt to b/ream, not ok, pipe stuck @ 3491m (with circulation), work pipe,
pipe free. B/ream&ream 3491/3484m.Circul hole clean .Slide drilling 3494/3497m.
29/06/04 : Slide drilling 3497/3504m. Pick up from 3504 to 3500m. Pipe stuck, work pipe, free. Pump 9m3 low-
viscosity + 6m3 hi-density pill to clean the well & circulate bottom up. Wiper trip 3504/3364m, ok. RIH 3364/3504m.
Slide drilling 3504/3523m.Rotary drilling 3523/3525m. Slide drilling 3525/3526m.
30/06/04 :Slide drilling 3526/3553m. Rotary drilling 3553/3554m. Slide drilling 3554/3564m.
01/07/04 :Slide drilling 3564/3592m. Rotary drilling 3592/3593m. Slide drilling 3593/3600m. Attemp to pick up, not
pick up, pipe stuck @ 3598m, work pipe, get free jarring down 1 time. Slide drilling 3600/3602m.
02/07/04 : Slide drilling from 3602 to 3619m. Pump 9m3 low-viscosity + 6m3 hi-density pill to clean the well &
circulate bottom up. Pump out of hole from 3619 to 3454m. POOH from 3454 to surface. Lay down bit, Vertitrack,
nortrack, circulation sub & stabilizer. Pull out wear bushing, set test plug & rig up Halliburton lines. Test BOPs, pre-
job safety meeting, test Halliburton lines to 6000psi.
03/07/04 : Test BOPs. 500psi low pressure – 5000psi high pressure (3500psi annular). Test ok. Pick up & test
Vertitrack. Make up new insert bit & BHA with new Nortrack & add shock sub. RIH to 2448m, test Vertitrack, ok. RIH
2448/3456m. Wash down & ream 3456/3619m. Slide drilling from 3619 to 3624m.
04/07/04 : Slide drilling from 3624 to 3663m.
05/07/04 : Slide drilling from 3663 to 3697m. Rotary drilling from 3697 to 3698m in order to improve ROP, without
success. Pump 9m3 low-viscosity + 6m3 hi-density pill to clean the well & circulate bottom up.
20. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 20
06/07/04 : Pump out from 3696 to 3606m. POOH to surface & lay down bit. Test Vertitrack, ok. Make up new bit and
RIH to 2368m. Service Top drive. RIH from 2368 to 3447m. Wash & down 3447/3455m. RIH from 3455 to 3661m.
Wash down & ream from 3661 to 3698m. Slide drilling from 3698 to 3706m.
07/07/04 : Slide drilling from 3706 to 3740m. Rotary drilling from 3740 to 3741m.
08/07/04 : Rotary drilling from 3741 to 3742m. Slide drilling from 3742 to 3780m. Tight zone when back ream: 3726-
3722m & 3770-3762m.
09/07/04 : Slide drilling from 3780 to 3806m. Perform short trip. Back ream out 4 stands from 3806 to 3691m.
Circulate clean hole and start to increase MW 1.17 1.19 sg. RIH 3691/3801m, took 20klbs weight @ 3801m. Wash
& ream to bottom 3806m. Slide drilling from 3806 to 3812m.
10/07/04 : Slide drilling from 3812 to 3848m.
11/07/04 : Slide drilling from 3848 to 3859m. Pump 9m3 low-viscosity + 6m3 hi-density pill to clean the well &
circulate bottom up. Pump out and backream from 3859 to 3719m (tight). POOH without circulation from 3719 to
3660m. Circulate clean hole. POOH to surface. Lay down bit & vertitrack. Pick up & test new vertitrack. Make up bit
and RIH BHA. Change jar.
12/07/04 : RIH to 2369m. Service Top drive & blocks. Slip & cur drilling line. RIH from 2369 to 2485m. Test
Vertitrack, ok. RIH from 2485 to 3774m. Wash & ream from 3774 to 3859m. Slide drilling from 3859 to 3882m.
13/07/04 : Slide drilling from 3882 to 3914m.
14/07/04 : Slide drilling, back reaming and surveys from 3914 to 3945m.
15/07/04 : Drilling (Sliding) from 3945 to 3958m - Circulate - Short trip to 3843m - RIH - Drilling (Sliding) from 3958 to
3068m.
16/07/04 : Drilling (Sliding) and surveys from 3968 to 4000m - Backreaming to 3952m OK - RIH to bottom OK.
17/07/04 : Circulate and survey - POOH to 3825m - Stuck pipes - Work pipes – POOH.
18/07/04 : POOH - BOP tests.
19/07/04 : Make up BHA - RIH - Ream from 3182 to 4000m - Drilling (Sliding) from 4000 to 4004m.
20/04/07 : Drilling (Sliding) and surveys from 4004 to 4031m - Stuck pipes @ 4029m - Work on pipe and free pipes -
Drilling and survey from 4031 to 4050m (Rotary 4039-4044m).
21/07/04 : Drilling (Sliding) and surveys from 4050 to 4087m ; (Rotary : 4068-4074, 4076-4084).
22/04/07 : Drilling (Sliding) and survey from 4087 to 4097m - Short trip to 3950m (Tight spots @ 4039, 4036, 4029
and 4019m) - Drilling (Sliding) and survey from 4097 to 4109m.
23/07/04 : Drilling and surveys from 4109 to 4125m (Rotary 4120-4125) - POOH with rotation and circulation.
24/07/04 : POOH - Make up new BHA – RIH.
25/07/04 : RIH to 4000m - Ream down to 4125m - Drilling (Sliding) and surveys from 4125 to 4137m.
26/07/04 : Drilling and surveys from 4137 to 4170m (Rotary 4144-4155 & 4169-4170m).
27.07/04 : Drilling and surveys from 4170 to 4212m (Rotary 4187-4199 & 4210-4212m)
28/07/04 : Drilling and survey from 4212 to 4228m (Rotary to 4216m) - Short trip to 4041m - Drilling and survey from
4228 to 4263m (Rotary : 4228-4242, 4252-4263).
29/07/04 : Drilling and survey from 4263 to 4294m (Rotary : 4263-4266, 4274-4293). - Circulate - POOH to 4070m.
30/07/04 : POOH - Stuck @ 4030m - Work pipes and free - POOH with circulation and rotation.
31/07/04 : POOH to surface - RIH Schlum and tag @ 3172m - Log Run#1.1.1 (NGT-DSI-GPIT-OBMI) - Change
tools config. - Attempts to pass negative - POOH Schlum.
21. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 21
01/08/04 : POOH and Rig down Schlum - RIH for wiper trip - Reaming down from 3172m.
02/08/04 : Reaming down to 4294m - Circulate and condition mud : hole clean - POOH.
03/08/04 : POOH - R/U and RIH Schlum - Log run 1.2.1 from 4294 to 3169m - R/D Schlum - Prepare for casing job.
04/08/04 : R/U for casing - RIH casing 9"5/8 to 1914m.
05/08/04 : RIH 9"5/8 casing @ 4288m.
06/08/04 : Circulate - Cementing job (14m3
lead slurry d=1.65 + 8.3m3
tail slurry d=1.89) - Nipple down BOP.
07/08/04 : Install well head - Nipple up BOP - Test BOP - Lay down DC+HWP.
• Phase 8”1/2 : 4294 to 4955m
08/08/04 : P/U and test Motor+MWD - M/U BHA - RIH to 4237m - Drill out float collar and shoe to 4288m.
09/08/04 : Clean out to 4294 - Drilling fro 4294 to 4296m - FIT (deq=1.62) - Drilling and surveys to 4328m (Sliding :
4310-4314m & 4319-4323m).
10/08/04 : Drilling (Rotary) and surveys from 4328 to 4369m.
11/08/04 : Drilling (Rotary) from 4369 to 4379m. Sliding from 4379 to 4381m. Drilling with rotary from 4381 to
4412m.
12/08/04 : Drilling with rotary from 4412 to 4445m. Sliding from 4445 to 4448m. Drilling with rotary 4448 to 4451m.
13/08/04 : Drilling with rotary from 4451 to 4462m. Pump out of hole from 4462 to 4434m. POOH from 4434 to
4318m. Circulate. Perform FIT @ 4318m. Results:
3180 psi with MW: 1.27 sg.
Equivalent MW: 1.8 sg.
0.6 bbls injected in formation
RIH to 4346m. Drop & pump down Gyro. POOH from 4346 to 355m. Flow check & POOH with BHA. Retrieve & lay
down Gyro. POOH to surface. Retrieve MWD, lay down stabilizer and motor. Pick up new motor & stabilizer, set
bend to 1.15°. Orient motot & UBHO. Make up bit N° 66. Test motor & MWD. Pick up Monel & RIH with directional
assembly + BHA to 169m.
14/08/04: RIH to 4442m. Wash and ream from 4442 to 4462m. Drill with rotary from 4462 to 4480m. Sliding from
4480 to 4483m.
15/08/04 : Drilling with rotary from 4483 to 4499m. Sliding from 4499 to 4502m. Drilling with rotary from 4502 to
4509m. Sliding from 4509 to 4514m. Drilling with rotary from 4514 to 4518m. Sliding from 4518 to 4522m. Drilling
with rotary from 4522 to 4526m.
16/08/04 : Drilling with rotary from 4526 to 4531m. Sliding from 4531 to 4536m. Drilling with rotary from 4536 to
4540m. Sliding from 4540 to 4544m. Drilling with rotary from 4544 to 4547m. Sliding from 4547 to 4551m Drilling
with rotary from 4551 to 4561m. Sliding from 4561 to 4566m.
17/08/04 : Drilling 4566/4569m. Sliding 4569/4572m. Drilling 4572/4607m.
18/08/04 : Drilling 4607/4625m. Pump out of hole 4625/4618m. Backream 4618/4559m. POOH 4559/4528m, with
max drag 40-50 klb. Work stuck pipe @ 4528m (pack off). Jaring down. Pump low-vis & hi-dens pill to clean the well.
Ream from 4528/4586m, while increasing MW 1.35 sg. Pump out of hole 4586/4555m. Circulate hole clean with
large amount of cavings on shakers.
19/08/04 : Circulate to clean the hole. Pump out 4570/4293m. Circulate to clean the hole. POOH from 4293 to
surface. Lay down MWD, motor, bit. Make up new BHA with new bit (PDC). Test motor & MWD, OK. RIH to 3563m.
20/08/04 : RIH to 4293m. Circulate while Increasing MW 1.40 sg. Wash down 4305/4579m. Wash & ream
4579/4625m. Drilling 4625/4659m. Sliding 4659/4663m. Drilling 4663/4668m. Sliding 4668/4669m.
21/08/04 : Sliding 4669/4672m. Drilling 4672/4681m. Sliding 4681/4685m. Drilling 4685/4690m. Sliding 4690/4694m.
Drilling 4694/4700m. Sliding 4700/4703m.
22. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 22
22/08/04 : Drilling 4703/4734m. Circulate. Perform Short trip: pump out from 4734 to 4588m, max overpull 50 klbs.
RIH from 4588 to 4734m. Sliding 4734/4737m. Drilling 4737/4743m.
23/08/04 : Drilling from 4743 to 4785m. Sliding: 4745/4748m – 4763/4766m – 4773/4779m – 4782/4785m.
24/08/04 : Drilling from 4785 to 4818m. Sliding: 4785/4789m – 4794/4807m – 4811/4818m.
25/08/04 : Drilling from 4818 to 4850m. Sliding: 4818/4821m – 4825/4833m – 4835/4843m – 4846/4850m.
26/08/04 : Drilling from 4850 to 4880m. Sliding: 4850/4851m – 4855/4861m – 4866/4872m – 4873/4880m.
27/08/04 : Drilling from 4880 to 4900m. Sliding: 4880/4887m – 4889/4896m.
Perform Short trip from 4900 to 4774m.
Drilling from 4900 to 4913m. Sliding: 4900/4907m.
28/08/04 : Drilling from 4913 to 4918m. Loose MWD signal & attemp to regain without success. Drilling from 4918 to
4919m. Geological circulation bottom up. POOH to surface. Perform BOP test:
29/08/04 : Continue Test BOP. RIH with new BHA & new bit to 4293m. Circulate bottom up. POOH from 4293 to
4265m. Repair lower & upper I-BOP valves.
30/08/04 : Continue change I-BOP valves. RIH to 4895m. Ream from 4895 to 4919m. Circulate out trip gas. Drilling
with rotary from 4919 to 4937m.
31/08/04 : Drilling with rotary from 4937 to 4955m. Pump 6 m3 high density pill & circulate hole clean. POOH from
4955 to 336m.
01/09/04 : POOH to surface. Clean and organize rig floor. Perform electrical logs.
Run #1: UBI-NGS-GPIT-DSI
Run #2: AIT-PEX-EMS
02/09/04 : Lay down motor, MWD, monel & 2 stabilizers. Make up wiper trip BHA & RIH to 4270m. Slip and cut
drilling line. Service Top Drive and blocks. RIH from 4270 to 4630m, tight hole. Wash & ream from 4630 to 4833m.
POOH with circulation from 4833 to 4771m (check BHA condition, large amount of metal on magnet).
03/09/04 : POOH with circulation from 4771 to 4630m. POOH to surface. Lay down scrapper (good condition). Lay
down full gauge near bit stabilizer. Make up under gauge near bit stabilizer. RIH to 4261m. Service Top drive &
blocks. RIH to 4915m, hole in good condition. Wash and ream from 4915 to 4955m. Circulate bottom up. Perform
short trip from 4955 to 4875m. Hole in good condition. Pump & displace 28 bbl heavy pill @ 4955m (1.9 sg).
04/09/04 : POOH to surface. Rig up casing equipment. RIH 7” Liner to 888m. Rig down casing equipment. Circulate.
RIH 7” Liner (with DP) to 1390m.
05/09/04 : RIH 7” Liner with DP to 4893m. Wash down from 4893 to 4902m. Rig up cementing head and lines to
cementing unit. Circulate @ 4902m. Test cementing lines to 4000 psi. Circulate. Drop ball and set liner hanger @
4005.5m. Circulate. Pump 20 bbl diesel + solvent – 58 bbl tuned spacer – 145 bbl cement slurry. Drop plug, pump 2
bbl tuned spacer and displace with 372bbl of mud. Bump plug with 3700 psi. Hold pressure for 10 min. Bleed off
pressure. Set packer with 60 klbs. Sting out of liner. Space out DP. Circulate in reverse 396bbl (intenal volume of DP
x 1.5).
7” Liner Shoe @ 4902m
7” Liner landing collar @ 4855.5m
7” Liner Top @ 4005.5m
06/09/04 : Finish reverse circulation. Circulate out 19.5bbl of cement & spacers. Pump 31bbl of walnut pill. Circulate
in reverse walnut pill. POOH running tool & DP from 4005 to 755m. Lay down 6”1/2 DC out of derrick. POOH DP to
surface. Pull wear bushing. Change bottom pipe rams to 2”7/8x5” variable rams. Test BOP: pull up test plug, install
new rubber. Start BOP test, attempt to teszt upper 5”1/2 pipe rams. Search for leack. Ram packing leak on lock
down flange. Tighten it, re-test, still leaking. Drain BOP stack. Change ram packing on lock down flange. Re-fill BOP
stack. Continue BOP test; 2 test succesfull, 3 test leaking. Other ram packing leak on lock down flange and choke
HCR valve leaking. Drain BOP stack. Change second ram packing on lock down flange. Re-fill BOP stack. Close
manual valve on choke line in order to continue BOP test and change the HCR valve later on. Continue BOP test, no
leaks.
23. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 23
• Phase 6”: 4955 to 5600m
07/09/04 : Continue BOP test, no leaks. Re-install check valves on both kill lines. Finish BOP test. All good, except
choke line HCR valve. Pull test plug. Lay down test assembly. Re-install wear bushing. Change elevator. Pick up DC
handing tools. Pick up motor. Wrong conection on top motor. Change out Baker locked XO on motor. Make up float
sub, stabilizer, UBHO, MWD. Connect TDS. Test motor, negative test. Pull out MWD, clean out MWD and make
back up. Re-test MWD & motor, test succesfull. Continue to pick up BHA (4”3/4 DC & 3”1/2 DP) and RIH to 1227m.
Fill pipes and break circulation. RIH from 1227 to 1990m. Fill drill string every 25 stands. Pull & install casing rubbers
protectors as per program.
08/09/04 : RIH to 3900m - Test Casing to 5000psi : OK - RIH to 4845m - String plugged – POOH.
09/09/04 : POOH - Flush lines - RIH without MWD - Drill out cement.
10/09/04 : Drill out cement - Monitor well (no pressure) - Drill from 4957 to 4958m - LOT (EMW=1.66, injected
3.75bbl) - Run MWD probe with wireline.
11/09/04 : Rig down wire line - RIH to 4945m - Test MWD - Relog section from 4945 to 4958m - Drilling (rotary) and
survey to 4983m - Circulate - Drilling ahead to 4988m.
12/09/04 : Drilling and surveys from 4988 to 5000m (Sliding 4998-4999) - POOH to change bit.
13/09/04 : POOH - Change BHA and bit - RIH - Drilling from 5000 to 5004m (Sliding : 5003.5-5004m).
14/09/04 : Sliding from 5004 to 5007m - Rotary drilling to 5013m - Circulate for samples - Perform survey - POOH -
P/u coring BHA.
15/09/04 : RIH Core assy - Cut core from 5013 to 5015.5m - Core jammed – POOH.
16/09/04 : POOH - Retrieve core K#1 (Recuperation 2m = 80%) - RIH turbine - Relog from 4995m to 5012m (driller
depths).
17/09/04 : Ream cored section - Turbodrilling and surveys from 5015.5 to 5035m.
18/09/04 : Turbodrilling and surveys from 5035 to 5064m.
19/09/04 : Turbodrilling and surveys from 5064 to 5093m.
20/09/04 : Turbodrilling and surveys from 5093 to 5124m.
21/09/04 : Turbodrilling and surveys from 5&é’ to 5150m – Circulation.
22/09/04 : Circulate - POOH - R/u logging equipment - Log and lay down Run#3.1.1. : AIT-PEX-EMS - R/u
Run#3.1.2 : UBI-NGT-GPIT-DSI.
23/09/04 : RIH and record Run#3.1.2 : UBI-NGT-GPIT-DSI - Log Run#3.1.3 : CBL-VDL-CCL - RIH scrapper assy.
24/09/04 : RIH - Scrap 7" Liner - POOH - RIH RTTS packer.
25/09/04 : RIH - Test casing to 6600psi – POOH.
26/09/04 : Test BOP - Make up and RIH test assy.
27/09/04 : RIH test assembly
28/09/04 : RIH test assembly; set packer at 4870m.
29/09/04 : Open well to 8/64” adjustable choke. Switch to 24/64” for clean up ; Gas at surface; flow to fare.
Switch to 28/64”, then 32/64” choke.
30/09/04 : Swtich to 36/64”, then 40/64” and pass flow through separator; switch to 44/64” choke, then to 36/64” and
one contingency set of surface sample at separator. Switch to 28/64”
24. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 24
01/10/04 : Switch to 24/64”; close well on POTV and start build up.
02/10/04 : Continue first build up (total 2h). Open well on 24/64” and pass through separator; traces of diesel;
decided to make now clean up, divert flow to fare and switch to 32/64”, then 44/64”, 48/64”, 52/64” and 24/64”.
Close well on POTV and start build up 2 : 24h.
03/10/04 : Open well for main flow; First flow, 6h on 24/64”choke; second flow, 6h on 28/64”, third flow 6h on 32/64”.
04/10/04 : Continue flow on 32/64”choke; switch to 36/64” choke; well head pressure and temperature stabilized;
only light smell of diesel in the effluent, no visual evidence of diesel; Take PVT sample. Close well on POTV for main
build-up (60h).
05/10/04 : Main Build up.
06/10/04 : Main build up.
07/10/04 ; Open well for PLT. Run PLT. Unable to pass in 6section at 4960m; lost signal after first flowing pass.
POOH to surface
08/10/04 : RIH PLT#2 and perform it from 4905 to 4960m. Close well at POTV; Pooh and rig down PLT.
Close well at surface. Pooh test assembly.
09/10/04 : POOHtest assembly.
10/10/04 ; POOH test assembly.
11/10/04 : POOH test assembly to surface and rig down; End of test at 01h30.
BOP tests – RIH with tricone.
12/10/04 : RIH to 4930m. Wash & ream (light reaming) from 4950 to 5093m. Gas increase to 46%, close annular &
circulate through choke. Wash & ream from 5093 to 5150m. Drilling from 5150 to 5151m. Gas increase to 53%, pick
up to 5145m, close annular & circulate through choke. Drilling from 5151 to 5168m.
13/10/04 : Drilling from 5168 to 5172m. Circulate. POOH to surface. Make up BHA with turbine and impregnated bit.
RIH.
14/10/04 : RIH to 4979m (tag). Wash & ream from 4979 to 5136m. Log GR from 5136 to 5172m. Perform Survey.
Turbodrilling from 5172 to 5185m.
15/10/04 : Turbodrilling from 5185 to 5223m.
16/10/04 : Turbodrilling from 5223 to 5225m. Stall turbine @ 5225m, attempt to back ream, neg. Work stuck bit &
free turbine. Ream & back ream last stand. Turbodrilling from 5225 to 5258m.
17/10/04 : Turbodrilling from 5258 to 5277m. Short trip from 5277 to 5160. RIH to bottom. Turbodrilling from 5277 to
5296m.
18/10/04 : Turbodrilling from 5296 to 5338m.
19/10/04 : Turbodrilling from 5338 to 5382m.
20/10/04 : Turbodrilling from 5382 to 5394m. Relog GR from 5374 to 5379m, due to trouble with MWD. Turbodrilling
from 5394 to 5422m.
21/10/04 : Turbodrilling from 5422 to 5464m.
22/10/04 : Turbodrilling from 5464 to 5472m. Back ream tight spot from 5472 to 5282m. POOH to surface, lay down
bit, turbine & slim pulse. Pick up new turbine (with up sleeve 5”1/2 & lower sleeve 5”15/16). & slim pulse, test same.
Make up new bit DDS Impregnated, SSS82. RIH with BHA to 115m & change out jar.
23/10/04 : RIH to 4881m. Slip & cut drilling line. Service TDS. RIH to 5293m. Wash down from 5293 to 5440m (relog
5317/5324m for GR calibration). Wash & ream from 5440 to 5472m. Turbodrill from 5472 to 5488m.
25. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 25
24/10/04 : Turbodrilling from 5488 to 5533m.
25/10/04 : Turbodrilling from 5533 to 5575m.
26/10/04 : Turbodrill from 5575 to 5600m. Circulate hole clean & flow check. POOH from 5600 to 5165m: Back
ream, ream & pump out 5539/5537m, 5506/5504m, 5287/5285m, 5215/5210m. Circulate open hole volume, perform
flow check & pump slug. POOH from 5165 to 4344m.
27/10/04 : POOH from 4344 to 1825m. Can’t drop 2”1/4 rabbit due to mud viscosity. Circulate slug out of string,
rabbit still not able to drop in drill string. POOH to surface. Run WLL 4.1.1 (AIT – EMS – PEX). Attempt to pass
5288m without success. Log section from 5288 to 5120m. POOH WLL in order to perform control trip.
28/10/04: POOH WLL tools. Pick up & make up wiper trip BHA. RIH to 4900m. Change and test wash pipe & service
TDS. RIH from 4900 to 5250m. Wash & ream from 5250 to 5600m – Tight spots: 5285, 5306, 5505m. Hard reaming
from 5511 to 5517m. Very hard reaming from 5537 to 5539m -. Pump 45 bbls of hi-vis pill & circulate hole clean.
29/10/04 : Circulate out hi-vis pill. Hole clean. POOH without circulation & without rotation from 5600 to 5250m. No
overpull. POOH to surface. Pick up electrical logging tools. Run WLL# 4.2.1 (UBI-NGS-GPIT-DSI).
30/10/04 : Continue to run WLL #4.2.1 (UBI-NGS-GPIT-DSI). POOH & lay down. Run WLL #4.2.2 (AIT-EMS-PEX).
POOH & lay down. Pick up, make up & test MDT logging tools (WLL 4.2.3). RIH to 1698m. Rig up and install wire
line equipement. Perform dummy run with wire line to 1650m.
31/10/04 : POOH dummy run. RIH TLC MDT from 1698 to 4866m. Make up XO’s and side entry sub. RIH electric
line with wet connector. RIH TLC MDT from 4866 to 4893m. RIH electric line and make good connection with logging
tools. RIH TLC MDT from 4893 to 4930m. RIH & log with TLC MDT from 4930 to 5340m.
01/11/04 : RIH & log with TLC MDT from 5340 to 5368m. Upper MRMS valve not functioning, no multi sampling
possible; Attempt to set dual packer : internal valve remained open, unable to operate dual packer; POOH & log with
MDT from 5368 to 5024m. POOH TLC MDT to 4879m. POOH electric line & lay down side entry sub. POOH TLC
MDT to surface. Lay down MDT tools. Perform BOP test.
03/11/04 : Perform VSP (149 stations) - Check MDT tool.
04/11/04 : Repair MDT tool - RIH MDT in TLC mode to 4850m - RIH wet connector.
05/11/04 : RIH wet connector - RIH MDT connected to 5346m - Attempts to take sample negative (Problems on flow
control valve: unable to operate flow control module; Trouble shooting with pump-out module: unable to take fluid
sample) - Perform pretest @ 5368m - Attempts to repair pump module negative – POOH.
06/11/04 : L/d MDT - RIH for wiper trip - Circulate (Maximum Total Gas = 33%) - POOH to shoe – Circulate
(Maximum Total Gas = 3.4%) and wait for Schlumberger spare parts.
07/11/04 : Circulate - POOH - Repair MDT - RIH MDT with DP.
08/11/04 : RIH MDT @ 4855m - Circulate to observe normal pressure - P/u Sub entry sub and set wet connector -
RIH to 5348m - Set Dual packer – Sampling.
09/11/04 : Continue sampling @ 5348m - Deflate packer - Set packer @ 5259m - Sampling - Deflate packer
(4000lbs overpull)- Attempts to set packer @ 5074m negative - POOH - R/d MDT.
10/11/04 : Recover MDT samples – End of Drilling Operations on 10 November 2004 at 0h15.
Well suspended by one bridge plug @ 4874m and two cement plugs (4874-4674m and 4946-4846m).
15/11/04 : Rig Demobilization at 12h.
31. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 31
Comments:
From 2436m to 2589m (drilling with Vertitrack without azimut measurement), the azimut of the well is assumed to be
the azimut of the window, i.e 272° E.
35. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 35
3.1. Mud Logging General Data
The Geoservices mud logging ALS 2.5 unit arrived on location on 02 October 2003 and the well was spudded on 6-
10-2003.It was operational from 6-10-2003 to the end of the well (10 November2004).
Standard equipment (depth sensors, pit levels, SPP, MW in/out, pump sensors, torque and RPM sensors…) and
extra equipment were installed: Real time data transmission link to the base, and, from 20-12-2003, high quality gas
detector system type Reserval with GZG constant volume gas trap. This Reserval was in use all along the drilling of
the side-track, with OBM mud.
The gas trap was located on shaker box where the mud enters directly, without “waterfall” inside the flow line to
avoid light gases losses. Two gas sample lines in PVC run between trap and detector, without buckle to avoid water
condensation and deposit; The total transit time was 55 to 65 seconds.
36. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 36
3.2. Mud Logging Cost (Side Track only)
MD drillers (M):2406m-5150m
Type Days in Daily cost Total cost
operation $ $
Mud logging unit : ALS 2.5 194.5 698 135761
Real time link 194.5 86 16727
Reserval 194.5 389 75660.5
Benzene detector 6.5 540 3510
Benzene box 1200
DTM 1+4 3576
236434.5
Crew man daily cost total cost
day $ $
TDC 2 140 54460
Mud logger 2 93 36177
Sample catcher 2 37 14393
105030
Wooden box & plastic + paperbags & metalic canned 5959
Mud logging cost (US $) 347423.5
Activities level credit 1% 3390.6
Total Mud logging cost (US $) 344032.9
Date :30-04 to 10-11-2004(12h)
37. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 37
3.3. Cutting Collections
In addition, 250cc of slightly washed undried, in plastic bag, were taken each 10m and sent quickly to TOTAL
France, for quick paleontological datation and geochemistry.
38. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 38
3.4. Hydrocarbon Shows
Comments
The observations were difficult due to Oil Based Mud.
In Los Monos Formation, from 4604 to 4607m, only a few patchy, light yellow direct fluorescence was observed on
Sandstone.
In the Huamampampa reservoir, from 4914 to 4955m, the direct fluorescence was uniform, fair yellow, with a whitish
blue, fast cloudy cut. Down from 4955m to 5009m the direct fluorescence decrease in intensity, and its color trends
to brown. Cut fluo decrease also in intensity, down to 4989m.
Note, between 5019 and 5022m the presence of very few small plaques of brown bitumen, with light yellow direct
fluo and cut.
After 5022m to TD (5600mMD), no shows were observed.
39. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 39
3.5. Gas Shows
The Gas log, and the GWD log (Gas while drilling) are shown in Annex 3&4.
3.5.1. Quality Control
• As in the first ICS-X1 member, line and panel were tested regularly for Quality control .
o The line was controlled twice a day, injecting 20cc methane with syringe in simple aspiration
above the gas trap. Transit time was between 55 to 65 seconds, and value from 4 to 6% of CH4
during the whole well.
o The panels Main and back-up) were checked every 5 days with 1% and 10% gas mixture. The
% errors were 0.5 to 1% for C1-C2-C3, and 2 to 4% for C4 –C5, far away from tolerance limit.
o During the casing set, a long time line – panel (close circuit) output check was systematically
made.
o C1-C5 curves permanent comparison between Main FID and back up (on Winlog file)
As in ICS-X1, the main problem of the quality control stays in the difference between the Total Gas reading (TG) and
the corrected sum SumCor=(C1+2C2+3C3+4C4+5C5).
Theoretically, the ratio TG/SumCor should be equal to 1 +/- 0.2, i.e. between 0.8 and 1.2, and, But in this well,
values around 2 to 4 and locally up to 8 have been observed.
This phenomenon seems to be independent of the types of gas-trap and chromatograph.
It was observed, in first member, with classic FID+ old GZ11 degaser, with Geo-Fast FID + constant
volume GZG gas trap, and with the Reserval + GZG gas trap; the gap still persisted with all
combinations(but less important with classic FID), included the reserval from sidetrack member.
No obvious explanation could be found:
CO2 hypothesis is not possible, because the FID detector does not read CO2.
Heavier gas as C5 could explain this gap; but if they exist, they do not come from organic matter, because bitumen
and asphalt were not seen in the cuttings.
It could be a pollution made by the Oil Base Mud; Some similar events were reported in Algeria and Syria, with the
same mud and weak values of gas done by low porosity (like here).
But in ICS-X1, the gap existed, in water base mud and aerated mud.
Note that Geoservices already encountered this phenomena in several similar wells in Bolivia.
Meanwhile, the data are good, and usable for a GWD interpretation
• Drilling bits effects on the Total gas value and composition (Fig 3.1 and 3.2)
The two figures illustrate the influence of the drilling bits on the gas composition observed in surface. Three
impregnated bits were used, after coring, to the bottom (from 5015.5 to 5150m, for the first one, and from 5172 to
5600m for the two other), with a conventional bit between 5150 and 5172m. From 5172 to 5526m, the Geofast FID
was used, due to a Reserval failure, but it seems that this change did not affect the results. The drilled lithologies
varied between Siltstone, Sandstone and Shale.
It can be seen that the “blue” points, representative of the intermediate conventional bit, follow the “green” and
“yellow” trend, meaning that the cloud “red”, “magenta” and “ochre”, is representative of the influence of the
impregnated bits with turbodrilling.
The “Rock-Eval” effect observed in the first well is still present here. The figures below show an increase of the
Normalized Total Gas, and a diminution of %C1 versus Total Gas, meaning that a greater amount of heavier gases
are extracted.
40. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 40
Colour Codes for figures 3.1 and 3.2
Green : Los Monos Siltstone Conventional bit Reserval
Yellow : HMP Sandstone Conventional bit Reserval
Red : HMP Sandstone Impregnated bit Reserval
Blue : HMP Sandstone Conventional bit Reserval
Magenta : HMP Sandstone, Siltstone & Shale Impregnated bit Geofast
Ochre : HMP Shale Impregnated bit Reserval
47. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 47
3.5.3. Gas while drilling (GWD) preliminary analysis
The GWD composite log (Annexe 4) has 6 gas analysis column:
o Column 1: TG and NTG (normalised total gas)
o Column2: C1/C2 and TG/Sum Cor (Corrected Sum of C1-C5 read on the chromatograph) for
theoretic quality control. On ICS-X1-ST1 well, this quality check is not available (see chapter 3.4.1)
o Column 3:’’ Wetness’’(C2+C3+C4+C5)/Sum C) versus ‘’Balance’’ (C1+C2)/C3 curves in opposite
drawing disposition.
o Column 4: C1 and C3; C1 decrease and C3 increase when entering in oil window.
o Column 5: C45 vs C12 to see the heavy gas components evolution with the depth.
o Column 6: C45 and iC5/nC5; same objective as column 5.
See Annex 4.
This chapter synthesizes the “rush” analyses separately done on 8”1/2 and 6” phases of the ICS-X1-ST1 Well, down
to 5150m. On both phases, the mud logging data depths have been shifted approximately 3m downward in order
than the Total Gas variations fit with GR and resistivity. This offset corresponds also with the observed shift between
geological descriptions, in driller depths, and wireline loggings.
8”1/2 Phase
QC:
Meanwhile, the data are good, and usable for a GWD interpretation (Fig 3.3 & 3.4). In details, the possible effects of
the short trip at 4900mMD, and mainly the bit change at 4818mMD might have an influence on this interpretation.
The HC bearing levels obtained with the cut-off agree, more or less, with the Petrolan interpretation
Results:
Gas events seem to be enough significant (Fig 3.5 & 3.6) to indicate the presence of HC bearing levels (see table
below).
Composition analyze leads to identify a single gas signature in both formations (Los Monos and Huamampampa).
The Huamampampa reservoir N1 shows a single fluid behavior, therefore, no contact.
It is not possible to precise the bottom fluid nature.
48. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 48
GWD QUALITY CONTROL 1/2
Context:
-Deviatedl well section (dev max=10.34°)
GL= ? ZT= ?
- Rig:
- Mud:OBM: 1.40 to 1.42 g/cc
- Geoservices gas chain: GZG + Reserval? Software
version:? Analyse module: ?
- Gas data sample rate: 1m
ICS-X1.ST1 8’’1/2 phase
Maximum C1 value reached at
4606m: 38 259 ppm:
No Reserval saturation
Despite low values of C1/C2, C1-
C2 separation quality remains
medium
Only C5 values are locally in
limit of representativeness
Global good consistency between
Detector and chromatograph
measurements, despite some
strong values.
Fig 3.3: GWD Quality Control (4555 – 4960m)
49. TE&PB INCAHUASI-X1-ST1 ICS-X1-ST1
ICS-X1-ST1 GWR 49
GWD QUALITY CONTROL 2/2ICS-X1.ST1 8’’1/2 phase
Good consistency
between the different
compounds
measurements
Fig 3.4: GWD Quality Control (4575 – 4965)