RD2003-030 System Enhancements. System Enhancements, RD2003-030, Priority 4  Improve and enhance the performance and/or add value to existing systems.

Slides:



Advertisements
Similar presentations
Title Slide – Technology or Company Name
Advertisements

SituationGantt Chart Brainstorm:Design Brief Page 1 GCSE Product DesignYour NameCandidate Number.
Third International Conference
The first total drilling fluid in a single sack..
ASPHALT RUBBER BINDER Properties Quality Control An overview of the
PETE 411 Drilling Engineering
TITLE OF PROJECT PROPOSAL NUMBER Principal Investigator PI’s Organization ESTCP Selection Meeting DATE.
Jaypol™ HN70 polymer for Laundry Detergents.
What the Future Holds! Phase 2 Data Collection and Measurement Ruth S. Gubernick, MPH Quality Improvement Advisor Florida Pediatric Medical Home Demonstration.
Drilling Engineering Association Project Proposal DEA #113 – Phase 2 “Drilling Gumbo Shale – A Study of Environmentally Acceptable Muds to Eliminate Shale.
NFS-Cement Shield ® Process. Description NFS-Cement Shield ® Process is a dewatering system that can be applied through the drill string into any fracture.
Strategic formulation
July 29, Bench Top Tests for Surfactant Selection Ayantayo Ajani The University of Tulsa.
MUD SYSTEMS, MUD DATA & HYDRAULICS A.Fresh Water Muds B.Inhibited Muds C.Water Base Emulsion D.Oil Base & Synthetic Muds I- MUD SYSTEMS.
Jaypol™ 213 polymer for Fabric Softeners
DuPont™ FEA-1100: Zero ODP, Low GWP, Non-Flammable Alternative for DuPont™ FEA-1100: Zero ODP, Low GWP, Non-Flammable Alternative for HCFC-141b Helen Walter-Terrinoni.
Fundamentals of Onshore Drilling
STRATEGIES TO INCREASE FUEL EFFICIENCY INCREASE FUEL EFFICIENCY AT LEAST BY 10% IN OUR DEALINGS WITH THE POWER GENERATION INDUSTRY - WHERE GETTING THE.
New Fluid Solutions, Inc. NFS-BlackSeal ®. Overview Generally, the types of formations that are prone to lost returns are cavernous and vugular, naturally.
Enhanced Oil Recovery Through Electro-Treatment GLOBAL OIL RECOVERY SYSTEMS,LLC.
Business Opportunity EPRS Energy Co. Inc.. Overview World-wide oil production has been declining for decades. There are over 400,000 stripper or marginal.
Classification: Internal Status: Draft Cold Climate Lubrication ( the Swedish Experience) "Lubricants Russia 2007", November 28 – 29, Moscow Prof. Thomas.
Severn Tidal Power Feasibility Study Background to the study Terms of reference announced in January 08 Aim of the study: To enable Government to decide.
Rheology of Viscoelastic surfactants and foam in homogeneous porous media Aarthi Muthuswamy, Clarence Miller, Rafael Verduzco and George Hirasaki Chemical.
1 Appraisal Smart Quickstart Guide for Appraisors Last updated: 28 January 2011.
Regional Technical Forum End-use Load Shape Business Case Project Project Initiation Meeting Portland, OR March 5, 2012.
Economic benefits from using formate brines - Latest paper.
NFSI Super System Our Mission Is to provide our customers the best new technologies and select existing technologies with honesty and integrity. NFSI.
Silicate/Polymer Mud System
Performance Through Engineering Extended Reach/Horizontal Drilling Solutions EXTENDED REACH / HORIZONTAL DRILLING.
Bringing Value to Russian Federation Fracturing Business:
Eastern Hemisphere Technology Center Novel Water-Based Systems Development and Field Application of a 3rd Generation Silicate Drilling Fluid Steve Young,
Exploratory IND Studies
SIXTH FRAMEWORK PROGRAMME FP INCO-MPC-1 MEditerranean Development of Innovative Technologies for integrAted waTer managEment.
NFS-Super Squeeze™ “The Hole-In-One” Process. Description NFS-Super Squeeze™ Process is a dewatering system that can be applied directly into the well.
 Definition ◦ Scale up studies refers to the act of using results obtained from laboratory studies for designing a prototype and a pilot plant process;
Patents and Medicines: How the system has discouraged innovation and reduced patient access to benefits of knowledge GREG PERRY Director General, EGA World.
First Sildril-K trial in Russia. Background. Region:Western Siberia, Russia Oil field:Samotlor Operator:TNK-Nizhnevartovsk Drilling contractor:NBN Drilling.
SILICADRILL* - Silicate Water Based Drilling Fluid
S15: Supervision and review. Objective of supervision and review  To ensure that the audit is done efficiently and effectively so that the audit opinion.
The New Drug Development Process (www. fda. gov/cder/handbook/develop
[PROJECT] PROJECT KICKOFF PRESENTATION MONTH DAY, YEAR.
Development of a Research Roadmap Related to Safe and Reliable Transportation of Ethanol in Pipelines Gap Analysis - Phase 1 Prepared for Pipeline Research.
Current Development of Ultra High Temperature Aqueous and Non-Aqueous Drilling Fluids.
Grocery Store Measures Door Gasket, Automatic Door Closers, and Strip Curtain Laboratory Testing.
Utilities’ Update on Energy Savings Assistance Program Studies Ordered in D LIOB Meeting August 21, 2013 Sacramento, California.
Initiatives Drive Pediatric Drug Development January 30, 2002.
Liquid Cationic Coagulant DESCRIPTION BHAVIFLOCK 5070ST is a Medium to High molar mass, High charge density Cationic Liquid Polymer that perform effectively.
Clinical Trials.
Principal Investigator ESTCP Selection Meeting
SCS Summer School 2017 Past Exam Question Russell Cox.
Technologic liquid specific gravity for the well completion and workover brines
COMP390/3/4/5 Final Year Project Introduction & Specification
COMP390/3/4/5 Final Year Project Introduction & Specification
Principal Investigator ESTCP Selection Meeting
Quality Workshop The Local Council Award Scheme is a great guide for good practice in our sector and a way for councils to build confidence in their.
COMP390/3/4/5 Final Year Project Design
Sixth Power Plan Setting Conservation Targets and Implementation Strategies Jill Steiner, Snohomish Public Utility District Northwest Power and Conservation.
COMP390/3/4/5 Final Year Project Design
HN Accounting Network Kim Tree Writing an Alternative Assessment.
Project Management Process Groups
COMP390/3/4/5 Final Year Project Introduction & Specification
Principal Investigator ESTCP Selection Meeting
New Standard for Employer Responsiveness
Principal Investigator ESTCP Selection Meeting
Presentation transcript:

RD System Enhancements

System Enhancements, RD , Priority 4  Improve and enhance the performance and/or add value to existing systems through the application of existing or new technologies

RD A Drilplex

RD A - Drilplex Description Description  Develop additives to increase the technical application of the DRILPLEX system. Technical targets are: enhanced chemical shale inhibition, better fluid loss control and increased lubricity. Additives should not have a significant adverse effect on fluid properties and are low cost. Approach Approach  Compatibility study using commercially available, low cost, regionally available additives. Include new technology additives where appropriate. Deliverables Deliverables  Effective shale inhibitor package for the DRILPLEX system (end Q2).  Filtration control additive, better cost/performance than FLOPLEX (Q3).  List of candidate lubricants from compatibility study.  Temperature limitation of the DRILPLEX HDD system determined (Q4).

A - MSP Gantt Chart  Resource: 6 months  Time spent: 3 months  40% complete

RD A - Drilplex Potassium Salts in fresh water-DRILPLEX Viscosity hump/ transient flocculation effect with all K salts, except TKPP. Hardness data from Oxford clay cubes after recovery from fluids (150°F/ 16hrs).

EMI-733 and KLA-CURE have minimal effect on fluid properties. EMI-578 destroys DRILPLEX rheology. RD A - Drilplex Amine based Hydration Inhibitors in fresh water-DRILPLEX

Summary of Progress/Deviations Summary of Progress/Deviations  TKPP, EMI-733 and KLA-CURE show the most promise as shale hydration inhibitors.  GLYDRIL range of glycols promote foaming, and are ineffective in fresh water fluids.  Increasing the DRILPLEX concentration does not improve chemical shale inhibition.  Potassium salts lead to an increase in fluid loss, and transient flocculation of fresh water based fluids.  Benefits of HIBTROL and other polymeric inhibitors are marginal  Possible new material may invalidate some of this work Next Step Next Step  Compare performance of TKPP, EMI-733 and KLA-CURE using Foss Eikeland clay.  Accretion tests with TKPP, etc.  Final recommendations after long term ageing tests (4 days).  Proceed to Phase 2. RD A - Drilplex

RD B Sildril

Description Description  This project will define the density and temperature limits of the SILDRIL system and seek to identify products, which can be used to enhance its performance at higher temperatures. Specific targets include 12 ppg Sildril stable to 360F and fluids stable at mud weights of ppg  Approach  Compilation of prior field and laboratory data. HTHP density matrix testing of existing products to determine performance limits at different mud weights. Screening of HT products to seek to extend system perfprmance. Deliverables Deliverables  Comprehensive report compiled from lab and field data defining the HT performance limits of the Sildril system at defined mud weight.  Formulations to meet the field requirements of 12 ppg at 360F and ppg. RD B – HT Sildril

B - MSP Gantt Chart  Resource: 9 months  Time spent: 6 days  5% complete

Summary of Progress/Deviations Summary of Progress/Deviations  Project just getting going  Technical Service work in Stavanger has already pushed performance limits to 325F at 11ppg. This fluid successfully applied in an unspecified country  Project will clearly define where Sildril can and cannot be used.  There is significant technical risk the field requirements will not be met fully Next Step Next Step  Start lab work RD B – HT Sildril

RD C Low Cost Ecotrol

RD C – Low Cost Ecotrol Description Description  To source a product that delivers comparable technical performance at a minimum 20% improvement in cost over Ecotrol.  Additional aims are to obtain improved mud make-up in cold, low shear conditions and improved HTHP performance. Approach Approach  Market survey: Web search and existing manufacturer contacts  Mud tests in “Zero FL” and HTHP OBMs  Concentration profiles to assess cost effectiveness. Deliverables Deliverables  Report and recommendation on alternative products (Q3)

 Resource: 0.55 man year  Time spent: 1 month  25% complete RD C – MSP Gantt Chart

RD C – Low Cost Ecotrol Highlights Highlights

Summary of Progress/Deviations Summary of Progress/Deviations  7 Candidate Materials identified and tested so far benchmarked against Ecotrol  Screened in 11.5 ppg and 16.5 ppg Versaclean fluids  Appear at this stage to have a 10% cost advantage in 11.5 ppg Versaclean Next Step Next Step  Continue product screen  Take on the best materials for testing in HTHP fluids RD C – Low Cost Ecotrol

RD D Polymer Stabiliser

RD D – Polymer Stabiliser Description Description  To determine the efficiency of Gallic Acid as a temperature stabiliser for mainstream polymers in various Candidate M-I fluid systems and to provide sufficient information for a patent memo Approach Approach  Conduct screening tests and gather evidence of product efficacy in generic mud systems bench marking against untreated fluids  Determine benefit or otherwise of different alkalinity sources in the test fluids Deliverables Deliverables  Report on test findings and submit patent memo by end Q2

 Resource: 0.05 man year  Time spent: 2 month  80% complete RD D – MSP Gantt Chart

RD D – Polymer Stabiliser Highlight – typical synthetic polymer WB Fluid Benefits seen in Flopro Glydril HT synthetic polymer HT PAC starch fluid No benefits seen in Sildril Dipro

Summary of Progress/Deviations Summary of Progress/Deviations  Gallic Acid tested in HT formulations of Flopro, Dipro, Sildril, Starch PAC, Glydril and HT synthetic polymer  Gallic acid works well in monovalent salt systems  NaOH neutralised salt gives very good results  Optimum ratio of MgO:GA in a RDF enhances rheology  Increases temperature tolerance of PAC and synthetic polymer based FLA to in excess of 300°F  Raises temperature limit of starch based FLA from 250°F towards 300°F  Work on ongoing in Houston and Stavanger  Patent application underway  Additional time used as original allocation not sufficient Next Step Next Step  Complete screening with Summer School Student report and transfer technology RD D – Polymer Stabiliser