This document contains the resume of Dale F. Baade II. It summarizes his professional experience as a Senior Process Safety Engineer and Relief Valve Specialist, providing expertise in process hazard analysis, auditing, and managing relief systems. It lists his responsibilities in various roles, including facilitating HAZOP studies, developing reliability programs, and training personnel. His education is included as a B.S. in Mechanical Engineering from Oklahoma State University. Contact information and areas of specialized computer skills are also provided.
How Bell Energy can help you be a Sustainable and Profitable OrganizationChandrashekhar Kulkarni
Welcome to Bell Energy Corporate Presentation where we showcase our value added services and our resources that will help your company manage Process Safety, Health Safety & Environment, Asset Integrity, Corporate Governance and Sustainability.
How Bell Energy can help you be a Sustainable and Profitable OrganizationChandrashekhar Kulkarni
Welcome to Bell Energy Corporate Presentation where we showcase our value added services and our resources that will help your company manage Process Safety, Health Safety & Environment, Asset Integrity, Corporate Governance and Sustainability.
Sinds jaar en dag gebruiken hypotheekadviseurs het hypotheekrenteoverzicht waarin de aanvangsrente wordt getoond. In eerste instantie begrijpelijk, want die aanvangsrente is wat de geldverstrekkers proactief communiceren. Maar als je er wat langer over nadenkt, wordt het minder logisch.
Het is de taak van de adviseur om de vertaalslag te maken van wat geldverstrekkers communiceren naar wat voor de klant begrijpelijk en van toegevoegde waarde is. Die meerwaarde bestaat uit inzichten en advies. En als het goed is, streef je ernaar om de klant aan een hypotheek te helpen met de voor hem beste voorwaarden, tegen de laagste kosten.
Doordat geldverstrekkers bij aanvang van een hypotheek een risico-opslag hanteren, is de rente die de klant betaalt, aanvankelijk hoger. Zodra het risico daalt, bijvoorbeeld door aflossing, vervalt de topopslag. Nu zijn er veel verschillen in de wijze waarop die opslag vervalt, zo blijkt uit een onderzoek dat we recentelijk hebben uitgevoerd. De ene geldverstrekker verlaagt het automatisch, de andere periodiek en weer anderen verlagen het alleen op verzoek. Ook de staffel waarmee de renteopslag wordt verlaagd, verschilt per aanbieder. Op www.looptijdrente.nl kun je per aanbieder zien of deze automatisch de renteopslag verlaagt en wat de gemiddelde looptijdrente is.
Het is niet voor niets dat veel aanbieders liever de aanvangsrente communiceren. Wanneer je in je advies het vervallen van de renteopslag meeneemt, kom je tot lagere hypotheekrentekosten dan wanneer je uitgaat van de aanvangsrente. Bij een annuïteitenhypotheek van € 204.000 kan dat in totaal een verschil opleveren van bijna € 15.000,-.
De partijen die in het traditionele hypotheekrenteoverzicht als goedkoopste uit de bus komen, zijn over de gehele looptijd van de hypotheek dus lang niet altijd de goedkoopste. De informatie die je in het hypotheekrenteoverzicht ziet, is dus misleidend. Zeker wanneer je klant van plan is lang in de woning te blijven wonen en/of extra aflossingen te doen. Begin 2017 brengt De Nationale Hypotheekbond een tool uit, zodat adviseurs voortaan naast de aanvangsrente ook de looptijdrente kunnen hanteren. Want het huidige hypotheekrenteoverzicht alleen is echt niet meer van deze tijd.
Omdat lang niet alle hypotheekaanbieders automatisch de topopslag laten vervallen, moet de klant daar vaak zelf om vragen. Benader je klanten proactief die voor renteafslag in aanmerking komen – daar is gewoon software voor – en laat zo je meerwaarde zien. Gebruik daarbij eventueel deze voorbeeldbrief. Met slechts een kleine handeling realiseer je zo een aanzienlijke besparing voor je klant. En die zal je daarvoor dankbaar zijn.
Jeroen Oversteegen, directeur De Nationale Hypotheekbond
Sinds jaar en dag gebruiken hypotheekadviseurs het hypotheekrenteoverzicht waarin de aanvangsrente wordt getoond. In eerste instantie begrijpelijk, want die aanvangsrente is wat de geldverstrekkers proactief communiceren. Maar als je er wat langer over nadenkt, wordt het minder logisch.
Het is de taak van de adviseur om de vertaalslag te maken van wat geldverstrekkers communiceren naar wat voor de klant begrijpelijk en van toegevoegde waarde is. Die meerwaarde bestaat uit inzichten en advies. En als het goed is, streef je ernaar om de klant aan een hypotheek te helpen met de voor hem beste voorwaarden, tegen de laagste kosten.
Doordat geldverstrekkers bij aanvang van een hypotheek een risico-opslag hanteren, is de rente die de klant betaalt, aanvankelijk hoger. Zodra het risico daalt, bijvoorbeeld door aflossing, vervalt de topopslag. Nu zijn er veel verschillen in de wijze waarop die opslag vervalt, zo blijkt uit een onderzoek dat we recentelijk hebben uitgevoerd. De ene geldverstrekker verlaagt het automatisch, de andere periodiek en weer anderen verlagen het alleen op verzoek. Ook de staffel waarmee de renteopslag wordt verlaagd, verschilt per aanbieder. Op www.looptijdrente.nl kun je per aanbieder zien of deze automatisch de renteopslag verlaagt en wat de gemiddelde looptijdrente is.
Het is niet voor niets dat veel aanbieders liever de aanvangsrente communiceren. Wanneer je in je advies het vervallen van de renteopslag meeneemt, kom je tot lagere hypotheekrentekosten dan wanneer je uitgaat van de aanvangsrente. Bij een annuïteitenhypotheek van € 204.000 kan dat in totaal een verschil opleveren van bijna € 15.000,-.
De partijen die in het traditionele hypotheekrenteoverzicht als goedkoopste uit de bus komen, zijn over de gehele looptijd van de hypotheek dus lang niet altijd de goedkoopste. De informatie die je in het hypotheekrenteoverzicht ziet, is dus misleidend. Zeker wanneer je klant van plan is lang in de woning te blijven wonen en/of extra aflossingen te doen. Begin 2017 brengt De Nationale Hypotheekbond een tool uit, zodat adviseurs voortaan naast de aanvangsrente ook de looptijdrente kunnen hanteren. Want het huidige hypotheekrenteoverzicht alleen is echt niet meer van deze tijd.
Omdat lang niet alle hypotheekaanbieders automatisch de topopslag laten vervallen, moet de klant daar vaak zelf om vragen. Benader je klanten proactief die voor renteafslag in aanmerking komen – daar is gewoon software voor – en laat zo je meerwaarde zien. Gebruik daarbij eventueel deze voorbeeldbrief. Met slechts een kleine handeling realiseer je zo een aanzienlijke besparing voor je klant. En die zal je daarvoor dankbaar zijn.
Jeroen Oversteegen, directeur De Nationale Hypotheekbond
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In order to introduce myself, as a hard worker and team player, who already has some strong experience as a Process Control Engineer, hereby I’d like to present in a summary manner my background and expertise, while stating my willingness to contribute with my employers in achieving goals and reaching high levels of quality and profitability in business.
Thanks in advance for your interest in my profile.
Regards.
Fernando Vasquez.
In order to introduce myself, as a hard worker and team player, who already has some strong experience as a Process Control Engineer, hereby I’d like to present in a summary manner my background and expertise, while stating my willingness to contribute with my employers in achieving goals and reaching high levels of quality and profitability in business.
Thanks in advance for your interest in my profile.
Regards.
Fernando Vasquez.
In order to introduce myself, as a hard worker and team player, who already has some strong experience as a Process Control Engineer, hereby I’d like to present in a summary manner my background and expertise, while stating my willingness to contribute with my employers in achieving goals and reaching high levels of quality and profitability in business.
Thanks in advance for your interest in my profile.
Regards.
Fernando Vasquez.
1. DALE F. (RICK) BAADE II
10511 Seaford, Houston, Tx 77089
(832)771-1972 (Cell) - rickbaade@yahoo.com
SUMMARY
I am currently a senior Process Safety Engineer in which I facilitate Process Hazard Analysis by
use of the HAZOP and What-if techniques to identify high risk hazards within Chevron and I
perform OE and PSM audits within Chevron businesses. I am a trained instructor for Managing
Process Safety (MPS) in Chevron and Management of Change (MOC) classes. In a previous job
I held the position of a Senior Mechanical Reliability Engineer with extensive experience in
refineries and chemical plants. I have expertise in reliability of fixed equipment including safety
relief devices, pressure vessels, piping, and specialty valves. I have extensive knowledge of
specialized computer programs including Plant Condition Management System (PCMS), PHAPro
Process Safety reporting program, and Excel. My key strengths include process safety
management systems in accordance with OSHA 1910.119, knowledge of codes and standards,
team leadership, and communication. I was a Subject Matter Expert (SME) for relief devices at a
refinery in Texas City.
CAREER HIGHLIGHTS
Trained instructor for the 4 day MPS in Chevron class and for the 2 day MOC class. I have co-
instructed 5 MPS in Chevron classes in various location including Houston; Luanda, Angola; and
Lekki, Nigeria. I had the opportunity to update the MPS in Chevron presentation to help give clarity
to the relief protective devices and effluence headers portion of the slide deck.
Trained auditor for OE and PSM Audits within Chevron. I have performed 5 OE and PSM Audits
within Chevron which included the PSM topics Technical Codes and Standards (TC&S), Process
Safety Information (PSI), and Asset Integrity (AI). I performed the audits in refineries including 1 at
BAPCO in Bahrain and 1 at the Chevron shipping company. I also performed 4 peer reviews on the
OE elements, PSM standards, and SIDs in various locations within EMC, shipping and
transportation, and NMA in Lekki, Nigeria.
Trained Facilitator for Process Hazard Analysis (PHA) including HAZOP Technique, Layers of
Protection Analysis (LOPA), and What-if evaluation. I also have been trained in the IHAZID process
as a Facilitator for Chevron. I have facilitated 6 major HAZOP studies (a Pipestills unit, 3 high
pressure reformer units, an environmental facility, and a Sulfur Recovery Unit) within the refining
industry. I also performed several minor HAZOPs, Mechanical design, and what-if studies within
Chevron. I have extensive knowledge in the field of Risk Management by the use of the PHA
techniques listed above in which I have reduced the refinery Safety Risk profile, reduced the
Environmental Reportable incidences, and improved the Financial Performance.
Developed the Electrical Area Classification (FPM-DC-6987) specification for Chevron to support
the API RP 500 and 505 recommended practices, the NFPA 30, 70, 496, and 497 codes, and the
existing Chevron Engineering specification and Fire Protection Specifications.
Developed safety relief device reliability / maintenance program for a Texas City refinery which
included a proper maintenance process for safety relief devices, a root cause failure analysis
process for failed safety relief devices, and established a computerized program to properly track all
processes that may be performed on safety relief devices. Developed Risk Based Inspection (RBI)
policies and procedures for safety relief devices that predicts failures and establishes inspection
frequencies through the use of actual repair history of safety relief devices.
2. Provided extensive training on the topic of relief devices to all levels of personnel including
Operation, Maintenance, Technical, and Middle management. The training includes basic operation
of safety devices, typical design errors in the relief systems, reliability demonstration of actual
failures, and guidance on what can be done at the employee point-of-view in maintaining a safe and
reliable relief system.
Chaired the Joint PCMS User Group committee to re-design the relief devices module for the
PCMS program. The re-design included the total reconstruction of the relief devices module within
PCMS by establishing proper data fields, terms definitions, and calculations to predict failures and
determine relief device inspection frequencies. This re-design was supported by all other
users/owners of PCMS.
Provided expertise and knowledge to redesign a special high pressure letdown valve (Drag Valve)
for the refinery. This redesign eliminated the fires that routinely occurred on the high pressure unit.
This change also increased valve life and reliability. Fires were prominent with this valve due to the
high cyclic duty, high pressure, high temperature, and unique process properties.
Provide expertise to solve long term reliability issues on heat exchangers such as tube leaks,
flanges design, and tube arrangement. Issues such as how to find and repair tube leaks with
minimum effort. Determining minimum flange thickness for sealing issues and construction.
WORK EXPERIENCE
11/2013 – Present Senior Process Safety Engineer, ETC Chevron, Houston
Provide Process Safety support to Chevron organizations by:
Leading PHAs for projects and facilities using the HAZOP and What-if methodologies,
Functioning as the lead auditor for the Process Safety Standards for OE and PSM audits,
Provide training to employees on the subject of Managing Process Safety in Chevron (MPS),
Provide training to employees on the Chevron MOC standard.
Provide mentoring support to employee on Process Safety concerns, and
Provide functional and peer reviews to Chevron’s businesses in accordance to the Chevron Process
Safety Standards.
4/2009 - 10/2013 PHA/LOPA Facilitator, bp Refinery, Texas City, Texas
This includes:
Leading PHA/LOPA studies for 4 process units, a Sulfur Recovery Unit, and an Environmental
Facility,
Leading a number of HAZOP/LOPA studies for large projects,
Becoming proficient in the PHA Pro reporting software,
Mentoring the Facilitators, Unit Superintendent, Leadership team, and refinery personnel,
Provided training to employees on the subject of Risk Management and participation in PHA
studies.
Promoting action item and recommendation for closures by a thorough review of the closure
statement to match the intent of the action item or recommendation,
Developed a final report template to improve the efficiency of the PHA Facilitators so they can
complete the final report in a timely manner, and
Developed a leadership skill through proper communication to help foster participation in the studies
in order to identify risks
8/2001-4/2009 Relief Valve Specialist and Technical Authority (Mechanical), bp Refinery, Texas City,
Texas
Provide Relief Valve expertise in the area of engineering and reliability.
This includes:
Developed risk based program for determining test frequencies based on probability and
consequences for relief devices,
Reconfigured the Plant Condition Management System (PCMS) program for relief device inspection
process,
Dale F Baade II, Page 2
3. Developing Root Cause Failure Analysis techniques for all personnel in the area of the relief
devices,
Developing standards and policies for bp South Houston
Interpret the ASME Codes, API standards and recommended practices, and
Develop and give training to all levels of personnel within bp refining business units on the subject of
relief devices.
1/2001-8/2001 Mechanical Contact Engineer, ExxonMobil, Baytown, Texas.
Provide Mechanical and Reliability Support for Dewaxing, Hydrofining and Shipping Facilities.
This includes:
Trouble shooting failures by use of RCFA and TapRoot techniques,
Developing Reliability strategies for critical equipment,
Provide reliability and technical support to other members of the Technical Staff Department,
Provide TAR support in defining, developing, budgeting, and implementing TAR.
1996-2001 Reliability Engineer, Amoco Oil Co., Texas City, Texas.
Project manager for RV system design for Reliability and Risk Based Inspection.
Redesigned the CCI DRAG valve, negotiate cost and benefits, and evaluate final results.
Develop action plans to provide long term reliability of chronic equipment.
Provide technical and reliability support for the Residual Hydrotreating Units.
Provided technical and reliability support for the Hydrogen Units.
Developed a 10 year TAR inspection decision program.
Developed Turbine Trip calculation spread sheet program.
Trend and evaluate Pride data for turbine reliability
Evaluate inspection results and recommend repairs for stationary equipment to provide longer
equipment reliability.
Evaluate and make repair recommendation for rotating equipment failures to provide longer
equipment reliability.
Evaluate rotating and stationary equipment data to predict equipment failures.
Evaluate equipment repair history for chronic failures.
Participate and lead Root Cause Failure Analysis (RCFA).
Provide engineering expertise during Unit Shut Downs.
Develop and justify work list for the Unit Shut Downs.
1990-1996 Mechanical Engineer, Amoco Chemical Co., Alvin, Texas.
Provided leadership for PSM and PHA requirements.
Trained as a HAZOP leader.
Responsible for leading minor HAZOP’s for the Olefins complex.
Responsible for helping implement the new Electronic Document Management System (EDMS).
Was responsible for training the technical staff on the new EDMS.
Provide project leadership on small capital projects.
Was responsible for engineering project coordination for the Olefins shut downs.
Developed new process sewer covers to keep hydrocarbon liquids/vapors from escaping.
Designed platforms and structures.
Implemented new level detection technology for cryogenic services.
Designed piping systems to increase production.
Responsible for implementing new pipe stress programs within the technical department.
Responsible for installation of new equipment (pumps, exchangers, vessels, etc.).
Designed tank foundations.
Developed repair procedures for low pressure tanks.
Design relief valve systems using current methodology and codes.
Knowledgeable in API, ANSI, and ASME codes and standards.
Review all relief valve system designs and calculation for the Olefins complex.
Trained current staff in the relief valve methodology and codes.
Provide 24 hour technical support to maintenance and operations.
Responsible for making decisions on emergency work.
Provide consultation and training in cost estimating software.
Dale F Baade II, Page 3
4. Developed the teams priority decision chart for better organization of work load.
Trained and participated in semi-autonomous work group (Technical Team).
Mechanical Engineer Intern, Summer 1990.
1988-1989 O.S.U. Cooperative Education, Stillwater, Oklahoma.
Three semesters for Dow Chemical.
Designed and implemented new screen coating station.
Maintained the operation of a foam and pellethane plant.
1987-1990 Lab Assistant, O.S.U., School of Mechanical and Aerospace Engineering.
Maintained the lab and the machine shop equipment.
Supplied training for the safe operation of shop equipment.
EDUCATION, AWARDS, HONORS, AND ACHIEVEMENTS
U11 and up Girls Division Director for 2006-2007 Space City Fútbol Club
Chaired the PCMS redesign committee
Spring 1990 -- Engineer In Training (EIT) examination.
Oklahoma State University, Stillwater, Oklahoma, B.S. in
Mechanical Engineering, December, 1990.
PROFESSIONAL ASSOCIATIONS
American Society of Mechanical Engineers (ASME)
Questimate User Group, Vice President, Houston, Texas, 1993 - 1994
Pi Tau Sigma, Engineering Honorary, Student Council, 1988
SPECIAL COMPUTER SKILLS
TapRoot Program, PCMS Program, C, Pascal, Fortran, Lotus, Questimate, WordPerfect, Microsoft Word,
Microsoft Excel, Timeline, Microsoft Projects, Freelance, AutoSketch, Caepipe, and Caesar II.
SPECIAL CLASSES/SEMINARS
Advance PHA Leader Course, Revalidating Process Hazard Analyses Course, Layer of Protection Analysis
Course, TapRoot Training; PCMS Administrator; Amoco Production Vessels, Piping, and Exchangers
Course; Amoco Production Pump and Compressor Course; SPC; Quality Training; ISO 9000; Semi
Autonomous Work Groups (Teams); Questimate; ASME/ANSI B31.3; ASME Section VIII Division 1;
National Board Inspection Class for Repairs and Alteration; Chemical/Petroleum Processes, AICHE;
Principles of Project Management; Tech Pro Pump and Seal Course; Welding Engineering Training; AGCO
Relief Valves; DIERS Methodology for sizing Relief Valves (RSSTG); HAZOP Leader/Scribe course.
Dale F Baade II, Page 4