API AMPP Certifications
Regulatory inspection of tanks, pressure vessels, process piping, and coating systems performed by certified inspectors to ensure mechanical integrity and regulatory compliance at industrial facilities.
Regulatory inspection of tanks, pressure vessels, process piping, and coating systems performed by certified inspectors to ensure mechanical integrity and regulatory compliance at industrial facilities.
Structural assessment, calculation of the corrosion rate on the bottom and hull, and settlement inspection to determine maintenance intervals during out-of-service periods.
Volumetric and surface verification of boilers, process towers, and storage tanks, including calculation of the maximum allowable working pressure and remaining service life.
Inspection of piping systems using non-destructive testing to detect wall thinning caused by localized corrosion, erosion, or cracking before it leads to containment failures.
QA/QC supervision and quality control by CIP Level 1, 2, and 3 inspectors to ensure proper surface preparation, application, and adhesion in corrosion protection systems.
We use internationally standardized protocols to assess the mechanical condition of tanks, pressure vessels, piping, and protective coatings.
More than 25 years of technical experience in Oil & Gas and energy across 6 Latin American countries.
We guarantee independent and well-founded technical reports to regulatory agencies, ensuring that your equipment operates within safe operating parameters.
The API 653 standard does not specify a single time frame in years, but rather states that the internal inspection interval must be calculated based on the corrosion rate of the tank bottom. The maximum regulatory interval for internal inspection must not exceed 20 years (or sooner if the corrosion rate indicates that the minimum thickness will be reached in less time). External visual and thickness inspections must be performed every 5 years or at specified intervals.
A Level II NDT technician is certified (for example, under ASNT TC-1A) to perform specific non-destructive tests (ultrasonic, penetrant, radiographic) and interpret the results. An API 510-certified inspector is formally authorized by the American Petroleum Institute to conduct a comprehensive inspection of the pressure vessel, evaluate the results provided by NDT technicians, recalculate the maximum allowable working pressure, determine corrosion rates, and sign the certificate of operability or the repair plan.
API 570 classifies pipelines into categories (Class 1, Class 2, Class 3, and Class 4) based on the fluid’s risk level (flammability, toxicity, reactivity) and the pipeline’s location. The frequency of wall thickness inspections at TMLs (Thickness Measurement Locations) is determined by the pipeline class or half of the calculated remaining service life, whichever is shorter, ensuring that the pipeline is inspected before it reaches the thickness-of-withdrawal limit.
The implementation of RBI in accordance with API 580/581 shifts plant shutdowns from a fixed-time basis to a scheme focused on actual risk. This allows for extending inspection intervals on low-risk assets, reducing costs associated with unscheduled scaffolding and isolation, and concentrating investments in non-destructive testing on equipment with a high probability of failure or severe consequences, thereby increasing the plant’s overall availability.
More than 80% of premature failures in coating systems occur due to deficiencies in surface preparation or during the application process (inappropriate relative humidity, trapped solvents, thickness outside tolerance). The AMPP CIP inspector audits each phase of the process in real time in accordance with SSPC/NACE standards, preventing costly rework and ensuring that the corrosion barrier meets its projected service life.
API 579 Level 1 uses simplified tables and on-site calculations; if the defect (e.g., pitting or wall loss due to cracking) does not meet the conservative criteria of Level 1, it is escalated to Level 2 (more rigorous engineering calculations using precise profilometry data). If the geometry is complex or combined stresses are present, a Level 3 evaluation is performed using finite element analysis (FEA), which allows for the validation of the equipment’s integrity while avoiding unnecessary replacements or plant shutdowns.
We provide a comprehensive integrity report that includes: an inspection report signed by an API-certified inspector and bearing the registration seal; a thickness measurement map; a spreadsheet detailing corrosion rates and remaining life; a recalculation of georeferenced photographic records; a prioritized findings matrix; and, in the event of repairs, the recommended work plan in accordance with the applicable code.
Our inspections are strictly independent to ensure the objectivity of the assessment and to avoid conflicts of interest. However, we provide detailed engineering designs and technical specifications so that the client can carry out repair or modification work in accordance with ASME/API code guidelines using qualified welding contractors.
We combine data collection using advanced, high-resolution NDT equipment with quantitative remaining life modeling in accordance with API 579.
Diagnostics aimed at preventing unscheduled downtime by optimizing inspection plans using the RBI methodology to reduce the total cost of asset ownership.
Plans strictly aligned with international standards (API, ASME, AMPP).
Assessments conducted and independently signed by professionals with active registrations on the official API portal (Directory of Certified Personnel) and the AMPP platform.
Cathodic protection - Online
Juan Bermudez
Assets integrity, NDT Inspections, TECNA GPS Interrupter - Online
Diego Mendoza
Carbon Footprint, GIS, HSEQ, Process Safety, Risk, Software Dev, Technology - Online
Erika Milena Rincón
20+ años de experiencia en ingeniería y tecnología en la industria (20+ years of engineer and technology experience in the industry).
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It contains the relevant KPIs to obtain a risk ranking, which are represented by means of dashboards.

Integrates the PIDT Plants with the SCADA tool, in order to calculate the risk, making use of variables such as pressure,
temperature, flow, etc.

Bulk loading of inspections performed on static equipment, generating an inspection plan derived from RBI and sending SAP alerts.
It allows the centralization and codification of the information related to the integrity of the Asset: The necessary nomenclatures are defined in order to identify each document according to its origin. Likewise, each document can be classified in relation to the process in which it is involved. It allows organizing documents by means of a hierarchical tree that enables searches and filters to quickly find documents.

Allows the management, analysis and visualization of information compared to company targets related to:
Allows the evaluation and control of modifications to the design of facilities, operation, organization or activities; prior to implementation, in order to ensure that no new elements will be introduced that increase the risk and existing hazards to the business, people or the environment based on applicable regulations.
Allows the consultation of information associated with the life cycle of the asset and its accessories.
Assesses and analyzes the risk level of the Assets to generate an inspection plan. It is designed to perform the calculation and analysis of static equipment risk under the RP API 581-16 standard. The user will be able to create the required risk assessments
to generate a valuation and inspection plan.

It allows the centralization and codification of the information related to the integrity of the Asset: The necessary nomenclatures are defined in order to identify each document according to its origin. Likewise, each document can be classified in relation to the process in which it is involved. It allows organizing documents by means of a hierarchical tree that enables searches and filters to quickly find documents.
