Gabriel Perez Irion

Chemical absorbers for carbon capture They are similar to as used in gas sweetening, and are mostly Amines. This is how existing processes can solve emerging challenges. Amines are used to capture H2S and/or CO2 (acid gases) from sour gas in a gas processing plant. Liquid amine solvents are contacted with sour gas, generally through counter current method. H2S and CO2 get absorbed in amine (rich amine). Concentrated CO2 (~99%v) liberated from amine can be stored and utilized (CCUS). Amine mixture is composed to absorb H2S selectively over CO2, if required, and for other considerations. The same amines are emerging for exclusive capture of CO2. They can absorb CO2 from gas plants, power-houses, and other industries. MonoEthanolAmine (MEA), Di-EthanolAmine (DEA), Di-IsopropanolAmine (DIPA) MethyDi-EthanolAmine (MDEA) are some of the amines.

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Material Solutions for Subsea Pipeline Risk and Integrity: Carbon Steel with Internal Coating vs. Corrosion Inhibitors Subsea pipelines are crucial for transporting hydrocarbons but face significant corrosion and integrity risks. Two main solutions to mitigate these risks are carbon steel with internal coatings and corrosion inhibitors. Here’s a brief overview of their advantages and disadvantages, along with relevant case studies. 1. Carbon Steel with Internal Coating Advantages: Corrosion Resistance: Internal coatings like epoxy and polyurethane provide a barrier against corrosive substances. Lower Maintenance Costs: Coated pipes reduce the frequency and costs of maintenance and inspections. Extended Lifespan: Coated pipelines, such as the Nord Stream Pipeline, benefit from increased durability and less maintenance. Disadvantages: Application Complexity: The coating process can be intricate; improper application may lead to corrosion. Damage Risk: Coatings can be compromised during installation or operation, exposing the steel. Initial Costs: High-quality coatings may have significant upfront costs, although these can be offset by reduced maintenance. Case Study: Nord Stream Pipeline The Nord Stream Pipeline uses advanced internal coatings that effectively mitigate corrosion, enhancing operational reliability. 2. Corrosion Inhibitors Advantages: Versatility: Effective in various environments and fluid types, suitable for multiple applications. Cost-Effectiveness: Often cheaper than extensive coating systems, particularly in existing pipelines. Ongoing Protection: Provide continuous protection that can be adjusted based on monitoring. Disadvantages: Dependency on Conditions: Their effectiveness can vary with environmental factors, requiring careful management. Environmental Risks: Some inhibitors may harm marine ecosystems in sensitive areas. Frequent Reapplication: Regular monitoring and reapplication can lead to increased operational costs. Case Study: Gulf of Mexico Pipelines Corrosion inhibitors are effectively used in Gulf of Mexico pipelines but require consistent monitoring for effectiveness. Conclusion Both carbon steel with internal coatings and corrosion inhibitors have distinct benefits and drawbacks. The choice between them depends on project conditions and long-term strategies. Combining both approaches may offer the most effective solution for managing subsea pipeline integrity.

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On March 23, 2005, a series of explosions occurred at the BP Texas City, Texas, refinery during the restarting isomerization unit— killing 15 workers and injuring 180 others. The explosions occurred when a distillation tower flooded with hydrocarbons and was overpressurized, causing a geyser-like release from the vent stack. BP formed the BP U.S. Refineries Independent Safety Review Panel also referred as Banker Panel. Excerpt from the Baker Panel report: “BP has emphasized personal safety in recent years and has achieved significant improvement in personal safety performance but BP did not emphasize process safety. BP mistakenly interpreted improving personal injury rates as an indication of acceptable process safety performance at its U.S. refineries. BP's reliance on this data, combined with an inadequate process safety understanding, created a false sense of confidence that BP was properly addressing process safety risks."

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How does LNG disperse when leaking and what happens when the cloud ignites. See the video!

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Eugen has been our colleague for over 30 years and has never shied away from challenges. At #Petrobrazi, he ensures that the refinery follows the best practices and contributes to optimizing our operations within the projects he manages. Discover his story ⬇️ #Petrobrazi90

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Mist, our Methane Inventory and Abatement tool, has some new features tailored to mid and downstream segments. 🛢️ Join us for a Mist webinar 📺 as Christos Kalavrytinos and Anastasia Isaenko reveal the new functionality and share the value it can bring as midstream and downstream operators build and manage their inventory. 📊 📅 Dates 10th July, 9:00 – 10:00 CEST 11th July, 16:00- 17:00 CEST Registration 🔗: https://lnkd.in/d9XqxT3z Topics: 🔍 Introduction to Mist 🔀 The mid and downstream segments and OGMP 2.0 🔄 Mist’s new and updated emission categories ❓ Q&A Don’t miss out on this opportunity to learn more about Mist and its new features. Register now and join us on the 10th or 11th of July! 👈 #mist #methanemanagement #methaneemissions Get to know Mist: www.mist.carbonlimits.no

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Continuing the series of posts about H2 production methods, today I present to you some points about SMR catalyst, support, and promoter. These papers cover the types of catalysts, and what the requirements for catalyst selection are. #Hydrogen #EnergyTransition #SustainableEnergy #GreenHydrogen #CleanEnergy #IndustrialApplications #HydrogenProduction #EnergyStorage #RenewableEnergy #Innovation #SMR #Catalyst

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#pep publishes a report on use of hydrogen as fuel in process heaters and gas turbines, and storage methods. One crucial aspect of hydrogen is its role in decarbonization efforts. However, once produced, hydrogen requires storage if it is not utilized on-site. This report will consider hydrogen's use as a substitute fuel for refinery process furnaces and gas turbines, as well as explore current research into underground hydrogen storage options. Using hydrogen as a replacement for natural gas poses several technical challenges. Hydrogen has only one-third of the volumetric energy content of natural gas, leading to concerns about fugitive losses. Material in contact with hydrogen must be considered since hydrogen embrittlement can occur. Additionally, its higher flame temperature results in increased NOx emissions. Safety considerations are also paramount; hydrogen's wider explosion range, lower ignition temperature, and tendency to form gas pockets at the top of enclosures all warrant careful attention. This report will delve into these issues, addressing the requirements and potential challenges of retrofitting natural gas-fed systems for hydrogen use. We will specifically examine the integration of hydrogen into operations, including analyses of the capital and operating costs associated with retrofitting typical refinery furnaces and using hydrogen in gas turbines. Additionally, the report will cover hydrogen storage methods, with a focus on the economics of underground storage. #pep A clear-eyed view of the future #spwpc Meet the PEP experts at WPC 2025 in Houston Terrika Duckett, SSM, POPM,Peeyush Varshney, Ph.D.,Jordan Brooksher,Natalie Stockton,Ben Siaw,Ezzat Eid,Yuriko Kato, James Chia, Imad Nassar, Thabo Pitsi,Mohammad Kurdi,Mohamed Dawoud,Stephanie Liew,Hyungkeun Park, Turbold Erdenejargal,Takashi Matsuda, Tomoya Shiina, Koichi Ariyoshi,Anupam Bagri,Dipti Davé,kumar jain,Rajesh Debnath, CEng MIChemE

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Massive explosion in Philadelphia Energy Solutions Refinery, At approximately 4 am on Friday June 21, 2019 there was a release of vapor in the PES refinery alkylation unit. The vapor found an ignition source, causing a fire and multiple explosions. Consider new revisions of API and ASTM in persuit of this process safety event. Final Report Released On: October 11, 2022 2019-04-I-PA-4 Update API RP 751 Safe Operation of Hydrofluoric Acid Alkylation Units to require the following: Protection of critical safeguards and associated control system components, including but not limited to wiring and cabling for control systems and primary and backup power supplies, from fire and explosion hazards, including radiant heat and flying projectiles; and Installation of remotely-operated emergency isolation valves on the inlet(s) and outlet(s) of all hydrofluoric acid containing vessels, and hydrocarbon containing vessels meeting defined threshold quantities. Final Report Released On: October 11, 2022 2019-04-I-PA-5 Revise ASTM A234 to incorporate supplementary requirements for piping used in HF service, as defined in HF supplementary requirements S9.1 through S9.7 in ASTM A106 version 19a. #psm #incidentinvestigation #safety #training #refinery #petrichemicalindustries #mechanicalengineering #chemicalengineering #hse #mechanicalintegrity #rbi

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GENUINE and VALID gas processing plant of the RUSSIAN company SURGUTNEFTEGAZ. SURGUT GAS PROCESSING PLANT is the largest gas processing plant in Western Siberia, is a structural subdivision of SURGUTNEFTEGAZ. The total processing capacity of associated petroleum gas is 4.2-5 billion tons. cubic meters. The uniqueness of the Surgut Gas Processing Plant lies primarily in its extremely advantageous location - not far from the permanent, stable consumer of dry gas - GRES-1 and GRES-2. Receiving raw materials from the oil and gas fields of Western Siberia, the plant must instead give the consumer two finished products - dry gas and a wide fraction of liquid hydrocarbons (LFLU). After compressing and cooling the gas, during which it is divided into heavy and light fractions, the purified from unnecessary impurities and drained gas enters the furnaces of two Surgut power plants. SHFLU goes for further processing to the Tobolsk Petrochemical Plant, to other consumers. In addition to SHFLU and dry gas, the Surgut Gas Processing Plant produces propane-butane mixture, nitrogen and oxygen for its own needs. The product line of the SURGUTNEFTEGAZ gas processing plant: ● dry topped gas; ● thracia wide light beehive (SHFLU); ● straight-run gasoline; ● propane; ● nitrogen; ● oxygen; ● polypropylene; ● geotextile; ● agropolotno. SURGUTNEFTEGAZ gas processing plant is a modern complex that allows obtaining dry distilled compressed gas, as well as liquid hydrocarbons that are widely used in industrial and economic activities of the Russian Federation. The products produced by the plant have high quality indicators and meet the requirements of the state standards of the Russian Federation and technical regulations of the Customs Union. SURGUT GAS PROCESSING PLANT official website: https://lnkd.in/ePy3QHFr #innovation #management #humanresources #technology #digitalmarketing #entrepreneurship #careers #socialmedia #socialnetworking #futurism #startups #branding #advertisingandmarketing #creativity #marketing #sales #motivation #energy #money #sustainability #productivity #gettingthingsdone #leadership #education #strategy #business #europe #mindfulness #inspiration #engineering #africa #india #europeanunion #china #smallbusiness #success #production #oilandgas #collaboration #contentmarketing #research #globaltrade #onlineadvertising #dubai #kenya #abudhabi #socialmediamarketing #manufacturing #climatechange #work #science #logistics #hydrocarbons #shipping #growth #uae #marketresearch #oil #oilandgasindustry #agriculture #designer #oilfield #oilindustry #petroleum #trading #gas #chemistry #chemical #petrochemical #agro #refinery #import #export #industrial #agribusiness #quality 

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Meet us at the EEPC 2024 T.EN’s novel Primary Feed Effluent Exchanger for Low-emission cracking furnace for ethylene production is going to be presented at the 2024 European Ethylene Producers Committee Conference taking place in Sitges (Spain). Decarbonization for Ethylene plants is an essential requirement to meet the objectives of the net zero commitment made globally. Technip Energies (T.EN) has introduced its Low-Emission Cracking Furnace technology to achieve a low-emission ethylene plant. This innovative technology has the potential to reduce cracking furnace direct CO2 emissions by more than 30 percent upon adoption and provides the largest emission reduction compared to alternative high efficiency furnace designs. Serving as a corner stone for electrification of the back-end, integration with the power infra structure and implementation of partial or full hydrogen firing, this type of cracking furnace is meant to support the energy transition and provide an economically sound route to the full decarbonization of ethylene plants at term. The Primary Feed-Effluent Transfer Line Exchanger (PFEE) is the key innovation to enable the T.EN Low-Emission Cracking Furnace design to proceed. Positioned at the primary quench location, the PFEE receives the cracked gas directly from the radiant coils. By replacing the high-pressure steam generation service on the shell side by heating the radiant coil feed instead, the PFEE provides pre-heating of the feed/steam mixture upstream of the cracking coils. This novel design approach makes the T.EN Low-Emission Cracking Furnace unique in the landscape of available cracking technologies. Recently T.EN has developed and manufactured a PFEE specifically for this application. This novel PFEEs has subsequently been subjected to a series of tests at relevant operating conditions for the validation of its thermal performance and mechanical soundness. This presentation introduces the concept of PFEEs, and discusses the testing program results. #bepartofthesolution, Technip Energies, #ethylene 

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AMMONIA VESSELS BUNKERING PROCESSES & MODES ABTRACT Volume requirements of either pressurized gas or liquid HYDROGEN are not sufficiently high to be considered infeasible, but price is a hurdle, situation that is going to change with electrolysis technology & the decreasing cost of renewable power. With respect AMMONIA has several advantages over #HYDROGEN, for example less space is required for the same energy content, current market prices are more competitive. However, AMMONIA´S relatively low gravitational energy density negative impact the performance. Auxiliary services & post combustion devices should be considered also. #BATTERIES are particularly unlikely to meet the size, weight or price requirements for long distance shipping. #METHANOL, less desirable option due emissions but appeared to share similar characteristics with #AMMONIA. ESSENTIALS On currently the maximum expected propulsion demand per voyage is 9270 MWh. Important distinction, decarbonization would not encompass other pollutants such as Sulphur Oxides SOx, NOx & particulate matter. Ships can produce large quantities of these, which has led to strict restrictions from the IMO. MODES OF AMMONIA TRANSFER AMMONIA must be safely transferred from producers to suppliers & eventually to vessels powered by AMMONIA bunker fuel. Modes are Ship-to-ship STS breakbulk at an anchorage or a jetty-based location + Shore-to-ship SHTS breakbulk at a jetty-based location + STS bunkering at an anchorage or a jetty-based location + SHTS bunkering at a jetty-based location + Truck-to-ship bunkering at a jetty-based location. PROCESSES OF AMMONIA TRANSFER LAC TO ABV/LAC (STS) #BREAKBULK: Process flow for a Liquid AMMONIA Carrier LAC pump ammonia to AMMONIA Bunker Vessel ABV controlling the boil-off gas BOG generated by sending back from the ABV to the LAC through specific vapor equipment minimizing the BOG. Both LAC & ABV have reliquefication units to condense the BOG generated due to heat leaks within the LAC tanks. LAC TO ABV/LAC (STS) ANCHORAGE BREAKBULK: Process flow from a Liquid Ammonia Carrier to the ABV tanks is accomplished using transfer pumps located within the LAC tanks, controlling the boil-off gas BOG generated by sending back from the ABV to the LAC specific vapor device with high probability of hose failure comparing with marine loading arms limiting the transfer rate, again limiting BOG & doing reliquefication to condense the BOG generated due to heat leaks within the tanks. ABV TO AMONNIA POWERED SHIPS (STS) #BUNKERING AT ANCHORAGE: this process uses flexible hoses for transfer. Pumps at ABV tanks transfer ammonia to the APS tanks. BOG generated is sending from the APS tank to the ABV tank via a specific vapor hose. ASF TO APS (SHTS) BUNKERING: Terminal with transfer pumps capable of pumping AMMONIA to an AMMONIA -powered tugboat tank, without vapor connection while tugboats have no vapor return capability. The idea is to pressurize the AMMONIA tugboats tanks. #netzero

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Join the Vaisala team for an informative webinar on sulfuric acid measurement in oil & gas refineries! 🌟 Discover the magic of the STRATCO® Alkylation Technology, turning low-value olefins into high-value alkylate, a superstar for clean gasoline. Vaisala experts will dive into the challenges and solutions for measuring sulfuric acid, featuring Coriolis meters, inline refractometers, and titration sampling. Plus, the Vaisala team will share some amazing industry success stories and real-world use cases of inline refractometer installations. What the webinar will cover: 💡 Sulfuric Acid Chemical Applications in Oil & Gas Refineries 💡 Why Measure Sulfuric Acid? 💡 Measurement Solutions for Obtaining the Best Results 💡 Industry Successes Don't miss out! Register now to gain valuable insights and boost your processes! #Vaisala #ADMSystems #SulfuricAcid #Alkylation #CleanGasoline #OilAndGas #MeasurementSolutions #Webinar #IndustrySuccess #processrefractometer

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Our chemical treatment of spent resin removes and recovery inorganic C-14, liquefy spent resins, decomposes organic matter, and reduces the volume of spent resin waste by using a mild Fenton like oxidation process and an electrochemical advanced oxidation process. The first step is a selective removal of inorganic carbonates and an optional recovery of 14CO2 which can enable a lower level waste classification and facilitates final storage. In the second step, the ion exchanger is liquefied which allows blending of resins with different activity inventory and immobilization by grouting with a volume reduction factor of 3 – 4 in comparison with direct grouting. Partially organic matter is decomposed to mainly CO2 and H2O. The optional third step is to completely (> 99,9 %) decompose organic matter (e.g. complexing agents) which facilities long-term storage due to the higher stability of inorganic waste and minimizes risks to fail waste acceptance criteria. In an optional forth step the liquefied resin is transformed into a solid inorganic waste and the majority of radionuclides is separated from inactive ions resulting in a volume reduction factor for intermediate level waste (ILW) of up to 20 and of 3 – 4 for (very) low level waste (LLW). https://lnkd.in/dVADUX34 #NuclearEnergy #WasteTreatment #SpentResin #Framatome

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Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents, Volumes 1A & 1B, 5th Edition By A. Kayode Coker Published by Elsevier The volumes are dedicated to all personnel worldwide involved in petroleum and petrochemical activities, and to those who lost their lives in incidents such as Bhopal in India, Piper Alpha in the U.K., BP Refinery in Houston, Texas, US, and others involved in process accidents. The fifth edition of Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents continues the legacy of Ernest E. Ludwig’s seminal work, which began over 60 years ago. These updated volumes serve as an essential manual for chemical engineering process design, providing improved techniques and methodologies that are critical for practicing engineers. This edition emphasizes the integration of process safety incidents, presenting a thorough review of root causes and mitigation strategies to prevent future incidents. The updated content ensures engineers can achieve optimal operational and process conditions, and avoid issues related to inadequate equipment sizing and insufficient design details. The volumes deliver a balanced approach by combining fundamental theories with their direct applications. This method is invaluable for troubleshooting process equipment and conducting system performance analyses. Volume 1A encompasses chapters 1-6, while Volume 1B includes chapters 7-12. Key features of these volumes include: Case studies of process safety incidents sourced from the US Chemical Safety & Hazard Investigation Board (www.csb.gov) Appendices and over 40 process data sheets, also available in Excel format A glossary of petroleum and chemical terminologies Detailed physical and chemical characteristics of major hydrocarbons Conversion table software Access to Honeywell UniSim Design software Microsoft Excel programs Together, these tools and features provide a comprehensive resource for chemical and petrochemical process design, ensuring engineers are well-equipped to design, analyze, and optimize their processes effectively

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Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents, Volumes 1A & 1B, 5th Edition By A. Kayode Coker Published by Elsevier The volumes are dedicated to all personnel worldwide involved in petroleum and petrochemical activities, and to those who lost their lives in incidents such as Bhopal in India, Piper Alpha in the U.K., BP Refinery in Houston, Texas, US, and others involved in process accidents. The fifth edition of Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents continues the legacy of Ernest E. Ludwig’s seminal work, which began over 60 years ago. These updated volumes serve as an essential manual for chemical engineering process design, providing improved techniques and methodologies that are critical for practicing engineers. This edition emphasizes the integration of process safety incidents, presenting a thorough review of root causes and mitigation strategies to prevent future incidents. The updated content ensures engineers can achieve optimal operational and process conditions, and avoid issues related to inadequate equipment sizing and insufficient design details. The volumes deliver a balanced approach by combining fundamental theories with their direct applications. This method is invaluable for troubleshooting process equipment and conducting system performance analyses. Volume 1A encompasses chapters 1-6, while Volume 1B includes chapters 7-12.

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Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents, Volumes 1A & 1B, 5th Edition By A. Kayode Coker Published by Elsevier The volumes are dedicated to all personnel worldwide involved in petroleum and petrochemical activities, and to those who lost their lives in incidents such as Bhopal in India, Piper Alpha in the U.K., BP Refinery in Houston, Texas, US, and others involved in process accidents. The fifth edition of Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents continues the legacy of Ernest E. Ludwig’s seminal work, which began over 60 years ago. These updated volumes serve as an essential manual for chemical engineering process design, providing improved techniques and methodologies that are critical for practicing engineers. This edition emphasizes the integration of process safety incidents, presenting a thorough review of root causes and mitigation strategies to prevent future incidents. The updated content ensures engineers can achieve optimal operational and process conditions, and avoid issues related to inadequate equipment sizing and insufficient design details. The volumes deliver a balanced approach by combining fundamental theories with their direct applications. This method is invaluable for troubleshooting process equipment and conducting system performance analyses. Volume 1A encompasses chapters 1-6, while Volume 1B includes chapters 7-12. Key features of these volumes include: Case studies of process safety incidents sourced from the US Chemical Safety & Hazard Investigation Board (www.csb.gov) Appendices and over 40 process data sheets, also available in Excel format A glossary of petroleum and chemical terminologies Detailed physical and chemical characteristics of major hydrocarbons Conversion table software Access to Honeywell UniSim Design software Microsoft Excel programs Together, these tools and features provide a comprehensive resource for chemical and petrochemical process design, ensuring engineers are well-equipped to design, analyze, and optimize their processes effectively.

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Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents, Volumes 1A & 1B, 5th Edition By A. Kayode Coker Published by Elsevier The volumes are dedicated to all personnel worldwide involved in petroleum and petrochemical activities, and to those who lost their lives in incidents such as Bhopal in India, Piper Alpha in the U.K., BP Refinery in Houston, Texas, US, and others involved in process accidents. The fifth edition of Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents continues the legacy of Ernest E. Ludwig’s seminal work, which began over 60 years ago. These updated volumes serve as an essential manual for chemical engineering process design, providing improved techniques and methodologies that are critical for practicing engineers. This edition emphasizes the integration of process safety incidents, presenting a thorough review of root causes and mitigation strategies to prevent future incidents. The updated content ensures engineers can achieve optimal operational and process conditions, and avoid issues related to inadequate equipment sizing and insufficient design details. The volumes deliver a balanced approach by combining fundamental theories with their direct applications. This method is invaluable for troubleshooting process equipment and conducting system performance analyses. Volume 1A encompasses chapters 1-6, while Volume 1B includes chapters 7-12. Key features of these volumes include: Case studies of process safety incidents sourced from the US Chemical Safety & Hazard Investigation Board (www.csb.gov) Appendices and over 40 process data sheets, also available in Excel format A glossary of petroleum and chemical terminologies Detailed physical and chemical characteristics of major hydrocarbons Conversion table software Access to Honeywell UniSim Design software Microsoft Excel programs Together, these tools and features provide a comprehensive resource for chemical and petrochemical process design, ensuring engineers are well-equipped to design, analyze, and optimize their processes effectively.

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Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents, Volumes 1A & 1B, 5th Edition By A. Kayode Coker Published by Elsevier The volumes are dedicated to all personnel worldwide involved in petroleum and petrochemical activities, and to those who lost their lives in incidents such as Bhopal in India, Piper Alpha in the U.K., BP Refinery in Houston, Texas, US, and others involved in process accidents. The fifth edition of Ludwig’s Applied Process Design for Chemical and Petrochemical Plants Incorporating Process Safety Incidents continues the legacy of Ernest E. Ludwig’s seminal work, which began over 60 years ago. These updated volumes serve as an essential manual for chemical engineering process design, providing improved techniques and methodologies that are critical for practicing engineers. This edition emphasizes the integration of process safety incidents, presenting a thorough review of root causes and mitigation strategies to prevent future incidents. The updated content ensures engineers can achieve optimal operational and process conditions, and avoid issues related to inadequate equipment sizing and insufficient design details. The volumes deliver a balanced approach by combining fundamental theories with their direct applications. This method is invaluable for troubleshooting process equipment and conducting system performance analyses. Volume 1A encompasses chapters 1-6, while Volume 1B includes chapters 7-12. Key features of these volumes include: Case studies of process safety incidents sourced from the US Chemical Safety & Hazard Investigation Board (www.csb.gov) Appendices and over 40 process data sheets, also available in Excel format A glossary of petroleum and chemical terminologies Detailed physical and chemical characteristics of major hydrocarbons Conversion table software Access to Honeywell UniSim Design software Microsoft Excel programs Together, these tools and features provide a comprehensive resource for chemical and petrochemical process design, ensuring engineers are well-equipped to design, analyze, and optimize their processes effectively.

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