HALDIA PETROCHEMICALS LIMITED
Download as docx, pdf0 likes1,227 views
This document is an offer letter from Haldia Petrochemicals Limited to Dharmaraj D Daddikar for the position of Assistant Manager- Manufacturing in Haldia. The letter outlines the salary components including basic pay, allowances, and benefits. The total cost to the company is Rs. 605,825 which includes a maximum performance linked pay of Rs. 94,721. The letter was rejected by Dharmaraj for delaying the offer for 2 months.
1 of 3
Download to read offline
Ad
Recommended
Water Conservation & Uses.pptx
Water Conservation & Uses.pptxnnnagendranaik
油
The document discusses the importance of water conservation, highlighting the fact that only 0.5% of the Earth's water is suitable for drinking. It outlines various methods to conserve water in the home, including practical tips for the kitchen, bathroom, and outdoor areas, as well as traditional conservation techniques used in India. The document emphasizes why conserving water is crucial for sustainability, energy savings, and ensuring future availability of clean water.Short and long interruptions- UNIT-II-POWER QUALITY
Short and long interruptions- UNIT-II-POWER QUALITYST. MARTIN'S ENGINEERING COLLEGE
油
The document discusses interruptions in electrical supply, categorized by IEEE standards into short-duration and long-duration variations, with specific definitions for instantaneous, momentary, and temporary interruptions. It highlights the causes, consequences, and necessary measures to mitigate such interruptions, including the impact on sensitive equipment and the relationship between service quality and customer satisfaction. Additionally, it covers compensation mechanisms for customers, emphasizing the importance of managing interruption frequency and duration for maintaining a reliable power system.Settings Use and Maintenance of Mechanical Ventilator
Settings Use and Maintenance of Mechanical VentilatorSurendran Radjou
油
Mechanical ventilation involves using a mechanical device to assist breathing and improve gas exchange. It helps control the airway and breathing workload, replaces exhausted respiratory muscles, and allows use of medications that could otherwise suppress breathing. Key functions include setting oxygen levels, breathing rate and volume, as well as pressures to open collapsed airspaces. Modes include fully controlled, supported, and combined approaches. Weaning gradually reduces ventilator support levels as the patient recovers lung function and the ability to breathe independently.Mechanical Ventilation Weaning From Mechanical Ventilation
Mechanical Ventilation Weaning From Mechanical VentilationDang Thanh Tuan
油
- The document discusses various parameters and criteria used to determine when a patient can be safely disconnected from mechanical ventilation, including respiratory muscle strength, gas exchange, respiratory rate and volume.
- Common methods for gradually weaning a patient from mechanical ventilation are described, such as a T-piece trial, pressure support ventilation, and gradually decreasing the rate of support on SIMV.
- Failure criteria are outlined, including rapid shallow breathing, increased heart rate or blood pressure, distress signs. Determining the cause of failure and correcting it is important before subsequent weaning trials.DISTRIBUTED GENERATION TECHNOLOGIES
DISTRIBUTED GENERATION TECHNOLOGIESEditor IJMTER
油
The document discusses distributed generation (DG), which refers to power generation at or near the end-user, presenting its advantages over traditional centralized generation, particularly in the context of India's growing energy demands. It emphasizes the role of DG technologies, such as photovoltaics, wind turbines, and fuel cells, in providing clean and reliable energy, especially in rural areas where grid access is limited. Overall, DG is portrayed as an efficient, cost-effective, and environmentally friendly solution for addressing India's electricity supply challenges.Hydrogen Recovery
Hydrogen RecoveryDharmaraj Daddikar
油
The document discusses the recovery of hydrogen gas from purge gas in an ammonia production process. It describes using a combination of pressure swing adsorption (PSA) and Joule-Thomson processes to separate the gases. The PSA first removes ammonia and water. Then the Joule-Thomson process uses adiabatic throttling to liquefy and separate the remaining gases like methane, argon, nitrogen, and hydrogen based on their boiling points, recovering high-purity hydrogen gas. The condensed non-hydrogen gases are used to regenerate the PSA adsorbents.SOUTHERN PETROCHEMICALS INDUSTRIES CORPORATION LIMITED
SOUTHERN PETROCHEMICALS INDUSTRIES CORPORATION LIMITEDDharmaraj Daddikar
油
The document contains two job offers from Southern Petrochemicals Industries Corporation Limited to Dharmaraj Dhaddikar (first offer) and then to Raj (second offer) for the role of Assistant Manager Operations. The first offer details a monthly compensation of Rs. 65,000 with additional benefits like housing, medical insurance, and performance bonuses. This offer is noted as rejected. The second offer increases the monthly compensation to Rs. 75,000 and includes similar benefits but is also noted as rejected, with Raj going "AWOL/MIA".Finalized readings (mcfl rig).
Finalized readings (mcfl rig).Dharmaraj Daddikar
油
The document appears to contain experimental data from measurements of weight (WT), dip (DIP), and density pressure (DP) for samples under different conditions. It includes 28 rows of data with measurements for empty tube weight, total weight, DIP, DP, weight, and percentage error for different numbered samples. The data is organized into sections for samples with different nickel layer configurations, and includes calculations of totals, averages, and corrections.Catalyst unloading details
Catalyst unloading detailsDharmaraj Daddikar
油
1) The document outlines the step-by-step procedure for unloading the catalyst from a synthesis converter, including cooling down the catalyst bed, purging the synthesis loop with inert gas, dismantling connected pipelines and valves, and preparing for catalyst extraction.
2) The first basket catalyst is extracted using a vacuum system with inert gas bleed and safety precautions like breathing apparatus and safety ropes for workers inside the converter.
3) Once the first basket catalyst is extracted, the second basket catalyst is extracted following similar safety procedures, and then the second basket is removed along with the low pressure shell.PREPARATION FOR BOILER FEED WATER PRODUCTION
PREPARATION FOR BOILER FEED WATER PRODUCTIONDharmaraj Daddikar
油
The document discusses the preparation of boiler feed water (BFW) from raw water. Raw water is processed through demineralization to remove minerals, producing demineralized (DM) water. DM water is further conditioned in a deaerator, where it is mixed with recycled condensate, heated with low pressure steam to remove dissolved gases, and oxygen scavengers like hydrazine are added to produce high quality BFW for use in boilers. Maintaining proper BFW quality through continuous and intermittent blowdown is important to minimize impurities in the boiler system and produce stable steam.Steam Reforming - Carbon Formation
Steam Reforming - Carbon FormationGerard B. Hawkins
油
The presentation by Gerard B. Hawkins aims to explain carbon formation in catalytic processes, emphasizing the reasons, types, and prevention methods for carbon-related issues. It identifies three main types of carbon: cracking, Boudouard, and CO reduction, with a focus on cracking due to its prevalence. The document discusses the conditions that lead to carbon formation and suggests strategies for mitigating its impact on catalyst performance.Synthesis catalyst converter explanation
Synthesis catalyst converter explanationDharmaraj Daddikar
油
The document provides a detailed yet simplified explanation of the internals of a synthesis converter. It describes the main components, including the low pressure shell, two basket assemblies containing catalyst that allow radial gas flow, and two heat exchangers. Diagrams are provided to illustrate how the warm shot gas, cold shot gas, and product gases flow through the system, with the heat exchangers preheating the incoming gases and cooling the outgoing gases. The goal is to clearly explain the complex design to engineers and professionals working in the field.Reformer Catalyst Report
Reformer Catalyst ReportDharmaraj Daddikar
油
This document summarizes the annual catalyst unloading and reloading process for the primary reformer at a chemical plant. It describes removing the spent catalyst from 224 tubes using vacuum pumps over 48 hours. Samples were taken and tubes were cleaned. New catalyst was then loaded in two layers - a bottom layer of nickel catalyst in 5 buckets per tube and a top layer of nickel-potassium catalyst in 7 buckets per tube. Dip heights and pressure drops were measured to ensure proper loading. The process was completed over 11 days during the annual turnaround.The Benefits and Disadvantages of Potash in Steam Reforming
The Benefits and Disadvantages of Potash in Steam ReformingGerard B. Hawkins
油
The document discusses the inclusion of potash in steam reforming, highlighting its benefits in preventing carbon formation and aiding carbon removal during the process. It also outlines various disadvantages, such as potential fouling of heat exchangers and loss of catalyst strength due to potash capture issues. Despite the disadvantages, the overall conclusion is that potash offers more advantages and there are options to mitigate carbon formation challenges in most plants.Steam Reformer Surveys - Techniques for Optimization of Primary Reformer Oper...
Steam Reformer Surveys - Techniques for Optimization of Primary Reformer Oper...Gerard B. Hawkins
油
The document discusses optimizing the operation of primary reformers through surveys that assess catalyst performance, reformer operation, and tube life estimation. It includes various techniques such as tube wall temperature measurement, process data collection, and computer modeling to identify issues and suggest improvements, with case studies demonstrating significant cost savings. The methodology has been employed in over 30 plants, emphasizing the importance of accurate data collection and analysis for effective reformer management.Safety valve in process industry1
Safety valve in process industry1Nitesh Chauhan
油
Safety valves are automatic pressure relief devices that prevent excessive pressure buildup in systems like reactors, pipelines, and compressors. They open rapidly when pressure exceeds the set point to safely release pressure and reclose once normal pressure is restored. Proper safety valve design and sizing according to codes like API 520 and 526 is critical to ensure the valve can relieve the required flow rate without overpressurizing equipment. Key parameters include pressure conditions, required flow rate, orifice area, and type of valve.Steam Reforming - Catalyst Loading
Steam Reforming - Catalyst LoadingGerard B. Hawkins
油
This document provides best practices for loading catalyst into steam reformer tubes. It discusses using socks to uniformly distribute catalyst at a controlled rate of 3 feet or less of freefall. Pressure drop should be measured across tubes to ensure uniform packing. Common problems like bridging or uneven settling can be addressed through vibration or repacking. Precise loading techniques help minimize issues like temperature variations or methane slip that reduce efficiency and tube life.REFERENCE 2015
REFERENCE 2015Sherif Gabr
油
This document summarizes major oil and gas projects undertaken by IPSG between 2021-2022. It lists 21 separate projects for clients such as Danieli, ELNG, Delta Fertilizers, Al Futtaim Carillion, Cairo Oil Refinery, and Apache/Khalda involving activities like catalyst loading and unloading, district cooling piping installation, NDT inspection, heater decoking, and sewage treatment plant design, construction, and commissioning. The projects covered a wide range of operations and maintenance services for oil and gas facilities.Normal Operation of Steam Reformers on Hydrogen Plants
Normal Operation of Steam Reformers on Hydrogen PlantsGerard B. Hawkins
油
The document discusses the operation and optimization of steam reformers in hydrogen plants, focusing on controlled variables, data analysis, catalyst life predictions, and tube wall temperature measurements. It details the impact of factors such as exit temperature and steam/carbon ratio on performance and includes recommendations for monitoring operations and verifying plant data accuracy. The analysis of catalyst activity, methane slip, and approaches to equilibrium emphasizes the importance of accurate measurements for optimizing efficiency and safety in reformer operations.1.1 intro process_safety
1.1 intro process_safetyMohd.Rozalmi Suhaimi
油
This document discusses several major industrial accidents involving fires, explosions, and toxic releases from process plants. It begins by describing the 1984 Bhopal disaster in India, where a leak of methyl isocyanate gas from a Union Carbide plant killed thousands. Subsequent sections provide details on additional accidents, including the Piper Alpha oil rig fire in 1988 and the BP Texas City refinery explosion in 2005. The document outlines common hazards in process industries like fires, explosions, and toxic releases, and describes phenomena that can cause accidents such as vapor cloud explosions and BLEVE (boiling liquid expanding vapor explosion) events.Hydraulic valves
Hydraulic valvesAmitabh Gairola
油
The document discusses objectives related to hydraulic valves. It covers the functions of different types of valves including pressure, directional, and volume/flow control valves. Some key points include that pressure control valves are used to limit, reduce, or set system pressures. Relief valves come in direct acting and pilot operated types. Pressure reducing valves include constant reduced and fixed amount types. Directional control valves include check valves, rotary valves, poppet valves, electro-hydraulic valves, and spool valves. Valves can be actuated mechanically, with pilots, or electrically.Reformer Tube Metallurgy: Design Considerations; Failure Mechanisms; Inspecti...
Reformer Tube Metallurgy: Design Considerations; Failure Mechanisms; Inspecti...Gerard B. Hawkins
油
The document discusses the metallurgy of reformer tubes, focusing on design principles, failure mechanisms, and inspection methods. It highlights the importance of optimizing tube life through improved materials and monitoring techniques, as well as addressing failure responses. The analysis includes details on temperature effects on tube life, recent metallurgical advancements, and inspection methods like non-destructive testing (NDT).14 Tips for Process Safety Management
14 Tips for Process Safety ManagementVerde Ventures Pvt. Ltd.
油
The document discusses Process Safety Management (PSM) and provides an overview of its key elements. PSM is a comprehensive management system that proactively avoids incidents in hazardous industries handling toxic chemicals. It integrates risk management across 14 elements, including employee participation, process hazard analysis, operating procedures, training, and compliance audits. The presentation aims to help organizations manage process safety risks in a more structured way.Process Safety Kpi
Process Safety KpiArthurGroot
油
This document outlines a 4-phase approach to determining process safety key performance indicators (KPIs) using the BowTie methodology. Phase 1 involves setting up BowTie diagrams using risk assessment reports. Phase 2 selects leading and lagging KPIs linked to barriers in the BowTie diagrams. Phase 3 establishes criteria and reporting standards for the KPIs. Phase 4 integrates incident data into the BowTie diagrams and starts an improvement cycle. The approach aims to comply with legislation and standards while identifying relevant process safety KPIs in a bottom-up manner tied to an organization's safety management system.Theory of Carbon Formation in Steam Reforming
Theory of Carbon Formation in Steam Reforming Gerard B. Hawkins
油
The document discusses carbon formation in steam methane reformers, outlining its causes, effects, and prevention methods. It identifies key factors contributing to carbon formation, including catalyst activity, steam-to-carbon ratios, and heat transfer efficiency. Additionally, it details the chemistry behind carbon formation from various feedstocks and emphasizes the importance of understanding these processes for optimizing refinery operations.101 Things That Can Go Wrong on a Primary Reformer - Best Practices Guide
101 Things That Can Go Wrong on a Primary Reformer - Best Practices GuideGerard B. Hawkins
油
This document discusses common problems that can occur in primary reformers and associated equipment. It identifies issues that can lead to plant shutdowns or efficiency losses, grouping them under catalysts, tubes, furnace boxes, burners, flue gas ducts, headers, and refractories. Some examples discussed include carbon formation, tube overheating, flame impingement, leaks in air preheaters, combustion air maldistribution, and damage to coffins. The document provides an overview of these issues to improve plant reliability over its lifespan.Pre-reformer Operations Technical Supplement
Pre-reformer Operations Technical SupplementGerard B. Hawkins
油
This document discusses operating pre-reformers at high temperatures and the associated benefits and drawbacks. It notes that while higher temperatures allow for better thermal efficiency and feedstock flexibility in reformers, they can also cause hydrothermal sintering of catalysts over time from high heat and steam. The document provides guidelines for startup, reduction, and operation of pre-reformer catalysts to maximize performance while mitigating sintering risks.More Related Content
Viewers also liked (19)
Catalyst unloading details
Catalyst unloading detailsDharmaraj Daddikar
油
1) The document outlines the step-by-step procedure for unloading the catalyst from a synthesis converter, including cooling down the catalyst bed, purging the synthesis loop with inert gas, dismantling connected pipelines and valves, and preparing for catalyst extraction.
2) The first basket catalyst is extracted using a vacuum system with inert gas bleed and safety precautions like breathing apparatus and safety ropes for workers inside the converter.
3) Once the first basket catalyst is extracted, the second basket catalyst is extracted following similar safety procedures, and then the second basket is removed along with the low pressure shell.PREPARATION FOR BOILER FEED WATER PRODUCTION
PREPARATION FOR BOILER FEED WATER PRODUCTIONDharmaraj Daddikar
油
The document discusses the preparation of boiler feed water (BFW) from raw water. Raw water is processed through demineralization to remove minerals, producing demineralized (DM) water. DM water is further conditioned in a deaerator, where it is mixed with recycled condensate, heated with low pressure steam to remove dissolved gases, and oxygen scavengers like hydrazine are added to produce high quality BFW for use in boilers. Maintaining proper BFW quality through continuous and intermittent blowdown is important to minimize impurities in the boiler system and produce stable steam.Steam Reforming - Carbon Formation
Steam Reforming - Carbon FormationGerard B. Hawkins
油
The presentation by Gerard B. Hawkins aims to explain carbon formation in catalytic processes, emphasizing the reasons, types, and prevention methods for carbon-related issues. It identifies three main types of carbon: cracking, Boudouard, and CO reduction, with a focus on cracking due to its prevalence. The document discusses the conditions that lead to carbon formation and suggests strategies for mitigating its impact on catalyst performance.Synthesis catalyst converter explanation
Synthesis catalyst converter explanationDharmaraj Daddikar
油
The document provides a detailed yet simplified explanation of the internals of a synthesis converter. It describes the main components, including the low pressure shell, two basket assemblies containing catalyst that allow radial gas flow, and two heat exchangers. Diagrams are provided to illustrate how the warm shot gas, cold shot gas, and product gases flow through the system, with the heat exchangers preheating the incoming gases and cooling the outgoing gases. The goal is to clearly explain the complex design to engineers and professionals working in the field.Reformer Catalyst Report
Reformer Catalyst ReportDharmaraj Daddikar
油
This document summarizes the annual catalyst unloading and reloading process for the primary reformer at a chemical plant. It describes removing the spent catalyst from 224 tubes using vacuum pumps over 48 hours. Samples were taken and tubes were cleaned. New catalyst was then loaded in two layers - a bottom layer of nickel catalyst in 5 buckets per tube and a top layer of nickel-potassium catalyst in 7 buckets per tube. Dip heights and pressure drops were measured to ensure proper loading. The process was completed over 11 days during the annual turnaround.The Benefits and Disadvantages of Potash in Steam Reforming
The Benefits and Disadvantages of Potash in Steam ReformingGerard B. Hawkins
油
The document discusses the inclusion of potash in steam reforming, highlighting its benefits in preventing carbon formation and aiding carbon removal during the process. It also outlines various disadvantages, such as potential fouling of heat exchangers and loss of catalyst strength due to potash capture issues. Despite the disadvantages, the overall conclusion is that potash offers more advantages and there are options to mitigate carbon formation challenges in most plants.Steam Reformer Surveys - Techniques for Optimization of Primary Reformer Oper...
Steam Reformer Surveys - Techniques for Optimization of Primary Reformer Oper...Gerard B. Hawkins
油
The document discusses optimizing the operation of primary reformers through surveys that assess catalyst performance, reformer operation, and tube life estimation. It includes various techniques such as tube wall temperature measurement, process data collection, and computer modeling to identify issues and suggest improvements, with case studies demonstrating significant cost savings. The methodology has been employed in over 30 plants, emphasizing the importance of accurate data collection and analysis for effective reformer management.Safety valve in process industry1
Safety valve in process industry1Nitesh Chauhan
油
Safety valves are automatic pressure relief devices that prevent excessive pressure buildup in systems like reactors, pipelines, and compressors. They open rapidly when pressure exceeds the set point to safely release pressure and reclose once normal pressure is restored. Proper safety valve design and sizing according to codes like API 520 and 526 is critical to ensure the valve can relieve the required flow rate without overpressurizing equipment. Key parameters include pressure conditions, required flow rate, orifice area, and type of valve.Steam Reforming - Catalyst Loading
Steam Reforming - Catalyst LoadingGerard B. Hawkins
油
This document provides best practices for loading catalyst into steam reformer tubes. It discusses using socks to uniformly distribute catalyst at a controlled rate of 3 feet or less of freefall. Pressure drop should be measured across tubes to ensure uniform packing. Common problems like bridging or uneven settling can be addressed through vibration or repacking. Precise loading techniques help minimize issues like temperature variations or methane slip that reduce efficiency and tube life.REFERENCE 2015
REFERENCE 2015Sherif Gabr
油
This document summarizes major oil and gas projects undertaken by IPSG between 2021-2022. It lists 21 separate projects for clients such as Danieli, ELNG, Delta Fertilizers, Al Futtaim Carillion, Cairo Oil Refinery, and Apache/Khalda involving activities like catalyst loading and unloading, district cooling piping installation, NDT inspection, heater decoking, and sewage treatment plant design, construction, and commissioning. The projects covered a wide range of operations and maintenance services for oil and gas facilities.Normal Operation of Steam Reformers on Hydrogen Plants
Normal Operation of Steam Reformers on Hydrogen PlantsGerard B. Hawkins
油
The document discusses the operation and optimization of steam reformers in hydrogen plants, focusing on controlled variables, data analysis, catalyst life predictions, and tube wall temperature measurements. It details the impact of factors such as exit temperature and steam/carbon ratio on performance and includes recommendations for monitoring operations and verifying plant data accuracy. The analysis of catalyst activity, methane slip, and approaches to equilibrium emphasizes the importance of accurate measurements for optimizing efficiency and safety in reformer operations.1.1 intro process_safety
1.1 intro process_safetyMohd.Rozalmi Suhaimi
油
This document discusses several major industrial accidents involving fires, explosions, and toxic releases from process plants. It begins by describing the 1984 Bhopal disaster in India, where a leak of methyl isocyanate gas from a Union Carbide plant killed thousands. Subsequent sections provide details on additional accidents, including the Piper Alpha oil rig fire in 1988 and the BP Texas City refinery explosion in 2005. The document outlines common hazards in process industries like fires, explosions, and toxic releases, and describes phenomena that can cause accidents such as vapor cloud explosions and BLEVE (boiling liquid expanding vapor explosion) events.Hydraulic valves
Hydraulic valvesAmitabh Gairola
油
The document discusses objectives related to hydraulic valves. It covers the functions of different types of valves including pressure, directional, and volume/flow control valves. Some key points include that pressure control valves are used to limit, reduce, or set system pressures. Relief valves come in direct acting and pilot operated types. Pressure reducing valves include constant reduced and fixed amount types. Directional control valves include check valves, rotary valves, poppet valves, electro-hydraulic valves, and spool valves. Valves can be actuated mechanically, with pilots, or electrically.Reformer Tube Metallurgy: Design Considerations; Failure Mechanisms; Inspecti...
Reformer Tube Metallurgy: Design Considerations; Failure Mechanisms; Inspecti...Gerard B. Hawkins
油
The document discusses the metallurgy of reformer tubes, focusing on design principles, failure mechanisms, and inspection methods. It highlights the importance of optimizing tube life through improved materials and monitoring techniques, as well as addressing failure responses. The analysis includes details on temperature effects on tube life, recent metallurgical advancements, and inspection methods like non-destructive testing (NDT).14 Tips for Process Safety Management
14 Tips for Process Safety ManagementVerde Ventures Pvt. Ltd.
油
The document discusses Process Safety Management (PSM) and provides an overview of its key elements. PSM is a comprehensive management system that proactively avoids incidents in hazardous industries handling toxic chemicals. It integrates risk management across 14 elements, including employee participation, process hazard analysis, operating procedures, training, and compliance audits. The presentation aims to help organizations manage process safety risks in a more structured way.Process Safety Kpi
Process Safety KpiArthurGroot
油
This document outlines a 4-phase approach to determining process safety key performance indicators (KPIs) using the BowTie methodology. Phase 1 involves setting up BowTie diagrams using risk assessment reports. Phase 2 selects leading and lagging KPIs linked to barriers in the BowTie diagrams. Phase 3 establishes criteria and reporting standards for the KPIs. Phase 4 integrates incident data into the BowTie diagrams and starts an improvement cycle. The approach aims to comply with legislation and standards while identifying relevant process safety KPIs in a bottom-up manner tied to an organization's safety management system.Theory of Carbon Formation in Steam Reforming
Theory of Carbon Formation in Steam Reforming Gerard B. Hawkins
油
The document discusses carbon formation in steam methane reformers, outlining its causes, effects, and prevention methods. It identifies key factors contributing to carbon formation, including catalyst activity, steam-to-carbon ratios, and heat transfer efficiency. Additionally, it details the chemistry behind carbon formation from various feedstocks and emphasizes the importance of understanding these processes for optimizing refinery operations.101 Things That Can Go Wrong on a Primary Reformer - Best Practices Guide
101 Things That Can Go Wrong on a Primary Reformer - Best Practices GuideGerard B. Hawkins
油
This document discusses common problems that can occur in primary reformers and associated equipment. It identifies issues that can lead to plant shutdowns or efficiency losses, grouping them under catalysts, tubes, furnace boxes, burners, flue gas ducts, headers, and refractories. Some examples discussed include carbon formation, tube overheating, flame impingement, leaks in air preheaters, combustion air maldistribution, and damage to coffins. The document provides an overview of these issues to improve plant reliability over its lifespan.Pre-reformer Operations Technical Supplement
Pre-reformer Operations Technical SupplementGerard B. Hawkins
油
This document discusses operating pre-reformers at high temperatures and the associated benefits and drawbacks. It notes that while higher temperatures allow for better thermal efficiency and feedstock flexibility in reformers, they can also cause hydrothermal sintering of catalysts over time from high heat and steam. The document provides guidelines for startup, reduction, and operation of pre-reformer catalysts to maximize performance while mitigating sintering risks.HALDIA PETROCHEMICALS LIMITED
- 1. HALDIA PETROCHEMICALS LIMITED OFFER LETTER- Rejected & Bashed HR for delaying the offer for 2 months. Name Dharmaraj D Daddikar Asst. Manager- Manufacturing Location Haldia Sl. Salary Components Monthly Annualised 1 Basic 9,620 115,440 2 Additional Allowance 15,445 185,340 3 House Rent Allowance 3,608 43,296 4 Children Education Allowance 200 2,400 5 Children Hostel Allowance 600 7,200 6 Uniform Maintenance Allowance 500 6,000 7 Conveyance Allowance 0 0 8 Location Allowance* 3,125 37,500 A Pay Slip Gross 33,098 397,176 9 Leave Travel Allowance 601 7,212 10 Car Reimbursement 3500 42,000 11 Medical Reimbursement-Domiciliary 1,250 15,000 12 Uniform Reimbursement 1000 12,000 B Other Entitlements 6,351 76,212 13 Company's Contribution to Provident Fund 1,154 13,848
- 2. 14 Contribution to Superannuation Fund 1,443 17,316 15 Contribution to Gratuity Fund 546 6,552 C Contribution towards Retirals 3,143 37,716 D Cost to Company (CTC) (A+B+C) 42,592 511,104 E Maximum Performance Linked Pay (PLP) 94,721 F Total Cost to Company (TCC) (D+E) 605,825 Item 7 and 9 can not be claimed concurrently. In the event item 9 is not availe d, item 7 will be pa id within the overall limits of CTC. 1.0 *Location allowance is not included in calculation of PLP. This is base d on current place of posting. May change incase of permanent outstation transfer 2.0 *Interest subsidy on Housing Loan @5% subject to Company rules but not exceeding (annually) OFFER LETTER- Rejected & Bashed HR for delaying the worst offer. 57,720 3.0 *Maximum Benefit of Medical Reimbursement-Domiciliary (annually) 10,000 4.0 *Interest subsidy on Personal Loan @5% per annum on 60 EMIs on Max loan amount of 1,00,000 5.0 *Maximum benefit on the use of Car 0 6.0 Free hospitalization for self, family and dependent parents subject to Company rules. 7.0 Rs.40000/- maximum as Relocation Expenses + Air Check Fare by the shortest route 8.0 An amount not exceeding HRA will be deducted if accommodation is provided by Company. 9.0 Performance Linked Pay based on individual and organisational performance is payable subject to Company Rules 10.0 Superannuation, calculated as 15% of monthly Basic is contributed by the Company towards HPL Senior Staff Superannuation Fund, and is payable subject to Company rules. 11.0 The Gratuity amount is contributed towards the HPL Management Staff Gratuity Fund, and is payable subject to Company rules. * As per Company rule