Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
The document discusses the design of a Karr reciprocating-plate extractor (T-102) for a liquid-liquid extraction process in a biodiesel production plant. Key details include:
- Methanol will be used as the key component for the extractor design due to its solubility in both the feed and solvent streams.
- Design calculations are provided for the methanol recovery, distribution coefficient, continuous phase flux, and mass fraction of methanol in the raffinate stream.
- The operating feed to minimum solvent flow rate ratio is calculated as 2.2 based on the methanol distribution coefficient and mass fractions. This ratio is used to determine the minimum solvent flow rate of 2775.08 kg/h for
This document describes a process for producing hydrocarbon drying oils through the polymerization of butadiene and styrene monomers in the presence of sodium catalyst. It discusses conducting the reaction in a reactor, then treating the product solution with an organic acid to convert the sodium into a filterable salt. The process aims to improve upon large-scale production by continuously feeding reagents to a reactor while removing the polymerized product, and pre-treating make-up materials to improve reaction efficiency.
This document describes a process for producing hydrocarbon drying oils through the polymerization of butadiene and styrene monomers in the presence of sodium catalyst. It discusses conducting the reaction in a reactor, then treating the product solution with an organic acid to convert the sodium into a filterable salt. The process aims to improve upon previous large-scale methods by addressing issues like sodium handling hazards and slow reaction rates due to induction periods through continuous treatment of the product solution directly in the reactor with excess acid.
This document provides details on the urea granulation process. It describes the characteristics of granular urea including composition requirements. It outlines the granulation process which involves spraying liquid urea solution onto seed material in a fluidized bed. Key equipment involved includes the granulator, fluid bed coolers, screens, and conveying equipment. Startup and operating procedures are also summarized, focusing on gradually heating and preparing the granulator while maintaining proper process conditions.
Economics of ammonia production from offgasesVK Arora
This document discusses opportunities for producing ammonia from hydrogen-rich off-gas streams from various petrochemical processes. As ethane cracking increases in the US and Middle East, these cracker plants produce large volumes of hydrogen-rich off-gas that can be used to power ammonia plants. Several process options are reviewed for utilizing these off-gases in ammonia production, including PSA, nitrogen wash, and secondary reforming. A case study evaluates the economics of using off-gases from ethane crackers, propane dehydrogenation plants, and methanol plants to power ammonia facilities in the US Gulf Coast and Middle East. Producing ammonia from these off-gases can provide environmental benefits through reduced nitrogen oxide
Investigation on evaporative emission from a gasoline polycarbonate fuel tankeSAT Journals
Abstract It is estimated that about 15 to 20 percent of the vehicle hydrocarbon (HC) emission were due to evaporation of fuel. Hence a need was felt to understand the extent of evaporative emission from gasoline fuel system. A polycarbonate fuel tank that is predominantly used in two wheeled vehicles is considered for study. Emission can surface to atmosphere in three modes; diffusion through fuel tank wall, escaping through vent in tank and when fuel tank cap is opened for refueling. The average temperature condition which prevails in south India which is in the range of 27o C to 34oC was considered. From which temperatures which were at proximity to peak high and low day time were chosen. The complete set up was placed in open atmosphere to replicate the working environment. The emission constituents and its levels were measured by conducting the test particularly for averaged out day time high and low temperature condition. Further diffusion test was conducted within a range of 34oC to 36oC, this temperature is considered to be range of maximum temperature which prevails in south India. From which a temperature was chosen and the test was conducted. This comparative study gives an indication of emission and its quantity from the fuel tank at the ambient temperature. Keywords: Evaporative Emission, Fuel Tank, HC Emission
F E R T I L I Z E R I N D U S T R Y L E C T U R E 1Rishi Yadav
The document discusses the fertilizer industry and the manufacturing of nitrogen, phosphorus, and potassium (NPK) fertilizers. It explains that nitrogen, phosphorus, and potassium are essential nutrients for plant growth. Ammonia is synthesized from natural gas and used to produce nitrogen fertilizers like ammonium nitrate. Phosphoric acid is made from phosphate rock and used in phosphorus fertilizers. The different components are granulated, blended, and bagged to produce composite NPK fertilizer. Modern fertilizer production aims to synthesize ammonia and manufacture NPK fertilizers efficiently using optimized reactor designs and processes.
The document discusses offshore oil and gas production technology. It explains the key functions and design considerations of processing facilities, including separating reservoir fluids, treating them as needed, and storing or exporting the fluids. It also describes the types of reservoirs as crude oil, dry gas, or condensate wells. Additionally, the document outlines the essential components and processes on the topside of a floating production, storage, and offloading (FPSO) unit, including three-phase separation and treatment of the oil, gas, and water phases for export, disposal, injection or supporting production.
The document discusses the design of a Karr reciprocating-plate extractor (T-102) for a liquid-liquid extraction process in a biodiesel production plant. Key details include:
- Methanol will be used as the key component for the extractor design due to its solubility in both the feed and solvent streams.
- Design calculations are provided for the methanol recovery, distribution coefficient, continuous phase flux, and mass fraction of methanol in the raffinate stream.
- The operating feed to minimum solvent flow rate ratio is calculated as 2.2 based on the methanol distribution coefficient and mass fractions. This ratio is used to determine the minimum solvent flow rate of 2775.08 kg/h for
This document describes a process for producing hydrocarbon drying oils through the polymerization of butadiene and styrene monomers in the presence of sodium catalyst. It discusses conducting the reaction in a reactor, then treating the product solution with an organic acid to convert the sodium into a filterable salt. The process aims to improve upon large-scale production by continuously feeding reagents to a reactor while removing the polymerized product, and pre-treating make-up materials to improve reaction efficiency.
This document describes a process for producing hydrocarbon drying oils through the polymerization of butadiene and styrene monomers in the presence of sodium catalyst. It discusses conducting the reaction in a reactor, then treating the product solution with an organic acid to convert the sodium into a filterable salt. The process aims to improve upon previous large-scale methods by addressing issues like sodium handling hazards and slow reaction rates due to induction periods through continuous treatment of the product solution directly in the reactor with excess acid.
This document provides details on the urea granulation process. It describes the characteristics of granular urea including composition requirements. It outlines the granulation process which involves spraying liquid urea solution onto seed material in a fluidized bed. Key equipment involved includes the granulator, fluid bed coolers, screens, and conveying equipment. Startup and operating procedures are also summarized, focusing on gradually heating and preparing the granulator while maintaining proper process conditions.
Economics of ammonia production from offgasesVK Arora
This document discusses opportunities for producing ammonia from hydrogen-rich off-gas streams from various petrochemical processes. As ethane cracking increases in the US and Middle East, these cracker plants produce large volumes of hydrogen-rich off-gas that can be used to power ammonia plants. Several process options are reviewed for utilizing these off-gases in ammonia production, including PSA, nitrogen wash, and secondary reforming. A case study evaluates the economics of using off-gases from ethane crackers, propane dehydrogenation plants, and methanol plants to power ammonia facilities in the US Gulf Coast and Middle East. Producing ammonia from these off-gases can provide environmental benefits through reduced nitrogen oxide
Investigation on evaporative emission from a gasoline polycarbonate fuel tankeSAT Journals
Abstract It is estimated that about 15 to 20 percent of the vehicle hydrocarbon (HC) emission were due to evaporation of fuel. Hence a need was felt to understand the extent of evaporative emission from gasoline fuel system. A polycarbonate fuel tank that is predominantly used in two wheeled vehicles is considered for study. Emission can surface to atmosphere in three modes; diffusion through fuel tank wall, escaping through vent in tank and when fuel tank cap is opened for refueling. The average temperature condition which prevails in south India which is in the range of 27o C to 34oC was considered. From which temperatures which were at proximity to peak high and low day time were chosen. The complete set up was placed in open atmosphere to replicate the working environment. The emission constituents and its levels were measured by conducting the test particularly for averaged out day time high and low temperature condition. Further diffusion test was conducted within a range of 34oC to 36oC, this temperature is considered to be range of maximum temperature which prevails in south India. From which a temperature was chosen and the test was conducted. This comparative study gives an indication of emission and its quantity from the fuel tank at the ambient temperature. Keywords: Evaporative Emission, Fuel Tank, HC Emission
F E R T I L I Z E R I N D U S T R Y L E C T U R E 1Rishi Yadav
The document discusses the fertilizer industry and the manufacturing of nitrogen, phosphorus, and potassium (NPK) fertilizers. It explains that nitrogen, phosphorus, and potassium are essential nutrients for plant growth. Ammonia is synthesized from natural gas and used to produce nitrogen fertilizers like ammonium nitrate. Phosphoric acid is made from phosphate rock and used in phosphorus fertilizers. The different components are granulated, blended, and bagged to produce composite NPK fertilizer. Modern fertilizer production aims to synthesize ammonia and manufacture NPK fertilizers efficiently using optimized reactor designs and processes.
The document discusses offshore oil and gas production technology. It explains the key functions and design considerations of processing facilities, including separating reservoir fluids, treating them as needed, and storing or exporting the fluids. It also describes the types of reservoirs as crude oil, dry gas, or condensate wells. Additionally, the document outlines the essential components and processes on the topside of a floating production, storage, and offloading (FPSO) unit, including three-phase separation and treatment of the oil, gas, and water phases for export, disposal, injection or supporting production.
This document provides steps for starting up a urea production plant using the Saipem process. It describes conducting sealing tests, purging sections with nitrogen, heating equipment, charging ammonia, and feeding ammonia and carbon dioxide into the reactor while monitoring pressures and temperatures. The goal is to reach stable operating conditions for urea production. Diagrams are included to illustrate the reactor, separators, decomposers, and other key equipment involved in the startup process.
The document discusses offshore gas production and processing systems. It explains that associated gas from an FPSO can be 1) exported, 2) used for gas lifting/injection, 3) used as fuel gas, or 4) flared during shutdowns. It then describes the multi-stage compression and cooling processes the gas undergoes, including scrubbing, dehydration using glycol or molecular sieves, and cooling to remove condensates before export via pipelines. Hydrates are gas-water compounds that can form and block pipes, but chemical injection or dehydration can prevent their formation.
This document provides information about engine and emission control systems, including specifications, diagrams, component locations, and inspection procedures. It covers the crankcase emission control system, evaporative emission control system, exhaust gas recirculation system, and catalytic converter. Check procedures are described for the accelerator cable, positive crankcase ventilation system, purge control system, and exhaust gas recirculation valve. Specifications and diagrams are provided for reference.
This document describes an ammonia plant with three urea plants. It summarizes the key details of each plant including their commissioning dates, capacities, and revamp history. It then provides details on the ammonia and urea production processes, including descriptions of the main units involved at each stage of production from natural gas feedstock to the final urea product. Process diagrams and pictures are included to illustrate the key components and flow of materials through the plant.
This document provides a summary of an individual's qualifications for an operator role. It outlines 8.5 years of experience as an operator in India and Saudi Arabia, including experience operating ammonia plants and utilities. Educational qualifications include a Bachelor's degree in chemistry. Responsibilities have included operating equipment in areas like reforming, acid gas removal, refrigeration, and distillation. Safety training and qualifications are also mentioned. The individual is seeking an operator role utilizing their experience.
Veera Babu Gollapalli is applying for a position as a Process Operator or Panel Operator with over 8 years of experience working in ammonia plants and utilities in India and Saudi Arabia. He has a Bachelor's degree in Chemistry and is proficient in plant operations, pre-commissioning, commissioning, and maintenance activities. His responsibilities have included operating equipment across various plant sections including reforming, synthesis, refrigeration, and more. He is skilled in operating systems like compressors, turbines, heat exchangers, and other process equipment.
Environment management and advanced waste treatment system in nitrogenious fe...Prem Baboo
The paper intended to the standpoint of harmful emissions typical nitrogen-based fertilizer plants producing ammonia and urea plants using the advanced available technologies. The critical emission points are established and analyzed. Several possible actions have been taken in order to minimize the emissions are presented.The method is low cost and at the same time enhances the fertilizer value of sewage sludge. It therefore has a large potential of competing with more established methods of sanitization.
Hydrogen recovery from purge gas(energy saving)Prem Baboo
Ammonia is continuously condensed out of the loop and fresh synthesis gas is added. Because the synthesis gas contains small quantities of methane and argon, these impurities build up in the loop and must be continuously purged to prevent them from exceeding a certain concentration. Although this purge stream can be used to supplement reformer fuel gas, it contains valuable hydrogen which is lost from the ammonia synthesis loop In order to achieve optimum conversion in synthesis convertor, it is necessary to purge a certain quantity of gas from synthesis loop so as to as to reduce inerts concentration in the loop. Purge gas stream from ammonia process contains ammonia, hydrogen, nitrogen and other inert gases. Among them, ammonia itself is the valuable product lost with the purge stream. Moreover it has a serious adverse effect on the environment.This purge gas containing about 60% Hydrogen was fully utilised as primary reformer fuel.
The evaporative emission control system prevents fuel vapors from escaping into the atmosphere. It includes a canister that absorbs fuel vapors from the fuel tank, and solenoid valves including the purge control solenoid valve and pressure control solenoid valve that are controlled by the ECM. The system also has a fuel cut valve in the fuel tank and a fuel tank pressure sensor that is used to diagnose the system and check for leaks by varying the fuel tank pressure and measuring it.
This document summarizes a study on using ceramic membrane filtration for treating oily wastewater. The key findings are:
1) Ceramic membrane filtration was found to be an effective method for removing pollutants from oily wastewater, achieving over 85% removal of oil and grease, and over 98% removal of total suspended solids and turbidity.
2) The optimal operating parameters were determined to be a transmembrane pressure of 1.25 bar, cross-flow velocity of 2.25 m/s, and temperature of 32.5°C.
3) Periodic backwashing was able to recover 95% of the original flux, but chemical cleaning was required when flux
This document describes a system for on-site hydrogen production and its use in an internal combustion engine. The system generates hydrogen through the reaction of aluminum and water with sodium hydroxide as a catalyst. The hydrogen is then filtered, stored, and supplied to a modified internal combustion engine. An alternator coupled to the engine can power loads and a dosing pump to continuously supply reactants to the reaction chamber for on-demand hydrogen production. The system aims to provide a safe and portable way to generate power using hydrogen without high-pressure storage.
This document proposes a new concept for internal combustion engines that uses homogeneous combustion in a porous medium. It introduces porous medium technology, which utilizes the heat transfer and flame propagation properties of highly porous materials like silicon carbide foam. This technology aims to achieve homogeneous mixing, ignition, and combustion within the porous structure to reduce emissions and improve efficiency. Two types of porous medium engines are described - one with periodic contact and one with permanent contact between the working gas and porous medium. The technology offers advantages like very low emissions, higher efficiency, fast combustion, and multi-fuel capability.
The document provides details on the process of producing ethanol from corn using the dry milling method. It includes a block flow diagram outlining the key steps: preprocessing, liquefaction/saccharification, fermentation, and purification. A process flow diagram shows the flow of materials between major equipment like reactors, distillation columns, and storage tanks. Mass and energy balances are also presented, calculating theoretical yields at each stage based on inputs of 1,000,000 metric tons of corn feedstock per year. Key reactions and conversions are defined, with calculations of water, glucose, ethanol, carbon dioxide, alpha amylase, and yeast flows.
The document provides information about Uhde's ammonia process technology. It discusses Uhde's extensive experience designing and building ammonia plants dating back to 1928. Key aspects of the Uhde ammonia process are described, including modifications to reduce energy consumption in steam reforming, CO2 removal using aMDEA, and a high-conversion ammonia synthesis unit using a three-bed radial flow reactor design. The document also provides process details and performance figures for recent large-scale Uhde ammonia plants.
Brief desccription of ammonia & urea plants with revampPrem Baboo
This document provides an overview of the proposed revamp of the existing ammonia and urea plants at the Vijaipur fertilizer complex in India. The revamp aims to increase the capacity of the ammonia and urea plants through various energy saving measures. It will increase the ammonia capacity of Line I by 150 MTPD to 1750 MTPD and Line II by 225 MTPD to 1864 MTPD. The urea capacity of Line I will increase to 3030 MTPD and Line II to 3231 MTPD. A 450 MTPD carbon dioxide recovery plant will also be installed to meet the additional CO2 needs of the urea plants. The revamp aims to enhance self
The document summarizes a senior capstone design project for LyondellBasell involving improvements to an existing distillation column and condenser system. A team of 4 chemical engineering students was tasked with increasing the purity of ethylene in the overhead stream and propylene in the bottom stream. Their proposed design involved adding 10 feet of packing to the distillation column and replacing the existing stab-in condenser with a new overhead condenser. The team performed mass balances, determined the minimum number of stages and reflux ratio, and designed the new condenser. An economic analysis found the project would have a positive NPV of $700K and IRR of 38%, indicating the savings from improved reliability would outweigh the costs
P & i diagram and tagging philosphy forPrem Baboo
The document discusses Piping and Instrumentation Diagrams (P&IDs) which are diagrams used in process industries to show piping, equipment, instrumentation and process flow. It provides details on the components of P&IDs such as abbreviations, instrument symbols and tagging philosophies. It also includes examples of equipment lists and coding systems used for P&IDs.
This document presents a process design for producing ethanol from sugarcane at a plant in Louisiana. It includes mass and energy balances for the four main processes: milling, juice clarification, fermentation, and distillation. The total equipment cost is $21 million and the projected revenue is $145 million per year. A cash flow analysis over 20 years using a 7% discount rate yields a positive net present value of $60 million.
The document is a patent application for a system and method for rejuvenating coated components, such as turbine blades, of a gas turbine engine. The method involves uninstalling the damaged coated component, isolating a first coated portion from a second coated portion, and simultaneously depositing a first coating material on the first portion and a different second coating material on the second portion. The rejuvenated component is then reinstalled into the gas turbine engine. The system aims to provide a more efficient rejuvenation process compared to conventional full repair methods.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
This document provides steps for starting up a urea production plant using the Saipem process. It describes conducting sealing tests, purging sections with nitrogen, heating equipment, charging ammonia, and feeding ammonia and carbon dioxide into the reactor while monitoring pressures and temperatures. The goal is to reach stable operating conditions for urea production. Diagrams are included to illustrate the reactor, separators, decomposers, and other key equipment involved in the startup process.
The document discusses offshore gas production and processing systems. It explains that associated gas from an FPSO can be 1) exported, 2) used for gas lifting/injection, 3) used as fuel gas, or 4) flared during shutdowns. It then describes the multi-stage compression and cooling processes the gas undergoes, including scrubbing, dehydration using glycol or molecular sieves, and cooling to remove condensates before export via pipelines. Hydrates are gas-water compounds that can form and block pipes, but chemical injection or dehydration can prevent their formation.
This document provides information about engine and emission control systems, including specifications, diagrams, component locations, and inspection procedures. It covers the crankcase emission control system, evaporative emission control system, exhaust gas recirculation system, and catalytic converter. Check procedures are described for the accelerator cable, positive crankcase ventilation system, purge control system, and exhaust gas recirculation valve. Specifications and diagrams are provided for reference.
This document describes an ammonia plant with three urea plants. It summarizes the key details of each plant including their commissioning dates, capacities, and revamp history. It then provides details on the ammonia and urea production processes, including descriptions of the main units involved at each stage of production from natural gas feedstock to the final urea product. Process diagrams and pictures are included to illustrate the key components and flow of materials through the plant.
This document provides a summary of an individual's qualifications for an operator role. It outlines 8.5 years of experience as an operator in India and Saudi Arabia, including experience operating ammonia plants and utilities. Educational qualifications include a Bachelor's degree in chemistry. Responsibilities have included operating equipment in areas like reforming, acid gas removal, refrigeration, and distillation. Safety training and qualifications are also mentioned. The individual is seeking an operator role utilizing their experience.
Veera Babu Gollapalli is applying for a position as a Process Operator or Panel Operator with over 8 years of experience working in ammonia plants and utilities in India and Saudi Arabia. He has a Bachelor's degree in Chemistry and is proficient in plant operations, pre-commissioning, commissioning, and maintenance activities. His responsibilities have included operating equipment across various plant sections including reforming, synthesis, refrigeration, and more. He is skilled in operating systems like compressors, turbines, heat exchangers, and other process equipment.
Environment management and advanced waste treatment system in nitrogenious fe...Prem Baboo
The paper intended to the standpoint of harmful emissions typical nitrogen-based fertilizer plants producing ammonia and urea plants using the advanced available technologies. The critical emission points are established and analyzed. Several possible actions have been taken in order to minimize the emissions are presented.The method is low cost and at the same time enhances the fertilizer value of sewage sludge. It therefore has a large potential of competing with more established methods of sanitization.
Hydrogen recovery from purge gas(energy saving)Prem Baboo
Ammonia is continuously condensed out of the loop and fresh synthesis gas is added. Because the synthesis gas contains small quantities of methane and argon, these impurities build up in the loop and must be continuously purged to prevent them from exceeding a certain concentration. Although this purge stream can be used to supplement reformer fuel gas, it contains valuable hydrogen which is lost from the ammonia synthesis loop In order to achieve optimum conversion in synthesis convertor, it is necessary to purge a certain quantity of gas from synthesis loop so as to as to reduce inerts concentration in the loop. Purge gas stream from ammonia process contains ammonia, hydrogen, nitrogen and other inert gases. Among them, ammonia itself is the valuable product lost with the purge stream. Moreover it has a serious adverse effect on the environment.This purge gas containing about 60% Hydrogen was fully utilised as primary reformer fuel.
The evaporative emission control system prevents fuel vapors from escaping into the atmosphere. It includes a canister that absorbs fuel vapors from the fuel tank, and solenoid valves including the purge control solenoid valve and pressure control solenoid valve that are controlled by the ECM. The system also has a fuel cut valve in the fuel tank and a fuel tank pressure sensor that is used to diagnose the system and check for leaks by varying the fuel tank pressure and measuring it.
This document summarizes a study on using ceramic membrane filtration for treating oily wastewater. The key findings are:
1) Ceramic membrane filtration was found to be an effective method for removing pollutants from oily wastewater, achieving over 85% removal of oil and grease, and over 98% removal of total suspended solids and turbidity.
2) The optimal operating parameters were determined to be a transmembrane pressure of 1.25 bar, cross-flow velocity of 2.25 m/s, and temperature of 32.5°C.
3) Periodic backwashing was able to recover 95% of the original flux, but chemical cleaning was required when flux
This document describes a system for on-site hydrogen production and its use in an internal combustion engine. The system generates hydrogen through the reaction of aluminum and water with sodium hydroxide as a catalyst. The hydrogen is then filtered, stored, and supplied to a modified internal combustion engine. An alternator coupled to the engine can power loads and a dosing pump to continuously supply reactants to the reaction chamber for on-demand hydrogen production. The system aims to provide a safe and portable way to generate power using hydrogen without high-pressure storage.
This document proposes a new concept for internal combustion engines that uses homogeneous combustion in a porous medium. It introduces porous medium technology, which utilizes the heat transfer and flame propagation properties of highly porous materials like silicon carbide foam. This technology aims to achieve homogeneous mixing, ignition, and combustion within the porous structure to reduce emissions and improve efficiency. Two types of porous medium engines are described - one with periodic contact and one with permanent contact between the working gas and porous medium. The technology offers advantages like very low emissions, higher efficiency, fast combustion, and multi-fuel capability.
The document provides details on the process of producing ethanol from corn using the dry milling method. It includes a block flow diagram outlining the key steps: preprocessing, liquefaction/saccharification, fermentation, and purification. A process flow diagram shows the flow of materials between major equipment like reactors, distillation columns, and storage tanks. Mass and energy balances are also presented, calculating theoretical yields at each stage based on inputs of 1,000,000 metric tons of corn feedstock per year. Key reactions and conversions are defined, with calculations of water, glucose, ethanol, carbon dioxide, alpha amylase, and yeast flows.
The document provides information about Uhde's ammonia process technology. It discusses Uhde's extensive experience designing and building ammonia plants dating back to 1928. Key aspects of the Uhde ammonia process are described, including modifications to reduce energy consumption in steam reforming, CO2 removal using aMDEA, and a high-conversion ammonia synthesis unit using a three-bed radial flow reactor design. The document also provides process details and performance figures for recent large-scale Uhde ammonia plants.
Brief desccription of ammonia & urea plants with revampPrem Baboo
This document provides an overview of the proposed revamp of the existing ammonia and urea plants at the Vijaipur fertilizer complex in India. The revamp aims to increase the capacity of the ammonia and urea plants through various energy saving measures. It will increase the ammonia capacity of Line I by 150 MTPD to 1750 MTPD and Line II by 225 MTPD to 1864 MTPD. The urea capacity of Line I will increase to 3030 MTPD and Line II to 3231 MTPD. A 450 MTPD carbon dioxide recovery plant will also be installed to meet the additional CO2 needs of the urea plants. The revamp aims to enhance self
The document summarizes a senior capstone design project for LyondellBasell involving improvements to an existing distillation column and condenser system. A team of 4 chemical engineering students was tasked with increasing the purity of ethylene in the overhead stream and propylene in the bottom stream. Their proposed design involved adding 10 feet of packing to the distillation column and replacing the existing stab-in condenser with a new overhead condenser. The team performed mass balances, determined the minimum number of stages and reflux ratio, and designed the new condenser. An economic analysis found the project would have a positive NPV of $700K and IRR of 38%, indicating the savings from improved reliability would outweigh the costs
P & i diagram and tagging philosphy forPrem Baboo
The document discusses Piping and Instrumentation Diagrams (P&IDs) which are diagrams used in process industries to show piping, equipment, instrumentation and process flow. It provides details on the components of P&IDs such as abbreviations, instrument symbols and tagging philosophies. It also includes examples of equipment lists and coding systems used for P&IDs.
This document presents a process design for producing ethanol from sugarcane at a plant in Louisiana. It includes mass and energy balances for the four main processes: milling, juice clarification, fermentation, and distillation. The total equipment cost is $21 million and the projected revenue is $145 million per year. A cash flow analysis over 20 years using a 7% discount rate yields a positive net present value of $60 million.
The document is a patent application for a system and method for rejuvenating coated components, such as turbine blades, of a gas turbine engine. The method involves uninstalling the damaged coated component, isolating a first coated portion from a second coated portion, and simultaneously depositing a first coating material on the first portion and a different second coating material on the second portion. The rejuvenated component is then reinstalled into the gas turbine engine. The system aims to provide a more efficient rejuvenation process compared to conventional full repair methods.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Stanley A Meyer Legacy Back up Secret Docs Save all Protect Spread print and give to schools NEVER STOP!!!!!!! Join Support here https://www.patreon.com/securesupplies/shop
International Journal of Engineering and Science Invention (IJESI)inventionjournals
International Journal of Engineering and Science Invention (IJESI) is an international journal intended for professionals and researchers in all fields of computer science and electronics. IJESI publishes research articles and reviews within the whole field Engineering Science and Technology, new teaching methods, assessment, validation and the impact of new technologies and it will continue to provide information on the latest trends and developments in this ever-expanding subject. The publications of papers are selected through double peer reviewed to ensure originality, relevance, and readability. The articles published in our journal can be accessed online
A Critical Review on the Concept of Effect on Scavenging and Fuel Injection T...ijsrd.com
In present study, A spark ignition and a compression ignition engine with uniflow valve scavenging of the cylinder and a transfer valve in the piston crown have been described. A great disadvantage of two-stroke engines is ports which are made in the cylinder bearing surface. Under the heat which is realised during the combustion, the thermal extension of the range in proximity of the ports and other parts of the cylinder is different and so the distortion of the geometry of the cylinder liner surface force the designer to make the clearance between the piston and the cylinder liner bigger. This paper presents the critical review to study the effect of fuel injection timing and scavenging using diesel on the combustion and emission characteristics of a single cylinder, two stroke, air cooled direct injection diesel engine. It is well known that injection strategies including the injection timing and pressure play the most important role in determining engine performance, especially in scavenging emissions. However, the injection timing and pressure quantitatively affect the performance of the diesel engine.
The document discusses the purpose and function of various components of a vehicle's air intake and exhaust systems. It describes how the air intake filtration system removes dirt and particles from incoming air to protect engine components. Intake manifolds distribute the air/fuel mixture to cylinders, and can be designed for optimal performance. The exhaust system removes gases from the cylinders and includes manifolds, mufflers, and tailpipes to muffle sounds while safely expelling exhaust.
Stanley A Meyer Legacy Back up Secret Docs Save all Protect Spread print and give to schools NEVER STOP!!!!!!! Join Support here https://www.patreon.com/securesupplies/shop
This document describes improvements to an apparatus for applying edible fats to bakery dough pieces on a conveyor belt. The apparatus sprays precise amounts of oil onto dough pieces from nozzles connected to a high-pressure pump. Excess oil is scraped off the conveyor belt into a tray and drained back into the oil tank through strainers. The pump, nozzles, and conveyor speed are adjustable to ensure each dough piece receives only the optimal amount of lubrication.
The document discusses gas exchange processes in internal combustion engines. It covers topics like supercharging, turbocharging, scavenging processes, compressors, turbines, and factors that influence the residual gas fraction. It provides details on different scavenging configurations for 2-stroke engines and the intake and exhaust processes in a 4-stroke engine. Diagrams are included to illustrate the various concepts.
Stanley A Meyer Legacy Back up Secret Docs Save all Protect Spread print and give to schools NEVER STOP!!!!!!! Join Support here https://www.patreon.com/securesupplies/shop
Volvo L90D Wheel Loader Service Repair Manual Instant Download.pdffijsekkkdmdm3e
The document provides specifications and service information for engines, including:
- The L90D is equipped with a TD63KBE engine and the L120D with a TD73KDE engine.
- Both engines are 6-cylinder 4-stroke turbocharged diesel engines with intercoolers.
- The engines have wet cylinder liners and separate cylinder heads covering 3 cylinders each.
- Lubrication is provided by a force-feed system and the turbocharger supplies pressurized air.
Volvo L90D Wheel Loader Service Repair Manual Instant Download.pdftepu22753653
The document provides specifications and service information for engines, including:
- The L90D is equipped with a TD63KBE engine and the L120D with a TD73KDE engine.
- Both engines are 6-cylinder 4-stroke turbocharged diesel engines with intercoolers.
- The engines use wet cylinder liners and have two separate cylinder heads.
- Lubrication is provided by a force-feed lubrication system and the turbocharger is cooled by engine oil.
Volvo L90D Wheel Loader Service Repair Manual Instant Download.pdffapanhe306271
The document provides specifications and service information for engines. It describes the TD63KBE and TD73KDE engines, including their outputs, dimensions, lubrication systems and components like the turbocharger and intercooler. It also provides instructions for installing and removing the engines, listing the steps and necessary tools and equipment. Specification tables outline engine weights and capacities, tightening torques and other technical details.
Volvo L90D Wheel Loader Service Repair Manual Instant Download.pdfrou774513po
The document provides specifications and service information for engines, including:
- The L90D is equipped with a TD63KBE engine and the L120D with a TD73KDE engine.
- Both engines are 6-cylinder 4-stroke turbocharged diesel engines with intercoolers.
- The engines have wet cylinder liners and separate cylinder heads covering 3 cylinders each.
- Lubrication is provided by a force-feed system and the turbocharger supplies pressurized air.
Volvo L90D Wheel Loader Service Repair Manual Instant Download.pdff8iosedkdm3e
The document provides service information for engines including specifications, capacities, general information, tightening torques, and procedures for installing and removing engines. It details the engine types, their outputs and dimensions, lubrication systems, and installation and removal steps that include attaching lifting devices, disconnecting various components, and filling fluids.
Volvo L90D Wheel Loader Service Repair Manual Instant Download.pdflunrizan628
The document provides specifications and service information for engines. It describes the TD63KBE and TD73KDE engines, including their outputs, dimensions, lubrication systems and components like the turbocharger and intercooler. It also provides instructions for installing and removing the engines, listing the steps and necessary tools and equipment. Specification tables outline engine weights and capacities, tightening torques and other technical details.
This document describes a waterborne platinum coating composition for coating gas turbine engine components. The coating composition contains 20-40% platinum powder, 0.5-5% polymeric binder, less than 1% surfactant, and 55-80% water. It can be applied to components via dip or spray coating. Upon heating, the coating thermally decomposes to form a platinum diffusion coating, which can then be converted to a platinum aluminide coating for oxidation and corrosion protection at turbine operating temperatures. The coating composition allows platinum coating via lower-cost liquid application rather than expensive electroplating.
Caterpillar ammonia engine patent power production microgridsSteve Wittrig
This power system includes an ammonia-fueled combustion engine that generates mechanical power for driving an output device. The system also includes an electrical unit that can supplement the mechanical power delivered to the output device during certain operating conditions. This allows the system to operate reliably when combusting ammonia alone as the primary fuel in the engine.
The document discusses CFD analysis of a gas turbine combustor. It aims to optimize the diameter, position, and number of dilution holes in a can-type combustor. A 3D model was created using ANSYS CFX software. Simulations were performed with methane gas, varying the dilution hole parameters. The optimized design was found to have 5 holes of 30mm diameter in each of two rows arranged in a zigzag pattern. This provided the lowest combustor exit temperature. A structural analysis of the optimized model showed it was structurally stable with a safety factor of 2.95.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
Inventors and entrepreneurs have vocations fueled by passion. Many would have done it for free or as a hobby if it hadn’t become a profession. Mark Rosenzweig is a natural creator, driven by his passion. This fuel has led Mark to develop his ideas into viable products and innovations that he has been patenting since 2003. From an innovative filter sensor and indicator for vacuum cleaners to a basket for deep fryer and methods of cooking food products to a compact cyclonic bagless vacuum cleaner. Sometimes independently and often as part of creative teams, Mark has patented just under one hundred innovative inventions between 2003 and 2017.
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Ep3396116 a2
1. Printed by Jouve, 75001 PARIS (FR)
(19)EP3396116A2
TEPZZ¥¥96__6A T
(11) EP 3 396 116 A2
(12) EUROPEAN PATENT APPLICATION
(43) Date of publication:
31.10.2018 Bulletin 2018/44
(21) Application number: 18169458.9
(22) Date of filing: 26.04.2018
(51) Int Cl.:
F01D 25/00 (2006.01)
B08B 9/00 (2006.01)
B64F 5/30 (2017.01)
(84) Designated Contracting States:
AL AT BE BG CH CY CZ DE DK EE ES FI FR GB
GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO
PL PT RO RS SE SI SK SM TR
Designated Extension States:
BA ME
Designated Validation States:
KH MA MD TN
(30) Priority: 26.04.2017 US 201715498141
(71) Applicant: General Electric Company
Schenectady, NY 12345 (US)
(72) Inventors:
• MILLHAEM, Michael Robert
West Chester, OH Ohio 45069 (US)
• TIBBETTS, Nicole
Niskayuna, NY New York 12309 (US)
• PRITCHARD, Byron Andrew
Cincinnati, OH Ohio 45215 (US)
• BEWLAY, Bernard Patrick
Niskayuna, NY New York 12309 (US)
• LAURIA, Keith Anthony
Niskayuna, NY New York 12309 (US)
• KULKARNI, Ambarish Jayant
Niskayuna, NY New York 12309 (US)
• ROSENZWEIG, Mark
Cincinnati, OH Ohio 45215 (US)
• MORRA, Martin Matthew
Niskayuna, NY New York 12309 (US)
• SAMBOR, Timothy Mark
West Chester, OH Ohio 45069 (US)
• JENKINS, Andrew James
Cardiff, Mid Glamorgan CF15 7YJ (GB)
(74) Representative: Williams, Andrew Richard
GE International Inc.
GPO-Europe
The Ark
201 Talgarth Road
Hammersmith
London W6 8BJ (GB)
(54) METHODS OF CLEANING A COMPONENT WITHIN A TURBINE ENGINE
(57) A method of cleaning a component 127 within a
turbine 10 that includes disassembling the turbine engine
10 to provide a flow path 137 to an interior passageway
136 of the component from an access point 138. The
component 127 has coked hydrocarbons formed there-
on. The method further includes discharging a flow of
cleaning solution towards the interior passageway 136
from the access point 138, wherein the cleaning solution
is configured to remove the coked hydrocarbons from
the component 127.
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Description
BACKGROUND
[0001] The present disclosure relates generally to tur-
bine engines and, more specifically, to cleaning coked
hydrocarbons from a component within a turbine engine.
[0002] In a gas turbine engine, air is pressurized in a
compressor, mixed with fuel in a combustor, and ignited
such that hot combustion gas is generated. In at least
some known turbine engines, ignition of the air and fuel
can result in oxidation and partial decomposition of the
mixture, thereby resulting in coking within the turbine en-
gine. More specifically, coking is a process that forms
hard deposits within a fuel supply system of the turbine
engine, for example. The hard deposits also form from
other hydrocarbon-based substances in other areas of
the turbine engine, such as in a fan assembly of the tur-
bine engine. Excess buildup of the hard deposits in the
turbine engine can clog the components of the turbine
engine, and necessitate service of the turbine engine af-
ter prolonged use. For example, servicing the fuel supply
system generally includes detaching the turbine engine
from an airframe, removing fuel nozzles of the fuel supply
system from the turbine engine, replacing the fuel noz-
zles with different fuel nozzles, transferring the removed
fuel nozzles to another location for cleaning, and reat-
taching the turbine engine to the airframe. As such, a
stockpile of unused turbine engine components is main-
tained in the event a turbine engine is scheduled for serv-
ice. In addition, removing and replacing fuel nozzles in
the fuel supply system can be a time-consuming and la-
borious task. Moreover, if combusted engine oil is
trapped outside of the fuel supply system, such as in the
fanassembly,critical ventilation canbeblocked, resulting
in unscheduled engine removal and significant disas-
sembly to service the components at a piece-part level.
BRIEF DESCRIPTION
[0003] In one aspect, a method of cleaning a compo-
nent within a turbine engine is provided. The method in-
cludesdisassembling the turbine engine to provide a flow
path to an interior passageway of the component from
an access point. The component has coked hydrocar-
bons formed thereon. The method further includes dis-
charging a flow of cleaning solution towards the interior
passageway from the access point, wherein the cleaning
solution is configured to remove the coked hydrocarbons
from the component.
[0004] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, disassembling the tur-
bine engine includes disassembling the turbine engine
when the turbine engine is coupled to an airframe.
[0005] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, disassembling the tur-
bine engine includes disassembling a fuel manifold to
define an inlet port within the fuel manifold, wherein the
inlet port defines the access point.
[0006] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, discharging a flow of
cleaning solution includes discharging the flow of clean-
ing solution towards the interior passageway in a pulsed
interval having a discharge time defined within a range
between about 5 seconds and about 120 seconds.
[0007] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, discharging a flow of
cleaning solution includes discharging the flow of clean-
ing solution towards the interior passageway in at least
a first pulsed interval and a second pulsed interval,
wherein a residence time is defined between the first
pulsed interval and the second pulsed interval.
[0008] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, the method further in-
cludes defining the residence time within a range be-
tween about 2 minutes and about 30 minutes.
[0009] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, discharging a flow of
cleaningsolutioncomprisesheatingthecleaningsolution
to a temperature defined within a range between about
30°C and 95°C.
[0010] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, the method further in-
cludes disassembling the turbine engine to define a
drainage port in the turbine engine, wherein the cleaning
solution is drained from the turbine engine through the
drainage port.
[0011] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, the method further in-
cludes discharging a flow of rinsing solution towards the
interior passageway from the access point.
[0012] In another aspect, a method of cleaning a com-
ponent within a turbine engine is provided. The method
includes disassembling the turbine engine to provide a
flow path to an interior passageway of the component
from an access point, wherein the component has coked
hydrocarbons formed thereon, and filling a volume of the
interior passageway with an amount of cleaning solution.
The cleaning solution is configured to remove the coked
hydrocarbons from the component. The method further
includes holding the amount of cleaning solution within
the interior passageway for a predetermined residence
time.
[0013] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, disassembling the tur-
bine engine includes disassembling a fan assembly of
the turbine engine to define a first open end of a fan mid-
1 2
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shaft of the turbine engine, wherein the first open end
defines the access point.
[0014] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, the fan midshaft in-
cludes a second open end, and the method further in-
cludes sealing the second open end prior to discharging
the flow of cleaningsolution towards theinterior passage-
way.
[0015] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, sealing the second
open end includes positioning a plug within the interior
passageway of the component proximate the second
open end, wherein the plug is insertable through the first
open end of the fan midshaft when in a first operational
mode, and actuating the plug into a second operational
mode from the first operational mode, wherein the plug
is configured to seal the second open end when in the
second operational mode.
[0016] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, filling a volume of the
interior passageway includes filling the volume with the
cleaning solution including a foaming agent.
[0017] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, holding the amount of
cleaning solution comprises holding the amount of clean-
ing solution for the predetermined residence time defined
within a range between about 30 minutes and about 8
hours.
[0018] In yet another aspect, a method of cleaning a
component withina turbineengineis provided. The meth-
od includes disassembling the turbine engine to define
an access point to the component. The component has
coked hydrocarbons formed thereon. The method further
includes discharging a flow of cleaning solution towards
the component from the access point, wherein the clean-
ing solution is configured to remove the coked hydrocar-
bons from the component, and wherein the cleaning so-
lution includes at least one of citric acid or glycolic acid.
[0019] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, disassembling the tur-
bine engine includes disassembling the turbine engine
when the turbine engine is coupled to an airframe.
[0020] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, disassembling the tur-
bine engine includes disassembling the turbine engine
to provide access to a fuel nozzle of the turbine engine.
[0021] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, discharging a flow of
cleaning solution includes discharging the flow of clean-
ing solution that further includes a foaming agent.
[0022] In one aspect, which may include at least a por-
tion of the subject matter of any of the preceding and/or
following examples and aspects, the method further in-
cludes disassembling a fuel manifold to define an inlet
port within the fuel manifold, wherein the inlet port defines
the access point, and discharging the flow of cleaning
solution through the inlet port and towards the compo-
nent.
DRAWINGS
[0023] These and other features, aspects, and advan-
tages of the present disclosure will become better under-
stood when the following detailed description is read with
reference to the accompanying drawings in which like
characters represent like parts throughout the drawings,
wherein:
FIG. 1 is a schematic illustration of an exemplary
turbine engine;
FIG. 2 is a schematic illustration of an exemplary
fluid delivery system that may be used to clean the
turbine engine shown in FIG. 1;
FIG. 3 is a box diagram illustrating the fluid delivery
system shown in FIG. 2 providing fluid to a compo-
nent of the turbine engine shown in FIG. 1 from an
exemplary access point;
FIG. 4 is a box diagram illustrating the fluid delivery
system shown in FIG. 2 providing fluid to the com-
ponent of the turbine engine shown in FIG. 1 from
an alternative access point;
FIG. 5 is a box diagram illustrating the fluid delivery
system shown in FIG. 2 providing fluid to an alterna-
tive component of the turbine engine shown in FIG.
1 from an exemplary access point;
FIG. 6 is a schematic illustration of an exemplary
sealing and discharge assembly in a first operational
mode that may be used when delivering fluid to the
component shown in FIG. 5;
FIG. 7 is a schematic illustration of the sealing and
discharge assembly shown in FIG. 6 in a second
operational mode;
FIG. 8 is a flow diagram illustrating an exemplary
method of cleaning a component within a turbine en-
gine, in accordance with a first embodiment of the
disclosure;
FIG. 9 is a flow diagram illustrating an exemplary
method of cleaning a component within a turbine en-
gine, in accordance with a second embodiment of
the disclosure; and
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FIG. 10 is a flow diagram illustrating an exemplary
method of cleaning a component within a turbine en-
gine, in accordance with a third embodiment of the
disclosure.
[0024] Unless otherwise indicated, the drawings pro-
vided herein are meant to illustrate features of embodi-
ments of the disclosure. These features are believed to
be applicable in a wide variety of systems comprising
one or more embodiments of the disclosure. As such,
the drawings are not meant to include all conventional
features known by those of ordinary skill in the art to be
required for the practice of the embodiments disclosed
herein.
DETAILED DESCRIPTION
[0025] In the following specification and the claims, ref-
erence will be made to a number of terms, which shall
be defined to have the following meanings.
[0026] The singular forms "a", "an", and "the" include
plural references unless the context clearly dictates oth-
erwise.
[0027] "Optional" or "optionally" means that the sub-
sequently described event or circumstance may or may
not occur, and that the description includes instances
where the event occurs and instances where it does not.
[0028] Approximating language, as used herein
throughout the specification and claims, may be applied
to modify any quantitative representation that could per-
missibly vary without resulting in a change in the basic
function to which it is related. Accordingly, a value mod-
ified bya term or terms, such as "about", "approximately",
and "substantially", are not to be limited to the precise
value specified. In at least some instances, the approx-
imating language may correspond to the precision of an
instrument for measuring the value. Here and throughout
the specification and claims, range limitations may be
combined and/or interchanged. Such ranges are identi-
fied and include all the sub-ranges contained therein un-
less context or language indicates otherwise.
[0029] As used herein, the terms "axial" and "axially"
refer to directions and orientations that extend substan-
tially parallel to a centerline of the turbine engine. More-
over, the terms "radial" and "radially" refer to directions
and orientations that extend substantially perpendicular
to the centerline of the turbine engine. In addition, as
used herein, the terms "circumferential" and "circumfer-
entially" refer to directions and orientations that extend
arcuately about the centerline of the turbine engine.
[0030] Embodiments of the present disclosure relate
to cleaning cokedhydrocarbons from a component within
a turbine engine. More specifically, the systems and
methods described herein facilitate cleaning the turbine
engine without, for example, having to detach the turbine
engine from the airframe, and without having to remove
the component to be cleaned from the turbine engine. In
contrast, the systems and methods described herein pro-
vide a cleaning solution to the turbine engine via an ac-
cess point, which is defined by disassembling a portion
of the turbine engine while still coupled to the airframe.
For example, in one embodiment, fuel nozzles of the tur-
bine engine have coked hydrocarbons formed thereon,
and the turbine engine is disassembled such that clean-
ing fluid may be provided to the fuel nozzles from a single
access point. As such, the time and effort for disassem-
bling and cleaning components of the turbine engine are
reduced, thereby reducing the amount of time for return-
ing a refurbished turbine engine to service.
[0031] While the following embodiments are described
in the context of a turbofan engine, it should be under-
stood that the systems and methods described herein
are also applicable to turboprop engines, turboshaft en-
gines, turbojet engines, and ground-based turbine en-
gines, for example.
[0032] FIG. 1 is a schematic diagram of an exemplary
turbine engine 10 coupled to an airframe 11. Turbine en-
gine 10 includes a fan assembly 12, a low-pressure or
booster compressor assembly 14, a high-pressure com-
pressor assembly16, and a combustor assembly18. Fan
assembly 12, booster compressor assembly 14, high-
pressure compressor assembly 16, and combustor as-
sembly 18 are coupled in flow communication. Turbine
engine 10 also includes a high-pressure turbine assem-
bly 20 coupled in flow communication with combustor
assembly 18 and a low-pressure turbine assembly 22.
Fan assembly 12 includes an array of fan blades 24 ex-
tending radially outward from a rotor disk 26. Low-pres-
sure turbine assembly 22 is coupled to fan assembly 12
andbooster compressor assembly14throughafirst drive
shaft 28, and high-pressure turbine assembly 20 is cou-
pled to high-pressure compressor assembly 16 through
a second drive shaft 30. Turbine engine 10 has an intake
32 and an exhaust 34. Turbine engine 10 further includes
a centerline 36 about which fan assembly 12, booster
compressor assembly 14, high-pressure compressor as-
sembly 16, and turbine assemblies 20 and 22 rotate.
[0033] In operation, air entering turbine engine 10
through intake 32 is channeled through fan assembly 12
towards booster compressor assembly 14. Compressed
air is discharged from booster compressor assembly 14
towards high-pressure compressor assembly 16. Highly
compressed air is channeled from high-pressure com-
pressor assembly 16 towards combustor assembly 18,
mixedwith fuel, andthe mixture iscombustedwithin com-
bustor assembly 18. High temperature combustion gas
generated by combustor assembly 18 is channeled to-
wards turbine assemblies 20 and 22. Combustion gas is
subsequently discharged from turbine engine 10 via ex-
haust 34.
[0034] FIG. 2 is a schematic illustration of an exempla-
ry fluid delivery system 100 that may be used to clean
turbine engine 10 (shown in FIG. 1). In the exemplary
embodiment, fluid delivery system 100 is embodied as a
mobile flight line cart including a plurality of components
that, when used in combination, facilitate providing a flow
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of cleaning solution to turbine engine 10. Fluid delivery
system 100 includes a cleaning tank 102 that stores the
cleaning solution therein, and a rinse tank 104 that stores
a rinsing solution therein, such as deionized water.
Cleaning tank 102 includes a heater 106 positioned
therein for heating the cleaning solution to a predeter-
mined temperature. Heater 106 facilitates heating the
cleaning solution to any temperature that enables the
systems and methods to function as described herein.
In one embodiment, heater 106 heats the cleaning solu-
tion to a temperature defined within a range between
about 30°C and about 95°C before being discharged to-
wards turbine engine 10.
[0035] Cleaning tank 102 and rinse tank 104 are cou-
pled in flow communication with a first valve assembly
108 that is selectively operable to provide either the
cleaning solution or the rinsing solution to turbine engine
10. More specifically, fluid delivery system 100 includes
a first pump 110 coupled in flow communication with first
valve assembly 108. First pump 110 discharges either
the cleaning solution or the rinsing solution towards a
second valve assembly 112, which is selectively opera-
ble to discharge the selected solution towards turbine
engine 10 via a discharge line 114. In some embodi-
ments, fluid delivery system 100 includes a compressor
116 coupled in flow communication with discharge line
114, and compressor 116 is selectively operable to facil-
itate providing purge air through discharge line 114 when
draining solution from turbine engine 10. Fluid delivery
system 100 also includes an accumulator 118 coupled
between first pump 110 and second valve assembly 112.
Accumulator 118 modulates the flow pulses discharged
from first pump 110 to provide a steady flow to second
valve assembly 112.
[0036] In one embodiment, fluid delivery system 100
further includes a receiving line 120 coupled in flow com-
munication with turbine engine 10. As will be explained
in more detail below, receiving line 120 receives fluid that
has been channeled towards turbine engine 10 through
discharge line 114, circulated through turbine engine 10,
and subsequently drained from turbine engine 10. In the
exemplary embodiment, fluid delivery system 100 in-
cludes a second pump 122 coupled in flow communica-
tion with receiving line 120. When used cleaning solution
is channeled through receiving line 120, second pump
122 induces flow of the used cleaning solution from tur-
bineengine 10 and discharges theusedcleaningsolution
towards a filter 124. In some embodiments, filter 124 re-
moves contaminants from the used cleaning solution,
thereby forming reconditioned cleaning solution, which
is then discharged into cleaning tank 102 for further use.
[0037] Fluid deliverysystem 100 may use any cleaning
solution to clean turbine engine 10 that enables the sys-
tems and methods to function as described herein. In the
exemplary embodiment, the cleaning solution is formed
a cleaning detergent and water. In one embodiment, the
cleaning solution includes cleaning detergent of up to
about 20 percent byweight of thecomposition. Moreover,
thecleaningsolutionincludesanycleaningdetergentthat
enables the systems and methods to function as de-
scribed herein. In one embodiment, the cleaning deter-
gent is generally effective at degreasing and decoking,
and contains an organic and alkaline solution of up to
about 20 percent by weight of the detergent. In some
embodiments, the organic and alkaline solution includes
alkyl and aromatic amines, non-ionic, anionic, and cati-
onic surfactants, and either a polycyclic aromatic hydro-
carbon or di-propylene glycol methyl ether.
[0038] In an alternative embodiment, the cleaning so-
lution includes at least one of citric acid or glycolic acid.
An example cleaning solution that includes at least one
of citric acid or glycolic acid includes, but is not limited
to, Citranox® ("Citranox" is a registered trademark of Al-
conox, Inc., of White Plains, NY). In some embodiments,
the cleaning solution also includes at least one of a foam-
ing agent, surfactants, or other suitable additives. In a
further alternative embodiment, the cleaning solution in-
cludes an organic solvent, such as a Turco® 8226 clean-
ing solution.
[0039] FIGS. 3-5 are box diagrams illustrating fluid de-
livery system 100 (shown in FIG. 2) providing solution to
a component of turbine engine 10 from an access point.
Intheexemplaryembodiment, turbineengine10 includes
a fuel supply system 126 including a component 127,
such as at least one fuel nozzle 128. Fuel supply system
126 also includes a fuel circuit 130, a split control unit
(SCU) 132 coupled in selective flow communication with
fuel circuit 130, and a fuel manifold 134 coupled in flow
communication SCU 132. In operation, fuel is channeled
towards fuel nozzle 128 from fuel circuit 130, through
SCU 132, through fuel manifold 134, and towards an in-
terior passageway 136 of fuel nozzle 128. As noted
above, coked hydrocarbons sometimes form on a com-
ponent within turbine engine 10 after prolonged use. In
the exemplary embodiment, the component is a compo-
nent of fuel supply system 126 or a fan midshaft, as will
be described in more detail below.
[0040] Referring to FIG. 3, a method of cleaning a com-
ponent, such as fuel nozzle 128, within turbine engine
10 is described herein. In the exemplary embodiment,
fuel nozzle 128 has coked hydrocarbons formed thereon,
such as within interior passageway 136 or on an outer
surface of fuel nozzle 128. The method includes disas-
sembling a first portion of turbine engine 10 to provide a
flow path 137 to interior passageway 136 of fuel nozzle
128 from an access point 138. More specifically, fuel
manifold 134 is disassembled by disconnecting SCU 132
from fuel manifold 134 to define inlet port 140 and access
point 138 at fuel manifold 134. A flow of cleaning solution
isthendischargedtowardsinterior passageway 136 from
access point 138, where the cleaning solution is config-
ured to remove the coked hydrocarbons from fuel nozzle
128. For example, in the exemplary embodiment, dis-
charge line 114 of fluid delivery system 100 (shown in
FIG. 2) is connected to fuel manifold 134 at inlet port 140,
and fluid delivery system 100 is actuated to discharge
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cleaning solution towards turbine engine 10.
[0041] Inoneembodiment, theflowof cleaningsolution
is discharged in at least one pulsed interval having a pre-
determined discharge time. For example, the flow of
cleaning solution is discharged in at least a first pulsed
interval and a second pulsed interval, where a predeter-
mined residence time is defined between the first pulsed
interval and the second pulsed interval. Introducing the
cleaning solution into turbine engine 10 in the first pulsed
interval and then allowing a predetermined residence
time to elapse before discharging the second pulsed in-
terval facilitates allowing the cleaning solution of the first
pulsed interval to settle and interact with the coked hy-
drocarbons formed on fuel nozzle 128. The second
pulsed interval is then discharged after the predeter-
mined residence time has elapsed such that the cleaning
solution within turbine engine 10 is refreshed. Alterna-
tively, a flow of rinsing solution is discharged into turbine
engine 10 after the predetermined residence time has
elapsed after the first pulsed interval.
[0042] The predetermined discharge time and the pre-
determined residence time may be of any duration that
enables the systems and methods to function as de-
scribed herein. In one embodiment, the predetermined
discharge time is defined within a range between about
5 seconds and about 120 seconds. In addition, in one
embodiment, the predetermined residence time is de-
fined within a range between about 2 minutes and about
30 minutes.
[0043] In the exemplary embodiment, the flow of clean-
ing solution is channeled through inlet port 140, through
fuel manifold 134, through interior passageway 136 of
fuel nozzle 128, and is then discharged from fuel nozzle
128. The method further includes disassembling a sec-
ond portion of turbine engine 10 to define a drainage port
142 therein. Drainage port 142 is coupled in flow com-
munication with fuel nozzle 128 such that the solution
channeled into turbine engine 10 is drained from turbine
engine 10 through drainage port 142. In one embodi-
ment, drainage port 142 is defined by uninstalling at least
one ignitor plug (not shown) from turbine engine 10,
where the at least one ignitor plug is located at about a
6 o’clock position within turbine engine 10. As such, the
solution is gravity drained from turbine engine 10. More
specifically, the solution is discharged from fuel nozzle
128 and into a combustor dome, is drained through air
holes in the combustor dome into a combustor case, and
is then drained from the combustor case through drain-
age port 142. Moreover, in the exemplary embodiment,
receiving line 120 of fluid delivery system 100 is coupled
to turbine engine 10 at drainage port 142 such that used
cleaning solution is recycled to fluid delivery system 100,
as described above.
[0044] The method further includes discharging a flow
of rinsing solution towards interior passageway 136 of
fuel nozzle 128 from access point 138. More specifically,
fluid delivery system 100 is actuated as described above
to facilitate discharging the flow of rinsing solution
through discharge line 114 rather than the flow of clean-
ing solution. The rinsing solution is then drained through
drainage port 142.
[0045] Referring to FIG. 4, the method includes disas-
sembling a portion of turbine engine 10 to provide direct
access to fuel nozzle 128 having coked hydrocarbons
formed thereon.
[0046] More specifically, turbine engine 10 is disas-
sembled to define an access point 144 at an inlet port
146 of turbine engine 10. For example, inlet port 146 is
defined by uninstalling at least one ignitor plug from tur-
bine engine 10, or by uninstalling a borescope cover from
turbine engine 10. The flow of cleaning solution is then
discharged towards fuel nozzle 128 from access point
144, such that the cleaning solution impinges against an
outer surface 148 of fuel nozzle 128. In some embodi-
ments, the cleaning solution enters fuel nozzle 128
through an opening defined therein such that coked hy-
drocarbons are also removed the interior of fuel nozzle
128.
[0047] Referring to FIG. 5, the method includes disas-
sembling fan assembly 12 of turbine engine 10 to provide
access to component 127 installed therein. For example,
in the exemplary embodiment, fan assembly 12 includes
a fan midshaft 150 and a center body 152 and a center
vent tube 153 coupled to fan midshaft 150. Disassem-
bling fan assembly 12 includes removing center body
152 from fan midshaft 150 to define a first open end 154
in fan midshaft 150, and removing center vent tube 153
from fan midshaft 150 to provide access to an interior of
fan midshaft 150. More specifically, first open end 154
defines an access point 156 to an interior passageway
158 of fan midshaft 150, which has coked hydrocarbons
formed therein. The cleaning solution is then discharged
into interior passageway 158, and a volume of interior
passageway 158 is filled with an amount of cleaning so-
lution in theform of anaeratedfoam. Interior passageway
158 is filled with the amount of cleaning solution for a
predetermined residence time that facilitates allowing the
cleaning solution to interact with the coked hydrocarbons
formed therein, ranging effectively from 30 minutes to 8
hours. The cleaning solution is then drained through first
open end 154 and rinsing solution is discharged into in-
terior passageway 158 followed by mechanical removal
of additional coking products lifted from the fan mid shaft
inner diameter employing an articulating brush com-
prised of nylon.
[0048] FIG. 6 is a schematic illustration of an exempla-
ry sealing and discharge assembly 160 in a first opera-
tional mode that may be used when delivering fluid to fan
midshaft 150, and FIG. 7 is a schematic illustration of
sealing and discharge assembly 160 in a second oper-
ational mode. In the exemplary embodiment, sealing and
discharge assembly 160 includes a discharge shaft 162,
an inflatable plug 164, and a supply line 166 coupled in
flow communication with inflatable plug 164. Discharge
shaft 162 includes a first end 168 and a second end 170.
Inflatable plug 164 is coupled to discharge shaft 162 at
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first end 168, and a sealing cap 172 is coupled to dis-
charge shaft 162 at second end 170.
[0049] Referring to FIG. 7, fan midshaft 150 includes
first open end 154 and a second open end 174. When in
the first operational mode, inflatable plug 164 is deflated
to a size such that sealing and discharge assembly 160
is insertable through first open end 154, and such that
inflatable plug164 is positionablewithin interior passage-
way 158 proximate second open end 174. Referring to
FIG. 7, the inflatable plug 164 is then actuated from the
first operational mode to the second operational mode,
where the inflatable plug 164 seals second open end 174
when in the second operational mode. More specifically,
fluid is supplied to inflatable plug 164 via supply line 166
to inflate inflatable plug 164 to a size that facilitates seal-
ingsecondopenend174. Secondopenend174issealed
prior to discharging the flow of cleaning solution towards
interior passageway 158.
[0050] When sealing and discharge assembly 160 is
fully inserted within interior passageway 158, sealing cap
172 couples to fan midshaft 150 with an interference fit
to facilitate sealing first open end 154. Discharge shaft
162 is coupled in flow communication with discharge line
114 (shown in FIG. 2), for example, and includes at least
one discharge outlet 176 defined therein. As such, when
sealed, interior passageway 158 is provided with clean-
ing solution discharged from discharge outlet 176 to fa-
cilitate removing coked hydrocarbons formed therein.
[0051] In one embodiment, a volume of interior pas-
sageway 158 is filled with an amount of the cleaning so-
lution, and the amount of cleaning solution is held within
interior passageway 158 for a predetermined residence
time. The predetermined residence time is defined within
a range between about 30 minutes and about 8 hours.
In some embodiments, the cleaning solution includes a
foaming agent, which facilitates filling the volume of in-
terior passageway 158 and enabling the cleaning solu-
tion to interact with coked hydrocarbons on the surface
of fan midshaft 150 without being directly applied thereto.
[0052] After the predetermined residence time has
elapsed, interior passageway 158 is drained through at
least one of first open end 154 and second open end
174. In some embodiments, the method includes suc-
tioning the cleaning solution from interior passageway
158. Moreover, in the exemplary embodiment, fan mid-
shaft 150 includes at least one annular member 178 po-
sitioned within interior passageway 158. When draining
solution from interior passageway 136, the solution may
pool in a space defined between adjacent annular mem-
bers 178. As such, in one embodiment, suctioning solu-
tion from interior passageway 158 includes providing a
directed suction force to the space defined between ad-
jacentannularmembers178 tofacilitateremovingpooled
solution from interior passageway 158. Fan midshaft 150
is then cleaned mechanically and rinsed, or a second
application of cleaning solution is provided.
[0053] FIGS. 8-10 are flow diagrams illustrating exem-
plary methods of cleaning a component within turbine
engine 10. Referring to FIG. 8, a method 200 includes
disassembling 202 turbine engine 10 to provide a flow
path 137 to interior passageway 136 of component 127
from access point 138 in turbine engine 10. Component
127 has coked hydrocarbons formed thereon. Method
200 further includes discharging 204 a flow of cleaning
solution towards interior passageway 136 from access
point 138. The cleaning solution is configured to remove
the coked hydrocarbons from component 127.
[0054] Referring to FIG. 9, a method 206 includes dis-
assembling 208 turbine engine 10 to provide a flow path
to interior passageway 158 of component 127 from ac-
cess point 156 in turbine engine 10. Component 127 has
coked hydrocarbons formed thereon. Method 206 further
includes filling 210 a volume of interior passageway 158
with an amount of cleaning solution, wherein the cleaning
solution is configured to remove the coked hydrocarbon
from the component, and holding 212 the amount of
cleaning solution within interior passageway 158 for a
predetermined residence time.
[0055] Referring to FIG. 10, a method 214 includes dis-
assembling 216 turbine engine 10 to define access point
144 to component 127. Component 127 has coked hy-
drocarbons formed thereon. Method 214 further includes
discharging 218 a flow of cleaning solution towards com-
ponent 127 from access point 144. The cleaning solution
is configured to remove the coked hydrocarbons from
component 127, and the cleaning solution includes at
least one of citric acid or glycolic acid.
[0056] An exemplary technical effect of the assembly
and methods described herein includes at least one of:
(a) cleaning internal components of a turbine engine
while coupled to an airframe; (b) cleaning internal com-
ponents of theturbine engine in aquick and efficient man-
ner; and (c) reducing an amount of time for cleaning and
returning a cleaned turbine engine to service.
[0057] Exemplary embodiments of a cleaning system
for use with a turbine engine and related components are
described above in detail. The system is not limited to
the specific embodiments described herein, but rather,
components of systems and/or steps of the methods may
be utilized independently and separately from other com-
ponents and/or steps described herein. For example, the
configuration of components described herein may also
be used in combination with other processes, and is not
limited to practice with a fuel nozzles or a fan section of
a turbine engine. Rather, the exemplary embodiment can
be implemented and utilized in connection with many ap-
plications where removing coked hydrocarbons from an
object is desired.
[0058] Although specific features of various embodi-
ments of the present disclosure may be shown in some
drawings and not in others, this is for convenience only.
In accordance with the principles of embodiments of the
present disclosure, any feature of a drawing may be ref-
erenced and/or claimed in combination with any feature
of any other drawing.
[0059] This written description uses examples to dis-
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close the embodiments of the present disclosure, includ-
ing the best mode, and also to enable any person skilled
in the art to practice embodiments of the present disclo-
sure, including making and using any devices or systems
and performing any incorporated methods. The patent-
able scope of the embodiments described herein is de-
fined by the claims, and may include other examples that
occur to those skilled in the art. Such other examples are
intended to be within the scope of the claims if they have
structural elements that do not differ from the literal lan-
guage of the claims, or if they include equivalent struc-
tural elements with insubstantial differences from the lit-
eral languages of the claims.
[0060] Various aspects and embodiments of the
present invention are defined by the following numbered
clauses:
1. A method of cleaning a component within a turbine
engine, said method comprising:
disassembling the turbine engine to provide a
flow path to an interior passageway of the com-
ponent from an access point in the turbine en-
gine, wherein the component has coked hydro-
carbons formed thereon; and
discharging a flow of cleaning solution towards
the interior passageway from the access point,
wherein the cleaning solution is configured to
remove the coked hydrocarbons from the com-
ponent.
2. The method in accordance with clause 1, wherein
disassembling the turbine engine comprises disas-
sembling the turbine engine when the turbine engine
is coupled to an airframe.
3. The method in accordance with any preceding
clause, wherein disassembling the turbine engine
comprises disassembling a fuel manifold to define
an inlet port within the fuel manifold, wherein the inlet
port defines the access point.
4. The method in accordance with any preceding
clause, wherein discharging a flow of cleaning solu-
tion comprises discharging the flow of cleaning so-
lution towards the interior passageway in a pulsed
interval having a discharge time defined within a
range between about 5 seconds and about 120 sec-
onds.
5. The method in accordance with any preceding
clause, wherein discharging a flow of cleaning solu-
tion comprises discharging the flow of cleaning so-
lution towards the interior passageway in at least a
first pulsed interval and a second pulsed interval,
wherein a residence time is defined between the first
pulsed interval and the second pulsed interval.
6. The method in accordance with any preceding
clause, further comprising defining the residence
time within a range between about 2 minutes and
about 30 minutes.
7. The method in accordance with any preceding
clause, wherein discharging a flow of cleaning solu-
tioncomprisesheatingthecleaningsolutiontoatem-
perature defined within a range between about 30°C
and 95°C.
8. The method in accordance with any preceding
clause, further comprising disassembling the turbine
enginetodefine adrainageport in theturbineengine,
wherein the cleaning solution is drained from the tur-
bine engine through the drainage port.
9. The method in accordance with any preceding
clause, further comprising discharging a flow of rins-
ing solution towards the interior passageway from
the access point.
10. A method of cleaning a component within a tur-
bine engine, said method comprising:
disassembling the turbine engine to provide a
flow path to an interior passageway of the com-
ponent from an access point in the turbine en-
gine, wherein the component has coked hydro-
carbons formed thereon;
filling a volume of the interior passageway with
an amount of cleaning solution, wherein the
cleaning solution is configured to remove the
coked hydrocarbons from the component; and
holding the amount of cleaning solution within
the interior passageway for a predetermined
residence time.
11. The method in accordance with any preceding
clause, wherein disassembling the turbine engine
comprises disassembling a fan assembly of the tur-
bine engine to define a first open end of a fan mid-
shaft of the turbine engine, wherein the first open
end defines the access point.
12. The method in accordance with any preceding
clause, wherein the fan midshaft includes a second
open end, said method further comprising sealing
the second open end prior to discharging the flow of
cleaning solution towards the interior passageway.
13. The method in accordance with any preceding
clause, wherein sealing the second open end com-
prises:
positioning aplugwithintheinterior passageway
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of the component proximate the second open
end, wherein the plug is insertable through the
first open end of the fan midshaft when in a first
operational mode; and
actuating the plug into a second operational
mode from the first operational mode, wherein
the plug is configured to seal the second open
end when in the second operational mode.
14. The method in accordance with any preceding
clause, wherein filling a volume of the interior pas-
sageway comprises filling the volume with the clean-
ing solution including a foaming agent.
15. The method in accordance with any preceding
clause, wherein holding the amount of cleaning so-
lution comprises holding the amount of cleaning so-
lution for the predetermined residence time defined
within a range between about 30 minutes and about
8 hours.
16. A method of cleaning a component within a tur-
bine engine, said method comprising:
disassembling the turbine engine to define an
access point to the component, wherein the
component has coked hydrocarbons formed
thereon; and
discharging a flow of cleaning solution towards
the component from the access point, wherein
the cleaning solution is configured to remove the
coked hydrocarbons from the component, and
wherein the cleaning solution includes at least
one of citric acid or glycolic acid.
17. The method in accordance with any preceding
clause, wherein disassembling the turbine engine
comprises disassembling the turbine engine when
the turbine engine is coupled to an airframe.
18. The method in accordance with any preceding
clause, wherein disassembling the turbine engine
comprises disassembling the turbine engine to pro-
vide access to a fuel nozzle of the turbine engine.
19. The method in accordance with any preceding
clause, wherein discharging a flow of cleaning solu-
tion comprises discharging the flow of cleaning so-
lution that further includes a foaming agent.
20. The method in accordance with any preceding
clause, further comprising:
disassembling a fuel manifold to define an inlet
port within the fuel manifold, wherein the inlet
port defines the access point; and
discharging the flow of cleaning solution through
the inlet port and towards the component.
Claims
1. A method of cleaning a component (127) within a
turbine engine (10), said method comprising:
disassembling the turbineengine (10) to provide
aflowpath(137) toaninterior passageway (136)
of the component (127) from an access point
(138) in the turbine engine (10), wherein the
component (127) has coked hydrocarbons
formed thereon; and
discharging a flow of cleaning solution towards
the interior passageway (136) from the access
point (138), wherein the cleaning solution is con-
figured to remove the coked hydrocarbons from
the component (127).
2. The method in accordance with claim 1, wherein dis-
assembling the turbine engine (10) comprises dis-
assembling the turbine engine (10) when the turbine
engine (10) is coupled to an airframe (11).
3. The method in accordance with either of claim 1 or
2, wherein disassembling the turbine engine (10)
comprises disassembling a fuel manifold(134) to de-
fine an inlet port (140) within the fuel manifold (134),
wherein the inlet port (140) defines the access point
(138).
4. The method in accordance with any preceding claim,
wherein discharging a flow of cleaning solution com-
prises discharging the flow of cleaning solution to-
wards the interior passageway (136) in a pulsed in-
terval having a discharge time defined within a range
between about 5 seconds and about 120 seconds.
5. The method in accordance with any preceding claim,
wherein discharging a flow of cleaning solution com-
prises discharging the flow of cleaning solution to-
wards the interior passageway (136) in at least a first
pulsedinterval andasecondpulsedinterval, wherein
a residence time is defined between the first pulsed
interval and the second pulsed interval.
6. The method in accordance with claim 5, further com-
prising defining the residence time within a range
between about 2 minutes and about 30 minutes.
7. The method in accordance with any preceding claim,
wherein discharging a flow of cleaning solution com-
prises heating the cleaning solution to a temperature
defined within a range between about 30°C and
95°C.
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10. EP 3 396 116 A2
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5
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20
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30
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45
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8. The method in accordance with any preceding claim,
further comprising disassembling the turbine engine
(10) to define a drainage port in the turbine engine
(10), wherein the cleaning solution is drained from
the turbine engine (10) through the drainage port.
9. The method in accordance with any preceding claim,
further comprising discharging a flow of rinsing so-
lution towards the interior passageway (136) from
the access point.
10. A method of cleaning a component (127) within a
turbine engine (10), said method comprising:
disassembling the turbine engine (10) to provide
a flow path to an interior passageway (158) of
the component (127) from an access point (156)
in the turbine engine (10), wherein the compo-
nent (127) hascokedhydrocarbonsformedther-
eon;
filling a volume of the interior passageway (158)
with an amount of cleaning solution, wherein the
cleaning solution is configured to remove the
coked hydrocarbons from the component (127);
and
holding the amount of cleaning solution within
the interior passageway (158) for a predeter-
mined residence time.
11. The method in accordance with claim 10, wherein
disassembling the turbine engine (10) comprises
disassembling a fan assembly (12) of the turbine en-
gine (10) to define a first open end (154) of a fan
midshaft (150) of the turbine engine (10), wherein
the first open end (154) defines the access point
(156).
12. The method in accordance with claim 11, wherein
the fan midshaft (150) includes a second open end
(174), said method further comprising sealing the
second open end (174) prior to discharging the flow
of cleaning solution towards the interior passageway
(158).
13. The method in accordance with claim 12, wherein
sealing the second open end (174) comprises:
positioning an inflatable plug (164) within the in-
terior passageway (158) of the component (127)
proximate the second open end (174), wherein
the inflatable plug (164) is insertable through the
first open end (154) of the fan midshaft (150)
when in a first operational mode; and
actuating the inflatable plug (164) into a second
operational mode from the first operational
mode, wherein the inflatable plug (164) is con-
figured to seal the second open end (174) when
in the second operational mode.
14. The method in accordance with any of claims 10 to
13, wherein filling a volume of the interior passage-
way (158) comprises filling the volume with the
cleaning solution including a foaming agent.
15. A method of cleaning a component (127) within a
turbine engine (10), said method comprising:
disassembling the turbine engine (10) to define
an access point (138, 144) to the component
(127), wherein the component (127) has coked
hydrocarbons formed thereon; and
discharging a flow of cleaning solution towards
thecomponent (127) from the accesspoint (138,
144), whereinthecleaningsolutionisconfigured
to remove the coked hydrocarbons from the
component (127), and wherein the cleaning so-
lution includes at least one of citric acid or gly-
colic acid.
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