This document discusses options for developing an oleoresin extraction pilot plant in Pakistan. It analyzes extraction technologies, raw material availability, budgets, and provides specifications for 6 potential pilot plant systems. The top options are a 100L German system for $106,800, a 200L Chinese system for $35,000, and an Italian 50L system for $91,466. These pilot plants would help customize an appropriate size commercial plant to manufacture oleoresin using local chili varieties and current extraction technologies.
The document outlines the scope of work for hiring a third party inspector to evaluate and inspect two solvent extraction units in China prior to shipping. Key deliverables for the inspector include verifying that the units and all components meet specifications for materials, design parameters, quality controls and other standards outlined in referenced documents. The inspector will validate specifications for items like vessel volumes, motor specifications, filtration mesh sizes, and that all parts are made of food-grade stainless steel.
Air / Steam Regeneration Procedure for Primary Reforming CcatalystGerard B. Hawkins
GBH Enterprises specializes in refinery process catalysts, including performance evaluation, analysis, and development of new technologies. The document provides procedures for air/steam regeneration of primary reforming catalysts either during shutdown or startup. During shutdown, steaming should continue for two hours before introducing a small amount of air to burn off carbon deposits, monitored by CO2 levels. During startup, normal heating with steam is followed by the same air regeneration process once temperatures reach 1300-1325°F, before removing air and resuming steam for two hours prior to introducing feed gas.
GBH Enterprises specializes in catalyst and process technology for refining, gas processing, and petrochemical industries. They provide catalyst performance evaluation, heat and mass balance analysis, and commercialization of new technologies. The document describes two case studies of olefin hydrogenation using Vulcan catalysts. Both cases require a recycle stream to control exotherms. The results show the reactor sizing and operating parameters needed to meet a 5-year minimum catalyst life for both cases.
This document is a curriculum vitae for Suresh Kumar Muthuramalingam. It includes his contact information, career objective, qualifications, and professional experience. His career objective is to get a challenging opportunity in the petrochemical industry, leveraging his 7+ years of experience in control room and field operations, erection, and commissioning. He has over 6 years of experience in production, maintenance, process control, quality, and safety at petrochemical, chemical, and gas plants. Currently he works as a panel and process plant operator at Al-kout Industrial Projects in Abu Dhabi, UAE. His qualifications include a diploma in petrochemical engineering and professional experience includes roles as a
Rashid Jalal has over 8 years of experience as an oil and gas process operator. He has a diploma in petroleum engineering and has worked in facilities in Pakistan and Abu Dhabi operating units like crude oil processing, gas treatment, and compression. He is proficient in DCS and other control systems and responsible for monitoring operations, maintenance, and safety.
The document outlines the scope of work for hiring a third party inspector to evaluate and inspect two solvent extraction units in China prior to shipping. Key deliverables for the inspector include verifying that the units and all components meet specifications for materials, design parameters, quality controls and other standards outlined in referenced documents. The inspector will validate specifications for items like vessel volumes, motor specifications, filtration mesh sizes, and that all parts are made of food-grade stainless steel.
Air / Steam Regeneration Procedure for Primary Reforming CcatalystGerard B. Hawkins
GBH Enterprises specializes in refinery process catalysts, including performance evaluation, analysis, and development of new technologies. The document provides procedures for air/steam regeneration of primary reforming catalysts either during shutdown or startup. During shutdown, steaming should continue for two hours before introducing a small amount of air to burn off carbon deposits, monitored by CO2 levels. During startup, normal heating with steam is followed by the same air regeneration process once temperatures reach 1300-1325°F, before removing air and resuming steam for two hours prior to introducing feed gas.
GBH Enterprises specializes in catalyst and process technology for refining, gas processing, and petrochemical industries. They provide catalyst performance evaluation, heat and mass balance analysis, and commercialization of new technologies. The document describes two case studies of olefin hydrogenation using Vulcan catalysts. Both cases require a recycle stream to control exotherms. The results show the reactor sizing and operating parameters needed to meet a 5-year minimum catalyst life for both cases.
This document is a curriculum vitae for Suresh Kumar Muthuramalingam. It includes his contact information, career objective, qualifications, and professional experience. His career objective is to get a challenging opportunity in the petrochemical industry, leveraging his 7+ years of experience in control room and field operations, erection, and commissioning. He has over 6 years of experience in production, maintenance, process control, quality, and safety at petrochemical, chemical, and gas plants. Currently he works as a panel and process plant operator at Al-kout Industrial Projects in Abu Dhabi, UAE. His qualifications include a diploma in petrochemical engineering and professional experience includes roles as a
Rashid Jalal has over 8 years of experience as an oil and gas process operator. He has a diploma in petroleum engineering and has worked in facilities in Pakistan and Abu Dhabi operating units like crude oil processing, gas treatment, and compression. He is proficient in DCS and other control systems and responsible for monitoring operations, maintenance, and safety.
Critical Variables in Catalytic Reforming and Unit Monitoring Best PracticesGerard B. Hawkins
This document discusses optimization strategies for catalytic reforming processes in oil refineries. It outlines best practices for identifying and monitoring critical variables, and provides examples of critical variables like catalyst activity and recycle gas composition. The document also discusses principles of reformer optimization like defining objectives, layered management practices, and optimizing operations. Overall it provides guidance on monitoring performance, catalyst management, and using online optimization to improve profitability of refinery catalytic reforming units.
Revamp objectives
Revamp Philosophy
Revamp options
Semi-Regenerative Reforming Unit
Typical Flow Scheme
Continuous Reforming Unit
Typical Flow Scheme
Revamp to Hybrid Operation
What may be achieved?
Typical C5+ Yield at Decreasing Pressure
Changes Required for Full Conversion
Typical Benefits of Full Conversion
Revamping of Existing Continuous Reforming Units
Fired Heaters Revamp
Burners
Reactor Options
Regeneration Section
Summary
This document provides guidance for conducting a pre-commissioning safety review of a process or plant (Hazard Study 5). The purpose is to check that the detailed implementation meets requirements before start-up. A cross-functional team inspects arrangements for employee health, safety, and environmental protection. The commissioning manager coordinates inspection of all areas, using a checklist to ensure all factors are considered. Any outstanding actions must be closed or scheduled before start-up. The review verifies the project complies with standards and is ready to safely commence operations.
Mechanical Constraints on Thermal Design of Shell and Tube ExchangersGerard B. Hawkins
Mechanical Constraints on Thermal Design of Shell and Tube Exchangers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 STANDARD DIMENSIONS
4.1 Shell Diameters
4.2 Tube Lengths
4.3 Tube Diameters
4.4 Tube Wall Thicknesses
5 CLEARANCES
5.1 Tube Pitch
5.2 Pass Partition Lane Widths
5.3 Minimum 'U' Bend Clearance
5.4 Tube-to-Baffle Clearance
5.5 Baffle-to-Shell Clearance
5.6 Bundle-to-Shell Clearance
6 TUBESHEET THICKNESS
7 END ZONE LENGTHS
8 TUBE COUNTS
8.1 Program Correlations
8.2 Use of Tube count Tables
8.3 Graphical Layout
8.4 Use of Computer Programs
8.5 Tie Rods
TABLES
1 HEAT EXCHANGER SHELLS - GEOMETRICAL DATA
FOR INLET & OUTLET BRANCHES: PIPE WITH ANSI
150 FLANGE
2 HEAT EXCHANGER SHELLS - GEOMETRICAL DATA
FOR INLET & OUTLET BRANCHES: PIPE WITH ANSI
300 FLANGE
3 TEMA TIE ROD STANDARDS
FIGURES
1 DEFINITION OF TUBE PITCH, LIGAMENT THICKNESS & PASS PARTITION LANE WIDTH
2 DEFINITION OF PASS PARTITION LANE WIDTH FOR U-TUBES
3 BUNDLE TO SHELL CLEARANCES FOR DIFFERENT BUNDLE TYPES
4 ESTIMATED TUBESHEET THICKNESS FOR FIXED TUBE CONSTRUCTION
5 ESTIMATED TUBESHEET THICKNESS FOR U-TUBE CONSTRUCTION
6 END ZONE
7 EXAMPLE OF OPTU3 GRAPHICAL OUTPUT
A.B.RAJESWARA RAO has over 18 years of experience in refinery operations including as a shift supervisor. He has a post-graduate degree in oil and gas and lives in the Kingdom of Bahrain. Currently he works as a shift supervisor at BAPCO, overseeing units like hydrotreating and distillation. Previously he has worked for companies in Abu Dhabi, India, and has experience in commissioning, pre-commissioning, process safety, and operating control systems. He seeks to use his expertise gained over many years to benefit oil and gas operations.
This document describes the responsibilities of an operator for a plant that produces sulfuric acid. The plant uses a furnace to produce steam from sulfur dioxide off-gas and sends the gas through an electrostatic precipitator and induced draft fan to a sulfuric acid plant. The operator monitors plant parameters through a distributed control system, takes corrective actions when needed, and ensures safe startup and shutdown following standard operating procedures.
Berlie Technologies Inc. is a sludge treatment specialist located in LaPrairie, Quebec near the US border. It has 85 employees including engineers, technicians, and field crew. The company has annual sales of $25 million and certifications in pressure equipment, sanitary fabrication, and boiler and pressure vessel inspection. Berlie specializes in the design of sludge digestion and dewatering systems using various technologies like high performance digesters, drying systems, belt filter presses, and more. It has reference projects across Europe, the Middle East, and North America for municipal and industrial wastewater and sludge treatment.
Pratik Parmar is seeking assignments in operations and maintenance, commissioning, and project management of boilers and turbines up to 500 TPH and 120 MW. He has 6 years of experience in operations and maintenance of boilers and turbines, troubleshooting, commissioning, project management, and starting up and shutting down boilers. He is proficient in overseeing the commissioning of boilers, turbines, and their auxiliaries.
This document contains the resume of Bansil Gandhi. It summarizes his personal and professional details including his educational qualifications, work experience, skills, training and objective of seeking a challenging career in a reputed organization. He has over 8 years of experience working in oil refineries in India and Saudi Arabia as a field operator and executive handling various refinery units and processes like distillation, hydrotreating and hydrocracking.
Mayur Amin is applying for the position of Panel Operator/DCS Operator. He has over 18 years of experience in refinery operations, including over 8 years experience working at Laffan Refinery in Qatar. He has extensive experience operating and maintaining various refinery units including hydrotreaters, distillation columns, and sweetening units. He is proficient in DCS systems from Honeywell and Foxboro and has experience commissioning and starting up new plants.
Adiabatic Reactor Analysis for Methanol Synthesis Plant Note Book Series: P...Gerard B. Hawkins
The document discusses adiabatic reactor analysis for methanol synthesis from syngas. It provides the reaction kinetics and calculates conversion, temperature, and reactor volume needed at different conversions. Energy and mass balances are used to derive relationships between conversion, temperature and reaction rate. Data is generated to plot conversion versus volumetric flow rate for reactor sizing. The plot indicates a continuous stirred tank reactor (CSTR) could achieve 85% conversion before switching to a plug flow reactor (PFR) for higher conversion with less volume.
Gas Mixing
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 RECOMMENDATIONS FOR GAS MIXING:
PLUG FLOW
5 RECOMMENDATIONS FOR GAS MIXING:
BACKMIXED INITIAL ZONE
6 BIBLIOGRAPHY
Leandro E. Miranda is applying for the position of control room operator. He has over 20 years of experience working in control rooms for oil and gas facilities, including FPSOs. He is knowledgeable in operating various distributed control systems including ABB, Emerson, and Yokogawa systems. Miranda has experience starting up, operating, and shutting down complex process facilities like gas plants, methanol plants, and power plants. He is skilled at monitoring systems, identifying issues, and ensuring safe operation.
This document summarizes the commercialization of Velocys' advanced Fischer-Tropsch synthesis technology. Key points include:
Velocys has 15+ years of experience and over $300 million invested in developing their microchannel reactor technology. Their pilot plant demonstrates stable long-term operation with excellent catalyst regenerability and lifetime. Their process is designed for modular scalability.
Velocys works with world-class partners and has commercial rollout underway, with resources including technical centers and a permanent pilot plant. Their technology offers advantages including isothermal behavior, robustness, economy, and high productivity.
Experimental design and validation ensure the catalyst and process meet commercial requirements for stability, performance, and tolerance to variations
How to Use the GBHE Mixing Guides
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 THE MIXING GUIDES
4.1 Mixing Guides
4.2 GBHE Mixing and Agitation Manual
5 DEVICE SELECTION
6 MIXING QUESTIONNAIRE
6.1 What is being mixed?
6.2 Why is it being mixed?
6.3 How is it to be mixed?
6.4 Is Heat Transfer Important?
6.5 Is Mixing Time Important?
6.6 Is Inventory Important?
6.7 Is Subsequent Phase Separation Important?
6.8 What Quantities?
6.9 What are the Selection Criteria?
6.10 What Data are required?
7 BASICS
7.1 Bulk Movement
7.2 Shear and Elongation
7.3 Turbulent Diffusion
7.4 Molecular Diffusion
7.5 Mixing Mechanisms
APPENDICES
A ROTATING MIXING DEVICES
B MIXING DEVICES WITHOUT MOVING PARTS
This document summarizes an innovative energy efficiency project at Hindustan Coca-Cola Beverages Pvt. Ltd's Goblej plant to optimize the PET bottle blowing pressure and reduce power consumption of the 40 bar air compressor. The project team optimized the blowing pressure from 30kg/cm2 to 26kg/cm2 and installed a variable frequency drive for the compressor, resulting in annual energy savings of 1.8 million Indian rupees with a payback period of 8 weeks.
This document discusses DSM's yeast technologies for ethanol production. It introduces several DSM sales and technical representatives. DSM offers two yeast products, eBOOST and eBOOST GT, which can increase ethanol yields by 3% on average compared to standard yeast. These yeasts also reduce glycerol production by up to 68% and decrease levels of contaminants like acetaldehyde. Commercial trial data shows higher ethanol levels and yields from eBOOST yeast. Charts are presented comparing eBOOST GT to a competitor's yeast showing eBOOST GT's higher sugar consumption and ethanol tolerance.
Newest Edition of the Kontro Quarterly!!! Features HMD Kontro's newest ANSI Model CSA!! We Salute HMD's Jo Whitling!! DXP Ohio River Valley in the Spotlight!!
Presentation by
Primary Information Services
www.primaryinfo.com
mailto:primaryinfo@gmail.com
Download PDF Version at
https://www.slideshare.net/thorapadi/presentations
See You tube Channel
https://www.youtube.com/user/ch600091/videos?view_as=subscriber
The document summarizes the history and operations of NOGA Private Limited, an agro-processing company in Maharashtra, India. It began as a cold storage facility for oranges in 1946 and was later taken over by the state government. NOGA processes various fruits into products like juices, squashes, jams and sells them to retail markets, hotels and airlines. It has received several awards for its products. NOGA continues to expand its product range and distribution network to meet growing demand.
This document provides a summary of Abhishek Thummar's first monthly assessment for an in-plant training on the production of Nitrosyl Sulfuric Acid (NSA). It discusses the raw materials used, chemical reaction, properties and applications of NSA, equipment used in the process, material and utility requirements, and safety procedures. The document also includes an equipment list, material balance calculation showing a production of 11,150 kg of NSA, and responses to assessment questions covering various unit operations employed.
Critical Variables in Catalytic Reforming and Unit Monitoring Best PracticesGerard B. Hawkins
This document discusses optimization strategies for catalytic reforming processes in oil refineries. It outlines best practices for identifying and monitoring critical variables, and provides examples of critical variables like catalyst activity and recycle gas composition. The document also discusses principles of reformer optimization like defining objectives, layered management practices, and optimizing operations. Overall it provides guidance on monitoring performance, catalyst management, and using online optimization to improve profitability of refinery catalytic reforming units.
Revamp objectives
Revamp Philosophy
Revamp options
Semi-Regenerative Reforming Unit
Typical Flow Scheme
Continuous Reforming Unit
Typical Flow Scheme
Revamp to Hybrid Operation
What may be achieved?
Typical C5+ Yield at Decreasing Pressure
Changes Required for Full Conversion
Typical Benefits of Full Conversion
Revamping of Existing Continuous Reforming Units
Fired Heaters Revamp
Burners
Reactor Options
Regeneration Section
Summary
This document provides guidance for conducting a pre-commissioning safety review of a process or plant (Hazard Study 5). The purpose is to check that the detailed implementation meets requirements before start-up. A cross-functional team inspects arrangements for employee health, safety, and environmental protection. The commissioning manager coordinates inspection of all areas, using a checklist to ensure all factors are considered. Any outstanding actions must be closed or scheduled before start-up. The review verifies the project complies with standards and is ready to safely commence operations.
Mechanical Constraints on Thermal Design of Shell and Tube ExchangersGerard B. Hawkins
Mechanical Constraints on Thermal Design of Shell and Tube Exchangers
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 STANDARD DIMENSIONS
4.1 Shell Diameters
4.2 Tube Lengths
4.3 Tube Diameters
4.4 Tube Wall Thicknesses
5 CLEARANCES
5.1 Tube Pitch
5.2 Pass Partition Lane Widths
5.3 Minimum 'U' Bend Clearance
5.4 Tube-to-Baffle Clearance
5.5 Baffle-to-Shell Clearance
5.6 Bundle-to-Shell Clearance
6 TUBESHEET THICKNESS
7 END ZONE LENGTHS
8 TUBE COUNTS
8.1 Program Correlations
8.2 Use of Tube count Tables
8.3 Graphical Layout
8.4 Use of Computer Programs
8.5 Tie Rods
TABLES
1 HEAT EXCHANGER SHELLS - GEOMETRICAL DATA
FOR INLET & OUTLET BRANCHES: PIPE WITH ANSI
150 FLANGE
2 HEAT EXCHANGER SHELLS - GEOMETRICAL DATA
FOR INLET & OUTLET BRANCHES: PIPE WITH ANSI
300 FLANGE
3 TEMA TIE ROD STANDARDS
FIGURES
1 DEFINITION OF TUBE PITCH, LIGAMENT THICKNESS & PASS PARTITION LANE WIDTH
2 DEFINITION OF PASS PARTITION LANE WIDTH FOR U-TUBES
3 BUNDLE TO SHELL CLEARANCES FOR DIFFERENT BUNDLE TYPES
4 ESTIMATED TUBESHEET THICKNESS FOR FIXED TUBE CONSTRUCTION
5 ESTIMATED TUBESHEET THICKNESS FOR U-TUBE CONSTRUCTION
6 END ZONE
7 EXAMPLE OF OPTU3 GRAPHICAL OUTPUT
A.B.RAJESWARA RAO has over 18 years of experience in refinery operations including as a shift supervisor. He has a post-graduate degree in oil and gas and lives in the Kingdom of Bahrain. Currently he works as a shift supervisor at BAPCO, overseeing units like hydrotreating and distillation. Previously he has worked for companies in Abu Dhabi, India, and has experience in commissioning, pre-commissioning, process safety, and operating control systems. He seeks to use his expertise gained over many years to benefit oil and gas operations.
This document describes the responsibilities of an operator for a plant that produces sulfuric acid. The plant uses a furnace to produce steam from sulfur dioxide off-gas and sends the gas through an electrostatic precipitator and induced draft fan to a sulfuric acid plant. The operator monitors plant parameters through a distributed control system, takes corrective actions when needed, and ensures safe startup and shutdown following standard operating procedures.
Berlie Technologies Inc. is a sludge treatment specialist located in LaPrairie, Quebec near the US border. It has 85 employees including engineers, technicians, and field crew. The company has annual sales of $25 million and certifications in pressure equipment, sanitary fabrication, and boiler and pressure vessel inspection. Berlie specializes in the design of sludge digestion and dewatering systems using various technologies like high performance digesters, drying systems, belt filter presses, and more. It has reference projects across Europe, the Middle East, and North America for municipal and industrial wastewater and sludge treatment.
Pratik Parmar is seeking assignments in operations and maintenance, commissioning, and project management of boilers and turbines up to 500 TPH and 120 MW. He has 6 years of experience in operations and maintenance of boilers and turbines, troubleshooting, commissioning, project management, and starting up and shutting down boilers. He is proficient in overseeing the commissioning of boilers, turbines, and their auxiliaries.
This document contains the resume of Bansil Gandhi. It summarizes his personal and professional details including his educational qualifications, work experience, skills, training and objective of seeking a challenging career in a reputed organization. He has over 8 years of experience working in oil refineries in India and Saudi Arabia as a field operator and executive handling various refinery units and processes like distillation, hydrotreating and hydrocracking.
Mayur Amin is applying for the position of Panel Operator/DCS Operator. He has over 18 years of experience in refinery operations, including over 8 years experience working at Laffan Refinery in Qatar. He has extensive experience operating and maintaining various refinery units including hydrotreaters, distillation columns, and sweetening units. He is proficient in DCS systems from Honeywell and Foxboro and has experience commissioning and starting up new plants.
Adiabatic Reactor Analysis for Methanol Synthesis Plant Note Book Series: P...Gerard B. Hawkins
The document discusses adiabatic reactor analysis for methanol synthesis from syngas. It provides the reaction kinetics and calculates conversion, temperature, and reactor volume needed at different conversions. Energy and mass balances are used to derive relationships between conversion, temperature and reaction rate. Data is generated to plot conversion versus volumetric flow rate for reactor sizing. The plot indicates a continuous stirred tank reactor (CSTR) could achieve 85% conversion before switching to a plug flow reactor (PFR) for higher conversion with less volume.
Gas Mixing
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 RECOMMENDATIONS FOR GAS MIXING:
PLUG FLOW
5 RECOMMENDATIONS FOR GAS MIXING:
BACKMIXED INITIAL ZONE
6 BIBLIOGRAPHY
Leandro E. Miranda is applying for the position of control room operator. He has over 20 years of experience working in control rooms for oil and gas facilities, including FPSOs. He is knowledgeable in operating various distributed control systems including ABB, Emerson, and Yokogawa systems. Miranda has experience starting up, operating, and shutting down complex process facilities like gas plants, methanol plants, and power plants. He is skilled at monitoring systems, identifying issues, and ensuring safe operation.
This document summarizes the commercialization of Velocys' advanced Fischer-Tropsch synthesis technology. Key points include:
Velocys has 15+ years of experience and over $300 million invested in developing their microchannel reactor technology. Their pilot plant demonstrates stable long-term operation with excellent catalyst regenerability and lifetime. Their process is designed for modular scalability.
Velocys works with world-class partners and has commercial rollout underway, with resources including technical centers and a permanent pilot plant. Their technology offers advantages including isothermal behavior, robustness, economy, and high productivity.
Experimental design and validation ensure the catalyst and process meet commercial requirements for stability, performance, and tolerance to variations
How to Use the GBHE Mixing Guides
0 INTRODUCTION/PURPOSE
1 SCOPE
2 FIELD OF APPLICATION
3 DEFINITIONS
4 THE MIXING GUIDES
4.1 Mixing Guides
4.2 GBHE Mixing and Agitation Manual
5 DEVICE SELECTION
6 MIXING QUESTIONNAIRE
6.1 What is being mixed?
6.2 Why is it being mixed?
6.3 How is it to be mixed?
6.4 Is Heat Transfer Important?
6.5 Is Mixing Time Important?
6.6 Is Inventory Important?
6.7 Is Subsequent Phase Separation Important?
6.8 What Quantities?
6.9 What are the Selection Criteria?
6.10 What Data are required?
7 BASICS
7.1 Bulk Movement
7.2 Shear and Elongation
7.3 Turbulent Diffusion
7.4 Molecular Diffusion
7.5 Mixing Mechanisms
APPENDICES
A ROTATING MIXING DEVICES
B MIXING DEVICES WITHOUT MOVING PARTS
This document summarizes an innovative energy efficiency project at Hindustan Coca-Cola Beverages Pvt. Ltd's Goblej plant to optimize the PET bottle blowing pressure and reduce power consumption of the 40 bar air compressor. The project team optimized the blowing pressure from 30kg/cm2 to 26kg/cm2 and installed a variable frequency drive for the compressor, resulting in annual energy savings of 1.8 million Indian rupees with a payback period of 8 weeks.
This document discusses DSM's yeast technologies for ethanol production. It introduces several DSM sales and technical representatives. DSM offers two yeast products, eBOOST and eBOOST GT, which can increase ethanol yields by 3% on average compared to standard yeast. These yeasts also reduce glycerol production by up to 68% and decrease levels of contaminants like acetaldehyde. Commercial trial data shows higher ethanol levels and yields from eBOOST yeast. Charts are presented comparing eBOOST GT to a competitor's yeast showing eBOOST GT's higher sugar consumption and ethanol tolerance.
Newest Edition of the Kontro Quarterly!!! Features HMD Kontro's newest ANSI Model CSA!! We Salute HMD's Jo Whitling!! DXP Ohio River Valley in the Spotlight!!
Presentation by
Primary Information Services
www.primaryinfo.com
mailto:primaryinfo@gmail.com
Download PDF Version at
https://www.slideshare.net/thorapadi/presentations
See You tube Channel
https://www.youtube.com/user/ch600091/videos?view_as=subscriber
The document summarizes the history and operations of NOGA Private Limited, an agro-processing company in Maharashtra, India. It began as a cold storage facility for oranges in 1946 and was later taken over by the state government. NOGA processes various fruits into products like juices, squashes, jams and sells them to retail markets, hotels and airlines. It has received several awards for its products. NOGA continues to expand its product range and distribution network to meet growing demand.
This document provides a summary of Abhishek Thummar's first monthly assessment for an in-plant training on the production of Nitrosyl Sulfuric Acid (NSA). It discusses the raw materials used, chemical reaction, properties and applications of NSA, equipment used in the process, material and utility requirements, and safety procedures. The document also includes an equipment list, material balance calculation showing a production of 11,150 kg of NSA, and responses to assessment questions covering various unit operations employed.
This document provides information on biodiesel, including its composition as fatty acid methyl esters derived from vegetable oils, animal fats, and waste cooking oils. It discusses the transesterification process used to produce biodiesel from these feedstocks and some of the standards and properties of biodiesel. It also addresses the economics and viability of biodiesel production in India, highlighting the potential for employment generation and use of wastelands without impacting food supplies.
1) The document discusses India's petroleum products and supply chain network. It outlines the various petroleum products categorized and traded in India such as base oils, bitumen, crude oil, fuel oil, and others.
2) It describes India's international petroleum trade, pipelines operations and objectives, and supply chain and distribution network. The key aspects of exploration, production, refining, and marketing in the supply chain are highlighted.
3) The objectives of a successful petroleum supply chain are outlined as minimizing costs while meeting demand and responding quickly to opportunities. Suggestions to improve the supply chain such as long-term raw material agreements and transportation infrastructure investments are provided.
The document compares four major oil marketing companies - Essar Oil, Reliance Industries Limited, Petronas, and ExxonMobil - on the basis of their operations, types of products, market factors, innovation, and environmental sustainability. It finds that while ExxonMobil and Petronas have a large global presence, they have less penetration in the Indian market which is dominated by public sector companies. Reliance has the highest refining capacity and revenue, while Essar has more retail outlets than Reliance.
This document summarizes a company that provides pharmaceutical grade solvents for global requirements. The company produces high purity ethanol and sterile solvents and custom blends in production quantities. They have facilities around the world that are FDA registered and operate under cGMP. Their purpose is to provide solvents that meet increasing global regulations to support their clients.
Boris van Thiel discusses how small incremental improvements, or marginal gains, can provide significant benefits. He outlines how thyssenkrupp achieves marginal gains through innovative technologies like their STAR process for propylene production and urea fertilizer production with elemental sulfur. Process improvements and asset management also provide marginal gains through initiatives like mechanical design changes that reduce energy use by 7%. These many small improvements, though only 1% individually, have large cumulative impacts when implemented across an organization.
This document provides an overview of Arabian American Development Co., including its petrochemical and mining segments. The petrochemical segment, South Hampton Resources, operates a processing facility in Texas and markets high purity hexanes and pentanes used in products like polyethylene, polyurethane foams, and synthetic rubber. The mining segment consists of a 35% ownership in a joint venture mining company in Saudi Arabia.
This document provides an overview of Arabian American Development Co., including its petrochemical and mining segments. The petrochemical segment, South Hampton Resources, operates a processing facility in Texas and markets high purity hexanes and pentanes used in products like polyethylene, polyurethane foams, and synthetic rubber. The mining segment consists of a 35% ownership in a joint venture mining company in Saudi Arabia.
This document provides a business plan for growing oyster mushrooms on 1 acre of land. It details the initial investment needed, including costs for temporary sheds, equipment, and one production cycle. The total initial investment is approximately Rs. 606,500. Each subsequent 60-90 day production cycle costs around Rs. 90,000-130,000 excluding initial costs. The projected returns are around 195,000 rupees for the first cycle, with returns increasing to 50% in the second cycle and 60% from the third cycle onward. The business plan also outlines plans for marketing, production expansion, distribution centers, sales centers, and cooking units to grow the business over 5 years on a national and international scale.
This technical proposal summarizes the scope of work for a 350 KLD effluent treatment plant (ETP) to treat evaporation pond water from Cairn India. The key components of the ETP system include preliminary treatment, coagulation, flocculation, tube settling, filtration, industrial reverse osmosis, product water storage, and dosing pumps. The treated water must meet specifications for injection water and be continuously monitored. The ETP is designed to process 300-350 cubic meters of water per day to generate treated water that meets the required specifications.
The document provides an overview of the oil and gas industry in India, benchmarking major companies and innovations. It discusses BPCL's integrated operations and opportunities to adopt marketing strategies like organizing expos, brand associations, and content marketing. The document also outlines gaps in Indian and global fuel retail practices and how technologies can be used to capture methane waste. It proposes an advertising campaign around cancer prevention focused on awareness, research funding, and vaccine education.
Conesa produces a variety of vegetable products for different customers in Europe. It has a business model focused on sustainability in economic, social, and environmental terms. It produces many different products for brand-oriented customers where sustainability is very important. Conesa aims to farm and process tomatoes efficiently and sustainably by reducing water, fertilizers, pesticides, and costs through various measures like sustainable farming certification, new varieties, traceability, and farmer support. It also processes tomatoes efficiently through dedicated high-capacity lines, automation, recovering resources, and running at full capacity.
Visakh Refinery in India has increased its capacity over 8-fold since 1957 to process various imported and domestic crude oils. It produces products like LPG, gasoline, diesel, and jet fuel. The refinery uses computer-controlled in-line blending to optimize blending of products like gasoline to meet specifications like vapor pressure and octane at lowest cost. While gasoline blending showed no quality giveaway, diesel blending experienced some quality giveaway. In-line blending, real-time analyzers, and additional storage are recommended to reduce losses from diesel quality giveaway.
Aarti Pharmalabs Ltd specializes in the clinical phase and commercial production of APIs and NCEs, intermediates, regulatory starting materials, key building blocks and xanthine derivatives. Our offerings include process R&D, analytical method development and validations, stability studies, scale-up and process optimization, process validations and commercial production. The quality and purity of our products have enabled us to be the leading Active Pharmaceutical ingredients manufacturers in India.
The document describes KUAI Energy Systems' modular crude oil minirefineries. The refineries range in capacity from 500 to 50,000 barrels per day and produce products like gasoline, kerosene, diesel, and asphalt. They minimize environmental impact by being air cooled and sited near oil fields. The modular design allows for flexible configurations and production capacities.
Latest HVACR Trends by Danfoss - GineersNow Engineering MagazineGineersNow
GineersNow HVACR Leaders Magazine Issue 002
HVACR Leaders Magazine: Danfoss, Levan Taskin, President of Middle East, North Africa and Turkey on HVAC innovations - through the years.
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This document outlines the operations of a petroleum products factory. It discusses the factory's QHSE policy which is based on client focus, leadership, engaging people, and process approach. The factory has a blending plant with 50 ton daily capacity and storage tanks for virgin oil, finished products, and blending vessels. It sources base oils from various suppliers and categorizes them into groups. The factory produces a variety of automotive and industrial lubricants, greases, and specialty products meeting various standards.
Similar to Final report chili oleoresin project usaid amd 045 14 may 2018 (20)
Project overview
Compost produced from biological wastes does not contain any chemicals unfavorable to
living soil. This organic fertilizer is also one of them which contain phosphate, nitrogen
solubilizing bacteria and decomposing fungi, which is co-friendly and protect the plants from
various soil borne diseases.
Production of composed fertilizer from Sugar press mud, residues by-products of sugar
industries is found to be worthy for maintaining health of plant and soil properties and protects
the plant from various soil borne diseases. In this feasibility paper, composting of SPM on
commercial basis is discussed.
Availability in Pakistan:
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planted on approximately 1.1 M Hectors producing 5.5 Million tones sugar with an average
yield of 51 tones per Hector. In which almost 82-84 % cane is utilized in sugar industries.
According to an estimate Pakistan sugar industry is producing about 1.2 - 1.8 million tones of
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Formulation and product development of CBD formulations at AHL _wo_ingredien...Dr Syed Arshad raza
Cannabinoids are chemical compounds present in cannabis plants as well as present naturally in the body , have diversified effect on whole body. Some key cannabinoids present in hemp / cannabis plants are THC (< than 0.3 % in hemp), Cannabidiol (CBD), CBDA, CBDV, CBG, CBN, CBC and terpenes are other minor constituents.
CBD is devoid of psychoactive effects and have broad clinical potential for a wide spectrum of ailments such as Neuroprotective, anxiolytic, anti-inflammatory, Antioxidant. Arthritis cancer, Epilepsy, Alzheimer’s disease, Schizophrenia, cognitive dysfunction & Psychosis.
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Oral as well as topical dosage delivery forms are developed by Arshad herbal Laboratories to utilize the benefits of CBD synergistic blends.
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Industrial hemp the global boom final draft 19 june 2019.pptxDr Syed Arshad raza
Industrial hemp the Green Gold global boom Opportunities for economic Prosperity & Challenges for Pakistan. Pakistan’s Northern areas offer a unique prospective opportunity of economic uplift by cultivation & value addition industrial hemp “THE GREEN GOLD”, Its thriving market size was estimated at USD 3.9 billion globally in 2017, expanding at a CAGR of 14.0%, expected to reach USD 10.6 billion by 2025. Impact on industries and economy ► Will Revolutionize various industries & sectors as Agriculture, Textiles, Pharmaceutical, Nutraceutical, Food & Nutrition, Building & construction, Automobiles, with positive impact on reducing CO2 emissions & environment. (Biomass for carbon sequestration). ► Restores, Revolutionize and improve performance of troubled textile sector. ► Production is 3 X than cotton per acre. ► Marginal water requirements compared to cotton. ► Negligible pesticide requirements compared to cotton, Natural habitat of dry and cold mountainous climate of northern areas. ► Can generate US$ 1 Billion worth of revenue in just 1 - 2 years. ► Can generate 100,000 -200,000 jobs in just a year time. ► Biomass for carbon sequestration 70 ton dry weight per hectare.
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Seaweed meal for poultry industry has diversified and versatile functional properties and is ideal for countries like Pakistan where poultry industry is facing challenges such as Bacterial resistance etc
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derivatives for Pharmaceuticals, Nutraceuticals, cosmaceuticals, tobacco &
confectionary industry from high quality licorice roots from Afghanistan.
Afghanistan has abundant supply of species of high quality licorice roots,
where as Glycyrrhiza glabra seems to be the major species.
We are prime manufacturer of herbal extracts from Pakistan. Our
manufacturing facility lies adjacent to raw material source, is equipped
with modern manufacturing and analytical instrument (HPLC, UV
,HPTLC,GC) and competent professionals to manufacture high quality
licorice extract. Great care is taken to procure the best quality licorice
roots and optimum process is adapted to ensure highest quality licorice
extracts.
Heptavite AF is a combination of nutraceuticals that has effective anti-fibrotic properties. It works by decreasing oxidative stress in the liver and down-regulating the activation of hepatic stellate cells, which play a key role in liver fibrosis. The formulation contains antioxidants and compounds that inhibit hepatic stellate cell proliferation, extracellular matrix production, and pro-inflammatory signaling pathways involved in fibrosis. By reducing inflammation and oxidative damage in the liver and targeting hepatic stellate cells, Heptavite AF can help arrest and potentially reverse the progression of liver fibrosis.
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Final report chili oleoresin project usaid amd 045 14 may 2018
1. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
US-Pakistan Partnership for Agricultural
Market Development (AMD)
“
”
14 may 2018
2. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
1. Background.
Based on our previous working experience
on oleoresin extraction, we developed a
research methodology to investigate the
local market requirements and develop
specifications to finalize/customize an
appropriate size pilot plant to be used in
manufacturing of oleoresin based on
current technologies and available units.
3. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
2. Types of oleoresins.
Specification Capsicum Chili/pepper Paprika
Odor / taste Very pungent &
aromatic
Pungent &
Aromatic
Aromatic
Color Light red to red Red Deep red
SHU 80000-500000 80000-500000 Negligible
Capsicine 0.6-3.9 0.6-3.9 Negligible
Color Units (cu) < 4000 < 20000 40000-150000
4. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Our current engagement in chili oleoresin.
We are engaged in manufacturing oleoresin extracts
with chili and turmeric as main raw materials, have
developed oleoresin capsicum and chili oleoresin
from dandi cut chili, paprika oleoresin from sweet
verity chili and turmeric oleoresin for curcuminoids.
Our main products are oleoresin capsicum for
pungency & oleoresin turmeric for curcuminoids.
Oleoresin capsicum does have a color value
however the finished products are usually
concerned with the biological activities of capsaicin
(pungent principle).
5. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
3. Research methodology.
I. Current status of industry.
II. Types of raw material Availability.
III. Budget.
IV. Current technologies available in extraction of oleoresin.
6. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Evaluation of Current status of industry.
• Understand demand of Grantees.
• Understand Local demand of Potential
Customers.
• Types of oleoresin products consumed in local
market.
7. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Type of raw material Availability.
• Dandi Cut moderate yield, Pungency values 30000 -
45000* and color values 35-65 ASTA*.
• Hybrid moderate yield, Pungency values 60000-75000 and
color values 35-65 ASTA*.
• Talhar Sweet chili moderate yield, Pungency values 4000-
5000 and color values 100-130 ASTA*.
*Values provided by NFL
8. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Budget.
A Financial budget of Rs.
9000000 is allocated for the
purchase of oleoresin plant by
USAID-AMD.
9. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Current technologies available in extraction of oleoresin.
• Low temperature:
I. SCFE (Super Critical fluid extraction).
II. Subcritical (Hydrocarbon extraction).
• Solvent Extraction
10. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Low temp. Super critical Fluid extraction (SCFE).
• Preferred technology by customers Oleoresin Industry in
Developed countries & uses CO2 as solvent.
• High initial investment and low processing cost.
• No solvent residue and low temperature application.
• Not preferred in paprika oleoresin industry due to poor
solubility of pigments in CO2.
11. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Low Temperature Subcritical Hydrocarbon extraction.
• New technology mostly applied in manufacturing of
cannabis extracts.
• Uses propane or butane or a combination with high initial
investment.
• Practically very low level of solvent residue, low solvent
requirement and Low temperature application.
• Issues with Compatibility with other raw materials.
12. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Comparison of different techniques available for Chili oleoresin extraction
Parameters SCFE Subcritical Solvent
Temperature Low Low Moderate
Temp duration Less Less more
Yield Low Adequate Good
Capsaicin Adequate Low Good
Color Low Adequate Good
Investment Very High High Economical
Process cost Low Low High
Compatibility* Low -
moderate
Low - moderate Good
Residual solvent No Negligible Considerable
*compatibility with other raw materials
13. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Solvent Extraction.
• Most widely used technology.
• Uses various solvents and combinations.
• Adequate data for processing of all raw materials
available.
• Increased processing cost due to solvent concentration
and recovery as compared to SCFE and Hydrocarbon.
• Suitable for all types of extracts, oleoresin and oils.
• Solvent residue is major concern and require careful
processing to keep residual solvent under limit.
14. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Pilot Plant selection.
On the basis of above researched factors a suitable
size Solvent extraction plant is to be
selected/customized from vendors having
technological capabilities, experience and willingness
to develop a pilot size oleoresin extraction plant. It was
indicated by USAID-AMD that pilot may preferably
selected from European or American origin. However
we have also included plants of Chinese origin for
comparison.
16. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Process flow in Solvent Extraction.
Pre-Processing
(Grinding)
Extraction with
suitable solvent/s
Filtration/separation
of liquid extract from
raw material
Concentration of
extract (solvent
removal)
Collection of extract
17. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Key Customized Features required for pilot size
oleoresin extraction plant.
• Easy to handle Plug and Play.
• Easy material input and output handling.
• Must perform extraction efficiently.
• Must have adequate equipment to concentrate &
distill off residual solvent from extract.
• Following units are under consideration for
customization Preferably supplied from
experienced and renown companies.
18. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
1. 100 L Pilot Extraction Plant Germany (SOL01) Devex.
• Connect - Plug – Produce: Plant is ready for operation, after
connection to the local utility supplies.
• For development of oleoresin a small pilot Extraction/concentration
plant provides the ideal solution for developing product in a reliable
and easy to use configuration, or for small batch processing.
• The plant consists of 1x100 L extraction vessels, 200 L extract
collection tank, a plate evaporator with a downstream centrifugal
separator. A vacuum pump is connected to the condenser, and the
vacuum can be adjusted. The evaporation temperature can be
adjusted according to the product specific boiling curve through the
applied vacuum.
• Supplier Location: Germany Price : Euros 89,950/USD $106800
20. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
2. Herbal Extractor, Concentrator, Storage Tank
STCTL (SOL02 ).
Model DT-0.5m3 ,The whole unit includes Extractor,
Single effect concentrator 200 L/hr., Extract storage
tanks.
Price: USD 32200 China.
21. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
2. Herbal Extractor, Concentrator, Storage Tank
STCTL(SOL02 )
22. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
2.
• Normal temperature & pressure extraction,
dynamic recycling extraction, countercurrent
extraction & other processes. This device can
perform as dynamic continuous countercurrent
recycling extra-dynamic continuous
countercurrent extractor. It consist of 200 L
cryogenic extractor, vacuum concentrator and
chiller.
• Total Price Fob shanghai 35,000 USD
23. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
200L multifunctional extraction & concentrating machine China.
24. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
3. MAXI 50 PE-R 200 Lt heater vessel &
concentrator HP 10 Italy (SOL03) Timatic.
Equipment is high efficiency, latest developed small
dynamic extraction unit. It is composed of 50 L extracting
tank, evaporating concentrator 10 L/hr. and process
piping, with dynamic heat reflux extraction, vacuum
concentration and solvent recovery as a whole.
Unit Price USD 91466. FOB Italy
25. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
3. MAXI 50 PE-R 200 Lt heater vessel &
concentrator HP 10 Italy (SOL03).
26. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
3. MAXI 50 PE-R 200 Lt heater vessel & concentrator
HP 10 Italy (SOL03).
27. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
4. 200L multifunctional Dynamic versatile extraction &
concentrating machine China (SOL07 ).
• Normal temperature & pressure extraction, dynamic
recycling extraction, countercurrent extraction & other
processes. This device can perform as dynamic
continuous countercurrent recycling extra-dynamic
continuous countercurrent extractor. It consist of 200 L
cryogenic extractor, vacuum concentrator and chiller.
• Total Price Fob shanghai 35,000 USD
28. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
4. 200L multifunctional Dynamic versatile extraction &
concentrating machine China (SOL07 ).
29. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
5. High Efficiency Low Temperature Extraction &
Concentration Production Line (SOL04).
• Based on soxhlet principle it consist of 600 Liters extraction tank,
concentrator evaporator 800 L/hr., It can extract 400-600 kg raw
material in single batch.
• Price : 95,500 USD/set FOB China.
30. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
5. High Efficiency Low Temperature Extraction &
Concentration Production Line (SOL04).
31. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
6. LPMIE High Efficiency Low Temperature Extraction &
Concentration Production Line (SOL05).
• 200L multi-function hot reflux extraction and
concentrate tank unit.
• Residue discharged from side of tank.
• Explosion-proof electric control cabinet
• Price: USD23000.00 FOB China
32. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
6. LPMIE High Efficiency Low Temperature Extraction &
Concentration Production Line (SOL05).
33. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
7. RGMCL 500L herb extractor and concentrator
(SOL06)
• Unit composed of extractor, concentrator, condenser,
receiver and pipes, valves, meters and so on
• It is heated by steam, button control system
• Material contact parts are mirror polished, it is
stainless steel in compliance with GMP standard.
• Price: USD21500.00 FOB China
34. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
7. RGMCL 500L herb extractor and concentrator
(SOL06)
35. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
7. 200L multifunctional Dynamic versatile extraction &
concentrating machine China (SOL07 ).
• Normal temperature & pressure extraction, dynamic
recycling extraction, countercurrent extraction & other
processes. This device can perform as dynamic
continuous countercurrent recycling extra-dynamic
continuous countercurrent extractor. It consist of 200 L
cryogenic extractor, vacuum concentrator and chiller.
• Total Price Fob shanghai 35,000 USD
36. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
7. 200L multifunctional Dynamic versatile extraction &
concentrating machine China (SOL07 ).
37. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Efficacy Comparison of different solvent plants under evaluation.
Reference #
Sol: solvent,
HC: Subcritical
Location Model Type
Ext. tank
Effective
Volume
Raw
material
capacity per
batch kg
(Approx.)
Batch
time hrs.
(Approx.)
Finished
Product
per batch
kg
(Approx.)
Finished
product
per day
(8 hours)
kg
(Approx.)
Price
SOL01 Germany
200L-
180017
Solvent 100 L 10 2 1 4 $106800
SOL02 China DT-0.5m3 Solvent 500 L 50 2 5 15-20 $32,200
SOL03 Italy 50 L Solvent 50 L 10 10 1 1-2 $91466
SOL04 China
LTQ-
6m3/1500
Solvent 600 L 500 8 50 50 $95,500
SOL05 China LPMIE 200 Solvent 200 L 20 2 2 8 $23000
SOL06 China 500 L Solvent 500 L 50 2 5 20 $21500
SOL02 China
200 L
MHUECM
Solvent 200 L 20 1 2 15 $50,000
38. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
5. Hydrocarbon subcritical extractor (HC01) 4.5 kg.
• Based on low temperature hydrocarbon subcritical
extraction, this unit processes more than 10 lbs. of
material per run with an average 60 minute recovery
time making it ideal for small scale commercial
production.
• Location: USA
• Price: USD 138404
39. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Hydrocarbon subcritical extractor (HC01).
40. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
6. Hydrocarbon subcritical extractor 40 kg (HC02).
• Based on low temperature hydrocarbon subcritical
extraction, this unit processes more than 90 lbs. of
material per run with an average 4 hour recovery time
making it ideal for medium scale commercial production.
• Location: USA
• Price: USD 258590
41. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
6. Hydrocarbon subcritical extractor 40 kg (HC02).
42. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
7. Hydrocarbon subcritical extractor 4.50 kg (HC03).
• Based on low temperature hydrocarbon subcritical
extraction, this unit can processes more than 3 kg of
material per run with an average 60 minute recovery time
making it ideal for small scale commercial production.
• Location: USA
• Price: USD $60,000
43. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Hydrocarbon subcritical extractor 4.50 kg (HC03)
44. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
8. Hydrocarbon subcritical extractor 150 kg (HC04).
• Based on low temperature hydrocarbon subcritical
extraction, more than 130 kg of material may be
processes per run with an average 6-8 hour recovery
time making it ideal for medium scale commercial
production.
• Location: China
• Price: USD 90500
45. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Hydrocarbon subcritical extractor 150 kg (HC04).
46. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Efficacy Comparison of different plants under evaluation.
Reference #
Sol: solvent,
HC: Subcritical
Location Model Type
Ext. tank
Effective
Volume
Raw
material
capacity
per batch
kg (Aprx.)
Batch
time
hrs.
Aprx.
Finished
Product
per batch
kg (Aprx.)
Finished
product
per day
(8 hours)
kg (Aprx.)
Price
SOL01 Germany
200L-
180017
Solvent 100 L 25 2 2.5 10 $106800
SOL02 China
200 L
MHUECM
Solvent 200 L 20 0.5 2 30 $50,000
SOL03 Italy 50 L Solvent 50 L 20 10 2 2 $91466
SOL04 China
LTQ-
6m3/1500
Solvent 600 L 500 8 50 50 $95,500
HC01 USA X 10 Subcritical 14L x 2 4.5 1 0.45 3.15 $138,404
HC02 USA PX 40 Subcritical 180L 40 4 4 8 $258,590
HC03 USA
10LB
Active PSI
Subcritical 10 L 3 1 0.3 2.1 $60,000
HC04 China
150L
LTSEE
Subcritical 150 L 150 8 15 15 USD 90500
47. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Conclusions.
As of the information available following conclusions may be
derived:
1. Raw material Availability & oleoresin Demand.
2. Extraction unit from EU Germany.
3. Extraction unit from EU Italy.
4. Extraction unit from China.
48. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Raw material Availability & oleoresin Demand.
1. Availability: There is substantial quantity to raw material
available for Capsicum and chili pepper oleoresin and
adequate raw material for paprika oleoresin is available
and new varieties of sweet chili should be introduced for
cultivation.
2. Demand: There is adequate demand of chili oleoresin
specially paprika oleoresin.
49. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Extraction unit from EU Germany.
This is an excellent well developed plug and play unit
with all the parameters well suited for manufacturing of
extraction, with only minor customization required if
needed. Only compatibility of various solvents is to be
evaluated and manufacturer confirms to update us in
this regard if a purchase decision is made. Vacuum
pump can create adequate pressure for removal of
solvent under permissible limits.
Back-to-Basics Training Series
50. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Extraction unit from EU Italy.
• This is also an innovative effort, an excellent well
developed computer controlled unit based on high
pressure extraction technology with all the
parameters well suited for manufacturing of oleoresin
with only minor customization required if needed.
Compatibility of various solvents is to be evaluated
and manufacturer confirms to update us in this regard
if a purchase decision is made. It consist of a
separate concentration unit and both units are to be
connected to perform complete processing. Vacuum
pump can create pressure for removal of solvent.
51. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Extraction units from China.
• We have evaluated several units from china. The
working capacity to cost ratios are better from
Europeans. However the technology is relatively
inferior.
• Durability is also questionable.
However a few plants have shown good parameters and
these plants can be further customized/upgraded to
improve the performance as well as durability to match
EU plants.
52. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Recommendation
• Italian unit may fits in budget but needs to proper
evaluated to finalize it for extraction.
• Supplier has recommended us to visit them to
properly evaluate the plant.
• Chinese plant can also be improved, customize and
upgraded to compete for durability with plants of EU
origin.
• An initial lab scale unit can be developed from
Chinese supplier to test it for oleoresin than go for
pilot size plant.
53. U.S. PAKISTAN PARTNERSHIP FOR AGRICULTURAL MARKET DEVELOPMENT
Thank you for selecting
AHL for Chili oleoresin
Project.