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		<title>Technology of Lubrication &#038; Lubricants, Crude Oil Processing, Catalysts in Petroleum Refining and Petrochemical Processes with Mineral Turpentine Oil</title>
		<link>https://projectreports.eiriindia.org/product/technology-lubrication-lubricants-crude-oil-processing-catalysts-petroleum-refining-petrochemical-processes-mineral-turpentine-oil/</link>
		
		<dc:creator><![CDATA[EIRI Team]]></dc:creator>
		<pubDate>Thu, 30 Aug 2018 10:56:44 +0000</pubDate>
				<guid isPermaLink="false">https://projectreports.eiriindia.org/?post_type=product&#038;p=11734</guid>

					<description><![CDATA[<p>The Book covers the following chapters: Lubrication and Lubricants, Benzene, Ethylene,  Monoethylene Glycol, Diethylene Glycol, Triethylene Glycol, Ethylene Oxide, Toluene,  Xylene,  Petroleum jelly,  Bioethanol Production From Sugar Cane Molasses,  Production of Bio-ethanol from Molasses by Schizosaccharomyces Species, Petroleum Crude Oils, Crude Oil Processing,  Chemicals Based on Methane, Ethane and Higher Paraffins-Based Chemicals,  Chemicals Based On Ethylene,  Chemicals Based on Propylene,  C4 Oleffins and Diolefins- Based Chemicals,  Chemicals Based on Benzene, Toluene, and Xylenes, Synthetic Petroleum-Based Polymers,  Catalysts in Petroleum Refining and Petrochemical Processes, Petrochemicals Future, Plant Economics of Mineral Turpentine Oil (MTO),  Plant Economics of Lubricating Oil (20w40 Grade SN Type),  Plant Economics of Oil Re-refining Unit, Plant Economics of Crude Oil Refining.</p>
<p>The post <a href="https://projectreports.eiriindia.org/product/technology-lubrication-lubricants-crude-oil-processing-catalysts-petroleum-refining-petrochemical-processes-mineral-turpentine-oil/">Technology of Lubrication &#038; Lubricants, Crude Oil Processing, Catalysts in Petroleum Refining and Petrochemical Processes with Mineral Turpentine Oil</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
]]></description>
										<content:encoded><![CDATA[<div><strong>Contents:</strong></div>
<div></div>
<div><strong>Lubrication and Lubricants </strong></div>
<ul>
<li>Functions of Lubricants</li>
<li>Lubrication Principles</li>
<li>Tests of Lubricants</li>
<li>Lubricants of Mineral Origin</li>
<li>Synthetic Lubricants</li>
</ul>
<div><strong>Benzene </strong></div>
<ul>
<li>Manufacturing Process From Petroleum by</li>
<li>Catalytic Reforming</li>
</ul>
<div><strong>Ethylene </strong></div>
<ul>
<li>From Refinery Gas by Thermal Cracking</li>
</ul>
<div><strong>Monoethylene Glycol</strong></div>
<ul>
<li>Molecular Formula</li>
</ul>
<div><strong>Diethylene Glycol </strong></div>
<ul>
<li>Molecular Formula</li>
</ul>
<div><strong>Triethylene Glycol </strong></div>
<ul>
<li>Monoethylene Glycol From Ethylene and Oxygen</li>
<li>Uses</li>
<li>Grades</li>
<li>Toxicity</li>
</ul>
<div><strong>Ethylene Oxide  </strong></div>
<ul>
<li>Molecular Formula</li>
<li>Properties</li>
<li>Manufacturing Process</li>
<li>From Ethylene and Oxygen</li>
<li>Raw material requirement</li>
</ul>
<div><strong>Toluene  </strong></div>
<ul>
<li>Properties</li>
<li>Manufacturing Process</li>
<li>From Petroleum by Hydroforming</li>
<li>Raw material requirement</li>
</ul>
<div><strong>Xylene </strong></div>
<ul>
<li>Properties of Xylene Isomers</li>
<li>Manufacturing Process</li>
<li>Form Petroleum by Catalytic Reforming or</li>
<li>hydroforming</li>
</ul>
<div><strong>Petroleum jelly </strong></div>
<ul>
<li>Physical properties</li>
<li>Comparison with glycerol</li>
<li>Uses</li>
<li>Medical treatment</li>
<li>Skin and hair care</li>
<li>Preventing moisture loss</li>
<li>Hair grooming</li>
<li>Skin lubrication</li>
<li>Product care and protection</li>
<li>Coating</li>
<li>Finishing</li>
<li>Lubrication</li>
<li>Production processes</li>
<li>Tattooing</li>
<li>Explosives</li>
<li>Mechanical, barrier functions</li>
<li>Surface cleansing</li>
<li>Pet care</li>
<li>Clean-up</li>
<li>Properties of Petroleum Jelly</li>
<li>Skin Care</li>
<li>Face Care</li>
<li>Hair Care</li>
<li>Nail Care</li>
<li>Household Needs</li>
</ul>
<div><strong>Bioethanol Production From Sugar Cane </strong><strong>Molasses </strong></div>
<ul>
<li>Ethanol</li>
<li>Feedstock for bioethanol production</li>
<li>Sucrose-containing feedstocks</li>
<li>Starchy materials</li>
<li>Lignocellulosic biomass</li>
<li>Ethanol from cane molasses</li>
<li>Processes of ethanol production</li>
</ul>
<div><strong>Production of Bio-ethanol from Molasses </strong><strong>by Schizosaccharomyces Species </strong></div>
<ul>
<li>Introduction</li>
<li>Materials And Methods</li>
<li>Collection of Samples</li>
<li>Isolation of Schizosaccharomyces</li>
<li>Production of Ethanol from Molasses</li>
<li>Identification of the Microorganisms</li>
<li>Originally Present in Molasses</li>
<li>Inoculation of Molasses by Isolated Yeast</li>
<li>Distillation and Detection of Ethanol</li>
<li>Results And Discussion</li>
<li>Isolation of Schizosaccharomyces</li>
<li>Species</li>
<li>Physical Characteristics of the</li>
<li>Molasses Sample</li>
<li>Microorganisms Originally Present</li>
<li>in Molasses</li>
<li>Production of Ethanol from Raw</li>
<li>Molasses</li>
<li>Production of Ethanol from Molasses</li>
<li>with Different Concentrations of Sucrose</li>
<li>Detection of Ethanol</li>
</ul>
<div><strong>Petroleum Crude Oils </strong></div>
<ul>
<li>Composition of Crude Oils</li>
<li>Hydrocarbon Compounds</li>
<li>Alkanes (Paraffins)</li>
<li>Cycloparaffins (Naphthenes)</li>
<li>Aromatic Compounds</li>
<li>Non-hydrocarbon Compounds</li>
<li>Sulfur Compounds</li>
<li>Acidic Sulfur Compounds</li>
<li>Non-acidic Sulfur Compounds</li>
<li>Nitrogen Compounds</li>
<li>Basic Nitrogen Compounds</li>
<li>Non-Basic Nitrogen Compounds</li>
<li>Oxygen Compounds</li>
<li>Acidic Oxygen Compounds</li>
<li>Non-Acidic Oxygen Compounds</li>
<li>Metallic Compounds</li>
<li>Density, Specific Gravity and API Gravity</li>
<li>Salt Content</li>
<li>Sulfur Content</li>
<li>Pour Point</li>
<li>Ash Content</li>
</ul>
<div><strong>Crude Oil Processing</strong></div>
<ul>
<li>Physical Separation Processes</li>
<li>Atmospheric Distillation</li>
<li>Vacuum Distillation</li>
<li>Absorption Process</li>
<li>Adsorption Process</li>
<li>Solvent Extraction</li>
<li>Conversion Processes</li>
<li>Thermal Conversion Processes</li>
<li>Coking Processes</li>
<li>Thermal Cracking Reactions</li>
<li>Delayed Coking</li>
<li>Fluid Coking</li>
<li>Viscosity Breaking (Vis-breaking)</li>
<li>Catalytic Conversion Processes</li>
<li>Catalytic Reforming</li>
<li>Reformer Feeds</li>
<li>Reforming Catalysts</li>
<li>Reforming Reactions</li>
<li>From Acetylene and Acetone</li>
<li>From Isobutylene and Formaldehyde (IFP Process)</li>
<li>From Isobutylene and Methylal (Sun Oil Process)</li>
<li>From Propylene (Goodyear Process)</li>
</ul>
<div><strong>Chemicals Based on Methane</strong></div>
<ul>
<li>Chemicals Based On Direct Reactions of Methane</li>
<li>Carbon Disulfide (CS)</li>
<li>Uses Of Carbon Disulfide</li>
<li>Hydrogen Cyanide (Hcn)</li>
<li>Chloromethanes</li>
<li>Production of Chloromethanes</li>
<li>Uses of Chloromethanes</li>
<li>SYNTHESIS GAS</li>
<li>CHEMICALS BASED ON SYNTHESIS GAS</li>
<li>AMMONIA (NH)</li>
<li>Uses of Ammonia</li>
<li>Nitric Acid (HNO)</li>
<li>Hydrazine (HN-NH).</li>
<li>Methylalcohol (CHOH)</li>
<li>Production of Methanol</li>
<li>Uses of Methanol</li>
<li>Methyl Chloride (CHCI)</li>
<li>Acetic Acid (CHCOOH)</li>
<li>Methyl Tertiary Butyl Ether ((CH)C-O-CH)</li>
<li>Dimethyl Carbonate (CO(OCH))</li>
<li>Methylamines</li>
<li>Ethylene Glycol</li>
</ul>
<div><strong>Ethane and Higher Paraffins-Based Chemicals </strong></div>
<ul>
<li>Ethane Chemicals</li>
<li>Propane Chemicals</li>
<li>Oxidation of Propane</li>
<li>Nitration of Propane (Production of Nitroparaffins)</li>
<li>N-butane Chemicals</li>
<li>Oxidation of N-butane (Acetic Acid and</li>
<li>Acetaldehyde)</li>
<li>Maleic Anhydride:</li>
<li>Aromatics Production</li>
<li>Isobutane Chemicals</li>
<li>Naphtha-based Chemicals</li>
<li>Chemicals From High Molecular Weight</li>
<li>N-paraffins</li>
<li>Oxidation Of Paraffins (Fatty Acids And Fatty</li>
<li>Alcohols)</li>
<li>Chlorination Of N-paraffins (Chloroparaffins)</li>
</ul>
<div><strong>Chemicals Based On Ethylene</strong></div>
<ul>
<li>Introduction</li>
<li>Oxidation Of Ethylene</li>
<li>Derivatives of Ethylene Oxide</li>
<li>Ethylene Glycol (CHOHCHOH)</li>
<li>Ethoxylates</li>
<li>Ethanolamines</li>
<li>,-Propanediol</li>
<li>Acetaldehyde (Chcho)</li>
<li>Important Chemicals From Acetaldehyde</li>
<li>Acetic Acid</li>
<li>N-butanol</li>
<li>Oxidative Carbonylation of Ethylene</li>
<li>Chlorination of Ethylene</li>
<li>Vinyl Chloride (Ch=Chcl)</li>
<li>Linear Alcohols</li>
</ul>
<div><strong>Chemicals Based on Propylene</strong></div>
<ul>
<li>Oxidation of Propylene</li>
<li>Acrolein (CH=CHCHO)</li>
<li>Uses of Acrolein</li>
<li>Ammoxidation Of Propylene</li>
<li>(Acrylonitrile [CH=CHCN])</li>
<li>Uses of Acrylonitrile</li>
<li>Adiponitrile (NC(CH)CN)</li>
<li>Deriatives and Uses of Propylene Oxide</li>
<li>Propylene Glycol (CHCH(OH)CHOH)</li>
<li>Allyl Alcohol (CH=CHCHOH)</li>
<li>Oxyacylation of Propylene</li>
<li>Chlorination of Propylene</li>
<li>(Allyl Chloride [Ch=Chchcl])</li>
<li>Hydration of Propylene</li>
<li>(Isopropanol [Chchohch])</li>
<li>Properties And Uses of Isopropanol</li>
<li>Acetone Production</li>
<li>Propertles and Uses of Acetone</li>
</ul>
<div><strong>C4 Oleffins and Diolefins- Based Chemicals </strong></div>
<ul>
<li>Introduction</li>
<li>Chemicals From N-butenes</li>
<li>Oxidation of Butenes</li>
<li>Acetic Acid CHCOH</li>
</ul>
<div><strong>Chemicals Based on Benzene, Toluene, and </strong><strong>Xylenes </strong></div>
<ul>
<li>Reactions and Chemicals of Benzene</li>
<li>Reactions and Chemicals of Toluene</li>
<li>Oxidation of Toluene</li>
<li>Caprolactam Production</li>
<li>Phenol from Benzoic Acid</li>
<li>Terephthalic Acid from Benzoic Acid</li>
<li>Chlorination of Toluene</li>
<li>Nitration of Toluene</li>
<li>Carbonylation of Toluene</li>
<li>Chemicals From Xylenes</li>
<li>Terephthalic Acid (Hoocc6h4cooh)</li>
</ul>
<div><strong>Synthetic Petroleum-Based Polymers </strong></div>
<ul>
<li>Introduction</li>
<li>Thermoplastics And Engineering Resins</li>
<li>Polyethylene</li>
<li>Low-Density Polyethylene</li>
<li>High-Density Polyethylene</li>
<li>Linear Low-Density Polyethylene</li>
<li>Properties and Uses of Polyethylenes</li>
<li>Polypropylene</li>
<li>Copolymerization</li>
<li>Properties and Uses of Polypropylene</li>
<li>Properties and Uses of Polyvinyl Chloride</li>
<li>Properties and Uses of Styrene Polymers</li>
<li>Nylon Resins</li>
<li>Thermoplastic Polyesters</li>
<li>Polycarbonates</li>
<li>Properties and Uses of Polycarbonates</li>
<li>Polyether Sulfones</li>
<li>Properties and Uses of Aromatic Polyether Sulfones</li>
<li>Poly(phenylene) Oxide</li>
<li>Polyacetals</li>
<li>Thermosetting Plastics</li>
<li>Polyurethanes</li>
<li>Properties and Uses of Polyurethanes</li>
<li>Epoxy Resins</li>
<li>Properties and Uses of Epoxy Resins</li>
<li>Unsaturated Polyesters</li>
<li>Phenol-formaldehyde Resins</li>
<li>Properties and Uses of Phenolic Resins</li>
<li>Amino Resins (Aminoplasts)</li>
<li>Urea-Formaldehyde and Urea-Melamine Resins</li>
<li>Properties and Uses of Aminoplasts</li>
<li>Polycyanurates</li>
<li>Synthetic Rubber</li>
<li>Butadiene Polymers And Copolymers</li>
<li>Properties and Uses of Polybutadiene</li>
<li>Styrene-Butadiene Rubber (SBR)</li>
<li>Nitrile Rubber (Nbr)</li>
<li>Polyisoprene</li>
<li>Properties and Uses of Polyisoprene</li>
<li>Polychloroprene (Neoprene Rubber)</li>
<li>Butyl Rubber</li>
<li>Ethylene-propylene Rubber</li>
<li>Transpolypentamer</li>
<li>Thermoplastic Elastomers</li>
<li>Synthetic Fibers</li>
<li>Polyester Fibers</li>
<li>Polyethylene Terephthalate Production</li>
<li>Properties and Uses of Polyesters</li>
<li>Polyamides (Nylon Fibers)</li>
<li>Nylon  (Polyhexamethyleneadipate)</li>
<li>Nylon  (Polycaproamide)</li>
<li>Nylon  (Polylaurylamide)</li>
<li>Nylon  (Polybutyramide)</li>
<li>Nylon  (Polyundecanylamide)</li>
<li>Other Nylon Polymers</li>
<li>Properties and Uses of Nylons</li>
<li>Acrylic And Modacrylic Fibers</li>
<li>Properties and Uses of Polyacrylics</li>
<li>Carbon Fibers (Graphite Fibers)</li>
<li>Polypropylene Fibers</li>
</ul>
<div><strong>Catalysts in Petroleum Refining and </strong><strong>Petrochemical Processes  </strong></div>
<ul>
<li>Introduction</li>
<li>Homogeneous and Heterogeneous Catalysts</li>
<li>Catalyst Morphology and Activity</li>
<li>Catalysts for Petroleum Refining</li>
<li>Cracking Catalysts</li>
<li>Reforming Catalysts</li>
<li>Hydrotreating Catalysts</li>
<li>Catalysts For Petrochemicals Industry</li>
<li>Catalysts For Synthesis Gas</li>
<li>Hydrogenation Catalysts</li>
<li>Hydrocarbon Oxidation Catalysts</li>
<li>Polymerization Catalysts</li>
<li>Recent Advances in Industrial Catalysis</li>
<li>Dual-Function Catalysts</li>
<li>Super-Active Metal Catalysts</li>
<li>Supported-Ziegler Catalysts</li>
<li>Advances in Homogeneous Catalysis</li>
<li>Role of Polymers in Catalysis</li>
</ul>
<div><strong>Petrochemicals Future </strong></div>
<ul>
<li>Integrated Petrochemicals Complex</li>
<li>Natural Gas As Petrochemical Feedstock</li>
<li>Impact Of Heavy Feedstocks</li>
<li>On Petro-chemicals</li>
<li>Ecology And The Energy Crisis</li>
<li>Coal As An Alternative To Oil</li>
<li>Energy Crisis and the Industrial Fuels</li>
<li>Natural Fuels</li>
<li>Synthetic Fuels</li>
<li>Hydrogen: Fuel for tomorrow</li>
<li>Trends in Petrochemical Industry</li>
<li>Development in Cracking Technology</li>
<li>Olefins Vs Paraffins</li>
<li>Prospect for Propylene</li>
<li>Size of Plant</li>
<li>Biomass: Renewable Resource for Petrochemicals</li>
<li>Waste Disposal</li>
</ul>
<div><strong>Plant Economics of Mineral Turpentine Oil (MTO) </strong></div>
<ul>
<li>Plant &amp; Machinery</li>
<li>Fixed Capital</li>
<li>Raw Materials</li>
<li>Total Working Capital/Month</li>
<li>Total Capital Investment</li>
<li>Turn Over/Annum</li>
</ul>
<div><strong>Plant Economics of Lubricating Oil (20w40  </strong><strong>Grade Sn-Type) </strong></div>
<ul>
<li>Plant &amp; Machinery</li>
<li>Fixed Capital</li>
<li>Raw Materials</li>
<li>Total Working Capital/Month</li>
<li>Total Capital Investment</li>
<li>Turn Over/Annum</li>
</ul>
<div><strong>Plant Economics of Oil Re-refining Unit </strong></div>
<ul>
<li>Plant &amp; Machinery</li>
<li>Fixed Capital</li>
<li>Raw Materials</li>
<li>Total Working Capital/Month</li>
<li>Total Capital Investment</li>
<li>Turn Over/Annum</li>
</ul>
<div><strong>Plant Economics of Crude Oil Refining </strong></div>
<ul>
<li>Plant &amp; Machinery</li>
<li>Fixed Capital</li>
<li>Raw Materials</li>
<li>Total Working Capital/Month</li>
<li>Total Capital Investment</li>
<li>Turn Over/Annum</li>
</ul>
<div></div>
<div><strong>List of Tables</strong></div>
<div>Table : Properties and uses of various types of greases</div>
<div>Table : Specification for Commercial Grades of Benzene</div>
<div>Table : Typical specification for polymer-grade ethylene</div>
<div>Table :  Specifications of Technical Grades of</div>
<div>Ethylene Glycol</div>
<div>Table :  Specification for Technical Grade Diethylene</div>
<div>Glycol and Triethylene Glycol</div>
<div>Table : Commercial specifications of Industrial Xylene</div>
<div>Table : Type of feedstock</div>
<div>Table : Physical properties of Ethanol</div>
<div>Table : Different feedstock for bioethanol production and their comparative production potential.</div>
<div>Table : Main components of cane black strap molasses</div>
<div>Table : Microbiological analysis of sugarcane</div>
<div>molasses</div>
<div>Table : Production of ethanol and pH value from raw molasses</div>
<div>Table : Production of ethanol and pH value from molasses with different concentrations of sucrose</div>
<div>Table : Heating values of methane and heavier hydrocarbons present in natural gas</div>
<div>Table : Typical analysis of some crude oils</div>
<div>Table : Approximate ASTM boiling point ranges for</div>
<div>crude oil fractions</div>
<div>Table: Types of petroleum cokes and their end uses</div>
<div>Table : Major thermoplastic polymers</div>
<div>Table : Important properties of polyethylenes</div>
<div>Table : Properties of Polypropylene</div>
<div>Table : Properties of polycarbonates compared with</div>
<div>some thermoplastics</div>
<div>Table : Selected properties of some elastomers</div>
<div>Table : Important properties of polyesters</div>
<div>Table : Melting points of various nylons and the</div>
<div>monomer formula</div>
<div>Table :  Physical properties of fiber-grade</div>
<div>polypropylene</div>
<div>Table : Characteristics of Typical Catalysts used in Petroleum Refining.</div>
<div>Table :  Important Catalytic Processes of Refining</div>
<div>and Petrochemical Industry</div>
<div>Table : Major Catalysts in use in IPCL Plants</div>
<div>Table : Industrially Important Free-Racial</div>
<div>Polymerization Catalysts</div>
<div>Table :  Ziegler-Type Catalysts used in Polymer</div>
<div>Manufacture</div>
<div>Table : HOPE Catalysts.</div>
<div>Table :  Miscellaneous Catalysts used In Polymer</div>
<div>Industry.</div>
<div>Table :  Relative Cost of Ethylene Production from</div>
<div>Various Feedstocks</div>
<div>Table : Octane Number of Aromatics.</div>
<div>Table : Calorific Value of Fuels.</div>
<div>Table :  Comparative Cost of Production of Various</div>
<div>Fuels.</div>
<div>Table : Sources of Hydrogen.</div>
<div>Table :  Yield Pattern from a High Severe Cracking</div>
<div>Furnace.</div>
<div>Table :  Comparative Study of Propane and</div>
<div>Propylene Routes to Acrylonitriie</div>
<div>List of figures</div>
<div>Fig  Fluid film formation in bearing</div>
<div>Fig : Ethanol structure</div>
<div>Fig : Sugar refinery process</div>
<div>Fig.: Enzymatic hydrolysis of starch to glucose.</div>
<div>Fig. : Flow chart of ethanol production from cereal</div>
<div>grains.</div>
<div>Fig.  Culture characteristics of Schizosacc-</div>
<div>haromyces species</div>
<div>Fig.  Microscopic appearance of Schizosacc-</div>
<div>haromyces species using Gram stain technique</div>
<div>Fig.  KMnOH+ before addition of sample (a),</div>
<div>Reduction of KMnOH+ to colourless after</div>
<div>addition of sample (b)</div>
<div>Fig.  KCrOH+before addition of</div>
<div>sample (a), KCrOH+after addition change</div>
<div>into colour (b)</div>
<div>Fig.  Iodine reagent before addition sample (a),</div>
<div>addition of sample and heating, colour of iodine</div>
<div>change into blue colour (b) and when cooling in water</div>
<div>and added NaOH, the reaction formed yellow colour</div>
<div>precipitate</div>
<div>called iodo-form (c)</div>
<div>Fig  Flow diagram of atmospheric and vacuum</div>
<div>distillation units: (,) heat exchangers; () desalter,</div>
<div>(,) heater; () distillation column, () overhead</div>
<div>condenser, (-) pump around streams, () vacuum</div>
<div>distillation heater; () vacuum tower.</div>
<div>Fig  Important chemicals based on methane,</div>
<div>synthesis gas, ammonia, and methanol.</div>
<div>Fig  A block flow diagram showing the combined</div>
<div>reforming for methanol synthesis.</div>
<div>Fig  The Haldor Topsoe and Nippon Kasei</div>
<div>process for producing formaldehyde:  () blower,</div>
<div>() heat exchanger, () reactor, () steam boiler,</div>
<div>() absorber, (,) coolers, () incinerator, () heat</div>
<div>recovery, () methanol evaporator, () boiler</div>
<div>feed water.</div>
<div>Fig  Major chemicals based on ethylene.</div>
<div>Fig  Important chemicals based on propylene.</div>
<div>Fig . Important chemicals based on benzene.</div>
<div>Fig . The reaction scheme for o-xylene to phthalonitrile</div>
<div>Fig  The Union Carbide Unipol process for producing</div>
<div>Fig  The Union Carbide gas-phase process for gh</div>
<div>producing polypropylene: () reactor, () centri-</div>
<div>fugal compressor, () heat exchanger, () product</div>
<div>discharge tank (unreacted gas separated from product),</div>
<div>() impact reactor, () compressor, () heat exchanger,</div>
<div>() discharge tank (copolymer separated from reacted</div>
<div>gas).</div>
<div>Fig  Polyvinyl chloride</div>
<div>Fig  The European Vinyls Corp. process for</div>
<div>producing polyvinyl chloride using suspension polymeri-</div>
<div>zation : () reactor, () blow-down vessels (to</div>
<div>separate unreacted monomer), () stripping column,</div>
<div>() reacted monomer recovery, () slurry centrifuge,</div>
<div>() slurry drier.</div>
<div>Figure  The Lummus Crest Inc. process for</div>
<div>producing polystyrene: () reactor, () holding</div>
<div>tank (Polystyrene beads and water), () centrifuge,</div>
<div>() pneumatic drier, () conditioning tank, () screening of</div>
<div>beads, (,) lubrication and blending, () shipping product.</div>
<div>Figure  The comparative thickness for the same</div>
<div>degree of insulation (dry conditions).</div>
<div>Figure  A process for producing ,-polyisoprene</div>
<div>(&gt;%) by a continuous solution polymerization.</div>
<div>Figure  The Inventa AG Process for</div>
<div>producing polyethylene-terephthala</div>
<div>Figure  The Inventa-Fisher process for producing</div>
<div>nylon  from caprolactam: () Melting station, (, )</div>
<div>polymerization reactors, () extruder, () intermediate</div>
<div>vessel, () extraction column, (,) extraction</div>
<div>columns, () cooling silo.</div>
<p>The post <a href="https://projectreports.eiriindia.org/product/technology-lubrication-lubricants-crude-oil-processing-catalysts-petroleum-refining-petrochemical-processes-mineral-turpentine-oil/">Technology of Lubrication &#038; Lubricants, Crude Oil Processing, Catalysts in Petroleum Refining and Petrochemical Processes with Mineral Turpentine Oil</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
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			</item>
		<item>
		<title>SOLVENT EXTRACTION OF RICE BRAN OIL WITH REFINING (REFINED RICE BRAN OIL)</title>
		<link>https://projectreports.eiriindia.org/product/solvent-extraction-rice-bran-oil-refining-refined-rice-bran-oil/</link>
		
		<dc:creator><![CDATA[EIRI Team]]></dc:creator>
		<pubDate>Wed, 10 Sep 2014 10:21:00 +0000</pubDate>
				<guid isPermaLink="false">http://projectreports.eiriindia.org/?post_type=product&#038;p=2495</guid>

					<description><![CDATA[<p style="text-align: justify;">        Rice  bran is the most important source of edible oil  among the  unconventional  sources.   Rice bran is  the  brown  coating around  the  white  starchy  rice kernel  which  is  obtained  by dehusking  paddy and polishing the rice.  Despite the  impressive growth  of rice bran technology in the country, only a  third  of the available potential has been exploited.</p>
<p><strong>   Project Report Covers:</strong></p>
<ul>
<li>    Introduction</li>
<li>    Uses and Applications</li>
<li>    Properties</li>
<li>    Market Survey with future aspects</li>
<li>    Present Manufacturers</li>
<li>    B.I.S. Specifications</li>
<li>    Manufacturing Process with Formulae</li>
<li>   Cost Economics with Profitability Analysis</li>
<li>    Capacity</li>
<li>    Land &#38; Building Requirements with Rates</li>
<li>    List &#38; Details of Plant and Machinery with their Costs</li>
<li>    Raw Materials</li>
<li>    Details/List and Costs</li>
<li>    Power &#38; Water Requirements</li>
<li>    Labour/Staff Requirements</li>
<li>    Utilities and Overheads</li>
<li>    Total Capital Investment</li>
<li>    Turnover</li>
<li>    Cost of Production</li>
<li>    Break Even Point</li>
<li>    Profitability</li>
<li>    Land Man Ratio</li>
<li>    Suppliers of Plant &#38; Machineries and Raw Materials.</li>
</ul>
<p>The post <a href="https://projectreports.eiriindia.org/product/solvent-extraction-rice-bran-oil-refining-refined-rice-bran-oil/">SOLVENT EXTRACTION OF RICE BRAN OIL WITH REFINING (REFINED RICE BRAN OIL)</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
]]></description>
										<content:encoded><![CDATA[<p>The post <a href="https://projectreports.eiriindia.org/product/solvent-extraction-rice-bran-oil-refining-refined-rice-bran-oil/">SOLVENT EXTRACTION OF RICE BRAN OIL WITH REFINING (REFINED RICE BRAN OIL)</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
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			</item>
		<item>
		<title>Technology Book of Oilseeds Processing, Oils &#038; Fats and Refining</title>
		<link>https://projectreports.eiriindia.org/product/technology-oilseeds-processing-oils-fats-refining/</link>
		
		<dc:creator><![CDATA[EIRI Team]]></dc:creator>
		<pubDate>Wed, 19 Feb 2014 09:49:22 +0000</pubDate>
				<guid isPermaLink="false">http://projectreports.eiriindia.org/?post_type=product&#038;p=1232</guid>

					<description><![CDATA[<p>The book Technology of Oilseeds Processing, Oils &#038; Fats and Refining  covers Chemical constituents of Fats, Oleaginous Seeds and their oils, Olive and Olive Oil, Palm Oil and Its Fractions, Animal Fat, Technology of Refining of Fats,  Hydrogenation Technology, Fractionation Technology, Margarine Technology,Production of Neat Soap with 63% fatty acids, Oilseed Processing Technology.</p>
<p>The post <a href="https://projectreports.eiriindia.org/product/technology-oilseeds-processing-oils-fats-refining/">Technology Book of Oilseeds Processing, Oils &#038; Fats and Refining</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
]]></description>
										<content:encoded><![CDATA[<p>The role of dietary fats and oils in human nutrition is one of the most important areas of concern and investigation in the field of nutritional science. The findings of investigations on this subject have wide-ranging implications for consumers, healthcare providers and nutrition educators as well as food producers, processors and distributors. New evidence concerning the benefits and risks associated with particular aspects of dietary fat is constantly emerging in both the scientific literature and the popular media. At times, controversies about these findings emerge. Sifting through all the claims and counterclaims, incomplete and incompatible studies, and biases and competing interests for the elements of truth and a prudent course of action is a challenge. However, such discrimination in essential because changing views about the effects of dietary fats and oils can profoundly influence the consumption of various foods and, ultimately, health and nutritional status, agricultural production, food processing technologies, food marketing practices and nutrition education. Fats are the main source of energy for satisfactory growth and physical activity during early infancy. This energy requirement is not easily met where diets are low in fat (less than 15 per cent of total calories), which partly explains the high prevalence of malnutrition in such areas. Fats should also be considered in terms of their structural function during the first two years of life. They provide the fatty acids and cholesterol needed to form cell membranes in all the organs.</p>
<p>Moreover, important organs such as the retina and the central nervous system are mainly composed of fats. Most of the fats needed to form these tissues are essential fatty acids (EFAs) which cannot be synthesized by the organism and have to be acquired through nutrition. Mother&#8217;s milk has a special fat composition that makes it unique for goodchild nutrition. It contains factors that facilitate the digestion of fats, while its chemical composition makes it more digestible and includes a balanced supply of n-6 and n-3 fatty acids. Oilseed processing equipment with a daily capacity of less than 50 tons per day typically employs a mechanical extraction process to separate the oil from an oilseed. Mechanical extraction processes apply pressure to separate oil from the meal in an oilseed. A common method for applying mechanical pressure is through a screw press.</p>
<p>Within India there are regional variations in ghani design, which probably arose form the nature of the oilseeds that were regionally available for crushing. The large granite ghanis of southern India have a capacity of 35 to 40 kg, requiring two animals yoked side by side and two operators, one for the animals and the other near the mortar. The load-beam is very long and curved and rides on a strong outer groove on the mortar. These ghanis have a life of four to five years, after which the pit is too worn to be useful. The wooden ghani of western India has a capacity of 8 to 15 kg, has an oil outlet at the base of the pit (which is kept plugged during crushing) and frequently has the operator seated on the load-beam. Margarine is an emulsion of water in oil type (W/O) which include two essential phases: continuous phase: FATTY PHASE dispersed phase: AQUEOUS PHASE It contains also some additives (lecithin, monoglycerides, salt, colouring agent, antioxidant, preservatives, vitamins) distributed partly in the fatty phase (soluble or dispersible in fats) and partly in the aqueous phase (soluble or dispersible in water and/or milk). Emulsion is a liquid system including two immiscible phases, one being finely dispersed in the other. But because of its thermodynamic instability, the emulsion tends to separate for restructuring the two original phases. In the case of margarine, it is therefore necessary to facilitate emulsion and to stabilize that condition. This is the role of emulsifying agents which reduce the quantum of labour for formation of a homogeneous mixture of these two immiscible phases, final stability of the product is obtained by crystallization of the fatty phase in the emulsion.</p>
<p>The complete definition of margarine is thus one of a polydispersed system of fats to solid and liquid states, in water and/ or milk, of ingredients and sometimes of gas bubbles. Mechanical extraction processes have two main elements. The first is seed preparation. Seed preparation methods vary depending on seed characteristics. For example, seed preparation for canola often is limited to seed cleaning while other oilseeds may need to be cleaned, de-hulled, cracked, rolled, and/or flaked. Additional equipment may be required to complete seed preparation. A producer should identify the oilseeds that they are likely to process in order to determine exactly what equipment will be needed.The second element is the removal of oil from the oilseed. In a screw press operation, seed is fed from a hopper into the screw press, which uses pressure to force oil contained in an oilseed through small openings in the side of the press. Meal, that is too large to exit through the small openings is extruded through larger openings at the end of the press. Screw presses are capable of removing approximately 65 percent to 75 percent of the oil contained in an oilseed. Some mechanical presses preheat seed as it enters the press. Preheating increases oil recovery rates to 65 percent to 80 percent. Alternatively, if seed is processed at low temperatures (for example, below freezing) oil recovery rates may be less than 60 percent. Actual recovery rates will depend on press quality, press operation, seed quality, seed type and seed temperature.</p>
<p>The present volume <b><i>Technology of Oilseeds Processing, Oils &amp; Fats and Refining </i></b>contains 11 chapters on various aspects of oilseed processing refining, i.e. <i>Chemical Constituents of Fats, Oleaginous Seeds and their Oils, Olive and Olive Oil, Palm Oil and its Fractions, Animal Fat, Technology of Refining of Fats, Hydrogenation Technology, Fractionation Technology, Margarine Technology, Production of Neat Soap with 63% Fatty Acids, Oilseed Processing Technology</i></p>
<p>&nbsp;</p>
<p><strong>TECHNOLOGY OF OILSEEDS PROCESSING, OILS &amp; FATS AND REFINING</strong> contains:</p>
<p><strong>Chemical Constituents<br />
of Fats</strong></p>
<ul>
<li>Fatty acids</li>
<li>Rules of Nomenclature</li>
<li>Numbering</li>
<li>Nomenclature</li>
<li>Symbols</li>
<li>Saturated Acids</li>
<li>Acids with an even number of carbon atoms</li>
<li>Acids with an odd number of carbon atoms</li>
<li>Branched chain acids</li>
<li>Monoenic acids</li>
<li>Monoenic acids: ethylene bond at 9</li>
<li>Monoenic acids: ethylene</li>
<li>bond at n – 9</li>
<li>Position isomers of oleic acid</li>
<li>Monoenic acids: trans ethylene bond</li>
<li>Monoenic acids: terminal ethylene bond</li>
<li>Polyenic Acids</li>
<li>Other Polyunsaturated Acids</li>
<li>Acids with conjugated</li>
<li>ethylene bonds</li>
<li>Cyclic Acids</li>
<li>Cyclopropenic Acids</li>
<li>Cyclopentenic Acids</li>
<li>Semisynthesized Cyclic</li>
<li>Acids</li>
<li>Acids with Secondary Groups</li>
<li>Hydroxy Acids</li>
<li>Epoxy Acids and Ketoacids</li>
<li>Fatty Acid Distribution</li>
<li>Glycerides</li>
<li>Overview</li>
<li>Stereospecific numbering</li>
<li>and nomenclature</li>
<li>Partial Glycerides</li>
<li>Single-acid diglycerides</li>
<li>Diglycerides with two fatty acids</li>
<li>Triglycerides</li>
<li>Glyceride Structure</li>
<li>Glyceride Composition</li>
<li>Glyceride Distribution</li>
<li>Hypothesis and Distribution Laws</li>
<li>Minor Constituents</li>
<li>Phosphatides</li>
<li>Phosphatidic Acids</li>
<li>Phosphatidyl Amino Alcohols</li>
<li>Phosphatidyl Polyols</li>
<li>Phosphoglyceride Fatty Acids</li>
<li>Sphingolipids</li>
<li>Glucolipids</li>
<li>Monogalactosyl diglyceride Cerides</li>
<li>Unsaponifiable Matter</li>
<li>Triterpenes and their Derivatives</li>
<li>Fat-Soluble Vitamins</li>
<li>Vitamin E, Tocopherols and Tocotrienols</li>
<li>Forms of Vitamin A</li>
<li>Forms of Vitamin D</li>
<li>Fatty Alcohols</li>
<li>Hydrocarbons</li>
<li>Aliphatic Hydrocarbons</li>
<li>Terpenic Hydrocarbons</li>
<li>Carotenes and Carotenoids</li>
<li>Other Constituents</li>
<li>Chlorophylls and their Derivatives</li>
</ul>
<p><strong>Oleaginous Seeds<br />
and their Oils</strong></p>
<ul>
<li>Oil Composition</li>
<li>Oleic Sunflower</li>
<li>Rapeseed and mustard</li>
<li>Rapeseed and Mustard Species</li>
<li>Rapeseed or Mustard Plant</li>
<li>Agronomy of Rapeseed and Mustard</li>
<li>Genetic Improvements</li>
<li>Rapeseed and Mustard Seed</li>
<li>Fatty Acids of Rapeseed and Mustard Oils</li>
<li>Unsaponifiable Fraction of Rapeseed Oil</li>
<li>SOYBEAN</li>
<li>Plant</li>
<li>Seed</li>
<li>Composition of Soybean Oil</li>
<li>Corn and Grapeseeds</li>
<li>Corn</li>
<li>Botany, Crop Growing, Production</li>
<li>Technology</li>
<li>Oil</li>
<li>Physicochemical Characteristics</li>
<li>Triglyceride Composition</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Grapeseeds</li>
<li>Botany, Growing, Production</li>
<li>Technology</li>
<li>Grapeseed Oil</li>
<li>Physicochemical Characteristics</li>
<li>Triglyceride Composition</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Safflower, sesame, Camelina, poppy seed oil</li>
<li>Safflower</li>
<li>Botany, Growing, Production Technology</li>
<li>Safflower Oil</li>
<li>Physicochemical Characteristics</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Sesame</li>
<li>Botany, Growing, Production</li>
<li>Technology</li>
<li>Sesame Oil</li>
<li>Physicochemical Characteristics</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Camelina</li>
<li>Botany, Growing, Production</li>
<li>Camelina Oil</li>
<li>Physicochemical Characteristics</li>
<li>Fatty Acid Composition</li>
<li>Unsaponifiable Fraction</li>
<li>Poppy Seed Oil</li>
<li>Botany, Growing, Production</li>
<li>Poppy Seed Oil</li>
<li>Physicochemical Characteristics</li>
<li>Triglyceride Composition</li>
<li>Fatty Acid Composition</li>
<li>Unsaponifiable Fraction</li>
<li>Oleaginous Flax</li>
<li>Seed</li>
<li>Oil Composition</li>
<li>Almond, Hazelnut, Walnut</li>
<li>Almond</li>
<li>Botany, Growing, Production</li>
<li>Almond Oil</li>
<li>Physicochemical Characteristics</li>
<li>Composition of Triglycerides</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Hazelnut</li>
<li>Botany, Growing, Production</li>
<li>Technology</li>
<li>Hazelnut Oil</li>
<li>Physicochemical Characteristics</li>
<li>Triglyceride Composition</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Walnut</li>
<li>Botany, Growing, Production</li>
<li>Technology</li>
<li>Walnut Oil</li>
<li>Physicochemical Characteristics</li>
<li>Fatty Acid Composition</li>
<li>Composition of Unsaponifiable Fraction</li>
<li>Evening Primrose, Borage, And Blackcurrant Seeds</li>
<li>Overview</li>
<li>Evening Primrose</li>
<li>Botany and Genetics of Primrose</li>
<li>The Œnothera genus</li>
<li>Evening Primrose Seed</li>
<li>Upgrading of the Evening Primrose for Production</li>
<li>of g-Ln</li>
<li>Evening Primrose Oil</li>
<li>Borage</li>
<li>Seed</li>
<li>Some Agronomical Data</li>
<li>Borage Oil</li>
<li>&#8220;Virgin&#8221; Oil or &#8220;Refined&#8221; Oil ?</li>
<li>Main Uses of Borage Oil</li>
<li>Blackcurrant Seeds</li>
<li>Botany</li>
<li>Blackcurrant Seed Oil</li>
<li>Main Uses of Blackcurrant Seed Oil</li>
<li>Competing</li>
<li>Biotechnologies</li>
</ul>
<p><strong>Olive and Olive Oil</strong></p>
<ul>
<li>The Olive and its tree</li>
<li>Composition and characteristics of olive oil</li>
<li>Triglyceride composition</li>
<li>Fatty Acid Distribution in Internal and External Positions</li>
<li>Fatty Acid Composition</li>
<li>Unsaponifiable Matters</li>
<li>Contaminants</li>
<li>Quality and specifications:</li>
<li>The International COI Standard</li>
</ul>
<p><strong><br />
Palm Oil and its Fractions</strong></p>
<ul>
<li>The plant</li>
<li>Botany</li>
<li>Crop growing techniques</li>
<li>Ecology &amp; Growing Area</li>
<li>Yields and Production</li>
<li>Palm oil</li>
<li>Characteristics and Chemical Composition</li>
<li>Utilization</li>
</ul>
<p><strong>Animal Fat</strong></p>
<ul>
<li>Fat rendering industry land animal</li>
<li>Raw Material</li>
<li>Source</li>
<li>Characteristics</li>
<li>Collecting Fat</li>
<li>Rendering Process Principle</li>
<li>Batch dry Rendering System</li>
<li>Continuous Wet Rendering System</li>
<li>Continuous Dry Rendering System</li>
<li>Materials</li>
<li>Metal Elimination</li>
<li>Cookers</li>
<li>Pre-heaters</li>
<li>Dryers</li>
<li>Separators</li>
<li>Bone fat extraction</li>
<li>Choice of a rendering process</li>
</ul>
<p><strong>Technology of Refining of Fats</strong></p>
<ul>
<li>Minor Components and Contaminants to be Eliminated</li>
<li>Free Fatty Acids</li>
<li>Partial Glycerides</li>
<li>Phospholipids</li>
<li>Colouring Agents</li>
<li>Free Sugars, Glycolipids</li>
<li>Hydrocarbons, Resins</li>
<li>Sterols</li>
<li>Tocopherols</li>
<li>Waxes</li>
<li>Metal Compounds</li>
<li>Flavours</li>
<li>Naturally Food-Borne Toxic Substances</li>
<li>Substances of External Origin</li>
<li>Receiving and Storing Crude Oils</li>
<li>Quality Control before Unloading</li>
<li>Crude Oil Warehousing</li>
<li>Determining Quantities, Gaugings</li>
<li>Classical Chemical Refining</li>
<li>Eliminating Phospholipids</li>
<li>Caustic Soda Neutralization</li>
<li>Waterwashing</li>
<li>Drying</li>
<li>Quality Control of Neutral Oil</li>
<li>Acidity</li>
<li>Moisture Content</li>
<li>Phosphorous</li>
<li>Soap</li>
<li>Neutralization Equipment Technology: Pumps, Exchangers, Mixers, Contactors</li>
<li>Feed Pumps</li>
<li>Dosing Pumps</li>
<li>Flow-Meters</li>
<li>Disc Heat-Exchangers</li>
<li>Spiral Exchangers</li>
<li>Welded Plate Heat-Exchangers</li>
<li>&#8220;Compablock&#8221; Exchangers</li>
<li>Scraped Surface Heat Exchangers</li>
<li>Mixers and Contactors</li>
<li>Neutralization Equipment Technology: Centrifugal Separators</li>
<li>Different Types of Continuous Centrifugal Separators</li>
<li>Peripherals of the Centrifugal Separators</li>
<li>Programming System of the Self-Cleaning Separators</li>
<li>Theoretical Data Determining the Bowls Characteristics</li>
<li>Study of Some Equipments</li>
<li>Cylindrical Bowls Separators</li>
<li>Westfalia&#8217;s Separators, Type RTA or OSM with Double Turbine</li>
<li>Alfa-Laval type SRG separator</li>
<li>Separators with Self-Cleaning Bowls</li>
<li>Westfalia&#8217;s Type RSA Self-Cleaning</li>
<li>Separators</li>
<li>Alfa-Laval Type SRPX</li>
<li>Self-cleaning Separators</li>
<li>Bowls Cleaning,</li>
<li>Starting up and Ending Procedures</li>
<li>Self-cleaning Bowls</li>
<li>Dismantling the Bowls</li>
<li>Reassembling the Bowls</li>
<li>Starting and Stopping a Centrifuge</li>
<li>Neutralization Loss</li>
<li>Determining Neutralization</li>
<li>Loss Using an Inventory Balance</li>
<li>Determination Using Loss Control</li>
<li>Determining Neutralization Loss with Chemical Methods</li>
<li>Bleaching</li>
<li>The Absoption Phenomenon</li>
<li>Bleaching Agents</li>
<li>Bleaching Clays</li>
<li>Activated Carbon</li>
<li>Side Effects of Bleaching Agents</li>
<li>&#8220;Trisyl&#8221; and other Similar Products</li>
<li>Bleaching Monitoring</li>
<li>Filtration and filters</li>
<li>Porous Walls</li>
<li>Filters: Process and Technology</li>
<li>Example of a Metallic Cloth Filter: Niagara Filter</li>
<li>Example of a Metal Mesh Filter:</li>
<li>Funda Filter</li>
<li>Example of a Metal Mesh Filter: Bernardini Filter</li>
<li>Plugging of Metal Filters</li>
<li>Safety Filters</li>
<li>Filters Using Paper Filtering Discs: Filter Presses</li>
<li>Filters Using Filtration Discs: Bubble Cap Filters</li>
<li>Filtration Quality Control &#8211; Computerizing  the Process</li>
<li>Control with a Filtration Test</li>
<li>Control with a Turbidity Measure</li>
<li>Monitek Turbidity Instrument</li>
<li>APV-Bowser Turbidity Instrument</li>
<li>De-Oiling Spent Earth</li>
<li>Analyses to be Carried Out on Bleached Oil</li>
<li>Dewaxing Vegetable Oils</li>
<li>Waxes &amp; their Measuring</li>
<li>Dewaxing by Filtration</li>
<li>Dewaxing by Centrifugation, Double Purification</li>
<li>Pre-Dewaxing by Chilling and Centrifugating after Neutralization</li>
<li>Pre-Dewaxing by Chilling and Centrifugating after Partial Neutralization</li>
<li>Pre-Dewaxing by Cold Degumming</li>
<li>Eliminating Spent Earths</li>
<li>&#8220;Demargarination&#8221; of Selectively Hydrogenized Oils</li>
<li>Prechilling Peanut Oils</li>
<li>Deodorization</li>
<li>Flavour and Odour Releasing Substances</li>
<li>Substances Characterizing Non-Alterated Oil</li>
<li>Substances Produced by Oil Degradation</li>
<li>Basic Principles of Deodorization</li>
<li>Influence of Various Parameters</li>
<li>Amount of Steam Injected</li>
<li>Influence of Temperature</li>
<li>Influence of the Duration of the Operation</li>
<li>Influence of Pressure</li>
<li>Influence of the Way Cooling is Conducted</li>
<li>Loss During Deodorization</li>
<li>Inevitable Loss</li>
<li>Other Loss</li>
<li>Product Quality</li>
<li>Deodorization Equipment</li>
<li>Example of a Semicontinuous Deodorizer</li>
<li>Example of a Continuous Deodorizer</li>
<li>Semicontinuous Deodorizer with Continuous Inlet and Outlet</li>
<li>Thin Film Deodorization</li>
<li>Saturation with Nitrogen</li>
<li>Pollution and Nuisance Due to Deodorization</li>
<li>Physical Refining</li>
<li>Basic Principles</li>
<li>Superdegumming</li>
<li>treating the by-products</li>
<li>Soapstocks</li>
<li>Earths From Bleaching</li>
<li>Earths from Dewaxing</li>
<li>Deodorization By-products</li>
<li>Waste Water Treatment</li>
</ul>
<p><strong>Hydrogenation Technology</strong></p>
<ul>
<li>Diagrammatic Principle of Hydrogenation</li>
<li>Hydrogen</li>
<li>Catalysts</li>
<li>Different Types of Catalysts</li>
<li>Catalyst Poisons</li>
<li>Fats and Oils to be Hydrogenated</li>
<li>Hydrogenation Equipment</li>
<li>Discontinuous or Vat Process</li>
<li>DEAD-END System</li>
<li>Continuous Hydrogenation</li>
<li>Comparison with Discontinuous Processes</li>
<li>Principle of Continuous Process</li>
<li>Equipment Models</li>
<li>Separation of Catalyst &amp; Operations</li>
<li>Filtration Conditions</li>
<li>Filtration Apparatus</li>
<li>Handling of Catalyst</li>
<li>General Layout of an Installation</li>
<li>Improvement in Hydrogenation Techniques</li>
<li>New Stirring Techniques</li>
<li>BUSS Loop Reactor</li>
<li>Helicoidal L.M. LITZ</li>
<li>Mechanism</li>
<li>Other Hydrogenation Techniques</li>
<li>Improvement in Energy Yield</li>
<li>Control of Reaction</li>
<li>Process Control</li>
<li>Controlling the End of</li>
<li>Reaction (End Point)</li>
<li>Control of Finished Product</li>
<li>Characteristics of Some Hydrogenated Oils</li>
<li>Safety Problems</li>
<li>Hydrogen-Related Problems</li>
<li>Problems in Handling of Catalyst</li>
<li>Problems of Installation Safety</li>
</ul>
<p><strong>Fractionation Technology</strong></p>
<ul>
<li>Fractionation of palm oil</li>
<li>Fractionation of lightly hydrogenated lard or tallow</li>
<li>Fractionation of Hydrogenated Oils</li>
<li>Dewaxing of Sunflower Oil</li>
<li>Different Methods of Fractionation</li>
<li>Chromatography</li>
<li>Fractionated Crystallization</li>
<li>Liquid/liquid Extraction</li>
<li>Fractionated Crystallization</li>
<li>Principle and Method</li>
<li>Some Theoretical Considerations on Crystallization Technology</li>
<li>Heat transfer between</li>
<li>Rate of nuclei diffusion</li>
<li>Effect of Temperature Gradient (At)</li>
<li>Effect of the Surface (S) of Transfer</li>
<li>Effect of Viscosity</li>
<li>Dry Fractionation</li>
<li>Principle</li>
<li>The TIRTIAUX Process</li>
<li>Fractionation in Solvent</li>
<li>Phase</li>
<li>Principle</li>
<li>Operating Conditions</li>
<li>Installation of Fractionation by Solvent</li>
<li>Fractionation in Presence of Detergent (Lanza process)</li>
<li>Principle</li>
<li>Operating Conditions</li>
<li>Installation Using LANZA Process</li>
<li>Brief Comparison of the Three Processes</li>
<li>Liquid/Liquid Fractionation</li>
<li>Freeman Rule</li>
</ul>
<p><strong>Margarine Technology</strong></p>
<ul>
<li>General Production</li>
<li>Principles</li>
<li>Importance of Crystallization</li>
<li>Polymorphism</li>
<li>Mixed Crystals</li>
<li>Dimension and Form of Crystals</li>
<li>Importance of Rate of Solid</li>
<li>Does the Aqueous Phase and Ingredients Have a Role to Play?</li>
<li>General Production Pattern</li>
<li>Vegetable Oils and Fats</li>
<li>Animal Oils</li>
<li>Formulation of Fatty Phases</li>
<li>Equivalent of Rates of Solids</li>
<li>Introduction of Data of Crystallization</li>
<li>Problems Linked to Hardness</li>
<li>Evaluation of Margarine for Pastry</li>
<li>Elasticity and Spread</li>
<li>Taste of Margarines</li>
<li>Melting Speed</li>
<li>Sensation of  &#8220;freshness &#8220;</li>
<li>Sensation of  &#8220;thickness&#8221;</li>
<li>Oil Exudation</li>
<li>Characteristics of the Fatty Phase</li>
<li>Production Additives and Auxiliaries</li>
<li>Ingredients Soluble in the Fatty Phase</li>
<li>Emulsifying Agent</li>
<li>Monoglycerides of Fatty Acids</li>
<li>Colouring agents</li>
<li>Aromas Soluble in Fatty Phase</li>
<li>Liposoluble Vitamins</li>
<li>Ingredients Soluble in Aqueous Phase</li>
<li>Water</li>
<li>Milk</li>
<li>Salt</li>
<li>Preservatives</li>
<li>pH Regulators</li>
<li>Antioxidants</li>
<li>Emulsion Preparation</li>
<li>Preparation of the Fatty</li>
<li>Phase</li>
<li>Preparation of Aqueous</li>
<li>Phase</li>
<li>Water and Brine</li>
<li>Sugar</li>
<li>Matured Milk</li>
<li>Acidity Regulator</li>
<li>Final Emulsion</li>
<li>Diverse Processes of Manufacture</li>
<li>Semi-Continuous</li>
<li>Processes or Proces-</li>
<li>ses on Drum</li>
<li>The Traditional Processes Represented by the</li>
<li>System of Tubular</li>
<li>Cooling and Scraped Surface</li>
<li>VOTATOR Process</li>
<li>The Perfector System</li>
<li>Conditioning</li>
<li>Quality Control</li>
<li>Control During Manufacture</li>
<li>Control of the Fat Phase</li>
<li>Salt and Sugar</li>
<li>Testing the Finished</li>
<li>Product</li>
<li>Testing the Water Content</li>
<li>Testing Weight of Bricks</li>
<li>Salt Content</li>
<li>Content of Air and Occluded Gases</li>
<li>pH Measurement</li>
<li>Measurement of Hardness</li>
<li>Other Tests</li>
<li>Organoleptic Quality</li>
<li>Bacteriological Control</li>
<li>Packaging Checks</li>
<li>Oil Emulsions in Water</li>
<li>Emulsions</li>
<li>Physical Stability</li>
<li>Sedimentation or Creaming</li>
<li>Floculation or Coagulation</li>
<li>Coalescence or Rupture of Emulsion</li>
<li>Bacteriological Stability</li>
<li>Organoleptic Stability</li>
<li>Mayonnaise</li>
<li>Definition</li>
<li>Raw Materials Used</li>
<li>Oil</li>
<li>Egg yolk</li>
<li>Mustard</li>
<li>Vinegar</li>
<li>Other Ingredients</li>
<li>Additives and Aromas</li>
<li>Formulation</li>
<li>Production</li>
<li>Discontinuous Production</li>
<li>Quality Control</li>
<li>Mayonnaise</li>
<li>Raw Materials</li>
<li>Packaging</li>
<li>Sauces</li>
<li>Variety Sauces</li>
<li>Bearnaise Sauce</li>
<li>Tartar Sauce</li>
<li>Burgundy Sauce</li>
<li>Ailloli Sauce</li>
<li>Salad Sauces</li>
<li>Vinegar</li>
</ul>
<p><strong>Production of Neat Soap with 63% Fatty Acids</strong></p>
<ul>
<li>Saponification Reaction</li>
<li>Batch Process</li>
<li>Equipment</li>
<li>Saponification</li>
<li>Washing</li>
<li>Fitting</li>
<li>Continuous Processes</li>
<li>Sharples Process</li>
<li>Monsavon Process</li>
<li>Alfa-Laval Process</li>
<li>Saponification</li>
<li>Mazzoni Process</li>
<li>Washing cycles</li>
<li>Latest Developments in Processes</li>
<li>Other Processes</li>
<li>Soap from Fatty Acids</li>
<li>Methyl Ester Soap</li>
<li>Miscellaneous Processes</li>
<li>Drying and Finishing of Soap</li>
<li>Drying of Household Soaps</li>
<li>Drying of Toilet Soap</li>
<li>Finishing of Toilet Soap</li>
<li>Wrapping and Packaging</li>
<li>Glycerine Recovery</li>
<li>Lye Processing</li>
<li>Concentration</li>
<li>Distillation</li>
<li>Bleaching</li>
</ul>
<p><strong>Oilseed Processing Technology</strong></p>
<ul>
<li>Importance of fats and oils</li>
<li>Availability of edible oils</li>
<li>Traditional oil processing</li>
<li>Ghani technology</li>
<li>Crushing oilseeds</li>
<li>Oil yield</li>
<li>Evolution of oil</li>
<li>processing</li>
<li>Advantages and disadvantages of ghani crushing</li>
<li>Authenticity of edible oils</li>
<li>Olive oil</li>
<li>Purity criteria</li>
<li>Free Fatty Acid</li>
<li>Content (FFA)</li>
<li>Peroxide Value (PV)</li>
<li>Specific Extinction (SE)</li>
<li>Fatty Acid Composition</li>
<li>Sterol Composition</li>
<li>Codex standards to combat fraud</li>
<li>Future developments</li>
<li>Recommendations on</li>
<li>Fats and Oils in Human Nutrition</li>
<li>Minimum Desirable</li>
<li>Intakes for Adults</li>
<li>Recommendations</li>
<li>Minimum desirable intakes for infants and young children</li>
<li>Recommendations</li>
<li>Upper limits of dietary fat and oil intakes</li>
<li>Recommendations</li>
<li>Saturated and unsaturated fatty acids and cholesterol</li>
<li>Recommendations</li>
<li>Isomeric fatty acids</li>
<li>Recommendations</li>
<li>Substances associated with fats and oils</li>
<li>Recommendations</li>
<li>Essential fatty acids</li>
<li>Recommendations</li>
<li>Dietary information and programme needs</li>
<li>Recommendations</li>
</ul>
<p>The post <a href="https://projectreports.eiriindia.org/product/technology-oilseeds-processing-oils-fats-refining/">Technology Book of Oilseeds Processing, Oils &#038; Fats and Refining</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
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		<title>MINI OIL PLANT SUITABLE FOR GROUNDNUT OIL AND COTTON SEED OIL</title>
		<link>https://projectreports.eiriindia.org/product/mini-oil-plant-suitable-groundnut-oil-cotton-seed-oil/</link>
		
		<dc:creator><![CDATA[EIRI Team]]></dc:creator>
		<pubDate>Tue, 22 Oct 2013 01:17:04 +0000</pubDate>
				<guid isPermaLink="false">http://projectreports.eiriindia.org/?post_type=product&#038;p=158</guid>

					<description><![CDATA[<p>Ground Nut Powder otherwise known as peanut oil, arachis oil, or earthnut oil, is one of the two or three most important edible Oils in (oil content 45-55%) of the plant arachis hypogaea,which is grown in large quantities is Africa, India and china. The oil is pate yellow and has the characteristic order and flavour of peanuts. Compared with other seed oils, particularly cottonseed oil, it is relatively free of phosphatides and nonoil constituents. Groundnut oil is used mainly for edible purposes in the preparation of shortenings, margarine, and mayonnaise and as a cooking and salad oil of pharmaceutical quality is obtained from the seed by cold expression. The B.P recommends its use as a substitute for olive oil in making ointments, liniment its, plasters and soaps. Its use is authorized in preparations such as solutions of vitamin A and D Groundnut oil is considered to be an aperients and an emollient. In veterinary medicine, it is used as a nutritive laxative and emollient. It has been employed in the form of an emulsion for the control of several insect pests of plants.</p>
<p><strong>DETAILED FEASIBILITY REPORT COVERS:</strong></p>
<ul>
<li>Introduction</li>
<li>Uses and Applications</li>
<li>Properties</li>
<li>Market Survey with future aspects</li>
<li>Present Manufacturers</li>
<li>B.I.S. Specifications</li>
<li>Manufacturing Process with Formulae</li>
<li>Plant Layout</li>
<li>Cost Economics with Profitability Analysis</li>
<li>Capacity</li>
<li>Land &#38; Building Requirements with Rates</li>
<li>List &#38; Details of Plant and Machinery with their Costs</li>
<li>Raw Materials</li>
<li>Details/List and Costs</li>
<li>Power &#38; Water Requirements</li>
<li>Labour/Staff Requirements</li>
<li>Utilities and Overheads</li>
<li>Total Capital Investment</li>
<li>Turnover</li>
<li>Cost of Production</li>
<li>Break Even Point</li>
<li>Profitability</li>
<li>Land Man Ratio</li>
<li>Suppliers of Plant &#38; Machineries and Raw Materials.</li>
</ul>
<p>The post <a href="https://projectreports.eiriindia.org/product/mini-oil-plant-suitable-groundnut-oil-cotton-seed-oil/">MINI OIL PLANT SUITABLE FOR GROUNDNUT OIL AND COTTON SEED OIL</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
]]></description>
										<content:encoded><![CDATA[<p>The post <a href="https://projectreports.eiriindia.org/product/mini-oil-plant-suitable-groundnut-oil-cotton-seed-oil/">MINI OIL PLANT SUITABLE FOR GROUNDNUT OIL AND COTTON SEED OIL</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
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		<title>Solvent extraction plant of cotton seed</title>
		<link>https://projectreports.eiriindia.org/product/solvent-extraction-plant-cotton-seed/</link>
		
		<dc:creator><![CDATA[EIRI Team]]></dc:creator>
		<pubDate>Thu, 10 Oct 2013 11:06:24 +0000</pubDate>
				<guid isPermaLink="false">http://projectreports.eiriindia.org/?post_type=product&#038;p=115</guid>

					<description><![CDATA[<p>Cotton, the king of natural fibres is mainly cultivated for its Lint which is the most sought after textile fibre till date due To its inherent ecofriendly and comfort characteristics. It is Also one of the important cash crops of many of the afro-asian Countries like india, iran, egypt, sudan, uzbekistan, tanzania, Etc. And plays a major role in their economic development. However, of late, cotton cultivation in general and especially in These countries is becoming non-remunerative on account of higher Cost of inputs by way of plant protection measures, low Productivity in rain fed cultivation, etc. As a result, The cultivators are not able to get adequate returns Commensurate with their inputs. Hence, there is an urgent need to Explore alternative means of increasing the returns from cotton Farming. While efficient use of available resources, good quality Seeds, organic cultivation, transgenic cotton etc. Could reduce The cost of cultivation and enhance productivity, a judicious Approach to promote the use of by-products from cotton Cultivation through value addition route offers an attractive Proposition to generate additional income to the farming Community and the industries. Cotton is one of the most important Commercial crops of india and is the single largest natural Source of fibre. It plays a dominant role in its agrarian and Industrial economy as the backbone of textile industry, which Consumes 70% of the country's total fibre produced.</p>
<p><strong>Project Report covers:</strong></p>
<ul>
<li>Introduction</li>
<li>Uses and Applications</li>
<li>Properties</li>
<li>Market Survey with future aspects</li>
<li>Present Manufacturers</li>
<li>B.I.S. Specifications</li>
<li>Manufacturing Process with Formulae</li>
<li>Plant Layout</li>
<li>Cost Economics with Profitability Analysis</li>
<li>Capacity</li>
<li>Land &#38; Building Requirements with Rates</li>
<li>List &#38; Details of Plant and Machinery with their Costs</li>
<li>Raw Materials</li>
<li>Details/List and Costs</li>
<li>Power &#38; Water Requirements</li>
<li>Labour/Staff Requirements</li>
<li>Utilities and Overheads</li>
<li>Total Capital Investment</li>
<li>Turnover</li>
<li>Cost of Production</li>
<li>Break Even Point</li>
<li>Profitability</li>
<li>Land Man Ratio</li>
<li>Suppliers of Plant &#38; Machineries and Raw Materials.</li>
</ul>
<p>The post <a href="https://projectreports.eiriindia.org/product/solvent-extraction-plant-cotton-seed/">Solvent extraction plant of cotton seed</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
]]></description>
										<content:encoded><![CDATA[<p>The post <a href="https://projectreports.eiriindia.org/product/solvent-extraction-plant-cotton-seed/">Solvent extraction plant of cotton seed</a> appeared first on <a href="https://projectreports.eiriindia.org">EIRI - eBooks and Project Reports</a>.</p>
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