The document discusses various phytochemical processing techniques including extraction, purification, and case studies. It provides charts classifying extraction methods based on solvent polarity and examples of raw herbal materials. Case studies examine specific processes for producing products like cinnamon oil, tongkat ali extract, soybean powder, curcuminoid, stevia sugar, and pegaga powder.
method to separate compounds based on their relative solubilities in two different immiscible liquids, usually water and an organic solvent. It is an extraction of a substance from one liquid into another liquid phase.
method to separate compounds based on their relative solubilities in two different immiscible liquids, usually water and an organic solvent. It is an extraction of a substance from one liquid into another liquid phase.
Different methods of extraction of essential oilChetanChauhan123
all about the different methods of oil extraction classical and modern extraction method on the basis of review and research paper by chetan kumar chauhan
introduction, theory of drying, applications of drying, construction & working about fluidised bed dryer,use of tray dryer,construction about vacuum dryer, construction & working about drum dryer, construction about spray dryer
This presentation comprehensively tells about not only the classical methods of extraction but also the modern methods by which herbal products can be easily and efficiently extracted for further use in isolation and formulation
Cloves are the aromatic flower buds of a tree in the family Myrtaceae, Syzygium aromaticum. They are native to the Maluku Islands in Indonesia, and are commonly used as a spice. Cloves are commercially harvested primarily in Indonesia, India, Madagascar, Zanzibar, Pakistan, Sri Lanka and Tanzania.
We Provide Amla juice,Herbal Amla juice,Ayurvedic Piles management kit, Herbal product for total piles control, Indian herbs for Men's health, Ayurvedic medicine for Men's stamina, Herbal Micro Nutrition, Herbal Green Food Supplement, Herbal Unique Cuisine Hing, Indian herbs for eye care, Herbal Best Care For Eye Care, Herbal health digestion video, Herbal Joint pain Oil kit
The project was a study based report on the RAN evolution path of 2.5G EDGE Networks to HSDPA. HSDPA is a 3.5G wireless cellular system, a cost-efficient upgrade to UMTS systems and promises to deliver performance comparable to today’s wireless LAN services, but with the added benefit of mobility and ubiquitous coverage. It can offer data rates of up to 14.4 Mbps which is far beyond what 2.5G and 3G cellular systems could offer. The project focuses on a two-step upgrade, first from GSM towards the deployment of UMTS/WCDMA and then towards HSDPA. It begins a new era of “Mobile broadband” services and faces competition from “WiMAX” – but with GSM services having an obvious upgrade path to WCDMA, HSDPA seems to be leading the market in several parts of the world. HSDPA is an extremely cost-effective path to higher data rates and provides more efficient use of valuable spectrum. It enables operators to compete effectively in increasingly converged markets and satisfy the need for enhanced QoS in an efficient and cost-effective manner.
Different methods of extraction of essential oilChetanChauhan123
all about the different methods of oil extraction classical and modern extraction method on the basis of review and research paper by chetan kumar chauhan
introduction, theory of drying, applications of drying, construction & working about fluidised bed dryer,use of tray dryer,construction about vacuum dryer, construction & working about drum dryer, construction about spray dryer
This presentation comprehensively tells about not only the classical methods of extraction but also the modern methods by which herbal products can be easily and efficiently extracted for further use in isolation and formulation
Cloves are the aromatic flower buds of a tree in the family Myrtaceae, Syzygium aromaticum. They are native to the Maluku Islands in Indonesia, and are commonly used as a spice. Cloves are commercially harvested primarily in Indonesia, India, Madagascar, Zanzibar, Pakistan, Sri Lanka and Tanzania.
We Provide Amla juice,Herbal Amla juice,Ayurvedic Piles management kit, Herbal product for total piles control, Indian herbs for Men's health, Ayurvedic medicine for Men's stamina, Herbal Micro Nutrition, Herbal Green Food Supplement, Herbal Unique Cuisine Hing, Indian herbs for eye care, Herbal Best Care For Eye Care, Herbal health digestion video, Herbal Joint pain Oil kit
The project was a study based report on the RAN evolution path of 2.5G EDGE Networks to HSDPA. HSDPA is a 3.5G wireless cellular system, a cost-efficient upgrade to UMTS systems and promises to deliver performance comparable to today’s wireless LAN services, but with the added benefit of mobility and ubiquitous coverage. It can offer data rates of up to 14.4 Mbps which is far beyond what 2.5G and 3G cellular systems could offer. The project focuses on a two-step upgrade, first from GSM towards the deployment of UMTS/WCDMA and then towards HSDPA. It begins a new era of “Mobile broadband” services and faces competition from “WiMAX” – but with GSM services having an obvious upgrade path to WCDMA, HSDPA seems to be leading the market in several parts of the world. HSDPA is an extremely cost-effective path to higher data rates and provides more efficient use of valuable spectrum. It enables operators to compete effectively in increasingly converged markets and satisfy the need for enhanced QoS in an efficient and cost-effective manner.
Biofuel from Algae for future use (Lipid extraction)Pravin clap
Lipid Extraction from algae Bio fuel production for future use
Submitted by,
Ahamed Nashath A, Pravin C, Vishak P
Research Guide. Dr. Helen sheeba, Department of Microbiology, Scott Christian College, Nagercoil
May 2023 Project thesis submitted to Scott Christian College (Autonomous) In partial fulfillment of the degree of Bachelor of Science in Microbiology
Increasing global demand for fuels and the consequent increases in environmental pollution and human health risks have collectively driven research toward finding sustainable and economically viable alternatives. The third-generation biofuels have been considered as promising strategies for meeting this goal.
Algae are chlorophyll-containing photosynthetic organisms found everywhere on the earth, such as in the sea, rivers, lakes, soil, in animal, and plants. Algae represent a potential biomass to be explored as a source to develop biofuel because algal biomass is abundant, fast-growing, and unexploited resource often left to decompose on the shores posing waste problems. High percentage of lipids and carbohydrates make algae an excellent candidate for the synthesis of biofuel.
Algae are an economical choice for biodiesel production, because of its availability and low cost. Our results prove that biodiesel can be produced from macroalgae. In this way algae can be used as renewable energy. Many researchers reported that microalgae might better for higher biodiesel production.
Biofuels are liquid or gaseous fuels primarily produced from biomass, and can be used to replace or can be used in addition to diesel, petrol or other fossil fuels for transport, stationary, portable and other applications. Crops used to make biofuels are generally either high in sugar (such as sugarcane, sugarbeet, and sweet sorghum), starch (such as maize and tapioca) or oils (such as soybean, rapeseed, coconut, sunflower).
Biodiesel is a clean-burning diesel fuel produced from vegetable oils, animal fats, or grease. Its chemical structure is that of fatty acid alkyl esters (FAAE). Biodiesel as a fuel gives much lower toxic air emissions than fossil diesel. In addition, it gives cleaner burning and has less sulfur content, and thus reducing emissions. Because of its origin from renewable resources, it is more likely that it competes with petroleum products in the future.
The benefits of using biodiesel are as follows,
Algae is a economical choice for Biodiesel
It reduce vehicle emission which makes it eco-friendly.
It is made from renewable sources and can be prepared locally.
It has excellent lubricity.
Increased safety in storage and transport because the fuel is nontoxic and bio degradable (Storage, high flash pt)
Production of bio diesel in India will reduce dependence on foreign suppliers, thus helpful in price stability.
Reduction of greenhouse gases at least by 3.3 kg CO2 equivalent per kg of biodiesel.
Thank you for viewing and reading 😊
Extraction of Essential Oil from Neem Seed by Using Soxhlet Extraction MethodsIJAEMSJORNAL
Extraction of essential neem oil from neem seed was carried by soxhelt extraction method using different organic solvents and parameters. Physico-chemical property of the extracted oil was also determined by using classical wet chemical method. Result revealed that, soxhlet extraction using hexane has 40.35%; using ethanol-hexane mixture of 60:40% volume proportion has 43.71%, using ethanol 42.65% and using methanol 42.89%. For all solvent type particle size has 355μm, extraction time 1hr up to 3hrs and applied constant and varies temperatures .At smaller extraction time, hexane produced oil yield greater than from ethanol and methanol. Actually, ethanol not produced oil at one hour extraction time. Thus, by effective determination of factors like particle sizes, solvent type, temperature, and time it is possible to investigate the result on the quality and quantity of neem oil. Surprisingly, mixtures of Ethanol and Hexane gave admirable results. Predominantly, ethanol-hexane mixtures of 60:40, and 40:60% (volume proportions) gave better oil yields of 44%, and 41.2% respectively than that of hexane (40.35%) at 3 hours of process time.
dairy plant operations like Preparation of pasteurised milk, SMP, ETP or waste treatment in dairy plant. This is about concerned dairy plant OMFED, Odisha.
En el marco de la jornada Microalgas, ¿una fuente de petróleo verde?, organizada con IMDEA y celebrada el 8 de abril en EOI, Escuela de Organización Industrial, Emilio Molina Grima, de la Universidad de Almería, presenta como han llegado a un proceso eficiente de producción en laboratorio de aceite de algas.
8_04_2010
Alcoholic fermentation, also referred to as, Ethanol fermentation, is a biological process in which sugars such as glucose, fructose, and sucrose are converted into cellular energy and thereby produce ethanol and carbon dioxide as metabolic waste products. Because yeasts perform this conversion in the absence of oxygen ethanol fermentation is classified as anaerobic.
India Orthopedic Devices Market: Unlocking Growth Secrets, Trends and Develop...Kumar Satyam
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Sustainability has become an increasingly critical topic as the world recognizes the need to protect our planet and its resources for future generations. Sustainability means meeting our current needs without compromising the ability of future generations to meet theirs. It involves long-term planning and consideration of the consequences of our actions. The goal is to create strategies that ensure the long-term viability of People, Planet, and Profit.
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Phytochemical Processing
1. PHYTOCHEMICAL PROCESSING SAIFUL IRWAN ZUBAIRI PMIFT, Grad B.E.M. B. Eng. (Chemical-Bioprocess) (Hons.), UTM M. Eng. (Bioprocess), UTM ROOM NO.: 2166, CHEMISTRY BUILDING, TEL. (OFF.): 03-89215828, FOOD SCIENCE PROGRAMME, CENTRE OF CHEMICAL SCIENCES AND FOOD TECHNOLOGY, UKM BANGI, SELANGOR
2.
3. Chart of Classification and Separation of Plant Material Based on Solvent Polarity and Process (Phytochemicals Approach) Plant Material H2O-Glycerol Extraction Non-Polar compound extraction SFE (Phytonics: Phytosol) Terpenoids Essential Oil (e.g. mono & Esquiterpenes: geraniol, limonese Diterpenoids (Phytol, abietic acid) Triterpenoids (Cucurbitacin) Carotenoids ( β-Carotene, lutien, Zeaxanthin, etc) Multi Solvent Extraction Process Terpenoids (e.g. Menthol, carrone, squalene, α-Carotene, lycopene) Lipids Polar Compound Extraction Flavanoid (e.g. anthocyanin-cyanidin, flavanols- Kaemferol, isoflavanoid-rotenone) Polar alkaloid (e.g. Ephedrine) Sugar & Derivatives (e.g. monosacharide, Oligosacharide, sugar alcol) Fiber Acid Hydrolysis filtrate Cellulose filtrate Hemicellulose filtrate Lignin
4. Chart of Classification and Separation of Plant Material Based on Solvent Polarity and Process (Herbal Approach) Plant Material Solvent Extract filtrate Freeze dried Whole concrete extract Membrane Filtration or Low T vacuum evaporation Whole concentrate extract Water Extract Spray dried Whole powder extract Freeze dried Whole freeze dried extract Spray dried Concentrate extract
5. EXAMPLES OF RAW MATERIALS TEA TREE PANDAN CITRONELLA EUCALYPTUS CINNAMON KESUM CURRY TONGKAT ALI
18. CASE STUDY I: Production of Cinnamon Oil from Cinnamon Leaves Process Flow Chart for Crude Cinnamon Oil Production Cinnamon Leaves Drying Size Reduction Extraction ( Apply heat & agitation) Condensation Product (Crude Essential Oil) Deionized Water Steam is formed carrying along essential oil
19. Process Flow Chart for Crude Cinnamon Oil Purification Crude Essential Oil Neutralization (pH Control) Separation (centrifuge) Other method: clarifying, purifying and decanting Product (Essential Oil) Distillation (using laboratory set) Solvent Solubility (add solvent) Evaporation CASE STUDY I: Production of Cinnamon Oil from Cinnamon Leaves
20. C Cinnamon Leaf (1000 kg) 1000 kg COARSE GRINDER Deionized water (5000 kg) Condensation Rate : 700 kg/hr Water Oil (15%) Oil (85%) Leaf + 30% water Water + Oil 1 L 0.5 M NaOH 26 L Cinnamon Oil C Soap Purified Cinnamon Oil (25 L) CASE STUDY I: Production of Cinnamon Oil from Cinnamon Leaves
21. CASE STUDY II: Production of Phyto-Extract from Tongkat Ali Process Flow Chart for Herb Processing – Tongkat Ali Tongkat Ali Sizing (Grinding)/Drying Extraction Filtration Product (Concentrate Extract) Packaging Solvent (Deionized Water) Spray Dryer (other product intensification method can also be used - freeze drying) Concentrate Product (Powdered Form) EXTRACTION
22. CASE STUDY II: Production of Phyto-Extract from Tongkat Ali Deionized Water (120kg) T = 120 O C t = 2 Hr Extract + fibre (40kg) Slurry Water Extract T feed = 70 O C 1.5 brix FILTER efficiency = 56% EXTRACTOR SPRAY DRYER efficiency = 80% Hot Air 306 kg/hr T = 170 O C T 1 = 170 O C T 2 = 103 O C Evaporation Rate = 12.6 kg/hr Recovery = 3% Moisture content = 2% t = 7 hrs HOLDING TANK Temperature = 70 0 C Tongkat Ali (40kg)
23. CASE STUDY III: Production of Soybean Powder Soy bean Soak (24 hrs) Dehulling Wet Grinding (Soy: Water 1:4) Soy Extract Product Solvent (Deionized Water) Filtration Spray Dry T = 90 0 C, t = 1 hr 5% Maltodextrin, 1% Sodium Casienate
24. Dehulling 1000 kg Soy 4000 kg Deionized water Soy Fiber 4000 kg extract 200 kg Maltodextrin 40 kg Sodium Casienate T = 90 0 C t = 1 hr 2420 kg Soy Solution 2 brix T 1 = 185 0 C T 2 = 105 0 C Hot Air Feed (2300 kg/ hr) t = 24 hrs Evaporation Rate = 100 kg/ hr Product Flow Rate = 20.16 kg / hr Recovery = 20 % Moisture content = 2 % CASE STUDY III: Production of Soybean Powder Wet Grinding Filter Press
25. CASE STUDY IV: Extraction of Oleoresin (Curcuminoid) from Turmeric Process Flow Chart for Production of Cucurminoid Turmeric Sizing & Drying Steam Distillation Wet Turmeric Fine Grinding Crystallization Solvent (Deionized Water) Drying Vacuum Distillation Volatile Oil Product (Curcuminoid) Packaging Ethanol
26. CASE STUDY IV:Extraction of Oleoresin (Curcuminoid) from Turmeric Coarse Grinder Fine Grinder 1000 Kg Turmeric 5000 kg Dioinized water Evaporation Rate: 833 kg/hr 4200 kg water + volatile Oil Water 20 kg volatile oil 70% Water 600 kg fine turmeric 800 kg water + 1000 kg turmeric DRYER VACUUM DISTILLATION UNIT STEAM DISTILLATION UNIT OIL SEPARATOR OIL STORAGE Volatile Oil Packaging CRYSTALLIZER 24 Kg Curcuminoid FILTER UNIT EXTRACTION VESSEL
27. Raw Material Sizing (Grinding)/Drying Extraction Filtration Ultrafiltration Spray Dryer Solvent (Deionized Water) Microfiltration Reverse Osmosis PURIFICATION CASE STUDY V: Production of Plant-Based Sugar from Stevia Product (Stevioside: 66%) T = 100 0 C, t = 2 hrs Maltodextrin
28. CASE STUDY V: Production of Plant-Based Sugar from Stevia Sweet Tea (100kg) Deionized Water (2500kg) T = 100 O C t = 2 hrs Water Extract Water Extract (400 kg solution + 2 kg maltodextrin) T feed = 70 O C 1.5 brix EXTRACTOR SPRAY DRYER efficiency = 80% Hot Air 550kg/hr T = 170 O C T 1 = 170 O C T 2 = 103 O C Evaporation Rate = 100 kg/hr Product Flow Rate = 1.75 kg/hr Recovery = 5% Moisture content = 2% Purity = 66% t = 4 hrs PURIFICATION (microfiltration, Ultrafiltration Reverse osmosis) Impurities
29. CASE STUDY VI: Production of Pegaga Powder M EXTRACTOR M M Pegaga (cleaned and ground) Deionized Water BLENDING TANK EVAPORATOR SPRAY DRYER PLATE & FRAME FILTER T = 120 0 C t = 2 hrs T = 70 0 C Water Extract T feed = 70 O C 5 brix Hot Air 306 kg/hr T = 170 O C T 1 = 170 O C T 2 = 103 O C Recovery = 2% from raw material Moisture content = 2% max Water Process Plant Layout for the Production of Pegaga Powder
30. Pegaga Cleaning Sizing Extraction Evaporation Blending Spray Drying Packaging Dehydrated Product Figure 1: Process Flow for the Production of Pegaga Powder