This presentation summarizes coagulation and flocculation techniques used in water treatment. Coagulation involves adding chemicals like alum to destabilize colloidal particles in water. Flocculation then aggregates these micro-flocs into larger macro-flocs that are easier to remove by settling. Jar tests are used to determine the optimum pH and coagulant dose. Various mixers like paddles and turbines are used for flocculation to induce velocity gradients and differential settling of the flocs.
areation and types of aeration in waste water treatmentAmi jasani
this presentation shows the aeration process among the whole process of waste water treatment. It is related to diploma civil engineering students of GTU.
areation and types of aeration in waste water treatmentAmi jasani
this presentation shows the aeration process among the whole process of waste water treatment. It is related to diploma civil engineering students of GTU.
Download PPT by clicking on following link
http://pharmastuff.blogspot.com/2018/07/spherical-crystallization-ppt.html
Spherical crystallization is a particle design technique, by which crystallization and agglomeration can be carried out simultaneously in one step.
Improves flowability and compressibility.
Crystalline forms of a drug to be converted into different polymorphic form having better bioavailability.
For masking of the bitter taste of drug.
General guide lines for the spherical agglomeration of drugs
Chow et al postulated some general guide lines for the spherical agglomeration of drugs
• For compounds that are water soluble, a water-immiscible organic solvent is used as the external medium and salt solutions of high concentration without common ions can be used as the bridging liquid.
• For compounds that are soluble in one or more organic solvents water is employed as the external phase and a water-immiscible organic solvent as the bridging liquid.
For compounds that are only soluble in water-miscible organic solvents a saturated aqueous solution of the compound can serve as the external phase and an organic solvent mixture as the bridging solvent.
• For compounds that are insoluble in water or any organic solvents a water-immiscible organic solvent can act as the external phase and a 20% calcium chloride solution as the bridging liquid. In addition, a binding agent such as PVP or PEG is required for agglomeration since the powders are not sufficiently soluble in the bridging liquids to allow binding through recrystallization and fusion.
Concerned with the coagulation-flocculation-settling removal of colloidal and suspended solids.
Coagulation and flocculation is explained, and coagulating and flocculating agents and their functioning is described.
Design of different units including the clari-flocculator associated with the coagulation-flocculation-settling process is described.
Conducting a settling column test, plotting settling profile graph and using the settling profile graph in the design of a clarifier is described.
NUMERICAL SIMULATIONS OF HEAT AND MASS TRANSFER IN CONDENSING HEAT EXCHANGERS...ssuser7dcef0
Power plants release a large amount of water vapor into the
atmosphere through the stack. The flue gas can be a potential
source for obtaining much needed cooling water for a power
plant. If a power plant could recover and reuse a portion of this
moisture, it could reduce its total cooling water intake
requirement. One of the most practical way to recover water
from flue gas is to use a condensing heat exchanger. The power
plant could also recover latent heat due to condensation as well
as sensible heat due to lowering the flue gas exit temperature.
Additionally, harmful acids released from the stack can be
reduced in a condensing heat exchanger by acid condensation. reduced in a condensing heat exchanger by acid condensation.
Condensation of vapors in flue gas is a complicated
phenomenon since heat and mass transfer of water vapor and
various acids simultaneously occur in the presence of noncondensable
gases such as nitrogen and oxygen. Design of a
condenser depends on the knowledge and understanding of the
heat and mass transfer processes. A computer program for
numerical simulations of water (H2O) and sulfuric acid (H2SO4)
condensation in a flue gas condensing heat exchanger was
developed using MATLAB. Governing equations based on
mass and energy balances for the system were derived to
predict variables such as flue gas exit temperature, cooling
water outlet temperature, mole fraction and condensation rates
of water and sulfuric acid vapors. The equations were solved
using an iterative solution technique with calculations of heat
and mass transfer coefficients and physical properties.
Forklift Classes Overview by Intella PartsIntella Parts
Discover the different forklift classes and their specific applications. Learn how to choose the right forklift for your needs to ensure safety, efficiency, and compliance in your operations.
For more technical information, visit our website https://intellaparts.com
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Cosmetic shop management system project report.pdfKamal Acharya
Buying new cosmetic products is difficult. It can even be scary for those who have sensitive skin and are prone to skin trouble. The information needed to alleviate this problem is on the back of each product, but it's thought to interpret those ingredient lists unless you have a background in chemistry.
Instead of buying and hoping for the best, we can use data science to help us predict which products may be good fits for us. It includes various function programs to do the above mentioned tasks.
Data file handling has been effectively used in the program.
The automated cosmetic shop management system should deal with the automation of general workflow and administration process of the shop. The main processes of the system focus on customer's request where the system is able to search the most appropriate products and deliver it to the customers. It should help the employees to quickly identify the list of cosmetic product that have reached the minimum quantity and also keep a track of expired date for each cosmetic product. It should help the employees to find the rack number in which the product is placed.It is also Faster and more efficient way.
6th International Conference on Machine Learning & Applications (CMLA 2024)ClaraZara1
6th International Conference on Machine Learning & Applications (CMLA 2024) will provide an excellent international forum for sharing knowledge and results in theory, methodology and applications of on Machine Learning & Applications.
Hierarchical Digital Twin of a Naval Power SystemKerry Sado
A hierarchical digital twin of a Naval DC power system has been developed and experimentally verified. Similar to other state-of-the-art digital twins, this technology creates a digital replica of the physical system executed in real-time or faster, which can modify hardware controls. However, its advantage stems from distributing computational efforts by utilizing a hierarchical structure composed of lower-level digital twin blocks and a higher-level system digital twin. Each digital twin block is associated with a physical subsystem of the hardware and communicates with a singular system digital twin, which creates a system-level response. By extracting information from each level of the hierarchy, power system controls of the hardware were reconfigured autonomously. This hierarchical digital twin development offers several advantages over other digital twins, particularly in the field of naval power systems. The hierarchical structure allows for greater computational efficiency and scalability while the ability to autonomously reconfigure hardware controls offers increased flexibility and responsiveness. The hierarchical decomposition and models utilized were well aligned with the physical twin, as indicated by the maximum deviations between the developed digital twin hierarchy and the hardware.
2. Outlines
Purpose of Techniques
Coagulation
Coagulants
Selection of Coagulant
Amount of Coagulant
Flocculation
Types of Flocculation
Flocculation Mixers
Conclusion
2
3. Purpose
Settling of stabilized particles
Destabilization of colloidal particles
Increase the density of colloidal particles
Reduction in repulsive forces between
particles
Diminish the turbidity of water
3
4. Coagulation
Coagulation is the destabilization of colloidal
and fine suspended solids by adding a chemical
coagulant such as alum in the water.
Neutralization of negatively charged particles
Micro-flocs formation
4
+
Coagulant
Coagulation
Tank
Destabilization
of colloids
7. Selection of Coagulant
A coagulant is selected on the basis of:
Type of Coagulant (anionic, cationic)
Molecular Weight (high)
Charge Density (high)
Toxicity (non toxic)
Solubility (insoluble in neutral pH range)
7
8. Type of Coagulant
Cationic:
In the process of coagulation
Positively charged coagulant
Anionic:
In the process of flocculation
Negatively charged coagulant used as
flocculent
8
10. Jar Test
Jar test is a laboratory procedure to determine
the optimum pH and the optimum coagulant
dose
A jar test simulates the coagulation and
flocculation processes
Fill the jars with raw water sample (500 or
1000 mL), usually 6 jars
10
Determination of optimum pH:
11. Jar Test - Optimum pH
Adjust pH of the jars while mixing using
H2SO4 or NaOH/lime (pH: 5.0; 5.5; 6.0; 6.5;
7.0; 7.5)
Add same dose of the selected coagulant (alum
or iron) to each jar (coagulant dose: 5 or 10
mg/L)
Rapid mix each jar at 100 to 150 rpm for 1
minute. The rapid mix helps to disperse the
coagulant throughout each container
11
12. Jar Test - Optimum pH
Reduce the stirring speed to 25 to 30 rpm and
continue mixing for 15 to 20 mins. This slower
mixing speed helps to promote flocs formation
by enhancing particle collisions, which lead to
larger flocs
Turn off the mixers and allow flocs to settle for
30 to 45 mins
Measure the final residual turbidity in each jar
Plot residual turbidity against pH
12
13. Jar Test - Optimum pH
13Optimum pH: 6.3
0
5
10
15
20
4.5 5 5.5 6 6.5 7 7.5 8
TurbidityRemaining
pH
Graph b/w Turbidity Remaining and pH
14. Jar Test - Optimum Dose
Optimum coagulant dose:
Repeat all the previous steps
This time adjust pH of all jars at optimum (6.3
found from first test) while mixing using
H2SO4 or NaOH/lime
Add different doses of the selected coagulant to
each jar
(Coagulant dose: 5; 7; 10; 12; 15; 20 mg/L)
14
15. Jar Test - Optimum Dose
Rapid mix each jar at 100 to 150 rpm for 1
minute. The rapid mix helps to disperse the
coagulant throughout each container. Reduce
the stirring speed to 25 to 30 rpm for 15 to 20
mins
Turn off the mixers and allow flocs to settle for
30 to 45 mins
Then measure the final residual turbidity in
each jar
Plot residual turbidity against coagulant dose 15
17. Flocculation
Flocculation is the aggregation of micro-flocs
into macro-flocs to enhance their settling by
gravity sedimentation.
Anions are used as bridging media between
micro-flocs.
+ Flocculent
17
Micro-flocs Macro-flocs
….
20. Types of Flocculation
Micro Flocculation
Macro Flocculation
Micro Flocculation:
Due to random motion of fluid molecules
Size range from 0.001 to about 1 µm
20
Randomly Moving Molecules Flocs Formation
21. Types of Flocculation
Macro Flocculation:
Size greater than 1 µm
21
Macro Flocculation
Induced Velocity
Gradients
Differential
Settling
22. Induced Velocity Gradients
Due to change in velocity of particles
Fast moving particles overtake slow moving
particles
Large particle formation due to stickiness of
particles
22
L.P
S.P
Flocs Formation
23. Differential Settling
Large particles overtake small particles
Settling through gravity
23
L.P
S.P
Flocs Formation
25. Hydraulic Flocculation
25
Due to the flow of water
Horizontally Baffled Tank
Vertically Baffled Tank
Horizontally Baffled Tank:
H2O
H2O
Horizontally Baffled Tank
Baffle
27. Types of Flocculation Mixers
Following are the types of flocculation mixers:
Static Mixer
Paddle Mixer
Turbine Mixer
Static Mixer:
Static vanes or baffles for mixing
Water passes through vanes or baffles
Horizontally baffled tank (slide no. 25) 27
30. Conclusion
A coagulant is necessary to destabilize the
stable impurities of water
Flocculation is necessary to develop the macro-
flocs of impurities that are settled down easily
30
31. References
Wastewater Engineering Treatment by Metcalf
Eddy
Water and Waste Water Engineering by
Mackenzie L. Davis
Unit Operations and Processes in
Environmental Engineering
31