The document describes an experiment on plate and frame filter press. It provides theoretical background on how filter presses work through pressure filtration. Key steps of the experiment include preparing calcium carbonate slurries at 10% and 20% concentrations and measuring filtration rate over time. Results showed filtration rate decreased with time and was slower for the higher concentration slurry due to the heavier solid requiring more time to filter. The document concludes various factors like solid properties and concentration affect filtration rate.
Episode 43 : DESIGN of Rotary Vacuum Drum Filter
Theory of Separation
Rotary vacuum drum filter (RVDF) is one of the oldest filters used in the industrial liquid-solids separation .A rotary vacuum filter consists of a large rotating drum covered by a cloth. The drum is partially immersed in liquid/solids slurry with approximately up to (25-75) % of the screen area.
As the drum rotates into and out of the trough, the slurry is sucked on the surface of the cloth and rotated out of the liquid/solids suspension as a cake. When the cake is rotating out, it is dewatered in the drying zone. The cake is dry because the vacuum drum is continuously sucking the cake and taking the water out of it. At the final step of the separation, the cake is discharged as solids products and the drum rotates continuously to another separation cycle.
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Cross Flow or Tangential Flow Membrane Filtration (TFF) to Enable High Solids...njcnews777
Cross Flow or Tangential Flow Filtration (TFF) Membrane Plants are used in Desalination, Brackish Groundwater Treatment, High Chloride Surface Water Treatment, Waste Water Treatment Plant Effluent Reuse, Biopharmaceutical, Food & Protein Applications for removal of undesired constituents and harvesting of desireable products. Cross flow membrane filtration technology has been used widely in industry globally. Filtration membranes can be polymeric or ceramic, depending upon the application. The principles of cross-flow filtration are used in reverse osmosis, nanofiltration, ultrafiltration and microfiltration. When purifying water, it can be very cost effective in comparison to the traditional evaporation methods. Techniques to improve performance of cross flow filtration include:
Backwashing: In backwashing, the transmembrane pressure is periodically inverted by the use of a secondary pump, so that permeate flows back into the feed, lifting the fouling layer.
Clean-in-place: Clean-in-place systems are typically used to remove fouling from membranes after extensive use. The CIP process may use detergents, reactive agents such as sodium hypochlorite and acids and alkalis such as citric acid and sodium hydroxide.
Concentration: The volume of the fluid is reduced by allowing permeate flow to occur. Solvent, solutes, and particles smaller than the membrane pore size pass through the membrane, while particles larger than the pore size are retained, and thereby concentrated. In bioprocessing applications, concentration may be followed by diafiltration.
Diafiltration: In order to effectively remove permeate components from the slurry, fresh solvent may be added to the feed to replace the permeate volume, at the same rate as the permeate flow rate, such that the volume in the system remains constant. This is analogous to the washing of filter cake to remove soluble components. Dilution and re-concentration is sometimes also referred to as "diafiltration."
Hahnemühle‘s Albet LabScience brand is a range of products designed for general filtration applications and complex filtration processes in life science and analytical applications in chemical and biological laboratories. The technical specifications of our membranes and syringe filters allow their use in areas where reproducibility and consistency are of major importance.
Quality
Our syringe filters undergo strict quality controls during and after production. The storage life of the finished products in the
warehouse is constantly monitored. Each filter holder undergoes the following five tests: bubble point, burst pressure, membrane absorption, flow rate and extractable substances. The range includes filter holders for the reliable separation of microorganisms and particles in liquids, air and other gases. Clear and sterile filtration, sample production, sterile aeration and medical applications are just some of the areas where disposable filter holders are typically used. They are available in different pore sizes and with different hydrophilic or hydrophobic membrane materials.
Our microfiltration range also includes membrane units. The first step towards successful analysis is choosing the right membrane unit. We offer you different membrane filters with pore sizes from 0.2 μm – 8 μm for particle removal or for the collection of the microorganisms to be examined from solutions. Various cellulose-based membranes and polymer materials cover a wide range of application areas, from clarification and sample preparation to sterile and air filtration to aeration and microbiological control. See our quick and easy to use guidelines on page 8f, which will help you to decide which product is perfect for you.
Episode 43 : DESIGN of Rotary Vacuum Drum Filter
Theory of Separation
Rotary vacuum drum filter (RVDF) is one of the oldest filters used in the industrial liquid-solids separation .A rotary vacuum filter consists of a large rotating drum covered by a cloth. The drum is partially immersed in liquid/solids slurry with approximately up to (25-75) % of the screen area.
As the drum rotates into and out of the trough, the slurry is sucked on the surface of the cloth and rotated out of the liquid/solids suspension as a cake. When the cake is rotating out, it is dewatered in the drying zone. The cake is dry because the vacuum drum is continuously sucking the cake and taking the water out of it. At the final step of the separation, the cake is discharged as solids products and the drum rotates continuously to another separation cycle.
SAJJAD KHUDHUR ABBAS
Ceo , Founder & Head of SHacademy
Chemical Engineering , Al-Muthanna University, Iraq
Oil & Gas Safety and Health Professional – OSHACADEMY
Trainer of Trainers (TOT) - Canadian Center of Human
Development
Cross Flow or Tangential Flow Membrane Filtration (TFF) to Enable High Solids...njcnews777
Cross Flow or Tangential Flow Filtration (TFF) Membrane Plants are used in Desalination, Brackish Groundwater Treatment, High Chloride Surface Water Treatment, Waste Water Treatment Plant Effluent Reuse, Biopharmaceutical, Food & Protein Applications for removal of undesired constituents and harvesting of desireable products. Cross flow membrane filtration technology has been used widely in industry globally. Filtration membranes can be polymeric or ceramic, depending upon the application. The principles of cross-flow filtration are used in reverse osmosis, nanofiltration, ultrafiltration and microfiltration. When purifying water, it can be very cost effective in comparison to the traditional evaporation methods. Techniques to improve performance of cross flow filtration include:
Backwashing: In backwashing, the transmembrane pressure is periodically inverted by the use of a secondary pump, so that permeate flows back into the feed, lifting the fouling layer.
Clean-in-place: Clean-in-place systems are typically used to remove fouling from membranes after extensive use. The CIP process may use detergents, reactive agents such as sodium hypochlorite and acids and alkalis such as citric acid and sodium hydroxide.
Concentration: The volume of the fluid is reduced by allowing permeate flow to occur. Solvent, solutes, and particles smaller than the membrane pore size pass through the membrane, while particles larger than the pore size are retained, and thereby concentrated. In bioprocessing applications, concentration may be followed by diafiltration.
Diafiltration: In order to effectively remove permeate components from the slurry, fresh solvent may be added to the feed to replace the permeate volume, at the same rate as the permeate flow rate, such that the volume in the system remains constant. This is analogous to the washing of filter cake to remove soluble components. Dilution and re-concentration is sometimes also referred to as "diafiltration."
Hahnemühle‘s Albet LabScience brand is a range of products designed for general filtration applications and complex filtration processes in life science and analytical applications in chemical and biological laboratories. The technical specifications of our membranes and syringe filters allow their use in areas where reproducibility and consistency are of major importance.
Quality
Our syringe filters undergo strict quality controls during and after production. The storage life of the finished products in the
warehouse is constantly monitored. Each filter holder undergoes the following five tests: bubble point, burst pressure, membrane absorption, flow rate and extractable substances. The range includes filter holders for the reliable separation of microorganisms and particles in liquids, air and other gases. Clear and sterile filtration, sample production, sterile aeration and medical applications are just some of the areas where disposable filter holders are typically used. They are available in different pore sizes and with different hydrophilic or hydrophobic membrane materials.
Our microfiltration range also includes membrane units. The first step towards successful analysis is choosing the right membrane unit. We offer you different membrane filters with pore sizes from 0.2 μm – 8 μm for particle removal or for the collection of the microorganisms to be examined from solutions. Various cellulose-based membranes and polymer materials cover a wide range of application areas, from clarification and sample preparation to sterile and air filtration to aeration and microbiological control. See our quick and easy to use guidelines on page 8f, which will help you to decide which product is perfect for you.
Filtration is a physical, biological or chemical operation that separates solid matter and fluid from a mixture with a filter medium that has a complex structure through which only the fluid can pass
"Membrane contactors are devices that allow a gaseous phase and a liquid phase to come into direct contact with each other, for the purpose of mass transfer between the phases, without dispersing one phase into the other.
Filtration is a physical, biological or chemical operation that separates solid matter and fluid from a mixture with a filter medium that has a complex structure through which only the fluid can pass
"Membrane contactors are devices that allow a gaseous phase and a liquid phase to come into direct contact with each other, for the purpose of mass transfer between the phases, without dispersing one phase into the other.
The studies influence techniques of filtration, its various types, and theories involved in the rate of filtration. This topic useful for physical pharmacy students and other concerned with filtration.
Filtration is commonly the mechanical or physical operation which is used for the separation of products like solids from fluids by interposing a medium through which only the fluid can pass.
Similar to Press and frame filter- Ed Ryan M. Ruales (20)
TECHNICAL TRAINING MANUAL GENERAL FAMILIARIZATION COURSEDuvanRamosGarzon1
AIRCRAFT GENERAL
The Single Aisle is the most advanced family aircraft in service today, with fly-by-wire flight controls.
The A318, A319, A320 and A321 are twin-engine subsonic medium range aircraft.
The family offers a choice of engines
Industrial Training at Shahjalal Fertilizer Company Limited (SFCL)MdTanvirMahtab2
This presentation is about the working procedure of Shahjalal Fertilizer Company Limited (SFCL). A Govt. owned Company of Bangladesh Chemical Industries Corporation under Ministry of Industries.
Student information management system project report ii.pdfKamal Acharya
Our project explains about the student management. This project mainly explains the various actions related to student details. This project shows some ease in adding, editing and deleting the student details. It also provides a less time consuming process for viewing, adding, editing and deleting the marks of the students.
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.
Hybrid optimization of pumped hydro system and solar- Engr. Abdul-Azeez.pdffxintegritypublishin
Advancements in technology unveil a myriad of electrical and electronic breakthroughs geared towards efficiently harnessing limited resources to meet human energy demands. The optimization of hybrid solar PV panels and pumped hydro energy supply systems plays a pivotal role in utilizing natural resources effectively. This initiative not only benefits humanity but also fosters environmental sustainability. The study investigated the design optimization of these hybrid systems, focusing on understanding solar radiation patterns, identifying geographical influences on solar radiation, formulating a mathematical model for system optimization, and determining the optimal configuration of PV panels and pumped hydro storage. Through a comparative analysis approach and eight weeks of data collection, the study addressed key research questions related to solar radiation patterns and optimal system design. The findings highlighted regions with heightened solar radiation levels, showcasing substantial potential for power generation and emphasizing the system's efficiency. Optimizing system design significantly boosted power generation, promoted renewable energy utilization, and enhanced energy storage capacity. The study underscored the benefits of optimizing hybrid solar PV panels and pumped hydro energy supply systems for sustainable energy usage. Optimizing the design of solar PV panels and pumped hydro energy supply systems as examined across diverse climatic conditions in a developing country, not only enhances power generation but also improves the integration of renewable energy sources and boosts energy storage capacities, particularly beneficial for less economically prosperous regions. Additionally, the study provides valuable insights for advancing energy research in economically viable areas. Recommendations included conducting site-specific assessments, utilizing advanced modeling tools, implementing regular maintenance protocols, and enhancing communication among system components.
Quality defects in TMT Bars, Possible causes and Potential Solutions.PrashantGoswami42
Maintaining high-quality standards in the production of TMT bars is crucial for ensuring structural integrity in construction. Addressing common defects through careful monitoring, standardized processes, and advanced technology can significantly improve the quality of TMT bars. Continuous training and adherence to quality control measures will also play a pivotal role in minimizing these defects.
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
Vaccine management system project report documentation..pdfKamal Acharya
The Division of Vaccine and Immunization is facing increasing difficulty monitoring vaccines and other commodities distribution once they have been distributed from the national stores. With the introduction of new vaccines, more challenges have been anticipated with this additions posing serious threat to the already over strained vaccine supply chain system in Kenya.
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In present era, the scopes of information technology growing with a very fast .We do not see any are untouched from this industry. The scope of information technology has become wider includes: Business and industry. Household Business, Communication, Education, Entertainment, Science, Medicine, Engineering, Distance Learning, Weather Forecasting. Carrier Searching and so on.
My project named “Event Management System” is software that store and maintained all events coordinated in college. It also helpful to print related reports. My project will help to record the events coordinated by faculties with their Name, Event subject, date & details in an efficient & effective ways.
In my system we have to make a system by which a user can record all events coordinated by a particular faculty. In our proposed system some more featured are added which differs it from the existing system such as security.
Halogenation process of chemical process industries
Press and frame filter- Ed Ryan M. Ruales
1. 1
1. INTRODUCTION
A separation process is a method that results in conversion of a mixture or solution of
chemical substances into two or more distinct product mixtures. The resulting distinct products
may contain more of the original mixture’s certain component.
One method of separation is by filtration. Filtration is any of various mechanical,
physical or biological operations that separate solids from fluids (liquids or gases) by adding a
medium through which only the fluid can pass. The fluid that passes through is called
the filtrate. For filtration, the resistance is equal to the resistance through the cake plus the
resistance through the filter medium.
Filtration is different from sieving. In sieving, particles that are too big to pass through
the holes of the sieve are retained. In filtration, a multilayer lattice retains those particles that
are unable to follow the porous channels of the filter. Particles that cannot pass are called cake
and usually blocks the surface of the filter and hinders the filtration. Commercially, the term
filter is applied to membranes where the separation lattice is so thin that the surface becomes
the main zone of particle separation, even though these products might be described as sieves.
Filtration is also important and widely used as one of the unit operations of chemical
engineering. It may be simultaneously combined with other unit operations to process the feed
stream, as in the biofilter, which is a combined filter and biological digestion device.
An industrial filter press is a tool used in separation processes, specifically to separate
solids and liquids. The process uses the principle of pressure drive thus, the presence of a pump
is required. Among other uses, filter presses are utilized in marble factories in order to separate
water from mud in order to reuse the water during the marble cutting process.
2. 2
This experiment, entitled “Plate and Frame Filter Press”, is to determine how concentration is
related to the weight and volume of cake that it obtains and the length of time a certain volume
of filtrate is obtained. This also shows the plot between the volume of filtrate versus time per
volume of filtrate.
3. 3
2 THEORITICAL BACKGROUND
A filter press is a piece of batch operation, fixed volume equipment that separates
liquids and solids using pressure filtration. A slurry is pumped into the filter press and
dewatered under pressure. It is used for water and wastewater treatment in a variety of different
applications ranging from industrial to municipal.
A plate and frame filter is also referred as membrane filter plate. This type of filter press
consists of many plates and frames assembled alternately with the supports of a pair of rails.
Figure 2.1 shows a simple mechanism on how a filter press works. This filter uses a centrifugal
pump to drive the slurry to the plate and frame and to avoid the solids from settling. For each
of the individual separating chambers, there is one hollow filter frame separated from two filter
plates by filter cloths. The introduced slurry flows through a port in each individual frame, and
the filter cakes are accumulated in each hollow frame. As the filter cake becomes thicker, the
filter resistance increases as well. So when the separating chamber is full, the filtration process
is stopped as the optimum pressure difference is reached. The filtrate that passes through filter
cloth is collected through collection pipes and stored in the filter tank. The cake accumulation
occurs at the hollow plate frame, then being separated at the filter plates by pulling the plate
and frame filter press apart. The cakes then fall off from those plates and are discharged to the
final collection point. Figure 2.2 shows the parts of a simple filter press.
Figure 2.1 Mechanism of filter press
4. 4
Figure 2.2 Filter press
Variable that affects the filtration process includes the following: volume of slurry,
density of slurry, weight of slurry, solid in cake, volume of water, etc.
𝑉𝑠𝑙𝑢𝑟𝑟𝑦 = 𝑉 𝑤𝑎𝑡𝑒𝑟 + 𝑉𝐶𝑎𝐶𝑂3
𝜌 𝑆𝑙𝑢𝑟𝑟𝑦 =
𝑀𝑠𝑙𝑢𝑟𝑟𝑦
(
𝑀
𝜌
)
𝑤𝑎𝑡𝑒𝑟
+ (
𝑀
𝜌
)
𝐶𝑎𝐶𝑂3
𝑊𝑡 𝑠𝑙𝑢𝑟𝑟𝑦 = 𝑉𝑠𝑙𝑢𝑟𝑟𝑦 × 𝜌𝑠𝑙𝑢𝑟𝑟𝑦
𝑆𝑜𝑙𝑖𝑑 𝑐𝑎𝑘𝑒 = 𝑤𝑡% 𝐶𝑎𝐶𝑂3 × 𝑤𝑡% 𝑠𝑙𝑢𝑟𝑟𝑦
𝑊𝑡 𝑜𝑓 𝑤𝑎𝑡𝑒𝑟 𝑖𝑛 𝑠𝑙𝑢𝑟𝑟𝑦 = 𝑤𝑡. 𝑜𝑓 𝑠𝑙𝑢𝑟𝑟𝑦 − 𝑤𝑡. 𝑜𝑓 𝑠𝑜𝑙𝑖𝑑
𝑉 𝑤𝑎𝑡𝑒𝑟 =
𝑀 𝑤𝑎𝑡𝑒𝑟
𝜌 𝑤𝑎𝑡𝑒𝑟
5. 5
3. EXPERIMENTAL SECTION
3.1. Materials and Apparatus
Plate and Frame Filter Press Equipment
Water
Calcium Carbonate
3.2 Procedure
• 18 liters of slurry containing 10% by weight of calcium carbonate and 90% by
weight water was prepared. The feed tank was fed with the predetermined amount in
slurry. To be secured, the movable head was tightened to lock. The experiment was
started by opening the necessary valves. The agitator and the pump was switched on
simultaneously The switch of both the agitator and the pump was switched off when
the slurry from the head tank was already contained. The procedure was repeated using
20% by weight calcium carbonate.
6. 6
4. RESULTS AND DISCUSSION
The data included the following: initial weight of plate, weight of plate + wet cake,
weight of plate + dry cake, filtering time, presence of cake cracks, and percentage moisture and
the summary can be found in the Appendix. The calculations of form filtration rate of both the
Ca(OCl)2 and CaCO3 were made and the results was plotted against time.
Figure 4.1 Form filtration rate vs. time in seconds of Ca(OCl)2
Figure 4.1 shows the filtration rate of Ca(OCl)2 against time of filtration in minutes.
the form filtration rate of Ca(OCl)2 is seen to be inversely proportional with the filtering time.
0
5
10
15
20
0 5 10 15 20 25
FIltrationrate
time (sec)
Filtration of Ca(OCl)2
7. 7
Figure 4.1 Form filtration rate vs. time in seconds of CaCO3
Figure 4.2 shows the filtration rate of CaCO3 against time of filtration in minutes. the
form filtration CaCO3 rate of is seen to be inversely proportional with the filtering time.
Figure 4.3 Comparison of the form filtration rate vs. time in seconds of Ca(OCl)2 and
CaCO3
0
5
10
15
20
25
30
35
40
45
0 10 20 30 40 50 60 70
Filtrationrate(kg/hft^2)
Filtering time (s)
Filtration of CaCO3
0
5
10
15
20
25
30
35
40
45
0 20 40 60 80
FiltrationRate
time, s
CaCO3
Ca(OCl)2
8. 8
It is observed in Figure 4.3 that CaCO3 has a longer filtering time interval compared
to Ca(OCl)2. This is because of the factors affecting the filtration rate. One factor is the weight
of the solid that is to be filtered. the heavier the substance or compound, the longer is filtering
time. CaCO3 has a molar mass of 100 g/mol and Ca(OCl)2 has a molar mass of 142.9 g/mol.
Since weight is a factor that affects filtration, CaCO3 must have a longer time interval compared
to Ca(OCl)2
9. 9
5. CONCLUSION
A higher concentration of solids provide longer filtration rate since more solids are
needed to be filtered to obtain a certain volume of the filtrate. The cake obtained during the
filtration increases in longer filtration time. This is due to the accumulation of the cake in
overtime. Thus, with higher concentration of solute in the feed, longer time is needed to obtain
a certain volume of filtrate and this leads to increase of cake weight. Filtration also takes longer
time in dealing with heavy solids just like the CaCO3 than in lighter ones such as Ca(OCl)2.
Other factors affect the rate of filtration such as properties of the fluid (density, viscosity, etc.)
and solid properties (size, density, suspension, etc.)
The rate of filtration also decreases with an increase of time since the cake are
accumulating the top of the filter thus the fluid cannot pass through the filter anymore. It is
crucial to know the importance of the time of filtration. This can estimate whether the filtration
is sufficient and save time and resources by less inspection.
6. RECOMMENDATION
For the students to be able to fully grasp the knowledge behind the equipment used
in filtration, the laboratory should both have a rotary drum filter and filter press.
10. 10
7. REFERENCES
1. Geankoplis, C.J. 2003. Transport Processes and Separation Process Principles 4th
Edition. Pearson Education, Inc. pages 800-814
2. McCabe, W.L. and Smith, J.L. 1993. Unit Operations of Chemical
Engineering.McGraw-Hill Inc. pages 1002-1003
3. http://www.mwwatermark.com/en_US/what-is-a-filter-press/
4. https://en.wikipedia.org/wiki/Filter_press
8. APPENDIX
Table 1. Cake Weight of Ca(OCl)2
Test No. Initial Plate Weight
(g)
Wt. of Plate + Wet
Cake (g)
Wt. of Plate + Dry
Cake (g)
1 34.90 119.80 66.4
2 34.80 158.80 81.6
3 32.90 181.7 89.2
4 32.60 202.8 98.0
Table 2. Initial Moisture Content of Ca(OCl)2
Test No. Filtering Time (s) Cake
Cracks
Cake Weight %Moisture
Form Wash Dry Wet Dry
1 5 30 60 Yes 84.9 31.5 62.8
2 10 30 60 Yes 123.9 46.7 62.3
3 15 30 60 Yes 148.8 56.3 62.16
11. 11
4 20 30 60 Yes 170.2 65.4 61.57
Table 3. Filtration Rate of Ca(OCl)2
Test No. Form Filtration Rate (kg/ft2.h) Full Scale Filtration Rate (kg/ft2.h)
1 18.144 0.1265
2 13. 45 0.09396
3 10.81 0.07536
4 9.47 0.06564
Table 4. Cake weight of CaCO3
Test No. Initial Plate Weight
(g)
Wt. of Plate + Wet
Cake (g)
Wt. of Plate + Dry
Cake (g)
1 34.60 91.10 43.5
2 37.80 118.3 50.5
3 38.90 120.5 52.1
4 35.60 124.6 49.5
Table 5. Initial Moisture Content of CaCO3
Test No. Filtering Time (s) Cake
Cracks
Cake Weight %Moisture
Form Wash Dry Wet Dry
1 5 30 60 Yes 34.10 16.10 52.8
2 30 30 60 Yes 43.50 21.00 52.3
3 45 30 90 Yes 60.7 30.40 50.16
12. 12
4 60 30 90 Yes 76.8 38.00 50.2
Table 6. Filtration Rate of CaCO3
Test No. Form Filtration Rate (kg/ft2.h) Full Scale Filtration Rate (kg/ft2.h)
1 38.64 0.06465
2 28.2 0.01405
3 18.31 0.01357
4 11.23 0.01271
Problem 2:
A calcium carbonate slurry is to be filtered in a press having a total area of 14.3 m2 and
operated at a constant pressure drop of 2 atm. The frames are 30mm thick. Assume that the
filter medium resistance is 1.15x10^10 per ft. Calculate the filtration time and the volume of
the filtrate obtained in one cycle. Cake density is 70lb/ft3 The specific cake resistance,
2.9x10^10 (in lb/ft2. Slurry concentration is 15.6lbft3.
Solution:
𝐶 =
𝑐 𝑠
1 − (
𝑚 𝑓
𝑚 𝑐
− 1)
𝐶𝑠
𝜌
=
15.6
1 − ( 2 − 1 )
15.6
62.3
= 20.81
𝑙𝑏
𝑓𝑡3
∆𝑝 = 2𝑎𝑡𝑚 × 14.69 = 29.29
𝑙𝑏𝑓
𝑖𝑛2
𝐴 = 𝑓𝑖𝑙𝑡𝑟𝑎𝑡𝑖𝑜𝑛 𝑎𝑟𝑒𝑎 =
14.3
2
= 7.15 𝑚^2 = 76. 9 𝑓𝑡^2
𝑡ℎ𝑖𝑐𝑘𝑛𝑒𝑠𝑠 = 30𝑚𝑚 = 0.0984 𝑓𝑡
𝑚 𝑐 = 𝑡𝑜𝑡𝑎𝑙 𝑚𝑎𝑠𝑠 𝑜𝑓 𝑡ℎ𝑒 𝑐𝑎𝑘𝑒 𝑓𝑜𝑟𝑚𝑒𝑑 𝑖𝑛 𝑜𝑛𝑒 𝑐𝑦𝑐𝑙𝑒