The document describes the process for manufacturing urea from ammonia and carbon dioxide. There are six main steps: (1) hydrogen and ammonia production via the Haber process, (2) carbon dioxide removal from the gas stream, (3) shift conversion of carbon monoxide to carbon dioxide, (4) synthesis of ammonia, (5) reaction of ammonia and carbon dioxide to form urea, and (6) concentration and granulation of the urea product. Heat recovery and recycling of water and carbon dioxide are used to improve the efficiency and economics of the process.
Di-ammonium phosphate (DAP) is the world’s most widely used phosphorus fertilizer. It’s made from two common constituents in the fertilizer industry, and its relatively high nutrient content and excellent physical properties make it a popular choice in farming and other industries
This is a precise presentation on NPK fertilizers or complex fertilizers. It has detailed flowsheets with descriptions about all manufacturing processes of NPK fertilizers as well
this is one of bost beneficial slide to know the urea production this is not theoretical knowledge the training is done in nfl and the whole report is made on the basis of deep study of whole plant
Di-ammonium phosphate (DAP) is the world’s most widely used phosphorus fertilizer. It’s made from two common constituents in the fertilizer industry, and its relatively high nutrient content and excellent physical properties make it a popular choice in farming and other industries
This is a precise presentation on NPK fertilizers or complex fertilizers. It has detailed flowsheets with descriptions about all manufacturing processes of NPK fertilizers as well
this is one of bost beneficial slide to know the urea production this is not theoretical knowledge the training is done in nfl and the whole report is made on the basis of deep study of whole plant
Manufacture of manufacturing of single superphosphate and triple superphospah...MuhammadAyyanKhan
Introduction * Different Grade of Phosphate Rock * Different Forms of Super Phosphate * Manufacturing Single Superphosphate * Advantages and Use Single Superphosphate * Granular Single Super Phosphate Process & Advantages * Conclusion * Manufacturing Triple Superphosphate * Advantages and Use Triple Superphosphate * Side Effects of using Triple Superphosphate
Mixed Fertilizers - Definition, Preparation and Compatibility. VisanthGuhan
Definition for Mixed Fertilizers, It's Advantages and Disadvantages, Incompatibility of Mixed Fertilizers, Physical and chemical changes that affects the preparation and Mixed Fertilizer preparation process.
This is great Presentation with 3D effects which is all about production of ammonia from natural gas.
I am damn sure you will be getting everything here searching for.
its better to download it and then run in powerpoint 2013.
Manufacture of manufacturing of single superphosphate and triple superphospah...MuhammadAyyanKhan
Introduction * Different Grade of Phosphate Rock * Different Forms of Super Phosphate * Manufacturing Single Superphosphate * Advantages and Use Single Superphosphate * Granular Single Super Phosphate Process & Advantages * Conclusion * Manufacturing Triple Superphosphate * Advantages and Use Triple Superphosphate * Side Effects of using Triple Superphosphate
Mixed Fertilizers - Definition, Preparation and Compatibility. VisanthGuhan
Definition for Mixed Fertilizers, It's Advantages and Disadvantages, Incompatibility of Mixed Fertilizers, Physical and chemical changes that affects the preparation and Mixed Fertilizer preparation process.
This is great Presentation with 3D effects which is all about production of ammonia from natural gas.
I am damn sure you will be getting everything here searching for.
its better to download it and then run in powerpoint 2013.
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such as argon and methane to a limited extent. The source of H2 is demineralized water and the hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The present article intended the description of ammonia plant for natural gas based plants and the possible material balance of some section.
In the plant, ammonia is produced from synthesis gas containing hydrogen and nitrogen in the
ratio of approximately 3:1. Besides these components, the synthesis gas contains inert gases such
as argon and methane to a limited extent. The source of H2 is demineralized water and the
hydrocarbons in the natural gas. The source of N2 is the atmospheric air. The source of CO2 is
the hydrocarbons in the natural gas feed. Product ammonia and CO2 is sent to urea plant. The
present article intended the description of ammonia plant for natural gas based plants and the
possible material balance of some section
Production of Syngas from biomass and its purificationAwais Chaudhary
This project includes production of syngas from biomass and its purification. Firstly we discuss feasibility and availability of raw material. Then we have literature survey. A lot of techniques are there to produce syngas, we have discuss process selection. Environmental considerations are also have been discussed. Piping and instrumentation (P&ID) diagrams also have been attached. At the end we've our conclusion and our recommendations.
What Is A Control Valve
Process Control Terminology
Sliding-Stem Control Valve Terminology
Rotary-Shaft Control Valve Terminology
Control Valve Functions and Characteristics Terminology
Other Process Control Terminology
sliding stem control valve
introduction to thermal powerplant,type of thermal powerplant,captive powerplant,rankin cycle,co-generation powerplant,subcritical powerplant,supercritical powerplant,theory of operation,working principle,parts of powerplant,boiler,turbine,etc
introduction to flow,flow type,laminar,turbulent,one dimensional flow,two dimensional flow,type of flow measurement,flow measuring elements,orifices,nozzles,venturi,pitot tubes,limitations,advantages of the elements,application of elements
Describe the workflow to integrate 3rd party devices
Describe the purpose of the Device Integration Center (DIC)
Import a device into the FF Library
Instantiate a device in the HSE subnet
Configure third party FF Devices
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.
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.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
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.
Explore the innovative world of trenchless pipe repair with our comprehensive guide, "The Benefits and Techniques of Trenchless Pipe Repair." This document delves into the modern methods of repairing underground pipes without the need for extensive excavation, highlighting the numerous advantages and the latest techniques used in the industry.
Learn about the cost savings, reduced environmental impact, and minimal disruption associated with trenchless technology. Discover detailed explanations of popular techniques such as pipe bursting, cured-in-place pipe (CIPP) lining, and directional drilling. Understand how these methods can be applied to various types of infrastructure, from residential plumbing to large-scale municipal systems.
Ideal for homeowners, contractors, engineers, and anyone interested in modern plumbing solutions, this guide provides valuable insights into why trenchless pipe repair is becoming the preferred choice for pipe rehabilitation. Stay informed about the latest advancements and best practices in the field.
Final project report on grocery store management system..pdfKamal Acharya
In today’s fast-changing business environment, it’s extremely important to be able to respond to client needs in the most effective and timely manner. If your customers wish to see your business online and have instant access to your products or services.
Online Grocery Store is an e-commerce website, which retails various grocery products. This project allows viewing various products available enables registered users to purchase desired products instantly using Paytm, UPI payment processor (Instant Pay) and also can place order by using Cash on Delivery (Pay Later) option. This project provides an easy access to Administrators and Managers to view orders placed using Pay Later and Instant Pay options.
In order to develop an e-commerce website, a number of Technologies must be studied and understood. These include multi-tiered architecture, server and client-side scripting techniques, implementation technologies, programming language (such as PHP, HTML, CSS, JavaScript) and MySQL relational databases. This is a project with the objective to develop a basic website where a consumer is provided with a shopping cart website and also to know about the technologies used to develop such a website.
This document will discuss each of the underlying technologies to create and implement an e- commerce website.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
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.
COLLEGE BUS MANAGEMENT SYSTEM PROJECT REPORT.pdfKamal Acharya
The College Bus Management system is completely developed by Visual Basic .NET Version. The application is connect with most secured database language MS SQL Server. The application is develop by using best combination of front-end and back-end languages. The application is totally design like flat user interface. This flat user interface is more attractive user interface in 2017. The application is gives more important to the system functionality. The application is to manage the student’s details, driver’s details, bus details, bus route details, bus fees details and more. The application has only one unit for admin. The admin can manage the entire application. The admin can login into the application by using username and password of the admin. The application is develop for big and small colleges. It is more user friendly for non-computer person. Even they can easily learn how to manage the application within hours. The application is more secure by the admin. The system will give an effective output for the VB.Net and SQL Server given as input to the system. The compiled java program given as input to the system, after scanning the program will generate different reports. The application generates the report for users. The admin can view and download the report of the data. The application deliver the excel format reports. Because, excel formatted reports is very easy to understand the income and expense of the college bus. This application is mainly develop for windows operating system users. In 2017, 73% of people enterprises are using windows operating system. So the application will easily install for all the windows operating system users. The application-developed size is very low. The application consumes very low space in disk. Therefore, the user can allocate very minimum local disk space for this application.
Automobile Management System Project Report.pdfKamal Acharya
The proposed project is developed to manage the automobile in the automobile dealer company. The main module in this project is login, automobile management, customer management, sales, complaints and reports. The first module is the login. The automobile showroom owner should login to the project for usage. The username and password are verified and if it is correct, next form opens. If the username and password are not correct, it shows the error message.
When a customer search for a automobile, if the automobile is available, they will be taken to a page that shows the details of the automobile including automobile name, automobile ID, quantity, price etc. “Automobile Management System” is useful for maintaining automobiles, customers effectively and hence helps for establishing good relation between customer and automobile organization. It contains various customized modules for effectively maintaining automobiles and stock information accurately and safely.
When the automobile is sold to the customer, stock will be reduced automatically. When a new purchase is made, stock will be increased automatically. While selecting automobiles for sale, the proposed software will automatically check for total number of available stock of that particular item, if the total stock of that particular item is less than 5, software will notify the user to purchase the particular item.
Also when the user tries to sale items which are not in stock, the system will prompt the user that the stock is not enough. Customers of this system can search for a automobile; can purchase a automobile easily by selecting fast. On the other hand the stock of automobiles can be maintained perfectly by the automobile shop manager overcoming the drawbacks of existing system.
2. THE AMMONIA MANUFACTURING
PROCESS
• Ammonia is produced in a process known as the Haber
process, in which nitrogen and hydrogen react in the presence
of an iron catalyst to form ammonia. The hydrogen is formed
by reacting natural gas and steam at high temperatures and
the nitrogen is supplied from the air1 . Other gases (such as
water and carbon dioxide) are removed from the gas stream
and the nitrogen and hydrogen passed over an iron catalyst at
high temperature and pressure to form the ammonia. The
process is shown schematically in Figure 1.
• Step 1 - Hydrogen production Hydrogen is produced by the
reaction of methane with water. However, before this can be
carried out, all sulfurous compounds must be removed from
the natural gas to prevent catalyst poisoning. These are
removed by heating the gas to 400o C and reacting it with zinc
oxide:
• ZnO + H2S → ZnS + H2O
3. • Following this, the gas is sent to the primary
reformer for steam reforming, where
superheated steam is fed into the reformer with
the methane. The gas mixture heated with
natural gas and purge gas to 770o C in the
presence of a nickel catalyst. At this temperature
the following equilibrium reactions are driven to
the right, converting the methane to hydrogen,
carbon dioxide and small quantities of carbon
monoxide:
• CH4 + H2O =3H2 + CO
• CH4 + 2H2O =4H2 + CO2
• CO + H2O =H2 + CO2
• This gaseous mixture is known as synthesis gas.
4. Step 2
• Nitrogen addition The synthesis gas is cooled
slightly to 735o C. It then flows to the secondary
reformer where it is mixed with a calculated
amount of air. The highly exothermic reaction
between oxygen and methane produces more
hydrogen. Important reactions are:
• CO + H2O =CO2 + H2
• O2 + 2CH4 =2CO + 4H2
• O2 + CH4 =CO2 + 2H2
8. • 2O2 + CH4 = 2H2O + CO2
• In addition, the necessary nitrogen is added in the
secondary reformer. As the catalyst that is used to form the
ammonia is pure iron, water, carbon dioxide and carbon
monoxide must be removed from the gas stream to prevent
oxidation of the iron. This is carried out in the next three
steps.
• Step 3 - Removal of carbon monoxide Here the carbon
monoxide is converted to carbon dioxide (which is used
later in the synthesis of urea) in a reaction known as the
water gas shift reaction:
• CO + H2O = CO2 + H2
This is achieved in two steps. Firstly, the gas stream is
passed over a Cr/Fe3O4 catalyst at 360o C and then over a
Cu/ZnO/Cr catalyst at 210o C. The same reaction occurs in
both steps, but using the two steps maximizes conversion.
9. • Step 4 - Water removal The gas mixture is further cooled to
40o C, at which temperature the water condenses out and
is removed. Step 5 - Removal of carbon oxides The gases
are then pumped up through a counter-current of
UCARSOL solution (an MDEA solution, see article). Carbon
dioxide is highly soluble in UCARSOL, and more than 99.9%
of the CO2 in the mixture dissolves in it. The remaining CO2
(as well as any CO that was not converted to CO2 in Step 3)
is converted to methane (methanation) using a Ni/Al2O3
catalyst at 325 Deg C
• 2 CO + 3H2 = CH4 + H2O
• CO2 + 4H2 =CH4 + 2H2O The water which is produced in
these reactions is removed by condensation at 40o C as
above. The carbon dioxide is stripped from the UCARSOL
and used in urea manufacture. The UCARSOL is cooled and
reused for carbon dioxide removal.
10. • Step 6 - Synthesis of ammonia
• The gas mixture is now cooled, compressed and
fed into the ammonia synthesis loop (see Figure
1). A mixture of ammonia and unreacted gases
which have already been around the loop are
mixed with the incoming gas stream and cooled
to 5o C. The ammonia present is removed and
the unreacted gases heated to 400o C at a
pressure of 330 bar g and passed over an iron
catalyst. Under these conditions 26% of the
hydrogen and nitrogen are converted to
ammonia. The outlet gas from the ammonia
converter is cooled from 220o C to 30o C. This
cooling process condenses more the half the
ammonia, which is then separated out. The
11. • remaining gas is mixed with more cooled, compressed
incoming gas. The reaction occurring in the ammonia
converter is:
• N2 + 3H2 = 2NH3 The ammonia is rapidly
decompressed to 24 bar g. At this pressure, impurities
such as methane and hydrogen become gases. The gas
mixture above the liquid ammonia (which also contains
significant levels of ammonia) is removed and sent to
the ammonia recovery unit. This is an absorber-
stripper system using water as solvent. The remaining
gas (purge gas) is used as fuel for the heating of the
primary reformer. The pure ammonia remaining is
mixed with the pure ammonia from the initial
condensation above and is ready for use in urea
production, for storage or for direct sale.
12. THE UREA MANUFACTURING PROCESS
• Urea is produced from ammonia and carbon dioxide in two
equilibrium reactions:
• 2NH3 + CO2 = NH2COONH4 ammonium carbamate
• NH2COONH4 = NH2CONH2 + H2O
• urea The urea manufacturing process, shown schematically
in Figure 2, is designed to maximise these reactions while
inhibiting biuret formation:
• 2NH2CONH2 = NH2CONHCONH2 + NH3
biuret This reaction is undesirable, not only because it
lowers the yield of urea, but because biuret burns the
leaves of plants. This means that urea which contains high
levels of biuret is unsuitable for use as a fertiliser. The
structure of these compounds is shown in Figure
14. • Step 1 - Synthesis
• A mixture of compressed CO2 and ammonia at
240 bar g is reacted to form ammonium
carbamate. This is an exothermic reaction, and
heat is recovered by a boiler which produces
steam. The first reactor acheives 78% conversion
of the carbon dioxide to urea and the liquid is
then purified. The second reactor recieves the gas
from the first reactor and recycle solution from
the decomposition and concentration sections.
Conversion of carbon dioxide to urea is
approximately 60% at a pressure of 50 barg. The
solution is then purified in the same process as
was used for the liquid from the first reactor.
15. • Step 2 - Purification
• The major impurities in the mixture at this stage are water
from the urea production reaction and unconsumed
reactants (ammonia, carbon dioxide and ammonium
carbamate). The unconsumed reactants are removed in
three stages3 . Firstly, the pressure is reduced from 240 to
17 barg and the solution is heated, which causes the
ammonium carbamate to decompose to ammonia and
carbon dioxide:
• NH2COONH4 =2NH3 + CO2 At the same time, some of the
ammonia and carbon dioxide flash off. The pressure is then
reduced to 2.0 barg and finally to -0.35 barg, with more
ammonia and carbon dioxide being lost at each stage. By
the time the mixture is at -0.35 barg a solution of urea
dissolved in water and free of other impurities remains. At
each stage the unconsumed reactants are absorbed into a
water solution which is recycled to the secondary reactor.
The excess ammonia is purified and used as feedstock to
the primary reactor.
16. • Step 3 - Concentration 75% of the urea solution is heated under vacuum,
which evaporates off some of the water, increasing the urea concentration
from 68% w/w to 80% w/w. At this stage some urea crystals also form. The
solution is then heated from 80 to 110o C to redissolve these crystals prior
to evaporation. In the evaporation stage molten urea (99% w/w) is
produced at 140o C. The remaining 25% of the 68% w/w urea solution is
processed under vacuum at 135o C in a two series evaporator-separator
arrangement.
• Step 4 - Granulation Urea is sold for fertiliser as 2 - 4 mm diameter granules.
These granules are formed by spraying molten urea onto seed granules
which are supported on a bed of air. This occurs in a granulator which
receives the seed gransules at one end and discharges enlarged granules at
the other as molten urea is sprayed through nozzles. Dry, cool granules are
classified using screens. Oversized granules are crushed and combined with
undersized ones for use as seed. All dust and air from the granulator is
removed by a fan into a dust scrubber, which removes the urea with a water
solution then discharges the air to the atmosphere. The final product is
cooled in air, weighed and conveyed to bulk storage ready for sale.
17. UTILITIES
• The ammonia and urea manufacturing facilities are separate, so each
has its own utilites. These are listed below.
• Ammonia manufacture Heat recovery The heat of the gas from the
primary reformer (Step 1) is used to produce steam for the primary
reformer using a boiler. The gas is then discharged. Heat from the
process gas from the secondary reformer (Step 2) is used to produce
steam for a turbogenerator.
• Water recycling Excess water from the water gas shift converter, the
methanator and the ammonia synthesis loop is used for boiler feed
water and as the absorbing water for ammonia recovery.
• Carbon dioxide stripper The used UCARSOL is sent to the carbon dioxide
stripper. Here the UCARSOL is heated to remove a mixture of CO2 and
water, cooled and reused. The water is removed from the CO2 by
condensation and the pure CO2 sent directly to the urea plant for
compression and use in urea synthesis.
18. • Ammonia recovery Gases purged from the ammonia synthesis loop
and gases collected during ammonia decompression are mixed and
sent to the ammonia recovery system. Here the gas mixture is
introduced at the bottom of a column and passes up through a
counter-current of cold water. 96% of the ammonia in the gas is
absorbed into the water, leaving a gas mixture that is used as a fuel
gas to heat the primary reformer. The ammonia is distilled out of
the ammoniawater mixture, condensed and pumped to join the
rest of the ammonia from the ammonia synthesiser. Urea
manufacture.
• Heat recovery The heat of the reaction in which ammonium
carbamate produces steam at 7 bar g. This is used in the
decomposition and evaporation sections for heating. Ammonia and
carbon dioxide recovery During urea decomposition a mixture of
gaseous carbon dioxide and ammonia is collected and absorbed
into a dilute aqueous urea solution. This mixture is recycled by
being fed back into the secondary urea reactor. The excess
ammonia is condensed and used as feedstock to the primary
reactor. Water recycling Evaporated water from the concentration
step is used during the third stage of decomposition as the initial
recycle solution.