Executive Summary Example
Executive Summary Example. Big Roller. One Line Pitch: A new experience in moving. Business Summary: We have invented a revolutionary piece of technology that
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*This sample was adapted by the UAGC Writing Center from an original paper by a student. Used by permission. An executive summary is a concise summary of a
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You must rename them: Rename the Excel file Financials Template for Distribution to the name of your company (“Jones General Store” for example).
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An executive summary is a concise document demonstrating the problem
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The Executive Summary (1-2 pages) will eventually be given to judges at the Semi- Accessed at http://www.unh.edu/news/docs/Conway_May08.pdf.
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whole report generally in less than a page. On the next three pages are examples of an executive summary. Do each of these have the relevant elements of
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How to Write an Executive Summary
An executive summary is a concise document demonstrating the problem
How to Write an Executive Summary - Harvard University
An executive summary is a concise document demonstrating the problem findings and recommendation of a longer policy report Writing an executive summary will help your audience quickly understand the policy problem and proposed solution of your report
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The Executive Summary (1-2 pages) will eventually be given to judges at the Semi-Finals and Final Round of the competition Your document should quickly summarize: the problem your idea and the benefits of your solution The format can be a bullet-point list or it can contain more graphics
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o The Executive Summary explicitly names basic assumptions for the rationale supporting the methodology findings and recommendations Without those assumptions readers will not be pers? of the report’s ultimate recommendations The Executive Summary then advocates its
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Executive Summary Example #1 Copied from: Lumsdaine Lumsdaine and Shulnett Creative Problem Solving and Engineering Design McGraw Hill 1999 Executive Summary Proposal to Design a Pedestrian Bridge over Freedom Boulevard at Morningdale Avenue Pumpkin Center North Carolina
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5 EXECUTIVE SUMMARY TO THE 2021 FINANCIAL REPORT OF THE U S GOVERNMENT Chart 2 compares the government’s budget deficit (receipts vs outlays) and net operating cost (revenues vs costs) for FYs 2017 - 2021 During FY 2021: • A $269 7 billion increase in outlays was more than offset by a $626 0
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Executive summary of pre-feasibility study by Fluor for
4 EXECUTIVE SUMMARY OF PRE-FEASIBILITY STUDY BY FLUOR FOR LARGE-SCALE INDUSTRIAL AMMONIA CRACKING PLANT Space requirements The plot space requirements including storage as estimated by Fluor based on the information from the various licensors for the entire 1 million tons of hydrogen capacity range between 200000 m² and 450000 m²
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Executive Summary Executive summaries provide a brief summary of a larger document and are meant to persuade decision makers to read the larger work The executive summary is typically the first document of the body of a report or proposal and it should function independently of the larger document The importance of the
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An Executive Summary will usually contain: 1 Subject matter of report 2 Methods employed 3 Findings 4 Conclusions 5 Recommendations 6 Limitations of report Document adapted for use with reading software by Claire Burrell Original document produced by Aron Truss Faculty of Business and Law Study Support: click here to email study support
What should be included in an executive summary example?
- For example, to write an executive summary of an environmental study, you would compile a report on the results and findings once your study was over. But for an executive summary in project management, you want to cover what the project is aiming to achieve and why those goals matter.
How can I write an effective executive summary?
- Just like any content, your executive summary needs to grab the reader's attention and keep them engaged. The introduction to your executive summary should include a hook, something like an interesting statistic about your industry or niche, or maybe a compelling story.
What are the benefits of an executive summary?
- Including a compelling executive summary in your document can increase the reader’s interest and encourage them to read the rest of the document. It can also help to inform people who can’t afford to read the entire document by presenting all the relevant details they need.
How long should an executive summary be?
- An executive summary should ideally be between 1 and 2 pages, or 5-10% of the report if it is a much longer proposal. This should be a quick read that hits all the important points of your proposal, so that an executive could read it and have an understanding of what is included in your proposal and why specifically your proposal should be picked.
1 EXECUTIVE SUMMARY OF PRE?FEASIBILITY STUDY BY FLUOR FOR LARGE?SCALE INDUSTRIAL AMMONIA CRACKING PLANT LARGE?SCALE
INDUSTRIAL AMMONIA
CRACKING PLANT
Executive summary of
pre-feasibility study by Fluor for: Commissioned by Port of Rotterdam Authority (PoR), Air Liquide, Aramco, bp, E.ON/Essent, ExxonMobil, Gasunie, Global Energy Storage (GES), HES International, Koole Terminals, Linde Gas, RWE, Sasol, Shell, Uniper, Vopak and VTTI.2 EXECUTIVE SUMMARY OF PRE?FEASIBILITY STUDY BY FLUOR FOR LARGE?SCALE INDUSTRIAL AMMONIA CRACKING PLANT
Executive summary pre-feasibility study
LARGE?SCALE INDUSTRIAL AMMONIA
CRACKING PLANT
Given the large interest in developing ammonia
cracking facilities to enable the import of hydrogen for decarbonisation of the Industrial Complex in the Port of Rotterdam and other regions further afield,18 parties joined forces to commission a pre-feasi-
bility study for a large-scale industrial ammonia cracking plant. Port of Rotterdam Authority (PoR), together with Air Liquide, Aramco, bp, E.ON/Essent,ExxonMobil, Gasunie, Global Energy Storage (GES),
HES International, Koole Terminals, Linde Gas, RWE, Sasol, Shell, Uniper, Vopak, and VTTI commissionedFluor to perform this pre-feasibility study.
The study investigated the possibilities for a large central ammonia cracking facility to generate hydro gen from imported ammonia in the Port of Rotterdam, with a capacity of 1 million tons of hydrogen per year (equivalent to ~3000 ton/day or 1.3 million Nm³/h of H₂). This results in an approximate consumption of 20,000 tons of ammonia (NH₃) per day. In addition to the ammonia cracking process plant, the study also looked at possible setups for the storage and distribution of the ammonia imported into theHarbour Industrial Complex (HIC).
The key aims of the study were to get a first under standing of the technologies available on offer, how far these processes are developed for commercial deployment, the energy and utility consumption of such processes, the number of process trains required to achieve the desired H₂ capacity (related to the maximum feasible per-train capacity), environmental footprint / emissions, general plot space requirements, safety and logistics associated with ammonia storage and handling, capital and operating cost of the required facilities, and the benefits of a central large scale ammonia cracking facility versus several smaller decentralised plants. The figures below provide a brief example of this. HYDROGEN
POWERPRODUCTION
• SHORT SEA • BARGE • PIPELINE WATERAMMONIA VALUE CHAIN
NH productionTransportationUseSHIPPING FUEL
CHEMICAL INDUSTRY
N 2Figure 1 -
Overview of the ammonia value chain
3 EXECUTIVE SUMMARY OF PRE?FEASIBILITY STUDY BY FLUOR FOR LARGE?SCALE INDUSTRIAL AMMONIA CRACKING PLANT
Ammonia cracking is an endothermic equilibrium
reaction requiring external heat supply. The study looked at ammonia cracking technology from Haldor Topsoe, KBR, Thyssenkrupp, Johnson Matthey, Duiker,Casale and H2SITE.
Most licensors have technology available today to
provide ammonia cracking plants of capacity, using several parallel process trains. Whereas many of the licensors offer process designs based on conventional 'reformer' technology (vertical catalyst filled tubes in a firebox with radiant heat transfer to the process tubes) as employed in grey hydrogen production, ammonia production, and methanol production plants, notable differences were also observed in the overall flowsheet and in the core reactor section. Duiker's technology employs catalyst-filled tubes in an alternate configu ration to prevent direct exposure to flames. H2SITE's technology consists of a reactor column filled with catalyst, containing Pd-based membranes. All licen sors confirmed that they could provide the required H₂ product purity and pressure of 99.9 mol% and 50 barg.The various technologies have TRL levels of 6-9.
Safety
Previous studies commissioned by the Port of
Rotterdam have found that the import, storing, and transporting of large amounts of ammonia can be done efficiently and safely within the safety contours of the Port. Moreover, companies in the HIC have the experience and skills to handle different chemical substances and dangerous goods. That said, the focus of all participants of this study is to ensure that the use and transportation of ammonia will be done safely. This means that the safest transport routes need to be researched and used and that the safety requirements around the cracking process also need to be resear ched further. In the study, ammonia transportation via pipeline and the best available technology forAmmonia storage have been included.
Centralised and decentralised options
Schemes for ammonia offloading and storage logistics for centralised and de-centralised cracking options were developed. Given that determining the location of these plants was not part of this study, three plausi ble options were identified:STORAGESHIPPING
H 2CRACKINGSTORAGE
SHIPPING
H 2STORAGECRACKINGSHIPPING
H 2Option 1
Centralised ammonia cracker with ammonia
offloading and storage at six different locations.Option 2
Centralised ammonia cracker with ammonia
offloading and storage at the same location; size of storage tanks based on those typical today with potential optimisation in the future.Option 3
Six decentralised ammonia cracker plant locations, each with its own ammonia offloading and storage facilities.4 EXECUTIVE SUMMARY OF PRE?FEASIBILITY STUDY BY FLUOR FOR LARGE?SCALE INDUSTRIAL AMMONIA CRACKING PLANT
Space requirements
The plot space requirements including storage as
estimated by Fluor based on the information from the various licensors for the entire 1 million tons of hydrogen capacity range between 200,000 m² and450,000 m². These are conservative estimates. It is not
typical for licensors to provide well-developed plot plans for such a high-level study. The plot space requi rements can be further optimised once the potential plant location(s) have been determined. CostsThe capital cost of an ammonia cracking plant is
considered roughly equal for central and decentral options. This is because, for most licensors, the number of parallel trains required is so high that there should not be a major capital cost difference between having the same number of trains all at one location, or at six different locations. However, with advances in ammonia cracking technology, a greater amount of ammonia may be cracked in one train, reducing the overall number of trains. This would benefit a central facility in reducing capital investment resulting from economies of scale. In addition, there are capital benefits of centralisa tion for ammonia storage and logistics. Hydrogen compression at a centralised location is less capital intensive as the number of equipment items is gover ned by the compression duty required instead of sparing of equipment. Utility systems can be centrali sed and constructed in one location. Despite the substantial investment in the cracker and the storage, it was found that approximately 80-90% of the cost of H₂ production (starting from fixed ammonia prices delivered at the port of Rotterdam) lies in the cost of NH₃ feedstock.Emissions
There are no CO₂ emissions from the plant as the designs were based on the exclusive use of carbon- free fuel. The required flue gas NOx (expressed as NO₂) specification of 80 mg/Nm³ on a dry, 3 vol% O2 basis could be met by all licensors by the application of Selective Catalytic Reduction technology, indica ting that the production process can be operated within the stipulated environmental limitations.Conclusions
The study helped gain insight into the ammonia crac- king technology landscape and made it clear that the technology for producing 1 million tons of hydrogen from ammonia is available today and requires a multi- train facility. The various trains may be located at a centralised plant or dispersed across several locations. There are clear capital cost benefits associated with building a centralised ammonia cracking plant with offloading and storage facilities at the same location. This does require a significant investment. However, the bulk of the cost of H₂ production from ammonia cracking (at the feedstock prices assumed in the study) lies in the cost of ammonia feedstock. As a follow up to this work and to further develop this project, a more detailed licensor evaluation study must be carried out for an ammonia cracking plant with a defined plant location, capacity per location, and associated ship offloading & storage locations. A quantified safety / risk analysis study for the same including dispersion modelling calculations will enable greater insight into the environmental friendliness of the process.quotesdbs_dbs14.pdfusesText_20[PDF] executive summary startup
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