Physics and Firearms :: physics firearm gun guns ballistics

So you are into reloading and you wonder how well that little package with 77 grains of IMR 4350 powder behind a 300 grain round nose, full metal jacket bullet will do. Well, you can do two things, a little bit of physics calculations, or go out and touch it off, hoping that it doesn’t explode in the barrel! I would choose to do a little physics myself†¦ By using some basic physics equations, you can figure out just about any part of the rifles ballistics data. For instance, if you know a few variables, you can predict range with physics, or if you like you can figure things like drag on the bullet, pressure and expansion values inside the gun, on the bullet and much more, all from physics. So, lets take a look at both the potential and kinetic energies of the .338 Winchester magnum. I will use a load given by the Winchester Reloading manual, which can be found online at: http://www.winchester.com/reloader/index.html This load is a 300 grain bullet, using 59.8 grains of Winchester 760 powder, and this gives a muzzle velocity of 2285 ft/sec. For potential energy we know that PE=mgh, where PE= Potential Energy, m=mass, g=acceleration due to gravity, and h=height. So for a 300-grain bullet, the potential energy is calculated by first finding the mass. To do this, take 300grains/7000grains/pound. This gives you a value of .042857lbs. Then we need to convert pounds to slugs (slugs are the units of mass†¦) .042857lb/32.2ft/s^2=.001331slugs. Now we can calculate the potential energy of our 300-grain bullet. We will assume that h=six feet, since that is roughly the height of the barrel when I shoot from a standing position. So, since PE=mgh, we get PE=(.00133slugs)(32.2ft/sec^2)(6ft)=.256956lbft. The answer is pretty much nothing and so we can pretty much ignore the potential energy of that bullet sitting at six feet in the air, but now lets look at the Kinetic energy of this bullet when shot. Since this bullet will be twisting when it flies, it will have rotational kinetic energy, but I really don’t want to get into those calculations and from what I have read, the amount of energy given by rotation versus that of the charge behi nd the bullet is really insignificant so I will only calculate the KE as if the bullet is not rotating. The formula is KE=1/2mv^2.

Pipeline Hydraulics Design Basis Engineering Essay

It includes the pipe and flow features of the transported fluid under specified operating conditions as established in the design footing.SpeedThe grapevine has to be laid for the distance of 770km between Portland and Montreal, the fluid in the pipe is Light Crude Oil. Speed of flow in a grapevine is the mean speed based on the pipe diameter and liquid flow rate. Its choice is first measure in the scheming process of our undertaking. The flow speed can hold both advantages and drawbacks. High speeds can do turbulency, and the contact of the fluid on the walls of the pipe which will do harm to the pipes and finally gnaw away the pipe, while low speed on the other manus can do the deposition of particulates in the line and cleanliness of the fluid will be compromised. Therefore, to avoid these problemsliquid lines are usually sized to keep a speed sufficient to maintain the solid atoms from lodging and besides to forestall the eroding of the pipe. Under these considerations the recommended speed is in the scope of 3ft/s to 8ft/s. From this selected scope of speed we have to choose a individual speed. The speed we have selected for our line is 5ft/s. This is the intermediate speed from the recommended scope and all the farther computations will be done on this speed.Velocity SelectionThe scope as mentioned above is taken every bit 3ft/s to 5ft/s. The following measure is to choose a individual speed from this scope. We have selected 5ft/s for our line. The ground for this speed choice is the tradeoff between pipe diameter and figure of pump Stationss. Harmonizing to continuity equation if we increase the speed, the corresponding diameter will cut down but the force per unit area loss will increase due to which a higher figure of pump Stationss are required. Similarly if we decrease the speed, the figure of pump Stationss will cut down but the diameter will increase for a given flow rate. Since the grapevine is laid over a long distance, the grapevine cost holds the major portion of the capital investing hence increasing the diameter will adversely impact the economic sciences of grapevine. This tradeoff is seeable in the computations shown in appendix A. The other ground for taking this speed is that if the flow rate fluctuates in the hereafter for any ground the diameter selected from this intermediate speed will be able to suit those fluctuations without impacting our system.Diameter CalculationCalculation of the diameter is the nucleus of the hydraulic designing.The diameter selected should be able to back up the emphasiss on the pipe, the capacity of the fluid and minimise the force per unit area losingss. Under given flow rate and false speeds, we can cipher the pipe diameter utilizing continuity equation:V=Q/AVolt: Flow speed Q: Volume flow rate A: Cross sectional country The flow rate is given as 109,000bbl/day or 7.1ft^3/s. The diameters are calculated at 3, 4, 5ft/s speeds and the several diameters are 20.83 † , 18.04 † and 16.14 † .Choice of DiameterAs mentioned above 5ft/s is selected as the recommended speed and the corresponding internal diameter ( ID ) is 16.14in.Nominal Pipe SizeFor the internal diameter later we have to cipher the nominal pipe size. To cipher the nominal diameter we refer to the â€Å" Pipe Data † provided for the Carbon Steel. From the tabular array shown in appendix B, it is found out that attendant nominal pipe size will be 18in.Features of FlowDifferent flow belongingss are calculated to find the government of flow, losingss in the pipes. The nature of the flow can be laminal or turbulent.There are two types of the losingss. Major losingss include the losingss due to clash in consecutive pipes and minor losingss due to decompression sicknesss, valves, tees. To cipher these we will be covering with Reynolds figure ( for nature of flow ) , Moody diagram ( for clash factor ) and head loss computations.LosingssAs the fluid flows through the pipe there is clash at the pipe wall and unstable interface in the consecutive parts of the pipe due to interference between the fluid and the walls of the pipe. This clash consequences in consequences in the loss of energy in the lineat the disbursal of liquid force per unit area and the losingss are known as the major losingss. Pipe systems consist of constituents in add-on to consecutive pipes. These include decompression sicknesss, valves, tees etc and add farther to the losingss in the line. These losingss are termed as minor losses.Experimental information is used to cipher these losingss as the theoretical anticipation is complex.Major LosingssThe force per unit area bead due to clash in a grapevine depends on the flow rate, pipe diameter, pipe raggedness, liquid specific gravitation, and viscousness. In add-on, the frictional force per unit area bead depends on the Reynolds figure ( and therefore the flow government ) . Therefore, the fluid in the grapevine will undergo force per unit area losingss as it runs in the line and cut down the operating force per unit area. This loss needs to be recovered and to keep the force per unit area pumps are installed at specific locations harmonizing to the demand ( pumps are discussed in Chapter in front ) . These force per unit area losingss are calculated by ut ilizing the Darcy-Weisbach expressiona?† P = degree Fahrenheit ( L/D ) ( V^2/2 ) I?Where, f=Darcy clash factor, dimensionless, normally a figure between 0.008 and 0.10 L=Pipe length, foot D=Pipe internal diameter, foot The force per unit area loss for speed of 5ft/s comes out to be 9625.15psi. All the relevant computations are shown in appendix A.Minor LosingssReal grapevine systems largely consist of more than consecutive pipes. The extra constituents ( valves, tees and decompression sicknesss ) add to the overall loss of the system. These are termed as minor losingss. In instance of really long pipes, these losingss are normally undistinguished incomparison to theA unstable clash in the length considered. But in caseA of short pipes, these minor losingss may really be major losingss such as inA suction pipe of a pumpwith strainer and pes valves.These losingss represent extra energy dissipation in the flow, normally caused by secondary flows induced by curvature or recirculation. Minor loss in diverging flow is much larger than thatA in meeting flow. Minor lossesgenerally increase with an addition in the geometric deformation of the flow. Thoughminor losingss are normally confined to a veryA short length of way, the effects mayA notdisappear for a considerable distance downstream. ItA is undistinguished in instance ofA laminar flow. The force per unit area bead through valves and adjustments is generallyexpressed in footings of the liquid kinetic energy V2/2g multiplied by a head loss coefficient K. Comparing this with the Darcy-Weisbach equation for caput loss in a pipe, we can see the undermentioned analogy. For a consecutive pipe, the caput loss H is V2/2g multiplied by the factor ( fL/D ) . Therefore, the caput loss coefficient for a consecutive pipe is fL/D. Therefore, the force per unit area bead in a valve or adjustment is calculated as follows:h=K ( V^2 ) /2gWhere, h=Head loss due to valve or suiting, foot K=Head loss coefficient for the valve or adjustment, dimensionless V=Velocity of liquid through valve or adjustment, ft/s g=Acceleration due to gravitation, 32.2 ft/s2 in English units The caput loss coefficient K is, for a given flow geometry, considered practically changeless at high Reynolds figure. K increases with pipe raggedness and with lower Reynolds Numberss. In general the value of K is determined chiefly by the flow geometry or by the form of the pressureloss device. Minor loss is by and large expressed in one ofA the two ways In footings of minor loss factor K. In footings length, tantamount to aA certain length of consecutive pipe, usuallyexpressed in footings of figure of pipe diameter. The minor losingss for our system are calculated and consequence in a really low value and can easy be neglected.Reynolds NumberFlow in a liquid grapevine may be smooth, laminar flow, besides known as syrupy or streamline flow. In this type of flow the liquid flows in beds or laminations without doing Eddies or turbulency. But as the speed increases the flow alterations from laminar to turbulent with Eddies and turbulencies. The of import parametric quantity used in sorting the type of flow in the pipe is called Reynolds Number. Reynolds figure gives us the ratio of inertial forces to syrupy forces and is used to find the nature of flow utilizing the recommended speed and the internal diameter. Reynolds figure is given byRe = I?VD/A µFlow through pipes is classified into three chief flow governments and depending upon the Reynolds figure, flow through pipes will fall in one of the undermentioned three flow governments. 1. Laminar flow: R & lt ; 2000 2. Critical flow: R & gt ; 2000 and R & lt ; 4000 3. Disruptive flow: R & gt ; 4000Friction FactorFriction Factor is a dimensionless figure required to cipher the force per unit area losingss in the pipe. Trials have shown that degree Fahrenheit is dependent upon Reynolds figure and comparative raggedness of the pipe. Relative raggedness is ratio of absolute pipe wall raggedness I µ to the pipe diameter D. For laminar flow, with Reynolds figure R & lt ; 2000, the Darcy clash factor degree Fahrenheit is calculated from the simple relationshipf=64/RFor laminar flow the clash factor depends merely on the Reynolds figure and is independent of the internal status of the pipe. Therefore, irrespective of whether the pipe is smooth or unsmooth, the clash factor for laminar flow is a figure that varies reciprocally with the Reynolds figure. For turbulent flow, when the Reynolds figure R & gt ; 4000, the clash factor degree Fahrenheit depends non merely on R but besides on the internal raggedness of the pipe. As the pipe raggedness additions, so does the clash factor. Therefore, smooth pipes have a smaller clash factor compared with unsmooth pipes. More significantly, clash factor depends on the comparative raggedness ( I µ/D ) instead than the absolute pipe raggedness I µ . In the disruptive part it can be calculated utilizing either the Colebrook-White equation or the Moody Diagram.Colebrook-White EquationThe Colebrook equation is an inexplicit equation that combines experimental consequences of surveies of turbulent flow in smooth and unsmooth pipe The Colebrook equation is given as:1/a?sf = -2log ( ( I µ/3.7D ) + ( 2.51/Rea?sf ) )But the turbulent flow part ( R & gt ; 4000 ) consists of three separate parts: Turbulent flow in smooth pipes Turbulent flow in to the full unsmooth pipes Passage flow between smooth and unsmooth pipes For disruptive flow in smooth pipes, pipe raggedness has a negligible consequence on the clash factor. Therefore, the clash factor in this part depends merely on the Reynolds figure as follows:1/a?sf = -2log ( 2.51/Rea?sf )For disruptive flow in to the full unsmooth pipes, the clash factor degree Fahrenheit appears to be less dependent on the Reynolds figure as the latter additions in magnitude. It depends merely on the pipe raggedness and diameter. It can be calculated from the undermentioned equation:1/a?sf = -2log ( ( I µ/3.7D )For the passage part between turbulent flow in smooth pipes and turbulent flow in to the full unsmooth pipes, the clash factor degree Fahrenheit is calculated utilizing the Colebrook-White equation given above:1/a?sf = -2log ( ( I µ/3.7D ) + ( 2.51/Rea?sf ) )Moody DiagramThe Colebrook equation is an inexplicit equation and requires test and mistake method to cipher f.To provide the easiness for ciphering f scientists and research workers developed a gra phical method known as Moody diagram.The Moody chart or Moody diagramis a graph that relates the clash factor, Reynolds figure and comparative raggedness for to the full developed flow in a round pipe.In the diagram clash factor is plotted poetries Reynolds figure. The curves are plotted utilizing the experimental information. The Moody diagram represents the complete clash factor map for laminar and all disruptive parts of pipe flows. To utilize the Moody diagram for finding the clash factor degree Fahrenheit we foremost calculate the Reynolds figure R for the flow. Following, we find the location on the horizontal axis of Reynolds figure for the value of R and pull a perpendicular line that intersects with the appropriate comparative raggedness ( e/D ) curve. From this point of intersection on the ( e/D ) curve, we read the value of the clash factor degree Fahrenheit on the perpendicular axis on the left.Other Pressure Drop RelationsHazen-Williams EquationThe Hazen-Williams equation is normally used in the design of waterdistribution lines and in the computation of frictional force per unit area bead inrefined crude oil merchandises such as gasolene and Diesel. This methodinvolves the usage of the Hazen-Williams C-factor alternatively of pipe roughnessor liquid viscousness. The force per unit area bead computation utilizing the Hazen-Williams equation takes into history flow rate, pipe diameter, and specificgravi ty as follows:h=4.73L ( Q/C ) 1.852/D4.87Where, h=Head loss due to clash, foot L=Pipe length, foot D=Pipe internal diameter, foot Q=Flow rate, ft3/s C=Hazen-Williams coefficient or C-factor, dimensionless In customary grapevine units, the Hazen-Williams equation can berewritten as follows in English units:Q=0.1482 ( C ) ( D ) 2.63 ( Pm/Sg ) 0.54Where, Q=Flow rate, bbl/day D=Pipe internal diameter, in. Pm=Frictional force per unit area bead, psi/mile Sg=Liquid specific gravitation Another signifier of Hazen-Williams equation, when the flow rate is in gal/ min and caput loss is measured in pess of liquid per thousand pess of pipe is as follows:GPM=6.7547A-10-3 ( C ) ( D ) 2.63 ( HL ) 0.54Where, GPM=Flow rate, gal/min HL=Friction loss, foot of liquid per 1000 foot of pipe In SI units, the Hazen-Williams equation is as follows:Q=9.0379A-10-8 ( C ) ( D ) 2.63 ( Pkm/Sg ) 0.54Where, Q=Flow rate, m3/hr D=Pipe internal diameter, millimeter Pkm=Frictional force per unit area bead, kPa/km Sg=Liquid specific gravitationShell-MIT EquationThe Shell-MIT equation, sometimes called the MIT equation, is used in the computation of force per unit area bead in heavy petroleum oil and heated liquid grapevines. Using this method, a modified Reynolds figure Rm iscalculated foremost from the Reynolds figure as follows:R=92.24 ( Q ) / ( DI? )Rm=R/ ( 7742 )Where, R=Reynolds figure, dimensionless Rm=Modified Reynolds figure, dimensionless Q=Flow rate, bbl/day D=Pipe internal diameter, in. I?=Kinematic viscousness, Central Time Than depending on the flow ( laminal or turbulent ) , the clash factor is calculated from one of the undermentioned equations:f=0.00207/Rm ( laminal flow )f=0.0018+0.00662 ( 1/Rm ) 0.355 ( disruptive flow )Finally, the force per unit area bead due to clash is calculated utilizing theequationPm=0.241 ( f SgQ2 ) /D5Where, Pm=Frictional force per unit area bead, psi/mile f=Friction factor, dimensionless Sg=Liquid specific gravitation Q=Flow rate, bbl/day D=Pipe internal diameter, in. In SI units the MIT equation is expressed as follows:Pm=6.2191A-1010 ( f SgQ2 ) /D5Where, Pm=Frictional force per unit area bead, kPa/km f=Friction factor, dimensionless Sg=Liquid specific gravitation Q=Flow rate, m3/hr D=Pipe internal diameter, millimeter

Leonardo Da Vinci Background (Art History Final)

For my final project I felt a drawing would be best, for I am not much of a painter, a carver, or a photographer. In fact as far as artistic abilities I am really only good at drawing, so it was not hard to decide what I would do. I thought I would have trouble choosing a drawing at first, for many artists we studied were painters, but then I remembered Leonardo Da Vinci was a man of many talents, and one of those talents was drawing.So I decided to replicate a drawing he had intended to become a sculpture of a horse, but was unfortunately never built in his lifetime. I used simple materials to recreate the drawing, using just a regular pencil, some thick sketching paper, and lots of time and patience. Leonardo Da Vinci was adept at many things such as painting, drawing, sculpting, engineering, and took a special interest in science and anatomy. He was both an artist and a scientist.In fact, if he were to tell you his profession, he may have told you any number of things: a painter, an engineer, a cartographer. His talents seemed limitless and it appears he made his best efforts to explore all he possibly could of his talents. The horse I decided to replicate was originally meant to be the largest equestrian model in the world. The man who asked Da Vinci to create the sculpture was named Ludovico il Moro. He was the Duke of Milan and requested the statue be built to honor his father, Francesco, in the year of 1482.Da Vinci first drew sketches of what the statue would look like and began making the sculpture from clay. Unfortunately in 1499 the French destroyed his clay model and the sculpture remained unfinished for centuries. Since 1970, however, there have been many replicas made from Leonardo Da Vinci’s many drawings of the potential horse sculpture. Some of these replicas can be found in Hungary, Italy, and the USA in various sizes and interpretations of the piece.

Life as a Master Cosmetologist Essay

What is a master cosmetologist? A master cosmetologist is an individual that has knowledge and skills in the field of cosmetology through advanced education. Cosmetology is defined as the art and science of beautifying and improving skin, hair, and nails. (Houghton Mifflin, 2009) In order to obtain the title master cosmetologist certain requirements must be met. A master cosmetologist may provide beauty services, massages and scalp treatments, apply make- up, style wigs, perform some hair removal and provide nail and skin care services. Life as a Master Cosmetologist A master cosmetologist has several advantages. One advantage from working as a master cosmetologist is the option to work on skin, hair, or nails. Many choose to work in a specific field after they are licensed. Job titles reported for a master cosmetologist are; hair stylist, hairstylist, hair dresser, hairdresser, barber stylist, manager stylist, platform artist, celebrity stylist, make-up artist and nail technician. A state issued license is required to practice cosmetology, although educational requirements to receive such license vary depending on state. Georgia State Board of Cosmetology first requires an individual to receive 1500 credit hours from an accredited cosmetology school. Coursework is taught by licensed professional instructors and consist of lectures and labs covering bacteriology, sterilization, customer service and business. † (Master cosmetologist, 2011) Additional coursework includes anatomy, physiology and chemistry. Secondly, the individual must submit an application to state board for an examination date. You must past a written and practical exam with a score of 70 or above. Following, an application for initial licensure along with a money order must be submitted. The fees vary by state between $30 and $50. A Master Cosmetologist License should be renewed every two years before March 31. Some states may allow a license holder to apply for reciprocity in another state. Reciprocity may be extended to licensees from other states or countries that have similar training and licensing requirements. The state of Georgia does not reciprocate with Florida, Hawaii, New York or California. There is an endless list of job descriptions associated with a master cosmetologist. A job description is defined as a document that outlines all duties and responsibilities of a particular position in a salon. The following entries are examples of such job descriptions. *Develop new styles and techniques. *Demonstrate and sell hair care products and cosmetics. *Operate cash registers to receive payments from patrons. *Shampoo, rinse, and condition scalp, hair or hairpieces. *Update and maintain customer information records, such as beauty services provided. *Bleach, color or tint hair using temporary, demi-permanent, semi-permanent, or permanent hair color. * Schedule client appointments. *Analyze patrons’ hair and other physical features to determine and recommend beauty treatments or suggest hairstyles. Cut, trim, and shape hair or hairpieces based on customers’ instructions, hair type and facial features. *Keep work stations clean and sanitize all tools, implements, and equipment. The skills of a master cosmetologist are limitless. Providing personal assistance, emotional support, and other personal care has proven to be the most valuable. Others include but are not limite d to; performing for or working directly with the public, thinking creatively, updating and using relevant knowledge, active listening, time management, judgment and decision making, critical thinking and management of financial resources. Being aware of others’ reactions and understanding why they react the way they do is an important skill known as social perceptiveness. (E-Best resumes, 2011) Employment Most employers require a person to have a high school diploma or GED and cosmetology license. â€Å"Candidates must have a professional presentation and strong customer service skills. † (Cosmetologist career profile, 2011) Employers may ask that a salon stylist also provide an employment portfolio and resume. A portfolio is a collection of photos and documents that reflect your skills, accomplishments, and abilities in your field. A resume can be described as a written summary of a person’s education and work experience. By law, a master cosmetologist must display his or her credentials at his or her station, and clients may ask to see a license in areas where the license need not be displayed by law. A lengthy career in cosmetology may cause physical damages to the body. These damages would be considered disadvantages of working as a master cosmetologist. One disadvantage would be carpal tunnel syndrome. Carpal tunnel syndrome is caused by pressure on the median nerve- the nerve in the wrist that supplies feeling and movement to parts of the hand. It can lead to numbness, tingling, weakness or muscle damage in the hands or fingers. Varicose veins are swollen twisted and sometimes painful veins that have filled with an abnormal collection of blood and would be considered another disadvantage of this profession. Moreover, lower back pain is triggered by a combination of overuse, muscle strain, and injury to the muscles, ligaments, bones and discs, making the back more prone to injury and re-injury. Low back pain can lead to overall imbalance in the spinal structure. Occupational Outlook The market seems favorable in years to come for cosmetologists. Cosmetology could be one of the few recession proof careers; things would have to get pretty bad for most people to prompt taking haircuts and hairstyling out of their budgets. â€Å"In fact, as stress and anxiety about the economy rise, so does business at salons, where clients can find relaxation and relief in the midst of the turmoil. †(Cosmetology career trends, 2011) According to SimplyHired. com, as of 2010, the average salary for a master cosmetologist is $31,000 per year. Income may vary due to customers’ tipping habits, services provided, experience of the cosmetologist, and whether he or she works on commission. The demand for cosmetologist is expected to grow by 20% between 2008 and 2018. Opportunities should remain plentiful, especially for new graduates seeking entry-level positions. Finally, to be successful you must take ownership of your education. Not surprisingly, employment will be greater for those with professional experience and those licensed to provide a broad range of services. A demand for specialized hair services has increased in recent years. This trend will continue, leading to a favorable occupational outlook for cosmetologists.

The Past Present and Future of Technology Inventory Control Essay

The Past Present and Future of Technology Inventory Control - Essay Example Technology evolved to the second generation, which included electronic computers for scientific and numerical calculations. These computers were now convenient, reliable and could store much information. Standard packages emerged for inventory control applications, making it easy to sort, analyze, and process data. The result was reduction in prices of goods and services leading to increased transactions and hence demanding more efficient and faster equipment. The third generation was online network databases that enabled online transaction processing (Gray 4). This era enabled a person to run many concurrent transactions and many users shared one database. Many programs developed in this era are still useful today in inventory control (Chief Supply Chain Officer Insights 13). The fourth generation inventory control devices were relational databases that enabled data definition, data navigation, and data manipulation (Gray 5). It enabled the capturing of inputs and outputs of merchandise to the user device. The programs in this generation are convenient even in today’s life for client server computing. The devices that followed emerged in the year 1995 and were multimedia databases that still exist in today’s life (Gray 6). In complex objects, the database made it possible to search, compare, and manipulate the data. This database could store and retrieve information and it made inventory control easy by adding on time and time interval data types. In the present, computer hardware has enabled the evolution of inventory control from manual and paper based processing to information search engines. The inventory control devices used in the present include barcode scanners to read every barcode in every item, mobile computers to capture data like the batch numbers and the inventory software for tracking the inventory sales

The development of business activities Essay Example | Topics and Well Written Essays - 2000 words

The development of business activities - Essay Example One of the major obstacles towards the increase of performance of the firm’s stores across the country seems to be the lack of fair and effective performance appraisal methods and reward systems; despite the fact that the performance appraisal methods should be based on the close cooperation between managers and employees (Falcone et al., 2007, 5) in DIY the level of cooperation among employees of different levels seems to be quite low. In fact, the store managers do not particularly interested in communicating with the employees of the store that is under their supervision – rather they are likely to emphasize on the increase of the profitability of the store – an increase of which they are going to be rewarded – through the Performance Related Pay (PRP) scheme applied to all the firm’s stores across Britain. At a next level, employees in DIY do not participate in the procedures related to the appraisal of their performance – even if their p articipation in the relevant schemes is required – as noted in the study of Harrington (2007, 58) where an emphasis is paid to the importance of performance reviews conducted by employees. It should be noted that no training of employees seems to be included in the firm’s current performance management system; training should be offered to employees and refer not only to the aspects of the firm’s performance management system but also to their skills – aiming to increase the employees’ skills and capabilities; such a training scheme would help towards the improvement of employees’ motivation.

Sociopolitical Paper Essay Example | Topics and Well Written Essays - 750 words

Sociopolitical Paper - Essay Example vel will require to use a lot of time and resources in studying the pros and cons of the car and even more time in changing the existing road safety laws and having to formulate new ones on manufacturing, production as well as distribution. This will lead to political implications both negative and positive. The automotive industry owners will also need to get new manufacturing equipment, seek scientists and software technocrats to install the technology or use billions in purchasing the technology from Google with the returns not being felt for several more years. The first users have to incur the high cost of production through the high price of the vehicles. The impacts are acceptable. The future stakeholders are the consumers and the automotive industries that have to bear and meet the high costs of production as well as the laws changing. However, even though the initial costs may be high, the returns in the long run will be worth it with the numerous benefits these cars are promising to bring to the human generation. The government is bound to adopt the technology because in the long it will save lives and billions of dollars in road repairs and other infrastructure that are constantly damaged by road accidents, it will save on money used when drivers are arrested and charged for traffic violation among offences in relation to cars and roads. The consumers will adopt as it will save on insurance money, expenses of car repair and traffic violation as well as letting people text while still driving. When people adopt the technology and view its advantages, the other stakeholders will benefit in increased profit through mass production due to high demand. The engineers are concerned with making the car as safe as possible as their main aim is to reduce the human loss and health problem brought about by accidents. The engineers are therefore concerned with adding as many safety features as possible while at the same time ensuring the cost will not be too much