Ethics and Legal Considerations in Strategic Management (StilSim Essay

Ethics and Legal Considerations in Strategic Management (StilSim Company ) - Essay Example Virtues such as integrity and honesty have always been valued here in the stilsim company, not only that, we also believe in quality customer service, openness, personal excellence, continual self improvement and mutual respect. We respect our committment that we have with our cliental and cutomers and we believe in providing the best service that is out there to all of our associations. We here hold ourselves accountable to not only our customers but also to our share holders, our partners and our employees and we pride ourselves on honouring our commitments with them and providing the best of the results that we can. We try our best to live up to the expectations of our cliental and customers. To understand more about the work here at stilsim and the principles on which we work, we provide our employees and clientals with our brochures and handbook. These handbooks have all the essential information about the stilsim and what this company is about. Generally, ethics considered as the moral standards by which behaviour of the people is judged. Often the ethics re considered as the â€Å"golden rule†, this however is only the general consideration of ethics and this standard can not be used to define the buisiness ethics. In a business you are answerable to diffrent set of people such as customers, shareholders and the clients. Business ethics is is a highly compex field where determining your next move when an ethical dilemma arises among diffrent interests is an extremely tricky job. Right now the stilsim company is dealing with many internal and external issues and once we impliment our new strategy, the ethics should be kept in our minds while making any important decision. Since the stilsim company has been in the business for such a long period of time , we believe that we hold a great deal of responsibilty towards our employees, our stake holders, our shareholders, our customers and even the

Julius Caesar Essay Example for Free

Julius Caesar Essay Julius Caesar is a film version (1953) of Shakespeare’s play and is called to be the most successful Hollywood adaptation. The director of the film Joseph L. Mankiewicz made a successful attempt to authentically preserve the characters, themes and actions. Mankiewicz used the technique of the screen to the utmost advantage in the use of close-ups, of detail to illustrate key moments in film terms. Julius Caesar is a tragedy of an assassin â€Å"who is too honorable to succeed†. Caesar is a ghost story, seduction, study of marriage and fortune-telling. The film production is also a course in public speaking, social studies lesson, history of civil war and revenge and forgiveness, dramatic story about regretted decisions, tribute to the power of mental images. The historical context is Caesar’s victory over Italians and Pompey’s sons whereas the historical events presented in the film production are the conspiracy between Cassius and Brutus to assassinate Julies Caesar and the power of Roman Empire that is so desired by certain characters. Brutus, Caesar’s best friend, is easily convinced that assassinating the best friend can be justified as it will assist in establishing liberty in Roman Empire. It resulted in Brutus agreement to join the conspiracy. Caesar ignored the warning about attending the Senate meeting and thus he was assassinated by conspirators. Although at the funeral Brutus made an attempt to justify his crime appealing to the crowd, he made a fatal mistake allowing Mark Antony to speak, because Mark was the most faithful follower of Caesar. the crowd was incited and turned away from conspirators Morality won in a certain way, because Antony’s military forces defeated the conspirators and Brutus committed a suicide. After reviewing the historical context and events it is seen that a row of historical issues arose from the film. The first issue is tyranny that was so common in those times. In a certain way Julius Caesar is a story about the death of a benevolent tyrant. Although Caser had some good virtues in his character, he was a tyrant at heart and many people suffered from his cruelty. He was responsible for killing of innocent people as accepted no compromises thinking firstly about his own welfare. The next common historical issue is the question of betrayal. Although Brutus is portrayed as a respectable and noble person, he is betrayer at heart. It is necessary to note that being a weak person in a certain way he was all the more easily manipulated into killing his best friend. Brutus betrayed Caser when stabbing him when Caesar looked him in the eyes and betrayed Caesar for the second time when believing he did it for the good of the Roman Empire. He explained even his motives to the citizens, but remained misunderstood. Another issue arising from betrayal is the desire of absolute power, because for the characters it meant more than position and name it was everything. Although every power has limitations and there is no absolute power, every character in the film had in a certain way his power. It appeared from the movie that characters used their power only for their convenience. Finally the last important issue is the question of loyalty which was rather unique and uncommon for those times. If the loyalty had not been involved in the film, the Roman Empire â€Å"would not have been torn apart†. Otherwise if loyalty had been involved in all aspects, tyrant Caesar would have the emperor of for many years. War would not have broken out if people would have been more loyal to Caesar. The example of loyalty in the film is Mark Antony, a character misunderstood by all people. In conclusion it is necessary to admit that film is really successful in making people think about historical issues and problems, because many of the problems are still present in contemporary society. It is possible to state that the movie complements the historical discussion of the written texts, because it presents all historical events in more vivid and realistic way and it is easier for more people to understand the problem. All these conceptions of the play are valid, because people for four hundred years have been periodically returning to admire Julius Caesar. References Jorgens, Jack J. (1985) Shakespeare on Film and Television. New York: Scribners.

Inserted-Plate Coated of Methanol Steam Reformer

Inserted-Plate Coated of Methanol Steam Reformer High Efficiency Inserted-Plate Coated of Methanol Steam Reformer: PEM Fuel Cell Applications Methanol can be easily stored and transported and converted to H2 using a reforming reactor that makes it an excellent hydrogen and energy source for fuel cell applicationsEasily storage, transporting and converting to H2 by a reforming reactor using makes it an excellent energy source for PEMFC applications [1-3] During the last decades, there has been a growing interest on developing technologies taking advantage of clean energy sources. The reduction of atmospheric pollution and, namely, the emission of greenhouse gases have become imperative and, among the new technologies for mitigating these emissions, fuel cells have the ability to efficiently convert chemical into electrical energy. In particular, PEMFCs are zero-pollutants emission systems because they transform the chemical energy of the electrochemical reaction within hydrogen and oxygen into clean electrical powerTodays, for environmental issues, growing interest on developing technologies including clean energy sources has been focused. Pollution issue and, especially, the emission of greenhouse gases have become crucial and, the new technology for elimination of these emission, can be achieved by PEMFC. [4, 5] Meanwhile, compared to other feedstocks, methanol exploitation shows various advantages as a hydrogen carrier for fuel cell applications and, namely, it can be produced from renewable sources[9], and the reforming reaction occurs at relatively low temperatures, ca. 240–260 1CAmong these, methanol exploitation leads various advantages as a hydrogen carrier and, especially, reforming reaction applying at relatively low temperature (240-260 C) [6] , compared to the methane reforming, normally performed at 800–1000 1C, compared to the methane reforming, normally carry out at 800-1000 C[7] . Methanol steam reforming (MSR) reaction has been seen as a very attractive and promising process for hydrogen production and, according to the scientific literature on the argument, it can be described by the following chemical reactions:Attractive and promising of the methanol steam reforming process cause especial insight to this reaction which according to the scientific references, occurs by the following chemical reactions: Where reactions 1, 2 and 3 represent MSR reaction, water gas shift reaction and methanol decomposition reaction, respectively.Reaction (1), represents MSR reaction, reaction (2) represents water gas shift reaction and reaction (3) represents the methanol decomposition reaction The reactor design has direct impact on the reaction conversion, but owing to higher technical complexity and manufacturing costs of other designs, the reformers and MRs are normally tubular. However, recent efforts in the area of micro-processing made possible and easier to manufacture other reactor designs and namely well-structured à ¯Ã‚ ¬Ã¢â‚¬Å¡at micro-reactors. A micro-reactor is defined as a device that contains micro structured features, with a sub-millimeter dimension, in which chemical reactions are performed in a continuous manner They present advantages compared to conventional ones such as higher surface-to-volume ratio, smaller mean distance of the specific à ¯Ã‚ ¬Ã¢â‚¬Å¡uid volume to the reactor walls, better heat and matter transfer properties and à ¯Ã‚ ¬Ã¢â‚¬Å¡ow patterns that fit with the reaction needs. Furthermore, à ¯Ã‚ ¬Ã¢â‚¬Å¡at reformers are suitable for stack integration with fuel cells. Packed-bed micro-reactors require well-define catalyst particles, wi th regular shape and much smaller than the internal dimensions of the micro-channels, which is a problem for most of commercial catalysts.The reactor design, directly impress reaction conversion but owning to higher complexity and fabrication costs should be considered. Common normally MRs are in tubular shape. However, recent researches show easier to manufacture and possibility of other designs and namely well-structured flat micro-reactors. A reactor containing micro structure features and sub-millimeter dimension through performing in a continues manner representing advantages such as higher surface to volume ratio, smaller mean distance of the specific fluid volume to the reactor walls, improving heat and mass transfer make appropriate situation of stack integration with fuel cells. [8]. Many studies have been developed to explore the advantages of micro/mini-reactors to produce hydrogen through MSR The design of a reactor targets the maximization of the conversion and selectivity at the lowest costs and its performance is inà ¯Ã‚ ¬Ã¢â‚¬Å¡uenced by the à ¯Ã‚ ¬Ã¢â‚¬Å¡ow pattern, velocity profile, pressure drop and heat transfer, so all these aspects must be consideredTo fabricate an effective micro-reactor having maximum conversion and selectivity at a low cost is impressed by the flow pattern, velocity profile, pressure drop and heat transfer, therefore all these approaches should be considered[9]. For conducting MSR reaction, most of the used reactor designs are rectilinear channels, pin-hole, coil-based and radial (Fig. 2).Coil-based reactor designs allow high conversions, but impose a significant pressure drop penalty, which may be a limitation for compact applications Categorization of the design consist rectilinear channels, pin-hole, coil-based and radial (Fi g. 2). Among these, Coil based leads high conversion and pressure drop preventing compact applications[9]. In the other hand, the rectilinear channel designs exhibit a small-pressure drop, but the conversion is low due to uneven mass distribution and is affected by the Reynolds number while, the first exhibit a small pressure drop, uneven mass distribution cause lower conversion which impressed by Reynolds number[9]. Yet, by adjusting the channels width [69] or by imposing a pressure drop at the channels entrance even distributions on rectilinear channel designs can be obtained, improving the methanol conversion[10]. Conventional packed-bed reactor has disadvantages, such as hot spots, delays in start-up, and mass and heat transfer limitations. For micro-scale reactor, the pressure drop is somewhat higher due to space constraints of channels being blocked with catalysts. A micro-pump used in portable applications may not be capable of overcoming a high pressure drop. On the other hand, microchannel reactor offers advantages, such as fast heating and cooling, large surface-area-to volume ratios, and less energy input The packed-bed reactors as a classic system, have disadvantages, such as hot spot, slow start-up, and heat and mass transfer limitations. Micro-structure scale of this group utilizing a micro pump is necessary, due to high pressure and channel blockage [10]. Some research has shown that wall-coated reactor performs better than packed bed reactor for SRM reaction various researches has proofed better performance of the wall-coated than packed bed reactor for SRM reaction[11, 12]. Experimental Catalyst preparation Firstly, 200 ml deionized water was heated to 80ËÅ ¡C and then metal nitrates of Cu, Zn and Fe (to prepare CuZnFe) were dissolved into the water until get the 0.2M solution. This solution was added to the heated water (80ËÅ ¡C) over stirrer under 350 rpm. To control and adjust pH around 7, the precipitation agent of 0.5M Na2CO3 was used. The obtained precipitates were aged at 60 ËÅ ¡C for 2 h under vigorous stirring. Afterward, the solids were filtered and washed with warm deionized water for several times and dried at 110 ËÅ ¡C for 12 h. then, the dried powder was calcined in a furnace at 350 ËÅ ¡C for 4h. Catalyst slurry preparation PVA (87-90% hydrolyzed, average mol wt 30,000-70,000,SIGMA-ALDRICH) was added to deionized water first, and stirred at 70 C until totally dissolved, then cooled at room temperature. As-synthesized, high-performance CuZnFe catalyst (10 wt.% catalyst) was added into the PVA solution (0.5 wt.%, 1 wt.%, 2 wt.% PVA) as-prepared. The catalyst slurry was kept in the ultrasonic bath for 1 h. Catalyst coating by electrophoretic deposition on stainless steel plates To prepare a regular, controlled catalytic layer, a well-stable suspensions of the catalyst powder are necessary which depend on the particle size, solvent characteristics and additional agents. To do this, the powder were milled to get a uniformity of particle size distribution below 40 micron, at least. Isopropanol was selected as solvent due to lower conductivity limiting solvent transportation than of the aqueous ones. Moreover, presence of aqueous base cause water electrolysis following poor coverage of catalyst. Electrophoretic deposition was performed at constant voltage (140 V) using a power supply unit (SPS-900NP-Navasanpardaz). The stainless steel (AISI-304) palates (7.04 cm2) were used as electrodes in the EPD bath. To cover both sides of the plate, a system including three electrodes was selected which, were mounted at a distance of 15 mm in a cell with a total volume of 120 ml. slurry of 72 g/L of catalyst in isopropanol and 1 g/L of PEI as binder was prepared through 15 min strongly stirring and then, 15 min signification in an ultrasonic bath (1200M-Soltec). The time of 4 min as coating time was fixed for all samples. After coating, the plates were dried in room temperature and then calcination at 350 C for 2 h. Method and materials According to the procedure in fig. 1, a series of CuZnFe slurries and samples were prepared. The synthesized powder was milled at 250 rpm for 10 min (due to initial fine powder structure short milling time was chosen) by a milling apparatus. It make a stable behavior of the slurry and homogenous final layer deposited. Results and Discussion After the coating procedure, the changing structure of the CuZnFe catalyst, the operating parameters and micro-channel characterization affect the efficiency of hydrogen in the output. In this study, explored a number of vital parameters characterization, including channeling arrangement and shape, coating methods and the efficiency of hydrogen production. Micro-Channeling Theory Design and micro-channel arrangement optimization cause select an appropriate structure limited by performance efficiency, constant cost like startup, Fabrication, and variable costs (Catalyst stability, coated layer quality, appropriate life time). Regardless of the constant costs, overall state and changing catalytic plates while the plates have been channelized, replacement and re-channelizing, coating procedure should be more difficult. Although, chein et. Al. [13] adopt three types reformer including the microchannel, the plain channel and the inserted catalyst layer while utilizing channeling over cover plate is different. All proposed structure of a square microchannel have been shown below†¦Ã¢â‚¬ ¦Ã¢â‚¬ ¦. In this research, flexibility and replacing of an aged micro-reformer has been emphasized, an appropriate configuration with the minimum of fabrication cost through a recoverable coating procedure, minimum catalyst consuming and high efficiency has been adopted. A treated stainless steel as active layer was coated by the high efficiency CuZnFe catalyst which coated in an electrophoretic bath under a high controlling ability condition. The EPD producer will be discussed elsewhere, in detail. According to the optimum condition of a constant parameters, type of micro-channels, length and stability have been investigated. Reactor design The reactors were designed as flat-plate composed of stainless steel 304 plates. The microstructures were introduced by CNC technology. The both cover plate were machined to cover the active catalytic layer and increasing area to volume concept. The active layers were coated by home-made synthesized high efficiency steam reforming catalyst. Subsequently, the housing sealed by graphite gasket and bolts. The size and number of channels are summarized in table 1. Table 1.  Summary of the dimensions of the reactor: the channel dimensions are only provided for the reformate side of the plates Parallel channel Zig-zag channel Length(mm) Wide(mm) Depth(mm) Length(mm) Wide(mm) Depth(mm) The test plates and reformer design details are shown in fig. 1. On the top side of the cover plate, as shown in fig. 1(a), microchannel were patterned zig-zag path to reduce pressure drop along the path, holding high activity of the catalyst through the contact time increasing.(ref) the feed methanol-water mixture is sent to the vaporizer section including an inert alumina granule packed developing the heat transfer, and then, collected in an triangle manifold in the reformer inlet to obtain a more uniformly distributed flow. The design of the reformer channel (as shown in fig) leads splitting-jointing in an alternatively manner. In order to identify the reactant flow pattern effect on the reforming performance, the reformer channels shown in fig.1 were investigated. Catalyst coating The results of coating procedure, have been shown in fig 2. For all the plates, the same catalyst loading of 25mg was coated. Experimental setup A schematic diagram of the experimental setup is shown in fig. 3. The main components of the system are reactants, micro-reformer and products. To provide the heat of the reaction an electrical furnace was used controlled by a TIC. The feedstock system including methanol-water in liquid phase was sent by a syringe pump (model nnn) in a designed feed composition and determined S/C= 1.3 in all the tests. The reformed gas stream was then sent to a cold trap to eliminate the unreacted liquid phase. In continues, the rest of the gases was conducted to a gas chromatography equipped via two columns of carboxen and hysep Q (model shimadzu GC-8A). Based on the achieved fractions and compositions, the methanol conversion, CO selectivity, hydrogen yield and stability of the active layer cab be achieved. A K-type thermocouple connected at the end of the holes which designed to measure temperature of determined spots along the axis, default of the measurement is based on the central point of the reformer for all the tests. Results and Discussion 50 mm parallel microchannel Fig. 4 and fig. 5 display the performance of the microchannels according to the length. The investigation was performed under different temperature and micro channel types. It can be observed that the methanol conversion rates with various lengths is no different although the magnitude of this depends on the micro channel arrangement and for the direct parallel channels is more obvious. In the experiments, the effect of reaction temperature could overcome length and full conversion of methanol was achieved, finally. For the zig zag type, by variation in length in a range of 20 to 50 mm, no difference was observed. The arrangement cause more efficiency in reduction of surface to volume ratio. Actually the need of a sufficient contact time of the reactants on the catalytic active sites is necessary for a satisfying conversion. In the zag-zag type the contact time will increased and the at least of the sufficient length of full conversion is about 25mm. other lengths below those was not possible due to the limitation of the mass flow controller. On the other hand, being endothermic of MSR, the least requirement heat of reaction can be supplied by increasing of the contact time on the cover plate which is contacted to the heating source, consequently following the micro channel length. About the CO content, however, due to being full conversion in considered lengths, there is no significant different among the cases. Higher conversion can cause producing some more CO in the outlet. On the other hand, sufficient existing catalyst affect the CO production due to being active rWGS in lower loading of the catalyst. (ref). Zig-Zag microchannel Felani et al. [ ] proposed that a novel channel arrangement with a certain sizing could guarantee better flow distribution, higher contact time being accessible of reaction and heating, and lower pressure drop than those of conventional ones. The proposed model can increase the methanol conversion. Fig. 6 shows the illustration of the micro-reactor with such zig-zag microchannel. The performances of parallel microchannels and that of zig-zag microchannels are compared by the present experiment. The micro-reactor in this study is different from that of chein et al. [13]. In chein’s paper, the reactor only has simple inserted plate without channelizing. It is noticed that in this experiment novel catalyst of CuZnFe has been used and the goal of this experiment is not the comparison of the cases. Advantages of easily replacing, lower costs of recoating and flexibility managing of the fuel processor. Fig. 7 shows the variation of the methanol conversion with the temperatures. It c an be found that with the increase of the temperature, the methanol conversion decrease. The conversion in zig-zag microchannels were higher than those in parallel microchannels. When the temperature is high, methanol conversion in zig-zag microchannels could be 20% higher than that in parallel microchannels. As mentioned before, zig-zag microchannels induce potential of providing more contact time to react under the help of catalysts, thereby enhancing the methanol conversion. Conclusions In this paper, the experiment of methanol steam reforming were performed in a micro-reformer coated with novel CuZnFe catalyst. The following conclusion can be achieved. 1. The impacts of reaction temperature, gas hourly space velocity, H2O-to-CH3OH molar ratio and catalyst stability were also investigated in this stainless micro-reformer. Condition selection of optimum operation can be achieved by these useful guidance. 2. Micro-reactor with two types microchannel arrangement, including zig-zag path and parallel microchannels, different lengths of 15, 30 and 60 mm were evaluated. It is found that methanol conversion in microchannels with zig-zag path are much higher than that of parallel path. In addition, since zig-zag path cause more contact time of the reactants on active sites of catalyst, there is no different of methanol conversion with length variation, while in the parallel path, it was obvious that higher length leads to more methanol conversion. References [1] D.R. Palo, R.A. Dagle, J.D. Holladay, Chemical Reviews 107 (2007) 3992-4021. [2] L. F Brown, International Journal of Hydrogen Energy 26 (2001) 381-397. [3] C. Liao, P.A. Erickson, International Journal of Hydrogen Energy 33 (2008) 1652-1660. [4] J.-H. Wee, Renewable and sustainable energy reviews 11 (2007) 1720-1738. [5] S. Bose, T. Kuila, T.X.H. Nguyen, N.H. Kim, K.-t. Lau, J.H. Lee, Progress in Polymer Science 36 (2011) 813-843. [6] R.Y. Chein, Y.C. Chen, Y.S. Lin, J. Chung, International Journal of Energy Research 36 (2012) 466-476. [7] A. Basile, A. Iulianelli, T. Longo, S. Liguori, M. De Falco, Membrane Reactors for Hydrogen Production Processes, Springer, 2011, pp. 21-55. [8] V. Hessel, S. Hardt, H. Là ¶we, Chemical micro process engineering: fundamentals, modelling and reactions, John Wiley Sons, 2006. [9] H. An, A. Li, A.P. Sasmito, J.C. Kurnia, S.V. Jangam, A.S. Mujumdar, Chemical Engineering Science 75 (2012) 85-95. [10] X. Ouyang, L. Bednarova, R. Besser, P. Ho, AIChE journal 51 (2005) 1758-1772. [11] A. Karim, J. Bravo, D. Gorm, T. Conant, A. Datye, Catalysis today 110 (2005) 86-91. [12] J. Bravo, A. Karim, T. Conant, G.P. Lopez, A. Datye, Chemical Engineering Journal 101 (2004) 113-121. [13] R.-Y. Chein, Y.-C. Chen, Y.-S. Lin, J. Chung, International Journal of Thermal Sciences 50 (2011) 1253-1262.

The Florence Baptistery :: essays research papers fc

People often try to imitate a finished product if it has become popular. When this is done after several years it is considered a revival. Usually the artist or patron has a purpose such as modeling after a powerful culture or religious significance. They may slightly change or mix other styles to make the best of past and present. In Florence Italy there stands a baptistery. It resides west of the Florence Cathedral, which was modeled after the baptistery. The Cathedral began in 1296 by Arnolfo di Cambio. Although the two resemble each other, they are considered to be from two different styles. The Baptistery of S. Giovanni is categorized as Romanesque while the cathedral is considered Gothic. The exterior of the cathedral doesn't appear to be Gothic, it's the interior that is. The baptistery possesses an octagonal structure with an extension to the west. This extension was originally an apse. There are doors to the north, south, and east sides. All of the doors are decorated with beautiful sculptures. The first doors were done by Andrea Pisano and set the standards for the next to come. The second set, the first done by Lorenzo Ghiberti, were originally hung on the east end, but were soon moved to the north side to make room for the final set. These final doors, by Ghiberti, have earned the name 'Gates of Par adise.'; The name S. Giovanni was given to the baptistery because of the remains of Piazza S Giovanni found beneath the floor in a medieval cemetery. Historians have argued the baptistery's date for a few hundred years and it is still completely unsure what is it. The first recorded documentation of the baptistery's existence was March 4th, 897. Many have come to agree that the original constructed was during the 6th and 7th centuries and much of the restoration happened around 1059. Through the years nature's forces have taken their toll upon the San Giovanni. Several restorations have been made to the exterior and the interior since the 10th century. The most drastic change done would have to be the exterior marble. Around 1293 the corner pilasters were reconstructed with alternating slabs of green and white marble. This technique wasn't ever seen in the Florentine school and was assumed to have originated in Pisa. The use of alternating marbles and the arcade sills wrap around th e entire building. It gives a sense flowing continuity.

Declaration of Sentiments: Blog Response Essay

After 156 years, you would think that the issues brought up in the Declaration of Sentiments would have been resolved by this day, but unfortunately that is not the case. Since the dawn of capitalism, developing around the same time period the Declaration was written, it has become one of the most powerful (if not THE most powerful) economic structures in the world. It is no coincidence that this structure has become increasingly dependent on the destruction of women’s self-image, self-respect, and self-worth in order to sell more products. In the Declaration of Sentiments, one of the grievances listed recounts men’s continuing dominance over women’s self- respect. It reads as follows: â€Å"[Man] has endeavored, in every way that he could to destroy her confidence in her own powers, to lessen her self-respect, and to make her willing to lead a dependent and abject life.† It’s heartbreaking to see that this issue is still so pervasive today. It is not a learned behavior to hate one’s own appearance, hate one’s own size, and to feel as though there is a rigid sphere in which a person should inhabit. All of these self-worth issues have repeatedly been projected at women by men for years– whether it be through religious standards, social norms, or in this case, through profit. This method is much more insidious and less blatant than the traditional concept of men literally exerting physical dominance over women. In fact, the destruction of women’s self-worth via modern capitalism is so normal that it goes completely unnoticed. It’s because of subtleties like this that some people believe that sexism is no longer a problem. However, many people don’t seem to give any thought to the fact that women aren’t born believing that they are not pretty enough, not the right size, and that there are only a set amount of career options for them. Around age seven, a roughly equal number of boys and girls have ambitions to become the president of the United States. However, when asked the same question again at age 14, the number of girls with the same ambition dropped significantly . Most of the sexism perpetrated today feels normalized and flies under the radar for most of the media-consuming population. Another subtle way in which sexism exists isn’t even committed by men—women are taking part in a cycle of misogyny and hatred of the members of their own gender. Very commonly nowadays you see young girls and even grown women claim to be different from their female peers in order to seem more appealing to men. It’s a very simple self-perpetuating way for misogyny to exist without ever being perpetrated by males. With the â€Å"not-like-other-girls† mindset, women are pitted against other women, as opposed to standing in solidarity against the very institutional sexism they have been unknowingly perpetuating. Girl-on-girl hate has been sensationalized and normalize in the media via television shows (see Gossip Girl), movies (see Mean Girls), and books (see The Clique series) all of these are specifically targeted for young girls. Often the antagonists of these stories are female peers and the happy ending or â€Å"reward† is finally getting to be with which ever boy that has been lusted over for the length of the story. While they do highlight the very real issue of bullying in schools, these stories do little to nothing to promote the friendship and commonality that young girls have together. In relation to the aforementioned grievance, self-image doesn’t have to be limited to one’s personality or appearance—it can refer to one’s gender, and can lead to the dislike of members of one’s own gender. It’s easy to focus on the issues that have yet to be resolved. However women have made many strides since this Declaration of Sentiments was written. One of the first monumental movements started, led, and accomplished by women was women’s suffrage. This led to later allowing women the equal opportunity to work in office. Smaller yet equally necessary movements have been sprouting all across the globe such as body positivity, anti-street harassment, and sex positivity, which aims to get rid of the double standard between men and women’s sexual activity. Although many feel sexism has been irradiated it is still very much alive despite the many victories women have had. Socially, politically, and sexually women have been repressed and overpowered but with hopeful generations massive amounts of development is yet to come. Bibliography Cogdon, Jessica, Claire Dietrich, and Jenny Raskin. Miss Representation. Prod. Jennifer S. Newsom. 22 Jan. 2011. Television.

Neighbors essays

Neighbors essays On the street where I live, I see vibrant azaleas and blooming roses in my neighbors flowerbed. I see kites gliding through the sky on a cool spring afternoon as if they were angels on a cloud. I see the beautiful skyline of Memphis, TN and the bright lights of the Memphis Bridge as I look off of my balcony. I see large boats sailing down the Mississippi River. I see children playing and riding their bicycles, smiling as if it were the greatest day of their life. I see people walking, jogging and roller-skating on the river walk. I see some people lying on blankets just enjoying the moment, leaving the stress and pressures of their jobs and the world behind them, taking time out to enjoy family and self. I see fathers playing catch with their sons and mothers reading novels. When I look down my street I see happiness. On the street where I live, I hear crickets chirping, bees buzzing and birds singing. I hear the horns of cars, tug boats and trolley trains as they pass my apartment building. I hear dogs barking and howling to the screeching sounds of the fire truck sirens. I hear construction workers yelling, jackhammers pounding the concrete and the shifting gears of dump trucks driving away. I hear the up-tempo roar of motorcycles drag racing down the street. I hear the sounds of a trumpet coming from the Taylors apartment two doors down from mine. At twelve p.m. I hear the bells ringing from the local Catholic Church. I hear the sounds of the inner city. On the street where I live, I smell the aroma of mesquite bar-b-que. I smell sweet bubble gum ice cream as my son eats his favorite dessert. I smell freshly cut grass and the stench of mulch in the air. I smell fragrant flowers and honeysuckle overridden by the smell of burning oil at the local refinery. On the street where I live, I feel a cool breeze off the river blowing in my face. I feel the vibration from the train as it crosses the bridge. ...