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Vector 10 (2015) 59 - 64 Design of a production plant of LDPE in Colombia
Cristian Felipe Jimenez-Varon1*, Reinel Tabares Soto2 1 Engineer. Professor, Department of Maths and Statistics, Universidad Nacional de Colombia, Manizales 2 Engineer. Professor, Department of Electronic and Automation, Department of Maths and Physics, Universidad Autonoma de Manizales, Manizales Recibido: 28/09/2015. Aprobado: 05/12/2015.
The present article is a study on the production of polyethylene as a product of the polymerization reaction of ethylene monomer, a
thorough analysis of its production, raw materials and catalyst required to carry out this reaction. The study begins by inquiring about generalities on the compound, physical and chemical properties, and current industrial applications.
Key words : Polyethylene, ethylene, polymerization, monomer, tubular reactor.
Diseño de una planta de LDPE en Colombia
El presente artículo es un estudio sobre la producción de polietileno como un producto de la reacción de polimerización del monómero de
etileno, un análisis exhaustivo de su producción, materias primas y del catalizador necesario para llevar a cabo esta reacción. El estudio comienza por preguntar sobre generalidades sobre el compuesto, propiedades físicas y químicas y aplicaciones industriales actuales.
Palabras clave: polietileno, etileno, polimerización, monómeros, reactor tubular
presence of a reaction initiator and thus produces tubular reactors polyethylene, low density.
Polyethylene is made from a raw material derived from petroleum: Ethane, and subsequently by reacting, Production and Characterization
ethylene monomer catalytic cracking is obtained.
The reaction for obtaining ethylene cracking is The polyethylene in the market is produced at a carried out at high temperatures and special conditions cost of between US $1200/t and US$ 1800/t, the average of pressure.
annual world production is 80 million tons, which Once the ethylene is obtained through a reaction of are directed to various processing industries where appropriate ethylene polymerization, several chains of polyethylene is used for molding processes such as ethylene are formed. This polymer has properties and blow types, compression transfer, among others, diversity of changes in pressure and temperature used for various applications where the polyethylene is in the processes.
Polyethylene is an olefin, a member of the family of The production plant of LDPE, was modeled for thermoplastics. The raw material for the manufacture is the production of about 12 t/h, from a feedstock flow high purity ethylene produced from ethane flows, from of 65 t/h of ethylene entering a compressor in order the gas oil cracking process, which in the Colombian to rapidly increase the pressure before entering the context is currently produced by the Ecopetrol industry reaction zone.
(Martin, 2005).
The main physical characteristics that contain the The high purity ethylene is subjected to high main information of each compound, including the pressure and temperature for polymerization in the principal raw material and product characterization that will be obtained, were found in Malppas (2012).
* Autor de correspondencia.
[email protected] (CF Jimenez Varón) Cómo citar este artículo: Jimenez-Varon C.F., Tabares Soto R. (2015). Design of a production plant of LDPE in Colombia. Revista Vector, 10: 59-64.
Cristian Felipe Jimenez-Varon, Reinel Tabares Soto / Vector 10 (2015) 59-64 radicals, for our process, benzoyl peroxide and Di terc butyl peroxide were used as substances Currently the only producer of LDPE in Colombia for the initiation of the reaction. Polyethylene is the Ecopetrol business group, which has two production requires a source of pure ethylene, suitable production plants, one in Cartagena and the other compression equipment to operate at about 2000 bar, in Barrancabermeja. Ecopetrol Business Group is the and a high pressure reactor to perform quick and high greatest supplier of raw material, and has high levels exothermic polymerization control. The process takes of production of this requirement, the plant plans to place in continuous operation.
build and operate in the municipality Puerto Colombia The process of production of LDPE, basically has located in the Atlantico department due to this town three key stages (see Figure 1) which are: Pretreatment, is near to the plant ecopetrol and it is a strategic site an essential step to adapt the conditions of pressure and given its port as an enabler to export polyethylene in temperature of the stream prior to entering the reaction the form of raw material (APCA, 2013).
zone commodities, this stage consists of equipment The location of the plant is chosen by the ease and such as compressors and heat exchangers, which ensure efficiency improvement in the processes of internal that the flow of the ethylene and the initiators being and external logistics regarding acquisition of raw introduced in the reactor of polymerization are at least materials and distribution of products and in terms 2000 bar and about 150 degrees centigrade. The second of transportation costs, distribution and cellar times key step is the reaction zone, this process is modelled of both raw materials and products.
in high pressure tubular reactors, which has a water vapor stream to ensure the temperature conditions in the reactor, the plant as a reaction zone is subdivided into four subzones, since injection points are the initiators for One of the beneficiaries of this project are the the start of reaction mechanism. The final part is the area petroleum businesses, since they would have a large of separation, consisting of a Flash equipment, which customer demand for its products as raw material, evaporates the amount of ethylene that do not react and produced as a product of petroleum. Also, there are then it is used in recirculation but also in the current industries getting benefits from the prosecution of obtained from the product (Textos Científicos, 2005).
plastic to finished products requiring the LDPE as raw material, not only in the national context, just as Riduco Reactor Operation
in the city of Manizales, but in the international context as well. All of this due to LDPE is the most widely used For this part of the process, an exhaustive review of the polymer in the thermoplastic industry worldwide for literature was carried out, from which the following conclusions were addressed: The polymerization The following companies are currently the largest reaction occurs by a kinetic chain reaction mechanism producers of plastic in the global market based on by free radicals, consisting of 10 semi-reactions (Odian, sales of chemicals: BASF, Germany Dow Chemical, 2004).
USA INEOS Group, LyondellBasell England, and Netherlands ExxonMobil, USA SABIC, Saudi Arabia · The tubular reactor is a PFR in countercurrent, DuPont, USA Total, France Formosa Plastics Group, countercurrent PFR, divided into 4 sections due Taiwan Bayer and Germany (C&EN, 2014).
to the injection of the initiators of the reaction Given that the plant that uses different resources derived from petroleum, this production would increase the commercialization of these derivatives · The reactor operating temperature is between 150- for various applications which would increase the development, and the economy of the country.
· The reaction works at high pressures in a range of 2. Methods and Structure of process
2000-3000 bars.
· The length of the reactor is about 1000 m.
Process Basic Structure
· The internal diameter of the tubular reactor is in a Polyethylene is produced from the polymerization range of 25-50 mm.
of ethylene. The polymerization reaction is sensitive to a very large number of catalysts and it is initiated · Conversion reactor is quite low for the process, particularly easy by compounds that produce free about 20 % (Cuevas, 2012).

Design of a production plant of LDPE in Colombia Figure 1. Flow-sheet of the LDPE production plant (Textos Cientificos, 2005).
3. Process Description
The reaction zone is conducted by a mechanism of Ethylene Pre-treatment
reaction of 10 reactions (Kienle et al., 2005).
The reaction rate constants (k) are represented by The ethylene required as input into this process modified Arrhenius equations (Kienle et al., 2005); is transported in tankers to withstand high pressure including the effects of temperature (T), change of liquid inflammable from the supplier company, pressure and Activation Energy: Ecopetrol. This is acquired and deposited in a storage tank at atmospheric conditions before entering to the process (Ecopetrol, 2014).
After it enters the process, it is initiated in the conditions of pretreatment to have the raw material prepared before being in the reaction zone.
Here K is the frequency factor specified for each The ethylene stream is required to be pressurized reaction, the term is the activating thus it enters a compressor prior the reaction zone.
Energy, IR the Gas constant and T is the temperature. After the content of ethylene stream is pressurized, The kinetics for the reactions is of first order, the it is split into two streams: The first one is going to kinetics parameters were found in (Brandup, 1989).
react to the first two reaction zones with injection of the The reactor is the central body in the production initiators, and this must react at a higher temperature.
process, this works continuously, therefore the The second stream enters another heat exchanger injection of the initiators should always be listed in each that should be operated at a lower temperature and also section of the reactor, and the tubular reactor shall keep enters the mixer with the injection of new initiators in its conditions of temperature, pressure and condition addition to the current coming from the reaction zone of phase to the reactive mixture, so that the kinetic rate 2. The mixture has to be carried out before entering the laws and reaction mechanisms are not affected (Dong reaction zone 3 and 4.
and Piet, 2004).
Different points in the reactor have steam inlets Reaction
in order to maintain an appropriate temperature and pressure conditions; this steam is supplied by a boiler The reaction process is carried out in PFR tubular producing it at medium pressure.
reactors, where a reaction mechanism of PCR is performed; this is subdivided into 10 reactions or Cristian Felipe Jimenez-Varon, Reinel Tabares Soto / Vector 10 (2015) 59-64 steps in the various stages of the mechanism, such of ethylene that does not react and is evaporated in as initiation, which generates free radicals that will the Flash separator. The reagent that does not react link with different chains of ethylene, forming a vinyl is carried out to some storage tanks, which have to polymer. Then at the stage of propagation different enter a purification process before returning to the transfers of radical and monomer occur in order to starting point.
gradually increase the number of chains formed. The storage tank must have hermetic conditions to Finally, the polymerization process is completed by maintain the pressure and temperature for the ethylene temperature conditions that disrupt the chemical stream.
bond formed, producing low density polyethylene in the temperature range established for the reaction 4. Results
(Idarraga, 2010).
LDPE is polymerized forming large chains and Simulation Process
generating enough entropy in the order of their bonds between monomers, causing a reduction of their The project was carried out using a process of density given that the internal structure has different simulation tools. The objective of this procedure was types of defects (Donald et al., 2004).
to generate the mass and energy balances from which raw materials were required. The utilities and energy Specifying the fluid service
needs are calculated.
The main simulation tool used was the commercial In order to preserve the conditions of the reaction, package Aspen Plus V8.0.
specify and justify the operating conditions, reactors The method of calculation of the properties for should have a thermal fluid service, which for our the polymerization process is known as the Sanchez- case is water.
Lacombe equation, also known as the basis Polysil method in the Aspen Plus software.
Sanchez-Lacombe equations are few models used to calculate thermodynamic properties of liquid solutions In the design of the production plant of LDPE, there for polymers (Dimitrios et al., 2011).
are two separators: Flash isothermal type, located at the exit of the reaction zone 4, which is used to reduce the Sanchez-Lacombe Equation State
pressure to an intermediate value at the atmospheric pressure, in order to carried out Flash separation is The equation of state of Sanchez and Lacombe (1976), is based on the theory of crosslinked flow, assuming that the polymer has a liquid structure · A total mass balance.
flexible. This limits the use of this equation a non- · A mass per component balance.
crystalline polymer. This equation is also used to · A total energy balance.
model the solubility of supercritical CO2 in solid and amorphous and molten polymers. It also describes The first Flash separator works at high pressures; the subsequent swelling of the polymer when the FSC the second Flash separator works at lower pressures in the polymer dissolves. Three considerations are (Lipatov and Nesterov, 1998).
necessary when Sanchez-Lacombe equation is used: In the Flash 1, the liquid phase contains the 1. The solubility of gas in the polymer represents a monomer and polymer, whereas the gas phase is a balance data, 2. the solubility of the polymer in the recycle stream since it is not a product. Ethylene by stage of high pressure gas is essentially zero and itself does not react.
3. Amorphous polymer about its glass transition The Flash 2 is assumed as an ideal separator for temperature can be modeled as a liquid (Rozzi and polymer-monomer mixture, the monomer is recycled Singh, 2006).
to the process and the polymer is removed from the Table 1. Simulation results.
Treatment of ethylene recirculation
Due to the low conversion in the polymerization Ethylene For Recirculation reaction that produces polyethylene, the large amount Polyethylene (LDPE)

Design of a production plant of LDPE in Colombia Figure 2. Scheme process for LDPE production.
Environmental analysis of the production of LDPE
this project.
The environmental analysis developed in WAR- The environmental analysis was performed with the GUI required: help of software WAR-GUI, which is an algorithm that analyzes the conditions and environmental impacts · Flow rate and composition of each in and out of the project from 8 different categories (EPA, 2011).
stream of the process.
The environmental potential impact was defined as the effect that could have on the environment emissions · Rate of energy consumption.
of gases such as ethylene and others that are part of Figure 3. Environmental impact by the formation of smog.
Cristian Felipe Jimenez-Varon, Reinel Tabares Soto / Vector 10 (2015) 59-64 As noted in Figure 3, the environmental impact is Dimitrios M., Prokopis P., Apostolos B., Costas K. (2011). Prediction largely marked by the formation of smog, aquatic and of the molecular and b polymer solution properties of LDPE in a high-pressure tubular reactor using a novel Monte Carlo approach. Chemical Engineering Science, 66: 1685-1696.
It must be taken into account that a process that Donald A., Pradeep P. Phulé. (2004). Ciencia e ingeniería de los uses raw materials derived from petroleum has high materiales. Thomson Editores: México. 1003 p.
emissions of carbonic gas into the atmosphere. Caution Dong M.K., Piet D.L. (2004). Molecular weight distribution in is required given the output currents of the process and low-density polyethylene polymerization; impact of scission mechanisms in the case of a tubular reactor. Chemical Engineering especially those that are gases.
Science, 59, 10: 2039-2052.
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quienes-somos/acerca-de-ecopetrol/. [Visitada en octubre de 2015].
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recycle of ethylene, it was concluded that the amount cgi/P100DZKT.PDF?Dockey=P100DZKT.PDF. [Visitada en octubre of ethylene that does not react is considerable, which affects largely the efficiency of the process, reaching Idarraga L.M. (2010). Características de los reactores flujo piston. only a 30 %. It should be recycled before a purification caracteristicas-de-los-reactores-flujo.html. [Visitada en octubre stage in order to increase the rate of the operative profitability of the production process of LDPE.
Lipatov Y., Nesterov A. (1998). Polymer thermodynamic library. Springer: Netherlands. 450 p.
Kienle A., Boll M., Schmith C.U., Schwibach M. (2005). Dynamic simulation of a tubular reactor for the production of low- density polyethylene using adaptive method of lines. Journal of APCA. (2013). Nuestra alcaldía, ¿Quiénes somos? Alcaldía de Computational and Applied Mathematics, 183: 288-300.
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Malppas D.B. (2012). Introduction to Industrial Polypropylene: Properties, Catalysts Processes. John Wiley & Sons: New York. 360 p.
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Odian G. (2004). Principles of Polymerization. John Wiley & Sons: Brandup J., Immergut E.H. (1989). Polymer Handbook. John Wiley: New York. 812 p.
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& Engineering News (C&EN). Disponible en: Textos Científicos. (2005). Obtención de Polietileno, Polietileno de articles/92/i30/CENs-Global-Top-50-Chemical.html. [Visitada en alta presión. Disponible en: octubre de 2015].
polimeros/polietileno/obtencion. [Visitada en octubre de 2015.
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