Distillation column design nptel pdf

Many of these factors will be adjusted as design progresses, but you will want to know what your targets are at the beginning. Catalytic cracking, cracking reactions, zeolite catalysts. Chemical engineering chemical engineering design ii nptel. Graphical determination of a distillation column design step 1. So, under which we will first consider design based on individual mass transfer. Engineering design guidelines distillation column rev. We have worked out our flow rates using hysys and we obtained the following data. Distillationabsorption column tray design che 4253 design i tray spacing. From a capacity viewpoint, a liquid rate greater than 6 gpm inch of weir weir loading, is the rate at which a higher number of flow paths should be considered. Che396 senior design distillation 7 theory section 1. Equilibrium separation column in equilibrium separation processes, two or more coexisting zones are created with preferential distribution of the different components involved in the process in each zone. A simple design method for multicomponent distillation columns d. The distillate flow rate of light key component that is a is. A distillation column is sized by determining the diameter of the tower.

Column diameter and pressure dropflooding determines the minimum possible diameter of the absorber column, and the usual design is for 60 to 80 percent of the flooding velocity. A simple design method for multicomponent distillation. Repetition of this type of calculation for different conditions produces a design chart like that shown in figure 8 for the ethanolwater system. Whatever be the earlier conception, today a chemical engineer is expected to be able to make complete design of a piece of chemical equipment. Nptel chemical engineering chemical engineering design ii joint initiative of iits and iisc funded by mhrd page 2 of 30 lecture 1. Design and construction features of column internals 1. A read is counted each time someone views a publication summary such as the title, abstract, and list of authors, clicks on a figure, or views or downloads the fulltext.

The gasliquid contact in a packed column is continuous, not stagewise, as in a plate column. In contrast, continuous columns process a continuous feed stream. Pdf on dec 1, 2015, maneet goyal and others published design of distillation column for separating a mixture of benzene and toluene. Perform overall material and component balances to determine the. High vacuum distillation in the column revamps structured is use to increase capacity and reduce. Packed hydraulic engineering design guideline author. Large if froth is expected, also allow space for crawling 12 to 24. Cracking feedstocks and reactors, effect of process variables. Design size a distillation column with condenser and reboiler operating at atmospheric pressure with constant reflux, to separate and purify an equimolar mixture of benzene i, toluene ii, ethylbenzene iii, and oxylene iv, containing 100 kmol of each, at molar fractions of 0. In batch operation, the feed to the column is introduced batchwise. Distillation operation, control, design and troubleshooting course for maintenance personnel introduction the success of every company depends of each employees understanding of the businesss key components. It is particularly well suited for high purity separations since any degree of separation can be obtained with a. Employee training and development will unlock the companies profitability and reliability.

Distillationabsorption column design che 4253 design i 1800 or earlier now. These trays promote mass transfer of light components into the vapor flowing up the column and of heavy components into the liquid flowing down the column. Plate and packed towers, number of plates, diameter and height of the. Design of batch distillation columns using shortcut. Turndown ratio in any plant is the ratio of maximum to minimum throughput it can process to produce the products with the desired specifications. The principles of vacuum distillation resemble those of fractional distillation commonly called atmospheric distillation to distinguish it from the vacuum method, except that largerdiameter columns are used to maintain comparable vapour velocities at reduced operating pressures. This design guideline covers the basic elements in designing a typical distillation column system, which includes column internals selection and sizing. Included in this guideline is an example of the data sheet used in the industry and a calculation spreadsheet for the engineering design. In the simplest case, the products of a distillation process are limited to an overhead distillate and a bottoms, whose compositions. Rao, amit kumar, ashok kumar, devendra agarwal, abhishek sinha department of chemical engineering, indian institute of technology, kanpur 208016, india abstract. Distillation and absorption are two most widely used mass transfer processes in chemical industries. Process design decisions and project economics by dr.

This note emphasizes on the development of design skills among the students to take design related decisions. Chemical process plants include a number of important equipment such as reactors, distillation columns, absorbers, heat exchangers, evaporators, crystallizers, etc. In the earlier lecture i told you that for separation of 3 component mixture, we need minimum 2. Pdf design of distillation column for separating a mixture of. So, we start our lecture with sequencing of the distillation column.

Mod05 lec01 introduction to distillation and phase diagrams. Petroleum refining petroleum refining vacuum distillation. Mechanical design of equipment addresses the stress. The numbers of flowpaths of liquid on tray are 1, 2, 3 or 4 as per liquid capacity requirement of column. In designing a distillation column, the thermodynamics of the vapor and liquid phases must be understood. The liquid flows down in the column over a packing surface and the vapor or the gas moves countercurrently, up the column. With the mccabethiele method, the total number of necessary plates, as well as the feed plate location can bidd if i lbbe estimated, and some information can also be determined about the enthalpic condition of. Several mechanisticallybased models have also been developed to help the design and optimization of cssp distillation columns linek et al. In nearatmospheric applications, pressure drop usually needs to be minimized to reduce the cost of energy for compression of the feed gas. Distillation control is a challenging endeavour due to 1 the inherent nonlinearity of distillation, 2 multivariable interaction, 3 the non.

So, the basis of the design for these columns are that we determine the number of stages the location of the feed to the column and the reflux ratio. Throughout design, tradeoff decisions will be made to arrive at an optimal design using distillation column design best practices. To design a distillation column, start with vaporliquid equilibrium. Thus the sizes, particularly the height, of distillation columns are determined by the vapour liquid equilibrium vle data for the mixtures. Nptel chemical engineering chemical engineering design ii joint initiative of iits and iisc funded by mhrd page 33 of 41 lecture 6. The most difficult part in the distillation column design is the description of this equilibrium between the vapour and the liquid. Nptel chemical engineering chemical engineering design ii joint initiative of iits and iisc funded by mhrd page 36 of 41 ii. The steps required for tray column design are shown in figure 5. Dear all, i am a final year student at nanyang technological university singapore, currently working on my chemical engineering design project, and my group and i have been tasked to size a methanol recovery tower in a biodiesel plant.

Packed distillation columns packed columns are used for distillation, gas absorption and liquidliquid extraction. Chemical engineering design by nptel download book. Design of plate column for absorption and distillation involves many common steps of calculation such as determination of number of theoretical plates, column. Introduction to distillation column design principals and best practices. Design concept of crude oil distillation column design.

It is relatively straightforward to derive models of distillation columns. Now, in this lecture we will mainly focus on design of packed distillation column. Computer aided design of distillation column article pdf available in journal of applied sciences research 1117. Distillation is based on the fact that the vapour of a boiling mixture will be richer in the components that have lower boiling points. Column tray and packing design university of oklahoma.

Design of plate column for absorption and distillation involves. Pdf mechanical engineering design of ipa distillation column. Design of such equipment should be carried out a priory to setup a process plant and thus, it is basic step in a chemical process. Forced circulation reboilers with vertical or horizontal tubes boiling may be designed. Multicomponentdistillation calculation methods are classified as rating or design methods. Moholkar,department of chemical engineering,iit guwahati. To describe the degree of separation between two components in a column or in. Therefore while designing the vessel stresses induced due to. The vast majority of industrial distillation columns are equipped with trays or plates sometimes called decks in the petroleum industry located every feet up the column. Distillation a process in which a liquid or vapour mixture of two or more substances is separated into its component fractions of desired purity, by the application and removal of heat. Introduction the typical gasliquid contacting operations include distillation, absorption, stripping, leaching and humidification. Citations are the number of other articles citing this article, calculated by crossref and updated daily.

A stepwise procedure for continuous distillation column design. Article views are the countercompliant sum of full text article downloads since november 2008 both pdf and html across all institutions and individuals. The design for a new packed distillation column for consideration as a new experiment for the university of florida department of chemical engineering unit operations laboratory was created to demonstrate the separation of water and isopropanol ipr and to evaluate a parallel applied multicorrelation approach to creating a high accuracy. So, to start with we do the complete material balance across distillation column. That is, the column is charged with a batch and then the distillation process is carried out. A sensitivity analysis was also done to make sure the column could withstand changing conditions like temperature and contaminant concentration. An initial estimation of the tower diameter can be done based on the vapor and liquid loadings in the column. Atmospheric distillation in the refining process is the separation of crude oil into various fractions. The vapourliquid equilibrium characteristics indicated by the shape of the equilibrium curve of the mixture will determine the number of stages, and hence the number of trays, required for the separation. The stripping column was designed to meet the specifications set in the design conditions, while also being as costeffective as possible.

The final column design used a 6 ft high packing of. These metrics are regularly updated to reflect usage leading up to the last few days. Introduction to column distillation distillation is the most common separation technique in chemical process industry, accounting for 9095% of the separation operations this is why more than a half of this course is devoted to distillation or column distillation, which includes binarymixture distillation. Determine process operation variables assumed feed rate, composition, purity of distillate and bottoms, and the quality of the feed are known. The vaporliquid equilibrium vle determines the minimum number. What is turndown ratio of a distillation column and what. When the desired task is achieved, a next batch of feed is introduced. For example, in distillation a liquid and vapor zones are created and the components are separated in different proportions between these zones. Equilibrium separation column jordan university of. If you are following the traditional approach, youve probably designed your column for reflux rates in the range of 1. Nptel provides elearning through online web and video courses various streams. This may not give you a column that can handle upsets well, so you may want to design for a capacity slightly greater than that increasing the flows by about 20% might be wise. What you need to know about distillation columns design. Distillation principles chemical engineering, 200711, rvce.

350 288 1554 1092 250 616 947 208 1441 141 249 1009 397 1 872 1198 1541 1217 816 1156 47 362 639 1626 724 121 1493 1583 1157 10 1299 297 898 1495 998 1440 1297 1147