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Masters work

 

The student of group ÌÀÃ-03: Solovyeva Svetlana Valerievna

The supervisor of studies: prof. Markin Alexander Dmitrievich

Theme : " The analysis of efficiency of regenerative heaters in a contour of technical training college at calculations of thermal circuits of blocks TPP".

            The wide circulation of the phenomena of heat exchange in power, the industries, transport, and also during interaction with an environment has demanded a plenty of designs heat exchanges devices. These designs in each concrete case should provide an optimum combination of thermal efficiency, convenience of operation, whenever possible small capital investments and working costs.

 In the given work theoretical bases of calculation heat exchanges are stated. The basic methods of the description and elements of the theory heat exchanges are included classification of types heat exchanges.

The given work contains a laconic and exact statement of classical bases of the theory of heat exchange and modern methods of calculation and designing heat exchanges equipments of the most various purposes.

Heat exchanges provide transfer of heat between two or the big number of streams of the heat-carriers occurbing through the device. The basic characteristic of a design heat exchanges is the type of relative movement of streams of heat-carriers, mutual geometry of these currents. The most general configurations of currents are below considered.

It is necessary to emphasize, that the described configurations represent some idealization of real situations. In practice never it is impossible to reach current of the heat-carrier conterminous to ideal variant.

Under heat exchanges it is understood such devices in which make an exchange of heat between two working bodies. In heat exchanges devices there is an exchange between heated up and cooling working bodies, or the ferry therefore the modular condition of working ph changes.

Used working bodies exchange heat and may be: water pairs, warm water, gases, various soluble salts, liquid metals.

By a principle of work all heat exchanges may divide on:

 - recuperative;

 - regenerative;

 - mixing type.

The analysis of process of designing heat exchanges devices should be based on clear understanding of criteria on which work heat exchanges will be checked. Basically these criteria are simple for formulating, but the problems may appear is more complex for some special cases. The general principles of a choice of criteria are considered below by way of a degree of their importance.

First of all it is necessary to note, that there are two big groups heat exchanges, and each group demands various approaches to designing and manufacturing. Undoubtedly, the most part of existing surfaces of heat exchange is duplicated in many devices, such as automobile radiators, household and industrial conditioners, boilers, coolers of greasing of machines etc. For such heat exchanges are made by the industry of thousand or even millions identical units. Basically from economic reasons process of creation of this group heat exchanges is reduced to manufacturing some number of devices of a various design, all-round test within the limits of expected working parameters, to a final choice of the most successful design and, at last, to a batch production heat exchanges, most relatives to the chosen prototype.

In a number of industries, for example on chemical and oil refineries, are used heat exchanges which are developed and made by small partiess and are usually applied in consecutive or parallel configuration. Their batch production is at a loss, first of all, because of absence of an opportunity of wide tests outside of industrial process. Frequently these heat exchanger are intended for heat-carriers, structure, properties and ability to formation of adjournment, on which surface are known insufficiently and speeds of streams (so, and conditions of course of heat exchange) may change daily. Obviously, such situation shows more rigid requirements to designing if any chances of success made. The given part of a management(manual) is devoted basically to this case.

The first criterion of satisfactory work heat exchanges the device is performance of requirements on working parameters: required capacity of the device should be provided in an operating time from one preventive repair up to another at the given restrictions on difference of pressure and irrespective of increase of adjournment at surfaces. However it is necessary to note, that at designing always there is an element of uncertainty as warmly physical properties are seldom known with a high degree of accuracy, settlement methods are based on use heat exchanges the equations which accuracy is within the limits of disorder of experimental data, itself heat exchanges is produced with the certain admissions, real operating conditions òåïëîîáìåííèêà in different days íåîäèíàêîâû and adjournment, as a rule, appear a little bit big, than it was supposed in the beginning (besides they in due course change). Therefore requirements to performance data are carried out in practice not always. From this point of view it is not enough for quantitative estimations as the statistical data on work of separate devices, and data on influence of efficiency of their work on other processes of manufacture. Hence, the designer with the help of calculation, considering influence of an overall performance heat exchanges on other processes of manufacture, should guarantee reliable work of the device with the proved probability.

The second criterion consists that heat exchanges should satisfy to conditions, general(common) for all equipment., first of all, the mechanical pressure(voltage) connected not only with normal work, but also with loading, assembly, start, a stop, and also a number(line) of the certain operations caused by infringement of production and possible(probable) emergencies here enter. There are the external mechanical pressure(voltage) caused by presence of pipes in heat exchanges and arising both in a stationary condition, and in transitive modes at change of temperature of heat-carriers. In heat exchanges, certainly, there should not be a corrosion from influence of heat-carriers and an environment. It can be achieved basically a choice of a material, and also a design. Adjournment on a surface of heat exchange should be whenever possible minimal, but means of the designer in this case are usually limited to application probably higher speeds of pressure allowable on difference and restrictions on erosion and vibration, and also warranting of that the surface polluted with adjournment will be accessible to clearing

The third criterion represents the requirement of an opportunity of periodic repair heat exchanges which usually includes clearing surfaces, heat exchange, replacement of pipes, condensation and any other elements of a design especially subject to corrosion, erosion, vibration or ageing. This requirement also may become the reason of restrictions on accommodation heat exchanges and maintenance of free space around of him(it).

The fourth criterion directly follows from the second and the third and consists what the designer should take into account advantages of multisection configuration with valves It allows to repair serially each section without special damage for work of all device Such service in particular favourably for condensers and coolers? When one or more sections may remain without the heat-carrier in winter time Or be used for regenerative hot conditioning very cold heat-carrier

The fifth criterion is reduced to that heat exchanges should have minimally possible(probable) cost under condition of, certainly, that it corresponds(meets) to the listed above criteria At economy of initial cost, however, always it is necessary to mean, that the increase of working costs owing to reduction of the sizes and heat exchanges î the device will result decrease(reductions) of reliability to that any possible(probable) prize in initial cost will be spent at some o'clock or days

At last, there may be restrictions on diameter heat exchanges, length, weight and (or) on an assortment of pipes owing to requirements to a place of accommodation, transportation, an opportunity of service, storage of spare pipes and condensation

If not it is possible to reach the efficiency given for a concrete case, never it follows to develop heat exchanges in hope, that it may be used in other conditions. The most part heat exchanges devices intends for the installations having service life, equal or greater, than a resource heat exchanges. The assumption, that heat exchanges with bad design characteristics it will be possible to use for any other technological process, results, faster, to that neither work heat exchanges, nor course of process will not be effective enough. It is much better to work in the assumption, that the greatest hopes for success as at designing heat exchanges, and development of technological process in which it heat participates, are given with the optimum decision of the given problem.

If you the theme and an object of research given has interested masters works and you want to learn about it more in detail, write to me:

My e-mail: semicvetik1925@mail.ru

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