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Master DonNTU Karpenko Olena

Olena Karpenko

Faculty "Mechanical engineering and machine-building"

Department of machinery and apparatus of chemical plants

Speciality "Machinery and apparatus of chemical plants" 

The adhesion of dispersed and granular media influence on the stability of the manufacturing process of the granulator running

Scientific adviser  Aleksander Parfenjuk 


About author

Abstract

Actuality of the theme
Aims and objectives
Basic concepts
Processes and methods of granulation
Factors affecting the adhesion of polymers to metals
Determination of the work of adhesion
Equipment
Conclusions
References
Actuality of the theme

    Protecting the environment from emissions of dust and harmful gases in the atmosphere for modern industries presently stands, along with the main characteristics of the enterprises. High concentrations of fine particles, whose size varies from micrometers to nanometers, released during the crushing, grinding and machining of various materials, causing enormous harm to the environment, leads to an irretrievable loss of large quantities of raw materials and finished product. Polydisperse dust, but as you progress through the material handling process, the content of the dust fraction less than 10 microns increases. All production units that produce dust, dust collectors installed devices, allowing not only to return a significant amount of finished product or semi-finished product, but also to prevent dust pollution of air pool plants and adjacent territories, so the collected dusts should be used. Finely divided materials used in production need to be processed because it provides a more convenient transportation, dosing, packing, reduced dusting and caking products. 

    Products from secondary processing of polymers are the grains. As the starting material are used waste products from polypropylene, polyvinylchloride, polystyrene, etc. Burning of these polymers is a serious threat to the environment, as this form dioxins  a substance hazardous to the human body and cause the appearance of malignant tumors. Reuse of these polymers can reduce the number of non-degradable waste. The most optimal solution for their processing is granulation, carried out mostly by extrusion, casting, crushing.

Aims and objectives

    The aim is to analyze the effect of adhesion and other physical and mechanical properties of dispersed and granular materials on the stability of the different types of granulators. When working pellet one of the main objectives is to ensure stability, since such conduct of all the main characteristics and parameters of aggregates and recycled materials do not exceed the allowable limits, ensuring the availability of units and raised the quality of products.

    Feature of the granulation process is intensive interaction of solid masses, located in a gas medium in the presence of liquid phase, with tools and surfaces granulators. 
In this case, the various possible interactions of both the regranulate working masses and granules, and contact interaction with work surfaces and the emergence of adhesive contacts prior to the termination of the granulator. These adhesive contact are: sticking, hang-up, layering, conglomeration, self-wedging. Particular influence mikroeffects dependent on raw material composition, surface quality, energy impacts, the regime of pressure and temperature. It is important to establish patterns of changes in the properties, determine the behavior of the working masses. Deviation of the allowable parameters will lead to undesirable for the normal course of events. The probability of occurrence of such manifestations will depend on the degree of deviation of material properties and influencing factors. Properties of the materials you need to know to further define the boundaries of their application. In particular, for use as filter materials for mass application, cleaning gases and liquids. This is especially true in the current conditions at large scale pollution.

    We analyzed the basis of adhesion: the theory of adhesion, the molecular interaction at the interface between the adhesive and the substrate and diffusion phenomena between them, forming an adhesive contact, methods of measuring adhesion, adhesion of polymers to metals, the strength of adhesive joints and mechanisms of their destruction. A mathematical model of fluidized bed method for dispersing the liquid particles in suspension was developed. The subject of study are the properties of dispersed and granular materials that could be decisive in ensuring the health pellet. These studies will be used to optimize the process of granulation and productivity machine.

Basic concepts

    Adhesion  a phenomenon compounds listed in the contact surfaces of condensed phases. These phases are the basis formed by molecular (across the interfacial area) contact adhesive joint and are called substrates, and the substances that provide connection to substrates  adhesives. Typically substrates  solids (metals, polymers, less glass, ceramics), adhesives  a liquid (solution or polymer melts, sometimes  low molecular weight products). Special case of adhesion  autogeziya realized at the molecular contact between two identical composition and structure of objects [8].

    Consider influencing factors on the adhesive properties of powders during  pressing (Fig.1 ) on the composite level.

img2

    Figure 1 – Scheme of laboratory setup for studying the adhesive properties of materials:
       1 
 cup 2  stand 3  mold, 4  sample, 5  punch, 6  shaft.


    In the process of granulation of powdered materials particles stick to the working surface of the device, which is caused by the action of adhesive forces. On the adhesion properties of the materials have a significant influence of humidity and particle size distribution. In assessing changes in adhesive properties of powders under external pressure shows that the adhesive force reaches its maximum value at relatively low specific loads. The specific pressure, which determines the maximum strength of adhesive bond depends on the type of powder, ie, from the crystalline structure of matter. With increasing specific compaction pressure seal structure of the sample accompanied by an increase in contact area of ​​particles to the surface of the punch, which leads to an increase in adhesive strength. Decrease in the adhesive bond between the sample and the punch in the high unit pressures due to the lubricating effect of a thin film of moisture on the contact surface, then squeezed out the pressed specimen. In this case the adhesive contact surface  the material is replaced by a weaker contact surface  liquid. When humidity powder, which is close to zero, the adhesion forces that occur at the contact surface, are determined by the surface energy of solid contact areas. Slight moistening of the samples leads to an increase in contact area, as sites of local vypressovyvaniya moisture to additional contacts, which is accompanied by an increase in strength adhesive bond. Further increase in moisture leads to the formation of a continuous liquid film on the surface of contact, which causes a decrease in adhesive strength, since there is a gap cohesional liquid film [6].

Processes and methods of granulation

Classification of the basic processes of granulation is shown here:

    Granulation process 

 From the liquid phase dispersion into droplets, followed by crystallization during dehydration or cooling; 

 From the solid phase by pressing, followed by crushing briquettes pellets desired size;

 A mixture of liquid and solid phase sintering of powders, followed by okatyvaniem agglomerates and hardening of relations between the particles when removing the liquid phase; 

From the gas phase condensation (desublimation) to form solid pellets; 

 A mixture of liquid and gaseous phases to the implementation of a chemical reaction; 

 A mixture of liquid, solid and gaseous phases to the implementation of a chemical reaction [6].

    Distinguish the granulation process: 1) proceeding without changing the particle size over time, 2) the change in particle size over time, 3) with the formation of new particles and growth of existing particles. Depending on the requirements for the grain composition of the product obtained by granulation of fine particles return to the process or not return. The effectiveness of the granulation process depends on the method of granulation and its hardware design [6].
In the granulation process are manifested almost all known types of physical-mechanical and physico-chemical bonds between the particles. 

    The action of capillary adsorption forces of cohesion between the particles due to the process of granulation by balling: agglomerates are formed from a uniformly wetted particles or layering of dry particles on the wetted core 
centers of granules. When granulation method balling are more productive links between the particles due to capillary forces, due to the use of liquidphase binding and the formation of crystalline bridges [6].

    Strong cohesive bonds form a dense structure of matter at granulating dry powder by pressing. One of the main manifestations of the adhesion, affecting the mechanism of granule formation by pressing are: 
 Education links between fine particles during their compaction on the basis of Van -der-Waals; 
 Ensuring the strength of the interparticle contact bonds due to the formation of additional bonds of crystalline type with subsequent cooling of the compressed product; 
 Surface tension of the wetted particles [6]. 


    When the atomization of the liquid melt on the surface of the particles is necessary to note the influence of adhesion:
 
 The probability of growth of grains on the surface of particles of a substance increases with increasing cohesive forces a drop of liquid and solid particles; 
With intergrown grains each agglomeration is possible for a sufficiently large binding forces between particles at the time of the collision  with an excess of fluid on the particle surface, since surface tension forces are more forces, providing relative motion of particles, and is sticking together; 
 The subsequent disappearance of the liquid phase (drying, cooling, etc.) form crystalline bridges connecting the pieces of durable agglomerate together; 
 Adhesive ability of the drop depends on the roughness of the surface material of granules, as well as fluid properties, the most important of which is the ratio of a drop of liquid and solid phases [6].
Factors affecting the adhesion  of polymers to metals

    On condition of formation of adhesive contact is influenced by the following factors: 

    Temperature regime 

    To fill the numerous indentations on the metal surface, the polymer melt must have a certain mobility. As the temperature increases the melt viscosity is reduced, it provides a high adhesion strength at the time of formation of adhesive contact. Supramolecular formation, existing in polymer melts, also hinder a more complete contact between the metal and polymer, but they are destroyed when the temperature rises. When comparing the experimental data, we can say that when reaching a certain maximum value of adhesion (strength of the joints was determined by dissection) starts decline, due to destructive and depolarization processes in polymers. Maximum adhesion is observed at a high content of polymers of vinyl, epoxide, carbonyl and carboxyl groups.The presence of polar groups in the polymer provides the appearance between the polymer and metal ion-dipole interaction and hydrogen bonding, which contributes to a sharp increase in adhesion. Also at high temperatures may cause chemical bonds of the Me  C, Me  C. The role of thermal and thermal-oxidative processes at the interface of the adhesive the substrate is sometimes more important rheological processes [2].

    Amount of plasticizer 

    In addition to temperature, the most important factor determining the formation of adhesive contact, is the amount of plasticizer. When introduced into the polymer plasticizer facilitates the achievement of contact between the adhesive and the substrate, reduced residual stress, but at the same time, deteriorating the strength properties of polymers. Therefore, there is an extreme dependence of adhesion strength on the number of plasticizer. Should expect an increase in adhesive strength with minor additions of plasticizer in adhesive acting as interpacket. Due to poor alignment with the polymer such plasticizers are introduced in the first place among the largest supramolecular formations, destroying them and thereby create more favorable conditions for the formation of adhesive contact [2].

    The nature and composition of the polymer adhesive 

    Polymers with low surface energy may form the metal is very strong adhesive bond. Nonpolar adhesive wets the metal surface is good, so even in the absence of active functional groups reached a certain adhesion. However, the stability of such compounds is low, a strong connection is achieved in the presence of functional groups that interact with the surface of the substrate. 

Free carboxyl groups present in the polymer, as well as hydroxyl, contribute to the achievement of high adhesion to the metal. The presence of the polymer, even a small amount of carboxyl groups increases the adhesion to the polar surface due to the formation of hydrogen bonds between the carboxyl groups of the copolymer and the factions HO metal oxide film is less than metal. When adhesion of the polymer to the metal part of the chemical nature of adhesive is critical. The adhesive must contain a certain amount of polar groups with the ability to enter into intensive interaction with surface groups of the substrate, for example, served as electron donors. For the adhesive systems is an important mechanism of interaction of polymer adhesives with the oxide film formed on virtually any metal surface. In many cases, at the polymer  metal may have ionic bonds, which are often realized at the contact of metals with carboxyl and hydroxylcontaining polymers [2].

    Nature of the metal 

    Maximum adhesion possess: nickel, steel, iron, minimum  tin and lead. Presumably, the location of metals in such a sequence is associated with their nuclear capacity: the lower the atomic volume of metal, the higher the bond strength of metal with the polymer [2].

Determination of the work of adhesion

         One of the most important parameters of adhesion is the work of adhesion. 

        Garkins reviewed the work of adhesion between two phases and linked it with the orientation of molecules at the interface [4].

        The work of adhesion is given by: 

f1,

         f2  – the surface tension at the interface between two fluids and these fluids at the interface with its own steam; 

Wа  – value that characterizes the work required to separate unit of the interphase surface between the two bodies fused at the two surfaces of these bodies on the border with its own steam. 

        Similar work is the separation of one body into two, called the work of cohesion (Fig. 2), is: 

f3 [4].

The difficulty for the practical application of this equation is a theoretical calculation of the work of adhesion. Have been proposed different equations to calculate the interphase tension, do not include the work of adhesion. If the two contacting phases are mutually insoluble, and their interaction is determined only by van der Waals forces, and the constant interaction obey the rule of geometric mean, then, for the interfacial free energy and adhesion work are valid equation Dzhirifalko and Hood: 

f4,

f5,

Ф – the interaction parameter contacting phases; 

f6

        V1, V2 – molar volumes of phases;
        А11 , А22 – their constant intermolecular interaction forces (Hamaker). 

 шimg

                        Figure 2  Scheme definition of the work of adhesion (a) and cohesion (b)[4].  

Parameter Ф varies from 0,5 to 1,2. 

If the interaction phase, with equal molar volumes and similar values ​​of the constants A, then Ф = 1, therefore: 

f7 [4].

          If the interaction between the contacting phases is solely due to dispersion forces, Ф = 1.

          Considering the surface energy as the sum of the growth rates of individual interactions, Fowkes proposed equation: 

f8,

         d, p  surface tension due to the dispersion and polar interactions; 


              x 
the rest of the surface tension, due to, for example, metallic bond, etc. 

        The equation can be rewritten as 

f9[4].

        Wu method gives the most correct values ​​of the polar and dispersive surface tension increments and calculate the corresponding work of adhesion: 

 f10

For two phases with similar values ​​of the polarizability dispersion contribution to the work of adhesion is calculated by the equation: 

f11,

and the polar growth rate of adhesion  the equation: 

                                    f12 [4].                             

    Knowing the corresponding growth rates, one can calculate the adhesion work of any contact tel. Targeted chemical and physical modification of polymeric fiber-forming materials can be made to reduce the dispersion and especially the polar component of surface tension and adhesion [4]

 

Equipment

    Granulators are classified according to various criteria. On mode of operation distinguishes devices continuous and intermittent, conical and jetting (Fig. 3). Fluidized bed can be heated fluidizing gas, which is used as heatagent (the most common method); overheating atomizing solution; conductive, through a heat exchanger in the bed. 

    By type of process aids are divided into without cycle and feed recycle; on design features 
for singleand multiple-chamber. A solution can be sprayed over the layer, feeding directly into the layer. The simplest device is a conformal cylindrical or rectangular, but there is a large carryover from the bed, since the rate of gas through the apparatus of the same height and liquefaction of the major factions, for fine rate of ablation will be more wandering speed. This disadvantage is eliminated in conical apparatus with increasing height section of the apparatus, so that the gas velocity in the upper layers is less than the rate in the lower layers, which ensures a boil polydisperse material [3].

шьп7

Figure 3  Types of facilities for dewatering and granulation solutions in a fluidized bed:
a 
 conical apparatus fluidized bed;  b  fluidized bed unit with the local fountain; в  cylindrical machines fluidized bed;  г  fluidized bed apparatus with spouting layer;
1 – solution;  
 heat-carrying agent; 3 retur; 4  the finished product [3].

    For the first construction of devices with spouting layer devices include a conical or cylindrical shape with an axisymmetric gas inlet (Fig. 4, b). The most widely used devices with a slit output gas (Fig. 4, ad). Slit air inlet provides a greater intensity of circulation, reliability and convenience of a large-scale transition. Obvious disadvantages of these designs is the uneven distribution of gas around the perimeter of the gap and a large hydraulic resistance machines [6].  

 i1

Figure 4  The main circuit apparatus spouting layer: 
a 
cylinder-conical  with the filing of the material on the layer; б  same with the filing of the material in the layer;  в with a conical insert; г  multisection slotted with a tangential inlet gas; д  the organized circulation of the material; 
fluidizing agent; II  the original material; III  atomizing agent; IV  finished granular product; V  retur; VI  separating the air; VII  the exhaust gases [6].

    Atomization – a process of increasing the liquid surface, carried out by transferring it into the statically unstable state  a thin jet, filament, film, and then in a statically stable – drops. Statically stable condition is in which the surface free energy is minimal, which is known to drop corresponds to a spherical shape. At the spraying is necessary to spend a certain amount of energy that is consumed as the creation of new surface (overcoming the surface tension forces) and to overcome the viscosity and the  transport to the newly formed drops of kinetic energy.  The simplest method of mechanical dispersion is the jet in which a jet of high velocity flows from the holes of small size. At the same time on the surface of the jet appear wavy deformation, leading to disintegration of the jet into small drops and the formation of flame spray [3].

    Technology "fluidized bed" is used not only for the granulation and drying of materials. Fluidized bed dryer used for drying various finegrained materials. Dryers are built in the form of cylindrical or rectangular chamber, inside which one or more of step gratings is in a "fluidized" state of dried material. To maintain a uniform "boiling" of particles in a layer of drying agent (air or flue gases) is filed under grill evenly and with appropriate speed distributed throughout its area. Submission of wet material on the grating is at the top of the drying chamber, and the selection of dried material is carried out at the level of the material layer at the bottom of the chamber (Fig. 5) [3].

img5

Figure 5 – Single-stage fluidized bed dryer:
1 – working chamber; 2 – sublattice space; 3 – grill; 4 – electrical fan; 5– cleanout; 6 – hydraulic threshold; 7– inning combustion (drying agent); 
8 – air flow for temperature control; 9 – exhaust gases by cyclone [3].

Conclusions

    In conclusion, this work must be said that the adhesion is an important factor influencing the process of granulation and working equipment. This multi-factor to be considered at several levels of the structure of materials: from the molecular to the composite. Knowledge of the adhesion processes occurring during the granulation, will calculate their value and, thus, to see the real picture of the granulation process. 

  Note! In writing this abstract master's work is not completed yet. Completion date: December 2011. Required materials on the subject and the complete text of the paper can be obtained from the author or his manager after that date.

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References

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  2. Берлин А.А., Басин В.Е. Основы адгезии полимеров. – М.: Химия, 1969.   321 с., ил.
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  6. Классен П.В., Гришаев И.Г. Основы техники гранулирования (Процессы и аппараты химической и нефтехимической технологии). – М.: Химия, 1982. – 272 с., ил.
  7. Лебедев П.Д. Теплообменные, сушильные и холодильные установки. – М.: Энергия, 1972.– 320 с., ил.
  8. Сайт о химии [электронный ресурс].– Режим доступа: http://www.xumuk.ru/encyklopedia


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