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STELA Laxhuber GmbH
Öttingerstr. 2
D-84323 Massing
Tel.: +49 (0)8724/899-0
Fax: +49 (0)8724/899-80
E-Mail: sales@stela.de
www.stela.de

 

 

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Grain drying
Process and applications in modern agriculture

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Introduction

Ever-increasing cultivated areas for growing cereals (also by mergers) require specific harvest plans to finish the harvest in the shortest possible time with most effectively utilized machines.
The harvest plans can be drawn up early considering the sowing time and the sort. These schedules must be kept as exactly as possible as otherwise the complete operation for the rest of the year will be delayed.
On the other hand, more and more supply contracts are concluded with a fixed date. The weather situation is and remains the great element of uncertainty.
In Europe, a lot of farmers still rely on a "dry" summer to harvest the grain with a storable final moisture. With this method, however, you depend completely on the weather and risk your economic success totally.
Harvesting in time, in connection with a powerful drying plant, makes you independent of the risk factor weather. Especially annoying are thunder storms and hail a few days before the official harvest date, as the year 2002 showed in an extreme way.
Furthermore, the harvest has been recently reduced locally to less than 14 days by the permanently increased performance of the harvesting equipment. Therefore, the trend towards more and more powerful drying plants continues. Mobile and easily movable systems make it possible for the operator to react more flexibly to the demand on the market.

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Drying methods

Grain is dried by means of hot air. This classical drying process is simple and has gained acceptance in the field of agriculture, as a powerful, high-quality and careful drying is achieved. The investment and operating costs are low compared with other methods like freeze, vacuum or radiation drying.
An essential division of the drying method results from the hot air generation.

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Hot air generation
               
There are the options of direct and indirect hot air generation for the drier.
The modern burner systems distinguish themselves by a very clean combustion of the used fuel. The combustion gases consist almost completely of carbon dioxide and steam; both are main constituents of the air around us. With direct air heating, these combustion gases are mixed with approx. 60 times the amount of fresh air and are led into the drier as hot air.
A lot of investors also think about an indirect air heater when buying a new drying plant operated with fuel oil. With indirect air heating, the combustion gases are drawn off separately from the fresh air to be heated through a chimney. The air heater works on the heat exchange principle.


Comparing both systems direct / indirect air heater makes the functioning principle clear.

With direct air heating, the heat of the combustion gases is added to the heated process air. Thus the firing efficiency is 100 %. The direct air heater consists of an outer casing, an intermediate casing against radiation losses and an open combustion chamber made of highly heat-resistant steel, which is arranged concentricly.


1a) direct air heater

With indirect air heating, combustion chamber and gas passes as heat exchanger areas are divided constructionally from the process air areas. The indirect air heater consists of an outer casing, an intermediate casing against radiation losses and a closed combustion chamber with gas passes made of highly heat-resistant steel. On demand, there are even indirect air heaters which can be changed over at direct heating in almost no time.



1b) indirect air heater

The indirect air heater has a disadvantage compared to direct heating: a firing efficiency of 100 % will never be achieved because of physical principles.
Therefore, the achieved efficiency has to be minded most when an indirect air heater is bought. If, e. g., 5000 t of maize are dried in one season (from 35 % to 15 %) and an oil consumption of approx. 25 liters is assessed for 1 t of wet maize, so a worsening of efficiency of e. g. 2 % at the indirect air heater means an increased consumption of 0. 5 liters per ton wet maize and for the whole season 2500 liters!
Consequently, indirect air heaters with an efficiency of approx. 80 % have a seasonal increased consumption of fuel oil of 12 500 liters – money that is really burnt.

Direct or indirect air heater – it is a fundamental decision which should be preceded by a market analysis. A detailed consultation by the manufacturer, whose technical design should be scrutinized most exactly, is recommended anyway.


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Drying principle

Drying processes are based on the principle of energy transfer to the product to be dried, which gives off moisture as a countermove. This moisture is taken up by the passing air and taken away. Consequently, the product to be dried gets warmer and drier during the process, the drying air gets moister and cools down. 
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Constructive designs

Generally, the construction of the so-called roof drier has proven itself. Specially it means that the air is taken in and carried off through horizontal roof-shaped air ducts, which are open downwards. In between, the product trickles through the drier by means of gravity. Horizontally arranged hot air and exhaust ducts run through the vertical product ducts. The optimized roof shape of these ducts guarantees an even product flow.
The roof-shaped ducts are open downwards at full length. The hot air streams into the column at the front side of the hot air roofs and then flows through the piled-up product. The product heats up, gives off its moisture to the passing air and dries. As a countermove, the air cools down and takes up moisture up to the saturation limit, depending on the product. The moist air escapes through the neighbouring exhaust roofs. This air is sucked out of the drier through the exhaust fan. The constructional design of the roof ducts guarantees an optimum and even drying result with the highest product care.
The throughput quantity is adjusted by means of a computer-controlled discharge. Furthermore, the construction guarantees easy transversal mixing and thus an even drying result. Then the desired operating mode of the drier is the main difference in process.
There is the possibility to operate the drier in continuous-mixed-flow mode or in the so-called circulating batch mode.
Modern drying plants are built in modular design, which makes it possible to meet exactly the customer's requirements concerning capacity and design.
 

                                       

Construction of the roof drier. Red: hot air supply (= hot, dry air), green: exhaust air (= cool, moist air), orange: product
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Environment

A certain amount of dust is in the exhaust air when grain is dried. A drier, however, can be equipped today according to the legal environmental rules without any problems.

Almost unnoticed by the public, new rules of the German federal immision law are valid since 01.01.2002. New limit values for the admissible dust content of exhaust chimneys and ducts were specified in the technical instructions for the air; the limit value was reduced by 60% from originally
50 ppm to 20 ppm.

For new plants, this requires a powerful dust extraction system according to the latest state of the art; conventional simple dust cyclones will not cope any more with these requirements.

For this application, there is a proven dust extraction system on the market – the centro separator.


                                        
                                         Zentroabscheider Typ ZA

This is a centrifugal separator which achieves a remarkably high separation degree by means of its clever double-cyclone design with internal diffuser (inlet guide vanes) with, at the same time, a compact design. Compared only to the air capacity of a cyclone (the increased separation capacity not yet taken into account), a centro separator is about 70 % smaller in size.


With the centro separator, the dust-laden air is led into a vortex chamber and put into rotation with only slight radial component. The dust particles then move to the side of the vortex chamber. Together with a small partial air-flow and by means of a tongue-flap in the last part of the spiral, the dust is separated from the main air-flow, led into the secondary separator and discharged.
A cylindrical baffle plate system reverses the direction of the air-flow in the vortex chamber before the cleaned air leaves. Thus the remaining dust particles are thrown outside and also led into the secondary separator.
This secondary separator has the shape of a cyclone the cone of which is bent. The cleaned secondary air is led back into the main air-flow through the central pipe.

The centro separator has a further important characteristic, especially for difficult installation sites: it produces the same result in every possible position. No matter whether it is installed horizontally, vertically or even diagonally, the result is always the same.

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Technical developments

The continuous-mixed-flow drier with roof-shaped air ducts works according to a proven system, nevertheless the technical development does not stand still. Today light and especially noncorrosive aluminium structures can be used because of an optimized design. The air duct system in the drier was optimized.
There is an excellent heat and air distribution by means of the modern burner technologies, gas line burners or fuel oil burners with air heaters or in small upright air heater units with several burner units spread out over the drier width. This has a direct effect on the evenness of the drying and guarantees a high product quality with low energy consumption.
Not least on request of the market, the existing product range is enlarged by new-developed drying plants. Especially as far as mobile driers are concerned, more and more powerful models are mass-produced. The control engineering makes it possible today to automate a drier in such a way that the operating personal can reduce the time needed for the drier to a minimum. The computer-controlled product feed and discharge and the automatic discharge control according to the final moisture can be mentioned as an example. The absolute on-line moisture measurement and control makes the permanent check of the final moisture possible without the usual measuring effort with conventional moisture measuring instruments. In the same way, the drying temperature of circulating batch driers can be varied depending on the drying time by means of the so-called Multi-Therm automatic system. Here great importance is attached to a still more careful temperature course

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Quality and profitability

Both aspects have always be regarded together. Profitability means maximum throughput rate with the lowest possible amount of energy. Either the operator himself determines the marks of quality or they are stipulated by his prospective customer. Each requirement going beyong the normal quality demands is cost-intensive. Working economically here means that only fully ripe, cleaned grain with a harvesting moisture as low as possible is dried to shelf life just below 15 %. Special requirements go for very long stock holding periods e. g. in intervention storehouses. Here usually final moistures of 12.5 up to 13 % are required. This means that residual moisture is a quality criterion, the required longer drying time and the higher amount of energy reduce the profitability. The future customers partly prescribe special quality criteria like e. g. the maximum admissible drying temperature or indirect air heating. Such parameters, however, justify a higher market price as they go beyond the normal quality requirements. Then you can produce quite profitably by means of the price. .
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Buying advice

Generally, the prospective buyer has to decide on the size and design of the drying plant. Here there are a lot of questions the prospective user of a drying plant has to answer himself in advance. Of course, the competent plant manufacturer helps as well.
A plant should neither be projected too big nor too small as there arise problems in operation with both extremes. Nevertheless, the drier should be as powerful as possible as the energy consumption decreases with an increasing throughput capacity. Here an active heat recovery by means of a circulating system has an especially positive effect.
Basically, there is the possibility to install and operate a drier as mobile or stationary plant.
Mobile driers can be used without much effort for assembly, installation and permission. They especially distinguish themselves by keeping their value. A mobile drier can always be exchanged against a more powerful drying plant.
The customer should insist anyway upon high-quality, corrosion-resistant and thus long-lived materials like e. g. aluminium. Purely galvanized driers are not to be recommended any more for reasons of corrosion. Mixed constructions made of chrome steel and galvanized sheet metal should be avoided because of the development of chemical reactions („Le clanché“ element, „primary cell“). The life span makes a more favourable calculation possible when a drier is bought.

By means of the energy cost, the cost budget for the drying of e. g. grain and a profitability study can be drawn up quickly. This is also based, of course, on the price that can be achieved on the market.
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Outlook


The last years have been marked by a concentration and centralization in the field of drying and processing of cereals like grain or e. g. also maize. Drier manufacturers have to be able to meet with this trend by means of a wide range of drying plants. Besides the increase in capacity, the operator demands long-lived and high-grade quality. Mobile or movable systems make it possible to react to the market conditions fast and flexibly.