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Herbs in Africa
Part 4 - Dehydration apparatus
Ivor Hughes
Part four in a series of articles which outline the basic
requirements, for small scale, sustainable cultivation, and processing
techniques, for rural communities continues. Links: Part One,
Part Two, Part Three.
Next in this series: Extraction apparatus.
Introduction
The techniques for the preservation of foods, along with the manufacture of
stone and bone tools, must rank amongst the very earliest of humankind's
technological achievements.
Combination smoking and sun drying, was a common technique of hunter-gatherer
cultures, which still finds widespread usage today. Strips of lean meat (jerky
or biltong) may be quickly and efficiently preserved in situ, by smoking and sun
drying. The process of haymaking in temperate climates, is sun drying on a large
scale.
The sun drying of medicinal plants, or parts, is an extremely destructive
process, during which, up to 85% of the plants bio-activity may be lost in a 12
hour period. Compare that with warm air drying, where the economic loss may be
reduced to 35%, or with skill, to as little as 15% within the same period of
time.

The Production of Warm Air - Simple Drying Shed.
In the early days of large scale herbal cultivation, such sheds were
commonplace. The introduced innovations were the provision of heated air and
drying racks which replaced the bunching and hanging of the herbs undercover.
For the first time the commercial herb grower had a modicum of control over his
main production process. The gains were considerable. The grower could plan
harvesting and dehydration schedules and operate on a 24 hour basis at peak
harvesting times. Temperature control was rudimentary and relied upon the
opening and closing of convection vents and doors, and the damping controls on
the combustion stoves. Ergonomically they left much to be desired and the crop
dried in an uneven manner. This necessitated much turning and moving of the
harvested material. Today the technology has advanced considerably and many
high-tech solutions are available. However many of those solutions are not
appropriate to the needs of small scale community production.
Appropriate Dehydrator Technology.
Solar
Vertical Stack Dryer. New Zealand 1984. The photograph is of my first, owner
built solar dehydrator, which I operated across 3 seasons. The sheathing was
weather treated plywood. The solar air heating panel to the front of the
apparatus was constructed from scavenged materials. The solar heat collecting
plate was made from corrugated roofing iron, painted matt black. It operated on
the principle of warm air convection. I was able, during sunny weather, to heat
the drying chamber to 40°C. That was usually, on average, 15°C above ambient
temperature. Crude temperature control was achieved by means of an adjustable,
ambient air flap, opposite, and at the same height as the solar air inlet. The
stack, which stands above the drying chamber, houses two cheap plastic domestic
bathroom convection fans to assist the warm moisture laden air to be vented to
the atmosphere. The fans are powered by warm air convection and not electricity.
The shape of the drying chamber roof and the narrowing of the stack was intended
to increase the air velocity needed, to carry the vaporised water into the
atmosphere
Observations and Comments
The sheathing was three ply. So that in those months that it was used
operationally. Considerable solar heat gain was garnered. It was also light in
weight. The apparatus was constructed so that it could be easily stripped down,
and reassembled at a new site. Therefore it would have potential to be
manufactured in kit sets. Now that sounds like a good community project to me !
The dryer is simple. However some thought must be given to the size of the
drying chamber, which in turn influences the dehydrator herb loading. The size
of the chamber must also bear some relationship to the size of the cultivation.
This in order to prepare a proper harvesting and dehydration schedule. The size
of the drying chamber will influence the size of the solar panel. The panel must
be sized to give the required heat gain needed for successful operation. It
produced herb of good aroma and cosmetic quality. The negatives were, it was
only operational from sunrise to sunset. There was always a risk of dew point
being reached in the dehydrator during the hours of darkness. I would close the
dehydrator down at dusk. This I did by closing off the air inlet from the solar
panel vent and opening the dehydrator door in order to cool the heated herb down
to ambient temperature. This decreased the risk of dew point in the dehydrator.
The door was then closed and the ambient air inlet flap opened slightly.
Operations commenced again 45 minutes after dawn.
Different Types of Dehydrators

The Hybrid System
Considerable savings in energy may be achieved by including a solar air heating
panel as the air inlet for the heating plenum.
The horizontal stack and tunnel dryer are fuel burners and use electricity powered axial flow
fans. The
horizontal stack is side loaded. Pride of place 
must go to the tunnel dryer, for
use on the larger commercial cultivation. It can be constructed from adobe or
mud bricks, soil cement bricks or concrete blocks. It has a Solar hot air panel
which forms the roof. The furnace is constructed from a suitably modified 200L oil
drum, which makes it economic in operation. The major expense is the power
required for the fans. A system of vents allows for precise temperature
adjustments and the recirculation of air. The dehydrator climate may be modified
at will to allow the operator precise air and temperature control through the
various drying phases. The moisture laden warm air on exit may be suitably
condensed to produce single distilled water which bears a relationship to the
herb from which it has been stripped. As such, after a further single
distillation, it may be used as part of a hydro-alcoholic solvent, to extract
the herb from which it was recovered.
Useful Data
Enthalpy of Evaporation.
Solar Gain Chart
Conversion Technology

Combustion and Fuel Values
Combustion, or burning, is a chemical process involving carbon, hydrogen and
oxygen. Oxygen reacts with the fuel and produces combustion products, some of
which contribute to ozone layer damage. The reaction is sensed as heat and
light.
Combustibles may be solid, liquid or gaseous; and the fuel energy values that
follow should be read as mean global values, because the hydrocarbon chemical
content of fossil fuels, eg,. coal, oil or gas, vary according to the
geographical source. The same situation applies to bio-mass fuels, eg., wood or
ethanol.
Fuel Energy Values
|
Fuel Type |
Source |
State |
Energy kJ/kg |
|
Carbon |
Elemental |
Solid |
33,000 |
|
Coal |
Fossil |
Solid |
30,000 |
|
Coke |
Coal |
Solid |
28,000 |
|
Fuel Oil |
Fossil |
Liquid |
42,000 |
|
Kerosene |
Oil |
Liquid |
45,000 |
|
Petrol |
Oil |
Liquid |
45,000 |
|
Coal Gas |
Coal |
Gaseous |
20,000 |
|
Methane |
Bio |
Gaseous |
42,000 |
|
Natural Gas |
Oil |
Gaseous |
38,000 |
|
Charcoal |
Bio. |
Solid |
33,000 |
|
Ethanol |
Bio. |
Liquid |
28,000 |
|
Wood |
Bio. |
Solid |
20,000 |
|
Solar Energy |
Sun |
Radiant |
1.025 kW/m2 |
More Information:
Ivor Hughes
www.herbdatanz.com
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