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De Humidifier - Dehumidifier Products - Air Treatment - Climate Control
Munters continuous research and development of existing
and proven techniques result in high performing Quantum™
desiccant drying wheel (rotor) - for demanding process
drying applications.
The gentle and energy efficient drying of products requires
ingenious system solutions. In this respect, solutions based
on desiccant dehumidification rotors are increasingly
replacing hot air systems, particularly when it is a
question of sensitive products such as vitamins or active
ingredients, or extremely thin layers, such as water-based
paints for example.
An important application of the process drying is spray
drying, which converts liquids into powder-based substances.
In general, spray drying is operated by hot air in a
temperature range between 150 and 300 °C. The substance to
be dried is blown through a top-mounted spray lance into a
spray tower and dried by the hot air. Due to its low
relative humidity the process air has a high water
extraction potential and provides a high degree of drying.
The performance of a spray tower is limited by the amount of
energy that can be supplied by the hot air. If an increase
in performance is required there are two possibilities:
either the temperature of the injected air is increased or
the air humidity is decreased. For sensitive products such
as milk or vitamins the injection temperature is reduced to
80 – 100 °C, in order to maintain quality, so that in
essence production can only be increased by drier air. In
this respect desiccant rotor based systems provide high
efficiency and uniform process conditions.
Air drying
Air drying systems according to the Munters principle use a
desiccant rotor for the drying of process air. From a
functional point of view a rotor of this sort is a
concentrator. The rotor consists of 86% honeycombed
micro-porous substrate with a very large surface area on
which a drying medium is deposited. As a desiccant material
Munters uses a titanium stabilized silica gel (Ti-HPS)
manufactured in-house. A rotor of this sort has an
operational life of over ten years.
The rotor is divided by a sealing system into a 90° segment
and a 270 ° segment. Process air is blown through the larger
rotor segment (270 °). In this way the humidity is absorbed
by electro-static attraction, i.e. water molecules
accumulate on the rotor. The smaller segment has hot air
from the counter flow blown through it, which activates the
accumulated water molecules. These break loose and are
conveyed to the outside by the desiccant or regeneration air
flow. In order to achieve continual drying of the process
air a drive motor turns the rotor 8 to 11 revolutions per
hour.
Rotor output
A silica gel rotor removes about 5 to 8g water per kg air
(g/kg) from the ambient air. The output depends on the
loading of the rotor and the temperature level of the
regeneration air. Fundamentally the lower the flow speed,
the larger the rotor (diameter and depth in the flow
direction) and the higher the energy input on the
regeneration side (higher temperature and greater quantity
of air) the higher the drying performance.
In Germany, a mean absolute humidity of the ambient air of
8g/kg is expected during the course of the year. For an
optimal drying process the humidity of the process air
should be about 2g/kg. If one assumes a rating for the
ambient air of 32 to 35 °C and an ambient air humidity of
12g/kg, the result for the process air is a volume flow of
25,000 to 120,000 m³/h (according to the size and
performance of the spray tower) with an injection air
humidity of 2g/kg. For a dehumidification output over 8g/kg
another technique must be employed.
Boost drying performance
If a higher drying performance (>8 g/kg) is required it is
conventional practice to fit a pre-dehumidifier with a cold
water cooler upstream of the rotor. The air is dehumidified
by being cooled to about 10°C in the cooler and the air
humidity condenses on the cold surfaces of the cooler. The
condensate drips into a collecting pan and is drained away.
The disadvantage of this system is that a cold water system
is required or an additional water cooling unit must be
used. Added to this there are the installation costs for the
pipe network and the additional operating costs. In addition
the condensate in the ventilator is considered to be a
health risk. The pre-dehumidifier has one big advantage,
however. This is the lower temperature required for the
regeneration of the rotor – about 125 °C. This temperature
can be provided by a factory steam network. As an
alternative to pre-dehumidification, high-performance rotors
may be used.
Quantum™ rotor, Munters High-performance rotor
The high-performance desiccant rotor dries the ambient air
without wet pre-dehumidification to an absolute humidity
value of 2g/kg, independently of the season and the ambient
air conditions. The rotor is a development of the titanium
silica rotor and uses a composite material of molecular
sieve (zeolite, which adsorbs gases, vapors and dissolved
substances with specific molecular sizes) and titanium
silica gel as desiccant substance. The additional outlay of
energy for the higher performance remains within limits and
does not increase out of proportion. For the regeneration,
however, an energy source such as natural gas or medium
steam pressure is required.
During adsorption the air in the rotor is dehumidified by up
to 14 g/kg and is heated concurrently to a maximum of 42K by
the zeolite in the molecular sieve, so that a post heater
for the process air can have smaller dimensions or be
restricted.
From a hygienic point of view dispensing with the wet
pre-dehumidification is a great advantage as no condensate
has to be drained away and the periodic cleaning of the heat
transfer surfaces of the pre-cooler is not required. The
energy efficiency of the system can be increased still
further using a rotor bypass. For favorable ambient air
conditions the bypass reduces the load on the system fan by
the lower pressure loss in the device.
Purge air lowers energy consumption
For processes with temperatures from 40 to 80 °C or
processes that do not need to run within the hygienic area,
process air pre-coolers may be used. In this respect it is
recommended that there is an exact inventory and analysis of
all fuels available on site. It’s very often the case that
the use of cold well water (or cooling tower water) can
positively influence the energy balance, in effect
compensating for a design feature by acting as a
pre-switching cooler for a high-performance rotor. The
cooler makes the rotor more absorptive and the dry air
outlet temperature is reduced. For fluidized bed dryers in
particular, which can be used for all types of powder and
instant products, a low process air outlet temperature is
required. For these applications “Power Purge” a
self-contained purge air process, is suitable.
To begin with the purge air withdraws thermal energy from
the part of the rotor that expels it from the regeneration
sector at about 120 °C. The hot purge air is fed into the
rotor segment that has just moved into the regeneration
sector and releases the heat to the rotor again. The process
increases the output of the rotor as the purge air cools the
rotor segment for process air drying and makes it more
absorptive. The energy consumption on the regeneration side
of the system is reduced by 30% and the temperature increase
in the dehumidification process by 20%, so that any post
cooler can be of smaller dimension or supplied with less
energy. The “Power Purge” process is also suitable for the
retrofitting for current rotor systems from 1000 mm rotor
diameter. For applications in the field of baby food or
other hygienic-relevant areas the use of terminal hygiene
filters is recommended.