processing lines and equipment for the instant coffee industry
TRANSCRIPT
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Processing Lines and Equipmentor Instant Coee Powder
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Everyone appreciates the convenience o
using a spoonul o instant coee to makean enjoyable cup o coee. Behind the
convenience, however, lies the challenge to
the beverage industry o processing the coee
bean types (Arabica, Robusta) to deliver aroma
and avour in the cup that appeals to the
consumer.
At Anhydro we know all about the important
role each instant coee processing stage
plays in creating the fnal product properties
that ensure coee drinking pleasure. Our
coee policy is about basing our instant
coee processing lines on our own specialized
liquid concentration and powder processing
technologies while, collaborating closely
with independent company members o
the Anhydro Coee Processing Technology
Alliance (ACPTA) who specialize in other
essential aspects o instant coee processing.
Our coee policy and oerings
This means that we can leverage our
international contract management andengineering experience going back over 60
years to oer our customers ully engineered
instant coee processing solutions that employ
the latest technology to ensure the right end-
product specifcations and consumer appeal at
the lowest possible total cost.
Our oerings include the design, engineering
and supply o processing lines with capacities o
150, 250 or 500 kg/h o instant coee powder
(see the table below or urther details).
In addition, we undertake modernization,
capacity upgrading and retroftting o existing
processing lines as well as the supply o
individual equipment items. This includes
auxiliary equipment (or steam raising/water
treatment, stand-by power generation, tote bin
powder storage, product laboratory analysis
etc.).
Capacity and Yield Data
Instant coffee powder capacity (kg/h) 150 250 500
at 3% H2O
Annual production (t/h), based on 7,920 1250 2000 4000
annual production hours
Corresponding green coee at 12% residual 345 - 360 550 - 575 1100 - 1150
moisture requirement* (kg/h)
Corresponding roasted and ground coee at 290 - 300 460 - 480 920 - 965
6%residual moisture requirement (kg/h)
Extraction yield based on roasted and ground 53 - 55 53 - 55 53 - 55
coee, based on Robusta (%)*Assuming 16% roasting loss
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Coee powder overview
The drying stage in the processing line is selected according to the desired end-
product properties and morphology o the instant coee powder. The three main
types o powder are as ollows:
Non-agglomerated Instant Coee Powder
This type o powder consists o individual spherical bead-like particles
giving the powder its ree-owability and good solubility in hot water.
It is most economically produced in spray dryers with tower drying
chambers. Powder bulk density is adjusted through inert gas injection
into the concentrated coee extract prior to high pressure atomization.
Agglomerated Instant Coee Powder
This type o powder consists o either medium-sized or large agglome-
rates with a minimum o small particles (fnes) present, giving the powder
superior ree-owability and solubility in hot and cold water. Medium-
sized agglomerates are most economically produced in spray bed dryers
incorporating uid bed agglomeration within the drying chamber. Large
agglomerates are best produced in a dedicated powder agglomerator
where spray dried instant coee is rewetted and dried under strictly con-
trolled conditions.
Granulated Instant Coee Powder
This type o powder consists o large granules and the absence o fne
particles gives the powder excellent ree-owability and solubility in hot
water. It is most economically produced in reeze dryers where the low
temperature drying environment maximizes aroma retention. The size
o the granules is determined by the degree o size reduction and size
classifcation applied to the rozen extract.
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Equipment requirements
Processing lines to produce coee powders
comprise various stages involving dierent
technologies within solids, liquid and powder
handling. Equipment requirements in these
stages are as ollows:
Coee Bean Handling
Coee Bean Cleaning Equipment
and Storage Silos*
Coee Bean Roasters*
Coee Bean Grinders*
Coee Extraction
Liquid-Solids Extractors
(Percolator Battery Columns
incorporating the high-yield dual-
dual extraction mode or achieving
premium coee extract quality)*
Coee Extract Handling
Extract Cleaning / Clarication
(Filters / Decanter-Centriuges)*Aroma Recovery
(Flash Separation,
Distillation / Stripping Columns)**
O-favour Removal*
Extract Concentrators
(Falling Film / Plate
Evaporators, Parafash)**
Concentrate-Recovered Aroma
In-line Mixing (Non-Foaming)**
* Equipment designed and supplied by members o the
Anhydro Coee Processing Technology Alliance (ACPTA).
** Equipment designed and supplied by Anhydro.
Applying Anhydro extract preparation techno-logy enables customers to beneft rom:
High Yield Perormance
(53 - 55 % o R&G Coee, depending on
the coee bean type, quality and blend)
Flexible design permitting dual-dual and
dual-split continuous operation
Intermediate cooling o the aroma-rich
raction during extraction to promote
aroma retention
Linear percolator extractor arrangement
Ease o capacity increase by installing
additional percolators in-line
Integrated aroma recovery system
Integrated system or removal o
undesired o-avours
Thermal extract concentration under
gentle conditions to promote aroma
retention
Reuse o the condensate rom extract
concentration or CIP cleaning and
percolator cooling, promoting highly
efcient water usage
PLC / PC Process Control
Process stages involved in the productiono spray and reeze dried coee powders
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Spent Grounds HandlingMechanical De-watering Screw Press**
Coee Extract Drying Freeze Dryers*
Spray Dryers**
Spray Bed Dryers**Coee Powder Agglomerators*
Powder PackingPacking lines or tins, jars,
bags or sachets*
Integrated PlantPLC Control System
Project Management
by Anhydro
* Equipment designed and supplied by members o the
Anhydro Coee Processing Technology Alliance (ACPTA).
** Equipment designed and supplied by Anhydro.
Anhydro drying technology enables customers
to beneft rom precise control o important
soluble powder properties:
Colour (brightness) o the fnal soluble
coee powder
Particle size distribution and powder
structure / morphology
Bulk density
Residual moisture content
Aroma retention
Flowability
Solubility
Mechanical stability
The latest technology includes Anhydros spray
dryer air disperser and drying chamber designs
that enable production o powder having the
desired particle morphology and taste through
enhanced retention o desirable aromatic
volatiles.
The Anhydro extract concentrate gas injection
and dosing unit installed on the high pressure
side o the spray dryer eed line represents the
latest design concept in the important area o
powder bulk density control and coee powder
brightness.
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Schematic diagram o a Falling Film Evaporator
with fnisher or high extract concentration.
Green coee bean handlingand extraction
The initial handling o green coee beans
involves the removal o oreign matter
ollowed by bean roasting and grinding.
Both operations are determined by the bean
blend and the desired degree o roast. Thepreparation o a concentrated coee extract
rom the roast and ground coee beans is
perormed in a series o high-yield percolator
battery columns operating continuously under
the so-called dual-dual extraction mode to
obtain the highest yields. This provides a
primary extract raction rich in aroma, and a
secondary hydrolyzed extract raction. The
high-quality aromas in the primary extraction
are recovered by ash separation ollowed
by immediate condensing and storage under
chilled conditions.
The process rom coee bean to powder
The coee bean type and the bean blend composition, together with the processing
conditions, determine the taste and aroma characteristics o the fnal coeepowder.
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Coee extract treatment andspent grounds handling
Preparing the extract or drying requires a
cleaning operation to remove remaining coee
grounds by fltration or decanter-centriuging,
ollowed by extract concentration. This
concentration is obtained in a alling flmtubular evaporator under vacuum at low
temperature or gentle extract handling. A
fnisher evaporator must be installed ater
the main evaporator in order to obtain coee
extracts with a solids content o 55-60% DM.
As the aroma is removed rom the coee extract
prior to concentration, the vapour condensate
ormed during evaporation is very pure and
ree o colour and odour. This condensate can
be reused as washing liquid in the Cleaning-in-
Place system o the processing plant.
The concentrated extract rom the evaporator
is mixed in-line with the liquid aroma raction
to orm an aroma-rich eed or the subsequent
drying stage. Extract concentration is essential
or achieving good product quality and easibi-
lity in the drying stage.
The extraction process results in waste product
consisting o substantial amounts o wet
spent coee grounds. These grounds can be
mechanically dewatered to reduce the moisturecontent, enabling their use as a bio-uel in the
plant steam generation boilers, and resulting in
a considerable reduction in uel costs.
Coee extract drying
The method o drying depends upon the
required powder properties. Spray drying is the
most widely used, producing either agglome-
rated or non-agglomerated coee powders.
The spray dryer design and operating conditions
determine the type o powder that can be
produced. Freeze drying produces a larger
particulate in granular orm. Granules are
generally associated with the premium quality
o powder, but spray drying can also produce
top quality powders in terms o avour, aroma
and colour when produced rom the best
quality green beans.
Spray drying eatures the spraying (atomization)
o concentrated extract into hot drying air. The
spray droplets dry to orm a non-agglomerated,
ree-owing powder consisting o large
individual spherical bead-shaped particles. An
agglomerated powder with low fnes content
can be produced by combining spray drying
with powder uidization in an integrated uid
bed built into the spray drying cone base (the
spray bed drying concept).
Powders consisting o very large agglomerates
are produced in a separate agglomeration
process in which spray dried powder is rewetted
by steam, agglomerated, and dried using
uidization and cascading powder principles.
Freeze drying includes pre-reezing, oaming
and reezing o the concentrated extract
ollowed by granulation - sieving o the rozen
granules, which are dried in trays (batchprocessing) or on a moving conveyer belt
(continuous processing).
On reezing, the water in the concentrated
extract orms ice crystals, which sublime under
the inuence o vacuum and applied heat to
leave a dry granular product. Sublimation is the
direct phase transition rom solid state (ice) to
gas phase (vapour). The conveyer belt permits
much shorter drying times, promoting improved
aroma retention as the coee granules are
exposed, only or a relatively short time, to thevacuum conditions inside the reeze drying
sublimation chamber.
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L-15-eng
Anhydro provides a ull range o evaporation
and drying equipment or the global dairy,
ood and beverage, industrial, healthcare,
pharmaceutical, and starch and ethanol indu-
stries. Focusing on exibility and attentiveness
to individual customer needs, Anhydro enables
excellence at every point along the value chain
as part o our commitment to our customers
success.
Anhydro acts as a strategic development
partner or leading manuacturers all overthe world. Through close collaboration
with our customers, Anhydro promotes the
development o innovative concepts and
optimization o existing processes, enabling
customers to introduce new products into the
market as quickly and as cost eectively as
possible.
Anhydro A/S
7 OestmarkenDK-2860 Soeborg
Copenhagen, Denmark
Tel: +45 7027 8222Fax: +45 7027 8223