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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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Belt drier with integrated CIP cleaning
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Short description:

Every owner of a belt drier, who demands certain minimum standards with regard to hygiene in his factory, knows the problems when cleaning his drier. Especially manufacturers of sticky products like e.g. coated cereals know the lengthy and arduous job of cleaning the drier tunnel.

From the field of food and dairy products e. g., CIP cleaning systems have been well-known for a longer time already, cleaning automatically with a greater number of stationary spray nozzles, tanks, piping etc. Such systems are out of the question for a belt drier. The reasons are, among other things, that numerous mobile parts of a belt drier have to be cleaned and the size of many drying tunnels requires a vast number of nozzles and, consequently, of cleaning solvent.

STELA Laxhuber now has developed a cleaning system with rotating high-pressure nozzles, installed on a slide moveable diagonally and longitudinally.

Rotating spray nozzles offer the best possible distribution of the cleaning solvents in all directions, that is to the front sides and the labyrinth sheets as well.

Through installation of rotating spray nozzles on an upper and lower slide, STELA has succeeded in managing with the lowest possible amount of cleaning solvents for this CIP cleaning system.

The regular drying process is not disturbed as the cleaning slide is situated outside the product zone.

The CIP system itself, which produces the cleaning solvent, can be conceived as a fresh-preparation cleaning because of the low amount of cleaning solvent required and the intensive cleaning. A batch cleaning system with several containers is not necessary.


Detailed description:

The integrated CIP cleaning system is used for cleaning belt driers for sticky and/or heavily polluting bulk goods or similar products.

The driers are cleaned via cleaning slides above and below the drying belts, which are equipped with rotating spray nozzles. Consequently, the areas above and below the belts are cleaned. The belt is cleaned in the separate online-cleaning station of the drier. The upper and lower slides each are supplied together and operated alternately. The supply of water and the cleaning solvents is carried out through 1” tubes with automatical tube take-ups.

The CIP system is installed as a compact unit on a base frame and consists essentially of a 2,500 l tank, a built-in recirculation pump, a heat exchanger, a re-rinseable screening unit and the proportioning equipment for the cleaning concentrates.

Cold water, hot water, lyes and acids are available as cleaning media. The cleaning tank is filled with water up to an adjustable amount according to demand. The water is cycled via the heat exchanger for heating. For preparation of acid or alkaline cleaning solvents, concentrate is dosed until the preselected reference value is achieved.

Pre-rinsing is carried out with cold or hot water, which is sprayed first over the upper and then over the lower sledges for one or two passages. The water rinses off easily detachable incrustations and washes them out of the drier. The considerably polluted pre-rinsing water is lead into the gully before the screening unit so that the sieve is not clogged.

Afterwards, a 1-2% soda lye or an appropriate cleaning agent is preparated and heated. The main incrustations are cleaned under the belt in circulation via the lower slide moving back and forth. For appropriate pollution, this procedure can also be carried out with the upper slide at first. When the temperature and the reference value have achieved the minimum values in return flow from the drier, this cleaning phase goes on for a preselected time or for a number of slide passages that have to be determined. Afterwards, the cleaning solvent is lead into the gully and the plant is rinsed with water.

Now, the drying plant is equally cleaned with nitric acid, with usually lower concentration and temperature and shorter cycles.

The re-rinsing with cold fresh water is carried out via the upper and the lower slide as long as the reference value in the return flow does not indicate residual cleaning agents any more.

A screening unit in the return flow prevents particles from flowing into the cleaning tank and from there into the nozzles and from clogging these nozzles. The current through the sieve can be changed through a bank of valves. When the surface of the sieve is clogged by the dirt, the pre-compression rises. The sieve is moved in a circle now and re-rinsed with a clean solvent directly from the tank. This automatic re-rinsing is possible at any time during cleaning.

The use of double-seat valves for the dosing of the concentrate and the distribution to the driers guarantees, in case of sealing failures as well, that the last rinsing water cannot be contaminated with chemicals. Furthermore, it is ensured that during cleaning moisture can never be pressed into another operating drier.

The nozzle systems are blown through by means of compressed air at the end of cleaning so that, after cleaning, water cannot drip from the nozzles onto the product to be dried.

At the front sides of the drier, the slides are moved to the wall to less than 700 mm each to drizzle these areas thoroughly.

Product distribution and drier screens are designed flexibly to enable the slide to pass.

Optionally, the scarcely polluted re-rinsing water can be collected and used for pre-rinsing of the next cleaning process to reduce water consumption for pre-rinsing.

The control is constructed as S7 with OP 37 visualization and operation. Communication is carried out via a H1-bus.

The cleaning process is determined by the CIP control. The programme can be started at the switchboard of the drier. The cycles are synchronized with the slide passages of the drier through a relevant exchange of signals.