
| GATE - 1993/01 - Solid Waste Management (GTZ GATE Magazine, 1993) |
| Focus |
From an End-of-Pipe Treatment System to In-Plant Methods
by Jurgen Pors
Depending on the raw materials, processes and end-products involved, the constituents of wastes from tannery operations vary in both quantity and importance. They include hair, hide scraps, pieces of flesh, blood, manure, dirt, salt, lime, soluble and insoluble proteins, sulphides, amines, chromium salts, tannins, soda ash, sugars and starches, oils, fats, greases, surfactants, mineral acids, dyes and solvents. The author discusses methods of controlling the most harmful pollutants.
Chrome tanning is carried out in rotating drums with chromium
(III) sulphate hydrate, starting at pH3.5 or lower and ending at almost pH 4 as
a result of basification. The chromium (Cr) penetrates the pelts, where it is
bound and cross-links the hide collagen molecules. About 6080 % of the chromium
in the bath is bound. The residual float contains about 6 g of Cr oxide per
litre (20 - 40% of the initial amount if no further additives are used.
Under
normal conditions the tanning bath is by no means exhausted. This is why
measures to improve chromium fixation in the leather and to recover chromium
from the residual float are of great interest from both an economic and an
ecological point of view.
Chromium fixation can be improved by a higher level
of basification, higher temperature, longer tanning periods and more
sophisticated chromium compounds. These measures will lower the residual
chromium concentration, but not sufficiently: chromium will still be found in
the sludge residue after effluent treatment. Moreover, the quality of the
leather produced by using these costly special agents (high exhaustion
techniques) cannot be maintained in the same way as when the conventional chrome
tanning process with 30% excess chromium sulphate is used.
This is why
tanners aiming for high quality and environmentally safe processes use the
conventional method, recovering the excess chromium from the used liquids by
precipitation (addition of alkaline substances to increase the pH) and
redissolution in sulphuric acid. The chromium can thus be reused for
tanning.
After chromium recovery the residual effluents meet all national and
international standard limits.
For the production of heavy leather, such as
sole, mechanical and saddle leather, vegetable tanning is employed - the
solution contains extracts from the bark of trees. The effluents from vegetable
tanning consists of tannins which are difficult to break down, cannot be removed
as easily as chromium and are intensively colored, causing a non-toxic but
highly non-degradable pollution load.
Chromium and sulphide
Since chromium and sulphide are the two most important and harmful
pollutants, they have to be removed from the effluents. This should be done as
close as possible to the point where they are generated. The widespread belief
that a spent chrome tanning bath is waste should also be refuted as quickly as
possible. Such liquids usually contain a quantity of chemicals: chromium (III)
salts are potentially toxic - the risk of oxidation to chromate cannot always be
excluded - and are valuable substances which should not be wasted. Thus, not
only environmental but also economic considerations are important.
Other
constituents of waste water are said to be reduced by pretreatment in the plant
itself: screening of solids and subsequent neutralization of alkaline partial
streams, followed by presedimentation, can be accomplished without any costly or
highly sophisticated techniques. Even small tanneries can implement these
pretreatment steps without any major investment.
Effluent control
Only if every leather processing plant carries out these
pretreatment stages can subequent chemical and biological treatment in an
ordinary effluent treatment plant be efficient and economical.
The present
state of the art in effluent control and treatment in Germany is a result of the
principle of treating effluents and pollutants as close as possible to the point
where they are generated. Only in this way can dilution or combination with
other effluent streams be avoided. Treatment, recovery or detoxification of
pollutants can be carried out with a minimum of equipment and at minimum cost
immediately following the point of generation.
Regulations should therefore
stipulate not only that waste water streams must be separated, but also how the
separated streams are to be treated, naturally in combination with different
standard limit values for the different constituents. Furthermore, regulations
should define minimum technical requirements, specifying which technology has to
be employed in order to meet them.
The approach to pollution control must
therefore be changed, from end-of-pipe treatment systems to in-plant
methods.
The recommendations in Table I were made for the treatment of
effluents and solid wastes from a cluster of tanneries comprising numerous very
small ("cottage"), some small and a few medium-sized tanneries in the vicinity
of Bogota, Columbia.
All effluents containing chromium should be collected
separately and the chromium recovered for reuse in the process after adding
fresh chromium salt.
Chromium recycling
Larger tanneries can afford to buy a recycling unit of their own. The minimum size is normally for between 500 and 1000 cattle hides per day. A prefabricated unit from a western country costs at least US$ 60,000 - 100,000. However, a plant can be produced in practically any country using locally available materials.
Table 1: Principles of Treatment of Tannery Effluents
|
Effluent type |
Treatment / Recycling |
Effects |
|
Used Cr tanning bath |
Collection and recovery in recycling plant; larger tanneries
recycle Cr in-plant. |
Quantitative removal from month. effluents; saving US$ 1,000
per |
|
Used unhairing bath containing sulphide |
In-plant collection and oxidation or: or: combined solution, reuse
of bath and final recovery |
Quantitative removal of sulphide from effluents. |
|
All others |
Medium-sized tanneries: neutralization and
presedimentation(in-plant); discharge into sewerage system |
Reduction of biochemical oxygen demand (BOD), chemical
oxygen |
|
Smaller tanneries: |
Demand (COD) | |
|
Discharge into sewerage system after screening of
effluents. |
Total dissolved and suspended solids, etc. | |
|
Effluent treatment plant for tannery and domestic effluents with
precipitation/flocculation and biological treatment in ponds. |
90 - 95 % reduction of BOD COD, solids, tannin and
colour. |
Chromium recycling is practiced with great success, whether in
shared or decentralized plants: for example in Italy, where a large shared
chromium recycling plant has been In operation for many years producing more
than 21 tons of chromium a day, recovered from the collected spent floats of
more than 150 tannieres in the area. The same system has recently been put into
operation in Portugal. Large and medium-sized tanneries known to the author in
India, China, Colombia and Brazil are also using this system successfully.
In
Germany, a large and well known producer of top quality leather has been running
a chromium recycling plant since 1923
