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WRITING DIVISION
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THE USE OF CHLORINATED SOLVENTS AS WASHING AGENTS IN THE METAL
AND STEEL INDUSTRIES, AND PARTICULARLY IN THE PRODUCTION OF BRASS
POINTS FOR WRITING INSTRUMENTS, WITH ASSOCIATED PROBLEMS
First Section
Introduction
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This document is intended to analyse the various problems
related to the use of solvents known as chlorine derivatives and
to sensitise users to their correct use with the aim of
preventing corrosion in the final products.
This section will focus on the characteristics of chlorinated
solvents normally used to degrease metals and on the problems
that might accidentally follow the inappropriate use of the
product.
The second section will concentrate on possible problems
arising from the use of uncontrolled solvents.
A thorough analysis of the issue was made necessary by various
defective cases registered all over the world in the last two
years. Refills manufactured and sold were then rejected by final
customers because they just stopped writing. Cases of that kind
had never occurred before, nor was the origin of the defect
known.
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Chlorinated solvents and problems related to their use
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Chlorinated solvents were introduced in the cleaning and
degreasing of metals at the beginning of the Sixties: they are
the most important class of substances belonging to the family of
halogen derivatives. They replaced conventional oil products
(special petrol and white spirit) with the disadvantage of being
inflammable whilst chlorinated solvents are not.
They are polar substances endowed with a remarkable solvent
power.
Chlorinated hydrocarbons usually possess a high solvent power
with greases, rubber, chlorine, etc.
They are insoluble in water but can be mixed with other
solvents; their sweetish smell is stronger than that of
unchlorinated solvents.
It can be stated that chlorohydrocarbons are currently the
main means through which chlorine is fixed and reaches the
chemical market.
Chlorinated hydrocarbons can e subdivided into three main
groups:
- Paraffin derivatives
- Derivatives of unsaturated hydrocarbons
- Derivatives of aromatic hydrocarbons
Chlorinated solvents are technically divided into:
- Chloroethanes
- Chloroethylenes
- Chloromethanes
We will confine our analysis to compounds used in the metal
and steel industry as degreasing agents for metals.
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Chloroethanes
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There are nine chlorinated solvents deriving from ethane;
their constitution varies according to the number of chlorine
atoms present in replacement compounds.
1,1,1-Trichloroethane
Thanks to its low toxicity this solvent has taken up a
remarkable importance in the cleaning of metal parts. It is
hydrolysed by hot water under pressure; the type of acid
generated depends on the amount of water reacting with the
solvent; more specifically the hydrochloric acid which is
produced caused a significant corrosion.
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Chloroethylenes
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More commonly known as Chlorothenes, these are six chlorinated
products derived from ethylene by replacement of one or more
hydrogen atoms with chlorine atoms. The most widely used types
are:
Perchloroethylene
It is conventionally used for the degreasing of metals. It is
not stabilised and exposed to water and light it can undergo a
slow oxidation process with consequent release of toxic and
corrosive substances.
Trichloroethylene
It is commonly used in metal degreasing. In the absence of
inhibitors or stabilisers, Trichloroethylene slowly oxidises in
contact with air and generates hydrochloric acid, thus becoming
corrosive with all metal surfaces. Impurities contained in this
chlorinated solvent are not allowed to exceed 10 parts per
million acidity, 10 parts per million insoluble residue, and what
is very important, 100 parts per million water.
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Chloromethanes
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They are four products obtained from the gradual replacement
of methane hydrogen atoms with chlorine atoms. The most
well-known is Methylene Chloride.
Methylene Chloride
Methane chlorinating has a specific importance and interest
because it is the only technology allowing for the production of
all the series terms. Because of its high volatility, it is not
normally used in metal degreasing.
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Table 1
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Flash Point |
Molecular Weight |
Boiling Range (°C) |
density (20°) |
| Methylene Chloride |
Not Inflammable |
84,94 |
Between 39,5 and 40,3 |
1,330 |
| Perchloroethylene |
Not Inflammable |
165,85 |
Between 120 and 122 |
1,623 |
| Trichloroethylene |
Not Inflammable |
131,40 |
Between 86 and 87,5 |
1,464 |
| 1,1,1-Trichloroethane |
Not Inflammable |
133,42 |
Between 73 and 75 |
1,320 |
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The following factors should be taken into consideration when
choosing the most appropriate cleaning method:
- Cold processes, though being direct and not requiring
special equipment or technologies, lead to a high loss of solvent
during the mechanical action accompanying the process and carry
the risk of polluting the surface,
- Processes based on heat, besides allowing for solvent re
condensation and therefore reuse, have a greater cleaning
efficacy.
During solvent re condensation however, there is the danger of
a greater concentration of water. The most widespread degreasing
methods in industry are as follows:
- Hot degreasing with solvent vapours
- Cold degreasing by shaking, immersion, sprinkling
- Ultrasound degreasing
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Ultrasound degreasing
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This is the method affecting the sector of writing instruments
directly and therefore the method we will be dealing with in this
document.
It is well-known that the motion of the cleaning solution or
of the object to be cleaned improves and accelerates the cleaning
process. Ultrasounds are a practical application of this theory.
Ultrasound energy is by definition a high frequency mechanical
vibration: a 50 hertz alternating current is sent to a generator
developing a frequency of 20.000 cycles a second, or even higher.
Transducers turn electric power into sonic energy and then
into sound waves; the latter are further transmitted to a fluid,
thereby generating cavitations.
The cavitation mechanical action coupled with the solvent
chemical action produce an effective degreasing process.
Ultrasounds start to remove fuel oil deposits and solids
adhering to metal surfaces that are usually insoluble in
conventional solvents.
Ultrasound cleaning is particularly useful for the removal of
impurities in areas difficult to access.
In order to ensure an optimal ultrasound degreasing, operating
temperatures should be 10-20°C lower than the solvent boiling
temperature.
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Main features of solvents used for metal degreasing
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The main features of these solvents are:
a) Non inflammability: it is one of the main reasons why they
are industrially used to degrease metals.
b) High solvent power: they can solve all kinds of greases,
oils, waxes and resins used in the metal and steel industry
during the production process.
Along with positive features we should like to mention some
negative ones, and namely:
a) They are reactive to metals: chlorinated solvents, if not
appropriately stabilised, may cause corrosion, stains and
oxidation in metal parts.
b) They are unstable in the absence of inhibitors.
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Precautions in the use of chlorinated solvents: Water contamination
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Water contamination is the most common cause of corrosion.
When a mixture of any chlorinated solvent and water comes into
contact with metal parts, corrosion may occur.
Corrosion occurring inside the degreaser may also stem from
thermal decomposition and the consequent formation of acid. This
situation may be caused by a solvent overheating locally because
of an excessively high temperature of the irradiating surfaces;
it may also stem from high boiling point caused by too much oil.
The formation of acid (induced by hydrolysis of the solvent
used) may also be the result of inadequate cleaning and
maintenance of the equipment.
The careful removal of water that happens to be in the solvent
is of the utmost importance to avoid the following
inconveniences:
- Condensation of air moisture in the heating coils used for
solvent re condensation.
- Presence of aqueous emulsions of blending oils on the parts
to be treated.
- Presence of water on machined parts.
To avoid all this, each machine used for washing should be
equipped with a very effective water separator.
Moreover, the amount of water present in solvents should be
kept under 200 PPM; when this amount increases and reaches 450
PPM (which corresponds to 450 grams of water every 1000 litres of
solvent !) the solvent must no longer be used but immediately
distilled or passed through a water separator.
To confirm this, suffices to mention that the aqueous extract
of a solution of 10 cc of stabilised but old
1,1,1-Trichloroethane with 90 cc of water at ambient temperature
moves from pH 7 to pH 4 in 24 hours; with the increase in
temperature, the pH goes down to 3.
If the same solution is exposed to sunlight for 48 hours, it
reaches a very high acidity (pH 2,8).
It should be considered that water together with solvent may
form an azeotropic mixture, that is a mixture of two or more
liquids with a constant boiling point, that does not change
composition, not even after a distillation.
A binary mixture may be characterised by a boiling point lower
than that of the most volatile component and higher than the
least volatile one.
It is because of the danger on introducing water into the tank
that the machine must have a water separator with a capacity
proportional to its working capacity.
Furthermore, to make separation easier, operating temperature
should be decreased so as to reduce solvent solubility in water.
Table n.2 shows a number of parameters related to
water-solvent azeotropic mixtures.
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Table 2
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Azeotropic water-solvent mixture boiling point (°C) |
Azeotropic mixture weight percentages |
Corresponding to (ppm) |
| Methylene Chloride |
38,1 |
1,5 water 98,5 solvent |
15.000 |
| Trichloroethylene |
73,3 |
5,4 water 94,6 solvent |
54.000 |
| Perchloroethylene |
87,8 |
15,8 water 84,2 solvent |
158.000 |
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No chlorinated solvent should be used when there is even the
slightest likelihood that vapours in a given pp concentration
might come into contact with live flame, when surfaces are too
hot, or when a distillation with too much oil or too little
solvent has been carried out. This may lead to decomposition with
the subsequent formation of hydrochloric acid, chlorine, carbon
dioxide, carbon oxide and phosgene.
Luckily, the irritating action of hydrochloric acid clearly
indicates the beginning of this decomposition, long before
phosgene concentration reaches dangerous levels.
It should also be kept in mind that besides causing
toxicological problems, decomposition by-products corrode the
metal parts they come into contact with. Table n.3 shows that the
starting temperature of thermal decomposition is higher for
Trichloroethane than for the other chlorinated solvents
conventionally used in metal degreasing. Moreover,
Trichloroethane produces by far fewer decomposition toxic
substances.
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Table 3
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Thermic decomposition starting temperature (°C) |
| 1,1,1-Trichloroethane |
163 |
| Trichloroethylene |
120 |
| Perchloroethylene |
140 |
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The choice of too volatile solvents like Methylene chloride
should be avoided for two main reasons:
1) In certain atmospheric situations, steam contained in the
air may condense on the metal surfaces cooled by the quick
solvent evaporation and consequently increase water
concentration;
2) An excessive solvent evaporation leads to a sudden increase
in the water-solvent ratio.
In both cases an azeotropic mixture may be the result.
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Storage
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Solvent drums must not be kept for long in humid places to
avoid a possible corrosion of containers and the subsequent
solvent contamination.
As far as the storage in tanks is concerned, excellent results
are obtained with stainless steel tanks with lined internal
walls, so as to avoid any possible corrosion due to moisture.
Before using a container to store chlorinated solvents, one
must make sure it is clean, dry and free from rust or metal
chips, or from any oil traces that might trigger deterioration
processes.
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Distillation
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Here are important instructions to be followed in the
distillation of chlorinated solvents:
a) Separate the water layer that might possibly cover the
solvent before carrying out distillation.
b) Remove possible chips and powders from the solvent before
distillation.
c) Collect the contaminated solvent into clean stainless steel
or plastic containers, since the presence of rust may catalyse
the impoverishment of stabilising agents.
d) Use a system of stabilisers with a boiling point as close
as possible to the solvent boiling point so that both go together
during distillation.
Inhibitors present in chlorinated solvents play an essential
role in reducing the risk of metal oxidation.
An incomplete distillation or insufficient equipment cleaning
frequency may lead to an excessive loss of inhibitors during
solvents utilisation or distillation.
A regular re-stabilisation of chlorinated solvents is very
important to avoid corrosion and oxidation.
For this reason every user must carry out a check at regular
intervals to assess the amount of stabiliser necessary to protect
chlorinated solvents from acidification.
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Regenerated solvents
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The purchase of regenerated chlorinated solvents in the market
may help you save money but may also cause inconveniences to the
user if he is not informed well enough. Indeed it should be
remembered that even a chlorinated solvent only partially
degraded after distillation may become acid and therefore
corrosive, with serious damage both to the equipment and, more
frequently, to metal parts.
The best way to avert these risks is refraining from buying
regenerated solvents from unknown sources or reckless suppliers.
Even a "home made" regenerating must be carried out
with high-quality solvents; it is a simple operation, but it
requires some attention and skills.
Remember that washing baths should never contain brass chips
or powder (if present they must be promptly removed) since they
catalyse the decomposition process.
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Checks
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Regular checks are recommended by all solvent manufacturers to
maintain the cleaning system in optimal conditions and to ensure
effective degreasing operations.
Some of these checks are very simple and do not require
special equipment or chemical know-how; they can be carried out
by the operators themselves.
Here are the most well-known control methods:
- Acid acceptability test
- Scratch test
- Aqueous extract pH test
The scratch test is generally used to assess the stability of
solvent with aluminium and therefore it does not fall into our
scope of analysis; the acid acceptability test is normally used
to assess the amount of stabiliser present necessary to protect
the solvent from acidification.
The simplest method known is the aqueous extract pH test; the
necessary material can easily be found.
To carry out this test put 50 ml of chlorinated solvent in a
clean container previously rinsed in distilled water, add the
same volume of distilled water previously brought to pH 7 with a
normal-hundred HCl solution, and shake for about two minutes.
Leave to separate and finally dip electrodes of the pH-meter
into the water and measure.
The pH should be as close as possible to 7. Lower values
indicate that the acidification process has already started and
that the solvent must therefore be regenerated.
All manufacturers can rely on laboratories with qualified
experts at the customers' disposal for technical tests or
consultancies; users may even be supplied a "test kit"
for a quick and easy assessment of solvent stability.
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Toxicity
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Every person responsible for the operation and maintenance of
degreasing equipment based on the use of solvents should be
well-trained to its correct use.
Every user should precisely know all the risks related to the
use of chlorinated solvents; it is only this way that, with some
precautions, they can be used safely.
Trichloroethylene and Perchloroethylene are marked by a
similar photochemical reactivity, but Trichloroethylene develops
a significant amount of photo-oxidation derivatives which may
lead to the release of a photo-chemical "smog".
Among these products, the most important one are: chlorine,
hydrochloric acid and phosgene.
The most dangerous one is phosgene; besides being highly
toxic, it has no property based on which it can be identified and
has delayed toxic effects.
Not in all chlorinated solvents the decomposition process
releases an amount of phosgene hazardous for health.
Trichloroethane for instance releases very limited amounts of
phosgene and only during arc-welding processes.
Users of chlorinated solvents are highly recommended to abide
by the following vital instructions:
- Use solvents with a limited toxicity.
- Use of appropriate and controlled equipment.
- Use of distillation plants.
- Development of preferential business relations with
solvent manufactures able to guarantee an excellent
technical service.
Table n.4 shows the toxicological properties of chlorinated
solvents most commonly used in metal degreasing.
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Table 4
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Smell |
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Effects |
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Perceptibility threshold (ppm) |
Weak (ppm) |
Irritating (ppm) |
None (ppm) (8 hours) |
Eyes Irritation (ppm) |
Respiratory Diseases (ppm) |
Coordination Lack (ppm) |
1,1,1- Trichloroethane |
100 |
350 |
1.000 |
500 |
1.000 |
2.000 |
1.000 (30-70 min.) 1.500 (15-60 min.) 2.000 (5 min.) |
| Trichloroethylene |
100 |
200 |
600 |
100 |
400 (weak) 1.000 (strong) |
1.000 |
400 (20 min.) 1.000 (6 min.) |
| Perchloroethylene |
50 |
150 |
400 |
100 |
400 |
600 |
200 (8 hours) 400 (2 hours) 600 (10 min.) |
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In November 1992 in Copenhagen, during the fourth Meeting of
the European Community, the application rules of the Montreal
protocol were modified. The protocol laid down the rules to be
followed in production control and use of Chlorofluorocarbons,
Hydrochlorofluorocarbons, Carbon Tetrachloride and
Trichloroethane.
Trichloroethane had already been included in the group of
products regulated by the 2° Review Meeting held in London in
June 1990.
Here are Trichloroethane control measures according to the
latest application rules:
Production freeze: January 1, 1992 at 1989 levels
50% reduction: January 1, 1994 at 1989 levels
Total elimination: January 1, 1996.
The only derogation still in force apply to Underdeveloped
Countries to meet the needs of their domestic markets.
It should be noted that the Montreal protocol provides for
general rules only, therefore some countries might decide to set
more restrictive rules to accelerate the reduction and
elimination of Trichloroethane.
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