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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
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.
Chlorinated solvents and problems related to their use
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:
  1. Paraffin derivatives
  2. Derivatives of unsaturated hydrocarbons
  3. 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.
Chloroethanes
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.
Chloroethylenes
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.
Chloromethanes
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.
Table 1
  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
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:
  1. Hot degreasing with solvent vapours
  2. Cold degreasing by shaking, immersion, sprinkling
  3. Ultrasound degreasing
Ultrasound degreasing
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.
Main features of solvents used for metal degreasing
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.

Precautions in the use of chlorinated solvents:
Water contamination
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.
Table 2
  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
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.
Table 3
  Thermic decomposition starting temperature (°C)
1,1,1-Trichloroethane 163
Trichloroethylene 120
Perchloroethylene 140
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.
Storage
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.
Distillation
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.
Regenerated solvents
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.
Checks
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:
  1. Acid acceptability test
  2. Scratch test
  3. 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.
Toxicity
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.

Table 4
   Smell     Effects      
  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.)
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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