This document develops in some detail the different stages in the manufacture of tinplate, from obtaining the base steel and its different varieties, to the successive sequences of tinplate tinning.
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INDEX
Introduction
1.- Manufacture of steelN
1.1.- Manufacture of the base steel
1.2.- Manufacturing sequence
1.3.- Base steel composition
1.4.- Types of base steel
2.- Tinning
2.1- Tin
2.2.-Electrolytic tin plating
3.- TFS
Tinplate is a material that although its invention comes from ancient times, it really reached its maximum development during the last century. It was the United States that was the driving force behind this industry, reaching its highest volume of activity in that country in the s. Then, the great deployment of beverage containers, which in North America used aluminum as raw material, the use of alternative containers and the obsolescence of the American steel industry, caused the decline of this market.
The same did not happen in other parts of the world. Europe was able to modernise its steel industry in time, maintaining its competitiveness, and was thus able to successfully resist the challenge of aluminium. However, a wide variety of packaging options put a bit of a dent in the industry, which responded successfully with a series of mergers, enabling it to maintain an excellent level of technology.
Also in other geographical areas such as South America, the Far East and Asia, the market for tinplate and other coated products maintained a good market position.
Today it is still an important sector worldwide, although in continuous competitive struggle. It is therefore worth knowing a little about how this material is manufactured.
Tinplate is normally by weight, 99% or more steel, and is therefore essentially a steel product. The manufacturing process actually starts in the blast furnace and tin smelter, but in practice it is considered to start from steelmaking. In fact, it is at this moment when the composition and type of steel ingot to be made is decided, defining its future use as a rolled product. Consequently, the basic raw materials for the manufacture of tinplate are steel and refined tin.
1.1.- Manufacture of the base steel.
There are two basic procedures for obtaining crude steel in liquid state: from (a) iron ore and b) scrap metal.
A.- From iron ore (smelting process): iron ore is a rock composed of iron oxides and various other minerals (gangue). The ores and scrap metals used in the smelting process are initially full of impurities. Iron is never in a pure state in nature; it is most often in the form of oxides and sulphides.
In the industrial process developed in the blast furnace, the aim is to obtain a product as rich as possible in iron, but other components will always appear in it. Among the parasitic materials, many have a lower combustion and evaporation temperature than iron, and will disappear by heating the ore, or have a lower density than iron, and will float on the melting metal. To free iron compounds in the form of ferrous (FeO), magnetic (Fe3O) and ferric (Fe2O3) oxides from oxygen, it is necessary to take advantage of the ease with which carbon reacts with oxygen.
Carbon in its combustion is a great devourer of oxygen, which will take it from the air, but also from the oxide to form the compounds CO and CO2 (carbon monoxide and carbon dioxide). In this operation, the excess carbon will leave traces of carbon combined with iron (3 to 6 %). This material produced in the blast furnace is called “melt”.
To get rid of the carbon, a complementary operation can be done by adding oxygen to form CO and CO2, carbon dioxide gases. This oxygen can also react with other elements contained in the melt, such as manganese forming manganese oxide (MnO), silica (SiO2), alumina (Al2O3)… All these operations are carried out first in the blast furnace and then, as we will see later, in the refining operation.
Summing up, we could say that in a blast furnace, after a stage of ore preparation in the agglomeration workshop, the iron is extracted in the blast furnace, with the help of a fuel: carbon (coke). Pure iron is not yet obtained, but iron smelting, a liquid mixture of iron (96%) plus carbon (3%) from the rest of the coke that has not been burnt, plus some residues (phosphorus, sulphur…) from the gangue. Figure 1 shows a vertical section of a blast furnace.
Figure 1: Schematic diagram of a blast furnace
B.- From scrap (“electrical process”): The components with which the furnace is fed can be from raw materials (e.g. machinery parts) duly selected, to scrap prepared, selected, crushed, calibrated, with a minimum iron content of 92%. The whole assembly is melted in an electric furnace.
Pig iron or iron from the blast furnace, or from scrap melted in an electric furnace, is an iron-carbon alloy, brittle and with a high content of the latter element. There may also be high sulphur and phosphorus content. Steelmaking is the process of refining, to reduce and control the percentages of elements other than iron, in order to produce ingots of the required purity, characteristics and malleability. In general terms, these elements and impurities are reduced by oxidation with iron oxide or oxygen, and removed by flotation with the addition of high melting point materials (e.g. limestone).
At present, four basic processes are used to obtain steel: the Siemens-Martin or open crucible process, the Bessemer or Thomas process, the top-blown oxygen process and the electric furnace. The latter is rarely used for the manufacture of tinplate. The first and the second are perhaps the most extensively used pneumatic procedures.
Open crucible” process – The crucible is usually charged with molten iron from the blast furnace, scrap and cold pig iron. The impurities are oxidized causing the formation of an oxidizing slag, and the fuel used can be liquid or gaseous. The capacity of a furnace of this type can be up to 400 tons and through the use of bulk oxygen, of relative economy, can have high performance, reaching up to 50 tons/hour. These ovens can be fixed or tilting.
Bessemer or Thomas process – In this system, the impurities are reduced by direct injection of air or oxygen through the molten metal by means of nozzles placed at the bottom of the converter. See figure nº 2:
Figure no. 2: Steel processing in the Thomas Converter
To burn the carbon from the melt, air or a mixture of air and oxygen is blown through the molten metal poured into the converter, which is a large steel retort with a capacity of 25 to 50 tons. The refractory walls of the converter are made of basic dolomite, untreatable to the lime that must be introduced to remove phosphorus from the melt. Productivity and quality can be improved by controlling the composition of the injected oxidizing gas, air, oxygen enriched air, oxygen, oxygen/carbon dioxide mixture, etc. For example, the VLN variant (very low nitrogen) not only increases production but also reduces the normally undesirable incorporation of nitrogen into the steel.
During the process several phases or periods can be distinguished. In the first period a lot of sparks are produced, caused by the combustion of the silicon which lasts from 2 to 3 minutes. In the second one, flames are generated by the combustion of carbon, with a persistence of 10 to 12 minutes. In the third is characterized by the expulsion of gases caused by the subsequent blowing and combustion of the phosphorus, its interval is 3 to 5 minutes.
Throughout the process, different solid elements are usually added, such as: lime, scrap, ferro-manganese or specular pig iron, depending on the needs.
There is a system called Duplex, which applied to the manufacture of tinplate steel, means the combination of the Bessemer acid process with the basic open crucible process. In the converter the main purification takes place, while in the second part of the process the phosphorus reduction takes place.
Superior oxygen injection process. The Bessemer process is widely used mainly because of its low installation cost and flexibility of operation, but it has great limitations in terms of final quality, as it requires a raw material with high phosphorus content and restrictions on the use of scrap. These difficulties strongly affected some manufacturers, which led to the development of superior oxygen injection processes, which allow to obtain steels of good and constant quality, with low nitrogen and high or low phosphorus content, according to needs. There are three systems widely used for laminated materials and they are called LD, DDAC and KALDO.
The LD process was the first one based on the availability of oxygen in large quantities. It consists of replacing the injection of air from the bottom of a Bessemer converter by the injection of a jet of oxygen at high pressure from the top, which produces a strong agitation, and therefore a very rapid oxidation of impurities. It is a fast and efficient process, with initial investments not much higher than with the Bessemer process, it reduces maintenance problems and produces a material with low nitrogen content, being one of its limitations the use of low or medium phosphorus content irons. This system was developed by two companies located in Linz and Donawitz. From the initials of these cities comes the name of the LD process.
DDAC is exactly the same process as above, except that lime is injected along with the oxygen. It is a technology of French origin
The KALDO process was first developed in Sweden and uses a rotating and tilting crucible or kiln, with the application of an oxygen jet at the top and the addition of lime by injection or in chunks.
Oxygen processes are versatile and allow the use of reasonable amounts of ore and scrap, producing low phosphorus and low nitrogen steel with good mechanical characteristics.
Casting of the steel – Once the steel has been obtained by one of the procedures described above, while it is still in the converter and in a liquid state, it must be transformed into a solid state by casting it. Industrially there are two casting processes. The most classic in which it can be converted into ingots (“ingot casting”) or follow the “continuous casting” procedure.
Ingot mould casting – This is the conventional procedure. By means of a ladle the molten steel is poured into ingot moulds, which once cooled give rise to manageable ingots with which the following operations are fed.
Continuous casting – This is the most modern process for the manufacture of plates. It has the main advantages of producing very high quality semi-finished products, it allows lower production costs, and increases the productivity of the steel mill. In fact, thanks to this system, the operations are fewer and simpler than in ingot mould casting. . It is banishing the use of ingots for steels intended for rolling. See figure nº 3:
Figure no. 3: Continuous casting
In continuous casting, the contents of the converter are poured by means of a ladle in a regular and uninterrupted manner into a cooled bottomless ingot mould with a cross-section that corresponds to that of the desired plate. It then passes through a series of rollers for flattening, and finally by means of an oxy-fuel torch the sheets are cut to the desired length. In this way we obtain slabs (slab) of length between 5 to 20 meters, width up to a little more than one meter and thickness of about 20 cms.
1.2.- Manufacturing sequence.
Figure nº 4 presents a sequence of the different operations or phases in the production of the steel plates that will be the basic raw material in the tinplate manufacturing plants.
Figure no. 4: Fabrication of steel plates
When the ingot casting process has been used, once the steel has been melted into ingots, the first operation carried out is the rolling of the ingot to turn it into a slab. This operation is usually carried out in reversible, double-high rolling mills. The so-called Universal type, have cylinders or side rollers that work simultaneously the 4 faces of the ingot, eliminating the operation of rotating the ingot on its axis during this stage.
The final product of this operation, the slab, is 125 to 230 mm thick, the approximate width of the tinplate that is finally desired, and a length that depends on the size of the original ingot.
The slabs generated both by continuous casting and by ingot rolling are prepared for treatment in hot rolling.
Hot rolling is the next step, although there is usually an intermediate stage, which consists of cooling and storing the plates, a selection process, a surface preparation (scarfing) and a heating of the plate to a suitable temperature for rolling. Eliminating this intermediate stage requires a very precise programming, and a very high technological capacity, which ensures the absence of defects in the plates or slabs. Figure nº 5 shows the different phases of hot rolling.
Figure no. 5: Hot rolling process
The surface preparation is carried out in the “descaling machine”, in which the plate is subjected to a detachment of iron oxides and impurities, which is achieved by means of a weak rolling pressure, detaching them by the action of water at high pressure. The plate is heated to a temperature of 880º C. It is necessary to remove this layer of oxides because it damages the laminate, as it causes rapid wear of the cylinders, streaks on the metal, oxide incrustations and other manufacturing defects (breaks, slipping, folds…).
The hot rolling mill reduces the sheet to a continuous strip of about 2 mm thickness. It normally consists of two sections, a roughing section and a finishing section. It can be of a continuous or reversible type, depending on the capacity of the installation, etc.
The roughing mill usually consists of 4 to 6 boxes that reduce the initial thickness of the plate by 25 to 50% per box. The finishing train has 4 to 7 boxes, again reducing the thickness by 25 to 30 % per box, except for the last one which only reduces by 10 %. The maximum speed of this operation can be in the 100km/h. At the exit the material is at 850º C. It proceeds to a cooling by water curtain up to 590º, forming coils with the same.
The coil produced must be pickled and lubricated before cold rolling. This operation is usually carried out in a succession of tanks containing hot dilute sulphuric acid (close to 100º C), washed, dried and lubricated with palm oil or other lubricant suitable for cold rolling. The pickling line is normally fitted with a circular cutter, which cuts the edges, thus ensuring that they are suitable for cold reduction or cold rolling, also setting the maximum width of tinplate to be obtained and also the one that will give the best economic results. See figure nº 6.
Figure No. 6: Cold rolling, annealing and skin-pass rolling of base steel
The next operation is cold rolling, which can be done in continuous (tandems) or reversible mills. Lubricants and coolants are used during this operation, and the resulting thickness is very close to the desired finish. The reduction is therefore of 1.8 or 2 mms to a measure between 0.15 to 0.3 mm approximately according to the final size of the tinplate to be produced.
The coil obtained is made of a very hard material and subject to strong tensions, and needs a suitable treatment to give it the necessary machinability, causing a recrystallization of the steel. This treatment is called annealing and involves heating the metal in a reducing atmosphere to avoid any oxidation (mixture of nitrogen and hydrogen) and can be done continuously (continuous annealing) or in batch annealing furnaces (batch annealing).
Continuous annealing: The strip circulates through a furnace at a temperature of 630º C, with each point of the material remaining in the furnace for a minimum of 1.5 minutes. Continuous annealing has a number of advantages and disadvantages such as:
Advantages:
– Reduction of materials “in process” of production.
– Reduction of manufacturing lead times.
– Improvement of the quality of the manufactured products:
o Constant and continuous heating along the entire length of the coil, which results in more homogeneous mechanical properties.
o Fast cycle, obtaining fine equiaxial grains, therefore an isotropic metal and superior mechanical properties, such as improvement of the elastic limit.
o Better corrosion resistance. The fast cycle does not allow elements such as carbon, manganese, phosphorus… to move to the surface of the material as happens in the base or bell annealing.
o Allows the use of a MR type steel composition, less loaded with hardening elements: carbon, manganese-…. (continuous annealing = 0.08 % carbon, base annealing = 0.10/0.13 % carbon) which favours operations such as welding, specialties…
Disadvantages:
– Manufacturing:
o Difficult programming of the orders, since the maximum variation in width between consecutive coils is of the order of 50 mm, and in thickness of the order of 10 %.
o Delicate conduction of the line. Risk of belt breakage in the oven. It is an important stop. The elastic limit of the strip at the annealing furnace temperature is low (approx. 30 N/mm2).
o Impossibility of line stops.
– Use:
o Fine crystallography that generates a less ductile metal, with weak anisotropy, which impairs drawing.
o Risk of presence of Lüder lines.
Annealing in a bell: Several stacked coils are covered with a bell in a reducing atmosphere at a temperature of 680º C for at least 85 hours, divided into 32 hours of heating, 34 hours of cooling under a bell up to 170º, and 19 hours of accelerated cooling in the open air. See figure nº 7
Figure nº 7: Diagram of the bell annealing process.
In both cases it is essential to previously eliminate the residues of the lubricating and cooling agents previously used, being the method used for this, consistent with the type of annealing to be done, normally by electrochemical means, such as a bath of degreasing agent heated to 95 ºC or mechanical, with brushing on both sides.
Next comes the tempering operation, surface treatment or finishing (temper rolling or skin-pass). It is made by means of a reduction or lamination, without lubricant and very light, which usually does not exceed 2% in thickness. For this purpose, a rolling mill consisting of two boxes is used. The strip, when passing between the cylinders under the effect of the established pressure and traction, undergoes a superficial modification of the structure, achieving an increase in the hardness of the surface layer, but preserving the internal softness.
In short, this operation gives the strip the desired hardness, a good flattening and a surface finish of the material depending on the roughness of the rolls used in the rolling mill boxes. Combining the surface finish of the cylinders of the boxes of this lamination, and the final remelting of the tin after the tinning operation, different surface finishes of the tinplate are achieved. The main types of finishes are:
Glossy finish: To achieve this finish, it is essential to obtain a mirror polish on the cylinders. In addition, it is necessary to apply the tin plating refusion. This type of finish is, together with the stone, the most requested.
Stone finish: The cylinders undergo two grinding passes with a special grain grinding wheel, which gives the product a striated appearance. As in the previous case, the tin coating is remelted, which also ensures brilliance.
Matte finish: It has a low reflective surface. To achieve this, the cylinders are shot-blasted and the remelting operation after tinning is omitted.
In the case of double reduced tinplate, the last size reduction is made by replacing the tempering operation with a further size reduction or rolling of approximately 33%, with the consequent lengthening of the material by a similar percentage, this time using surface lubricants. This gives the tinplate high mechanical properties with a small thickness.
It is common practice to prepare the coils prior to the tinning operation. It consists mainly in cutting the edges and eliminating the sections of low quality or out-of-spec calibre, forming coils of optimum size for the tinning line.
In electrolytic tin plating, the prepared material passes continuously through the operations of electrolytic cleaning, electrolytic pickling, electro-deposition of tin, tin remelting (flow-melting), passivation treatment and lubrication. After this series of operations, the product can be cut into sheets to the ordered size (length, as the width was given when preparing the coils), inspected, sorted and packed; or it can be wound for shipment to the customer or for slitting, etc. on a separate slitting line. It is normal to carry out on the same line, the selection of the material, before packing. We will return to these points in more detail later.
1.3.- Composition of the base steel.
For tinplate, the base steel is essentially a mild steel of low carbon content, with a generic composition of the following type:
– Carbon 0.04 – 0.15 %.
– Silicon 0.08 % maximum
– Sulfur 0.015 – 0.05 %.
– Phosphorus 0.01 – 0.14 %.
– Copper 0.02 – 0.20 %.
– Manganese 0.20 – 0.70 %.
– Nitrogen 0.001 – 0.025 %.
Due to the use of scrap in steelmaking, other elements such as nickel, chromium and tin may be present, but no other elements are intentionally added. The only exceptions are phosphorus and nitrogen, which can provide special properties. The use of copper to increase corrosion resistance, and of some carbides to control ageing has fallen into disuse.
The influence of some elements on the base steel of tinplate is given in outline in the following paragraphs.
– Carbon: Carbon increases yield strength, tensile strength and hardness, decreases elongation and ductility. Within the usual limits for tinplate, variations in the content of this element are of little importance, as other elements have a much greater influence.
– Silicon: It exists in tinplate as a residual element, very rarely is it added as a deoxidising agent. Slightly hardens and in some cases adversely affects corrosion resistance.
– Sulphur: In this type of steel, the effects of sulphur are counteracted by manganese, which is always present. However, due to its consequences on ductility, surface quality and corrosion resistance, every effort is made, within economic limits, to reduce it to the minimum possible.
– Phosphorus: It is an element that highly influences hardness and corrosion resistance. When there is a possibility of acid corrosion, it must be kept within certain limits, and the content is increased when greater steel strength is required and there is no danger of corrosion.
– Copper: Although it increases resistance, it does not do so effectively within the usual limits. Exceeding these limits increases atmospheric corrosion resistance, but may reduce internal corrosion resistance, so for most types of tinplate, a maximum copper content is specified.
– Manganese; It is used in the manufacture of steel for tinplate, mainly to react with other elements, mainly sulfur, rendering them inoperative.
– Nitrogen: In Bessemer steels, it is a normal constituent element in percentages higher than 0.01% and has always been considered a disadvantage. Subsequently it has been found that its intentional addition greatly increases the strength of the steel without appreciably modifying the corrosion resistance, although it may affect ageing. The development of oxygen processes (LD, etc.) has made it possible to accurately control the content of this element, giving a uniform and continuous quality.
– Nickel: At permitted levels, it does not affect the physical or mechanical properties of tinplate, but it does affect the chemical properties, especially corrosion in certain types of packaging. The same is true for chromium.
– Tin: This element has a high solubility in iron or steel, and percentages higher than 10% are necessary for a second phase to form. At normal levels it has no effect on the metallographic structure. Its presence progressively increases the elastic limit and the tensile breaking limit, with a reduction in the modulus of elasticity. It is important to note that small amounts of tin, in steels containing copper, can cause serious difficulties in hot working the steel.
In steelmaking, practical rules are sometimes used to calculate the effects of alloying and residual elements on the mechanical properties of tinplate steel. One of the most common is the Strohmayer index, which is calculated by multiplying the nitrogen content by 5, adding the phosphorus and multiplying the sum by .
1.4.- Types of base steel
Traditionally there are three basic types of tinplate steel, although with today’s technologies it is sometimes difficult to stay within the classic types. These are:
Type L: It is a cold rolled steel, coming from open crucible furnaces (Siemmens Martin). It has a low content in metalloids and residual elements, especially limited in phosphorus, with the following composition:
Carbon 0.05 – 0.13 %.
Manganese 0.30 – 0.60 %.
Sulphur 0.04 max.
Phosphorus 0.015 max.
Silicon 0.010 max.
Copper 0.06 max.
Nickel 0.04 max.
Chromium 0.06 max.
Molybdenum 0.05 max.
Arsenic 0.02 max.
Nitrogen 0.02 max.
It is used when a high resistance to very corrosive products is required.
Type MR: It is the most used. It is of the same origin as the previous one, cold rolled and used in moderately corrosive products. Your analysis is:
Carbon 0.05 – 0.15 %.
Manganese 0.30 – 0.60 %.
Sulphur 0.04 max.
Phosphorus 0.020max.
Silicon 0.010 max.
Copper 0.20 max.
Type MC: It is a steel made in Bessemer converter or Siemmens Martin furnace, used when the resistance and the content of the container is of low corrosiveness. Your sample analysis is as follows:
Carbon 0.05 – 0.15 %.
Manganese 0.25 – 0.60%.
Sulphur 0.04 max.
Phosphorus 0.03 – 0.15 %.
Silicon 0.010 max.
Copper 0.20 max.
There are also some special steels such as type D, aluminium quenched and tempered, used in specific cases of deep drawing.
Generally manufacturers in Europe have been forced to try to eliminate specialised tinplate productions and thus find economical and competitive procedures, so they try to simplify the problem.
Also important from the point of view of corrosion resistance is the surface of the steel, which depends in part on the type of atmosphere used during annealing. An atmosphere containing nitrogen, hydrogen, carbon dioxide and water vapour produces a less resistant tinplate than a dry nitrogen containing 4 to 8% hydrogen. Also dissolved tin ions have in general an inhibiting effect on the corrosion of tinplate by some products.
2.1.- Tin
When this material is intended for the manufacture of tinplate, it is logical to think that it will be in prolonged contact with foodstuffs and must therefore meet certain requirements in terms of impurities. The American Society for Testing and Materials (ASTM) classifies into five groups, each with minimum tin contents as follows: grade AA = 99.98 % tin, A = 99.80 %, B = 99.7 %, C-1 = 99.0 % and C-2 = 99.0 %. The minimum specified for the manufacture of tinplate is grade A. Its analysis is:
Tin (minimum) 99.80 %.
Antimony 0.04 %.
Arsenic 0.04 %.
Bismuth 0.015 % Bismuth 0.015 % Bismuth 0.015 % Bismuth 0.015
Copper 0.03 %.
Iron 0.015 % Iron 0.015 % Iron 0.015 % Iron 0.015 % Iron 0.015
Lead 0.05 %.
Nickel and Cobalt 0.015 %.
Silver 0.01 % Silver 0.01 % Silver 0.01 % Silver 0.01 % Silver 0.01 % Silver 0.01
Sulfur 0.003 % Sulfur 0.003 % Sulfur 0.003 % Sulfur 0.003
Zinc 0.001 % Zinc 0.001 % Zinc 0.001 % Zinc 0.001 % Zinc 0.001
Cadmium 0.001 %.
Aluminum 0.001 %.
The development of this tinning process was one of the most important steps in the tinning industry. The electro-deposition of tin on a continuous narrow strip (strip), started in Germany in , but it was during the 2nd World War when the technique was developed intensively, mainly in the USA, due to the shortage of tin.
There are a number of technical and economic reasons that made electrolytic tinplate take the market away from coke tinplate or hot tinplate, which was the traditional way of obtaining it. One of the most important is the precise control of the amount of tin deposited and the uniformity in thickness. Another is the availability of differential electrolytic tinplate, which consists of applying different thicknesses of tin coating on each side of the sheet.
As we have already indicated in the base steel tempering operation, electrolytic tinplate can be produced in various finishes, although three are the most common. “Bright”, which is the most common, “matt” which consists of tinning base steel with a rough surface and then not remelting the tin and finally “stone” which is the same finish as above but remelting the tin, which gives a shiny finish but not reflective.
The manufacturing methods are basically two, acid and alkaline or basic process, but the latter has two variants of wide use, horizontal halogen lines and alkaline or vertical lines. There is a fourth procedure, which uses fluoborates as electrolyte, but it is very little used.
The lines that use the acid process are the ones that produce the highest percentage of electrolytic tinplate. They are often called Ferrostan, as this was the name registered by U.S. Steel for its tinplate, with many subsequent licensees of its technology around the world.
Electrolytes are the most delicate part of every process. For example, in acid lines, it is a solution of stannous salts in acid, but the good performance as an electrolyte depends on the various additives used which have three main objectives, to avoid oxidation, to favour the formation of compact and non-fuzzy deposits, and to improve wettability.
Some classic advantages of using alkaline electrolyte are having a simpler, easier to handle and non-corrosive electrolyte in relation to steel, which reduces the initial cost of the equipment. The preparatory section is also simpler.
Acid lines have the advantage of using less current for tin plating than alkaline lines, less anode surface area is required and the electrical efficiency is higher in electrodeposition. However, alkaline lines produce a tinplate with better corrosion resistance characteristics.
Broadly speaking, the three types of lines are made up of the following sections:
Unwinding
Preparation
Tinning
Finishing
Cutting – winding – packaging
The entry or unwinding section has the necessary equipment for the handling of the black sheet coils, and for the continuous feeding of the line, by cutting the beginning and end of each coil and the electric welding of the end of one with the beginning of the next. Includes guide and feed rollers, tension rollers, etc.
Between the unwinding and preparation section, there is a device for storing black plate strip, intended to accumulate a certain amount of strip, which feeds the line while the coil is being changed and spliced in the previous unwinding section. There are several types, predominantly well and “accordion”.
The preparation section has two main objectives, cleaning (degreasing) and pickling. The first one is the removal of all residual elements on the belt surface, coming from lubricants, cooling agents, etc., while the second one aims to remove the iron oxide adhered to both sides of the belt.
The treatment is carried out in a succession of chemical or electro-chemical baths, with alternating water jet and/or steam washes. The layout and type depends on the line. For example, degreasing is normally done in a detergent or alkaline solution and in lines of this type it is eliminated or reduced because degreasing is done automatically in the tinning section.
The tinning section differs completely in each process, being that of the halogen process the one that occupies the largest surface, since the strip moves flat, normally in 3 levels, while in the other two systems it follows a sinusoidal or serpentine shape.
Figure no. 9: Tinning line, electrolytic tank and anodes
Before tinning, the marks corresponding to the differential tinplate are made on the black plate strip, when it is this type that is manufactured, therefore these marks go on the base steel. Some manufacturers may mark the base steel so that in the event of later difficulties with the tinplate, the manufacturer can be identified. These marks are not visible on the leaf as such, they must be found in the laboratory.
The finishing section includes different steps, the main ones being: remelting, passivation and lubrication.
The purpose of remelting is to give a shiny finish to the tinplate, as the simple electro-deposition of tin produces a micro-rough surface with a matt appearance. However, this step is of fundamental importance for tinplate intended to be in contact with corrosive elements. During remelting, a layer of iron-tin alloy is formed, and because of the rapidity with which it is produced, the thickness is very thin. It follows that dull tinplate, which has not undergone remelting, should not be used for those purposes which require the presence of a layer of iron-tin alloy.
Passivation is a characteristic of electrolytic tinplate. In this case, especially in low coatings, it is convenient to provide it with a protective layer that avoids oxidation, not only during manufacturing, but also in subsequent operations, such as varnishing. It is also necessary to give a surface chemically more suitable for lithography and varnishing, and of a certain protective hardness. Passivation is intended to cover this aspect, and basically consists of forming a chromic oxide layer. The methods used are various chemical or electro-chemical methods, each designed to obtain special characteristics. They are usually known by the acronym USS and a three digit number, the first digit indicates the type of solution (1 = chromic acid, 2 = chromium phosphate, 3 = sodium dichromate, 4 = sodium carbonate), the second digit indicates the polarity of the tinplate in the solution (0 = non-electrolytic, 1 = cathodic, 2 = cathodic/anodic) and the third digit refers approximately to the level of current used.
There are three basic types of passivation, which are:
– Passivation 300: It is obtained by chemical procedure, by immersion in sodium dichromate solution, generating a layer of chromium oxide. It gives good results from the point of view of varnish adhesion. It offers weak protection against sulphuration. This passivation is however unstable. Its effectiveness decreases over time
– Passivation 311Electroplating: Obtained by electrochemical process by electrolytic deposition in a bath of sodium dichromate of a layer of chromium and chromium oxide. It is the most commonly used passivation. It has convenient yields from the point of view of varnish adhesion, although lower than the 300 passivation. It is much more stable over time than the 300. It can therefore be considered a compromise between the stability over time and the quality of adhesion of lithographic systems.
– Passivation 312: It is obtained by the same system as 311. It is in fact a reinforced 311 passivation. It is mainly used for tinplates that must resist sulphur products, such as meats, soups, products for dogs and cats… Its adhesion to inks and varnishes is inferior to 311.
The different passivation treatments not only affect the adherence of varnishes, welding, etc., but also produce various forms of attack or staining, as the tinplate is subjected to contact with corrosive products or sulphur compounds. Even from an aesthetic or presentation point of view, this detail is important, for example with condensed milk.
Finally, the finishing section performs the lubrication operation. The purpose of this lubricant is not so much to protect the tinplate itself, but the passivation and not to counteract the properties of this is very light, so the most commonly used method of application is by electro-deposition, although it can be done by spraying or immersion. Three types of oil are normally used, cottonseed oil, dioctyl sebacate and dibutyl sebacate, the latter being the most common. The normal amount of lubricant is in the order of 0.005 grs/m2. The lubricant is usually dried by means of steam and hot air coils.
The last part of the line depends on the formation of the final product and the productivity to be obtained, rather than the type of line (acid, …). If the production is exclusively in coils, there will be no cutting but there will be a storage device for the band, to allow the change of coils. If the production is exclusively in cut sheets, the storage device is not necessary. In the cutting operation, the selection of surface defects is made, this control is not very efficient due to the speed of the line, so the product obtained is classified as “unassorted” (unassorted). If you want to separate “firsts” from “seconds”, you need to use the auxiliary services of a selection line. It is in this section that off-spec and pin hole sheets are separated. When coils are delivered, it is normal not to make this separation, which decreases the yield, and it is up to the customer to do this operation when cutting. The quality “unselected” is defined as a normal product of an electrolytic tin plating line.
An electrolytic tinning line has a very complex auxiliary equipment, more complex in fact than the line itself, something similar to icebergs happens, you can’t see the sunken part. Electrical and electronic equipment, controls, pumps, electrolyte tanks, purification equipment, water and steam systems, air, etc., are of great importance and are normally installed underground. The installed electrical power is also very strong.
The strip speed during tinning is a function of the electrical current available for electrolysis, the condition of the electrolyte, the size and thickness of the material, the tin deposition desired and other factors.
As a consequence of the increase in the price of tin and the risk of seeing the sources of supply of tin in danger, during the last third of the last century a substitute product for tinplate was developed, the TFS or chrome-plated sheet. This material soon aroused an interest that has increased over time. Its advantage lies in the fact that it is a perfectly valid option for the manufacture of lids, bottoms, accessories and deep-drawn containers, and slightly cheaper than tinplate.
The TFS is made of a support identical to that of tinplate: steel. Although protection is assured, not by a light layer of tin applied by electrolytic deposition and by a passivation film, but by a mixed coating of chromium and chromium oxide.
In the steel industry it is common to produce TFS on a mixed installation, which can produce tinplate or chrome plate with a series of not very complex changes, which are carried out in a moderate time. The application of chromium is also carried out by electrolytic system. Figure 10 shows the special part of a line for the production of chrome-plated sheet metal.
We do not go into detail in the process of obtaining it, because as we have already indicated the base steel is the same as for tinplate, and the coating line follows a sequence analogous to that of tin plating.
Finally, it is worth mentioning the important participation of the large packaging companies in the developments in the manufacture of steel for tinplate, in the manufacture of tinplate itself, in other alternative materials such as TFS, and of course, in its use.
Can integrity - the ability of the can to deliver safe wholesome food to the consumer - may be compromised by a wide variety of defects. These defects may arise throughout the various stages of can manufacture, filling, closing, processing, and handling before the can reaches the consumer. The defect types are arranged into 7 different sections to reflect the stage in which the defect is likely to originate.
This document:
The visual examination of commercially sterile low-acid and acidified low-acid foods packed in hermetically sealed containers is used to help assess compliance.
A dye test can be used to detect container integrity defects that result in leakage on any area of a container, including the scoreline, pull tab and/or double seam. Refer to The Compendium of analytical methods, Volume 2 (MFHPB-05: Method for the determination of micro-leaks in hermetically sealed metal and glass container, May ) for instructions on how to conduct a dye test.
Any discussion or description of can defects requires standard terminology relating to the can components (end, body, double seam). The terminology required to describe these components varies with style of construction thus, only the main construction types are discussed in this section.
The key-open style of full panel easy open (FPEO) ends may vary in material, shape, and may have reinforcement features similar to two piece bodies. A key is inserted onto the key tab and rotated, rolling up the tab, tearing the metal along the scoreline, and rolling the end from the can.
The pull tab style of full panel easy open (FPEO) ends may vary in material and shape, and may have reinforcement features similar to two piece bodies. By lifting and pulling back on the pull tab, the scoreline is broken. By continuing to pull, the scoreline tears along its length.
The double seam is the joint formed between the body and the end by the mechanical interlocking and compression of the can flange and the end curl. For heat-treated food in sanitary cans this seam must be hermetic: that is, it must be impervious to the flow of materials through it in either direction.
The double seam is usually formed in 2 operations and consists of 5 layers of plate, except in the crossover area of three piece soldered or welded cans where there are 7 layers and in the key tab area of key-open cans where there are 6 layers. The first operation determines the amount of material in the seam while the second operation compresses the layers together. The suggested dimensions of a double seam will vary according to a number of factors including the shape and size of the can, the thickness of end and body plate, and the manufacturer of the can components and double seaming equipment.
There are a wide variety of potential can defects. This is due to the many steps involved in producing a filled can. In order to assess can integrity, information regarding these various steps is required.
Ingots of steel or aluminum of predetermined chemical composition are sent to their respective rolling mills. Here the ingots are rolled into very long, narrow, thin (0.010 in.), continuous sheets; these strip sheets are rolled into coils. The coils of steel are passed through a tin bath or a chromium bath in which either of these metals are electroplated onto steel to produce electrolytic tin plate (ETP) or tin free steel (TFS). The tin layer is approximately 15 millionths of an inch thick while the chromium layer is 0.8 millionths of an inch thick. The coils of aluminum may or may not receive a surface treatment. The respective metals are shipped to the can making plants in coil form.
Once these coils arrive at the can making plant they are cut into sheets. These sheets vary in size according to the size of can to be made but are approximately 1 metre by 1 metre.
There are many types of organic coatings: phenolic, oleoresinous, acrylic, epoxy phenolic, polybutadiene, to name a few. The type to be applied will depend on the product to be canned, the expected shelf life and, in the case of outside coatings, appearance requirements. Organic coatings tend to serve as a barrier between the metal and the can contents or environment.
The coatings are applied to each sheet by means of rollers. The sheets then pass through a bake oven where the coatings are cured. Depending on requirements, the inside may be single or double coated and the outside given a plain coat or a lithographed label. Inside coatings are applied first; each coating is baked prior to application of the next. Aluminum and TFS are always inside coated; TFS is always outside coated. ETP may or may not be inside or outside coated depending on requirements.
When coating sheets are destined to become the bodies of three piece cans (soldered or welded), a plain (uncoated) narrow strip or margin is left along the 2 sides that will form the side seam. Can bodies cannot be soldered or welded without these margins. Margins are usually not left on sheets from which ends or two piece cans are to be made.
These can bodies are made only from ETP. The plain or previously coated sheets are fed into a slitter which cuts the sheets into individual can body blanks. These blanks are then fed into a body maker where they are slit, notched, the side seams are hooked, interlocked, tightened, fluxed and soldered after which inside and outside side seam stripes (organic coatings) are sprayed along the side seam if required.
Depending on requirements, the can body may be beaded. Beads are formed in: a) the bodymaker during cylinder formation; or b) in a beader flanger after side seaming. The soldered cylinder is flanged after which an end is applied. The open top can is then air pressure tested and palletized for shipment to the cannery.
Sheets of steel (ETP or TFS) previously organic coated as required are similarly slit into individual can body blanks. These body blanks are slightly longer than the perimeter of the welded cylinder. The body blanks are fed into the body maker where the cylinder is formed. The edges forming the side seam overlap slightly. These edges are bonded together using electric resistance or laser welding. Once the cylinder is formed an inside and outside side seam stripe is sprayed on as required. The cylinder is then flanged, and an end is applied. The open top can is air pressure tested in the usual manner.
Welded can bodies may also be beaded. This operation is done after the cylinder has been welded and side seam striped but before the end is applied. Beader flangers and Krupp can-o-mat are 2 common beading machines.
Sheets of steel (ETP or TFS) or aluminum, previously organic coated as required, are cut into strips which are fed into a press. A disc is cut out and then in one (single draw) or more (draw-redraw) operations the metal is stretched and worked to the desired flanged height and bottom profile. This basic can advances to the trim press where the extra flange metal is cut off. If the can body is to be beaded, the can advances to a separate station (beader) where the bead is formed. This finished container is then air pressure tested and packaged for storage and/or shipment to the cannery.
Coated or uncoated sheets are cut into strips and fed into a single or double die press. In one operation the disc is cut out and the end profile (contour) is impressed in the metal. The disc then drops into a curling wheel which bends the cut edge to form the curl. This round basic end progresses to the compound line where, under a stationary nozzle, the end is rotated. During rotation the nozzle dispenses compound into the curl area.
These ends are cut into strips in a manner similar to round ends. They are usually held stationary while curling rolls follow the end perimeter to form the curl. At the compound liner station the end is again held stationary while the nozzle travels the seaming panel perimeter and dispenses compound.
These are made from flat profile (non-beaded or basic) ends. The basic ends are fed into a conversion press in which the end is scored, the flat profile modified with strengthening and convenience features and the rivet is formed. Tab stock (coil of metal approximately 3 cm wide) is fed into the press where the pull tab is formed. The pull tab then advances to the modified basic end to which it is attached at the rivet.
It is easiest to make these type of ends from aluminum. Many types are also made with ETP and a few are made with TFS. Steel (ETP and TFS) easy open ends may be fitted with aluminum pull tabs.
These ends are made in a manner similar to those described above. The key tab is an integral part of the end curl which is die formed. The key is usually spot welded to the end panel.
Ends are applied to the vast majority of food cans by machines called double seamers. The double seamer takes its name from the fact that the double seam is formed in 2 distinct operations. In the majority of double seamers these 2 operations are performed by seaming rolls. The can body and end are clamped on a seaming chuck by a load applied vertically to the base plate or lifter (see Figure 3.5.a). The first operation roll, tucks the end curl under the can flange such that they become interlocked (Fig. 3.5.b). The second operation roll compresses these interlocked layers of metal, squeezing the compound into the voids to complete an hermetic seal (Fig. 3.5.c). In canneries the double seamers are more appropriately called closing machines. These are variously equipped to apply an end to a filled can under a number of specific conditions dependent on the product and the packer's needs such as vacuum closure, steam flow closure and vacuum gas closure.
Some of the terminology associated with the can closing operation is as follows:
The prerequisites for achieving good double seam integrity are:
If the first 3 prerequisites are satisfied then final seam appraisal is based on the latter 2 prerequisites, namely overlap and tightness rating/pressure ridge. The various measurements of the double seam that may be taken aid in a decision that the overlap and tightness will be sufficient to ensure the sealing compound is properly held under compression.
The body and end hooks must overlap sufficiently to ensure that the sealing compound is properly held under compression with the correct seam tightness. The length of the overlap varies with the dimensional guidelines for each seam. In each case, however, a minimum length is provided in the accepted double seam guidelines. See Table 4.1.5.
Body hook butting may be taken separately as one of the factors of the double seam integrity. Body hook butting calculations cannot be substituted for overlap measurement in evaluating a double seam. Body hook butting should be considered as one of the factors that may be used for assessing double seams; overlap, tightness and pressure ridge are other important factors. The length of the body hook in relation to the internal length of the seam must be sufficient to ensure that it is embedded in the lining compound. Experience indicates that a minimum of 70% body hook butting is required to ensure an adequate seal.
Formula for body hook butting - using optical method for measurements:
% Body Hook Butting = B÷C × 100
Formula for body hook butting - when doing a tear down:
% Body Hook Butting = (BH − 1.1tb ÷ SL − 1.1(2te + tb)) × 100
Where BH = Body Hook Length (use the minimum of the readings taken at points of routine measurement Fig. 4.1.2.a)
tb = Body plate thickness
SL = Seam Length
te = End plate thickness
Double seam length - Alternate terms: height
This dimension is an indicator of overlap in that as the length increases, relative to the ideal, the overlap is usually reduced. Seam length is partly dependent on the roll groove profile and the degree of seaming roll wear.
The double seam must be sufficiently tight to hold the sealing compound under compression but not so tight that the metal plate is deformed with the possibility of metal fracturing.
There are 2 aspects that must be taken into consideration when judging seam tightness:
Other external double seam measurements which indicate proper seam tightness are:
When straight edges of plate are folded over on themselves, the fold is smooth. When curved edges are folded over on themselves, the fold is not smooth, that is to say, it is wrinkled. The degree of wrinkling increases as the radius of curvature decreases. When fitting an end that is either partly or totally round, wrinkles form on the end hook in the first operation. The degree of wrinkling is reduced when the double seam is compressed in the second operation. The double seam must be sufficiently tight so that the free space is low, but not zero. This will ensure that the sealing compound is properly held under compression.
The tightness rating is a measure of the degree of wrinkle left on the end hook on the completed double seam.
The pressure ridge or pressure area is an impression on the inside of the can body in the double seam area and is formed by the second operation seaming roll pressure. In suitably tight seams the impression should appear continuous and uniform along the entire periphery. The size of impression may vary from a faint continuous line approximately 3 mm below the body hook radius, to an obvious 3 mm wide area of compression (pressure area) in which the appearance of the body is slightly altered. The degree of impression is dependent on the body plate temper, the can size and style, and the double seaming equipment used.
The presence of an excessive pressure ridge should be avoided. There are occasions when a pressure ridge may be faint, absent or excessive but the seam may be satisfactory when other parameters are measured. The presence of a pressure ridge will depend on chuck design and temper as well as the type of container.
This dimension is an indicator of double seam tightness. For a given can, the thickness range should not exceed accepted double seam guidelines.
Since end and body metal thicknesses sometimes vary on the same container, the actual thickness of the 5 layers of metal would be calculated as:
(2 × body metal thickness) + (3 × end metal thickness) = Calculated double seam thickness (with no sealing compound)
In order to allow for seaming compound and normal seaming characteristics, a measured double seam thickness should not exceed this calculated thickness by more than 33% in the prime sealing area. The measured double seam thickness should not exceed the calculated double seam thickness by more than 33% in the prime sealing area.
This is the maximum thickness of the double seam where it intersects the lap.
The difference between the measured seam thickness and the sum of the 5 thicknesses making up the seam. This calculation may be used as an indicator of tightness; however, it must not be used to replace tightness rating.
Free space = seam thickness − (2 × body plate thickness + 3 × end plate thickness)
The process of assessing the double seam embodies 3 aspects, each of which provides varying amounts of qualitative and quantitative information:
A careful external visual examination of the can and its seams is the primary means of detecting container and seam defects:
All measurements should be recorded and the can marked in such a way that these external measurements can be directly related to the corresponding internal (teardown) measurements when the body hook and end hook are no longer engaged. It is most useful to take seam measurements at the points which indicate possible problems, such as sharp seams or excessive thickness. Averaging of double seam dimensions must not be done. Measurements are not usually taken at the crossover.
Seam measurements on round cans should be made at 3 points around the circumference of the can. Record the measurements which are approximately 120 degrees apart and at least 1 half-inch away from the side seam crossover of a three-piece can.
Seam dimensions of non-round cans are measured using the same method as for round cans; however, due to the irregular shapes of non-round cans, measurements should be taken at additional points as indicated in Figure 4.1.2.a. (Individual can makers publish guidelines which may specify alternate points which provide equivalent assurances of seam quality.) Additional points may also be cut, especially where irregularities are noted. Cans having a key tab must also have measurements taken at the centre of, and immediately adjacent to, the tab.
Most 'hidden' defects (those that are not immediately obvious during visual examination of the double seam) manifest themselves by an increased thickness measurement at the defect. Therefore, after visually examining a double seam for obvious defects, a seam micrometer should be guided around the entire periphery of the can to determine excessively thick measurements. These points should be marked, the length and thickness measurements recorded, and a seam section cut (Section 4.1.4.c) to show the seam profile. In this manner, a number of sections/measurements could be obtained from the points of concern. 'Routine' measurements could then be obtained from the remaining portion of the double seam. It is imperative (when this initial examination method is employed) that diagrams, demonstrating where the sections/measurements were taken, be constructed in order that common problem locations can be identified.
In cases where this initial examination reveals no seam thickness profile anomalies, the points for suggested routine length and thickness measurements for the various non-round shaped cans are illustrated in Figure 4.1.2.a.
Key-open non-round cans have an extra metal thickness at the tab. Specific can seam dimensional guidelines obtainable from the manufacturer should be used to evaluate this part of the seam. Measure in the same way as any other can.
Note: Measurements should be taken as identified in published can maker's guidelines. These guidelines may specify alternate points and frequencies which provide equivalent assurance of the seam quality.
Note: Measurements should be taken as identified in the can maker's guidelines. These guidelines may specify alternate points and frequencies which provide equivalent assurance of the seam quality.
Hold the flat surface of the micrometer against the can body as shown in Figure 4.1.2.c.
When using the micrometer, remember to:
Balance the micrometer with the index finger immediately above the seam until the anvil assumes the same angle as the taper of the countersink wall as shown in Figure 4.1.2.d.
Prior to using the countersink gauge, ensure that the point is tightly screwed onto the shaft. Place the bar of the gauge on a flat surface, preferably a block of machined steel large enough to detect warps in the bar (the bar of a second countersink gauge is useful for this purpose). In this position the point of the gauge is at the zero position and the dial of the gauge should also read zero. To adjust the "zero" on the dial, loosen the knurled screw near the top of the dial, rotate the outer scale until the zero and the indicator coincide, and tighten the screw to lock the gauge at the zero position.
Rest the bar of the depth gauge on top of the seam across the top of the can as shown in Figure 4.1.2.e. Position the point of the depth gauge pin (shaft) at the lowest point adjacent to the countersink wall (but away from the crossover of three piece cans) as shown in Figure 4.1.2.f.
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By tearing down the double seam, the following internal parameters may be measured and evaluated: tightness rating, body hook, end hook, internal droop, pressure ridge, crossover rating and jumped seam. These internal measurements must correspond to their respective external measurements (length, width, etc.), thus it is necessary to mark the can appropriately prior to teardown.
It is extremely important to recognize and understand that the quality of the double seams cannot always be judged on measured dimensions alone. Visual inspection for tightness and visible abnormalities are equally important. Dimensions outside the can maker's guidelines do not necessarily mean that seam integrity is compromised. It means that the seam should be carefully evaluated. Final judgement must be based on the amount of deviation along with all of the other measurements and observations.
Can makers supply guidelines to their customers and indicate frequency of tests as well as points of measurement. These can makers' guidelines recognize the need to check certain attributes at certain points on the can. Not all tests need to be performed at every check.
(a) Cut out the centre section of the can end (with either a sanitary type can opener or with tin snips) approximately 1 cm (⅜") from the double seam as shown in Figure 4.1.3.a. In the case of the FPEO pull tab can, the hole cutting/trimming is eliminated by simply pulling the tab and removing the can end.
(b) Remove the remainder of the can end using nippers as shown in Figure 4.1.3.b.
(c) Cut through the double seam at least 1 inch from the side seam lap using the nippers as shown in Figure 4.1.3.c.
(d) Remove the stripped part of the end by gently tapping with the nippers as shown in Figure 4.1.3.d. Take care not to distort the can body hook.
(e) Measure the end hook length using the seam micrometer as shown in Figure 4.1.3.e.
(f) Measure the body hook length using the seam micrometer as shown in Figure 4.1.3.f.
(g) Inspect the pressure area on the inside of the can body near the bottom of the double seam as shown in Figure 4.1.3.g. The pressure ridge should appear as a continuous and visible impression (but not excessively deep) around the inside periphery of the can body (see section 3.5.2 for further information on pressure ridge).
(h) Inspect the inside of the end hook and assess the wrinkles in terms of the tightness rating.
Due to the nature of the seaming process, wrinkle formation on the end hook during the first operation seaming process is unavoidable especially in the case of non-round cans where there is a sharp change in the radius of the seam. These wrinkles should be ironed out during the second operation.
The wrinkles remaining at the end of the second operation may be either looseness wrinkles or ghost wrinkles. The ability to differentiate between these 2 wrinkles is required in order to estimate tightness, as only looseness wrinkles are assessed.
The presence of looseness wrinkles indicates incomplete tightness in the double seam.
These wrinkles have 3 dimensions:
As the double seam becomes tighter these dimensions decrease. The length of any looseness wrinkles remaining after the second operation may be visually estimated and used as an indication of the double seam tightness provided that other seam parameters are within the double seam guidelines. By grading residual wrinkles in a normally formed seam, a reliable method of estimating seam tightness has been established.
There are various ways of expressing the tightness rating (see Figure 4.1.3.h and Table 4.1.3). The most commonly used North American system is % Tightness which is the estimated ratio of the length of smooth (unwrinkled) portion of end hook compared to the end hook length, expressed as a percent. The tightness rating is based on the length of the longest looseness wrinkle on the entire end hook. Looseness is the opposite of the tightness rating, (for example, 60% tightness rating is equivalent to 40% looseness).
Since a looseness wrinkle has 3 dimensions, the classification of the tightness should not be based only on the length of the wrinkle. It should also take into account the depth and width of the wrinkle. One of the ways of overcoming the problem of evaluating the double seam tightness would be to also evaluate the free-space and the percent compactness, according to the specifications provided by the can maker.
The minimum acceptable percent compactness is 75% in the prime sealing area.
Ghost wrinkles have length and width but no depth. The face of the hook is smooth indicating that the double seam has been suitably compressed or ironed out. These "wrinkles" are usually the remains, that is to say, shadows of second operation wrinkles that have been completely ironed out. They may also be indicative that compound between the body hook and cover hook was highly compressed. In either event, since the end hook is smooth, ghost wrinkles are not indicative of looseness.
Table 4.1.3 - Different methods for expressing tightness rating LoosenessLooseness wrinkle length expressed as a fraction of the end hook length.
In the case of non-round cans, there will be differences in the tightness rating at different points on the seam perimeter. In areas of the seam where the perimeter is straight, the tightness can be expected to be similar to that found in round cans. However, where there is a sharp change in seam radius at corners, there is necessarily less tightness as the curve radius is quite small and a relatively large amount of metal must be bent and accommodated in this radius. The setup aim must result in a tightness rating which will meet the accepted can manufacturer's guidelines for the specific can and can end; efforts to improve this are apt to lead to seam defects such as vees or cutovers. When cans are encountered with loose seams (see 7.5.15 loose seams), several considerations must be taken into account:
(i) Inspect the inside of the end hook on either side of the crossover of three piece cans for looseness indicative of a jumped seam, as shown in Figure 4.1.3.j. (See section 7.5.9 - jumped seam.)
(j) Inspect the inside of the end hook at the crossover of three piece cans for the amount of internal crossover droop (juncture rating) as shown in Figure 4.1.3.k. The amount of internal droop at this point should not exceed accepted can maker's guidelines.
(k) Determine the plate gauge thickness by removing the enamel coatings of a section of end plate; methyl ethyl ketone or steel wool may be used. Measure the end plate thickness using a micrometer with a domed anvil. Do not use the double seam micrometer.
(l) Optical (actual) overlap - Optical overlap measurements using a seam saw and seam projector will provide the actual overlap at the point of cross sectioning (see Section 4.1.4).
The presence of the key tab adds an extra layer of metal to the double seam in the tab area. This will result in a corresponding reduction in overlap. The overlap in the key tab area must comply with the minimum length in the accepted can maker's guidelines.
(m) Calculation of theoretical overlap - It should be noted that use of the calculation for theoretical overlap has more variability and has been demonstrated to both overestimate and underestimate the actual overlap as measured optically. There is no accurate substitute for optical measurement. For those who wish to include this factor in their records, a theoretical overlap may be calculated as follows:
Calculated overlap = Body hook + end hook + end plate thickness - seam length.
To determine the theoretical overlap, an adjustment factor is added to the calculated overlap. The following table of adjustment factors used by the B.C. Salmon Canning Industry is included as an example.
Calculated overlap Calculated overlapIn routine teardown examinations of a double seam, both teardown and optical methods may be used for routine measurements. In routine destructive examinations of a double seam, either method, teardown or cross section, is acceptable to determine seam tightness and overlap/seam profile respectively.
The use of theoretical overlap is not an accurate substitute for optical overlap. Teardowns or cross sections are carried out individually on different sample units or alternatively may be carried out on the same unit utilizing more than 1 unit if needed to attain the suggested number of measurement points.
The preparation of double seam cross sections provides direct measurement of the seam dimensions and integrity factors such as actual overlap and percent body hook butting. Cross sections can be prepared by either filing, sawing with a hand-held jeweller's saw, or sawing using a double or single blade seam saw.
The type, size and location of defect, as well as whether the inspection is being carried out in the field or lab will determine which method(s) is/are best suited. For example, a file would be useful for field inspections, and where a saw (hand held or electric), is not readily available. A jeweller's saw would be useful for field inspections and where use of an electric seam saw might totally obliterate the defect; that is, a cut made by the seam saw is wider than the total width of the defect at the point of occurrence.
Clean/polish the seam section with either a fine stone or emery cloth.
If the seam parameter being measured indicates a borderline accept/reject situation, the observations made with the pocket seam scope should be confirmed through use of the more accurate seam projector.
Remove the end hook from the balance of the double seam and check the pressure ridge, evidence of jumped seam, juncture rating, and tightness rating as per Section 4.1.3(g) to (j).
The can manufacturer provides a guideline for each can size and style outlining the seam measurements and tolerances for which the double seam was designed to ensure an hermetic container. Inspection procedures must be implemented which enable the can manufacturer or the cannery to hold for investigation (HFI), any product which does not comply with accepted guidelines.
These can maker's guidelines will vary according to whether the cans are steel or aluminum, two or three piece, soldered or welded, and round or non-round. An example of HFI guidelines for three piece round sanitary cans is included in Table 4.1.5. These tentative double seam dimensional guidelines provide HFI limits for round sanitary food cans used by North American manufacturers. These guidelines are not necessarily applicable to cans of other shapes or manufacture.
It is extremely important to remember that the quality of double seams cannot be judged on dimensions alone. Visual inspection for tightness and for any visible abnormalities is equally important.
When one or more measurements fall outside the adjustment limits, check another sample immediately. If it too is outside the limits, take whatever corrective action is indicated.
Dimensions outside of the adjustment limits do not necessarily mean that the seam is unacceptable. This means that you must decide if the seam is adequate. Final judgement must be based on the amount of deviation along with all of the other measurements and observations.
In making your determination, the prime considerations are overlap and tightness. The seam may be considered satisfactory when overlap and tightness are within adjustment limits and other dimensions are within hold for investigate limits with no serious defects and the seam is properly formed.
When the total seam evaluation indicates questionable performance, the cans should be held for further investigation such as sorting, leakage tests, incubation for spoilage, or simply holding to determine whether any spoilage develops. The type of action required depends upon the circumstances.
Information source: Can Manufacturers Institute - Voluntary Industry Can Standards
After examining the double seams, the rest of the can should be examined prior to teardown. The following points provide a checklist.
End deflection is a measure from the top edge of the double seam to the geometric centre of the end. A calibrated gauge, similar to the countersink gauge, is used by resting the bar along the top of the seam and away from the crossover. The point of the gauge is positioned at the approximate centre of the can end. Ensure that the embossed coding does not interfere with the measurement.
Pressure testing may be used as part of a container integrity examination. This is a test by which a standard pressure of air is forced into the can by means of a special instrument used specifically for this purpose.
This test is most commonly applied to emptied cans. The can bodies must be completely dry and the compound lining free from oil and water before and during pressure testing. The can is then placed right side up in the pressure testing instrument and submerged in water. By placing the can right side up, all the critical areas of the can are exposed to the pressure including the scoreline, the double seam, and the pull tab rivet. Pressure must be increased slowly and the cans must show no sign of leakage below 69 kPa (10 psig). If a can leaks below 69 kPa (10 psig) pressure, a serious defect is considered to exist and further investigations must be conducted to determine the source of that defect. For cans which are not intended to hold vacuum, non-round or cans with easy-open scoreline features, a maximum pressure of 48 kPa (7 psig) should be used.
These tests may be used to aid in the detection of hidden defects, but a successful leakage test (that is to say, the can does not leak) does not in any way lessen the seriousness of any other defect which may be present. There may be instances when this factor becomes of paramount importance and should be included in a risk assessment.
Leakage testing can also be conducted by drawing a vacuum on a clean empty can, utilizing appropriate equipment and conditions to ensure that any leakage can be easily identified. The vacuum test is recommended for non-round cans. The vacuum (in inches of water gauge) will depend on the can size and shape and is normally specified by the can maker.
The dye test using a water-based or mostly water-based dye such as Zylox is the preferred laboratory diagnostic testing method for any can size or shape for testing for leakage paths. Solvent-based dyes are best used for scorelines, side seams and plate fracture testing. Water-based dyes, such as Zyglo, are recommended for double seam testing.
The dye test(s) should be performed as suggested by the dye manufacturer, or can manufacturer. Government inspections will follow the official procedures.
Easy open ends can be tested for leakage paths in the score, rivet or embossed areas using a penetrating dye. Either a fluorescent dye or a dye requiring a developer may be used to detect a loss of hermetic seal. This procedure can be conducted on unused ends and on cans which have been emptied and thoroughly washed and dried.
Pull tabs and scorelines should be tested using the dye test method. It is not necessary for these tests to use the water-based dye. A solvent-based dye would be acceptable.
In addition to defect category and type, can defects are also classified according to severity. The following are the definitions used for severity classification of hermetically sealed and sterilized cans.
A serious condition is one which provides evidence that:
A minor condition is one which is clearly an abnormal container characteristic, but one which does not result in loss or potential loss of container integrity (hermeticity), and consequently does not represent a potential public health risk.
This section provides an index of defect terminology, including alternate terminology, specific defect types, and associated defect conditions.
Index of defect terminology Terminology Section Abrasion 7.7.1 Acid salts corrosion 7.3.1 Blown can 7.6.2 Body blank inverted 7.3.7 Broken chuck 7.5.1 Buckled body 7.3.28 Buckled can 7.6.3 Burned weld 7.3.17 Burrs on curl 7.4.1 Cable cut 7.7.5 Chalkly side seam 7.7.2 Clinched only 7.5.2 Clipped curl 7.4.5 Clipped flange 7.3.29 Coater ash 7.2.3 Coating drip 7.2.1 Coating inside out 7.3.27 Coating skips 7.2.2 Coating, damaged 7.7.7 Cocked body 7.3.14 Coil weld 7.1.4 Cold solder 7.3.2 Compound skips 7.4.4 Compound smear 7.4.4 Corrosion 7.7.3 Crushed 7.7.4 Cutover 7.5.3 Cut seam 7.7.5 Cut-down flange (C.D.F.) 7.5.4 Damage to scoreline/pull tab 7.7.6 Damaged coating 7.7.7 Damaged curl/flange 7.7.8 Deadhead 7.5.21 Dent 7.7.9 Dirty ends 7.4.4 Distorted reform ridge 7.3.3 Double body 7.3.28 Double end 7.4.2 Double seam dent 7.7.10 Droop 7.5.5 Enamel flaw 7.2.2 Excess sealing compound 7.4.4 Excessive solder 7.3.4 Excessively deep or weak scoreline 7.4.3 Eyeholing 7.2.2 False seam 7.5.6 Faulty sealing compound 7.4.4 Feather 7.5.3 Flaking coating 7.2.2 Flange burrs 7.3.20 Flange indent marks 7.7.8 Flipper 7.6.2 Fluted body 7.3.21 Flux stains 7.3.5 Foreign contamination 7.7.11 Foreign particles in coating 7.2.3 Fractured bottom profile 7.3.22 Fractured seam 7.5.7 High ends 7.3.14 Holed 7.7.12 Incomplete abuse bead 7.3.24 Incomplete bottom profile 7.3.23 Incomplete curl 7.4.5 Incomplete flange 7.3.29 Index fault 7.5.4 Inverted side coating 7.3.7 Insufficient overlap 7.5.8 Insufficient solder 7.3.6 Jumped seam 7.5.9 Key tab not properly tucked 7.5.10 Key tab seamed to inside 7.5.11 Knocked-down curl (K.D.C.) 7.5.12 Knocked-down end (K.D.E.) 7.5.13 Knocked-down flange (K.D.F.) 7.5.14 Laminated plate 7.1.1 Lip 7.5.22 Loose seams 7.5.15 Malformed abuse bead 7.3.24 Metal plate flaw 7.1.1 or 7.1.2 Mis-locked side seam 7.3.8 Mis-notch 7.3.9 Misembossing 7.6.1 Mushroomed flange 7.7.8 Necked-in-can 7.3.10 No second operation 7.5.16 Notcher trim still attached 7.3.11 Off-register body blank coating 7.3.12 Open lap 7.3.13 Open weld 7.3.18 Out of square body 7.3.14 Overfill 7.6.2 Panelling 7.6.3 Peaked can 7.6.4 Peeling coating 7.2.2 Perforation 7.1.2 Pin lip 7.5.22 Pin-hole 7.1.2 Plate stain 7.1.3 Pleats 7.5.17 Pucker 7.5.18 Pull tab rivet fracture 7.4.6 Pulled seam 7.7.10 Puncture 7.7.12 Pushed-in bottom 7.5.13 Rim dent 7.7.10 Rust 7.7.3 Scored 7.7.13 Scoreline, damaged 7.7.6 Scoreline, excessively deep 7.4.3 Scrap-in-die marks (bodies) 7.3.25 Scrap-in-die marks (ends) 7.4.7 Scuffed seam 7.5.21 Seam inclusions 7.5.19 Sharp seam 7.5.3 Side seam droop 7.5.20 Skidder 7.5.21 Solder pellets 7.3.15 Solder, cold 7.3.2 Solder, excessive 7.3.4 Solder, incomplete 7.3.6 Spinner 7.5.21 Split droop 7.5.19 Springer 7.6.2 Spur 7.5.22 Swell 7.6.2 Thick lap 7.3.4 Torn droop 7.5.12 Torn seam 7.7.5 Trim press marks 7.7.8 Turned back corner 7.3.19 Turned back flange 7.7.8 Turned back lap 7.3.16 Turned can 7.3.6 Vee 7.5.22 Weak lap 7.3.13 Weld joint 7.1.4 Wire edge 7.5.3 Wrinkled curl 7.4.8 Wrinkled flange 7.3.26A plate lamination is considered a serious metal plate defect.
Metal body or end plate which can be separated into 2 layers of metal which are not bonded.
A pin-hole is considered as a serious metal plate defect.
A hole in the metal plate originating in the rolling mill. These will vary in size from barely visible to large irregular shaped holes with rough edges.
Plate stain is considered as a minor metal plate defect.
Readily visible stains on the metal plate surface. If the metal plate is coated, these stains may be visible through the coating.
Photo not available.
A weld joint is considered a serious metal plate defect when packed with a corrosive product, when there are gaps in the continuous weld such as in spot welds or when the weld is weakened to the point that it fails under finger pressure.
An obvious, black line (joint) approximately 5 mm (3/16") wide running across the can end or body. They seldom result in leakage although there is potential for corrosion along this weld which may lead to perforation.
A coater drip is considered a minor defect unless careful examination proves that the defect is a serious defect. A coater drip is considered a serious coating application defect if a hole and/or plate corrosion is detected, after a thorough examination, which would include opening the can or removal of the coater drip to determine the condition of the metal plate.
A drop of coating, exterior or interior, often appearing as tiny hard metallic bubbles of coating. A coating drip may resemble a scrap-in-die type defect.
Inside view of A
Coating skips are considered serious coating application defects if:
Coating skips are considered minor coating application defects if:
Any discontinuity (bare spots, hairline skips, eyeholing) in the coating. Corrosion or sulphide production (reaction with product) may be present. See also section 7.7.3 - corrosion
A minor coating application defect.
Small particles in the coating surface, often black in colour. Coating ash may appear as a line on the body wall of two piece cans as the result of the drawing operation.
Acid salts corrosion is considered a serious three piece can defect.
Acidic residues on the outside of the side seam area that result in rusting, or any deposit of salts on the inside of the can.
Cold solder is considered a serious three piece can defect.
A discontinuity (gaps or voids) or a rough and spongy irregularity of the side seam solder fillet which could result in a pathway through the side seam. The cold solder condition will most easily occur in the lap area at the extremities of the side seam, but cannot be properly checked unless the side seam and double seam are torn down for examination.
A distorted reform ridge is considered a serious three piece can defect.
Creasing of the body and flange area on the reform ridge of reformed cans such that it affects the integrity of the double seam or fractures the metal plate.
Excessive solder is considered a serious three piece can defect, if:
Excessive solder at the customer lap area of the side seam which may cause deformation of the double seam at the crossover, resulting in excessive side seam droop, a raised seam, or a jumped seam. Excessive solder may also cause a pleat to form in the side seam lap. A thick lap is a condition where the side seam contains excess solder between the laps.
Flux stains are considered as minor three piece can defects.
Dark brown resinous staining on the inside surface of the side seam or lap. The fluxes used for the manufacture of food cans in Canada are non-toxic and will not impart off-odors or off-flavours to the product.
Insufficient solder is considered a serious three piece can defect if the solder fillet is incomplete along the outside of the side seam and is accompanied by a defective sweat.
Solder voids in the outside side seam fillet resulting in incomplete soldering of the side seam. The fillet is the strip of solder deposited along the intersection of the 2 walls of folded metal plate of the side seam. A turned can, depending on the degree of turning, results in a solder void or an incomplete fillet along the outside of the side seam.
A sweat is the action of bonding together, by application of heat, of surfaces to which solder has already been applied. A defective sweat is the result of improper solder temperature or incorrect flux application.
The inverted inside coating is considered a serious three piece can defect for a soldered can. On a welded can it is considered a minor defect unless there is product/container incompatibility.
The inside coating margin pattern is visible. Plain rectangular areas show at each end of the side seam. These plain areas are normally concealed in the side seam. Soldering will be incomplete due to coated areas in the side seam fold.
A mis-locked side seam is considered a serious three piece can defect.
Failure of the side seam hooks to interlock along their entire length. Complete soldering of the side seam is not always possible. The side seam most probably will not leak.
A mis-notch is considered a serious three piece can defect when a 0.8 mm (1/32") gap extends into the depth of the flange.
A gap in the side seam lap area where the notched or cut away section is not overlapped by metal plate resulting in an incomplete flange.
A necked-in can is considered a serious three piece can defect. This classification only applies to those cans which were not designed to be necked-in.
A can body which has an end diameter that is unintentionally smaller than the main body cylinder diameter. Either one or both ends of the body cylinder may be necked-in.
Necked-in cans are now commonplace in the beverage industry and the technology may appear in other food containers. Necked-in cans are intentionally necked-in to strengthen the can body. The can ends for such cans are intentionally smaller in diameter.
Notcher trim still attached is considered a serious three piece can defect due to additional metal formed into the double seam.
Extraneous metal at the side seam lap area having the shape of the section of body blank that is normally cut away prior to the formation of the side seam hooks.
An off register body blank coating is considered a serious three piece can defect when complete soldering of the side seam is not possible.
An off register or misplacement of the inside and/or outside coating. This may result in coating of the margin(s) along the body blank edges which will form the side seam. This misplaced coating prevents soldering. The side seam margin will appear elsewhere on the can body giving the can a turned appearance.
Open or weak lap is considered a serious three piece can defect if the solder bond at the lap is broken either before or after flexing the lap inward 2.4 mm (3/32").
A condition where light finger pressure on an empty can will cause the bonded (soldered) lap joint to open. When empty cans with weak laps or open laps are seamed, the lap joint solder frequently fractures resulting in an open lap and leakage. Such an open lap is sometimes difficult to observe, and cans with this defect appear "normal" except for gross liquid loss.
An out-of-square body is considered a serious three piece can defect.
A can body with a step in the flange of the lap area due to the lap members being misaligned by 0.79 mm (1/32") or more. Also called "high ends".
The occurrence of extraneous, loose or easily dislodged solder pellets, flakes, or strings of solder are considered serious as a product contaminant. The presence of solder pellets will seldom compromise can integrity, unless they are in the double seam (see seam inclusions 7.5.19).
The presence of solder droplets or pellets adhering to the inside surface adjacent to the side seam of the open-top can. Solder pellets are considered foreign material in the can.
A turned back lap is considered a serious three piece can defect.
A condition where one of the overlapping edges (laps) of the can body has been turned back during formation of the side seam. Such a defect will most probably result in an open (leaking) side seam.
A burned through weld is considered a serious weld defect.
Excessive local heat due to the presence of foreign materials. This results in a burned through condition.
An open weld is considered a serious weld defect.
An incomplete or parted side seam weld bond.
A turned back corner is considered a serious weld defect.
A triangular hole at either end of the side seam.
Flange burrs are considered as serious can manufacturing defects if the burr protrudes greater than or equal to 0.50 mm (0.020"). Flange burrs are considered minor can manufacturing defects, if the burr protrudes between 0.50 mm and 0.25 mm (0.020" and 0.010").
A rough protrusion of metal plate (a burr) on the cut edge of the flange.
A fluted body defect is generally considered a minor defect. If the flutes extend into the flange area it is considered a serious defect, when the degree of wrinkling is sufficiently pronounced so as to interfere with the formation of double seams, compromising its integrity.
One or more deep wrinkles on the tapered body.
Fractured bottom profile is considered a serious two piece can defect if:
A fractured bottom profile radius of a two piece style can or a pinched bottom profile radius which may fracture during processing or handling.
An incomplete bottom profile is considered a minor two piece can defect provided that the can does not buckle during retorting.
The integral end profile is not completely formed. This end is then weaker and may buckle during retorting.
A malformed or incomplete abuse bead is considered a serious can manufacturing defect if the metal plate is deeply abraded or creased.
The abuse bead on the two piece body is misaligned or incomplete. The metal plate may be abraded, creased or dented to varying degrees.
Scrap-in-die marks are considered serious can manufacturing defects if:
Scrap-in-die marks are considered minor can manufacturing defects if the marks are smooth, round, and the impressions are shallow.
An abnormal mark or impression in the metal plate which may vary in size, shape, and depth. If the scrap mark affects the formation of the flange, double seam defects may result.
Refer to the section on damaged coating (7.7.7) for additional information on fractured coating.
Wrinkled flange is considered a serious two piece can defect when the degree of wrinkling is sufficiently pronounced so as to interfere with the formation of the double seam, compromising its integrity.
Wrinkles in the walls of a two piece style can body extending into the flange area. The resulting flange thickness may be outside of guidelines, or wrinkles may form open channels through the double seam.
Coating inside out is considered a serious defect for three piece cans and for two piece cans, if the metal is exposed to a corrosive product, otherwise coating inside out is considered a minor defect for two piece cans.
The inside coating is on the outside of the can, and the outside coating, if present, is on the inside of the can. In three piece cans, this results in coating being present in the area to be soldered which will preclude complete soldering of the side seam. In two piece cans, the hermeticity of the can will not be affected, however, the incorrect (outside) coating, if present, will be in contact with, and may react with, the product.
A double body is considered a serious can body defect for both two piece and three piece cans.
In a three piece can, this defect occurs when 2 body blanks form the body of one can. The double seams are often thicker and longer but otherwise normal in appearance. Often the outer body will buckle and the side seam may appear mislocked or incompletely soldered.
An incomplete flange is considered serious if the flange is reduced by 0.4 mm (.016") or more. An incomplete flange is considered minor if the flange is reduced by less than 0.4 mm (.016").
Clips or cuts in the flange resulting in reduced or zero overlap in the double seam.
Burrs on curl are considered serious can end manufacturing defects if the burr protrudes greater than or equal to 0.5 mm (.020"). Burrs on curl are considered minor can end manufacturing defects if the burr protrudes between 0.5 mm and 0.25 mm (0.020" and 0.010").
A rough protrusion of metal plate (a burr) on the cut edge of the curl.
No photo available
A double end is considered a serious container defect.
Two ends are seamed onto one end of a can body. The double seam has the appearance of additional thickness and length, and may have numerous droops or vees along the double seam.
Excessively deep scoreline is considered a serious can end manufacturing defect if any of the following conditions are present:
Other serious scoreline defects are:
The scoreline is a thin single or double line around the end panel where the plate gauge is mechanically reduced by the scoring punch. If the panel is scored too deeply it may fracture or be weakened to the extent that it will break during processing or handling.
An excessively deep scoreline defect should be assessed with reference to the can maker's guidelines, which must include the minimum residual thickness of the scoreline. Its resistance to leakage testing, dye testing or scoreline testing may also be used.
No photo available.
The improper application of the sealing compound to the can end. The result can be excessive sealing compound, uneven distribution of compound, voids or gaps in the compound on the inside of the end curl. Other faults may be smearing of the sealing compound elsewhere on the end or spraying the sealing compound on the outside of the end curl (called "dirty ends").
An incomplete curl is considered as a serious can end manufacturing defect if the curl is reduced by more than 0.4 mm (0.016").
An incomplete curl is considered as a minor can end manufacturing defect if the curl is reduced by less than 0.4 mm (0.016").
Clips or cuts in the end curl resulting in loss of overlap.
A fractured pull tab rivet is considered a serious defect.
A break in that portion of the end panel from which the rivet is formed.
No photo available.
Scrap-in-die marks are considered serious can end manufacturing defects if:
Scrap-in-die marks are considered minor can end manufacturing defects if the marks are smooth, round, and the impressions are shallow.
An abnormal mark or impression in the metal plate which may vary in shape, size, and depth. If the scrap mark affects the formation of the curl, double seam defects may result.
A wrinkled curl is considered as a serious can end manufacturing defect when the degree of wrinkling is sufficiently pronounced so as to interfere with the formation of the double seam, compromising its integrity.
Wrinkles formed in the curl of can ends. The resulting curl thickness may be outside of guidelines, or wrinkles may form open channels through the double seam.
There are certain cases in which a certain degree of wrinkling in the curl of the can end is introduced by the design of the can end. If such is the case, the wrinkles will be considered as a defect when they are outside of the guidelines of the can end maker.
A broken chuck is considered a serious seam defect, due to absence of tightness at the point of the defect.
A portion of the double seam which is not properly ironed-out because of a void in the chuck lip (insufficiently tight), and appearing as an irregularity on the countersink wall of the seam.
Clinched only is considered as a serious double seam defect.
Only the clinching operation was completed. Cans are removed to check the clinching operation; these cans must be replaced so that the seaming operation will be completed.
A cutover is a sharp seam that has fractured and is considered a serious seam defect. A sharp seam is considered a minor seam defect.
A sharp seam is a sharp fin of metal formed when the seaming panel radius of the end is forced over the top of the seaming chuck flange during the seaming operation. Cutovers are sharp seams which have fractured and often occur at the crossover and with product inclusions but may occur all the way around the double seam; are best detected by running a finger around the inside of the seam.
Alternate terms: wire edge, feather, feather edge
Cutovers are often accompanied by other external double seam defects (as shown above KDC with Cutover)
A cut-down flange is considered a serious seam defect due to the absence of overlap.
A portion of the body flange which is torn or cut with part of the flange turned back against the can body, without being engaged with the end hook, and may protrude below the bottom of the normal seam. Severe forms of this defect result in a hole in the can body just below the double seam.
A unique type of CDF is the "index fault" found on reformed cans which consists of a characteristic tear in the flange approximately 10-15 mm from the reform ridge on the can body, due to flange damage caused by the reformer picker finger.
The only true assessment is done in a teardown where optical seam measurements of the overlap and seam tightness are assessed applying can manufacturing guidelines.
Any droop assessed as having 25% or less optical overlap will be classified as a serious double seam defect.
Any droop assessed as having 25% to 50% optical overlap will be classified as a minor double seam defect.
When a visual assessment is carried out, the droop will be considered a serious double seam defect if it extends more than 20% of the seam length, or more than 1 cm (⅜") along the seam, or if there is more than one droop on the double seam (confirmation of the classification must be from optical overlap measurements as indicated above).
A smooth projection of the end hook of the double seam below the bottom of the normal seam. A droop which shows signs of second operation roll marks will be assessed for classification in terms of overlap; otherwise see fractured seam (7.5.7).
A false seam is considered a serious seam defect due to the absence of overlap.
A defect where a portion of the body flange is bent back against the body, without being engaged with the end hook, but does not protrude below the bottom of the end hook radius. This is similar to a knocked-down flange defect where the body flange is visible below the end hook radius. This defect is difficult to observe and requires close visual inspection of the underside of the double seam where sometimes 2 layers of metal can be seen. Confirmation of this classification often requires a seam cut to observe the configuration of the end curl and body flange.
A fractured seam is considered a serious seam defect when the metal is fractured.
A fracture or break in the end hook radius. This defect may be difficult to observe without magnification. Seams which show second operation roll marks should be closely examined for this defect, particularly at the side seam or if a droop is present.
Sometimes designated: Cut Seam (see cut seam 7.7.5)
Alternate term: split droop
Any portion of the double seam having an optical overlap of less than 25% of the internal seam length is considered to contain a serious double seam defect.
The can manufacturer provides a guideline for each can size and style outlining the seam measurements and tolerances for which the double seam was designed to ensure an hermetic container. Adequate overlap is an essential requirement for the integrity of a double seam.
The body and end hooks must overlap sufficiently to ensure that the sealing compound is properly held under compression with the correct seam tightness. Calculating overlap by formula provides only an estimate of the overlap. There is no accurate substitute for optical measurement.
No photo available.
A jumped seam is considered a serious seam defect due to inadequate seam tightness.
Externally, this defect may appear as a looseness of the seam at one side of the crossover. Internally this defect appears as 2 or 3 looseness wrinkles at one side of the crossover. The defect occurs when the seaming rolls jump off the extra thickness of the crossover area. The side of the crossover on which the defect occurs depends on the seaming roll direction in relation to the crossover.
Key tab not properly tucked is considered a serious double seam defect if:
The key tab portion of end curl not properly incorporated into the double seam resulting in reduced or no overlap. The key tab may be cocked (crooked) or extended downward (partially or completely). Vees may be present on either side of the key tab and the double seam may be fractured.
A key tab seamed to the inside of the double seam is considered a serious double seam defect.
The key tab is not visible from the exterior of the can. There may be vees on either side of the area where the key tab is normally located. The tab is seen on the inside of the can when opened.
A knocked-down curl is considered a serious double seam defect due to the absence of overlap.
A portion of the end hook which is not engaged with the body hook but is turned down against the can body exposing the cut edge of the end plate. Variations of this defect can range from a 'V' with the edge of the end plate exposed, to complete knocking-down of the end hook all the way around the can.
A knocked-down end is considered a serious seam defect, due to the absence of overlap.
Severe distortion of the can end, as though struck by a downward blow inside the countersink, such that the hooks are disengaged or fail to engage, and part of the curl is pulled back to expose the flange. In severe forms of this defect the end curl is pulled back to expose (form) a hole in the can end.
Alternate term: pushed-in bottom
A knocked-down flange is considered a serious seam defect due to the absence of overlap.
A portion of the body flange which is bent back against the body, without being engaged with the end hook, and protruding below the bottom of the end hook radius. This is similar to a false seam defect where the body flange is not readily visible below the end hook radius. Severe forms of this defect involve knocking-down of both the flange and body leaving a distinctive gap between the can end and body. When caused by a feed screw (spacer) on the canning line, the defect has a distinctive "V"-shaped dent to the flange and body with a "signature" scratch down the centre.
A loose seam is considered a serious double seam defect if:
containers which are non-round and are designed for no vacuum, and where can manufacturer's guidelines are not available, tightness ratings are less than 50%, and for other non-rounded containers and where manufacturer's guidelines are not available, tightness ratings as specified in table 4.1.5 will be applied; or
A loose seam is normally characterized by one or more of the following conditions: rounded appearance of the double seam profile (a bowed seam configuration); seam thickness which exceeds accepted can manufacturer's guidelines; the can has a faint or no pressure ridge; and a low tightness rating. In severe examples of loose seams, the body hook and the end hook of a cut out (seam saw cross section) double seam may slide apart. This slippage condition in the double seam would demonstrate loose seam condition.
No second operation is considered as a serious double seam defect.
Only the first operation was completed. Cans are removed to check the first seaming operation; these cans must be replaced so that the second operation seaming will be completed.
A pleat is considered a serious defect if the pleat extends to the bottom of the double seam.
A pleat is a fold in the end hook which may be accompanied by a small vee-shaped projection of the end hook radius and the metal of the fold may be fractured. A pucker is intermediate between a wrinkle and a pleat, where the end hook is locally distorted downwards; it may or may not be externally visible.
A pucker is considered a serious defect if there is insufficient overlap (see 7.5.8).
A pucker is intermediate between a wrinkle and a pleat where the end hook is locally distorted downwards; it may or may not be externally visible.
Seam inclusions are considered as serious double seam defects.
Extraneous material or product included in the double seam.
The only true assessment is done in a teardown where optical seam measurements of the overlap and seam tightness are assessed applying can manufacturing guidelines.
Any side seam droop assessed as having 25% or less optical overlap will be classified as a serious double seam defect.
Any side seam droop assessed as having 25% to 50% optical overlap will be classified as a minor double seam defect.
When a visual assessment is carried out, the droop will be considered a serious double seam defect if it extends more than 20% of the seam length, or more than 1 cm (⅜") along the seam, or if there is more than one droop on the double seam (confirmation of the classification must be from optical overlap measurements as indicated above).
A smooth projection of the end hook of the double seam below the bottom of the normal seam at the crossover. A slight droop at the crossover may be considered normal because of the additional plate thicknesses incorporated in the seam structure. However, excessive droop at this point is not acceptable.
A spinner is considered a serious seam defect due to inadequate tightness.
A spinner is an incompletely ironed out double seam. It occurs when the chuck slips on the can end. This defect is characterized by part of the seam having normal thickness and part of the seam being loose (thick). This defect may be accompanied by a scuffing of the countersink wall radius caused by the chuck slipping. First operation spinner shows signs of vees around can, second operation spinner has incomplete double seam.
Alternate terms: deadhead, skidder, incomplete double seam
Associated Conditions: scuffed seam
Vees are considered to be serious double seam defects due to the absence of overlap at the point of the vee.
A sharp 'V' shaped projection of the end hook of the double seam below the bottom of the normal seam which results in no overlap.
Alternate terms: lip, spur
Misembossing is considered a serious can end defect if:
Misembossing includes sharp, illegible, misplaced, or multiple embossing. Sharp embossing may fracture the coating, leading to corrosion and perforation, or it may fracture the metal plate. Misplaced embossing which interferes with the pull tab or is on the scoreline or reinforcement lines or rings is likely to cause a fracture of the metal plate.
Must be treated as a serious container defect unless testing proves otherwise.
The terms overfill, flipper, springer, and swell are used to describe cans which have end(s) distended to varying degrees from several causes. The cans must be checked for microbial growth, chemical reaction such as hydrogen gas production, internal corrosion or weight.
Panelling is considered a serious container profile defect if the can body has been sharply distorted such that the internal coating has fractured or the double seam or side seam has been distorted.
A permanent distortion (collapsing) of the can body generally observed on larger sized containers. Appears as flat, vertical panels or indentations of the can body.
A peaked can is considered a serious container profile defect if the can end has been sharply distorted such that the metal plate or coating has fractured or the double seam has been distorted.
A permanent outward distortion of the can end in the form of pyramidal-like deformities near the double seams, resulting from a large differential between internal and external container pressures. Excessive peaking will adversely affect the integrity of the double seam.
Alternate terms: buckling, buckled end
Abrasion is considered a serious container defect when the metal has been reduced to less than 50% of its normal thickness.
A mechanical wearing of the metal plate. Abrasion results in the weakening of the metal plate making the abraded area susceptible to either fracture or corrosion which could eventually perforate the metal plate.
Chalky side seam is considered a minor side seam defect.
Chalky white deposits or corrosion on the side seam solder, which are unlikely to develop into a rusting condition.
Corrosion is considered to be a serious container defect if:
The deterioration of the metal plate from the inside or the outside of the container as a result of chemical reaction which can lead to penetration of the metal plate. Most commonly seen is external corrosion (rust) due to dampness (see also coating skips 7.2.2).
A crushed can is considered a serious container defect.
An extreme mechanical deformation of the metal container.
A cut seam is considered a serious double seam defect.
The physical tearing or cutting through of the outer layer of metal plate on the double seam, such that the inner layers of the double seam are exposed and the integrity of the double seam is compromised.
Alternate terms: torn seam, cable cut
Sometimes designated: fractured seam (see 7.5.7)
Damage to scoreline and/or pull tab is considered a serious can handling defect when:
A pull tab which has been twisted or distorted out of the horizontal or parallel plane with the can end. The scoreline may be pierced by the point of the tab, possibly resulting in leakage. The pull tab rivet may have been fractured or broken.
Damaged coating is considered a serious material handling defect if metal is scored and the product packed is corrosive.
Damaged coating is considered a minor material handling defect when exposed metal is not susceptible to rust and corrosion.
Obvious physical damage to either the inside or outside coated surface of the can end or can body which exposes bare metal, such as scratches, rub or scuff marks, essentially cosmetic in nature, but susceptible to corrosion (see corrosion - 7.7.3).
While fracture of the metal plate is obviously a loss of hermetic seal, the fracture of the coating may or may not result in reaction of the metal with the product or loss of hermetic seal. Where the metal is coated with tin and then overlayered with an organic coating, there is a double system of protection. If the product is very aggressive to tinplate, then the organic coating is very important. If the product is not aggressive to tinplate, then the loss of the organic coating is not important, especially if there is no reduction in expected shelf life of the product.
A damaged end curl is considered a serious handling defect when the end curl interferes with the double seam formation.
A damaged flange is considered a serious handling defect when damage extends more than 0.8 mm (1/32") from the normal flange level or is of sufficient size to cause a defective double seam.
A dented, bent or deformed end curl on the can end(s) or flange on can body such that it may cause seaming difficulties such as can end feed jam-ups and defective double seams.
A dent is considered a serious container defect if the can body or end has been sharply distorted such that:
The pronounced mechanical distortion of the metal container resulting in either significant reduction of the internal volume of the container or deformity of the can end or body, the double seam, or the side seam. Dents may crease the metal plate which may adversely affect the internal coating causing susceptibility to corrosion. Dents may distort the double seam or side seam such that vacuum loss may occur.
Lower limit of a serious body dent. Body dent is sharp and deep and the double seam has been pulled down below the level of the countersink depth of the can.
Upper limit of a minor body dent. Body dent is sharp and deep. Need to assess the inside coating for possible fractures, if the contents are considered as being a corrosive product which will react with the container, and the double seam has been distorted so that the dimensions are outside of the can maker's guidelines.
A double seam dent is considered a serious defect when:
The mechanical deformation of the double seam (can rim) of the container, caused by a sharp blow or excessive mechanical force to the double seam. Double seam (rim) dents can adversely affect the integrity of the double seam resulting in a potential for post-process contamination.
Foreign contamination inside the can is considered a serious defect.
Any observable amount of oil, grease, glue or dirt which is present on the inside surface of can ends or can bodies.
A puncture is considered a serious container defect.
The complete penetration through the metal plate of the can body or end by a sharp object such that there is loss of hermeticity.
A scored can end or can body is considered a serious can handling defect.
A sharp linear stressing (deformation) of the metal plate such that either the metal plate is fractured (has failed), or there is potential for failure due to corrosion or stress from normal handling.
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