Adrien Claude Bernard Chenot | |
---|---|
Born | |
Died | November 27, 1855 52) | (aged
Citizenship | French |
Alma mater | École des mines de Paris |
Known for | Metallurgy carbon monoxide |
Awards | Gold Medal of Honour Exposition Universelle (1855) |
Scientific career | |
Fields | Chemistry |
Adrien C. B. Chenot (born on August 30, 1803; died November 27, 1855) [1] was a French engineer best known for his inventions in metallurgy as well as his research on manufactured gases. He is notably the inventor of one of the first modern methods of direct reduction of iron ore, based on the use of coal reacting with the ore in retorts . He exhibited the first samples of pre-reduced iron ore at the Lisbon Universal Exhibition of 1849, [2] and was awarded the "Grandes Medailles d'Or" [3] (Gold Medal of Honour) [4] at the Paris Universal Exposition of 1855. [5]
Born in Bar-sur-Aube, he went to school in Nancy then in Paris. In 1820, he entered the Ecole des mines de Paris, and on leaving this school, he was attached to the General Secretariat of the Department of Bridges and Roads. He left this post some time after to operate mines in Auvergne. [2]
In 1826, Chenot was asked by Auguste de Marmont, Duke of Raguse, to carry out metallurgical studies at Châtillon-sur-Saône, where he filed a first patent relating to the direct manufacture of iron by treating powdered ore, mixed with coal, on a hearth of reverberatory furnace.
In 1832, he built a first direct reduction device at his home in Haute-Saône, which caused a sensation among neighboring forge masters, then moved to Clichy-la-Garenne. [2]
Chenot was also interested in the production of manufactured gas, more particularly wood gas for supplying reverberation ovens. Until 1842, he worked and patents on gases, shale oils, lead sulphates, etc. He invented the use of alkalis for the dephosphorization and desulphurization of manufactured gases, and proposed a classification of combustible gases based on their reactivity with alkalis. He studied the use of porous materials, sponges, to improve gas production, etc.
In 1849, he returned to his metallurgical research related to the reduction of metal oxides. The development of direct metallurgy, which consists in producing metals without going through the stages of melting (in the blast furnace) and refining (then carried out painfully by puddling), requires a scientific optimization of the chemical reactions previously carried out empirically in low furnaces . This approach seemed to him capable of revolutionizing metallurgy:
“In fact, releasing heat by oxidation and absorbing it by reduction, giving rise to electro-chemical and electro-dynamic currents, which rapidly distribute the local effects in the universe, such is the great mechanism which functions in nature. by the actions of nascent bodies or sponges. The science of the manufacture of metallic sponges must therefore henceforth serve as a basis not only for the metallurgical art, but for all others."
- BC Chenot, 1849
Its knowledge of the production of reducing gases is essential for the development of its oxide reduction processes: it simultaneously improves the obtaining of the gases necessary for its metallurgical processes, just like the processes themselves. He also understood the importance of the purity of the ore to ensure an economic interest in direct reduction processes, and invented an "electrotrieuse" which removes a large part of the raw minerals from their sterile gangue.
His research concerns the obtaining of metal sponges from many bodies (aluminum, calcium, silicon, barium, etc.), of which he is also studying the properties of their alloys with iron.
Chenot died suddenly and unexpectedly in November 1855 [4] after falling out of a window [3] apparently due to disorientation and nausea from experimenting carbon monoxide poisoning. [6] He was only 52 years old and active in his final days, although very weakened by the toxic gases inhaled during his experiments.
The Chenot process is one of the first direct reduction processes to succeed blast furnaces. [4] The method took over 25 years to develop. [3]
The method is a retort furnace 10m high, 1.5m wide and 0.5m deep, associated in pairs and whose walls are heated by 4 coal fires. Retorts are loaded from above with a mixture of charcoal and iron ore, and their contents are discharged downwards as soon as the load is sufficiently reduced. [7] Despite the presence of a cooler under the retorts, designed to restore its heat to the loaded ore, the “Heating method is […] very imperfect; more heat is lost outside than it is used in the retort itself”. Indeed, to produce one tonne of pre-reduced iron ore, the Chenot process consumes 350 kg of charcoal and 780 kg of hard coal, which is much more than the blast furnaces of the time which carried out both smelting and reduction, by consuming less than 1000 kg of coke; the thermal efficiency of the process is then estimated at 26%, compared to 70 or even 80% of blast furnaces of the period. Thus, Isaac Lowthian Bellestimates the fuel cost 2.3 times higher, and the loss 3.5 times higher than a blast furnace and Bessemer converter. [8] [9]
The ore used must be of excellent quality (80 to 82% hematite ), and stays for nearly 8 days in the apparatus (half the time in the retort, then in the cooler ). However, loading and emptying are partial and therefore more regular: there is a processing capacity of 1.2 to 1.5 tonnes per day of ore, i.e. 400 tonnes per year per unit of production, far from the production capacities of blast furnaces. from epoch . The iron sponge obtained contains 13% of waste rock, which must be heated and slashed, or melted, to obtain a usable mass of iron. [7]
However, the process strongly marked its contemporaries because it exploited and validated the new understanding of chemical oxidation-reduction reactions in metallurgy . But, although it illustrates the perfect knowledge of its author of modern metallurgy, it raises many questions as to its profitability:
"It is difficult to understand today that the Chenot process was originally considered to be intended to revolutionize the iron industry, whereas it can only be applied to absolutely pure ores, all of which are the times that one does not resolve to remelt the sponge in the crucible or in the Martin oven. It is also not understood that, in a single factory, ten furnaces could have been assembled, representing a considerable expense, to manufacture a product involving, per tonne of sponge, the consumption of 1,400 kilos of charcoal for the reduction and 1,723 kilos of hard coal for heating retorts : the sponge could not be transformed into iron except by agglomerating it in the Comtois fire at the cost of a new consumption of coal." [5]
- A. Ledebur,
Operational in the 1850s in a few factories in France (at the Chenot de Clichy factory in 1855, at Pontcharra in 1856 and Hautmont in 1857), in Spain (at Barakaldo in 1852), in Belgium (at Couillet in 1856) and in Italy. [5] The process was also tried in the United States, where a slightly improved variant by Blair operated in Pittsburg until 1846. Another furnace, in Ravensdale (North Staffordshire), started up in 1875, without proving to be more profitable.
The Englishman Yates takes advantage of the fact that the hearths heating the retorts can be fed by a gas instead of coal, and in this sense proposes a modification of the Chenot process in 1860. [10] [7]
Also in 1860, the American Renton then, in 1875, the Frenchman Verdié in Firminy, proposed a more original variant, consisting in using the waste heat from the chimney of the puddling furnaces to heat a retort of reduced size. But, if “at first glance, the operation seems rational, the reduction is incomplete, the waste high, the bottom of the retort […] quickly corroded. It is always difficult to coordinate, in one oven, two separate operations: reducing waste heat and refining on the sole of the lamppost". [7]
Finally, his son Eugène Chenot continued his father's studies by building in 1862, at the Ramade plant in Clichy, a direct reduction furnace foreshadowing the continuous processes of direct reduction with gases alone, which however did not succeed. better than the process developed by his father.
The steel is obtained by soaking a part (about a quarter) of the iron sponge in a carburized liquid (wood tar, etc.), then by melting the carburized sponges with the non-carburized sponges. The steel obtained in this way is deemed to be of good quality, although there are better ones. In 1867, the cost price of a ton of Chenot steel produced in Clichy was estimated at 1,097.29 Fr, and 500 Fr at Baracaldo [10] where it was popular for use as horse-shoes nails. [3]
Carbon monoxide served as a reducing agent in the Chenot method. [3] Chenot was among the first to report the toxicity of carbon monoxide poisoning. [11] He suffered from the after-effects of carbon monoxide poisoning suffered during his numerous experiments. He was particularly seriously intoxicated in 1846, while working in the factories of the Marquis de Sassenay, in Prussia. According to him, “the carbon monoxide turns into carbonic acid causing deadly deoxidation. […] The cause of the pathophysiological disorders could also be a sudden increase in temperature due to the overoxidation of carbon in the blood”. Of course, Chenot, who "Admits that carbon monoxide plays in the blood the [same] role of reducing body as in metallurgy", can only offer a partial explanation since it does not carefully analyze the physiological aspects. Despite limitations of his analysis, Chenot remains among the first to propose a chemical theory of the mechanism of poisoning by this gas. [11] [12]
Adrien Chenot also campaigned for the repeal of the law relating to the establishment of major railway lines in France .
Smelting is a process of applying heat and a chemical reducing agent to an ore to extract a desired base metal product. It is a form of extractive metallurgy that is used to obtain many metals such as iron, copper, silver, tin, lead and zinc. Smelting uses heat and a chemical reducing agent to decompose the ore, driving off other elements as gases or slag and leaving the metal behind. The reducing agent is commonly a fossil fuel source of carbon, such as carbon monoxide from incomplete combustion of coke—or, in earlier times, of charcoal. The oxygen in the ore binds to carbon at high temperatures as the chemical potential energy of the bonds in carbon dioxide is lower than that of the bonds in the ore.
Steelmaking is the process of producing steel from iron ore and/or scrap. In steelmaking, impurities such as nitrogen, silicon, phosphorus, sulfur and excess carbon are removed from the sourced iron, and alloying elements such as manganese, nickel, chromium, carbon and vanadium are added to produce different grades of steel.
A blast furnace is a type of metallurgical furnace used for smelting to produce industrial metals, generally pig iron, but also others such as lead or copper. Blast refers to the combustion air being supplied above atmospheric pressure.
Industrial processes are procedures involving chemical, physical, electrical, or mechanical steps to aid in the manufacturing of an item or items, usually carried out on a very large scale. Industrial processes are the key components of heavy industry.
An open-hearth furnace or open hearth furnace is any of several kinds of industrial furnace in which excess carbon and other impurities are burnt out of pig iron to produce steel. Because steel is difficult to manufacture owing to its high melting point, normal fuels and furnaces were insufficient for mass production of steel, and the open-hearth type of furnace was one of several technologies developed in the nineteenth century to overcome this difficulty. Compared with the Bessemer process, which it displaced, its main advantages were that it did not expose the steel to excessive nitrogen, was easier to control, and permitted the melting and refining of large amounts of scrap iron and steel.
A bloomery is a type of metallurgical furnace once used widely for smelting iron from its oxides. The bloomery was the earliest form of smelter capable of smelting iron. Bloomeries produce a porous mass of iron and slag called a bloom. The mix of slag and iron in the bloom, termed sponge iron, is usually consolidated and further forged into wrought iron. Blast furnaces, which produce pig iron, have largely superseded bloomeries.
Pyrometallurgy is a branch of extractive metallurgy. It consists of the thermal treatment of minerals and metallurgical ores and concentrates to bring about physical and chemical transformations in the materials to enable recovery of valuable metals. Pyrometallurgical treatment may produce products able to be sold such as pure metals, or intermediate compounds or alloys, suitable as feed for further processing. Examples of elements extracted by pyrometallurgical processes include the oxides of less reactive elements like iron, copper, zinc, chromium, tin, and manganese.
Decarburization is the process of decreasing carbon content, which is the opposite of carburization.
Puddling is the process of converting pig iron to bar (wrought) iron in a coal fired reverberatory furnace. It was developed in England during the 1780s. The molten pig iron was stirred in a reverberatory furnace, in an oxidizing environment to burn the carbon, resulting in wrought iron. It was one of the most important processes for making the first appreciable volumes of valuable and useful bar iron without the use of charcoal. Eventually, the furnace would be used to make small quantities of specialty steels.
Direct reduced iron (DRI), also called sponge iron, is produced from the direct reduction of iron ore into iron by a reducing gas which either contains elemental carbon or hydrogen. When hydrogen is used as the reducing gas there are no greenhouse gases produced. Many ores are suitable for direct reduction.
The Boudouard reaction, named after Octave Leopold Boudouard, is the redox reaction of a chemical equilibrium mixture of carbon monoxide and carbon dioxide at a given temperature. It is the disproportionation of carbon monoxide into carbon dioxide and graphite or its reverse:
An Ellingham diagram is a graph showing the temperature dependence of the stability of compounds. This analysis is usually used to evaluate the ease of reduction of metal oxides and sulfides. These diagrams were first constructed by Harold Ellingham in 1944. In metallurgy, the Ellingham diagram is used to predict the equilibrium temperature between a metal, its oxide, and oxygen — and by extension, reactions of a metal with sulfur, nitrogen, and other non-metals. The diagrams are useful in predicting the conditions under which an ore will be reduced to its metal. The analysis is thermodynamic in nature and ignores reaction kinetics. Thus, processes that are predicted to be favourable by the Ellingham diagram can still be slow.
Cornwall Iron Furnace is a designated National Historic Landmark that is administered by the Pennsylvania Historical and Museum Commission in Cornwall, Lebanon County, Pennsylvania in the United States. The furnace was a leading Pennsylvania iron producer from 1742 until it was shut down in 1883. The furnaces, support buildings and surrounding community have been preserved as a historical site and museum, providing a glimpse into Lebanon County's industrial past. The site is the only intact charcoal-burning iron blast furnace in its original plantation in the western hemisphere. Established by Peter Grubb in 1742, Cornwall Furnace was operated during the Revolution by his sons Curtis and Peter Jr. who were major arms providers to George Washington. Robert Coleman acquired Cornwall Furnace after the Revolution and became Pennsylvania's first millionaire. Ownership of the furnace and its surroundings was transferred to the Commonwealth of Pennsylvania in 1932.
Zinc smelting is the process of converting zinc concentrates into pure zinc. Zinc smelting has historically been more difficult than the smelting of other metals, e.g. iron, because in contrast, zinc has a low boiling point. At temperatures typically used for smelting metals, zinc is a gas that will escape from a furnace with the flue gas and be lost, unless specific measures are taken to prevent it.
Endothermic gas is a gas that inhibits or reverses oxidation on the surfaces it is in contact with. This gas is the product of incomplete combustion in a controlled environment. An example mixture is hydrogen gas (H2), nitrogen gas (N2), and carbon monoxide (CO). The hydrogen and carbon monoxide are reducing agents, so they work together to shield surfaces from oxidation.
The Corex Process is a smelting reduction process created by Primetals as a more environmentally friendly alternative to the blast furnace. Presently, the majority of steel production is through the blast furnace which has to rely on coking coal. That is coal which has been cooked in order to remove impurities so that it is superior to coal. The blast furnace requires a sinter plant in order to prepare the iron ore for reduction. Unlike the blast furnace, smelting reduction processes are typical smaller and use coal and oxygen directly to reduce iron ore into a usable product. Smelting reduction processes come in two basic varieties, two-stage or single-stage. In a single-stage system the iron ore is both reduced and melted in the same container. In a two-stage process, like Corex, the ore is reduced in one shaft and melted and purified in another. Plants using the Corex process have been put use in areas such as South Africa, India, and China. First COREX process was installed in 1988 at South Africa.
A metallurgical furnace, often simply referred to as a furnace when the context is known, is an industrial furnace used to heat, melt, or otherwise process metals. Furnaces have been a central piece of equipment throughout the history of metallurgy; processing metals with heat is even its own engineering specialty known as pyrometallurgy.
In the iron and steel industry, direct reduction is a set of processes for obtaining iron from iron ore, by reducing iron oxides without melting the metal. The resulting product is pre-reduced iron ore.
Direct reduction is the fraction of iron oxide reduction that occurs in a blast furnace due to the presence of coke carbon, while the remainder - indirect reduction - consists mainly of carbon monoxide from coke combustion.
The Krupp–Renn process was a direct reduction steelmaking process used from the 1930s to the 1970s. It used a rotary furnace and was one of the few technically and commercially successful direct reduction processes in the world, acting as an alternative to blast furnaces due to their coke consumption. The Krupp-Renn process consumed mainly hard coal and had the unique characteristic of partially melting the charge. This method is beneficial for processing low-quality or non-melting ores, as their waste material forms a protective layer that can be easily separated from the iron. It generates Luppen, nodules of pre-reduced iron ore, which can be easily melted down.
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