Contact process
The contact process is the current method of producing sulfuric acid in the high concentrations needed for industrial processes. Platinum was originally used as the catalyst for this reaction; however, as it is susceptible to reacting with arsenic impurities in the sulfur feedstock, vanadium(V) oxide (VO) is now preferred. History. This process was patented in 1831 by British vinegar merchant Peregrine Phillips. In addition to being a far more economical process for producing concentrated sulfuric acid than the previous lead chamber process, the contact process also produces sulfur trioxide and oleum. In 1901 Eugen de Haën patented the  basic process involving combining sulfur dioxide and oxygen in the presence of vanadium oxides, producing sulfur trioxide which was easily absorbed into water, producing sulfuric acid. This process was improved remarkably by shrinking the particle size of the catalyst (e.g. :le 5000 microns), a process discovered by two chemists of BASF in 1914. Process. The process can be divided into four stages: Purification of the air and sulfur dioxide (SO) is necessary to avoid catalyst "poisoning" (i.e. removing catalytic activities). The gas is then washed with water and dried with sulfuric acid. To conserve energy, the mixture is heated by  exhaust gases from the catalytic converter by heat exchangers. Sulfur dioxide and dioxygen then react as follows: According to the Le Chatelier's principle, a lower temperature should be used to shift the chemical equilibrium towards the right, hence increasing the percentage yield. However too low of a temperature will lower the formation rate to an uneconomical level. Hence to increase the reaction rate, high temperatures (450 °C), medium pressures (1-2 atm), and vanadium(V) oxide (VO) are used to ensure an adequate (>95%) conversion. The catalyst only serves to increase the rate of reaction as it does  not change the position of the thermodynamic equilibrium. The mechanism for the action of the catalyst comprises two steps: Hot sulfur trioxide passes through the heat exchanger and is dissolved in concentrated HSO in the absorption tower to form oleum Note that directly dissolving SO in water is impractical due to the highly exothermic nature of the reaction. Acidic vapor or mists are formed instead of a liquid. o Oleum is reacted with water to form concentrated HSO. Purification unit. This includes the dusting tower, cooling pipes, scrubbers, drying tower, arsenic purifier and testing box. Sulfur dioxide has many impurities  such as vapours, dust particles and arsenous oxide. Therefore, it must be purified to avoid catalyst poisoning (i.e.: destroying catalytic activity and loss of efficiency). In this process, the gas is washed with water, and dried by sulfuric acid. In the dusting tower, the sulfur dioxide is exposed to a steam which removes the dust particles. After the gas is cooled, the sulfur dioxide enters the washing tower where it is sprayed by water to remove any soluble impurities. In the drying tower, sulfuric acid is sprayed on the gas to remove the moisture from it. Finally, the arsenic oxide  is removed when the gas is exposed to ferric hydroxide. Double contact double absorption. The next step to the contact process is "double contact double absorption" (DCDA). In this process the product gases (SO) and (SO) are passed through absorption towers twice to achieve further absorption and conversion of SO to SO and production of higher grade sulfuric acid. SO-rich gases enter the catalytic converter, usually a tower with multiple catalyst beds, and are converted to SO, achieving the first stage of conversion. The exit gases from this stage contain both SO and SO which are passed through intermediate  absorption towers where sulfuric acid is trickled down packed columns and SO reacts with water increasing the sulfuric acid concentration. Though SO too passes through the tower it is unreactive and comes out of the absorption tower. This stream of gas containing SO, after necessary cooling is passed through the catalytic converter bed column again achieving up to 99.8% conversion of SO to SO and the gases are again passed through the final absorption column thus achieving not only high conversion efficiency for SO but also enabling production of a higher concentration of sulfuric acid. The industrial production of sulfuric  acid involves proper control of temperatures and flow rates of the gases as both the conversion efficiency and absorption are dependent on these.