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Acetylene combustion reactions

Oxyacetylene welding torches burn acetylene gas, C2H2(g). Use the information in Table 8.2 to calculate AH° (in kilojoules) for the combustion reaction of acetylene to yield C02(g) and H20(g). [Pg.319]

How do you write the balanced equation for the complete combustion of acetylene (ethyne) Complete hydrocarbon combustion reactions follow a general format ... [Pg.581]

You know that acetylene (ethyne) and oxygen are the reactants. Since the reaction is a complete combustion reaction, carbon dioxide and water vapour are the products. [Pg.581]

When a welder uses an acetylene torch, the combustion of acetylene liberates the intense heat needed for welding metals together. The equation for this combustion reaction is... [Pg.639]

In this paper we present a new technique for the synthesis of carbon film with carbynoid structures. The basis of the method described here consists of a combustion reaction between oxygen and acetylene and particular parameters for flame conditions. The flame volume can be considered as the reaction chamber as in conventional chemical vapor deposition (CvD) or physical vapor deposition (PVD) methods. This technique provides a method of synthesizing carbyne at high growth rates and of obtaining better crystals. [Pg.82]

When welding is done with an acetylene torch, acetylene combines with oxygen to form carbon dioxide and water. This combustion reaction is exothermic, and enough energy is released to melt metal. [Pg.209]

The early theory of methane oxidation assumed that carbon and water ware tile initial products of reaction or that hydrogen burned preferentially to carbon. However, in 1861 Kersten0 declared that carbon monoxide and hydrogen were the primary products, and that although some free carbon may form at times, the carbon is normally oxidized to carbon monoxide before the hydrogeu is reacted upon. This idea, later revived by Misterli,7 involves the preferential combustion of carbon and is thus directly opposed to the hydroxylation theory. Tins theory might possibly apply to the case of acetylene combustion, since this hydrocarbou is sufficiently unstable as to explode alone under certain conditions, but cannot hold for the more saturated hydrocarbons which do not explode alone. [Pg.154]

Combustion reactions occur rapidly and frequently with visible flames. The combustion of acetylene gas, C2H2(g), in an acetylene torch produces a great deal of heat per mole of acetylene, which makes it an excellent fuel for reaching the high temperatures needed to cut sheets of iron. [Pg.179]

The composition of hydrocarbons in the engine exhaust gases is partially correlated with fuel composition inasmuch as a small portion of the fuel leaves the combustion chamber unburned. The lighter hydrocarbons, such as methane, ethane, ethylene, and acetylene, are formed by the fragmentation of the fuel components during the combustion process. Certain other species—for example, benzene—also are present with a higher relative abundance than in the fuel, which indicates that they must be formed by combustion reactions. [Pg.180]

Exliaust gases from spark ignited engines contain alkynes, essentially acetylene. Alkynes strongly coordinate on precious metal catalysts and inliibit all post-combustion reactions. This occurs even at the low alkyne concentrations characteristic of real exliaust gases. Tliree major consequences have been evidenced ... [Pg.787]

The reaction shown above is the combustion reaction of acetylene. This reaction is made use of in welding, commonly called the acetylene torch. Tremendous amount of heat is liberated as a result of this reaction and is used for welding purposes. As you can see from the equation, the number of moles of the reactants is greater than the number of moles of the products. Thus, as the reaction proceeds, there is a decrease in the number of moles of gas. If you predicted a decrease in entropy, your answer is correct. [Pg.143]

When a mixture of 10.0 g of acetylene (C2H2) and 10.0 g of oxygen (O2) is ignited, the resultant combustion reaction produces CO2 and H2O. (a) Write the balanced chemical equation for this reaction, (b) Which is the limiting reactant (c) How many grams of C2H2,02, CO2, and H2O are present after the reaction is complete ... [Pg.112]

A detailed understanding of combustion must start with simple processes such as hydrogen, methane or acetylene combustion in oxygen or air. Normal liquid hydrocarbons are considerably more complex and wood or coal combustion can hardly be attacked on a molecular level. Below we give some "effective" chemical reactions leading to a transformation of fuel and oxidant into carbon dioxide and water. The processes are strongly exothermic, which is, of course, a common feature for combustion processes (Table 10.1). [Pg.302]

Acetylene (C2H2) torches are used in welding. How much heat (in kj) evolves when 5.0 L of C2H2 (d = 1.0967 kg/m ) is mixed with a stoichiometric amount of oxygen gas The combustion reaction is... [Pg.291]

The electric discharge processes can supply the necessary energy very rapidly and convert more of the hydrocarbons to acetylene than in regenerative or partial combustion processes. The electric arc provides energy at a very high flux density so that the reaction time can be kept to a minimum (see... [Pg.384]

Flame or Partial Combustion Processes. In the combustion or flame processes, the necessary energy is imparted to the feedstock by the partial combustion of the hydrocarbon feed (one-stage process), or by the combustion of residual gas, or any other suitable fuel, and subsequent injection of the cracking stock into the hot combustion gases (two-stage process). A detailed discussion of the kinetics for the pyrolysis of methane for the production of acetylene by partial oxidation, and some conclusions as to reaction mechanism have been given (12). [Pg.386]

The unit Kureha operated at Nakoso to process 120,000 metric tons per year of naphtha produces a mix of acetylene and ethylene at a 1 1 ratio. Kureha s development work was directed toward producing ethylene from cmde oil. Their work showed that at extreme operating conditions, 2000°C and short residence time, appreciable acetylene production was possible. In the process, cmde oil or naphtha is sprayed with superheated steam into the specially designed reactor. The steam is superheated to 2000°C in refractory lined, pebble bed regenerative-type heaters. A pair of the heaters are used with countercurrent flows of combustion gas and steam to alternately heat the refractory and produce the superheated steam. In addition to the acetylene and ethylene products, the process produces a variety of by-products including pitch, tars, and oils rich in naphthalene. One of the important attributes of this type of reactor is its abiUty to produce variable quantities of ethylene as a coproduct by dropping the reaction temperature (20—22). [Pg.390]

Inert combustion gases are injected directly into the reacting stream in flame reactors. Figures 23-22 and 22>-22d show two such devices used for maldng acetylene from light hydrocarbons and naphthas Fig. 23-22 shows a temperature profile, reaction times in ms. [Pg.2099]

Burning a portion of a combustible reactant with a small additive of air or oxygen. Such oxidative pyrolysis of light hydrocarbons to acetylene is done in a special burner, at 0.001 to 0.01 s reaction time, peak at 1,400°C (2,552°F), followed by rapid quenching with oil or water. [Pg.2099]

Hydrochloric acid may conveniently be prepared by combustion of hydrogen with chlorine. In a typical process dry hydrogen chloride is passed into a vapour blender to be mixed with an equimolar proportion of dry acetylene. The presence of chlorine may cause an explosion and thus a device is used to detect any sudden rise in temperature. In such circumstances the hydrogen chloride is automatically diverted to the atmosphere. The mixture of gases is then led to a multi-tubular reactor, each tube of which is packed with a mercuric chloride catalyst on an activated carbon support. The reaction is initiated by heat but once it has started cooling has to be applied to control the highly exothermic reaction at about 90-100°C. In addition to the main reaction the side reactions shown in Figure 12.6 may occur. [Pg.314]

Oxyacetylene torches used for welding reach temperatures near 2000°C. The reaction involved in die combustion of acetylene is... [Pg.71]


See other pages where Acetylene combustion reactions is mentioned: [Pg.324]    [Pg.120]    [Pg.483]    [Pg.51]    [Pg.55]    [Pg.111]    [Pg.478]    [Pg.483]    [Pg.120]    [Pg.199]    [Pg.201]    [Pg.203]    [Pg.584]    [Pg.268]    [Pg.386]    [Pg.387]    [Pg.389]    [Pg.476]    [Pg.530]    [Pg.129]   
See also in sourсe #XX -- [ Pg.423 ]




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