My business is Franchises. Ratings. Success stories. Ideas. Work and education
Site search

Lower heating value of industrial oil. Specific heat of combustion of fuel and combustible materials

The calorific value is understood as the heat of complete combustion of a unit mass of a substance. It takes into account heat losses associated with the dissociation of combustion products and the incompleteness of chemical combustion reactions. Calorific value is the maximum possible heat of combustion per unit mass of a substance.

Determine the calorific value of elements, their compounds and fuel mixtures. For elements, it is numerically equal to the heat of formation of the combustion product. The calorific value of mixtures is an additive quantity and can be found if the calorific value of the components of the mixture is known.

Combustion occurs not only due to the formation of oxides, therefore in a broad sense we can talk about the calorific value of elements and their compounds not only in oxygen, but also when interacting with fluorine, chlorine, nitrogen, boron, carbon, silicon, sulfur and phosphorus.

Calorific value is an important characteristic. It allows you to evaluate and compare with others the maximum possible heat release of a particular redox reaction and determine in relation to it the completeness of the actual combustion processes. Knowledge of the calorific value is necessary when selecting fuel components and mixtures for various purposes and when assessing their completeness of combustion.

There are higher H in and below H n calorific value. Higher calorific value, in contrast to lower calorific value, includes the heat of phase transformations (condensation, solidification) of combustion products when cooled to room temperature. Thus, the highest calorific value is the heat of complete combustion of a substance when the physical state of the combustion products is considered at room temperature, and the lowest calorific value is at the combustion temperature. The higher calorific value is determined by burning the substance in a calorimetric bomb or by calculation. It includes, in particular, the heat released during the condensation of water vapor, which at 298 K is equal to 44 kJ/mol. The lower calorific value is calculated without taking into account the heat of condensation of water vapor, for example, using the formula

Where % H is the percentage of hydrogen in the fuel.

If calorific value values ​​indicate the physical state of combustion products (solid, liquid or gas), then the “highest” and “lowest” subscripts are usually omitted.

Let us consider the calorific value of hydrocarbons and elements in oxygen per unit mass of the original fuel. The lower calorific value differs from the highest for paraffins by an average of 3220-3350 kJ/kg, for olefins and naphthenes - by 3140-3220 kJ/kg, for benzene - by 1590 kJ/kg. When experimentally determining the calorific value, it should be borne in mind that in a calorimetric bomb the substance burns at a constant volume, and in real conditions, often at a constant pressure. The correction for the difference in combustion conditions ranges from 2.1 to 12.6 for solid fuel, about 33.5 for fuel oil, 46.1 kJ/kg for gasoline, and reaches 210 kJ/m3 for gas. In practice, this correction is introduced only when determining the calorific value of the gas.

For paraffins, the calorific value decreases with increasing boiling point and increasing C/H ratio. For monocyclic alicyclic hydrocarbons this change is much less. In the benzene series, the calorific value increases when moving to higher homologues due to the side chain. Dinuclear aromatic hydrocarbons have a lower calorific value than the benzene series.

Only a few elements and their compounds have a calorific value that exceeds that of hydrocarbon fuels. These elements include hydrogen, boron, beryllium, lithium, their compounds and several organoelement compounds of boron and beryllium. The calorific value of elements such as sulfur, sodium, niobium, zirconium, calcium, vanadium, titanium, phosphorus, magnesium, silicon and aluminum lies in the range of 9210-32,240 kJ/kg. For the remaining elements of the periodic system, the calorific value does not exceed 8374 kJ/kg. Data on the gross calorific value of various classes of fuels are given in table. 1.18.

Table 1.18

Gross calorific value of various combustibles in oxygen (per unit mass of fuel)

Substance

Carbon monoxide

iso-butane

n-Dodecane

n-Hexadecane

Acetylene

Cyclopentane

Cyclohexane

Ethylbenzene

Beryllium

Aluminum

Zirconium

Beryllium hydride

Psntaboran

Metadiborane

Ethyldiborane

For liquid hydrocarbons, methanol and ethanol, heating values ​​are based on the liquid starting state.

The calorific value of some fuels was calculated on a computer. It is 24.75 kJ/kg for magnesium and 31.08 kJ/kg for aluminum (the state of the oxides is solid) and practically coincides with the data in Table. 1.18. The highest calorific value of paraffin C26H54, naphthalene C10H8, anthracene C14H10 and methenamine C6H12N4 are 47.00, 40.20, 39.80 and 29.80, respectively, and the lowest calorific value is 43.70, 39.00, 38.40 and 28.00 kJ/kg.

As an example, in relation to rocket fuels, we present the heats of combustion of various elements in oxygen and fluorine, per unit mass of combustion products. The heats of combustion are calculated for the state of combustion products at a temperature of 2700 K and are shown in Fig. 1.25 and in table. 1.19.

Puc. 1.25. Heat of combustion of elements in oxygen (1) and fluorine(2), calculated per kilogram of combustion products

As follows from the data presented, to obtain maximum combustion heat, the most preferred substances are those containing hydrogen, lithium and beryllium, and secondarily, boron, magnesium, aluminum and silicon. The advantage of hydrogen due to the low molecular weight of combustion products is obvious. It should be noted that beryllium has an advantage due to its high heat of combustion.

There is the possibility of the formation of mixed combustion products, in particular gaseous oxyfluorides of elements. Since oxyfluorides of trivalent elements are usually stable, most oxyfluorides are not effective as combustion products of rocket fuels due to their high molecular weight. The heat of combustion with the formation of COF2 (g) has an intermediate value between the heats of combustion of CO2 (g) and CF4 (g). The heat of combustion with the formation of SO2F2 (g) is greater than in the case of the formation of SO2 (g) or SF6; (G.). However, most rocket fuels contain highly reducing elements that prevent the formation of such substances.

The formation of aluminum oxyfluoride AlOF (g) releases less heat than the formation of oxide or fluoride, so it is not of interest. Boron oxyfluoride BOF (g) and its trimer (BOF)3 (g) are quite important components of the combustion products of rocket fuels. The heat of combustion to form BOF (g) is intermediate between the heats of combustion to form oxide and fluoride, but oxyfluoride is thermally more stable than either of these compounds.

Table 1.19

Heat of combustion of elements (in MJ/kg), per unit mass of combustion products ( T = 2700 K)

oxyfluoride

Beryllium

Oxygen

Aluminum

Zirconium

When beryllium and boron nitrides are formed, a fairly large amount of heat is released, which allows them to be classified as important components of rocket fuel combustion products.

In table Table 1.20 shows the highest calorific value of elements when they interact with various reagents, referred to a unit mass of combustion products. The calorific value of elements when interacting with chlorine, nitrogen (except for the formation of Be3N2 and BN), boron, carbon, silicon, sulfur and phosphorus is significantly less than the calorific value of elements when interacting with oxygen and fluorine. The wide variety of requirements for combustion processes and reagents (in terms of temperature, composition, state of combustion products, etc.) makes it advisable to use the data in Table. 1.20 in the practical development of fuel mixtures for one purpose or another.

Table 1.20

Higher calorific value of elements (in MJ/kg) when interacting with oxygen, fluorine, chlorine, nitrogen, per unit mass of combustion products

  • See also: Joulin S., Clavin R. Op. cit.

What is fuel?

This is one component or a mixture of substances that are capable of chemical transformations associated with the release of heat. Different types fuels differ in their quantitative content of oxidizer, which is used to release thermal energy.

In a broad sense, fuel is an energy carrier, that is, a potential type of potential energy.

Classification

Currently, fuel types are divided according to their state of aggregation into liquid, solid, and gaseous.

Natural hard materials include stone, firewood and anthracite. Briquettes, coke, thermoanthracite are types of artificial solid fuel.

Liquids include substances containing substances of organic origin. Their main components are: oxygen, carbon, nitrogen, hydrogen, sulfur. Artificial liquid fuel will be a variety of resins and fuel oil.

Gaseous fuel is a mixture of various gases: ethylene, methane, propane, butane. In addition to them, the composition contains carbon dioxide and carbon monoxide, hydrogen sulfide, nitrogen, water vapor, and oxygen.

Fuel indicators

The main indicator of combustion. The formula for determining the calorific value is considered in thermochemistry. emit “standard fuel”, which implies the calorific value of 1 kilogram of anthracite.

Household heating oil intended for combustion in heating devices of low power, which are located in residential premises, heat generators used in agriculture for drying feed, canning.

The specific heat of combustion of a fuel is a value that demonstrates the amount of heat that is generated during the complete combustion of fuel with a volume of 1 m 3 or a mass of one kilogram.

To measure this value, J/kg, J/m3, calorie/m3 are used. To determine the heat of combustion, the calorimetry method is used.

With an increase in the specific heat of combustion of fuel, it decreases specific consumption fuel, and the coefficient useful action remains unchanged.

The heat of combustion of substances is the amount of energy released during the oxidation of a solid, liquid, or gaseous substance.

It is determined by the chemical composition, as well as state of aggregation combustible substance.

Features of combustion products

The higher and lower calorific values ​​are related to the state of aggregation of water in the substances obtained after combustion of fuel.

The higher calorific value is the amount of heat released during complete combustion of a substance. This value also includes the heat of condensation of water vapor.

The lowest working heat of combustion is the value that corresponds to the release of heat during combustion without taking into account the heat of condensation of water vapor.

The latent heat of condensation is the amount of energy of condensation of water vapor.

Mathematical relationship

The higher and lower calorific values ​​are related by the following relationship:

QB = QH + k(W + 9H)

where W is the amount by weight (in %) of water in a flammable substance;

H is the amount of hydrogen (% by mass) in the combustible substance;

k - coefficient equal to 6 kcal/kg

Methods for performing calculations

The higher and lower calorific values ​​are determined by two main methods: calculation and experimental.

Calorimeters are used to carry out experimental calculations. First, a sample of fuel is burned in it. The heat that will be released is completely absorbed by the water. Having an idea of ​​the mass of water, you can determine by the change in its temperature the value of its heat of combustion.

This technique is considered simple and effective; it only requires knowledge of technical analysis data.

In the calculation method, the higher and lower calorific values ​​are calculated using the Mendeleev formula.

Q p H = 339C p +1030H p -109(O p -S p) - 25 W p (kJ/kg)

It takes into account the content of carbon, oxygen, hydrogen, water vapor, sulfur in the working composition (in percent). The amount of heat during combustion is determined taking into account the equivalent fuel.

The heat of combustion of gas allows preliminary calculations to be made and the effectiveness of using a certain type of fuel to be determined.

Features of origin

In order to understand how much heat is released when a certain fuel is burned, it is necessary to have an idea of ​​its origin.

In nature, there are different versions of solid fuels, which differ in composition and properties.

Its formation occurs through several stages. First peat is formed, then it becomes brown and coal, then anthracite is formed. The main sources of solid fuel formation are leaves, wood, and pine needles. When parts of plants die and are exposed to air, they are destroyed by fungi and form peat. Its accumulation turns into a brown mass, then brown gas is obtained.

At high blood pressure and temperature, brown gas turns into coal, then the fuel accumulates in the form of anthracite.

In addition to organic matter, the fuel contains additional ballast. Organic is considered to be that part that is formed from organic substances: hydrogen, carbon, nitrogen, oxygen. In addition to these chemical elements, it contains ballast: moisture, ash.

Combustion technology involves the separation of the working, dry, and combustible mass of burned fuel. The working mass is the fuel in its original form supplied to the consumer. Dry mass is a composition in which there is no water.

Compound

The most valuable components are carbon and hydrogen.

These elements are contained in any type of fuel. In peat and wood, the percentage of carbon reaches 58 percent, in hard and brown coal - 80%, and in anthracite it reaches 95 percent by weight. Depending on this indicator, the amount of heat released during fuel combustion changes. Hydrogen is the second most important element of any fuel. When it binds with oxygen, it forms moisture, which significantly reduces the thermal value of any fuel.

Its percentage ranges from 3.8 in oil shale to 11 in fuel oil. The oxygen contained in the fuel acts as ballast.

It is not heat generating chemical element, therefore negatively affects the value of its heat of combustion. The combustion of nitrogen, contained in free or bound form in combustion products, is considered harmful impurities, therefore its quantity is clearly limited.

Sulfur is included in fuel in the form of sulfates, sulfides, and also as sulfur dioxide gases. When hydrated, sulfur oxides form sulfuric acid, which destroys boiler equipment and negatively affects vegetation and living organisms.

That is why sulfur is a chemical element whose presence in natural fuel is extremely undesirable. If sulfur compounds get inside the work area, they cause significant poisoning of operating personnel.

There are three types of ash depending on its origin:

  • primary;
  • secondary;
  • tertiary

The primary species is formed from minerals found in plants. Secondary ash is formed as a result of plant residues entering sand and soil during formation.

Tertiary ash appears in the composition of fuel during extraction, storage, and transportation. With significant ash deposition, a decrease in heat transfer on the heating surface of the boiler unit occurs, reducing the amount of heat transfer to water from gases. A huge amount of ash negatively affects the operation of the boiler.

Finally

Volatile substances have a significant influence on the combustion process of any type of fuel. The greater their output, the larger the volume of the flame front will be. For example, coal and peat ignite easily, the process is accompanied by minor heat losses. The coke that remains after removing volatile impurities contains only mineral and carbon compounds. Depending on the characteristics of the fuel, the amount of heat changes significantly.

Depending on the chemical composition, there are three stages of solid fuel formation: peat, lignite, and coal.

Natural wood is used in small boiler installations. They mainly use wood chips, sawdust, slabs, bark, and the firewood itself is used in small quantities. Depending on the type of wood, the amount of heat generated varies significantly.

As the heat of combustion decreases, firewood acquires certain advantages: rapid flammability, minimal ash content, and the absence of traces of sulfur.

Reliable information about the composition of natural or synthetic fuel, its calorific value, is in a great way carrying out thermochemical calculations.

Currently, there is a real opportunity to identify those main options for solid, gaseous, liquid fuels that will be the most effective and inexpensive to use in a certain situation.

Chemical reactions are accompanied by the absorption or release of energy, in particular heat. reactions accompanied by the absorption of heat, as well as the compounds formed during this process, are called endothermic . In endothermic reactions, heating of the reacting substances is necessary not only for the occurrence of the reaction, but also during the entire time of their occurrence. Without external heating, the endothermic reaction stops.

reactions accompanied by the release of heat, as well as the compounds formed during this process, are called exothermic . All combustion reactions are exothermic. Due to the release of heat, they, having arisen at one point, are able to spread to the entire mass of reacting substances.

The amount of heat released during complete combustion of a substance and related to one mole, unit of mass (kg, g) or volume (m 3) of a combustible substance is called heat of combustion. The heat of combustion can be calculated from tabular data using Hess's law. Russian chemist G.G. Hess in 1840 discovered a law that is a special case of the law of conservation of energy. Hess's law is as follows: the thermal effect of a chemical transformation does not depend on the path along which the reaction occurs, but depends only on the initial and final states of the system, provided that the temperature and pressure (or volume) at the beginning and end of the reaction are the same.

Let's consider this using the example of calculating the heat of combustion of methane. Methane can be produced from 1 mole of carbon and 2 moles of hydrogen. When methane is burned, it produces 2 moles of water and 1 mole of carbon dioxide.

C + 2H 2 = CH 4 + 74.8 kJ (Q 1).

CH 4 + 2O 2 = CO 2 + 2H 2 O + Q horizon.

The same products are formed by the combustion of hydrogen and carbon. During these reactions, the total amount of heat released is 963.5 kJ.

2H 2 + O 2 = 2H 2 O + 570.6 kJ

C + O 2 = CO 2 + 392.9 kJ.

Since the initial and final products in both cases are the same, their total thermal effects must be equal according to Hess’s law, i.e.

Q 1 + Q mountains = Q,

Q mountains = Q - Q 1. (1.11)

Therefore, the heat of combustion of methane will be equal to

Q mountains = 963.5 - 74.8 = 888.7 kJ/mol.

Thus, the heat of combustion of a chemical compound (or their mixture) is equal to the difference between the sum of the heats of formation of combustion products and the heat of formation of the burned chemical compound (or substances that make up the combustible mixture). Therefore, to determine the heat of combustion of chemical compounds, it is necessary to know the heat of their formation and the heat of formation of the products obtained after combustion.

Below are the heats of formation of some chemical compounds:

Aluminum oxide Al 2 O 3 ………

Methane CH 4 …………………………

Iron oxide Fe 2 O 3 …………

Ethane C 2 H 6 ……………………

Carbon monoxide CO………….

Acetylene C 2 H 2 ………………

Carbon dioxide CO2………

Benzene C 6 H 6 …………………

Water H 2 O ………………………….

Ethylene C 2 H 4 …………………

Water vapor H 2 O ……………

Toluene C 6 H 5 CH 3 …………….

Example 1.5 .Determine the combustion temperature of ethane if the heat of its formationQ 1 = 88.4 kJ. Let's write the combustion equation for ethane.

C 2 H 6 + 3.5O 2 = 2 CO 2 + 3 H 2 O + Qmountains.

For determiningQmountainsit is necessary to know the heat of formation of combustion products. the heat of formation of carbon dioxide is 396.9 kJ, and that of water is 286.6 kJ. Hence,Qwill be equal

Q = 2 × 396,9 + 3 × 286.6 = 1653.6 kJ,

and the heat of combustion of ethane

Qmountains= Q - Q 1 = 1653.6 - 88.4 = 1565.2 kJ.

The heat of combustion is experimentally determined in a bomb calorimeter and a gas calorimeter. There are higher and lower calorific values. Higher calorific value Q in is the amount of heat released during the complete combustion of 1 kg or 1 m 3 of a combustible substance, provided that the hydrogen contained in it burns to form liquid water. Lower calorific value Qn is the amount of heat released during the complete combustion of 1 kg or 1 m 3 of a combustible substance, provided that hydrogen is burned until water vapor is formed and the moisture of the combustible substance is evaporated.

The higher and lower heats of combustion of solid and liquid combustible substances can be determined using the formulas of D.I. Mendeleev:

where Q in, Q n - higher and lower calorific values, kJ/kg; W – content of carbon, hydrogen, oxygen, combustible sulfur and moisture in the combustible substance, %.

Example 1.6. Define lowest temperature combustion of sulfur fuel oil, consisting of 82.5% C, 10.65% H, 3.1%Sand 0.5% O; A (ash) = 0.25%,W = 3%. Using the equation of D.I. Mendeleev (1.13), we obtain

=38622.7 kJ/kg

The lower calorific value of 1 m3 of dry gases can be determined by the equation

Lower heat combustion of some flammable gases and liquids, obtained experimentally, is given below:

Hydrocarbons:

methane………………………..

ethane …………………………

propane………………………

methyl………………….

ethyl…………………………

propyl………………………

The lower calorific value of some combustible materials, calculated from their elemental composition, has the following values:

Gasoline……………………

Synthetic rubber

Paper ……………………

Kerosene………………

Wood

Organic glass..

air-dry………..

Rubber ………………..

in building structures...

Peat ( W = 20 %) …….

There is a lower limit of calorific value, below which substances become incapable of combustion in the air atmosphere.


Experiments show that substances are non-flammable if they are not explosive and if their lower calorific value in air does not exceed 2100 kJ/kg. Consequently, the heat of combustion can serve as an approximate estimate of the flammability of substances. However, it should be noted that the flammability of solids and materials largely depends on their condition. Thus, a sheet of paper, easily ignited by the flame of a match, when applied to the smooth surface of a metal plate or concrete wall, becomes difficult to combust. Consequently, the flammability of substances also depends on the rate of heat removal from the combustion zone.

In practice, during the combustion process, especially in fires, the heat of combustion indicated in the tables is not completely released, since combustion is accompanied by underburning. It is known that petroleum products, as well as benzene, toluene, acetylene, i.e. substances rich

carbon, burn in fires with the formation of a significant amount of soot. Soot (carbon) can burn and produce heat. If it is formed during combustion, then, consequently, the combustible substance emits less heat than the amount indicated in the tables. For substances rich in carbon, the underburning coefficient h is 0.8 - 0.9. Consequently, in fires when burning 1 kg of rubber, not 33520 kJ can be released, but only 33520´0.8 = 26816 kJ.

Fire size is usually characterized by the area of ​​the fire. The amount of heat released per unit area of ​​fire per unit time is called heat of fire Q p

QP= Qnυ mh ,

Where υ m– mass burnout rate, kg/(m 2 ×s).

The specific heat of fire during internal fires characterizes the thermal load on the structures of buildings and structures and is used to calculate the fire temperature.

1.6. Combustion temperature

The heat released in the combustion zone is perceived by combustion products, so they heat up to high temperature. The temperature to which combustion products are heated during combustion is called combustion temperature . There are calorimetric, theoretical and actual combustion temperatures. The actual combustion temperature for fire conditions is called fire temperature.

The calorimetric combustion temperature is understood as the temperature to which the products of complete combustion are heated under the following conditions:

1) all the heat released during combustion is spent on heating the combustion products (heat loss is zero);

2) the initial temperatures of air and flammable substances are 0 0 C;

3) the amount of air is equal to the theoretically required (a = 1);

4) complete combustion occurs.

The calorimetric combustion temperature depends only on the composition of the combustible substance and does not depend on its quantity.

Theoretical temperature, in contrast to calorimetric temperature, characterizes combustion taking into account the endothermic process of dissociation of combustion products at high temperature

2СО 2 2СО + О 2 - 566.5 kJ.

2H 2 O2H 2 + O 2 - 478.5 kJ.

In practice, the dissociation of combustion products must be taken into account only at temperatures above 1700 0 C. During diffusion combustion of substances in fire conditions, the actual combustion temperatures do not reach such values, therefore, to assess fire conditions, only the calorimetric combustion temperature and the fire temperature are used. There is a distinction between internal and external fire temperatures. The internal fire temperature is the average temperature of the smoke in the room where the fire occurs. External fire temperature – flame temperature.

When calculating the calorimetric combustion temperature and the internal fire temperature, it is assumed that the lower heat of combustion Qn of a combustible substance is equal to the energy qg required to heat the combustion products from 0 0 C to the calorimetric combustion temperature

, - heat capacity of the components of combustion products (heat capacity of CO 2 is taken for a mixture of CO 2 and SO 2), kJ/(m 3 ? K).

In fact, not all the heat released during combustion under fire conditions is spent on heating the combustion products. Most of it is spent on heating structures, preparing flammable substances for combustion, heating excess air, etc. Therefore, the temperature of an internal fire is significantly lower than the calorimetric temperature. The combustion temperature calculation method assumes that the entire volume of combustion products is heated to the same temperature. In reality, the temperature at different points of the combustion center is not the same. The highest temperature is in the region of space where the combustion reaction occurs, i.e. in the combustion (flame) zone. The temperature is significantly lower in places where there are flammable vapors and gases released from the burning substance and combustion products mixed with excess air.

In order to judge the nature of temperature changes during a fire depending on various combustion conditions, the concept of average volumetric fire temperature was introduced, which is understood as the average value of the temperatures measured by thermometers at various points of the internal fire. This temperature is determined from experience.

Types of calorific value

The heat of combustion can be related to the working mass of the combustible substance, that is, to the combustible substance in the form in which it reaches the consumer; to the dry mass of the substance; to a combustible mass of a substance, that is, to a combustible substance that does not contain moisture and ash.

There are higher () and lower () calorific values.

Under higher calorific value understand the amount of heat that is released during complete combustion of a substance, including the heat of condensation of water vapor when cooling the combustion products.

Net calorific value corresponds to the amount of heat that is released during complete combustion, without taking into account the heat of condensation of water vapor. The heat of condensation of water vapor is also called latent heat of combustion.

The lower and higher calorific values ​​are related by the relation: ,

where k is a coefficient equal to 25 kJ/kg (6 kcal/kg); W is the amount of water in the flammable substance, % (by mass); H is the amount of hydrogen in a combustible substance, % (by mass).

Calculation of calorific value

Thus, the higher calorific value is the amount of heat released during complete combustion of a unit mass or volume (for gas) of a combustible substance and cooling of the combustion products to the dew point temperature. In thermal engineering calculations, the higher calorific value is taken as 100%. The latent heat of combustion of a gas is the heat that is released during the condensation of water vapor contained in the combustion products. Theoretically, it can reach 11%.

In practice, it is not possible to cool the combustion products until complete condensation, and therefore the concept of lower calorific value (QHp) has been introduced, which is obtained by subtracting from the higher calorific value the heat of vaporization of water vapor both contained in the substance and those formed during its combustion. The vaporization of 1 kg of water vapor requires 2514 kJ/kg (600 kcal/kg). The lower calorific value is determined by the formulas (kJ/kg or kcal/kg):

(for solid matter)

(for a liquid substance), where:

2514 - heat of vaporization at a temperature of 0 °C and atmospheric pressure, kJ/kg;

I is the content of hydrogen and water vapor in the working fuel, %;

9 is a coefficient showing that the combustion of 1 kg of hydrogen in combination with oxygen produces 9 kg of water.

Heat of combustion is the most important characteristic of a fuel, as it determines the amount of heat obtained by burning 1 kg of solid or liquid fuel or 1 m³ of gaseous fuel in kJ/kg (kcal/kg). 1 kcal = 4.1868 or 4.19 kJ.

The lower calorific value is determined experimentally for each substance and is a reference value. It can also be determined for solid and liquid materials, with a known elemental composition, by calculation in accordance with the formula of D. I. Mendeleev, kJ/kg or kcal/kg:

The content of carbon, hydrogen, oxygen, volatile sulfur and moisture in the working mass of fuel in% (by weight).

For comparative calculations, the so-called conventional fuel is used, which has a specific heat of combustion equal to 29308 kJ/kg (7000 kcal/kg).

In Russia thermal calculations(for example, calculating the heat load to determine the category of a room for explosion and fire hazard) is usually carried out according to the lower calorific value, in the USA, Great Britain, France - according to the highest. In the UK and US, before the introduction of the metric system, specific heating value was measured in British thermal units (BTU) per pound (lb) (1Btu/lb = 2.326 kJ/kg).

The highest values ​​of heating value of natural gases from various sources

These data were obtained from the International Energy Agency.

  • Algeria: 42,000 kJ/m³
  • Bangladesh: 36,000 kJ/m³
  • Canada: 38,200 kJ/m³
  • Indonesia: 40,600 kJ/m³
  • Netherlands: 33,320 kJ/m³
  • Norway: 39,877 kJ/m³
  • Russia: 38,231 kJ/m³
  • Saudi Arabia: 38,000 kJ/m³
  • UK: 39,710 kJ/m³
  • United States: 38,416 kJ/m³
  • Uzbekistan: 37,889 kJ/m³
  • Belarus: 33,000 kJ/m³

The required amount of fuel to operate a 100 W light bulb for a year (876 kWh)

(The fuel quantities shown below are based on 100% heat-to-electricity conversion efficiency. Since most power generating plants and distribution systems achieve efficiencies of about 30% - 35%, the actual amount of fuel used to power a 100 W light bulb is will be approximately three times the specified amount).

  • 260 kg wood (at 20% humidity)
  • 120 kg of coal (low ash anthracite)
  • 73.34 kg kerosene
  • 78.8 m³ natural gas (using an average value of 40,000 kJ/m³)
  • 17.5 µg antimatter

Notes

Literature

  • Physical encyclopedic dictionary
  • Great Soviet Encyclopedia
  • Manual for NPB 105-03

see also


Wikimedia Foundation. 2010.

5. Categories of buildings according to explosion and fire hazard

5.1. A building belongs to category A if the total area of ​​category A premises in it exceeds 5% of the area of ​​all premises or 200 m 2.

It is allowed not to classify a building as category A if the total area of ​​category A premises in the building does not exceed 25% of the total area of ​​all premises located in it (but not more than 1000 m2), and these premises are equipped with automatic fire extinguishing installations.

5.2. A building belongs to category B if two conditions are simultaneously met:

a) the building does not belong to category A;

b) the total area of ​​premises of categories A and B exceeds 5% of the total area of ​​all premises or 200 m2.

It is allowed not to classify a building as category B if the total area of ​​premises of categories A and B in the building does not exceed 25% of the total area of ​​all premises located in it (but not more than 1000 m2), and these premises are equipped with automatic fire extinguishing installations.

b) the total area of ​​premises of categories A, B and B1-B3 exceeds 5% (10% if the building does not have premises of categories A and B) of the total area of ​​all premises.

It is allowed not to classify a building as categories B1-B3 if the total area of ​​premises of categories A, B and B1-C3 in the building does not exceed 25% of the total area of ​​all premises located in it (but not more than 3500 m2), and these premises are equipped with automatic fire extinguishing

5.4. A building belongs to category G if two conditions are simultaneously met:

b) the total area of ​​premises of categories A, B, B1-B3 and D exceeds 5% of the total area of ​​all premises.

It is allowed not to classify a building as category D if the total area of ​​premises of categories A, B, B1-C3 and D in the building does not exceed 25% of the total area of ​​​​all premises located in it (but not more than 5000 m2), and premises of categories A, B and B1-B3 are equipped with automatic fire extinguishing installations.

5.5. A building belongs to category B4 if it does not belong to categories A, B, B1-B3 or D.

5.6. A building belongs to category D if it does not belong to categories A, B, B1-B4, D.

Annex 1

Initial data for calculating the specific temporary fire load in premises

Table 1

Lower calorific value and density of THM, flammable liquid and gas liquid,

circulating in the premises of railway transport facilities

Name of substances and materials

Lower calorific value, MJ kg -1

Density,

Liquid flammable substances and materials

4. Butyl alcohol

5. Diesel fuel

6. Kerosene

8. Insulating impregnating varnish (BT-99, FL-98) (volatile content - 48%)

10. Industrial oil

11. Transformer oil

12. Turbine oil

13. Methyl alcohol

15. Solar oil

16. Toluene

17. White spirit

18. Enamel PF-115 (volatile content - 34%)

19. Ethyl alcohol

20. Glue (rubber)

Solid flammable substances and materials

21. Paper loosened

22. Paper (books, magazines)

23. Vinyl leather

24. Staple fiber

25. Construction felt

26. Pine wood ( W p = 20%)

27. Fiberboard (Fibreboard)

28. Chipboard (chipboard)

30. Carbolite products

31. Natural rubber

32. Synthetic rubber

33. Cable (power, lighting, control, automation)

34. Gray cardboard

35. Triacetate film

36. PVC linoleum

37. Flax loosened

38. Mipora (porous rubber)

39. Organic glass

40. Wiping material

41. Joiner's plate

42. Polyurethane foam

43. Polystyrene foam boards

44. Rubber

45. Fiberglass

46. ​​Cotton fabric (in bulk)

47. Wool fabric (in bulk)

48. Plywood

49. Rubber and polyvinyl chloride insulation of wires