- 1 To download the below and all other Useful Books and calculations Excel sheets please click here
- 2 To download the below and all other Useful Books and calculations Excel sheets please click here
- 3 Calculation of raw mix composition
- 3.1 Alligation alternate method
- 3.2 Calculation based on the hydraulic module
- 3.3 Calculation based on lime saturation factor
- 3.4 Calculation with lime saturation factor and silica ratio
- 3.5 Calculation of the quantity of coal ash absorbed by the clinker
- 3.6 Calculation with four raw material components
- 3.7 Raw mix calculation to find the required amount of potential clinker compounds
- 3.8 Oxide contents and potential composition
- 3.9 Download Link
Calculation of raw mix composition
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The purpose of calculating the composition of the raw mix is to determine the quantitative proportions of the raw components, in order to give the clinker the desired chemical and mineralogical composition. For this, there are many methods of calculation; from the most simple to the more complicated ones. The basis for calculation is the chemical composition of the raw materials. Generally, data of chemical analyses should be accurate to two decimals. Results of analyses in excess of 100 %, should be arithmetically reduced to 100 %, each constituent being proportion ally reduced. If on the other hand the total of the constituents is less than 100, the constituents are not pro portionally increased to 100; in this case the difference from 100 is denoted as “rest”, so that the total of all constituents is then 100.
Alligation alternate method
The simplest course of calculation for solving blending problems is known as alligation alternate; this method allows the determination of the proportion of two raw material components. In this case, only the required lime content is fixed as a setpoint, so that the proportion of both components can be determined.
What mixing proportion is required for limestone with 91 % CaC03, and clay with 31 % CaC03, to get a raw mix with a CaC03 content of 76 %? According to alligation alternate, the procedure is as follows:
To get a raw mix with a CaC03 content of 76 %, 45 parts of limestone should be mixed with 15 parts of clay. Thus the proportion of the components in the raw mix, i. e. limestone : clay = 45 : 15, or 3 : 1.
Calculation based on the hydraulic module
This method is applicable to two raw material components, with the hydraulic module selected for the clinker [15, 16]. To simplify the following calculations, symbols are used for the designation of the clinker components, the raw materials, and the coal ash; these symbols are placed in table 2.1.
Applying these symbols, the hydraulic moduli for clinker and raw mix will be:
Since both moduli are of the same value, one can equate:
According to this method of calculation it is assumed that x parts of the first raw material are apportioned to one part of the second raw material. Under this assumption, the quantities of the particular raw material components can be calculated by using the following formulas:
Inserting the values Cm, Sm. Am and Fm into the formula for the hydraulic module, we get
Since the oxide ·components are known from the chemical analysis of the raw materials, and the hydraulic module is selected according to the quality requirements, the only remaining unknown is x. After transformation of the above formula, to calcu late the value for x, the following formula appears:
Two raw materials are given with the following com position (see column 1 and 2 of table 2.2.)
Calculate the composition of the raw mix, assuming a hydraulic module of HM = 2.2. Solution:
i.e. to get a clinker with a HM = 2.2, we have to mix 3.324 parts limestone with one part of marl.
Thus the raw mix consists of:
76.87 % limestone, and
In table 2.2. the calculated raw mix components appear in column 3 and 4, and the composition of the
raw mix is given in column 5 (columns 3 + 4 =column 5). Column 6 contains the calculated clinker
composition as raw mix of column 5, free of loss on ignition. From column 6 we obtain the value for the
hydraulic module HM = 2.2.
Calculation based on lime saturation factor
Given are 2 raw materials (see table 2.3., column 1 and 2); Kind’s lime saturation module is:
Inserting into Kind’s formula the calculation symbols used previously, we get:
and solving for x:
With this formula we calculate how many parts of limestone in the raw mix are apportioned to one part of clay. Accordingly we get:
Thus 4.053 parts limestone are apportioned to one part of clay, and the raw mix consists of
80.20 % limestone, and 19.80 % clay.
Columns 3, 4, 5, and 6, of table 2.3. contain the calcu lated parts of components, as well as the raw mix and clinker composition. The resulting lime saturation factor is:
This proves the accuracy of the calculation.
Calculation with lime saturation factor and silica ratio
Calculation of a raw mix by. the aid of three raw materials; the required Kind’s lime saturation factor is 0.92, and the required silica ratio is 2.70. The analy ses of raw materials are shown in column 1, 2 and 3, of table 2.4.
The formula for Kind’s lime saturation factor was already outlined in example 2.3. Applying the sym bols used previously, the formula for the silica ratio reads:
The calculation is performed under the assumption that x parts by weight of limestone (component 1), and y parts by weight of clay (component 2), are apportioned to one part by weight of pyrites cinders (component 3). Then the following formulas apply to the oxide components of the raw mix :
Inserting the above expressions into the formula for the lime saturation factor, and into the formula for the silica ratio, we get two equations with two unknowns x and y; and after transformation we get:
For a better review, the following additional abbreviations or symbols are applied:
When employing these symbols, the equations quoted above will take the following form:
After solution of these equations, we get the values for x andy
To calculate the alumina ratio instead of the silica ratio, i. e. to calculate the lime saturation factor and the alumina ratio, a2, b2, and c2, will take the following values (a1, b1, and c1, remain unchanged):
To calculate the parts of limestone x, and of clay y, which are apportioned to one part of pyrites cinders, the above developed formulas for x and y should be used.
First the values for a1, b1, c1, as well as for a2, bz, and c2, must be calculated.
Now, the resulting values are inserted into the formu las for x and y:
The result is that 53.03 parts of limestone and 13.69 parts of clay are apportioned to 1 part of pyrites cinders, or that the raw mix will consist in percent of:
The calculated figures of columns 4, 5, 6, 7, and 8, of the table 2.4., prove the correctness of the method of calculation.
Calculation of a raw mix consisting of three compo nents: limestone, blast furnace slag, and pyrites cin ders. The required lime saturation factor is 0.90 and the silica ratio 2.5. The analyses of the raw materials are shown in columns 1, 2, and 3 of table 2.5.; columns 4, 5, 6, 7, and 8, of this table contain the calculated results.
The course of calculation is the same as for example 2.4.
The figures in columns 4, 5, 6, 7, and 8, of table 2.5., prove the correctness of the calculation.
There is no absorption of fuel ash by the clinker, when using natural gas or fuel oil for clinker burning. On the contrary, when using coal, the matter of coal ash absorption by the clinker should be taken into account.
In modern long rotary kilns as well as in preheater kilns, i. e. in all kilns where dust losses are almost eli minated, the ash absorption by the clinker is total. Short rotary kilns with high dust losses, show a low degree of ash absorption. Generally, the ash absorp tion rate by the clinker in rotary kilns is in the range from 30 to 100 %, depending upon the kiln type. Shaft kilns for clinker burning always show an ash absorp tion rate of 100 %. For a certain kiln type, the ash absorption rate is constant.
The ash absorption rate can be calculated by using the analyses of the raw mix, the clinker, and the coal ash. The symbols for the particular components and oxides are the same as specified above. The rate of ash – absorption in per cent of the clinker weight is denoted by q; then we get the following equations :
Solving these equations for q, we get the following expressions:
The arithmetical mean of q1 to q4 produces the desired value for q. The raw mix being specified as free of loss on ignition, the chemical analyses of the raw mix, the clinker and the coal ash are shown in table 2.6.
and the arithmetic mean
That is to say that the quantity of coal ash absorbed by the clinker during the burning process is 3.47% of the clinker weight.
Here, another method is presented to calculate the influence of the coal ash on the chemical composition of clinker.
The chemical composition of the coal ash is:
The composition of the clinker is:
The clinker composition without coal ash is:
It is assumed that the coal rate is 19 % of the clinker weight; the ash content of the coal is 12 %, and the ash absorption rate is 100 %. Then the ash components in the clinker are:
The corrected clinker composition is shown in table 2.7.
The modules of the ignited raw mix (column 5, of table 2.7.), are:
These moduli allow calculation of proportioning of a raw mix which consists of two or more components, using the proper calculation method applicable for multicomponent raw mixes. Clinker burned from raw mix which was calculated as shown, will then have the composition as specified in column 2 of table 2.7.
Calculate a raw mix consisting of two components, limestone and clay, considering the influence of the coal ash on the composition of the clinker; the lime saturation factor KSK (according to Kind), is assumed to be 0.90.
The chemical composition of these three raw material components is as shown in columns 2, 3, and 4, of table 2.8. .
The coal consumption is 35 % referred to the clinker weight; the ash content of the coal is 16.4 %; and the ash absorbed by the clinker is 65 %. Then the amount of ash embodied in the clinker comes to
Now, the values for at, bt, Ct, and for a2, b2, c2, are cal culated.
For this calculation it is assumed that x parts of lime stone, plus y parts of clay (ignition free) plus q parts of ash amount to 100 parts of clinker. Thus:
X+ y + q = 100
Applying the symbols shown in table 2.1., the oxides in the clinker can be expressed by the following equations:
If the above values are inserted into the lime satura tion factor for the clinker, then we get the following equation with 2 unknowns:
The equation can be expressed in the following form
When using the following abbreviations, we get:
To calculate x and y, the following two equations should be solved:
To get formulas similar to that wich were used in the previous calculations, the following abbreviations should be applied for the second equation:
The solution of the following two equations
Now, the example is calculated as follows:
Inserting the above values into the formulas for x and y, we get after conversion:
From the calculation results that 71.39 % limestone (ignited), 24.88 0/o clay (ignited), and 3.73 0/o coal ash participated in the clinker formation.
The computed chemical composition of the clinker is shown in columns 5, 6, 7, and 8, of table 2.8. As is shown by the calculation, the lime saturation factor is 0.90, i. e. as much as assumed for the calculation. This demonstrates the correctness of the calculation. For the practical completion of the proportioning of the raw materials, it is required to convert them to the unignited basis. This is performed as follows:
Calculation with four raw material components
The following example contains formulas to calculate a raw mix consisting of four raw material components, with selected values for the lime saturation factor, the silica ratio and the alumina ratio.
It is assumed that the ratio of the raw material com ponents is:1.component : 2. component : 3. component : 4. com ponent = x : y : z : 1; then the oxide formulas are inserted into the formulas for the lime saturation fac tor, the silica ratio, and the alumina ratio. The result ing three equations are then converted into the sim plified form of three linear equations with three un knowns; consequently we get:
where for reasons of simplification the following notation is used
After solving the above equations for x, y, and z, we get the following formulas for the computation of a raw mix composed of four raw material components :
The following demonstrates a calculation for the determination of the proportions of the raw material components to be used for producing a clinker of a required potential composition of minerals.
Given are two kinds of raw materials, limestone and clay, the chemical composition of which is shown in table 2.9., column 1, and 2. Columns 3, 4, 5, and 6, con tain the calculated composition of the clinker and the potential phase composition. Using the formulas in section 1.6. the four main minerals of the two raw materials, i.e. limestone and clay (ignition free), can be calculated. Table 2.10. contains the computed com position of the clinker minerals. The next step is to mix the limestone and clay in such a ratio that the blend of both components will result in the required content of tricalcium silicate, C3S, of 60% .
be calculated. Table 2.10. contains the computed composition of the clinker minerals. The next step is to mix the limestone and clay in such a ratio that the blend of both components will result in the required content of tricalcium silicate, C3S, of 60% .
This ratio is found with the help of the following formula:
In the formula x is the part of the second component (clay); A is the percentage of the desired mineral in component No.1 (limestone), B is the percentage of this mineral in component No.2 (clay), and R is the percentage of this mineral in the blend of these two components. Table 2.11. contains the calculated parts by weight of limestone and clay, which when blended, produce a raw mix or clinker with the required content of 60% C3S. For this mixture, it may be seen that 68.59 % limestone, and 31.41 % clay are necessary.
Calculation of a raw mix consisting of three components (limestone, clay, and sand), with specified con tents of tricalcium silicate, and dicalcium silicate.
For this, the calculation with determinants may be applied.
Columns 1, 2, and 3, of table 2.12., show the composi tion of the raw materials. The required raw mix should contain 50 0/o C3S, and 25 0/o C2S.
The calculated potential mineral composition of the three components is shown in table 2.13.
To solve this problem, we first assemble three linear equations as in example 2.9.:
and solve for x, y, and z, using third-order determinants [26, 5]:
As is well known, the solution involves multiplication of three elements located on a diagonal, as shown here schematically. For clarity, the first two columns are extended by repeating them on the right side.
As is known, if we multiply downwards, the products are added; and if we multiply upwards, the products are subtracted, as follows:
Now, we insert into the equations the required amount of minerals of the components
The value for z is being found by difference:
The percentages of the three components are (ignition free).
The calculated composition of the clinker as well as the conventionally calculated content of clinker minerals in round figures, are shown in columns 4, 5, 6, 7, and 8, of table 2.12.
Suppose that instead of 50 0/o C3S we insert into the above calculation, values of 25 % C3S, and 50 0/o C2S; we then get the following percentages of raw material components (ignition free):
Oxide contents and potential composition
The above calculation shows that small quantity fluctuations in the proportioning of the raw components, with their resultant small differences in the oxide contents, cause large fluctuations in the potential phase composition of the clinker and consequently,as in this case, the reduction of C3S-content by 50%, and an increase in C2S-content of 100 %. This is also shown in the following tabulated compilation of three different clinkers with small differences in the oxide contents, and the resulting large fluctuations in the calculated phase composition (see table 2.16.) .
Table 2.16. contains chemical compositions of three different clinkers. The oxide contents do not vary widely; but the calculated potential compositions show considerable differences. Therefore, when cal culating the composition of the raw mix, it should be taken into consideration that a variation of 1 % in the CaO-content causes a variation in the tricalcium sili cate content by about 10-14% and, vice versa, a fluctuation in the C3S-content by 1 %, causes a cor responding increase or decrease in the CaO-content by 1/14 = 0.07 %, or a change in the CaCOTcontent of the raw mix by 0.07 x 1.78 = 0.12 %. If the CaO content is kept constant and the values for the other oxides change, there is a corresponding change in contents of the resulting clinker minerals.
Also one and the same clinker can show different cal culated potential compound compositions, when on the one hand, one calculates with only the four main oxides, and on the other hand when including also the auxiliary components which participate in the formation of minerals. For a numerical presentation of this fact, the following clinker analysis may be used for calculation .
The calculated potential composition is:
Considering the mineral formation as quoted above, the potential clinker composition is:
A comparison of the two results shows wide differ ences in the potential composition of the same clinker. Also the ratio c3s : c2s has changed and is roughly 1 : 1, according to the second method of cal culation. Differences in potential composition are the result of differences in the mineral formations used for the calculation.