Авторы

  • ойбек Микхлиев
    Karshi State Technical University
  • Баходир Шамаев
    Termez State University of Engineering and Agrotechnology
  • Елнур Хушвактов
    Karshi State Technical University

DOI:

https://doi.org/10.71337/inlibrary.uz.imjrd.135060

Ключевые слова:

Foam density Foam density PAA – gel PAA – gel Structol SB-2195 Structol SB-2195 blue ribbon-TU blue ribbon-TU SFM. SFM.

Аннотация

The foam height and foam density formed during the decomposition of local dolomite raw materials in the presence of sulfuric acid under optimal conditions were determined, and methods and optimal conditions for reducing foam density were studied using “PAA-gel” and “Structol SB-2195” as antifoaming reagents.

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INTERNATIONAL MULTIDISCIPLINARY JOURNAL FOR

RESEARCH & DEVELOPMENT

SJIF 2019: 5.222 2020: 5.552 2021: 5.637 2022:5.479 2023:6.563 2024: 7,805

eISSN :2394-6334 https://www.ijmrd.in/index.php/imjrd Volume 12, issue 08 (2025)

276

STUDY OF THE SEPARATION PROCESS OF THE DOLOMITE SOIL FORMED

DURING THE DISSOLVING OF DOLOMITE WITH SULFURIC ACID INTO LIQUID

AND SOLID PHASES

Mixliyev Oybek Avloyorovich

Karshi State Technical University

Shamayev Baxodir Ergashevich

Termez State University of Engineering and Agrotechnology

Xushvaqtov Elnur Iskandar ugli

Karshi State Technical University

Abstract:

The foam height and foam density formed during the decomposition of local

dolomite raw materials in the presence of sulfuric acid under optimal conditions were

determined, and methods and optimal conditions for reducing foam density were studied using

“PAA-gel” and “Structol SB-2195” as antifoaming reagents.

Keywords:

Foam density, PAA – gel, Structol SB-2195, blue ribbon-TU, SFM.

In order to accelerate the process of sulfuric acid decomposition of local dolomite raw materials

and establish optimal conditions and technological parameters for its processing into liquid and

crystalline MgSO

4

, (NH

4

)

2

Mg(SO

4

)

2

, (NH

4

)

2

Mg(SO

4

)

2

·6H

2

O and liquid and granular nitrogen

calcium and magnesium fertilizers, as well as to carry out scientific research in laboratory

conditions, dolomite raw materials were imported from Dehqanabad district, Kashkadarya

region. The filtration rate of the sour slurry obtained from the decomposition of the selected

dolomite sample with sulfuric acid with a concentration of 20 to 40%, standard 110%, was

determined by slurry, liquid and solid phases, and the results obtained are presented in this table

[1].

The effects of surfactants (PAA - gel and Structol SB-2195) and acid concentrations on the

filtration rate of the slurry formed by the processing of dolomite raw materials with sulfuric

acid at acid concentrations of 20, 30 and 40%, standard 110%, solid:liquid phase ratios of 1:3.5,

1:2.8, 1:2.3, 1:2.0 and 1:1.8 and a temperature of 50 °C were determined. Technological

parameters for the filtration of sour slurry obtained from the processing of dolomite with

sulfuric acid, at a temperature of 50 °C and a pressure of 0.06 MPa or 450 mm.cm.st., the

effects of 10, 20 and 30 g/ton of PAA - gel and Struktol SB-2195 surfactants on the filtration

process on filter paper of the blue ribbon-TU 2642-001-05015242-07 brand were determined.

In this case, it was determined that the filtration rate of the slurry obtained by disintegrating the

dolomite raw material with sulfuric acid with a concentration of 20% was 2025.50 kg/m2·s for

the slurry without surfactants, 1418.30 kg/m2·s for the filtrate (sour liquid phase), 607.20

kg/m2·s for the solid phase and 162.80 kg/m²·s for the sum of the amounts of CaO+MgO.

When we added PAA-gel and Structol SB-2195 surfactants in the amount of 10-30 g/t to the

process of dolomite decomposition in 20% H

2

SO

4

(10 SFM added to 1 ton of dolomite raw

material), the filtration rate of the slurry increased from 3066.40 to 3355.40 kg/m³·s and

3152.50 to 3194.00 kg/m²·s for the slurry, from 2330.55 to 2550.20 kg/m²·s and 2404.80 to

2434.90 kg/m²·s for the filtrate (sour liquid phase), from 735.85 to 805.20 kg/m²·s and 747.70

to 797.35 kg/m²·s for the solid phase. and the sum of CaO+MgO increased from 246.65 to

269.70 kg/m²·s and from 253.40 to 256.70 kg/m²·s, respectively. The filtration rate of the slurry,

which was decomposed with 30% sulfuric acid, was 2184.00 kg/m2·s for the slurry without


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INTERNATIONAL MULTIDISCIPLINARY JOURNAL FOR

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eISSN :2394-6334 https://www.ijmrd.in/index.php/imjrd Volume 12, issue 08 (2025)

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surfactants, 1386.65 kg/m²·s for the filtrate (sour liquid phase), 797.35 kg/m²·s for the solid

phase, and 222.20 kg/m²·s for the sum of CaO+MgO.

Table 1.

The effect of surfactants on the filtration rate of slurry obtained from the decomposition of

dolomite with sulfuric acid (N=110%; t=50 °С and τ=40 min)

Const.

H

2

SO

4

%

Surfactant,

gr/ton

Porridge filtration rate, kg/m

2

·s

(0,06 MPа)
Bo‘tqa

bo‘yicha

Fil‘trat

(nordon

suyuq

faza)

bo‘yicha

Qattiq faza

bo‘yicha

CaO+MgO

bo‘yicha

20

0

2025,50

1418,30

607,20

162,80

PAA-gel

10

3066,40

2330,55

735,85

246,50

20

3210,90

2440,38

770,52

258,10

30

3355,40

2550,20

805,20

269,70

“Struktol SB 2195”

10

3152,50

2404,80

747,70

253,40

20

3173,25

2419,85

753,40

255,05

30

3194,00

2434,90

759,10

256,70

30

0

2184,00

1386,65

797,35

222,20

PAA-gel

10

2712,00

1672,17

1039,83

276,89

20

3229,30

1917,72

1311,58

332,71

30

3746,60

2163,27

1583,33

388,52

“Struktol SB 2195”

10

2861,96

1806,83

1055,13

292,15

20

2936,11

1844,34

1091,77

299,75

30

3010,25

1881,84

1128,41

307,34

40

0

2342,50

1355,00

987,50

327,95

PAA-gel

10

2357,60

1013,80

1343,80

330,06

20

3328,40

1452,73

1875,67

465,97

30

4299,20

1891,65

2407,55

601,88

“Struktol SB 2195”

10

2571,43

1208,87

1362,56

360,00

20

2698,97

1268,83

1430,14

377,85

30

2826,51

1328,78

1497,73

395,70

When we added PAA-gel and Structol SB-2195 surfactants in the process of dolomite

decomposition at 30% H

2

SO

4

in an amount of 10 - 30 g/t (10 SFM added to 1 ton of dolomite

raw material), the filtration rate of the slurry increased from 2712.00 to 3746.60 kg/m³·s and

2861.96 to 3010.25 kg/m²·s for the slurry, from 1672.17 to 2163.27 kg/m²·s and 1806.83 to

1881.84 kg/m²·s for the filtrate (sour liquid phase), from 1039.83 to 1583.33 kg/m²·s and


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1055/13 to 1128.41 kg/m²·s for the solid phase. It was also found that the sum of the

CaO+MgO amounts increased from 276.89 to 388.52 kg/m²·s and from 292.15 to 307.34

kg/m²·s, and the filtration rate of the slurry, which was crushed with 40% sulfuric acid

concentration of dolomite raw material, was 2342.50 kg/m²·s for the slurry without surfactants,

1355.00 kg/m²·s for the filtrate (sour liquid phase), 987.50 kg/m²·s for the solid phase, and

327.95 kg/m²·s for the sum of the CaO+MgO amounts. When we added PAA ‒ gel and

Structol SB-2195 surfactants in the process of dolomite decomposition in 40% H

2

SO

4

in an

amount of 10 - 30 g/t (10 SFM added to 1 ton of dolomite raw material), the filtration rate of

the slurry increased from 2357.60 to 4299.20 kg/m³·s and 2571.43 to 2826.51 kg/m²·s for the

slurry, from 1013.80 to 1891.65 kg/m²·s and 1208.87 to 1328.78 kg/m²·s for the filtrate (sour

liquid phase), from 1343.80 to 2407.55 kg/m²·s and 1362.56 to 1497.73 kg/m²·s for the solid

phase. and the sum of CaO+MgO amounts increased from 330.06 to 601.88 kg/m²·s and from

360.00 to 395.70 kg/m²·s. The experimental analyses conducted in the experimental model

device under laboratory conditions and the results obtained are presented in the table [2.3].

Thus, it was found that when decomposing the Dehqanabad mine dolomite raw material with

20% H

2

SO

4

, the filtration rate increased by 1.51 - 1.66 times and 1.55 - 1.58 times in slurry

compared to 10-30 g/ton of surfactants "PAA-gel" and "Structol SB 2195", while at 30% H

2

SO

4

,

the filtration rate increased by 1.24 - 1.72 times and 1.31 - 1.38 times in slurry. It was found

that the filtration rate increased by 1.01 - 1.83 times for porridge and 1.10 - 1.21 times for 40%

H

2

SO

4

.

References

1. O.A.Mixliyev.,X.Ch.Mirzaqulov.,R.Ch.Yorboboyev.,Sh.M.Olmurova.. The study of

rheological properties of dolomite raw materials during the processing of sulfuric acid into

magnesium sulfate and gypsum. Innovative developments and Research in education

International scientific-online conference. Part 28.April 23rd. Colletions Of Scientific Works.

Canada 2024 yil. с. 470-472.

2. O.A.Mixliyev., X.Ch.Mirzaqulov., R.Ch.Yorboboyev. Investigation of the foaming process

during decomposition of local dolomite gaiters and in sulfuric acid. Ethiopian in international

journal of multidisciplinary research. May. Hindiston-2024 yil. - c. 610-611.

3.

O.A.Mixliyev., X.Ch.Mirzaqulov.,

R.Ch.Yorboboyev. Dehqonobod koni dolomit

xomashyosi nitrat va sulfat kislota. bilan parchalanish jarayonida ko‘piklanish jarayonini

o‘rganish. Ilm fan xabarnomasi. Ilmiy elektron jurnal. 2-tom. Andijon-2024-yil. - с.462-464.

Библиографические ссылки

O.A.Mixliyev.,X.Ch.Mirzaqulov.,R.Ch.Yorboboyev.,Sh.M.Olmurova.. The study of rheological properties of dolomite raw materials during the processing of sulfuric acid into magnesium sulfate and gypsum. Innovative developments and Research in education International scientific-online conference. Part 28.April 23rd. Colletions Of Scientific Works. Canada 2024 yil. с. 470-472.

O.A.Mixliyev., X.Ch.Mirzaqulov., R.Ch.Yorboboyev. Investigation of the foaming process during decomposition of local dolomite gaiters and in sulfuric acid. Ethiopian in international journal of multidisciplinary research. May. Hindiston-2024 yil. - c. 610-611.

O.A.Mixliyev., X.Ch.Mirzaqulov., R.Ch.Yorboboyev. Dehqonobod koni dolomit xomashyosi nitrat va sulfat kislota. bilan parchalanish jarayonida ko‘piklanish jarayonini o‘rganish. Ilm fan xabarnomasi. Ilmiy elektron jurnal. 2-tom. Andijon-2024-yil. - с.462-464.