Authors

  • Khusan Nematov
    PhD, Karshi engineering-economics institute

DOI:

https://doi.org/10.71337/inlibrary.uz.aijmr.63248

Keywords:

Absorption drying adsorption drying condensation membrane method synthetic zeolite corrosion resistance.

Abstract

Currently, it is considered important to select adsorbents with high efficiency in drying gases. For this purpose, the following works are being carried out: physical and chemical parameters of  NaA (3Å) synthetic zeolite, physical and chemical properties of 3 types of KA (3Å) zeolite were reviewed. and other information is given in the article.


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Acumen:

International Journal of

Multidisciplinary Research

Volume 1, Issue 1

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Acumen: International Journal of Multidisciplinary Research

SELECTION OF ADSORBENTS WITH HIGH EFFICIENCY IN DRYING

GASES AND STUDY OF THEIR PHYSICO-CHEMICAL PROPERTIES

Nematov Khusan Ibodullayevich

PhD, Karshi engineering-economics institute

xusan85nematov@gmail.com

ВЫБОР АДСОРБЕНТОВ С ВЫСОКОЙ ЭФФЕКТИВНОСТЬЮ

ПРИ СУШКЕ ГАЗОВ И ИЗУЧЕНИЕ ИХ ФИЗИКО-ХИМИЧЕСКИХ

СВОЙСТВ

Нематов Хусан Ибодуллаевич

к.т.н. Каршинский инженерно-экономический институт

xusan85nematov@gmail.com

ABSTRACT

: Currently, it is considered important to select adsorbents with

high efficiency in drying gases. For this purpose, the following works are being carried
out: physical and chemical parameters of NaA (3Å) synthetic zeolite, physical and
chemical properties of 3 types of KA (3Å) zeolite were reviewed. and other information
is given in the article.

KAYS WORD:

Absorption drying, adsorption drying, condensation, membrane

method, synthetic zeolite, corrosion resistance.

АННОТАЦИЯ:

В настоящее время считается важным подбор

адсорбентов с высокой эффективностью осушки газов. С этой целью проводятся
следующие работы: рассмотрены физико-химические параметры синтетического
цеолита NaA (3Å), физико-химические свойства 3-х типов цеолита KA (3Å). и
другая информация приведена в статье.

KAYS WORD:

Абсорбционная сушка, адсорбционная сушка,

конденсация, мембранный метод, синтетический цеолит, коррозионная
стойкость.

Water vapor in gas can be separated by physical methods (adsorption,

absorption, membrane, condensation) and chemical methods (using CaCl

2

) and their

hybrid combination methods. Today, oil and gas processing industries use the following
traditional and modern gas drying methods [1]:

• Absorption drying;
• Adsorption drying;


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• Condensation. Spray cooling of hydrate inhibitors;
• Membrane method. Using elastomers and glassy polymers.
• Chemical method. Using hygroscopic salts. Metal chlorides are usually used.
Absorption and adsorption methods are widely used in the world.

Absorption drying of gases (Glycolic drying)

Drying gases using glycols is one of the most common methods, allowing gases

to be dried sufficiently for transmission or use as fuel.

Basic requirements for industrial consumers

In the absorption process, ethylene glycol, diethylene glycol and triethylene

glycol are mainly used as absorbers. In desorption cycle drying processes and repeated
application of the absorbent, almost no absorbent is consumed. Therefore, any
substance capable of separating the absorbent from the extracted component can be
used as an absorbent. However, in order to choose an absorber in the industry, a number
of the following requirements should be taken into account [2-3]:

• The absorbent must have a high absorption capacity relative to the component

to be extracted from the gas. The use of an absorbent with a low absorption capacity
leads to an increase in circulation of the circulating solution and an increase in the cost
of desorption.

• Absorbent should be easily regenerated during desorption. For this, the

component pressure in the absorbing solution must be high at the desorption
temperature.

• The selectivity of the absorbing solution should be high, that is, it should absorb

the desired component well and not absorb other substances in the gas.

• The absorption and desorption temperatures of the absorber should not have

high vapor pressure. Otherwise, the quantitative loss of this absorbent may increase.

• Absorbent should be chemically stable in working conditions, should not

change its age and structure. Chemical reactions should not occur between the gas and
the absorbent.

• The absorber must be cheap and have a large resource.
• The absorbent should not have a corrosive effect on the equipment of the

absorption process.

• The mass transfer coefficient must be sufficiently high.
It served as a basis for choosing effective adsorbents for natural gas drying. In

our study, various adsorbents were selected in order to improve the gas purification
process at Shurtanneftgaz LLC.


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Today, NaA synthetic zeolite with a pore size of 3 Å is used for natural gas

drying at Shurtanneftgaz LLC (Fig. 1). Physico-chemical parameters of this adsorbent
are presented in table 1.

1 – table

Physico-chemical parameters of NaA (3Å) synthetic zeolite

Indicator name

Demand for

TSh

Analysis results

1

Granular appearance

Cylindrical

Cylindrical

2

Adsorbent size, mm

2,8±3,

2,8

3

Cumulative

density,

g/cm

3

,

calculated relative to absolute dry
matter

0.65 is not less

0,94

4

Amount of zeolite phase crystals, %

Not less than

80.0

81,5

5

Moisture absorption capacity, mg/g

Not less than

160.0

205,0

6

Anti-aging strength, %

Not less than

92.0

92,0

7

Mass fraction of water resistance, %

Not less than

96.0

96,0

The composition of NaA zeolite is determined to be Na

2

O*Al

2

O

3

*SiO

2

.

Zeolites of this type are widely used in gas drying, deep cleaning of liquids and gases.
The main disadvantage of this type of zeolites is their water resistance and resistance
to high pressures compared to new generation zeolites.

1 – picture. Overview of NaA (3Å) synthetic zeolite

Taking into account the above, we have selected new generation adsorbents for

gas drying processes.


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For the first time in our research, we examined the physicochemical properties

of 3 types of KA (3Å) zeolite, which has been widely used in recent years. The obtained
results are presented in Table 2.

2 - table

Physico-chemical parameters of KA (3Å) zeolites

№ Indicator name

Spherical

1,6-2,5

Spherical

3-5

Spherical

1

Granule size, mm

1,6-2,5

3-5

1,6

2

The moisture content of gas
drying in static conditions,
mg/g, is not low

210

210

205

3

The moisture content of gas
drying in static conditions,
mg/cm

3

, is not low

2,0

2,0

2,0

4

Bulk density, g/cm

3

0,70

0,68

0,6

5

The amount of moisture in
zeolite, % is not much

1,0

1,0

1,0

6

Mass fraction of total loss, %

0,1

0,1

0,1

7

Moisture absorption capacity,
mg/g

230

220

215

8

Anti-aging strength, %

95,0

95,0

94,0

9

Mass fraction of water
resistance, %

99,0

99,0

99,0

2 – picture. General view of spherical KA (3Å) zeolite

The comparative analysis of the analysis results of KA (3Å) zeolites shows that

spherical zeolite 1.6-2.5 mm in size showed higher results compared to others and NaA
zeolite. Among these indicators, we can see that the main requirements for adsorbents


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Acumen: International Journal of Multidisciplinary Research

for gas drying are high, such as moisture absorption capacity, resistance to corrosion,
and water tolerance mass fraction.

In conclusion, the physico-chemical parameters of adsorbents NaA (3Å) and KA

(3Å) zeolites selected as a result of the research were studied. Their parameters such
as moisture absorption capacity, corrosion resistance, water tolerance mass fraction
were studied and used in natural gas drying at Shurtanneftgaz LLC.

LIST OF REFERENCES USED

1.

ТУ

2161-023-21742510-2008.

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2008. - 15 с.

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Серпионова E.H. Промышленная адсорбция газов и паров . М.:

Высшая школа, 1971.-413 с.

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Денисевич Е.В. Очистка и осушка природного газа силикагелями /

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Rakhimov, G., Kuybokarov, O., &Karshiyev, M. (2024). Research of the

catalytic properties of a catalyst selected for the production of high-molecular weight
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E3S WebofConferences

(Vol. 498,

p. 01008). EDP Sciences.

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Rakhimov, G. B. (2023). DEVELOPMENT OF ANTI-DETONATION

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Murtazaev, F. I., &Raximov, G. B. (2023). Synthesis of sorbents used in the

separation of halogens.

Sanoatda raqamli texnologiyalar

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References

ТУ 2161-023-21742510-2008. Адсорбент силикагелевый модифицированный РС-АССМ-М. Ярославль: ООО «Торговый дом «Реал Сорб», 2008. - 15 с.

Серпионова E.H. Промышленная адсорбция газов и паров . М.: Высшая школа, 1971.-413 с.

Денисевич Е.В. Очистка и осушка природного газа силикагелями / Е.В. Денисевич, JI.B. Моргун, С.А. Молчанов, Б.П. Золотовский // Газовая промышленность. 2001. - № 6. - С. 23-26.

Rakhimov, G., Kuybokarov, O., &Karshiyev, M. (2024). Research of the catalytic properties of a catalyst selected for the production of high-molecular weight liquid synthetic hydrocarbons from synthesis gas. In E3S WebofConferences (Vol. 498, p. 01008). EDP Sciences.

Rakhimov, G. B. (2023). DEVELOPMENT OF ANTI-DETONATION ADDITIVE. Экономика и социум, (12 (115)-1), 604-607.

Rakhimov, G. (2023). INCREASING REGENERATION EFFICIENCY BY RECYCLING ALKANOLAMINES. Sanoatda raqamli texnologiyalar /Цифровые технологии в промышленности, 1(2), 158-163.

Murtazaev, F. I., &Raximov, G. B. (2023). Synthesis of sorbents used in the separation of halogens. Sanoatda raqamli texnologiyalar, 1(01).