Verification of thermodynamic parameters of a mixture of generator gas on oxygen-hydrogen fuel with an excess of one of the fuel components

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Abstract

Liquid gas generators (LGG) are additional firing units in the power system of liquid rocket engines (LPRE). The LGG ensure the operation of the power units of the turbopump unit (TPU) of the engine by feeding combustion products (CP) to the turbine drive.

The main criteria for the efficiency of the generator gas is the complex (RT)gg and the thermodynamic properties of the mixture, depending on temperature, pressure, the degree of excess of the oxidizer and the enthalpy of the fuel, attributed to the conditions of supply to the nozzles of the GG. Changing the parameters of the generator gas leads to a change in the turbine power parameters due to its effect on the adiabatic operation of the Lad turbine. Depending on the engine circuit under consideration, CP GG can perform work in other units and elements of the engine, as well as influence many parameters of the LPRE. Among the main ones can be noted:

  • the power of the booster gas turbine of the booster turbopump unit (BTPU) in the case of the selection of the generator gas after the GG or turbogas after the main turbine;
  • the temperature of heating the refrigerant in the heat exchanger introduced in the GG;
  • specific impulse of a liquid rocket propulsion system (LRPS), depending on the quantity and properties of the turbogas entering the exhaust pipe of the engine (for the engine circuit without afterburning the generator gas);
  • mixing in the combustion chamber (CC) due to afterburning of turbogas entering the engine chamber after the turbine (for the engine circuit with afterburning of generator gas);
  • parameters of the firing wall of the engine in the case of using a high-temperature gas curtain by blowing generator gas into the supersonic part of the nozzle.

For many pairs of fuel during combustion in GG, the nonequilibrium of combustion products is characteristic (especially in hydrocarbon fuels).Due to the fact that the combustion products (CP) during the combustion of an oxygen-hydrogen mixture, due to the simplicity of the reaction, have time to form while staying in the GG (i.e., the time of chemical equilibrium of the CP is less than or equal to the time of stay in the GG), their thermodynamic parameters can be reliably determined using programs that simulate chemical equilibrium reactions.

In this article, the issue of obtaining reliable results of thermodynamic calculations of generator gas at low and high coefficients of oxidant excess is investigated. Verification of parameters obtained in the programs “Astra” and “Rocket Propulsion Analysis” with calculated values was carried out. The most suitable program for performing engineering calculations and modeling the thermodynamics of liquid gas generators has been determined.

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Introduction

Achieving carbon neutrality is underway in many countries around the world. Despite the low percentage of air pollution from launch vehicles compared to emissions of pollutants from industrial enterprises, the rocket industry is subject to some restrictions, forcing them to become more environmentally friendly.

One of the main tools for achieving carbon neutrality is alternative energy, the promising fuel of which is hydrogen due to its chemical kinetics [1]. Thus, back in the last century, hydrogen paired with oxygen was successfully used as fuel for liquid rocket engines [2; 3]. Liquid rocket engines developed in the Soviet Union [4], operating on hydroxygen, cannot compete with modern engines in terms of efficiency [5].

Following environmental trends [6] and taking into account the high energy content of hydrogen, the question arises of designing new [7] or modifying existing liquid propellant engines operating on this fuel [8]. At the same time, most modern liquid propellant propulsion systems contain liquid gas generators, in which, based on exothermic processes of decomposition or combustion of the corresponding substances, generator gas is produced with a relatively low temperature of the order of 500–1300 K [9]. The presence of a gas generator in the engine circuit allows throttling by regulating the ratio of fuel components in the gas generator [10], thus changing the thermodynamic parameters of the gas that drives the turbocharger turbine.

A feature of the LGG working process is that it occurs with a small supply of thermal energy to the fuel. Due to this, chemical reactions proceed more slowly than in a liquid-propellant rocket engine chamber [11]. As a result, high-temperature bundles may appear [12], which are characterized by increased temperatures with a disordered composition of fuel components [13], the presence of which has a negative effect on turbine blades [14]. Accordingly, the composition of combustion products is nonequilibrium. At the same time, modern programs for analyzing the thermodynamic parameters of combustion products (such as RPA and Astra) allow calculations only at equilibrium composition. Based on this, the question arises of obtaining reliable values of the parameters of the generator gas, which can be answered by creating mathematical models [15] that take into account the nonequilibrium composition [16].

The use of hydroxygen fuel should allow one to avoid the procedure for creating mathematical models due to the smaller number of chemical reactions occurring during the combustion process. In this regard, it is necessary to verify the calculated values of the thermodynamic parameters of the generator gas and the data obtained in programs for determining the equilibrium characteristics.

The use of oxygen and hydrogen as components of liquid propellant rocket engines makes it possible to achieve high values of specific thrust impulse (STI). At the same time, it becomes possible to use these engines as part of reusable rocket and space systems [17].

The advantage of reductive (RGG) and oxidative (OGG) RGGs based on oxygen-hydrogen fuel components is the chemical kinetics of the fuel itself, which makes it possible to drive turbines and achieve high values of adiabatic work at a sufficiently low or high excess oxidant ratio (EOR). At the same time, PSs provide high gas efficiency, as well as sufficient convergence of experimental data with thermodynamic calculations [18].

Calculation of the thermodynamic parameters of the LGG mixture using oxygen-hydrogen fuel

The thermodynamic parameters of the generator gas were calculated using the Rocket Propulsion Analysis (RPA) and Astra programs. These programs allow you to obtain the properties of combustion products at equilibrium gas composition. The Astra program was created at the Moscow State Technical University named after N. E. Bauman and is intended to determine the characteristics of equilibrium, phase and chemical composition of arbitrary systems, including for the thermodynamic calculation of liquid propellant engines [19].

RPA is a multi-platform analysis tool designed for use in the conceptual and preliminary design of chemical rocket engines [20]. RPA uses an expandable chemical library based on the NASA thermodynamic database and the L.V. Gurvich thermodynamic database, which includes data on numerous types of combustibles and oxidizers.

Table 1 [9] presents the thermodynamic parameters of the oxidizing generator gas [21], corresponding to the equilibrium composition and not taking into account the real working process.

Table 2 shows the calculated values of the reducing generator gas.

Comparison of the calculated parameters of the generator gas in the Astra and RPA programs with the values ​​from Tables 1 and 2 were carried out according to the following parameters: R is gas constant; T is temperature in the GG; k is the expansion isentropic index corresponding to the degree of gas expansion; C* is characteristic speed.

 

Table 1. Parameters of oxidizing generator gas of oxygen-hydrogen fuel

pгг, MPa

Parameter

αгг

8

9

10

11

13

14

15

16

10…25

T, К

1,449

1,313

1,199

1,103

945

881

824

773

R, J/(Kg∙K)

287.9

284.8

282.3

280.3

277.2

275.9

274.9

274

ккр

1.282

1.29

1.297

1.304

1.317

1.323

1.328

1.334

C*, m/s

974

920

873

833

764

735

709

684

 

Table 2. Chemical composition and parameters of reducing generator gas oxygen-hydrogen fuel

pгг,

МПа

Parameter

αгг

0.07

0.08

0.09

0.1

0.12

0.14

0.16

0.18

0,1…50

mH2O

0.402

0.435

0.467

0.496

0.545

0.593

0.639

0.662

mH2

0.598

0.565

0.533

0.504

0.455

0.407

0.361

0.338

R, Дж/

(Кг∙К)

2,665

2,540

2,415

2,313

2,131

1,954

1,868

1,698

0,1

T, К

553

631

709

785

935

1,081

1,220

1,355

ккр

1.389

1.382

1.379

1.375

1.36

1.35

1.331

1.321

к100

1.407

1.402

1.401

1.399

1.388

1.38

1.363

1.355

 

The end of Table 2

pгг,

MPa

Parameter

αгг

0.07

0.08

0.09

0.1

0.12

0.14

0.16

0.18

10

T, К

564

642

720

797

948

1,094

1,234

1,369

ккр

1.393

1.386

1.381

1.377

1.361

1.349

1.331

1.321

к100

1.41

1.405

1.402

1.4

1.386

1.376

1.36

1.352

50

T, К

606

686

766

847

999

1,148

1,290

1,427

ккр

1.392

1.385

1.379

1.373

1.358

1.341

1.327

1.314

к100

1.408

1.403

1.399

1.395

1.382

1.367

1.355

1.344

 

Based on the EOR values for the operation of two-component OGG and RGG according to the data in Table. 1, 2 calculations were carried out in the ranges 0,07 ≤ α ≤ 0,18 and 8 ≤ α ≤ 16.

Comparison of the results of calculations of the thermodynamic parameters of the RGG mixture in the RPA and Astra programs

When analyzing the results of calculating mass fractions obtained in the Astra program, the convergence of the data was confirmed with an average error of no more than 0.54 % (Fig. 1). While the values obtained in RPA (Fig. 2) have an average error of no more than 0.69 %.

 

Рис. 1. Химический состав генераторного газа при низких КИО, полученный в программе «Астра»

Fig. 1. Chemical composition of generator gas at low EOR obtained in the Astra program

 

Рис. 2. Химический состав генераторного газа при низких КИО (RPA)

Fig. 2. Chemical composition of generator gas at low EOR (RPA)

 

Figure 3 shows the dependence of the gas constant R on the oxidizer excess coefficient, which does not correspond to the calculated values by 0.7 and 1.3 % in the Astra and RPA programs, respectively.

 

Рис. 3. Значения газовой постоянной при низких КИО

Fig. 3. Values of the gas constant at low EOR

 

At pressures of 0.1 and 10 MPa (Fig. 4), temperature values were obtained with an average error of no more than 0.5 %. The temperatures obtained at a pressure of 50 MPa differ from the calculated temperatures by 6 % in both programs.

 

Рис. 4. Температуры генераторного газа при давлении 10 МПа и низких КИО

Fig. 4. Generator gas temperatures at a pressure of 10 MPa and low EOR

 

Figure 5 shows the values of the expansion isentropic index corresponding to the critical pressure difference (pgg/pa = 2) obtained in the RPA and Astra programs. When analyzing the values, it was revealed that they have close convergence (no more than 0.57 %) with the calculated data.

The values of the expansion isentropic index k100 obtained in RPA have a discrepancy of 10 % with the calculated data, and the results obtained using the ASTRA-M program show qualitative convergence (Fig. 6). The average error of thermodynamic calculations is given in table 3.

 

Рис. 5. Показатель изоэнтропы расширения при давлении в ГГ 10 МПа и низких КИО

Fig. 5. Isentropy of expansion at a pressure in GG of 10 MPa and low EOR

 

Рис. 6. k100 при давлении в ГГ 10 МПа и низких КИО

Fig. 6. k100 at a pressure in GG of 10 MPa and low EOR

 

Table 3. Average error relative to the calculated values of the reducing generator gas

Parameter

Error, %

Astra

RPA

mH2O

0.47

0.55

mH2

0.61

0.82

R

0.7

1.3

T

2.51

2.60

ккр

0.69

0.23

k100

1.04

9.54

 

Comparison of the results of calculations of the thermodynamic parameters of the OGG mixture in the RPA and Astra programs

Figures 7–9 show graphs of the dependences of the gas constant, temperature, and characteristic velocity on the oxidizer excess coefficient. The dependences were obtained for oxidizing generator gas in the gas generator pressure range of 10–25 MPa. The results of thermodynamic calculations carried out in the Astra and RPA programs show sufficient convergence with the calculated values (Table 4). The maximum error of the parameters is no more than 0.21 %.

 

Рис. 7. Значения газовой постоянной при высоких КИО

Fig. 7. Values of the gas constant at high EOR

 

Рис. 8. Температуры генераторного газа при давлениях 10–25 МПа и высоких КИО

Fig. 8. Generator gas temperatures at pressures of 10.25 MPa and high EOR

 

Рис. 9. Зависимость характеристической скорости от КИО

Fig. 9. Dependence of the characteristic velocity on the EOR

 

Table 4. Average error relative to the calculated values of oxidizing generator gas

Parameter

Error, %

Astra

RPA

T

0.59

0.10

R

0.02

0.02

ккр

0.04

0.09

C*

0.18

0.03

 

Conclusion

Verification of the parameters of the generator gas mixture on oxygen-hydrogen fuel at low and high EOR made it possible to establish that most of the values obtained in the Astra program have better agreement with the calculated data at low EOR and are 0.15% inferior to the RPA program at high EOR. The disadvantage of the Astra program is the inability to obtain mass fractions and the requirement for additional recalculation from other fractions.

The values of the thermodynamic parameters of the generator gas obtained in the RPA program also have sufficient convergence. The disadvantages of RPA include the inability to carry out calculations with an EOR equal to less than 0.1.

As a result, it was revealed that both programs can be used for engineering calculations and modeling of the thermodynamics of LGG. It was possible to confirm the sufficient convergence of calculations of the thermodynamic parameters of reducing and oxidizing gas generators using oxygen-hydrogen fuel to the values from calculations taking into account the nonequilibrium composition of the generator gas [22].

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About the authors

Vladislav A. Belyakov

Moscow Aviation Institute (National Research University); Experimental Design Bureau “Crystal”

Email: titflavii@rambler.ru

Cand. Sc., Assistant of the Department 202: Rocket Engines; Leading Engineer

Russian Federation, Moscow; Moscow

Dmitry O. Vasilevsky

Nevsky Plant; Baltic State Technical University “Voenmeh” named after D. F. Ustinov

Author for correspondence.
Email: zudwa_dwesti_dwa@rambler.ru

Leading Designer; Cand. Sc., Associate Professor of Department A8: Aircraft Engines and Power Plants

Russian Federation, Saint Petersburg; Saint Petersburg

Daniil V. Maslov

State Scientific Center “Keldysh Center”

Email: davmaslov@mai.education

Technician

Russian Federation, Moscow

Artemy A. Kilyashov

University of Information Technologies, Mechanics and Optics

Email: artemy.kiliashov@gmail.com

Postgraduate Student

Russian Federation, Saint Petersburg

Roman V. Romashko

Moscow Aviation Institute (National Research University); Experimental Design Bureau “Crystal”

Email: roma.romashko2015@yandex.ru

Postgraduate Student; Engineer of Department 202: Rocket Engines; Category III Design Engineer

Russian Federation, Moscow; Moscow

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Supplementary files

Supplementary Files
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1. JATS XML
2. Fig. 1. Chemical composition of generator gas at low EOR obtained in the Astra program

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3. Fig. 2. Chemical composition of generator gas at low EOR (RPA)

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4. Fig. 3. Values of the gas constant at low EOR

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5. Fig. 4. Generator gas temperatures at a pressure of 10 MPa and low EOR

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6. Fig. 5. Isentropy of expansion at a pressure in GG of 10 MPa and low EOR

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7. Fig. 6. k100 at a pressure in GG of 10 MPa and low EOR

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8. Fig. 7. Values of the gas constant at high EOR

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9. Fig. 8. Generator gas temperatures at pressures of 10.25 MPa and high EOR

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10. Fig. 9. Dependence of the characteristic velocity on the EOR

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Copyright (c) 2024 Belyakov V.A., Vasilevsky D.O., Maslov D.V., Kilyashov A.A., Romashko R.V.

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