CN110807249B - Rigid chemical reaction flow semi-hidden semi-explicit self-adaptive time step propulsion simulation method - Google Patents

Rigid chemical reaction flow semi-hidden semi-explicit self-adaptive time step propulsion simulation method Download PDF

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CN110807249B
CN110807249B CN201910998330.7A CN201910998330A CN110807249B CN 110807249 B CN110807249 B CN 110807249B CN 201910998330 A CN201910998330 A CN 201910998330A CN 110807249 B CN110807249 B CN 110807249B
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张斌
刘洪�
余彬
谢名云
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Shanghai Jiao Tong University
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Abstract

一种刚性化学反应流动半隐半显自适应时间步长推进模拟方法,根据超声速刚性燃烧流动问题的初始物理状态参量设置初始流场,在化学反应项的计算阶段,通过流动特征时间和反应特征时间计算出系统刚性,根据系统刚性选取导致演化能够稳定推进的最大时间步长,并用该时间步长不断进行时间推进,以更新流场数据信息。本方法极大地提升了半隐半显算法的计算效率,实现了时间步长最大化。

Figure 201910998330

A semi-implicit and semi-explicit adaptive time-step advancement simulation method for rigid chemical reaction flow. The initial flow field is set according to the initial physical state parameters of the supersonic rigid combustion flow problem. The system stiffness is calculated by time, and the maximum time step that can lead to stable advancement of the evolution is selected according to the system stiffness, and the time step is used to continuously advance time to update the flow field data information. This method greatly improves the computational efficiency of the semi-implicit and semi-explicit algorithm, and maximizes the time step.

Figure 201910998330

Description

刚性化学反应流动半隐半显自适应时间步长推进模拟方法Half-hidden and half-explicit adaptive time-step advancing simulation method for rigid chemical reaction flow

技术领域technical field

本发明涉及的是一种化学反应控制领域的技术,具体是一种刚性化学反应流动半隐半显(IMEX)自适应时间步长推进模拟方法。The invention relates to a technology in the field of chemical reaction control, in particular to a semi-hidden and semi-explicit (IMEX) self-adaptive time step advancing simulation method for rigid chemical reaction flow.

背景技术Background technique

随着计算流体力学(Computational fluid dynamics,CFD)的不断发展,学者们将化学反应源项和流动NS方程耦合起来,逐渐发展出了针对化学反应流动问题的一系列计算方法。但由于化学反应和流动时间尺度的不一致导致方程的刚性极大,从而计算效率极低。故针对化学反应流动问题的一大研究重点即为计算效率的提升。研究发现通过对化学反应源项的隐式处理可增大推进的时间步长,现有的三大算法:全隐法,半隐半显以及解耦方法均有通过隐式处理的方式来增大时间步长。但他们对于时间步长的选取基本采用固定CFL(Courant-Friedrichs-Lewy)数或固定时间步长,忽略了燃烧特征对时间步长选取的影响。这明显不利于计算效率的提高。With the continuous development of Computational fluid dynamics (CFD), scholars have coupled the chemical reaction source term with the flow NS equation, and gradually developed a series of calculation methods for chemical reaction flow problems. However, due to the inconsistency of chemical reaction and flow time scales, the equations are extremely rigid, resulting in extremely low computational efficiency. Therefore, a major research focus on chemical reaction flow problems is the improvement of computational efficiency. The study found that the time step of the advance can be increased through the implicit processing of the chemical reaction source term. The three existing algorithms: the full implicit method, the semi-implicit and semi-explicit method, and the decoupling method all increase the time step by implicit processing. large time steps. However, they basically adopted fixed CFL (Courant-Friedrichs-Lewy) number or fixed time step for the selection of time step, ignoring the influence of combustion characteristics on the selection of time step. This is obviously not conducive to the improvement of computational efficiency.

发明内容Contents of the invention

本发明针对现有技术存在的上述不足,提出一种刚性化学反应流动半隐半显自适应时间步长推进模拟方法,通过对化学反应源项隐式处理求解过程的深入分析,推导出隐式特征时间步长,对其进行进一步扩展即得到自适应时间步长推进形式,将燃烧特性融入时间步长选取机制,使得时间步长随物理瞬态特性而变化,得到演化稳定推进的最大时间步长,以提高计算效率。Aiming at the above-mentioned deficiencies in the prior art, the present invention proposes a half-hidden and half-explicit adaptive time step advancement simulation method for rigid chemical reaction flow, and derives the implicit The characteristic time step is further expanded to obtain an adaptive time step advancement form, and the combustion characteristics are integrated into the time step selection mechanism, so that the time step changes with the physical transient characteristics, and the maximum time step for evolutionary stable advancement is obtained length to improve computational efficiency.

本发明是通过以下技术方案实现的:The present invention is achieved through the following technical solutions:

本发明涉及一种刚性化学反应流动半隐半显自适应时间步长推进模拟方法,根据超声速刚性燃烧流动问题的初始物理状态参量设置初始流场,在化学反应项的计算阶段,通过流动特征时间和反应特征时间计算出系统刚性,根据系统刚性选取导致演化能够稳定推进的最大时间步长,并用该时间步长不断进行时间推进,以更新流场数据信息。The invention relates to a half-hidden and half-explicit self-adaptive time step advancement simulation method for rigid chemical reaction flow, which sets the initial flow field according to the initial physical state parameters of the supersonic rigid combustion flow problem, and passes through the flow characteristic time in the calculation stage of the chemical reaction item The system rigidity is calculated based on the reaction characteristic time and the system rigidity. According to the system rigidity, the maximum time step that leads to the evolution can be stably advanced is selected, and the time step is used to continuously advance the time to update the flow field data information.

所述的超声速刚性燃烧流动问题是指:控制方程为不考虑粘性影响带化学反应源项的欧拉方程:

Figure BDA0002240475000000011
其中:U为守恒量,E、F为通量,S为化学反应源项。The supersonic rigid combustion flow problem refers to: the governing equation is the Euler equation with no consideration of the viscosity influence and a chemical reaction source term:
Figure BDA0002240475000000011
Among them: U is the conserved quantity, E and F are the fluxes, and S is the chemical reaction source term.

所述的半隐半显是指:对流动和化学反应耦合求解,流动进行显式处理,化学反应源项进行隐式处理,得到:

Figure BDA0002240475000000012
其中:残差
Figure BDA0002240475000000013
Figure BDA0002240475000000014
The semi-implicit and semi-explicit means: to solve the coupling of flow and chemical reaction, the flow is explicitly processed, and the chemical reaction source item is implicitly processed to obtain:
Figure BDA0002240475000000012
where: residual
Figure BDA0002240475000000013
Figure BDA0002240475000000014

所述的系统刚性

Figure BDA0002240475000000021
其中:最大的特征时间τmax即流动特征时间
Figure BDA0002240475000000022
最小的特征时间τmin即最小化学反应特征时间
Figure BDA0002240475000000023
其中:τf为流动特征时间,Δx为网格间距,u为流场速度,c为声速。The rigidity of the system
Figure BDA0002240475000000021
Where: the largest characteristic time τ max is the flow characteristic time
Figure BDA0002240475000000022
The minimum characteristic time τ min is the minimum chemical reaction characteristic time
Figure BDA0002240475000000023
Where: τ f is the characteristic time of the flow, Δx is the grid spacing, u is the velocity of the flow field, and c is the speed of sound.

所述的最大时间步长,通过以下方式得到:使系统演化能够稳定推进的最大时间步长

Figure BDA0002240475000000024
其中:Ω为系统刚性,τf为流动特征时间,在刚性变化不大的情况下可视为常数,k通常为不大于1的常数,且小于CFL数;在求解系统刚性时,使用调整后的化学反应特征时间
Figure BDA0002240475000000025
来进行计算,其中
Figure BDA0002240475000000026
τc为化学反应特征时间,δt0为与推进时间步长相同量级的常数。The maximum time step is obtained by the following method: the maximum time step that enables the system evolution to advance stably
Figure BDA0002240475000000024
Where: Ω is the system rigidity, τ f is the flow characteristic time, which can be regarded as a constant when the rigidity changes little, and k is usually a constant not greater than 1 and smaller than the CFL number; when solving the system rigidity, use the adjusted The characteristic time of the chemical reaction
Figure BDA0002240475000000025
to calculate, where
Figure BDA0002240475000000026
τ c is the characteristic time of the chemical reaction, and δt 0 is a constant of the same magnitude as the advancing time step.

所述的稳定推进是指:模拟过程不出现非物理解,即负密度以及不发生发散,即无穷大的最大推进时间步长。The stable propulsion refers to: no non-physical understanding occurs in the simulation process, that is, negative density and no divergence, that is, the maximum propulsion time step of infinity.

所述的流场数据信息包括:守恒量以及温度,压力和密度等基本物理量,其更新通过以下方式实现:使用计算得到的自适应时间步长通过半隐半显方法对流场数据信息进行更新。The flow field data information includes: conserved quantities and basic physical quantities such as temperature, pressure and density, and its update is realized in the following way: using the calculated adaptive time step to update the flow field data information through a half-hidden and half-explicit method .

本发明涉及一种实现上述方法的系统,包括:流动求解模块、时间步长选取模块、化学反应模块和数据更新模块。The invention relates to a system for realizing the above method, comprising: a flow solution module, a time step selection module, a chemical reaction module and a data update module.

所述的半隐半显,包括显式处理和隐式处理,其中:The semi-hidden and semi-explicit includes explicit processing and implicit processing, wherein:

所述的显式处理是指:流动求解模块通过AUSM+(Advection Upstream SplittingMethod)方法计算得到通量;对化学反应源项进行隐式处理,通过对角简化的Jacobi矩阵得到相应的预处理矩阵以及残差;The explicit processing refers to: the flux is calculated by the flow solution module through the AUSM+ (Advection Upstream Splitting Method) method; the chemical reaction source item is implicitly processed, and the corresponding preprocessing matrix and residual matrix are obtained through the diagonally simplified Jacobi matrix. Difference;

所述的隐式处理是指:化学反应模块通过计算显式化学反应源项特征时间τc;根据流动速度数据等计算出流动特征时间,从而得到τf;时间步长选取模块根据前两个特征时间计算得到系统刚性

Figure BDA0002240475000000027
得到自适应时间步长
Figure BDA0002240475000000028
其中k为常数;数据更新模块通过推进时间步长对流场物理量如温度,压力等物理量进行更新。The implicit processing refers to: the chemical reaction module calculates the characteristic time τ c of the explicit chemical reaction source item; calculates the flow characteristic time according to the flow velocity data, etc., thereby obtaining τ f ; the time step selection module is based on the first two The characteristic time is calculated to obtain the system stiffness
Figure BDA0002240475000000027
get adaptive time step
Figure BDA0002240475000000028
Where k is a constant; the data update module updates the physical quantities of the flow field such as temperature and pressure by advancing the time step.

技术效果technical effect

与现有技术相比,本发明实现了在计算过程中可以根据流场燃烧特性来确定推进时间步长,使得计算在刚性变化时始终以最佳的时间步长推进,改进了之前使用的固定CFL数或固定时间步长的不合理方式,极大地提高了系统计算效率。Compared with the prior art, the present invention realizes that the advance time step can be determined according to the combustion characteristics of the flow field during the calculation process, so that the calculation always advances with the optimal time step when the rigidity changes, which improves the previously used fixed The unreasonable way of CFL number or fixed time step greatly improves the calculation efficiency of the system.

附图说明Description of drawings

图1为本发明流程图;Fig. 1 is a flowchart of the present invention;

图2为系统效率提升原理图;Figure 2 is a schematic diagram of system efficiency improvement;

图中1/dt线图与水平轴围成的面积与计算时间成正比;The area enclosed by the 1/dt line graph and the horizontal axis in the figure is proportional to the calculation time;

图3为计算域为2.5m的一维CJ爆轰波压力线图:Fig. 3 is a one-dimensional CJ detonation wave pressure diagram with a calculation domain of 2.5m:

图4为计算域为2.5m的一维CJ爆轰波效率提升原理图:Figure 4 is a schematic diagram of the one-dimensional CJ detonation wave efficiency improvement with a calculation domain of 2.5m:

图5为二维斜爆轰温度云图:Figure 5 is a two-dimensional oblique detonation temperature cloud map:

图6为二维斜爆轰效率提升原理图;Figure 6 is a schematic diagram of two-dimensional oblique detonation efficiency improvement;

图中圈出部分为最大刚性处,此时时间步长应小于某一常数;The circled part in the figure is the maximum rigidity, and the time step should be smaller than a certain constant at this time;

图7为二维超爆轰温度云图:Figure 7 is a two-dimensional superdetonation temperature cloud map:

图8为二维超爆轰中轴线压力分布线图:Figure 8 is a two-dimensional superdetonation central axis pressure distribution line diagram:

图9为二维超爆轰效率提升原理图。Figure 9 is a schematic diagram of two-dimensional superdetonation efficiency improvement.

具体实施方式Detailed ways

本实施例实现环境为集成开发环境(IDE,Integrated DevelopmentEnvironment)为Visual Studio Community 2017,编译器为Intel Parallel Studio XE2019软件中的Intel(R)Visual Fortran Compiler,采用Release模式运行,电脑CPU为Intel酷睿i7 6700K。The implementation environment of this embodiment is that the integrated development environment (IDE, Integrated Development Environment) is Visual Studio Community 2017, and the compiler is the Intel(R)Visual Fortran Compiler in the Intel Parallel Studio XE2019 software, adopts Release mode to run, and the computer CPU is an Intel Core i7 6700K.

实施例1Example 1

本实施例过程包括:在一个计算区域长2.5m的等截面区域,左端封闭,右端开口。计算区域内充满了H2/O2/Ar(物质的量比是2:1:7)的混合气体。计算网格取N=1250。化学反应模型选择9组分19反应的J模型。计算初始时刻,在计算区域左侧前5个网格的区域内充满了高温高压气体,其压力和温度分别为2000K和2MPa。计算区域其余部分为低温(298K)低压(6.67kPa)气体。本实施例中所用方法ITC(隐式时间步长控制)与固定CFL数和固定时间步长两种算法进行了比较。The process of this embodiment includes: a calculation area with a length of 2.5m and a constant cross-section area, the left end is closed and the right end is open. The calculation area is filled with the mixed gas of H 2 /O 2 /Ar (substance ratio is 2:1:7). The calculation grid takes N=1250. The chemical reaction model selects the J model of 9 components and 19 reactions. At the initial moment of calculation, the area of the first five grids on the left side of the calculation area is filled with high-temperature and high-pressure gas, and its pressure and temperature are 2000K and 2MPa, respectively. The rest of the calculation area is low temperature (298K) low pressure (6.67kPa) gas. The method ITC (Implicit Time Step Control) used in this example is compared with two algorithms of fixed CFL number and fixed time step.

所述的9组分19反应的J模型具体是指:The J model of described 9 components 19 reactions specifically refers to:

Figure BDA0002240475000000031
Figure BDA0002240475000000031

Figure BDA0002240475000000041
Figure BDA0002240475000000041

本实施例中计算最终时间为14ms。In this embodiment, the final calculation time is 14ms.

本实施例中压力线图如图3,效率提升原理图如图4。In this embodiment, the pressure line diagram is shown in Figure 3, and the efficiency improvement principle diagram is shown in Figure 4.

本实施例中计算效率对比表如表1。The calculation efficiency comparison table in this embodiment is shown in Table 1.

表1本方法ITC与固定CFL数和固定时间步长计算效率比较Table 1 Comparison of calculation efficiency between this method ITC and fixed CFL number and fixed time step

Figure BDA0002240475000000042
Figure BDA0002240475000000042

本实施例表明在保证精度近似不变的前提下,使用ITC可以使得效率得到很大提升。This embodiment shows that under the premise that the precision is kept approximately constant, the efficiency can be greatly improved by using the ITC.

实施例2Example 2

实施例2为斜爆轰算例,设置矩形计算域,H2:O2:N2=2:1:3.76的可燃混合气体以-25°的攻角射向壁面,计算域为5.25cm×2cm,来流马赫数为7.5,压力和温度分别为40KPa,293K,网格数为200×80。采用的化学反应模型仍为J模型。Example 2 is an oblique detonation calculation example, a rectangular calculation domain is set, the combustible gas mixture of H 2 :O 2 :N 2 =2:1:3.76 shoots at the wall at an angle of attack of -25°, and the calculation domain is 5.25cm× 2cm, the Mach number of incoming flow is 7.5, the pressure and temperature are 40KPa and 293K respectively, and the grid number is 200×80. The chemical reaction model used is still the J model.

该实施例为定常问题,计算终止时间为6×10-5s。This embodiment is a stationary problem, and the calculation termination time is 6×10 -5 s.

本实施例中温度云图如图5,计算效率提升原理图如图6。In this embodiment, the temperature cloud diagram is shown in Figure 5, and the calculation efficiency improvement principle diagram is shown in Figure 6.

本实施例中计算效率对比表如表2。The calculation efficiency comparison table in this embodiment is shown in Table 2.

表2本方法ITC与固定CFL数和固定时间步长计算效率比较Table 2 Comparison of calculation efficiency between ITC and fixed CFL number and fixed time step in this method

Figure BDA0002240475000000051
Figure BDA0002240475000000051

实施例3Example 3

本实施例针对的计算模型模型为半径为7.5mm的球,来流为满足化学当量比的H2/O2/Air混合气体,氢气、氧气和氮气的摩尔比为2:1:3.76。远场边界采用来流边界条件,壁面边界采用绝热无催化壁面条件,对称边界采用对称边界条件。来流马赫数为8.5,压力为42662Pa,温度为250K。沿球面法向分布100个网格,切向125个。采用的化学反应模型仍为J模型。该实施例为定常问题,计算终止时间为3×10-5s。The calculation model for this embodiment is a sphere with a radius of 7.5 mm, the incoming flow is a mixed gas of H 2 /O 2 /Air satisfying the stoichiometric ratio, and the molar ratio of hydrogen, oxygen and nitrogen is 2:1:3.76. The far-field boundary adopts the incoming flow boundary condition, the wall boundary adopts the adiabatic non-catalytic wall condition, and the symmetrical boundary adopts the symmetrical boundary condition. The incoming Mach number is 8.5, the pressure is 42662Pa, and the temperature is 250K. Distribute 100 meshes along the normal of the sphere and 125 tangentially. The chemical reaction model used is still the J model. This embodiment is a steady problem, and the calculation termination time is 3×10 -5 s.

本实施例中温度云图如图7,中轴线压力线图如图8,计算效率提升原理图如图9。In this embodiment, the temperature cloud diagram is shown in Figure 7, the central axis pressure line diagram is shown in Figure 8, and the calculation efficiency improvement principle diagram is shown in Figure 9.

本实施例中计算效率对比表如表3。The calculation efficiency comparison table in this embodiment is shown in Table 3.

表3本方法ITC与固定CFL数和固定时间步长计算效率比较Table 3 Comparison of calculation efficiency between ITC and fixed CFL number and fixed time step in this method

Figure BDA0002240475000000052
Figure BDA0002240475000000052

综上表明在保证精度近似不变的前提下,使用ITC可以使得计算效率得到很好提升。In summary, it shows that under the premise of ensuring that the accuracy is approximately unchanged, the use of ITC can greatly improve the computational efficiency.

以上组件中哪一个为本发明独创、从未被公开且其工作方式与任何现有文献记载均不相同的是:推进时间步长选取采用ITC方法,极大提升了计算效率。Which one of the above components is the original creation of the present invention, has never been disclosed, and its working method is different from any existing literature records: the selection of the advancing time step adopts the ITC method, which greatly improves the calculation efficiency.

与现有技术相比,本方法的性能指标提升在于:时间步长根据系统刚性进行选取,计算效率较现有CFL和固定时间步长方法得到有效提升。Compared with the existing technology, the performance index of this method is improved in that: the time step is selected according to the rigidity of the system, and the calculation efficiency is effectively improved compared with the existing CFL and fixed time step methods.

上述具体实施可由本领域技术人员在不背离本发明原理和宗旨的前提下以不同的方式对其进行局部调整,本发明的保护范围以权利要求书为准且不由上述具体实施所限,在其范围内的各个实现方案均受本发明之约束。The above specific implementation can be partially adjusted in different ways by those skilled in the art without departing from the principle and purpose of the present invention. The scope of protection of the present invention is subject to the claims and is not limited by the above specific implementation. Each implementation within the scope is bound by the invention.

Claims (4)

1. A rigid chemical reaction flow semi-hidden semi-explicit self-adaptive time step propulsion simulation method is characterized in that an initial flow field is set according to initial physical state parameters of a supersonic rigid combustion flow problem, system rigidity is calculated through flow characteristic time and reaction characteristic time in a calculation stage of a chemical reaction item, the maximum time step which causes evolution to be capable of being stably propelled is selected according to the system rigidity, and time propulsion is continuously carried out through the time step so as to update flow field data information;
the supersonic velocity rigid combustion flow problem refers to that: the governing equation is an euler equation with chemical reaction source terms without considering viscosity effects:
Figure FDA0003829177060000011
wherein: u is conservation quantity, E and F are fluxes, and S is a chemical reaction source term;
the semi-hidden and semi-obvious means: solving the coupling of the flow and the chemical reaction, carrying out explicit processing on the flow, and carrying out implicit processing on a chemical reaction source item to obtain:
Figure FDA0003829177060000012
wherein: residual error
Figure FDA0003829177060000013
Figure FDA0003829177060000014
The maximum time step is obtained by the following method: maximum time step for enabling stable propulsion of system evolution
Figure FDA0003829177060000015
Figure FDA0003829177060000016
Wherein: omega is the system stiffness, tau f K is a constant not greater than 1 and less than CFL for flow characteristic time, and the adjusted chemical reaction characteristic time is used when solving for system stiffness
Figure FDA0003829177060000017
To perform a calculation wherein
Figure FDA0003829177060000018
τ c Is the characteristic time of the chemical reaction, δ t 0 Is a constant of the same order of magnitude as the step of the propulsion time.
2. The method of claim 1, wherein said system is rigid
Figure FDA0003829177060000019
Wherein: maximum characteristic time tau mαx I.e. characteristic time of flow
Figure FDA00038291770600000110
Minimum characteristic time tau min I.e. minimum chemical reaction characteristic time
Figure FDA00038291770600000111
Figure FDA00038291770600000112
Wherein: tau. f For the flow characteristic time, Δ x is the grid spacing, u is the flow field velocity, and c is the acoustic velocity.
3. The method of claim 1, wherein said steady advancement is: the simulation process does not exhibit non-physical understanding, i.e., negative density, and does not exhibit divergence, i.e., infinite maximum step of propulsion time.
4. The method of claim 1, wherein said flow field data information comprises: conservation of quantity and temperature, pressure and density, its renewal is achieved by: and updating flow field data information by using the self-adaptive time step obtained by calculation through a semi-hidden semi-explicit method.
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