CN106650242B - A cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant - Google Patents
A cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant Download PDFInfo
- Publication number
- CN106650242B CN106650242B CN201611094101.5A CN201611094101A CN106650242B CN 106650242 B CN106650242 B CN 106650242B CN 201611094101 A CN201611094101 A CN 201611094101A CN 106650242 B CN106650242 B CN 106650242B
- Authority
- CN
- China
- Prior art keywords
- propellant
- weight
- temperature
- evaporation
- term
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000003380 propellant Substances 0.000 title claims abstract description 114
- 238000001704 evaporation Methods 0.000 title claims abstract description 72
- 230000008020 evaporation Effects 0.000 title claims abstract description 68
- 230000007774 longterm Effects 0.000 title claims abstract description 43
- 238000011156 evaluation Methods 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 22
- 238000004364 calculation method Methods 0.000 claims description 36
- 239000010410 layer Substances 0.000 claims description 32
- 239000012774 insulation material Substances 0.000 claims description 23
- 238000009413 insulation Methods 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 11
- 239000011810 insulating material Substances 0.000 claims description 7
- 125000006850 spacer group Chemical group 0.000 claims description 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- 239000011229 interlayer Substances 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 238000001816 cooling Methods 0.000 abstract description 9
- 238000004458 analytical method Methods 0.000 abstract description 2
- 238000005457 optimization Methods 0.000 abstract description 2
- 230000035515 penetration Effects 0.000 description 4
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000004584 weight gain Effects 0.000 description 1
- 235000019786 weight gain Nutrition 0.000 description 1
Classifications
-
- G—PHYSICS
- G16—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS
- G16Z—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS, NOT OTHERWISE PROVIDED FOR
- G16Z99/00—Subject matter not provided for in other main groups of this subclass
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种用于低温推进剂长期在轨蒸发量控制的代价评估方法,属于低温推进剂长期在轨贮存与管理领域。The invention relates to a cost evaluation method used for long-term on-orbit evaporation control of low-temperature propellants, belonging to the field of long-term on-orbit storage and management of low-temperature propellants.
背景技术Background technique
低温推进剂由于其比冲高、无毒无污染、价格相对低廉,在国内外运载火箭和上面级上得到了广泛的应用。低温推进剂被认为是进入空间及轨道转移最经济、效率最高的化学推进剂,也是未来人类月球探测、火星探测及更远距离的深空探测的首选推进剂。低温推进剂虽然性能高,但其沸点低,易因受热而蒸发,难于长时间存储,由于低温推进剂的损耗会显著影响运载火箭的性能及任务的执行。因此通过采取合理有效的措施解决低温推进剂蒸发量的控制问题,最终实现无损贮存,是低温推进剂长时间在轨应用的重要前提,也是亟待解决的问题。Low-temperature propellants have been widely used in domestic and foreign launch vehicles and upper stages due to their high specific impulse, non-toxic, non-polluting, and relatively low price. Cryogenic propellants are considered to be the most economical and efficient chemical propellants for entering space and orbital transfer, and are also the preferred propellants for future human lunar exploration, Mars exploration and longer-distance deep space exploration. Although low-temperature propellant has high performance, its boiling point is low, and it is easy to evaporate due to heat, and it is difficult to store for a long time. Due to the loss of low-temperature propellant, the performance of the launch vehicle and the execution of the mission will be significantly affected. Therefore, taking reasonable and effective measures to solve the control problem of low-temperature propellant evaporation, and finally achieve non-destructive storage, is an important prerequisite for long-term in-orbit application of low-temperature propellant, and it is also an urgent problem to be solved.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于克服现有技术的上述缺陷,提供一种用于低温推进剂长期在轨蒸发量控制的代价评估方法,该方法获取低温推进剂长期在轨贮存系统蒸发量和蒸发率,再获得蒸发量控制措施带来的重量代价,进而获得重量代价最小的最优设计工况,用于指导低温推进剂在轨贮存系统的设计。The object of the present invention is to overcome the above-mentioned defects of the prior art, and to provide a cost evaluation method for the long-term in-orbit evaporation control of low-temperature propellant, which obtains the evaporation and evaporation rate of the low-temperature propellant long-term in-orbit storage system, and then The weight cost brought by the evaporation control measures is obtained, and then the optimal design condition with the smallest weight cost is obtained, which is used to guide the design of the cryogenic propellant on-orbit storage system.
本发明的上述目的主要是通过如下技术方案予以实现的:The above-mentioned purpose of the present invention is mainly achieved through the following technical solutions:
一种用于低温推进剂长期在轨蒸发量控制的代价评估方法,包括如下步骤:A cost assessment method for long-term in-orbit evaporation control of cryogenic propellant, comprising the following steps:
(1)、确定低温推进剂在轨贮存净漏热量Qloss;(1), determine the low-temperature propellant on-orbit storage net heat leakage Q loss ;
(2)、根据净漏热量Qloss、低温推进剂饱和温度对应蒸发潜热γ和在轨工作时间t,获得不同工况下的低温推进剂蒸发量及蒸发率i表示不同的工况,i=1,2,……,N,其中N为工况数量;(2) According to the net heat leakage Q loss , the latent heat of evaporation γ corresponding to the saturation temperature of the low-temperature propellant, and the on-orbit working time t, the evaporation amount of the low-temperature propellant under different working conditions is obtained and evaporation rate i represents different working conditions, i=1, 2, ..., N, where N is the number of working conditions;
(3)、获得不同工况下引入制冷机带来的重量增加将同一工况下的与对应的蒸发量求和得到该工况下的系统重量代价遍历所有工况下的系统重量代价寻找系统重量代价的最小值;(3), to obtain the weight increase brought by the introduction of the refrigerator under different working conditions under the same conditions with the corresponding evaporation Summation to get the system weight penalty under this condition Traverse the weight cost of the system under all operating conditions Find System Weight Costs the minimum value of ;
(4)、记录系统重量代价取最小值时对应的工况,作为最优工况。(4), record system weight cost The working condition corresponding to the minimum value is taken as the optimal working condition.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,所述步骤(1)中确定低温推进剂在轨贮存净漏热量Qloss的具体方法如下:In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the specific method for determining the net heat leakage Q loss of cryogenic propellant in orbit storage in the step (1) is as follows:
Qloss=QMLI+Qstruts+Qparastitic+Qpenetrations-Qvapor-Qcryocooler Q loss =Q MLI +Q struts +Q parastitic +Q penetrations -Q vapor -Q cryocooler
其中:QMLI表示推进剂贮箱表面隔热材料漏热量;Qstruts表示推进剂贮箱支撑结构的漏热量;Qparastitic表示制冷机漏热量;Qpenetrations表示贮箱管路漏热量;Qvapor表示低温推进剂排气可利用冷量;Qcryocooler表示制冷机的制冷量。Among them: Q MLI is the heat leakage of the thermal insulation material on the surface of the propellant tank; Q struts is the heat leakage of the propellant tank support structure; Q parastitic is the heat leakage of the refrigerator ; The cryo-propellant exhaust can utilize the cooling capacity; Q cryocooler represents the cooling capacity of the cryocooler.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,推进剂贮箱表面隔热材料漏热量QMLI的计算公式如下:In the above cost evaluation method for long-term in-orbit evaporation control of low-temperature propellant, the formula for calculating the heat leakage Q MLI of the thermal insulation material on the surface of the propellant tank is as follows:
其中,Thot为贮箱隔热层外侧温度;Tcold为贮箱内部液态低温推进剂温度,Ns为多层隔热材料总层数。Among them, T hot is the outside temperature of the thermal insulation layer of the tank; T cold is the temperature of the liquid low-temperature propellant inside the tank, and N s is the total number of layers of multi-layer thermal insulation materials.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,推进剂贮箱支撑结构的漏热量Qstruts的计算公式如下:In the above cost evaluation method for long-term in-orbit evaporation control of low-temperature propellant, the calculation formula of the heat leakage Q struts of the propellant tank support structure is as follows:
对于液氧推进剂的Qstruts:Q struts for liquid oxygen propellant:
其中:C1为设计余量因子,C2为0.44,Mtank为低温推进剂贮箱重量;Mpropellant为低温推进剂重量;Among them: C 1 is the design margin factor, C 2 is 0.44, M tank is the weight of the cryogenic propellant tank; M propellant is the weight of the cryogenic propellant;
对于液氢推进剂的Qstruts:Q struts for liquid hydrogen propellant:
其中:C'2为0.021。Where: C' 2 is 0.021.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,贮箱管路漏热量Qpenetrations的计算公式如下:In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the calculation formula of Q penetrations of tank pipeline leakage is as follows:
其中:C1为设计余量因子;Thot为贮箱隔热层外侧温度;Tcold为贮箱内部液态低温推进剂温度,Vtank为贮箱体积。Among them: C 1 is the design margin factor; T hot is the temperature outside the thermal insulation layer of the tank; T cold is the temperature of the liquid low-temperature propellant inside the tank, and V tank is the volume of the tank.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,制冷机漏热量Qparastitic的计算公式如下:In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the formula for calculating the leakage heat Q parastitic of the refrigerator is as follows:
其中,为制冷机输入功率,Thot为贮箱隔热层外侧温度;Tcold为贮箱内部液态低温推进剂温度;C1为设计余量因子,C″2为阴影因子。in, is the input power of the refrigerator, T h o t is the temperature outside the insulation layer of the tank; T cold is the temperature of the liquid low-temperature propellant inside the tank; C 1 is the design margin factor, and C″ 2 is the shadow factor.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,低温推进剂排气可利用冷量Qvapor的计算公式如下:In the above cost evaluation method for long-term in-orbit evaporation control of low-temperature propellant, the formula for calculating the available cooling capacity Q vapor of low-temperature propellant exhaust is as follows:
其中,t为在轨时间,cp,T为推进剂在排气出口压力下的比热容,Tvapor_begin为排气出口温度,Tvapor_last为排气可利用冷量利用完之后的温度。Among them, t is the on-orbit time, cp,T is the specific heat capacity of the propellant at the exhaust outlet pressure, T vapor_begin is the exhaust outlet temperature, and T vapor_last is the temperature after the exhaust available cold energy is used up.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,所述步骤(2)中获得不同工况下的低温推进剂蒸发量及蒸发率的具体方法如下:In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of low-temperature propellant, in the step (2), the evaporation of low-temperature propellant under different working conditions is obtained and evaporation rate The specific method is as follows:
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,所述步骤(3)中引入制冷机带来的重量增加包括制冷机自身重量辐射器重量太阳能电池阵重量电子设备重量管路重量和线缆重量 In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the weight increase caused by the introduction of a refrigerator in the step (3) Including the weight of the refrigerator Radiator weight Solar array weight Electronic equipment weight Pipe weight and cable weight
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,制冷机自身重量的计算公式如下:In the above cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the weight of the refrigerator itself The calculation formula is as follows:
其中:Tc为制冷机的冷头温度。Where: T c is the cold head temperature of the refrigerator.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,辐射器重量的计算公式如下:In the above-mentioned cost estimation method for long-term in-orbit evaporation control of cryogenic propellant, the weight of the radiator The calculation formula is as follows:
太阳能电池阵重量的计算公式如下:Solar array weight The calculation formula is as follows:
电子设备重量的计算公式如下:Electronic equipment weight The calculation formula is as follows:
管路重量的计算公式如下:Pipe weight The calculation formula is as follows:
线缆重量的计算公式如下:Cable weight The calculation formula is as follows:
其中:为制冷机输入功率;为制冷机自身重量。in: input power for the refrigerator; is the weight of the refrigerator itself.
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,所述制冷机输入功率的计算公式如下:In the above cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the input power of the refrigerator is The calculation formula is as follows:
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,所述步骤(3)中还包括不同工况下引入的隔热材料重量将同一工况下的 与对应的蒸发量求和得到该工况下的系统重量代价遍历所有工况下的系统重量代价寻找系统重量代价的最小值。In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the step (3) also includes the weight of heat insulating material introduced under different working conditions under the same conditions with the corresponding evaporation Summation to get the system weight penalty under this condition Traverse the weight cost of the system under all operating conditions Find System Weight Costs the minimum value of .
在上述用于低温推进剂长期在轨蒸发量控制的代价评估方法中,隔热材料重量的计算公式如下:In the above-mentioned cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant, the weight of insulating material The calculation formula is as follows:
其中:ρm为多层隔热材料反射屏的平均面密度;tm为反射屏厚度;ρs为多层隔热材料间隔物的平均面密度,ts为间隔物厚度;为多层隔热材料层间密度,Ns为多层隔热材料总层数,A为多层隔热材料面积。Where: ρ m is the average areal density of the multi-layer thermal insulation material reflective screen; t m is the thickness of the reflective screen; ρ s is the average areal density of the multi-layer thermal insulation material spacer, t s is the spacer thickness; is the interlayer density of the multi-layer thermal insulation material, N s is the total number of layers of the multi-layer thermal insulation material, and A is the area of the multi-layer thermal insulation material.
本发明与现有技术相比具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)、本发明全面考虑了低温推进剂长期在轨贮存蒸发量控制系统各组件的漏热量,以及排气可利用冷量,设计了一种在轨蒸发量控制的代价评估方法,该方法首先获取低温推进剂长期在轨贮存系统蒸发量和蒸发率,再获得蒸发量控制措施带来的重量代价,进而获得重量代价最小的最优设计工况,用于指导低温推进剂在轨贮存系统的设计。(1) The present invention comprehensively considers the heat leakage of each component of the low-temperature propellant long-term in-orbit storage evaporation control system and the available cooling capacity of exhaust gas, and designs a cost evaluation method for in-orbit evaporation control. Firstly, the evaporation volume and evaporation rate of the long-term in-orbit storage system of cryogenic propellant are obtained, and then the weight cost brought by the evaporation control measures is obtained, and then the optimal design condition with the smallest weight cost is obtained, which is used to guide the cryogenic propellant in-orbit storage system. the design of.
(2)、本发明以系统重量轻、功率少、可实现性等系统效率指标为优化目标,建立工程评估方法,可有效开展低温推进剂长期在轨蒸发量控制系统分析。(2) The present invention takes system efficiency indicators such as system light weight, low power, and achievability as optimization goals, establishes an engineering evaluation method, and can effectively carry out long-term on-orbit evaporation control system analysis of low-temperature propellants.
(3)、本发明低温推进剂长期在轨蒸发量控制的代价评估方法遍历了所有在轨时间,所有制冷量、所有隔热材料厚度和所有推进剂重量等工况,考虑因素全面,大大提高了评估方法的准确性和可靠性。(3) The cost evaluation method for the long-term on-orbit evaporation control of the low-temperature propellant of the present invention has traversed all the on-orbit time, all the refrigeration capacity, all the thickness of the insulating material and all the propellant weights, etc., considering the factors comprehensively, greatly improving the The accuracy and reliability of the evaluation method.
(4)、本发明低温推进剂长期在轨蒸发量控制的代价评估方法具有高可靠、覆盖性广、精度高等优点。(4) The cost evaluation method for long-term in-orbit evaporation control of low-temperature propellant of the present invention has the advantages of high reliability, wide coverage and high precision.
附图说明Description of drawings
图1为本发明实施例中低温推进剂长期在轨蒸发量控制的代价评估方法流程图。FIG. 1 is a flowchart of a cost evaluation method for long-term in-orbit evaporation control of low-temperature propellant in an embodiment of the present invention.
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明作进一步详细的描述:Below in conjunction with accompanying drawing and specific embodiment, the present invention is described in further detail:
本发明在轨蒸发量控制的代价评估方法的具体实现步骤如下:The concrete realization steps of the cost evaluation method for on-orbit evaporation control of the present invention are as follows:
(一)、低温推进剂长期在轨贮存蒸发量控制系统净漏热量Qloss计算方法:(1) Calculation method for the net heat leakage Q loss of the evaporation control system for long-term in-orbit storage of cryogenic propellants:
根据能量平衡,系统净漏热计算见式(1):According to the energy balance, the calculation of the net heat leakage of the system is shown in formula (1):
Qloss=QMLI+Qstruts+Qparastitic+Qpenetrations-Qvapor-Qcryocooler (1)Q loss =Q MLI +Q struts +Q parastitic +Q penetrations -Q vapor -Q cryocooler (1)
其中:QMLI表示推进剂贮箱表面隔热材料漏热量;Qstruts表示推进剂贮箱支撑结构的漏热量;Qparastitic表示制冷机漏热量;Qpenetrations表示贮箱管路漏热量;Qvapor表示低温推进剂排气可利用冷量;Qcryocooler表示制冷机的制冷量。Among them: Q MLI is the heat leakage of the thermal insulation material on the surface of the propellant tank; Q struts is the heat leakage of the propellant tank support structure; Q parastitic is the heat leakage of the refrigerator ; The cryo-propellant exhaust can utilize the cooling capacity; Q cryocooler represents the cooling capacity of the cryocooler.
推进剂贮箱表面隔热材料漏热量QMLI的计算公式见式(2):The formula for calculating the heat leakage Q MLI of the thermal insulation material on the surface of the propellant tank is shown in formula (2):
其中,Thot为贮箱隔热层外侧温度,单位K;Tcold为贮箱内部液态低温推进剂温度,单位K;Ns为多层隔热材料总层数,例如,Ns取值为10~100。Among them, T hot is the outside temperature of the thermal insulation layer of the tank, in K; T cold is the temperature of the liquid low-temperature propellant inside the tank, in K; N s is the total number of layers of multi-layer thermal insulation materials, for example, N s is the value of 10 to 100.
推进剂贮箱支撑结构的漏热量Qstruts计算基于NASA所研制的支撑隔热结构(PODS)热导率数据:The heat leakage Q struts calculation of the propellant tank support structure is based on the thermal conductivity data of the support insulation structure (PODS) developed by NASA:
对于液氧推进剂的Qstruts的计算公式见式(3):For the calculation formula of Q struts of liquid oxygen propellant, see formula (3):
其中,C1为设计余量因子,例如取值为1~1.2,C2为0.44,Mtank为低温推进剂贮箱重量,单位kg;Mpropellant为低温推进剂重量,单位kg。Among them, C 1 is the design margin factor, for example, the value is 1 to 1.2, C 2 is 0.44, M tank is the weight of the cryogenic propellant tank, the unit is kg; M propellant is the cryogenic propellant weight, the unit is kg.
对于液氢推进剂的Qstruts的计算公式见式(4):For the calculation formula of Q struts of liquid hydrogen propellant, see formula (4):
其中,C1为设计余量因子,例如取值为1~1.2,C'2为0.021。Wherein, C 1 is a design margin factor, for example, it ranges from 1 to 1.2, and C' 2 is 0.021.
贮箱管路漏热量Qpenetrations的计算公式如下The formula for calculating the heat leakage Q penetrations of the tank pipeline is as follows
其中,C1为设计余量因子,例如取值为1~1.1,Vtank为贮箱体积。Among them, C1 is the design margin factor, for example, the value is 1 to 1.1, and V tank is the volume of the tank.
制冷机未工作时通过制冷机进入系统的热量主要基于“Spacecraft ThermalControl Handbook”中AIRS制冷机的数据,制冷机漏热量Qparastitic的计算公式如下:The heat entering the system through the refrigerator when the refrigerator is not working is mainly based on the data of the AIRS refrigerator in the "Spacecraft ThermalControl Handbook". The formula for calculating the leakage heat Q parastitic of the refrigerator is as follows:
其中,C1为设计余量因子,取值1~1.2,C″2为阴影因子(表示飞行器在阴影中时间的比例,制冷机在阴影区时不工作),为制冷机输入功率。Among them, C 1 is the design margin factor, which ranges from 1 to 1.2, and C″ 2 is the shadow factor (representing the proportion of the time the aircraft is in the shadow, and the refrigerator does not work when it is in the shadow area), Input power to the chiller.
低温推进剂蒸发排气可利用冷量Qvapor的计算公式如下:The formula for calculating the available cooling capacity Q vapor for the evaporative exhaust of low-temperature propellant is as follows:
其中,为低温推进剂蒸发量,t为在轨时间,取值1~500;cp,T为推进剂在排气出口压力下的比热容;Tvapor_begin为排气出口温度,Tvapor_last为排气可利用冷量利用完之后的温度。in, is the low temperature propellant evaporation, t is the on-orbit time, and ranges from 1 to 500; c p, T is the specific heat capacity of the propellant under the exhaust outlet pressure; T vapor_begin is the exhaust outlet temperature, and T vapor_last is the exhaust available. The temperature after the cooling capacity is used up.
低温制冷机冷量由其制冷能力决定,这里特指推进剂贮存温度下(饱和温度)对应的低温制冷机制冷量Qcryocooler,取值0~80。The refrigerating capacity of the cryocooler is determined by its refrigerating capacity, here specifically refers to the refrigerating capacity Q cryocooler of the cryocooler corresponding to the storage temperature of the propellant (saturation temperature), which ranges from 0 to 80.
(二)、联立式(1)~(9),根据低温推进剂饱和温度对应蒸发潜热γ和在轨工作时间t,获得不同工况下的净漏热量Qloss、低温推进剂蒸发量及蒸发率i表示不同的工况,i=1,2,……,N,其中N为工况数量;(2) For the simultaneous equations (1) to (9), according to the corresponding latent heat of evaporation γ of the low-temperature propellant saturation temperature and the on-orbit working time t, the net heat leakage Q loss and the low-temperature propellant evaporation under different operating conditions are obtained and evaporation rate i represents different working conditions, i=1, 2, ..., N, where N is the number of working conditions;
(三)、系统代价计算方法(3), system cost calculation method
获得不同工况下引入制冷机带来的重量增加将同一工况下的与对应的蒸发量求和得到该工况下的系统重量代价遍历所有工况下的系统重量代价寻找系统重量代价的最小值。Obtain the weight increase brought by the introduction of the refrigerator under different working conditions under the same conditions with the corresponding evaporation Summation to get the system weight penalty under this condition Traverse the weight cost of the system under all operating conditions Find System Weight Costs the minimum value of .
引入制冷机带来的重量增加包括制冷机自身重量辐射器重量太阳能电池阵重量电子设备重量管路重量和线缆重量 Weight gain due to introduction of chillers Including the weight of the refrigerator Radiator weight Solar array weight Electronic equipment weight Pipe weight and cable weight
即: which is:
根据目前的低温制冷机性能给出不同工况下制冷机自身重量的计算公式如下:According to the current performance of the cryogenic refrigerator, the weight of the refrigerator under different working conditions is given The calculation formula is as follows:
其中:Tc为制冷机的冷头温度。Where: T c is the cold head temperature of the refrigerator.
辐射器重量的计算公式如下:Radiator weight The calculation formula is as follows:
太阳能电池阵重量的计算公式如下:Solar array weight The calculation formula is as follows:
电子设备重量的计算公式如下:Electronic equipment weight The calculation formula is as follows:
管路重量的计算公式如下:Pipe weight The calculation formula is as follows:
线缆重量的计算公式如下:Cable weight The calculation formula is as follows:
其中:为制冷机输入功率;为制冷机自身重量。in: input power for the refrigerator; is the weight of the refrigerator itself.
上述公式中制冷机输入功率计算公式如下:The input power of the refrigerator in the above formula Calculated as follows:
该工况下的系统重量代价表示如下:System weight penalty under this condition It is expressed as follows:
此外该步骤中还包括不同工况下引入的隔热材料重量将同一工况下的与对应的蒸发量求和得到该工况下的系统重量代价遍历所有工况下的系统重量代价寻找系统重量代价的最小值。In addition, this step also includes the weight of the thermal insulation material introduced under different working conditions under the same conditions with the corresponding evaporation Summation to get the system weight penalty under this condition Traverse the weight cost of the system under all operating conditions Find System Weight Costs the minimum value of .
即可以表示如下:which is It can be expressed as follows:
其中隔热材料重量的计算公式如下:The weight of the insulation material The calculation formula is as follows:
其中:ρm为多层隔热材料反射屏的平均面密度;tm为反射屏厚度;ρs为多层隔热材料间隔物的平均面密度,ts为间隔物厚度;为多层隔热材料层间密度,Ns为多层隔热材料总层数,A为多层隔热材料面积。Where: ρ m is the average areal density of the multi-layer thermal insulation material reflective screen; t m is the thickness of the reflective screen; ρ s is the average areal density of the multi-layer thermal insulation material spacer, t s is the spacer thickness; is the interlayer density of the multi-layer thermal insulation material, N s is the total number of layers of the multi-layer thermal insulation material, and A is the area of the multi-layer thermal insulation material.
本实施例中具体取值为:取15~25layers/cm,ρm=0.00881kg/m2;tm=0.0064mm;ρs=0.0073kg/m2,ts=0.13mm;Ns取10~100,A与贮箱表面积相等。The specific values in this embodiment are: Take 15~25layers/cm, ρ m =0.00881kg/m 2 ; t m =0.0064mm; ρ s =0.0073kg/m 2 , t s =0.13mm; N s take 10~100, A is equal to the surface area of the tank .
如图1所示为本发明实施例中低温推进剂长期在轨蒸发量控制的代价评估方法流程图,本发明实施例中根据上述方法获得最优的工况为:对于液氧推进剂,在轨时间大于7天,相比仅采用被动隔热措施而言,增加主动制冷机后具有明显技术优势,系统代价最小。Figure 1 is a flowchart of the cost evaluation method for long-term on-orbit evaporation control of low-temperature propellant in the embodiment of the present invention. In the embodiment of the present invention, the optimal working condition obtained according to the above method is: The rail time is more than 7 days. Compared with only passive heat insulation measures, the addition of active refrigerators has obvious technical advantages and the system cost is the smallest.
以上所述,仅为本发明最佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。The above is only the best specific embodiment of the present invention, but the protection scope of the present invention is not limited to this. Substitutions should be covered within the protection scope of the present invention.
本发明说明书中未作详细描述的内容属于本领域专业技术人员的公知技术。Contents that are not described in detail in the specification of the present invention belong to the well-known technology of those skilled in the art.
Claims (14)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611094101.5A CN106650242B (en) | 2016-12-01 | 2016-12-01 | A cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611094101.5A CN106650242B (en) | 2016-12-01 | 2016-12-01 | A cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106650242A CN106650242A (en) | 2017-05-10 |
CN106650242B true CN106650242B (en) | 2019-06-18 |
Family
ID=58814707
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611094101.5A Active CN106650242B (en) | 2016-12-01 | 2016-12-01 | A cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106650242B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107967012B (en) * | 2017-10-30 | 2020-06-09 | 中国运载火箭技术研究院 | Active control system and control method for "zero evaporation" storage of cryogenic propellant |
-
2016
- 2016-12-01 CN CN201611094101.5A patent/CN106650242B/en active Active
Non-Patent Citations (3)
Title |
---|
低温推进剂长时间在轨的蒸发量控制关键技术分析;胡伟峰等;《低温工程》;20110615(第181期);第59-66页 |
低温推进剂长时间在轨的蒸发量控制技术进展;胡伟峰等;《导弹与航天运载技术》;20091210(第6期);第28-34页 |
低温推进剂长期在轨蒸发量控制分析;张少华等;《中国宇航学会深空探测技术专业委员会第九届学术年会论文集》;20121017;第1068-1073页 |
Also Published As
Publication number | Publication date |
---|---|
CN106650242A (en) | 2017-05-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Zheng et al. | Thermodynamic analysis and comparison of four insulation schemes for liquid hydrogen storage tank | |
Zheng et al. | Thermodynamic modelling and optimization of self-evaporation vapor cooled shield for liquid hydrogen storage tank | |
Hartwig et al. | Comparison of cryogenic flow boiling in liquid nitrogen and liquid hydrogen chilldown experiments | |
Fesmire et al. | Spray-on foam insulations for launch vehicle cryogenic tanks | |
Zheng et al. | Experimental study on composite insulation system of spray on foam insulation and variable density multilayer insulation | |
Zhou et al. | Numerical study on the cooling performance of a novel passive system: Cylindrical phase change material-assisted earth-air heat exchanger | |
Hedayat et al. | Analytical modeling of variable density multilayer insulation for cryogenic storage | |
Plachta et al. | Cryogenic boil-off reduction system testing | |
Meng et al. | Cooling effect analysis on para-ortho hydrogen conversion coupled in vapor-cooled shield | |
CN106650242B (en) | A cost evaluation method for long-term in-orbit evaporation control of cryogenic propellant | |
Sun et al. | A quasi-2D thermodynamic model for performance analysis and optimization of liquid hydrogen storage system with multilayer insulation and vapor-cooled shield | |
Kinefuchi et al. | Cooling system optimization of cryogenic propellant storage on lunar surface | |
Johnson et al. | Tank applied testing of load-bearing multilayer insulation (LB-MLI) | |
Johnson | Thermal performance of cryogenic multilayer insulation at various layer spacings | |
CN110486616B (en) | Low evaporation rate insulated storage system for precooling and cooling of offshore cryogenic liquids | |
Doherty et al. | Cryogenic fluid management technology for moon and mars missions | |
Kittel | Advances in Cryogenic Engineering | |
Johnson et al. | Analysis and testing of multilayer and aerogel insulation configurations | |
Barrios et al. | Thermal conductivity of spray-on foam insulations for aerospace applications | |
Hartwig et al. | Warm pressurant effects on the bubble point for cryogenic liquid acquisition devices | |
Cunnington | Thermodynamic optimization of a cryogenic storage system for minimumboiloff | |
Fesmire et al. | Cryogenic moisture uptake in foam insulation for space launch vehicles | |
Feller et al. | Demonstration of a cryogenic boil-off reduction system employing an actively cooled thermal radiation shield | |
CN115751189A (en) | An integrated thermal management system and method based on deep subcooled cryogenic propellants | |
Chen et al. | Heat transfer behaviors on combinational insulation of spray-on foam and variable density multilayer for cryogenic propellant tanks |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |