CN103755502B - Based on the explosive wastewater formulating of recipe method of dynamic measure and dynamic component dual regulation - Google Patents

Based on the explosive wastewater formulating of recipe method of dynamic measure and dynamic component dual regulation Download PDF

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CN103755502B
CN103755502B CN201410041991.8A CN201410041991A CN103755502B CN 103755502 B CN103755502 B CN 103755502B CN 201410041991 A CN201410041991 A CN 201410041991A CN 103755502 B CN103755502 B CN 103755502B
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component
adjustment
formula
energy characteristics
weight percentage
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CN103755502A (en
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赵宏安
赵凤起
耿国华
徐司雨
关博通
高红旭
王冰
李康
陈林
牛晓霞
雷元元
李志琴
张晓亮
姚沛延
王浩
张玉成
王博
李玉琴
江静
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Northwest University
Xian Modern Chemistry Research Institute
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Northwest University
Xian Modern Chemistry Research Institute
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Abstract

The invention discloses a kind of explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, designed explosive wastewater energy characteristics is n 0~ n 1and design process is as follows: one, basic components is chosen: choose component design based on a basic components from basic components storehouse; Two, energy characteristics judges: energy characteristics n basic design filled a prescription irespectively with n 0and n 1relatively: work as n i> n 1time, enter step 3; Work as n i< n 0time, enter step 4; Otherwise basic design formula is component design; Three, energy characteristics reduces adjustment; Step 4, energy characteristics increase adjustment; Step 3 and four includes capacity control measure grade and to determine and the dual regulation method that adopts capacity control recondition measure adjustment to combine with composition regulation method carries out formula adjustment two steps.The inventive method simple, reasonable in design and realize convenient, result of use is good, can solve the problems such as the cost that existing explosive wastewater formulating of recipe method exists is high, cycle length, repetition experiment number are many.

Description

Based on the explosive wastewater formulating of recipe method of dynamic measure and dynamic component dual regulation
Technical field
The present invention relates to a kind of formulating of recipe method, especially relate to a kind of explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation.
Background technology
Explosive wastewater (explosive), has volatile material, also known as explosive, when its be subject to suitable excite momentum after, chemical reaction fast can be produced, and release enough heats and a large amount of gaseous products, thus form certain physical disturbance effect and throwing effect.Explosive wastewater is divided into priming explosive, high explosive, gunpowder and pyrotechnic composition four class by its character and purposes.Wherein, the main application of priming explosive is the detonator as blast process, is used for exciting high explosive to carry out detonation.The main application of high explosive has sizable stability as the principal charge of various explosive and explosive, under sizable External Force Acting, normally under the exciting of priming explosive, just can cause detonation.The main application of gunpowder is as propelling charge, is used for launch cartridge and shell, and as the fuel of booster rocket, wherein propelling agent belongs to gunpowder.The main application of pyrotechnic composition is the powder charge as star shell, aerosol bomb, incendiary projectile and signal flare, and the tracer material of instruction trajectory.The characteristic that explosive wastewater has, mainly comprise energy characteristics, combustionproperty, blast performance, roadholding and compatibility performance etc., wherein energy characteristics is an important performance indexes of design explosive wastewater formula, and as solid propellant, specific impulse is the energy characteristics index of solid propellant.
At present, the formulating of recipe work of explosive wastewater is with the experimental knowledge of domain expert, completes in conjunction with chemical experiment, wherein there is the shortcomings such as cost is high, the cycle long, repetition experiment number is many.Practical experience is routinely seen, design, debug, and a practical formula of shaping, needs several years time to the more than ten years, and designs a practical formula, also needs long time.Thus, nowadays lack a kind of method steps simple, realize convenient and input cost is low, required time is short based on the explosive wastewater formulating of recipe method of dynamic measure with dynamic component dual regulation, effectively can solve the problems such as the cost that existing explosive wastewater formulating of recipe method exists is high, the cycle long, repetition experiment number is many.
Summary of the invention
Technical problem to be solved by this invention is for above-mentioned deficiency of the prior art, a kind of explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation is provided, its method steps simple, reasonable in design and realize convenient, result of use is good, effectively solves that the cost that existing explosive wastewater formulating of recipe method exists is high, the cycle long, repeat the problems such as experiment number is many.
For solving the problems of the technologies described above, the technical solution used in the present invention is: a kind of explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, is characterized in that: the energy characteristics of designed explosive wastewater is at n 0~ n 1between, n 0for the energy characteristics lower value of designed explosive wastewater, n 1for the energy characteristics higher limit of designed explosive wastewater; This formulating of recipe method comprises the following steps:
Step one, basic components are chosen: from the basic components storehouse set up in advance, choose component design based on the close basic components of the energy characteristics of an energy characteristics and designed explosive wastewater;
Multiple basic components of designed explosive wastewater and the energy characteristics of each basic components is stored in described basic components storehouse; Described basic components comprises kind, weight percentage, minimum design content and the highest design content of preparing designed explosive wastewater multiple ingredient names used and each component, and in described basic components, the weight percentage sum of multiple component is 100%;
Step 2, energy characteristics judge: by the energy characteristics n of basic design formula selected in step one irespectively with n 0and n 1carry out difference comparsion: work as n i> n 1time, enter step 3; Work as n i< n 0time, enter step 4; Work as n 0≤ n i≤ n 1time, formulating of recipe end of processing, the formula of described basic design formula for designing;
Step 3, energy characteristics reduce adjustment, and process is as follows:
Step 301, capacity control measure grade are determined: according to kind and the attribute information of N kind component in the constituent species attribute information base set up in advance of each component in described basic design formula, determine the capacity control measure grade of multiple component in described basic design formula;
Store the attribute information of the N kind component of designed explosive wastewater in described constituent species attribute information base, the attribute information of often kind of component includes kind and the capacity control measure grade of this kind of component; The capacity control measure grade of N kind component arranges from high to low according to the energy characteristics contribution of various component to designed explosive wastewater, and larger to the energy characteristics contribution of designed explosive wastewater, and capacity control measure higher grade; Wherein, N is positive integer and N >=2;
Step 302, the measure of employing capacity control regulate the dual regulation method combined to carry out formula adjustment with component concentration: combine the component attribute information base set up in advance, and according to capacity control measure grade order from high to low, by first to after carry out one or many formula adjustment; The quantity of described component attribute information base is N number of; The component attribute information of N kind component is stored respectively in N number of described component attribute information base; The component attribute information of often kind of component includes the attribute information of the multiple components belonging to this kind together, the attribute information of each component includes the title of this component, contribute energy grade, minimum design content and the highest design content, the contribute energy grade of multiple component arranges from high to low according to the energy characteristics contribution of each component to designed explosive wastewater, and larger to the energy characteristics contribution of designed explosive wastewater, contribute energy higher grade; Actual when carrying out formula adjustment, the formula adjustment method of each capacity control measure grade is all identical, and process is as follows:
Step 3021, capacity control recondition measure adjustment: first the weight percentage of component corresponding for capacity control measure grade current adjusted in described basic design formula is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%; In this step, component corresponding to current adjusted capacity control measure grade is designated as current regulated component;
Step 3022, energy characteristics judge: by the energy characteristics n of formula after adjustment in step 3021 jrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n j≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step 3021 after adjustment; Work as n j< n 0time, enter step 3023, carry out component concentration adjustment by current regulated component; Work as n j> n 1time, enter step 3024, carry out the formula adjustment of next capacity control measure grade;
Step 3023, component concentration regulate: according to minimum design content and the highest design content of current regulated component, first carry out increase and decrease to the weight percentage of current regulated component to regulate, again the weight percentage of remaining ingredient is reduced all in proportion or increased in proportion, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; In this step, after adjustment, in formula, the weight percentage sum of all components is 100%, and the formula of formula for designing after adjustment;
The formula adjustment of step 3024, next capacity control measure grade: according to the method described in step 3021 to step 3023, carries out the formula adjustment process of next capacity control measure grade;
Step 3025, one or many repeating step 3024, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
Step 4, energy characteristics increase adjustment, and process is as follows:
Step 401, capacity control measure grade are determined: according to the method described in step 301, determine the capacity control measure grade of multiple component in described basic design formula;
Step 402, the dual regulation method adopting capacity control recondition measure adjustment to combine with composition regulation method carry out formula adjustment, and process is as follows:
Step 4021, capacity control recondition measure adjustment: first the weight percentage of component corresponding for capacity control measure grade the highest for described basic design formula middle grade is risen to the highest design content, again the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%; In this step, component corresponding to current adjusted capacity control measure grade is designated as current regulated component;
Step 4022, energy characteristics judge: by the energy characteristics n of formula after adjustment in step 4021 krespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n k≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step 4021 after adjustment; Work as n k> n 1time, enter step 4023, carry out component concentration adjustment by current regulated component; Work as n k< n 0time, enter step 4024, carry out composition regulation;
Step 4023, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current the regulated component described in step 4021, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
Step 4024, composition regulation, process is as follows:
Step I, component are changed: according to the kind of current regulated component and the component attribute information of this kind of component, the contribute energy grade of current regulated component is determined, and by the contribute energy more higher leveled grade component stored in the component attribute information of this kind of component, current regulated component is changed, and component after replacing is designated as current regulated component;
Step II, capacity control recondition measure adjustment: first the weight percentage of current regulated component is risen to the highest design content, then the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
In this step, current regulated component is the component after changing in step I;
Step III, energy characteristics judge: by the energy characteristics n of formula after adjustment in step II smaxrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n smax≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step II after adjustment; Work as n smax> n 1time, enter step IV, carry out component concentration adjustment by current regulated component; Work as n smax< n 0time, return step I, carry out composition regulation;
Step IV, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current regulated component, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, it is characterized in that: carry out basic components in step one when choosing, adopt data handler to choose, and from described basic components storehouse, choose an energy indexes and n by difference comparsion 0~ n 1the immediate basic components of this energy design index is filled a prescription as described basic design; Described basic components storehouse, described constituent species attribute information base and multiple described component attribute information base set up by described data handler and it is all stored in data-carrier store, and described data-carrier store connects with described data handler; Carry out in energy characteristics judgement, step 3, carrying out energy characteristics in step 2 to reduce in adjustment and step 4, to carry out the process that energy characteristics increases adjustment, all adopt described data handler to process.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, is characterized in that: designed explosive wastewater is priming explosive, high explosive, gunpowder or pyrotechnic composition.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, it is characterized in that: carry out before basic components chooses in step one, also need to adopt the energy characteristics prediction model of described data handler foundation for carrying out energy characteristics judgement, and described energy characteristics prediction model is the computation model drawing this explosive wastewater energy characteristics according to the formula calculation of designed explosive wastewater; Carry out energy characteristics in step 2, in step 3022, in step 4022 neutralization procedure III when judging, described data handler all first calls described energy characteristics prediction model and carries out energy characteristics estimation.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, is characterized in that: designed explosive wastewater is solid propellant; Energy characteristics is carried out when judging, the energy characteristics n of selected basic design formula in step one in step 2 ifor the specific impulse that selected basic design is filled a prescription; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step 3021 in step 3022 jfor adjusting the specific impulse of rear formula; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step 4021 in step 4022 kfor adjusting the specific impulse of rear formula; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step II in step III smaxfor adjusting the specific impulse of rear formula.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, it is characterized in that: one or many repeating step 3024 in step 3025, and after completing the formula adjustment of the minimum capacity control measure grade of described basic design formula middle grade, the energy characteristics n filled a prescription after adjustment under current state jstill be less than n 0time, enter step 3026, carry out composition regulation; Further, component corresponding for capacity control measure grade minimum for formula middle grade after adjustment under current state is designated as current regulated component;
Step 3026, composition regulation, process is as follows:
Step I, component are changed: according to the kind of current regulated component and the component attribute information of this kind of component, the contribute energy grade of current regulated component is determined, and by the component of the contribute energy lower grade one-level stored in the component attribute information of this kind of component, current regulated component is changed, and component after replacing is designated as current regulated component;
Step II, capacity control recondition measure adjustment: first the weight percentage of current regulated component is risen to the highest design content, then the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
In this step, current regulated component is the component after changing in step I;
Step III, energy characteristics judge: by the energy characteristics n of formula after adjustment in step II tmaxrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n tmax≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step II after adjustment; Work as n tmax> n 1time, enter step IV, carry out component concentration adjustment by current regulated component; Work as n t< n 0time, return step I, carry out composition regulation;
Step IV, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current regulated component, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, is characterized in that: carry out component concentration in step 3023 when regulating, first by the n in step 3022 jwith the n in step 2 irespectively with n 0~ n 1this energy design index compares: draw n when comparing jcloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing icloser to n 0~ n 1during this energy design index, the mode adopting the weight percentage of current regulated component from described basic design formula successively to reduce the weight percentage of current regulated component carries out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
When carrying out component concentration adjustment according to the method described in step 3023 in step 4023, first by the n in step 4022 kwith the n in step 2 irespectively with n 0~ n 1this energy design index compares: draw n when comparing kcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing icloser to n 0~ n 1during this energy design index, the mode adopting the weight percentage of current regulated component from described basic design formula successively to increase the weight percentage of current regulated component carries out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
When carrying out component concentration adjustment according to the method described in step 3023 in step IV, first the weight percentage of component current regulated described in step II is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, the weight percentage sum obtaining all components is fill a prescription after the adjustment of 100%, the energy characteristics n will filled a prescription after adjustment afterwards sminwith the n in step III smaxrespectively with n 0~ n 1this energy design index compares: draw n when comparing smaxcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing smincloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
After each time the weight percentage of current regulated component being increased in step 3023, step 4023 and step IV or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, it is characterized in that: when carrying out component concentration adjustment according to the method described in step 3023 in step IV, first the weight percentage of current regulated component described in step II is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, the weight percentage sum obtaining all components is fill a prescription after the adjustment of 100%, the energy characteristics n will filled a prescription after adjustment afterwards tminwith the n in step III tmaxrespectively with n 0~ n 1this energy design index compares: draw n when comparing tmaxcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing tmincloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
After each time the weight percentage of current regulated component being increased in step IV or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, is characterized in that: in step 3 and step 4 after formulating of recipe end of processing, also need obtained energy characteristics at n 0~ n 1between adjustment after fill a prescription and be added in described basic components storehouse.
The above-mentioned explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation, it is characterized in that: after in step 2, energy characteristics judges, also need one or more components that weight percentage in basic components described in step one can not carry out adjusting to be labeled as non-adjustment component;
When adopting capacity control measure and component concentration to regulate the dual regulation method combined to carry out formula adjustment in step 302, without the need to carrying out formula adjustment to the capacity control measure grade being labeled as non-adjustment component; After the weight percentage of component corresponding for capacity control measure grade current adjusted in described basic design formula being down to minimum design content in step 3021, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
After the weight percentage of component corresponding for capacity control measure grade the highest for described basic design formula middle grade being risen to the highest design content in step 4021, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
After the weight percentage of current regulated component being risen to the highest design content in step II, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
The present invention compared with prior art has the following advantages:
1, method steps simple, reasonable in design and realize convenient.
2, input cost is low and use easy and simple to handle, significantly simplify the formula development process of solid propellant, substantially reduces the formula development cycle, greatly reduce formula development cost.
3, formulating of recipe process can adopt treater automatically to complete, and realizes conveniently, only needing just can complete whole formulating of recipe process the tens seconds time to several minutes.
4, capacity control measure is adopted to regulate the dual regulation method combined to carry out formula adjustment with component concentration, significantly simplify formula adjustment process, actual when carrying out formulating of recipe, first carry out capacity control measure, whether specifically corresponding to current judged capacity control measure grade component can meet design objective judges fast, specifically consider when this component at the highest design content whether can meet the requirement of the capacity control upper limit, consider the requirement that whether can meet capacity control lower limit when its minimal design content simultaneously, if meet design requirement, then component concentration adjustment is carried out to this component, component design can be obtained, as do not met design requirement, then need to carry out component replacing (component is changed to comprise and undertaken changing or changing by the component that contribute energy grade in same capacity control measure grade is more higher or lower than present component by the component that next capacity control measure grade is corresponding), whether can meet design objective to the component after replacing more afterwards to judge fast, if meet design requirement, then component concentration adjustment is carried out to this component, can component design be obtained, as do not met design requirement, then need again to carry out component replacing, until obtain component design.
5, popularizing application prospect extensively and practical value is high, effectively can be suitable for the formulating of recipe process to all explosive wastewater.
In sum, the inventive method step simple, reasonable in design and realize convenient, result of use is good, effectively solves that the cost that existing explosive wastewater formulating of recipe method exists is high, the cycle long, repeat the problems such as experiment number is many.
Below by drawings and Examples, technical scheme of the present invention is described in further detail.
Accompanying drawing explanation
Fig. 1 is method flow block diagram of the present invention.
Embodiment
Embodiment 1
In the present embodiment, a kind of explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation as shown in Figure 1, the energy characteristics of designed explosive wastewater is at n 0~ n 1between, n 0for the energy characteristics lower value of designed explosive wastewater, n 1for the energy characteristics higher limit of designed explosive wastewater; This formulating of recipe method comprises the following steps:
Step one, basic components are chosen: from the basic components storehouse set up in advance, choose component design based on the close basic components of the energy characteristics of an energy characteristics and designed explosive wastewater.
During actual use, designed explosive wastewater is priming explosive, high explosive, gunpowder or pyrotechnic composition.
In the present embodiment, designed explosive wastewater is solid propellant.Further, described solid propellant is modified double base solid propellant.Actual when carrying out formulating of recipe, adopt the present invention also can carry out formulating of recipe to priming explosive, high explosive, pyrotechnic composition and other gunpowder.
Multiple basic components of designed explosive wastewater and the energy characteristics of each basic components is stored in described basic components storehouse.Described basic components comprises kind, weight percentage, minimum design content and the highest design content of preparing designed explosive wastewater multiple ingredient names used and each component, and in described basic components, the weight percentage sum of multiple component is 100%.
Wherein, minimum design content and the highest design content carry out energy characteristics in step 3 to reduce to carry out in energy characteristics increase adjustment process in adjustment and step 4, the reference design content that need use.
Actual when choosing, specifically by the energy characteristics of each basic components that stores in described basic components storehouse respectively with n 0and n 1carry out difference comparsion, and find out an energy indexes closest to n 0basic components or energy indexes closest to n 1basic components based on component design.
In actual mechanical process, also first can find out an energy indexes closest to n 0basic components (being denoted as basic components one) and an energy indexes closest to n 1basic components (being denoted as basic components two), then calculate energy indexes and the n of basic components one 0between difference and the energy indexes of basic components two and n 1between difference, again two differences are compared afterwards, and find out component design based on a less basic components of difference (specifically basic components one or basic components two).
In the present embodiment, design objective and the requirement of designed solid propellant are as follows:
The energy characteristics of designed solid propellant is: specific impulse=2220.00NS/kg ~ 2230.00NS/kg.The low signature of designed solid propellant is smokeless or micro-cigarette.Designed solid propellant is plateau propellant and it fires between ram compression power platform area: 6.00Mpa ~ 9.00Mpa, and this propulsive charge adopts the molded manufacture craft of spiral shell.
That is, n 0=2220.00NS/kg, n 1=2230.00NS/kg.
In the present embodiment, recipe ingredient and the weight percent content of selected basic components are as follows: nitro-cotton (N=12.6%), 52.4%; Nitroglycerine, 34.9%; Ji Na, 8.7%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Hexogen, 1.00%; Lead phthalate (leadphthalatedibasic also claims Dythal), 1.00%; Cupric oxide, 0.50%.Further, energy characteristics (i.e. specific impulse, the specific impulse value specifically under the adiabatic expansion state) n of current selected basic components i=2469.8.
During actual use, the role that nitro-cotton (N=12.6%) is taken in formula is: binding agent and energy matter; Functional description: Energetic binding agent, it is the main mechanical skeleton of single base, double-basis or composite modified double base propellant.
The role that nitroglycerine is taken in formula: softening agent and energy matter; Functional description: nitroglycerine is used for plasticising nitrocotton (i.e. nitro-cotton (N=12.6%)), the two forms double-basis binding agent, bond coated solids component, form propelling agent mechanics skeleton, utilize pressure stretch or build formation propellant charge, nitroglycerine itself or a kind of oxygen enrichment energetic material, in propelling agent except serving as softening agent, also have oxygenizement, even if without special oxygenant in propelling agent, it also can be propelling agent oxidizing fire and provides prerequisite.
Ji is contained in the role taken in formula: containing energy solubility promoter; Functional description: Ji Na is a kind of containing energy solvent, and the high nitrogenous nitrocotton of auxiliary nitroglycerine plasticising, when adopting the nitrocotton of nitrogen content >13.1%, will add Ji Na, usually to improve the plastification of nitroglycerine to nitrocotton.
The role that hexogen (RDX) is taken in formula: high energy single chmical compound explosive; Functional description: hexogen belongs to nitramine class high energy single chmical compound explosive, adds hexogen and contributes to increasing substantially propelling agent energy, and comparatively HMX relative moderate, adding of it can't cause higher temperature rise to metal-powder.
The role that lead phthalate is taken in formula: catalyzer; Functional description: form the effect of low pressure adjustment of combustion rate with graphite (or carbon black) and cupric oxide.
Dimethyldiphenylurea Diphenyldimethylurea (centralite-2), the role's chemical stabilizer taken in formula; Functional description: the decomposition reducing nitro ester, extends powder charge and stablizes storage time.
The role that Vaseline is taken in formula: processing additive; Functional description: Vaseline: the molded process auxiliaries of propellant charge spiral shell or processing additive, lubricate, reduces the rate of catching fire rubbing and cause.
In described basic components, the component of minimum design content=0 is the optional Component of designed explosive wastewater, and the component of minimum design content > is the necessary component of designed explosive wastewater.In the present embodiment, nitro-cotton and nitroglycerine are two necessary components of designed modified double base solid propellant.
Step 2, energy characteristics judge: by the energy characteristics n of basic design formula selected in step one irespectively with n 0and n 1carry out difference comparsion: work as n i> n 1time, enter step 3; Work as n i< n 0time, enter step 4; Work as n 0≤ n i≤ n 1time, formulating of recipe end of processing, the formula of described basic design formula for designing.
In the present embodiment, the energy characteristics n of current selected basic components i> n 1time, then enter step 3.
Step 3, energy characteristics reduce adjustment, and process is as follows:
Step 301, capacity control measure grade are determined: according to kind and the attribute information of N kind component in the constituent species attribute information base set up in advance of each component in described basic design formula, determine the capacity control measure grade of multiple component in described basic design formula.
Store the attribute information of the N kind component of designed explosive wastewater in described constituent species attribute information base, the attribute information of often kind of component includes kind and the capacity control measure grade of this kind of component.The capacity control measure grade of N kind component arranges from high to low according to the energy characteristics contribution of various component to designed explosive wastewater, and larger to the energy characteristics contribution of designed explosive wastewater, and capacity control measure higher grade.Wherein, N is positive integer and N >=2.
Actual when carrying out formulating of recipe, in the various ingredients of described solid propellant, capacity control measure grade is respectively high energy single chmical compound explosive, metal incendiary composition, inert co-solvent, softening agent and alite paste from high to low.
In the present embodiment, in described basic design formula, comprise eight kinds of components such as nitro-cotton (N=12.6%), nitroglycerine, Ji Na, dimethyldiphenylurea, Vaseline, carbon black, hexogen, lead phthalate and cupric oxide.In the present embodiment, in described basic design formula, the capacity control measure grade of each component is respectively high energy single chmical compound explosive (i.e. hexogen), solubility promoter (i.e. Ji Na), softening agent (i.e. nitroglycerine) and alite paste (i.e. nitro-cotton (N=12.6%)) from high to low.
After in step 2, energy characteristics judges, also need one or more components that weight percentage in basic components described in step one can not carry out adjusting to be labeled as non-adjustment component.
In the present embodiment, the components such as dimethyldiphenylurea, Vaseline, carbon black, lead phthalate and cupric oxide are all very little to energy characteristics contribution, and the components such as dimethyldiphenylurea, Vaseline, carbon black, lead phthalate and cupric oxide are all labeled as non-adjustment component.Actually carry out in formulating of recipe process, the weight percentages such as dimethyldiphenylurea, Vaseline, carbon black, lead phthalate and cupric oxide are constant.
Step 302, the measure of employing capacity control regulate the dual regulation method combined to carry out formula adjustment with component concentration: combine the component attribute information base set up in advance, and according to capacity control measure grade order from high to low, by first to after carry out one or many formula adjustment.The quantity of described component attribute information base is N number of.The component attribute information of N kind component is stored respectively in N number of described component attribute information base; The component attribute information of often kind of component includes the attribute information of the multiple components belonging to this kind together, the attribute information of each component includes the title of this component, contribute energy grade, minimum design content and the highest design content, the contribute energy grade of multiple component arranges from high to low according to the energy characteristics contribution of each component to designed explosive wastewater, and larger to the energy characteristics contribution of designed explosive wastewater, contribute energy higher grade.In the present embodiment, in described component attribute information base, the minimum design content of each component and the highest design content carry out energy characteristics in step 3 to reduce to carry out in energy characteristics increase adjustment process in adjustment and step 4, the reference design content that need use.Actual when carrying out formula adjustment, the formula adjustment method of each capacity control measure grade is all identical, and process is as follows:
Step 3021, capacity control recondition measure adjustment: first the weight percentage of component corresponding for capacity control measure grade current adjusted in described basic design formula is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%; In this step, component corresponding to current adjusted capacity control measure grade is designated as current regulated component.
Step 3022, energy characteristics judge: by the energy characteristics n of formula after adjustment in step 3021 jrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n j≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step 3021 after adjustment; Work as n j< n 0time, enter step 3023, carry out component concentration adjustment by current regulated component; Work as n j> n 1time, enter step 3024, carry out the formula adjustment of next capacity control measure grade;
Step 3023, component concentration regulate: according to minimum design content and the highest design content of current regulated component, first carry out increase and decrease to the weight percentage of current regulated component to regulate, again the weight percentage of remaining ingredient is reduced all in proportion or increased in proportion, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; In this step, after adjustment, in formula, the weight percentage sum of all components is 100%, and the formula of formula for designing after adjustment;
The formula adjustment of step 3024, next capacity control measure grade: according to the method described in step 3021 to step 3023, carries out the formula adjustment process of next capacity control measure grade;
Step 3025, one or many repeating step 3024, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
In the present embodiment, carry out energy characteristics in step 2 when judging, the energy characteristics n of selected basic design formula in step one ifor the specific impulse that selected basic design is filled a prescription; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step 3021 in step 3022 jfor adjusting the specific impulse of rear formula.
In the present embodiment, carry out before basic components chooses in step one, also need to adopt the energy characteristics prediction model of described data handler foundation for carrying out energy characteristics judgement, and described energy characteristics prediction model is the computation model drawing this explosive wastewater energy characteristics according to the formula calculation of designed explosive wastewater; Carry out energy characteristics in step 2, in step 3022 neutralization procedure III when judging, described data handler all first calls described energy characteristics prediction model and carries out energy characteristics estimation.
In the present embodiment, described energy characteristics prediction model is theoretical specific impulse computation model, and the theoretical specific impulse computation model set up is in formula: I spfor theoretical specific impulse (Ns/Kg), T cfor chamber temperature (K), P efor engine jet pipe exit pressure (Pa), P cfor pressure in combustion chamber (Pa), for the average molecular mass of gaseous combustion product, R is that universal gas constant (Kgm/molK), k are specific heat ratio and the ratio of its specific heat at constant pressure and specific heat at constant volume, wherein T cwith be according to principle of minimum free energy the thermodynamical coordinate drawn and the quality proportioning of bonding solid propellant converts, P eand P cfor in advance by engine design parameters that described parameter input unit inputs.Wherein, R=8.3144Kgm/molK, k=1.1 ~ 1.3.
In the present embodiment, when adopting capacity control measure and component concentration to regulate the dual regulation method combined to carry out formula adjustment in step 302, without the need to carrying out formula adjustment to the capacity control measure grade being labeled as non-adjustment component; After the weight percentage of component corresponding for capacity control measure grade current adjusted in described basic design formula being down to minimum design content in step 3021, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
In the present embodiment, one or many repeating step 3024 in step 3025, and after completing the formula adjustment of the minimum capacity control measure grade of described basic design formula middle grade, the energy characteristics n filled a prescription after adjustment under current state jstill be less than n 0time, enter step 3026, carry out composition regulation; Further, component corresponding for capacity control measure grade minimum for formula middle grade after adjustment under current state is designated as current regulated component.
Step 3026, composition regulation, process is as follows:
Step I, component are changed: according to the kind of current regulated component and the component attribute information of this kind of component, the contribute energy grade of current regulated component is determined, and by the component of the contribute energy lower grade one-level stored in the component attribute information of this kind of component, current regulated component is changed, and component after replacing is designated as current regulated component.
Step II, capacity control recondition measure adjustment: first the weight percentage of current regulated component is risen to the highest design content, then the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
In this step, current regulated component is the component after changing in step I.
Step III, energy characteristics judge: by the energy characteristics n of formula after adjustment in step II tmaxrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n tmax≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step II after adjustment; Work as n tmax> n 1time, enter step IV, carry out component concentration adjustment by current regulated component; Work as n t< n 0time, return step I, carry out composition regulation.
Step IV, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current regulated component, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
In the present embodiment, when carrying out component concentration adjustment in step 3023, first by the n in step 3022 jwith the n in step 2 irespectively with n 0~ n 1this energy design index compares: draw n when comparing jcloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing icloser to n 0~ n 1during this energy design index, the mode adopting the weight percentage of current regulated component from described basic design formula successively to reduce the weight percentage of current regulated component carries out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
After each time the weight percentage of current regulated component being increased in step 3023 or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
When carrying out component concentration adjustment according to the method described in step 3023 in step IV, first the weight percentage of current regulated component described in step II is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, the weight percentage sum obtaining all components is fill a prescription after the adjustment of 100%, the energy characteristics n will filled a prescription after adjustment afterwards tminwith the n in step III tmaxrespectively with n 0~ n 1this energy design index compares: draw n when comparing tmaxcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing tmincloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
After each time the weight percentage of current regulated component being increased in step IV or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
In the present embodiment, in order to reduce the energy characteristics (i.e. specific impulse) of modified double base solid propellant, first adopt the highest capacity control measure grade to carry out capacity control recondition measure adjustment, wherein, the component that the highest capacity control measure grade is corresponding is hexogen.Because hexogen is the functionality of designed modified double base solid propellant and its minimum design content is 0.00%, thus first the content of hexogen is reduced to 0.00%.The weight percentage of nitroglycerine and nitrocotton is according to the ratio-dependent of 4 ︰ 6, and the weight percentage of Ji Na and nitroglycerine is according to the ratio-dependent of 1 ︰ 4.Formula after adjustment is as follows: nitro-cotton (N=12.6%), 52.91%; Nitroglycerine, 35.27%; Ji Na, 8.82%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Hexogen, 0.00%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2468.3 of current selected basic components.Thus, the energy characteristics n filled a prescription after adjustment j> n 1time, thus need the formula adjustment carrying out next capacity control measure grade.
In order to reduce the energy characteristics (i.e. specific impulse) of modified double base solid propellant further, then adopt next capacity control measure grade to carry out capacity control recondition measure adjustment, wherein, component corresponding to next capacity control measure grade is solubility promoter (i.e. Ji Na).Designed by Ji Nawei modified double base solid propellant functionality and its minimum design content is 0.00%, thus first the content of Ji Na is reduced to 0.00%.The weight percentage of nitroglycerine and nitrocotton is according to the ratio-dependent of 4 ︰ 6, and the weight percentage of Ji Na and nitroglycerine is according to the ratio-dependent of 1 ︰ 4.Formula after adjustment is as follows: nitro-cotton (N=12.6%), 58.20%; Nitroglycerine, 38.80%; Ji Na, 0.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2462.2 of current selected basic components.Thus, the energy characteristics n filled a prescription after adjustment j> n 1time, thus need the formula adjustment carrying out next capacity control measure grade.To sum up, estimate visible through energy: even if the content of Ji Na is adjusted to minimum safe level, the energy characteristics of designed double-basis modification propelling agent is still higher than the index upper limit, and component corresponding to the capacity control measure that energy grade must be adopted lower adjusts further.
In order to reduce the energy characteristics (i.e. specific impulse) of modified double base solid propellant further, next capacity control measure grade is adopted to carry out capacity control recondition measure adjustment again, wherein, the component that next capacity control measure grade is corresponding is softening agent (i.e. nitroglycerine).Because nitroglycerine is the neccessary composition of designed modified double base solid propellant and its minimum design content is 10.00%, thus first the content of nitroglycerine is reduced to 10.00%.The weight percentage of nitroglycerine and nitrocotton is according to the ratio-dependent of 4 ︰ 6, and the weight percentage of Ji Na and nitroglycerine is according to the ratio-dependent of 1 ︰ 4.Formula after adjustment is as follows: nitro-cotton (N=12.6%), 87.00%; Nitroglycerine, 10.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2288.8 of current selected basic components.Thus, the energy characteristics > n filled a prescription after adjustment 1time, thus need the formula adjustment carrying out next capacity control measure grade.To sum up, estimate visible through energy: even if the content of nitroglycerine is adjusted to minimum design content, the energy characteristics of designed double-basis modification propelling agent is still higher than the index upper limit, and component corresponding to the capacity control measure that energy grade must be adopted lower adjusts further.
In order to reduce the energy characteristics (i.e. specific impulse) of modified double base solid propellant further, next capacity control measure grade is adopted to carry out capacity control recondition measure adjustment again, wherein, the component that next capacity control measure grade is corresponding is alite paste (i.e. nitrocotton).In the present embodiment, after the content of nitro-cotton (N=12.0%) is adjusted to minimum design content, after adjustment, the energy characteristics of formula is still higher than the index upper limit.Thus, composition regulation need be carried out.
In the present embodiment, by reducing the nitrogen content in the nitrocotton in current formulation, reduce the object of component design than punching performance to reaching.That is, with nitro-cotton (N=12.0%), nitro-cotton (N=12.6%) is changed.The requirement of raising energy to design objective whether can be met in order to understand current reduction nitrocotton nitrogen content as early as possible, first the content of nitro-cotton (N=12.0%) is adjusted to maximum safe level (i.e. the highest design content): 90.00%, the weight percentage of nitroglycerine is adjusted to 7.00% simultaneously.Formula after adjustment is as follows: nitro-cotton (N=12.0%), 90.00%; Nitroglycerine, 7.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2208.9 of current selected basic components.Thus, the energy characteristics < n filled a prescription after adjustment 0.
Because current formulation energy is on the low side, the strategy of current higher-energy is that the content of nitro-cotton (N=12.0%) is adjusted to minimum design content: 85.00%.Formula after adjustment is as follows: nitro-cotton (N=12.0%), 85.00%; Nitroglycerine, 12.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2245.5 of current selected basic components.Thus, the energy characteristics > n filled a prescription after adjustment 1.To sum up, estimate visible through energy, after the content of nitro-cotton (N=12.0%) is adjusted to 85.00%, the energy characteristics of designed double-basis modification propelling agent is higher than the index upper limit.
Because current formulation energy is higher, current to fall low-energy strategy be that the content of nitro-cotton (N=12.0%) is adjusted to 87.00%.Formula after adjustment is as follows: nitro-cotton (N=12.0%), 87.00%; Nitroglycerine, 10.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2231.0 of current selected basic components.Thus, the energy characteristics > n filled a prescription after adjustment 1.To sum up, estimate visible through energy, after the content of nitro-cotton (N=12.0%) is adjusted to 87.00%, the energy characteristics of designed double-basis modification propelling agent is still higher than the index upper limit.
Because current formulation energy is higher, current to fall low-energy strategy be that the content of nitro-cotton (N=12.0%) is adjusted to 89.00%.Formula after adjustment is as follows: nitro-cotton (N=12.0%), 89.00%; Nitroglycerine, 8.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2216.3 of current selected basic components.Thus, after adjustment, the energy characteristics of formula is in n 0~ n 1between, now formulating of recipe end of processing.
In the present embodiment, the formula designed is: nitro-cotton (N=12.0%), 89.00%; Nitroglycerine, 8.00%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.
In the present embodiment, in step 3 after formulating of recipe end of processing, also need obtained energy characteristics at n 0~ n 1between adjustment after fill a prescription and be added in described basic components storehouse.
In the present embodiment, carry out basic components in step one when choosing, adopt data handler to choose, and from described basic components storehouse, choose an energy indexes and n by difference comparsion 0~ n 1the immediate basic components of this energy design index is filled a prescription as described basic design.Described basic components storehouse, described constituent species attribute information base and multiple described component attribute information base set up by described data handler and it is all stored in data-carrier store, and described data-carrier store connects with described data handler.Carry out energy characteristics in step 2 judge and in step 3, carry out the process that energy characteristics reduces adjustment, all adopt described data handler to process.Thus, intelligence degree of the present invention is very high and use easy and simple to handle, only need adjust design objective, just can complete the formulating of recipe process meeting design objective in tens seconds to several minutes.
Embodiment 2
In the present embodiment, as different from Example 1: the energy characteristics of designed solid propellant is: specific impulse=2580.00NS/kg ~ 2590.00NS/kg.The low signature of designed solid propellant is smokeless or micro-cigarette.Designed solid propellant is plateau propellant and it fires between ram compression power platform area: 6.00Mpa ~ 9.00Mpa, and this propulsive charge adopts the molded manufacture craft of spiral shell; That is, n 0=2580.00NS/kg, n 1=2590.00NS/kg; Energy characteristics is carried out when judging, the energy characteristics n of current selected basic components in step 2 i< n 0time, thus enter step 4.
Step 4, energy characteristics increase adjustment, and process is as follows:
Step 401, capacity control measure grade are determined: according to the method described in step 301, determine the capacity control measure grade of multiple component in described basic design formula.
Step 402, the dual regulation method adopting capacity control recondition measure adjustment to combine with composition regulation method carry out formula adjustment, and process is as follows:
Step 4021, capacity control recondition measure adjustment: first the weight percentage of component corresponding for capacity control measure grade the highest for described basic design formula middle grade is risen to the highest design content, again the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%; In this step, component corresponding to current adjusted capacity control measure grade is designated as current regulated component.
Step 4022, energy characteristics judge: by the energy characteristics n of formula after adjustment in step 4021 krespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n k≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step 4021 after adjustment; Work as n k> n 1time, enter step 4023, carry out component concentration adjustment by current regulated component; Work as n k< n 0time, enter step 4024, carry out composition regulation.
Step 4023, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current the regulated component described in step 4021, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
Step 4024, composition regulation, process is as follows:
Step I, component are changed: according to the kind of current regulated component and the component attribute information of this kind of component, the contribute energy grade of current regulated component is determined, and by the contribute energy more higher leveled grade component stored in the component attribute information of this kind of component, current regulated component is changed, and component after replacing is designated as current regulated component.
Step II, capacity control recondition measure adjustment: first the weight percentage of current regulated component is risen to the highest design content, then the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
In this step, current regulated component is the component after changing in step I.
Step III, energy characteristics judge: by the energy characteristics n of formula after adjustment in step II smaxrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n smax≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step II after adjustment; Work as n smax> n 1time, enter step IV, carry out component concentration adjustment by current regulated component; Work as n smax< n 0time, return step I, carry out composition regulation.
Step IV, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current regulated component, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
In the present embodiment, after the weight percentage of component corresponding for capacity control measure grade the highest for described basic design formula middle grade being risen to the highest design content in step 4021, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
After the weight percentage of current regulated component being risen to the highest design content in step II, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
In the present embodiment, carry out the process that energy characteristics increases adjustment in step 4, adopt described data handler to process.Further, carry out energy characteristics in step 4022 when judging, described data handler all first calls described energy characteristics prediction model and carries out energy characteristics estimation.
In the present embodiment, carry out energy characteristics in step 4022 when judging, the energy characteristics n of formula after adjustment in step 4021 kfor adjusting the specific impulse of rear formula; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step II in step III smaxfor adjusting the specific impulse of rear formula.
In the present embodiment, when carrying out component concentration adjustment according to the method described in step 3023 in step 4023, first by the n in step 4022 kwith the n in step 2 irespectively with n 0~ n 1this energy design index compares: draw n when comparing kcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing icloser to n 0~ n 1during this energy design index, the mode adopting the weight percentage of current regulated component from described basic design formula successively to increase the weight percentage of current regulated component carries out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
When carrying out component concentration adjustment according to the method described in step 3023 in step IV, first the weight percentage of component current regulated described in step II is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, the weight percentage sum obtaining all components is fill a prescription after the adjustment of 100%, the energy characteristics n will filled a prescription after adjustment afterwards sminwith the n in step III smaxrespectively with n 0~ n 1this energy design index compares: draw n when comparing smaxcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing smincloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
After each time the weight percentage of current regulated component being increased in step 4023 and step IV or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
In the present embodiment, whether can meet improve energy to the requirement of design objective to understand current adopted high energy single chmical compound explosive as early as possible, first by hexogen content be adjusted to maximum safe level (i.e. the highest design content).
Because current formulation energy is on the low side, current to carry high-octane strategy be that the content of high energy single chmical compound explosive is brought up to 50.00%, and the formula after adjustment is as follows: nitro-cotton (N=12.6%), 25.64%; Nitroglycerine, 17.09%; Ji Na, 4.27%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Hexogen, 50.00%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2547.8 of current selected basic components.Thus, the energy characteristics < n filled a prescription after adjustment 0.To sum up, estimate visible through energy, after the content of hexogen is adjusted to 50.00%, the energy characteristics of designed double-basis modification propelling agent is still lower than index lower limit.
Thus, need composition regulation be carried out, contribute energy more higher leveled grade single chmical compound explosive must be adopted to be replaced.In the present embodiment, otanitrocubane (octanitrocubane, ONC) is adopted to change hexogen.
In order to whether the single chmical compound explosive after understanding current replacing as early as possible can meet the requirement of raising energy to design objective.First the content of otanitrocubane is adjusted to the highest design content.
Because current formulation energy is on the low side, current to carry high-octane strategy be that the content of high energy single chmical compound explosive is brought up to 50.00%.Formula after adjustment is as follows: nitro-cotton (N=12.6%), 25.64%; Nitroglycerine, 17.09%; Ji Na, 4.27%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Otanitrocubane, 50.00%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2597.6 of current selected basic components.Thus, the energy characteristics > n filled a prescription after adjustment 1.To sum up, estimate visible through energy, after the content of otanitrocubane is adjusted to 50.00%, the energy characteristics of designed double-basis modification propelling agent is higher than the index upper limit.
Because current formulation energy is higher, current to fall low-energy strategy be reduced to by the content of single chmical compound explosive composition (i.e. otanitrocubane): 40.00%.Formula after adjustment is as follows: nitro-cotton (N=12.6%), 31.09%; Nitroglycerine, 20.73%; Ji Na, 5.18%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Otanitrocubane, 40.00%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.Further, the energy characteristics (i.e. specific impulse, the specific impulse value specifically under adiabatic expansion state)=2586.7 of current selected basic components.Thus, the energy characteristics > n filled a prescription after adjustment 1.To sum up, estimate visible through energy, after the content of otanitrocubane is adjusted to 50.00%, the energy characteristics of designed double-basis modification propelling agent is higher than the index upper limit.Thus, after adjustment, the energy characteristics of formula is in n 0~ n 1between, now formulating of recipe end of processing.
In the present embodiment, the formula designed is: nitro-cotton (N=12.6%), 31.09%; Nitroglycerine, 20.73%; Ji Na, 5.18%; Dimethyldiphenylurea, 1.0%; Vaseline, 0.30%; Carbon black, 0.20%; Otanitrocubane, 40.00%; Lead phthalate (leadphthalatedibasic), 1.00%; Cupric oxide, 0.50%.
In the present embodiment, in step 4 after formulating of recipe end of processing, also need obtained energy characteristics at n 0~ n 1between adjustment after fill a prescription and be added in described basic components storehouse.
The above; it is only preferred embodiment of the present invention; not the present invention is imposed any restrictions, every above embodiment is done according to the technology of the present invention essence any simple modification, change and equivalent structure change, all still belong in the protection domain of technical solution of the present invention.

Claims (10)

1., based on an explosive wastewater formulating of recipe method for dynamic measure and dynamic component dual regulation, it is characterized in that: the energy characteristics of designed explosive wastewater is at n 0~ n 1between, n 0for the energy characteristics lower value of designed explosive wastewater, n 1for the energy characteristics higher limit of designed explosive wastewater; This formulating of recipe method comprises the following steps:
Step one, basic components are chosen: from the basic components storehouse set up in advance, choose component design based on the close basic components of the energy characteristics of an energy characteristics and designed explosive wastewater;
Multiple basic components of designed explosive wastewater and the energy characteristics of each basic components is stored in described basic components storehouse; Described basic components comprises kind, weight percentage, minimum design content and the highest design content of preparing designed explosive wastewater multiple ingredient names used and each component, and in described basic components, the weight percentage sum of multiple component is 100%;
Step 2, energy characteristics judge: by the energy characteristics n of basic design formula selected in step one irespectively with n 0and n 1carry out difference comparsion: work as n i> n 1time, enter step 3; Work as n i< n 0time, enter step 4; Work as n 0≤ n i≤ n 1time, formulating of recipe end of processing, the formula of described basic design formula for designing;
Step 3, energy characteristics reduce adjustment, and process is as follows:
Step 301, capacity control measure grade are determined: according to kind and the attribute information of N kind component in the constituent species attribute information base set up in advance of each component in described basic design formula, determine the capacity control measure grade of multiple component in described basic design formula;
Store the attribute information of the N kind component of designed explosive wastewater in described constituent species attribute information base, the attribute information of often kind of component includes kind and the capacity control measure grade of this kind of component; The capacity control measure grade of N kind component arranges from high to low according to the energy characteristics contribution of various component to designed explosive wastewater, and larger to the energy characteristics contribution of designed explosive wastewater, and capacity control measure higher grade; Wherein, N is positive integer and N >=2;
Step 302, the measure of employing capacity control regulate the dual regulation method combined to carry out formula adjustment with component concentration: combine the component attribute information base set up in advance, and according to capacity control measure grade order from high to low, by first to after carry out one or many formula adjustment; The quantity of described component attribute information base is N number of; The component attribute information of N kind component is stored respectively in N number of described component attribute information base; Wherein, N is positive integer and N >=2; The component attribute information of often kind of component includes the attribute information of the multiple components belonging to this kind together, the attribute information of each component includes the title of this component, contribute energy grade, minimum design content and the highest design content, the contribute energy grade of multiple component arranges from high to low according to the energy characteristics contribution of each component to designed explosive wastewater, and larger to the energy characteristics contribution of designed explosive wastewater, contribute energy higher grade; Actual when carrying out formula adjustment, the formula adjustment method of each capacity control measure grade is all identical, and process is as follows:
Step 3021, capacity control recondition measure adjustment: first the weight percentage of component corresponding for capacity control measure grade current adjusted in described basic design formula is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%; In this step, component corresponding to current adjusted capacity control measure grade is designated as current regulated component;
Step 3022, energy characteristics judge: by the energy characteristics n of formula after adjustment in step 3021 jrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n j≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step 3021 after adjustment; Work as n j< n 0time, enter step 3023, carry out component concentration adjustment by current regulated component; Work as n j> n 1time, enter step 3024, carry out the formula adjustment of next capacity control measure grade;
Step 3023, component concentration regulate: according to minimum design content and the highest design content of current regulated component, first carry out increase and decrease to the weight percentage of current regulated component to regulate, again the weight percentage of remaining ingredient is reduced all in proportion or increased in proportion, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; In this step, after adjustment, in formula, the weight percentage sum of all components is 100%, and the formula of formula for designing after adjustment;
The formula adjustment of step 3024, next capacity control measure grade: according to the method described in step 3021 to step 3023, carries out the formula adjustment process of next capacity control measure grade;
Step 3025, one or many repeating step 3024, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
Step 4, energy characteristics increase adjustment, and process is as follows:
Step 401, capacity control measure grade are determined: according to the method described in step 301, determine the capacity control measure grade of multiple component in described basic design formula;
Step 402, the dual regulation method adopting capacity control recondition measure adjustment to combine with composition regulation method carry out formula adjustment, and process is as follows:
Step 4021, capacity control recondition measure adjustment: first the weight percentage of component corresponding for capacity control measure grade the highest for described basic design formula middle grade is risen to the highest design content, again the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%; In this step, component corresponding to current adjusted capacity control measure grade is designated as current regulated component;
Step 4022, energy characteristics judge: by the energy characteristics n of formula after adjustment in step 4021 krespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n k≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step 4021 after adjustment; Work as n k> n 1time, enter step 4023, carry out component concentration adjustment by current regulated component; Work as n k< n 0time, enter step 4024, carry out composition regulation;
Step 4023, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current the regulated component described in step 4021, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
Step 4024, composition regulation, process is as follows:
Step I, component are changed: according to the kind of current regulated component and the component attribute information of this kind of component, the contribute energy grade of current regulated component is determined, and by the contribute energy more higher leveled grade component stored in the component attribute information of this kind of component, current regulated component is changed, and component after replacing is designated as current regulated component;
Step II, capacity control recondition measure adjustment: first the weight percentage of current regulated component is risen to the highest design content, then the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
In this step, current regulated component is the component after changing in step I;
Step III, energy characteristics judge: by the energy characteristics n of formula after adjustment in step II smaxrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n smax≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step II after adjustment; Work as n smax> n 1time, enter step IV, carry out component concentration adjustment by current regulated component; Work as n smax< n 0time, return step I, carry out composition regulation;
Step IV, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current regulated component, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
2. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation according to claim 1, it is characterized in that: carry out basic components in step one when choosing, adopt data handler to choose, and from described basic components storehouse, choose an energy indexes and n by difference comparsion 0~ n 1the immediate basic components of this energy design index is filled a prescription as described basic design; Described basic components storehouse, described constituent species attribute information base and multiple described component attribute information base set up by described data handler and it is all stored in data-carrier store, and described data-carrier store connects with described data handler; Carry out in energy characteristics judgement, step 3, carrying out energy characteristics in step 2 to reduce in adjustment and step 4, to carry out the process that energy characteristics increases adjustment, all adopt described data handler to process.
3., according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation described in claim 1 or 2, it is characterized in that: designed explosive wastewater is priming explosive, high explosive, gunpowder or pyrotechnic composition.
4. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation according to claim 2, it is characterized in that: carry out before basic components chooses in step one, also need to adopt the energy characteristics prediction model of described data handler foundation for carrying out energy characteristics judgement, and described energy characteristics prediction model is the computation model drawing this explosive wastewater energy characteristics according to the formula calculation of designed explosive wastewater; Carry out energy characteristics in step 2, in step 3022, in step 4022 neutralization procedure III when judging, described data handler all first calls described energy characteristics prediction model and carries out energy characteristics estimation.
5., according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation according to claim 3, it is characterized in that: designed explosive wastewater is solid propellant; Energy characteristics is carried out when judging, the energy characteristics n of selected basic design formula in step one in step 2 ifor the specific impulse that selected basic design is filled a prescription; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step 3021 in step 3022 jfor adjusting the specific impulse of rear formula; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step 4021 in step 4022 kfor adjusting the specific impulse of rear formula; Energy characteristics is carried out when judging, the energy characteristics n of formula after adjustment in step II in step III smaxfor adjusting the specific impulse of rear formula.
6. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation described in claim 1 or 2, it is characterized in that: one or many repeating step 3024 in step 3025, and after completing the formula adjustment of the minimum capacity control measure grade of described basic design formula middle grade, the energy characteristics n filled a prescription after adjustment under current state jstill be less than n 0time, enter step 3026, carry out composition regulation; Further, component corresponding for capacity control measure grade minimum for formula middle grade after adjustment under current state is designated as current regulated component;
Step 3026, composition regulation, process is as follows:
Step I, component are changed: according to the kind of current regulated component and the component attribute information of this kind of component, the contribute energy grade of current regulated component is determined, and by the component of the contribute energy lower grade one-level stored in the component attribute information of this kind of component, current regulated component is changed, and component after replacing is designated as current regulated component;
Step II, capacity control recondition measure adjustment: first the weight percentage of current regulated component is risen to the highest design content, then the weight percentage of remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
In this step, current regulated component is the component after changing in step I;
Step III, energy characteristics judge: by the energy characteristics n of formula after adjustment in step II tmaxrespectively with n 0and n 1carry out difference comparsion: work as n 0≤ n tmax≤ n 1time, formulating of recipe end of processing, the formula of formula for designing in step II after adjustment; Work as n tmax> n 1time, enter step IV, carry out component concentration adjustment by current regulated component; Work as n t< n 0time, return step I, carry out composition regulation;
Step IV, component concentration regulate: according to the method described in step 3023, carry out component concentration adjustment by current regulated component, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing.
7. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation described in claim 1 or 2, it is characterized in that: carry out component concentration in step 3023 when regulating, first by the n in step 3022 jwith the n in step 2 irespectively with n 0~ n 1this energy design index compares: draw n when comparing jcloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing icloser to n 0~ n 1during this energy design index, the mode adopting the weight percentage of current regulated component from described basic design formula successively to reduce the weight percentage of current regulated component carries out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
When carrying out component concentration adjustment according to the method described in step 3023 in step 4023, first by the n in step 4022 kwith the n in step 2 irespectively with n 0~ n 1this energy design index compares: draw n when comparing kcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing icloser to n 0~ n 1during this energy design index, the mode adopting the weight percentage of current regulated component from described basic design formula successively to increase the weight percentage of current regulated component carries out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
When carrying out component concentration adjustment according to the method described in step 3023 in step IV, first the weight percentage of component current regulated described in step II is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, the weight percentage sum obtaining all components is fill a prescription after the adjustment of 100%, the energy characteristics n will filled a prescription after adjustment afterwards sminwith the n in step III smaxrespectively with n 0~ n 1this energy design index compares: draw n when comparing smaxcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing smincloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
After each time the weight percentage of current regulated component being increased in step 3023, step 4023 and step IV or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
8. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation according to claim 6, it is characterized in that: when carrying out component concentration adjustment according to the method described in step 3023 in step IV, first the weight percentage of current regulated component described in step II is down to minimum design content, again the weight percentage of remaining ingredient is increased all in proportion, the weight percentage sum obtaining all components is fill a prescription after the adjustment of 100%, the energy characteristics n will filled a prescription after adjustment afterwards tminwith the n in step III tmaxrespectively with n 0~ n 1this energy design index compares: draw n when comparing tmaxcloser to n 0~ n 1during this energy design index, the mode successively reducing the weight percentage of current regulated component from the highest design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing; N is drawn when comparing tmincloser to n 0~ n 1during this energy design index, the mode successively increasing the weight percentage of current regulated component from minimum design content is adopted to carry out formula adjustment, until obtain energy characteristics at n 0~ n 1between adjustment after fill a prescription, formulating of recipe end of processing;
After each time the weight percentage of current regulated component being increased in step IV or reducing, all first the weight percentage of remaining ingredient reduced all in proportion or increase in proportion, obtaining the weight percentage sum of all components is fill a prescription after the adjustment of 100%, then by the energy characteristics of filling a prescription after adjustment respectively with n 0and n 1carry out difference comparsion.
9. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation described in claim 1 or 2, it is characterized in that: in step 3 and step 4 after formulating of recipe end of processing, also need obtained energy characteristics at n 0~ n 1between adjustment after fill a prescription and be added in described basic components storehouse.
10. according to the explosive wastewater formulating of recipe method based on dynamic measure and dynamic component dual regulation described in claim 1 or 2, it is characterized in that: after in step 2, energy characteristics judges, also need one or more components that weight percentage in basic components described in step one can not carry out adjusting to be labeled as non-adjustment component;
When adopting capacity control measure and component concentration to regulate the dual regulation method combined to carry out formula adjustment in step 302, without the need to carrying out formula adjustment to the capacity control measure grade being labeled as non-adjustment component corresponding; After the weight percentage of component corresponding for capacity control measure grade current adjusted in described basic design formula being down to minimum design content in step 3021, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
After the weight percentage of component corresponding for capacity control measure grade the highest for described basic design formula middle grade being risen to the highest design content in step 4021, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is increased all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%;
After the weight percentage of current regulated component being risen to the highest design content in step II, the weight percent content being labeled as all components of non-adjustment component remains unchanged, and unless all components adjusted outside component in remaining ingredient is reduced all in proportion, obtain the formula after adjustment; In formula after adjustment, the weight percentage sum of all components is 100%.
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