CN103087754B - Industrial cracking furnace cracking product value maximization model construction method - Google Patents
Industrial cracking furnace cracking product value maximization model construction method Download PDFInfo
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Abstract
The present invention relates to an industrial cracking furnace cracking product value maximization model construction method. In petrochemical enterprises adopting industrial cracking furnaces as leading production devices, based on steam cracking experiment data, a cracking furnace cracking product yield prediction model is established, and industrial cracking furnace target cracking product mole content data is acquired and is adopted to correct and check the established prediction model, such that a calculation result of the prediction model and an actual operation result of the industrial cracking furnace are the same; and based on the corrected and checked model, a cracking furnace cracking product value maximization model is established, and is adopted to optimize operation of the cracking furnace, such that the total value of petrochemical products produced by the industrial cracking furnace is maximized so as to effectively improve income of the petrochemical production enterprises.
Description
Technical field
The present invention relates to the pyrolyzer of petrochemical complex, more specifically, relate to the optimization method of pyrolyzer operation in petrochemical production device.
Background technology
Petrochemical industry is mainstay of the national economy industry, and petrochemicals (abbreviation petroleum chemicals) widespread use national economy every field, has important to promoting national economic development.The most of intermediates of petrochemical complex and petroleum chemicals are raw material based on low-carbon alkene and aromatic hydrocarbons all.Low-carbon alkene and the raw materials used hydrocarbon of aromatic hydrocarbons account for that petrochemical iy produced always consumes raw material hydrocarbon 3/4ths.Low-carbon alkene is formed primarily of ethene, propylene, divinyl, and aromatic hydrocarbons is formed primarily of benzene,toluene,xylene.In petrochemical industry, except being produced aromatic hydrocarbons by reformation and by except Propylene recovery, butylene, divinyl in catalytic cracking by product, producing various alkene and aromatic hydrocarbons primarily of ethylene unit.Ethylene unit is made up of pyrolyzer and tripping device, and pyrolyzer is the leading production equipment of ethylene unit.
Ethene is most important basic organic chemical raw material, and the ethene of current more than 98% is produced in steam cracking mode by pyrolyzer.Ethene is mainly for the production of petroleum chemicals such as high-pressure polyethylene, low pressure polyethylene, linear low density polyethylene, polyvinyl chloride, oxyethane, ethylene glycol, ethanol, vinylbenzene, acetaldehyde, acetic acid, alpha-olefin, polyvinyl alcohol, ethylene-propylene rubber(EPR).
The petroleum chemicals such as propylene is fine mainly for the production of polypropylene, propylene, phenol, acetone, butanols, octanol, Virahol, vinylformic acid and lipid thereof, propylene oxide, epoxy chloropropane, polypropylene fibre.At present, the propylene of more than 50 ~ 70% is produced with steam cracking by pyrolyzer.
Divinyl is mainly used in generating the petroleum chemicals such as cis-1,4-polybutadiene rubber, styrene-butadiene rubber(SBR), isoprene-isobutylene rubber, chloroprene rubber, polyhutadiene, SBS, ABS resin.At the petrochemical industry initial stage, divinyl is produced primarily of butylene or butane dehydrogenation.At present, the divinyl of more than 90% is produced in steam cracking mode by pyrolyzer.
Iso-butylene is mainly used in isoprene-isobutylene rubber, polyisoprene rubber, methyl methacrylate, polyisobutene, the trimethyl carbinol and auxiliary agent production etc. as basic petrochemical raw material.In recent years, due to as methyl tertiary-butyl ether (MTBE) high speed development, iso-butylene demand is surged.Iso-butylene, except from except refinery and ethylene unit, produces iso-butylene by butane isomerization and dehydrogenation on a small quantity.
Butylene is mainly for the production of petroleum chemicals such as divinyl, cis-butenedioic anhydride, sec-butyl alcohol, heptene, polybutene.Along with the development of linear low density polyethylene, 1-butylene consumption is increasing, becomes butylene main application, and remaining butylene is mainly for the production of stop bracket gasoline additive and civil liquefied gas.
Aromatic hydrocarbons as basic petrochemical raw material mainly comprises benzene,toluene,xylene.
Benzene is mainly for the production of vinylbenzene, hexanaphthene (producing polyamide fibre further), phenol.In addition, benzene also can be used for the production of aniline, alkylbenzene, cis-butenedioic anhydride and the product such as medicine and agricultural chemicals.
Toluene is mainly for the production of benzene, dimethylbenzene.In addition, in solvent, coating, agricultural chemicals, explosive, cresols, tolylene diisocyanate (TDI) etc. are produced, also consume the toluene of a great deal of.
Dimethylbenzene comprises p-Xylol, o-Xylol, m-xylene.As petrochemical materials, p-Xylol consumption is maximum, mainly for the production of terephthalic acid (PTA) and bis--terephthalate (DMT), produce polyester (PET) thus further, on a small quantity for the production of butylene terephthalate (PBT).M-xylene and o-Xylol are mainly used in isomerization and produce p-Xylol, and wherein o-Xylol also can be used for the production of producing phthalic anhydride, coating, solvent, pesticide intermediate.
Ethylene unit is while production ethene, and by-product propylene, butylene, divinyl, aromatic hydrocarbons (benzene,toluene,xylene), become the main source of petrochemical industry basic material.Ethylene unit except producing except ethene, the propylene of 70%, the divinyl of 90%, 30% aromatic hydrocarbons all from the by-product of ethylene unit.With " triolefin " (ethene, propylene, divinyl) and " triphen " (benzene,toluene,xylene) total amount, about 65% from ethylene producing device.
Owing to going back other a large amount of alkene of by-product and aromatic hydrocarbons while steam cracking process production ethene, correspondingly, the inevitable production with multiple intermediates and petroleum chemicals of ethylene production is linked together.Therefore, petrochemical industry always centered by ethylene production, with the leading production equipment of pyrolyzer, the associated enterprises of supporting multiple product processing.The scale of ethylene production, cost, production stability, quality product all will play dominating role to whole associated enterprises.Ethylene unit becomes core production equipment related to the overall situation in petrochemical complex.Pyrolyzer is the faucet device in petrochemical complex, and the operation of pyrolyzer directly will affect the production operation of other petrochemical units.
The temperature of reaction higher (780-870 DEG C) of hydrocarbon vapours cracking, reaction process are strong endothermic processes, and the production run of pyrolyzer consumes a large amount of fuel.Therefore ethylene industry is high energy consumption industry, and Energy consumption of cracking furnace accounts for about 70% of ethylene unit energy consumption.Therefore, optimize pyrolyzer production operation, reduce production cost, improving the economic benefit of manufacturing enterprise, is the difficult problem that petroleum chemical enterprise pays close attention to for many years always.
Pyrolyzer patent business has very important effect in pyrolyzer technical development process, merges the whole world at present form six large pyrolyzer patent business, i.e. LUMMUS, S & M, KBR, TECKNIP, LINDE, SINOPEC through constantly recombinating.Pyrolyzer patent business is based on steam cracking reaction mechanism or steam cracking experimental data, adopt the method establishment such as derivation or mathematical regression industrial pyrolysis furnace simulation software, for predicting yield of cracked product and the cycle of operation etc., as the SPYRO etc. of PYPS, TECHNIP of LUMMUS.Although the numerous pyrolyzer of pyrolyzer patent business Design & reform, but for the operation optimization of pyrolyzer, ASPEN and TECHNIP is only had to propose the prioritization scheme of diene (ethene+propylene) yield at present, utilize the SPYRO software of TECHNIP and the tripping device simulation technique of APSEN and Advanced Control Techniques thereof, optimize pyrolyzer production operation, the mode mainly through the yield improving diene attempts the economic benefit improving manufacturing enterprise.
In split product, diene (ethene and propylene) weight yield is 38 ~ 60%.Besides the ethylene and the propylene, also have other split products, as hydrogen, divinyl, carbon four take out remaining cut, aromatic hydrocarbons (benzene,toluene,xylene), pyrolysis gasoline, Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO etc., all there is certain economic worth or higher economic value added, as divinyl can produce rubber, aromatics production polyester, chemical fibre etc.The market value of petroleum chemicals fluctuates by oil price and the demand-supply relation, and the petroleum chemicals price of the huge market demand and supply is high, and market demand is little and to supply large petroleum chemicals price lower.Therefore, in pyrolyzer production operation process, its petroleum chemicals price of split product that yield is high may not be high, and its petroleum chemicals price of split product that yield is low may not be low.Therefore, pyrolyzer operation optimization only considers that ethene and propene yield effectively can not improve the income of petrochemical complex manufacturing enterprise.
In addition, the Organic Chemicals such as the triolefin triphen that domestic ethylene is produced seldom commercially are bought and sold, the overwhelming majority produces corresponding petroleum chemicals by middle and lower reaches production equipment, as ethene and propylene produce polyolefin resin by manufacture of polyolefins device, divinyl produces rubber by poly-unit, and aromatic hydrocarbons produces polyester and chemical fibre etc. by the device such as extraction plant, polyester.Therefore, the petroleum chemicals market value that domestic petroleum chemical enterprise middle and lower reaches device is produced determines the income of manufacturing enterprise.The production operation of pyrolyzer not only will consider diene, also will consider the total value of all petroleum chemicals that pyrolyzer is produced.The petroleum chemicals total value only making petrochemical production device produce reaches maximum, and could effectively improve like this is the income of petrochemical enterprise.
By improving the economic benefit that diene yield is attempted to realize improving ethylene unit in prior art, but have ignored economic worth or the economic value added of other petroleum chemicals, the actual income that effectively can not improve petrochemical enterprise.In order to overcome the defect of traditional pyrolyzer operation optimization method, adopt from prior art that to improve the method that diene yield increases economic efficiency different, the present invention builds industrial pyrolysis furnace split product value maximization model, for optimizing industrial crack furnace operating, the petroleum chemicals total value that pyrolyzer is produced reaches maximum, thus effectively improves the income of petrochemical enterprise.
The present invention relates to the method for industrial pyrolysis furnace split product value maximization model construction, with in the petrochemical enterprise of the leading production equipment of industrial pyrolysis furnace, cracked product of cracking furnace predictive model is set up based on steam cracking experimental data, then utilize industrial pyrolysis furnace actual motion target split product molar content check predictive model, make predictive model calculated value and industrial pyrolysis furnace actual operating data basically identical; Based on the predictive model of checking, set up industrial pyrolysis furnace split product value maximization model, and for pyrolyzer operation optimization, the petroleum chemicals total value that pyrolyzer is produced reaches maximum.
Concrete technical scheme is as follows:
The present invention relates to the construction process of industrial pyrolysis furnace split product value maximization model, with in the petrochemical enterprise of the leading production equipment of industrial pyrolysis furnace, Mathematical Modeling Methods is adopted to set up cracked product of cracking furnace predictive model based on steam cracking experimental data, then the target split product molar content data gathering industrial pyrolysis furnace actual motion check predictive model, make the calculated value of predictive model and industrial pyrolysis furnace actual operating data basically identical; Based on the predictive model of checking, set up industrial pyrolysis furnace split product value maximization model, and for pyrolyzer operation optimization, the petroleum chemicals total value that pyrolyzer is produced reaches maximum, thus effectively improve the income of petrochemical enterprise.
The construction process of described a kind of industrial pyrolysis furnace split product value maximization model comprises the following steps:
(1) set up predictive model: based on steam cracking experimental data, utilize Mathematical Modeling Methods to set up industrial pyrolysis furnace yield of cracked product predictive model, yield of cracked product can be calculated according to cracking stock physical property, industrial pyrolysis furnace operational condition.(y
i=X (F, S, XOT, COT, P), y
i-represent split product component yield, F-inlet amount, S-thinning ratio, XOT-across section temperature, COT-coil outlet temperature, P-cracking stock physical property);
(2) target split product molar content: under the condition that cracking stock physical property, inlet amount, quantity of steam are constant, in industrial pyrolysis furnace coil outlet temperature (COT) normal operation range, gathered the target split product molar content data of industrial pyrolysis furnace operation by variation COT.The temperature range COT temperature range of adjustment is relevant with cracking stock, the COT of pyrolyzer operate span of control be totally 760-870 DEG C also, cracking stock is different, the temperature range of adjustment is different, the COT of petroleum naphtha controls usually at 810-845 DEG C, the control of lighter hydrocarbons is at 840-870 DEG C, and the control of hydrogenation tail oil or diesel oil is at 780-820 DEG C.Inflation method is as follows, in cracking stock temperature range, selects at least any three different COT temperature spots to run.
(3) check: utilize the target split product molar content data of the industrial pyrolysis furnace obtained by step (2) to check the predictive model obtained by step (1), make the data of the calculated value of the predictive model of check and industrial pyrolysis furnace actual motion basically identical.
(4) set up cracked product of cracking furnace value maximization model: set up cracked product of cracking furnace value maximization model according to the predictive model that step (3) obtains, split product price, cracking stock physical property, pyrolyzer service data can be utilized to calculate the maximum pyrolyzer operational condition of split product (petroleum chemicals) total value.Formula is
V
max=max (V (m)), wherein F-inlet amount, S-thinning ratio, XOT-across section temperature,
COT (m)-coil outlet temperature, P-cracking stock physical property, PR
j-split product component price,
V (m)-split product total value, V
max-split product total value maximum value);
Preferably, the production equipment of described petrochemical enterprise, with the leading production equipment of pyrolyzer, mainly comprises pyrolyzer, tripping device, polyolefin device etc.According to the design of petrochemical enterprise, aromatic extraction unit, styrene device, glycol unit, rubber device, ethylene oxide device, propylene oxide unit, polyester device, chemical fibre device etc. also may be comprised.Petrochemical production device is formed primarily of two portions, one is ethylene unit, form primarily of pyrolyzer and tripping device, next be low-carbon alkene and or aromatic hydrocarbons post-treatment device, at least comprise polyolefin device, also may have the devices such as polyester, chemical fibre, rubber device, post-treatment device product out can directly be sold to market, is exactly so-called petroleum chemicals in this patent; And split product refers to industrial pyrolysis furnace split product (mixture) before separation out.
Preferably, the liquid cracking stock that described cracking stock is produced primarily of oil-gas field or refinery is formed.Liquid cracking stock is primarily of C
4~ C
35stable hydrocarbon form, stable hydrocarbon comprises paraffinic hydrocarbons, naphthenic hydrocarbon, aromatic hydrocarbons.Liquid cracking stock mainly from oil refining apparatus, as tops, petroleum naphtha, diesel oil, hydrogenation tail oil etc.In addition, the generation condensate oil of oilfield process is also good cracking stock.
More preferably, described cracking stock physical property comprises density, grace formula distillation boiling range (ASTM), group composition (PONA), hydrogen richness or carbon content or ratio of carbon-hydrogen, carboloy residue, molecular weight, correlation index (BMCI), refractive index etc., or the detailed component of described cracking stock and content thereof.Cracking stock is primarily of C
4-C
35stable hydrocarbon form.Liquid cracking stock comprises petroleum naphtha, hydrogenation tail oil, diesel oil etc., its component at least reaches hundreds of, therefore utilize its detailed component and content comparatively difficult, usually select density, grace formula to distill boiling range (ASTM), group composition (PONA) etc. as physical parameter.
Preferably, described split product mainly comprises hydrogen, carbon monoxide, carbonic acid gas, methane, ethane, ethene, acetylene, propane, propylene, propine, propadiene, butane, butylene, divinyl, benzene,toluene,xylene, ethylbenzene, vinylbenzene, pyrolysis gasoline (aromatic free), Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO etc.Although the formation of liquid cracking stock differs greatly, and their split product component is substantially identical, only the yield distribution of split product component is different.
Preferably, described petroleum chemicals refer to the product of petrochemical enterprise commercially public offering, as polyethylene, polypropylene, styrene-butadiene rubber(SBR), polyester etc.In addition, the Organic Chemicals that petrochemical enterprise is produced or other products commercially public offering, can be considered petroleum chemicals, as hydrogen, LPG, ethene, propylene, divinyl, benzene,toluene,xylene, vinylbenzene etc.The kind of the petroleum chemicals that petrochemical enterprise is produced depends on design and the production and sales plan of production equipment.If ethene is all for the production of polyethylene and in market with polyethylene product public offering, ethene can not be considered as petroleum chemicals; If part ethene is with industrial chemicals at market public offering, ethene can be considered petroleum chemicals, and other petroleum chemicals by that analogy.
In petrochemical enterprise production equipment, liquid cracking stock from oil refining apparatus or oil-gas field is heated to the splitting gas that low-carbon alkene and aromatic hydrocarbons are rich in the production of high temperature generation steam cracking reaction in pyrolyzer, splitting gas and split product, mainly comprise hydrogen, carbon monoxide, carbonic acid gas, methane, ethane, ethene, acetylene, propane, propylene, propine, propadiene, butane, butylene, divinyl, benzene,toluene,xylene, ethylbenzene, vinylbenzene, pyrolysis gasoline (aromatic free), Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO etc.
Splitting gas forms Organic Chemicals and other raw materials, as hydrogen, fuel gas, ethene, propylene, C-4-fraction (comprising butane, butylene, divinyl), pyrolysis gasoline (containing aromatic hydrocarbons), Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO etc. through the isolation andpurification of tripping device.In tripping device, although the processing flow sequence that different patent business provides is different, as order separation process, the front-end deethanization flow process of LINDE, the predepropanization process of S & W of LUMMUS, but finally all carry out isolation andpurification according to the carbon number of hydrocarbon.Tripping device comprises the devices such as oil scrubber, water wash column, compressor, ice chest, demethanizing tower, deethanizing column, ethylene rectification tower, depropanizing tower, propylene rectification tower, debutanizing tower, carbon two C_3 hydrogenation device.Splitting gas part composition forms raw material, as hydrogen, ethene, propylene, C-4-fraction (comprising butane, butylene, divinyl), pyrolysis gasoline (containing aromatic hydrocarbons) through the separating-purifying of tripping device; Part composition is consumed or recycle, and as carbon monoxide forms fuel gas by methanation device process, methane generates fuel gas by demethanizing tower, and the fuel that fuel gas is used as pyrolyzer is consumed; Carbonic acid gas is absorbed by soda-wash tower; Acetylene, propine and propadiene generate ethene and ethane, propylene and propane through hydrogenator; Ethane, propane form cycle ethane, recycled propane through ethylene rectification tower, propylene rectification tower after purifying, and cycle ethane and recycled propane return pyrolyzer as cracking stock; Pyrolysis gas oil PGO and Pyrolysis fuel oil PFO form oil fuel through oil scrubber.
Ethene produces polyvinyl resin and the rubber of the various trade mark, as high-pressure polyethylene, low pressure polyethylene, linear low density polyethylene, polyvinyl chloride, polyvinyl alcohol, ethylene-propylene rubber(EPR) etc. by polyethylene device.Ethene also for the production of organic products, as oxyethane, ethylene glycol, ethanol, vinylbenzene, acetaldehyde, acetic acid, alpha-olefin etc.
Propylene produces the polypropylene of the various trade mark by polypropylene plant.In addition, propylene is used for producing multiple organic products, the petroleum chemicals such as fine in propylene, phenol, acetone, butanols, octanol, Virahol, vinylformic acid and lipid thereof, propylene oxide, epoxy chloropropane, polypropylene fibre.
C-4-fraction forms divinyl by butadiene extraction unit and carbon four takes out remaining cut, and divinyl can be used for producing various rubber by rubber device, as cis-1,4-polybutadiene rubber, styrene-butadiene rubber(SBR), isoprene-isobutylene rubber, chloroprene rubber, polyhutadiene, SBS, ABS resin etc.; Carbon four is taken out remaining cut and is produced MTBE or LPG by ether-based device.If do not build butadiene extraction unit in petrochemical enterprise, C-4-fraction produces LPG through hydrotreatment usually, or C-4-fraction is sold other petrochemical enterprises having butadiene extraction unit.
Pyrolysis gasoline (containing aromatic hydrocarbons) by gasoline hydrogenation device and aromatic extraction unit production C5 fraction, benzene,toluene,xylene, carbon more than nine cut, the product such as to raffinate oil, C5 fraction through being separated further, purifying, polymerization can produce the resin such as cyclopentadiene, isoprene.Benzene can be used for the production of producing vinylbenzene, hexanaphthene (producing polyamide fibre further), phenol, aniline, alkylbenzene, cis-butenedioic anhydride and the product such as medicine and agricultural chemicals; Toluene is produced benzene by de-alkyl device or is produced dimethylbenzene and benzene by transalkylation unit, also can be used for producing solvent, coating, agricultural chemicals, explosive, cresols, tolylene diisocyanate (TDI).Dimethylbenzene is by the production etc. of the devices such as isomerization for the production of p-Xylol, terephthalic acid (PTA) and bis--terephthalate (DMT), polyester (PET), chemical fibre, butylene terephthalate (PBT), phthalic anhydride, coating, solvent, pesticide intermediate; Carbon more than nine cut is generally used for the raw material of compressor washing oil or toluene disproportionation; Can be used as cracking stock more than taking out, also can be used for producing sherwood oil or being used as gasoline sales.If do not build the device such as pyrolysis gasoline hydrogenation and Aromatics Extractive Project in petrochemical enterprise, pyrolysis gasoline (containing aromatic hydrocarbons) usually external disclosure is sold.
Pyrolysis gas oil PGO and Pyrolysis fuel oil PFO can be produced oil fuel or be used as to produce the raw material of the products such as naphthalene.
The Organic Chemicals that domestic ethylene is produced seldom commercially is sold, and is usually transported to middle and lower reaches device and produces the petroleum chemicals such as resin, rubber.Therefore, the kind quantity of petroleum chemicals depends on design and the production program arrangement of petrochemical enterprise production equipment usually, and the sale of the petroleum chemicals that the income of the petrochemical enterprise overwhelming majority is produced from middle and lower reaches device.Therefore, the difference of the production equipment design of petrochemical enterprise middle and lower reaches, the petroleum chemicals of production also exist certain difference.
Preferably, described split product price depends on whether split product component can form petroleum chemicals and the selling price thereof of market sale through petrochemical production device.There is steam cracking reaction and produce splitting gas (split product) in cracking stock, split product itself does not have price, but split product forms through petrochemical production device the petroleum chemicals commercially sold has certain value in pyrolyzer.Therefore, fail to be formed the split product component of the petroleum chemicals commercially sold through petrochemical production device, its price is set to zero, as methane, carbon monoxide, carbonic acid gas, ethane, propane etc.; Form the cracking component of the petroleum chemicals commercially sold through petrochemical production device, its price is the market value of these petroleum chemicals.As can be seen here, by split product price and petroleum chemicals price, its split product price is made to reach maximum, even if the petroleum chemicals total price that pyrolyzer is produced reaches maximum by optimizing pyrolyzer operation.
In split product, the height of split product component price depends on the market value of its petroleum chemicals produced by petrochemical unit.For acetylene, propine and propadiene, they generate ethene and ethane, propylene and propane through hydrogenation, its price is transformation efficiency and the optionally product of ethene and propylene price and hydrogenation catalyst, lacking hydrogenation catalyst transformation efficiency and optionally under condition, its price can be considered the price of ethene and propylene; Form a kind of split product component of petroleum chemicals through petrochemical production device, its price is the petroleum chemicals price that this component is formed, as hydrogen, Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO; Form the split product component of multiple petroleum chemicals through petrochemical production device, its price can calculate in the following manner:
Wherein P
irepresent the price of split product component, x
jrepresent the market value of petroleum chemicals, w
jrepresent that this split product component is for the production of the part by weight shared by these petroleum chemicals.After establishment split product price, in fact split product price is exactly petroleum chemicals price.
Optimize for pyrolyzer production operation, key is cracked product of cracking furnace value maximization model.Cracked product of cracking furnace value maximization model is for optimizing the production operation of pyrolyzer, and the split product total value that pyrolyzer is produced reaches maximum.By cracked product of cracking furnace value maximization model, the operation optimization of pyrolyzer is associated with petroleum chemicals market value.
The construction process of a kind of industrial pyrolysis furnace split product value maximization model of the present invention, industrial pyrolysis furnace split product predictive model is set up based on steam cracking experimental data, the target split product molar content of industrial pyrolysis furnace actual motion is utilized to check predictive model, then check model is utilized to set up industrial pyrolysis furnace split product value maximization model, use it for pyrolyzer operation optimization, the market value summation of the petroleum chemicals that industrial pyrolysis furnace is produced reaches maximum, thus improves the income of petrochemical complex manufacturing enterprise.
Preferably, described industrial pyrolysis furnace split product value maximization model is based on yield of cracked product of cracking furnace predictive model, according to physical property, pyrolyzer service data, the split product price of cracking stock, in pyrolyzer operational condition restriction range, adopt Mathematics Optimization Method to search for or calculate the operational condition of the maximum correspondence of split product total value.
More preferably, described industrial pyrolysis furnace service data is feedstock amount, dilution steam generation amount or thinning ratio, across section temperature (XOT), the operational condition of optimization is coil outlet temperature (COT).Cracking stock is different, and the COT operation span of control of pyrolyzer is also different, and the COT as petroleum naphtha controls usually at 810-845 DEG C, and the control of hydrogenation tail oil or diesel oil is at 780-820 DEG C.In the optimizing process of cracked product of cracking furnace value maximization, COT necessarily controls within normal operating restraint, if the COT optimized exceedes the upper limit of normal running or rolls off the production line, can select the upper limit or operation of rolling off the production line when optimizing and revising COT.
More preferably, described cracking stock physical property comprises density, grace formula distillation boiling range (ASTM), group composition (PONA), hydrogen richness or carbon content or ratio of carbon-hydrogen, carboloy residue, molecular weight, correlation index (BMCI), refractive index etc., or the detailed component of described cracking stock and content thereof.Cracking stock is primarily of C
4-C
35stable hydrocarbon form.Liquid cracking stock comprises petroleum naphtha, hydrogenation tail oil, diesel oil etc., its component at least reaches hundreds of, therefore utilize its detailed component and content comparatively difficult, usually select density, grace formula to distill boiling range (ASTM), group composition (PONA) etc. as physical parameter.
More preferably, the Mathematics Optimization Method in described cracked product of cracking furnace Maximum Value model comprises searching method.
More preferably, yield of cracked product of cracking furnace predictive model distributes for the yield of cracked product of analog calculation pyrolyzer, can calculate the yield of split product according to cracking stock physical property and pyrolyzer operational condition.Based on steam cracking reaction mechanism, pyrolyzer patent business releases commercial pyrolyzer simulation software, can the yield of cracked product of analog calculation pyrolyzer, as the SPYRO software of TECHNIP, the PYPS software etc. of LUMMUS.Based on steam cracking testing data, yield of cracked product of cracking furnace predictive model can be set up by Mathematical Modeling Methods.Steam cracking experiment can be implemented on small testing device or simulating-estimating device or industrial pyrolysis furnace, for the industrial pyrolysis furnace type of furnace and operational condition scope, the steam cracking reaction process of simulation cracking stock and experimental data, experimental data comprises cracking stock physical property, operational condition, yield of cracked product.Sinopec Beijing Chemical Research Institute establishes steam cracking evaluation experimental device, can the yield of cracked product of industrial pyrolysis furnace of the various cracking stock of Simulation evaluation.
Still more preferably, described Mathematical Modeling Methods comprises the methods such as SVMs (SVM), artificial neural network, Multiple Non Linear Regression, genetic algorithm.Steam cracking experimental data is divided into two portions, and a part is used for training pattern, and a part is used for the precision of prediction of testing model.By the kernel function in adjustment Mathematical Modeling Methods, the model miscalculation of foundation is at least reached within 10%, preferably within 5%.Predictive model input variable cracking stock physical property, the operational condition set up, output variable is the yield of split product, that is:
y
i＝X(F，S，XOT，COT，P)
Wherein y
i-represent split product component yield
F-inlet amount
S-thinning ratio
XOT-is across section temperature
COT-coil outlet temperature
P-cracking stock physical property
Preferably, described target split product molar content is under the constant condition of cracking stock physical property, inlet amount, quantity of steam, within pyrolyzer COT operating restraint, the split product component that its molar content raises along with COT and increases or reduce, mainly comprises hydrogen, methane, ethene, acetylene, propane, butane, butylene, benzene,toluene,xylene etc.Target split product molar content can on-line measurement or off-line analysis obtain.No matter off-line or online, all need to do a thief hole in quenching boiler outlet, thief hole is connected with water cooler.When opening thief hole, splitting gas is cooled to 0-40 DEG C and forms gas-liquid two-phase, then utilizes the instrumental analysis such as industrial on-line chromatograph to obtain the molar content of the target split product in the logistics of gas phase or liquid phase.Chinese patent CN1456895A is described in detail off-line sampling unit and method, and CN2519911Y, CN201173877Y are described in detail industrial on-line chromatograph and device thereof.Because industrial on-line chromatograph is extensive at olefin production Application comparison, can mole composition content of hydrogen, methane, ethane, ethene, propane, propylene in analytical pyrolysis gas, and in liquid phase substantially containing above-mentioned composition, therefore utilize on-line chromatograph analyze methane in gas phase, ethene, propane molar content calibration model more for convenience, also can utilize the molar content of the gas phases such as HP7890, HP6850 and liquid-phase chromatographic analysis wherein target split product.
Preferably, described target split product molar content data are under the constant condition of cracking stock physical property, inlet amount, quantity of steam, in industrial pyrolysis furnace coil outlet temperature (COT) normal operation range, by its cracking severity data run of adjustment industrial pyrolysis furnace at least three COT temperature acquisitions.
More preferably, preferred five COT temperature.
In industrial pyrolysis furnace operational process, the thermopair measuring COT usually inserts or is bundled in waste heat boiler entrance, and waste heat boiler entrance and crack furnance radiation section furnace tube exist an isolation section between exporting.In addition thermopair itself has certain measuring accuracy and thermopair also exists systematic error in measuring process, and the true temperature that the COT usually causing industrial pyrolysis furnace to show and radiant coil export also exists certain temperature difference.
Preferably, described cracked product of cracking furnace predictive model check method is the operational objective split product molar content data based on collecting industrial pyrolysis furnace, target split product molar content under utilizing the predictive model set up to calculate industrial pyrolysis furnace collection target split product molar content data manipulation condition, and then the cracking severity calculated under different COT condition, then by comparing calculation value and actual motion value, find out predictive model and the actual temperature difference indicated between COT, then the temperature difference is put into predictive model, make the data of the calculated value of the predictive model of check and industrial pyrolysis furnace actual motion basically identical.
More preferably, described data are basically identical be calculated value and actual motion value deviation within 10%, and numerical value change rule is consistent.
Preferably, cracked product of cracking furnace value maximization model is based on cracked product of cracking furnace predictive model, adopt Mathematics Optimization Method, under the condition that inlet amount, water-oil ratio, XOT, cracking stock physical property, split product price are constant, in the COT normal operation range of industrial pyrolysis furnace, calculate the COT that split product total value maximum value is corresponding, that is:
V
max＝max(V(m))
Wherein, F-inlet amount
S-thinning ratio
XOT-is across section temperature
COT (m)-coil outlet temperature
P-cracking stock physical property
PR
j-split product component price
V (m)-split product total value
V
max-split product total value maximum value.
More preferably, described Mathematics Optimization Method comprises average search method.
The present invention is based on steam cracking experimental data and set up industrial pyrolysis furnace split product predictive model, the cracking severity data of industrial pyrolysis furnace actual motion are utilized to check predictive model, set up cracked product of cracking furnace value maximization model based on the predictive model of checking and operate for optimizing pyrolyzer, the petroleum chemicals market total price that pyrolyzer is produced reaches maximum, thus effectively improves the income of petrochemical enterprise.
Summary of the invention
Accompanying drawing explanation
Fig. 1 is that in embodiment 1, CBL-III pyrolyzer price maximizes the result figure optimized;
Fig. 2 is that in embodiment 2, GK-V pyrolyzer price maximizes the result optimized
To be illustrated in conjunction with embodiment
Embodiment
The present invention is further described below in conjunction with embodiment.The present invention includes but be not limited to the content involved by these embodiments.
Certain petrochemical enterprise has production equipment by ethylene unit, glycol unit, ethylene oxide device, polyethylene device, polypropylene plant, aromatic extraction unit, toluene dealkylation device, PTA device, PET production device, polyester device (staple fibre), LPG device.Ethylene unit has 6 pyrolyzer, and tripping device adopts the order separating technology of LUMMUS, and yearly capacity reaches 360,000 tons.Pyrolyzer has 5 for GK-V pyrolyzer, and 1 is CBL-III type pyrolyzer, and pyrolyzer operational condition is in table 1.
CBL-III pyrolyzer is the pyrolyzer adopting Sinopec self owned development technique to build, and is used widely in Sinopec olefin plant.CBL-III type pyrolyzer adopts 32 groups of 2-1 boiler tubes, and divide four to organize charging greatly, have 4 conventional quench boilers, cracking stock is hydrogenation tail oil, produces ethene 60,000 tons per year.
GK-V type pyrolyzer is by the industrial pyrolysis furnace of TECKNIP company designs, adopts 32 groups of 2-1 configuration boiler tubes, and divide four to organize charging greatly, have two conventional quench boilers, cracking stock is petroleum naphtha or lighter hydrocarbons.
Table 1 pyrolyzer operational condition
| The type of furnace | CBL-III | GK-V |
| Raw material | Hydrogenation tail oil | Petroleum naphtha |
| Inlet amount (ton/hour) | 24.537 | 24.788 |
| Thinning ratio | 0.8 | 0.633 |
| XOT(℃) | 570 | 633 |
| COT(℃) | 804 | 825 |
Petroleum chemicals mainly comprise polyethylene, oxyethane, ethylene glycol, polypropylene, LPG, purified petroleum benzin, p-Xylol, pure terephthalic acid, oil fuel, polyester slice, terylene (staple fibre).According to the petroleum chemicals market value historical data that this petroleum chemical enterprise sells, select in certain period that petroleum chemicals selling price is for the value maximization operation optimization of pyrolyzer, petroleum chemicals market value refers to table 2.
Table 2 petroleum chemicals market value (yuan/ton)
According to petrochemical production device flow process, the price determining split product refers to table 3, and method is specific as follows:
(1) hydrogen is mainly for oil refining apparatus and hydrogenation unit, not for sale in market, and its price is 0;
(2) methane, carbon monoxide, carbonic acid gas, ethane, propane are consumed by production equipment or absorb, and its price is 0;
(3) ethene is for the production of high-pressure polyethylene, low pressure polyethylene, linear polyethylene, ethylene glycol, oxyethane, its part by weight is respectively 30%, 20%, 20%, 15%, 15%, the price of ethene is made up of the market value of these five kinds of petroleum chemicals, that is:
Ethene price=Market of High Pressure Polyethylene price × 30%+ low pressure polyethylene market value × 20%+ linear polyethylene market value × 20%+ ethylene glycol market value × 15%+ oxyethane market value × 15%.
(4) acetylene, propine and propadiene generate ethene and ethane, propylene and propane through the hydrogenation unit of separation system, due to selectivity of catalyst and transformation efficiency all very high (more than 95%), its price is substantially identical with ethene, propylene price;
(5) propylene is for the production of polypropylene, and its price is polyacrylic market value;
(6) C-4-fraction is sold as LPG in market after hydrogenation, and its price is the market value of LPG;
(7) benzene is for the production of purified petroleum benzin, and its price is the market value of purified petroleum benzin;
(8) toluene is for the production of benzene, and its price is the market value of purified petroleum benzin;
(9) dimethylbenzene is for the production of p-Xylol, pure terephthalic acid, polyester slice, terylene, and its price is made up of these four kinds of petroleum chemicals market value, that is:
Dimethylbenzene price=p-Xylol market value × 40%+ essence p-Xylol market value × 30%+ polyester market value × 15%+ terylene market value × 15%;
(10) pyrolysis gasoline mix with petroleum naphtha be used as cracking stock return pyrolyzer, its price is 0;
(11) ethylbenzene, vinylbenzene mix as cracking stock with petroleum naphtha with pyrolysis gasoline, and its price is 0;
(12) Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO are used for oil fuel commercially public offering, and its price is the market value of oil fuel.
Table 3 split product price (yuan/ton)
Embodiment 1
According to CBL-III type pyrolyzer, set up CBL-III type pyrolyzer steam cracking hydrogenation tail oil split product value maximization model, modeling process is as follows.
1 steam cracking experimental data
For CBL-III industrial pyrolysis furnace and operational condition, gather multiple hydrogenation tail oil respectively and implement steam cracking experiment at Sinopec Beijing Chemical Research Institute steam cracking Simulation device, the yield of cracked product of hydrogenation tail oil under different operating condition is calculated by material balance and logistics compositional analysis, gather experimental data and set up CBL-III pyrolyzer steam cracking reaction sample database, data-base content comprises hydrogenation tail oil (proportion, ASTM boiling range, group composition), operational condition (inlet amount, water-oil ratio, XOT, COT), yield of cracked product.Associated steam experimental analysis instrument and equipment is as follows:
(1) hydrogenation tail oil density (60 DEG C) measured by ANTON PEAR company DE40 specific gravity hydrometer;
(2) German Haier tide company HDA627 analyzes hydrogenation tail oil grace formula distillation boiling range (ASTM) (initial boiling point, 10%, 30%, 50%, 70%, 90%, final boiling point);
(3) U.S.'s Agilent company HP6850 analysis hydrogenation tail oil group composition (paraffinic hydrocarbons, naphthenic hydrocarbon, aromatic hydrocarbons) and liquid-phase pyrolysis product form and weight content;
(4) U.S.'s Agilent company HP7890 analytical pyrolysis gas composition and molar content thereof.
2. set up CBL-III type cracked product of cracking furnace predictive model
Sample database is divided into two portions, and wherein a part is training data, and its data volume is 2/3rds of sample database amount, and remaining data is check data.Training data is inputted in BP neural network, set up yield of cracked product of cracking furnace predictive model.BP neural network kernel function adopts RBF kernel function, mode input variable hydrogenation tail oil physical property (proportion, ASTM boiling range, group composition), operational condition (throwing oil mass, water-oil ratio, COT, XOT), output variable is the yield of all split products.Yield of cracked product of cracking furnace predictive model calculates the numerical value of corresponding output variable according to input variable, that is:
y
i＝X(F，S，XOT，COT，DEN，ASTM，PONA)
Wherein y
i-represent split product component yield
F-inlet amount
S-thinning ratio
XOT-is across section temperature
COT-coil outlet temperature
DEN-density
ASTM-ASTM boiling range
PONA-group composition
3. gather CBL-III type industrial pyrolysis furnace operational objective split product molar content data
The target split product molar content data of CBL type pyrolyzer are obtained by industrial on-line chromatograph device analysis, and target split product is hydrogen.The VISTAII PGC2000 type that industrial chromatography adopts ABB AB to manufacture.The hydrogenation tail oil physical property of CBL type pyrolyzer cracking is in table 4.Keep that inlet amount is 24.537 tons/hour, water-oil ratio is 0.8 constant, COT is adjusted to 794 DEG C, 804 DEG C, 818 DEG C respectively, utilize the molar content of the hydrogen in industrial on-line analysis splitting gas simultaneously, and obtain the hydrogen molar content (referring to table 5) of industrial pyrolysis furnace actual motion with this.
Table 4 hydrogenation tail oil physical property
Hydrogen molar content in the splitting gas that the industrial on-line chromatograph of table 5 is analyzed
| COT(℃) | 794 | 804 | 818 |
| Content (mol%) | 7.56 | 7.86 | 8.42 |
4. Model Checking
Bring industrial pyrolysis furnace service data into predictive model and carry out multiple COT temperature hydrogen molar yield calculate, wherein gas phase is formed primarily of hydrogen, methane, ethane, ethene, acetylene, propane, propylene, propine and propadiene, butane, butylene, divinyl, carbon five, their weight yield can be calculated by predictive model, then gas phase molar yield is calculated according to their Molecular weights, obtain comparing the COT temperature of coincideing with industrial data, calculation result refers to table 6.By contrast table 6 and table 5 known, calculated value and industrial crack runtime value deviation are less than within 10% and along with the rising cracking severity of COT and reduce, as can be seen here, high 10 DEG C than predictive model of the COT displays temperature of industrial pyrolysis furnace actual motion, the COT therefore in predictive model adds 10 DEG C and checks predictive models.
The hydrogen molar content that table 6 predictive model calculates
| COT(℃) | Content (mol%) |
| 784 | 7.74 |
| 794 | 7.99 |
| 808 | 8.52 |
5. set up CBL-III cracked product of cracking furnace value maximization model
Based on cracked product of cracking furnace predictive model, adopt the mathematical method of average search method, under the condition that inlet amount, water-oil ratio, XOT, cracking stock physical property (proportion, ASTM boiling range, group composition), split product price are constant, in the COT normal operation range of industrial pyrolysis furnace, search out the COT that steam cracking product total value maximum value is corresponding, that is:
V
max＝max(V(m))
Wherein, F-inlet amount
S-thinning ratio
X-yield of cracked product
XOT-is across section temperature
COT-coil outlet temperature
DEN-density
ASTM-ASTM boiling range
PONA-group composition
P
j-split product component price
V (m)-split product total value
V
max-split product total value maximum value
6. be worth and optimize
According to the operation of the CBL-III cracked product of cracking furnace value maximization model optimization pyrolyzer set up.The physical property of CBL-III pyrolyzer Hydrocracking tail oil is in table 4, and pyrolyzer service data is in table 1.By in split product price (see table 3), cracking stock physical property, service data (inlet amount, thinning ratio, XOT, in table 1) input CBL-III cracked product of cracking furnace value maximization model, calculation result is shown in Fig. 1.
As shown in Figure 1, under aforesaid operations and split product price condition, within the scope of the true COT of hydrogenation tail oil normal running (780-820 DEG C), the true COT of CBL-III cracked product of cracking furnace value maximization is 820 DEG C (pyrolyzer operation COT displays temperature is 830 DEG C), and the petroleum chemicals total value of production is 108105.1 yuan/hour; The operation COT being worth pyrolyzer before optimizing is 804 DEG C, and true COT temperature is 794 DEG C, and the petroleum chemicals total value of production is 106072.4 yuan/hour.CBL-III pyrolyzer COT brings up to 830 DEG C by 804 DEG C, and petroleum chemicals (split product) total value that pyrolyzer is produced adds 2032.7 yuan/hour.
Embodiment 2
According to the GK-V type pyrolyzer type of furnace, set up GK-V type pyrolyzer steam cracking naphtha cracking product value maximization model, modeling process is as follows.
1 steam cracking experimental data
For GK-V industrial pyrolysis furnace and operational condition, gather multiple petroleum naphtha respectively and implement steam cracking experiment at Sinopec Beijing Chemical Research Institute steam cracking Simulation device, the yield of cracked product of petroleum naphtha under different operating condition is calculated by material balance and logistics compositional analysis, gather experimental data and set up GK-V pyrolyzer steam cracking reaction sample database, data-base content comprises petroleum naphtha (proportion, ASTM boiling range, group composition), operational condition (inlet amount, water-oil ratio, XOT, COT), yield of cracked product.Associated steam experimental analysis instrument and equipment is as follows:
(1) petroleum naphtha density (20 DEG C) measured by ANTON PEAR company DE40 specific gravity hydrometer;
(2) German Haier tide company HDA627 analyzes petroleum naphtha grace formula distillation boiling range (ASTM) (initial boiling point, 10%, 30%, 50%, 70%, 90%, final boiling point);
(3) U.S.'s Agilent company HP6850 analysis petroleum naphtha group composition (normal paraffin, isoparaffin, naphthenic hydrocarbon, aromatic hydrocarbons) and liquid-phase pyrolysis product form and weight content;
(4) U.S.'s Agilent company HP7890 analytical pyrolysis gas composition and molar content thereof.
2. set up GK-V type pyrolyzer steam cracking naphtha cracking product forecast model
Sample database is divided into two portions, and wherein a part is training data, and its data volume is 2/3rds of sample database amount, and remaining data is check data.Training data is inputted in SVMs (SVM), set up yield of cracked product of cracking furnace predictive model.SVMs (SVM) kernel function adopts RBF kernel function, mode input variable petroleum naphtha physical property (proportion, ASTM boiling range, group composition), operational condition (throwing oil mass, water-oil ratio, COT, XOT), output variable is the yield of all split products.Yield of cracked product of cracking furnace predictive model calculates the numerical value of corresponding output variable according to input variable, that is:
y
i＝X(F，S，XOT，COT，DEN，ASTM，PONA)
Wherein y
i-represent split product component yield
F-inlet amount
S-thinning ratio
XOT-is across section temperature
COT-coil outlet temperature
DEN-density
ASTM-ASTM boiling range
PONA-group composition
3. gather GK-V type industrial pyrolysis furnace 1-butylene molar content service data
The molar content of the 1-butylene of GK-V type pyrolyzer is obtained by off-line analysis.Draw one splitting gas in the outlet of GK-V pyrolyzer waste heat boiler, be cooled to less than 0-40 DEG C to form gas-liquid two-phase splitting gas, wherein liquid phase is hardly containing 1-butylene, utilizes HP7890 can analyze the molar content of the 1-butylene in gaseous stream.
GK-V type pyrolyzer steam cracking petroleum naphtha physical property is in table 6.Keep that inlet amount is 24.788 tons/hour, water-oil ratio is 0.633 constant, COT is adjusted to 802 DEG C, 810 DEG C, 815 DEG C, 831 DEG C, 840 DEG C respectively, simultaneously by the molar content of the 1-butylene in off-line sampling also analytical pyrolysis gas, and calculate the molar content (referring to table 7) of the 1-butylene of GK-V industrial pyrolysis furnace actual motion with this.
Table 6 petroleum naphtha physical property
The molar content of 1-butylene in table 7 splitting gas
| COT(℃) | 802 | 810 | 815 | 831 | 840 |
| 1-butylene (mol%) | 1.32 | 1.29 | 1.17 | 0.81 | 0.65 |
4. Model Checking
Bring GK-V type industrial pyrolysis furnace service data into predictive model and the 1-butylene molar content of carrying out multiple COT temperature calculates, and obtain comparing the COT temperature of coincideing with industrial data, calculation result refers to table 8.1-butylene molar content is calculated as follows, gas phase is formed primarily of hydrogen, methane, ethane, ethene, acetylene, propane, propylene, propine and propadiene, butane, butylene, divinyl, carbon five, their weight yield can be calculated by predictive model, then calculate gas phase molar yield according to their Molecular weights.By contrast table 7 and table 8 known, calculated value and actual motion value data deviation are less than within 10%, and calculated value and actual motion value all raise along with the rising of COT.As can be seen here, low 10 DEG C than predictive model of the COT displays temperature of industrial pyrolysis furnace actual motion, the COT therefore in predictive model subtracts 10 DEG C and checks predictive models.
The 1-butylene molar content that table 8 predictive model calculates
| COT(℃) | Content, mol% |
| 812 | 1.33 |
| 820 | 1.19 |
| 825 | 1.10 |
| 841 | 0.80 |
| 850 | 0.66 |
5. set up GK-V cracked product of cracking furnace value maximization model
Based on cracked product of cracking furnace predictive model, adopt the mathematical method of average search method, under the condition that inlet amount, water-oil ratio, XOT, cracking stock physical property (proportion, ASTM boiling range, group composition), split product price are constant, in the COT normal operation range of industrial pyrolysis furnace, search out the COT that steam cracking product total value maximum value is corresponding, that is:
V
max＝max(V(m))
Wherein, F-inlet amount
S-thinning ratio
X-yield of cracked product
XOT-is across section temperature
COT-coil outlet temperature
DEN-density
ASTM-ASTM boiling range
PONA-group composition
P
j-split product component price
V (m)-split product total value
V
max-split product total value maximum value
6. be worth and optimize
According to the operation of the GK-V cracked product of cracking furnace value maximization model optimization pyrolyzer set up.The physical property of GK-V pyrolyzer cracking naphtha is in table 6, and pyrolyzer service data is in table 1.By in split product price (see table 3), cracking stock physical property, service data (inlet amount, thinning ratio, XOT, in table 1) input GK-V cracked product of cracking furnace value maximization model, calculation result is shown in Fig. 2.
As shown in Figure 2, under the operating conditions described above with under split product price condition, the true COT of GK-IV cracked product of cracking furnace value maximization is 849 DEG C, the petroleum chemicals total value of producing is 100019.7 yuan/hour, and the highest true COT of petroleum naphtha normal running is 845 DEG C, therefore select 845 DEG C to be worth the COT temperature optimized, and the temperature of pyrolyzer operation COT display is 835 DEG C, its petroleum chemicals total value of producing is 99974.52.The common COT service temperature of GK-V type pyrolyzer is 825 DEG C, and actual real operation COT temperature is 835 DEG C, and the petroleum chemicals total value of production is 99596.63 yuan/hour.Optimize by being worth, GK-V industrial pyrolysis furnace COT brings up to 835 DEG C by 825 DEG C, and petroleum chemicals (split product) total value that pyrolyzer is produced adds 1103.661 yuan/hour.
Claims (16)
1. the construction process of an industrial pyrolysis furnace split product value maximization model, it is characterized in that, described method is for setting up industrial pyrolysis furnace value maximization model and operating for optimizing pyrolyzer, the petroleum chemicals total value that industrial pyrolysis furnace is produced reaches maximum, and described method comprises the following steps:
(1) set up predictive model: based on steam cracking experimental data, utilize Mathematical Modeling Methods to set up industrial pyrolysis furnace yield of cracked product predictive model, (y
i=X (F, S, XOT, COT, P), y
i-represent split product component yield, F-inlet amount, S-thinning ratio, XOT-across section temperature, COT-coil outlet temperature, P-cracking stock physical property); Yield of cracked product is calculated according to cracking stock physical property, industrial pyrolysis furnace operational condition;
(2) target split product molar content data are gathered: under the condition that cracking stock physical property, inlet amount, quantity of steam are constant, in industrial pyrolysis furnace coil outlet temperature normal operation range, the target split product molar content data run by adjustment outlet temperature acquisition industrial pyrolysis furnace;
(3) check: utilize the target split product molar content data of the industrial pyrolysis furnace obtained by step (2) to check the predictive model obtained by step (1), make the calculated value of the predictive model of check and the data consistent of industrial pyrolysis furnace actual motion;
(4) cracked product of cracking furnace value maximization model is set up: set up cracked product of cracking furnace value maximization model according to the predictive model that step (3) obtains; Formula is
v
max=max (V (m)), wherein F-inlet amount, S-thinning ratio, XOT-across section temperature, COT (m)-coil outlet temperature, P-cracking stock physical property, PR
j-split product component price, V (m)-split product total value, V
max-split product total value maximum value;
(5) ask for the maximized operational condition of cracked product of cracking furnace total value: according to the maximization model of step (4), input split product price, cracking stock physical property, pyrolyzer service data calculate the maximum pyrolyzer operational condition of split product total value.
2. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, the production equipment related in described method comprises pyrolyzer, tripping device, polyolefin resin device.
3. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, described cracking stock is liquid cracking stock, comprises petroleum naphtha, diesel oil, hydrogenation tail oil.
4. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 3, it is characterized in that, described cracking stock physical property comprises density, Engler distillation boiling range, group composition, hydrogen richness or carbon content or ratio of carbon-hydrogen, carboloy residue, molecular weight, correlation index and refractive index, or is detailed composition and the content formation thereof of cracking stock.
5. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, described split product refers to industrial pyrolysis furnace split product before separation out; Split product mainly comprises hydrogen, carbon monoxide, carbonic acid gas, ethane, ethene, acetylene, propane, propylene, propine, propadiene, butane, butylene, divinyl, benzene,toluene,xylene, ethylbenzene, vinylbenzene, pyrolysis gasoline, Pyrolysis gas oil PGO, Pyrolysis fuel oil PFO.
6. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, described petroleum chemicals are the products taking market sale to enterprise, from tripping device or polyolefin device or polyester; Mainly comprise ethene, propylene, divinyl, benzene,toluene,xylene, polyolefin resin, rubber, ethylene glycol, polyester, chemical fibre, oxyethane, propylene oxide, gasoline, diesel oil, oil fuel, LPG.
7. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, described target split product is under the constant condition of cracking stock physical property, inlet amount, quantity of steam, within pyrolyzer COT operating restraint, the split product component that its molar content raises along with COT and increases or reduce, comprises hydrogen, methane, ethene, acetylene, propane, butane, butylene, benzene,toluene,xylene.
8. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, described target split product molar content data be at industrial pyrolysis furnace under the condition keeping cracking stock physical property, inlet amount, water-oil ratio constant, within pyrolyzer COT normal operation range, the target split product molar content data obtained by adjustment at least three COT temperature.
9. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 8, it is characterized in that, described target split product molar content data be at industrial pyrolysis furnace under the condition keeping cracking stock physical property, inlet amount, water-oil ratio constant, within pyrolyzer COT normal operation range, by adjusting the target split product molar content data that five COT temperature obtain.
10. the construction process of a kind of industrial pyrolysis furnace split product value maximization model according to claim 1, it is characterized in that, in step (3), the method of described Model Checking utilizes predictive model to calculate the molar content of the target split product under industrial pyrolysis furnace operational condition, by comparing calculation value and industry park plan data, adjustment predictive model in COT, the molar content of the target split product that predictive model is calculated and the data of industry park plan basically identical.
The construction process of 11. a kind of industrial pyrolysis furnace split product value maximization models according to claim 10, it is characterized in that, the molar content of target split product that described predictive model calculates and the data consistent of industry park plan be calculated value and actual motion value deviation within 10%, and numerical value change rule is consistent.
The construction process of 12. a kind of industrial pyrolysis furnace split product value maximization models according to claim 1, it is characterized in that, described cracked product of cracking furnace value maximization model is based on yield of cracked product of cracking furnace predictive model, according to physical property, pyrolyzer service data, the split product price of cracking stock, in pyrolyzer operational condition restriction range, adopt mathematical method search or calculate the maximum operational condition of split product total value.
The construction process of 13. a kind of industrial pyrolysis furnace split product value maximization models according to claim 11, it is characterized in that, described industrial pyrolysis furnace service data is by feedstock amount, dilution steam generation amount or thinning ratio, form across section temperature, and being worth the operational condition optimized is coil outlet temperature.
The construction process of 14. a kind of industrial pyrolysis furnace split product value maximization models according to claim 11, it is characterized in that, described mathematical method comprises searching method.
The construction process of 15. a kind of industrial pyrolysis furnace split product value maximization models according to claim 11, it is characterized in that, described yield of cracked product of cracking furnace predictive model is based on steam cracking testing data, adopt the mathematical model that Mathematical Modeling Methods is set up, calculate yield of cracked product according to cracking stock physical property and pyrolyzer operational condition.
The construction process of 16. a kind of industrial pyrolysis furnace split product value maximization models according to claim 15, it is characterized in that, described Mathematical Modeling Methods comprises SVMs, artificial neural network, Multiple Non Linear Regression, genetic algorithm.
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