CN102452982A - Method for purifying epsilon-caprolactam and method for preparing epsilon-caprolactam - Google Patents
Method for purifying epsilon-caprolactam and method for preparing epsilon-caprolactam Download PDFInfo
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Abstract
The invention provides a method for purifying a crude epsilon-caprolactam product, which comprises the following steps of: dissolving the crude epsilon-caprolactam product in halogenated hydrocarbon to obtain a halogenated hydrocarbon solution of epsilon-caprolactam; and performing evaporative crystallization on the solution at the temperature of between -10 and 50 DEG C under reduced pressure to separate an epsilon-caprolactam crystal. The invention also provides a method for preparing the epsilon-caprolactam, which comprises the following steps of: performing Beckmann rearrangement reaction on gas-phase cyclohexanone-oxime in the presence of a molecular sieve catalyst with a melt flow index (MFI) structure, and distilling a reaction product to obtain the crude epsilon-caprolactam product; and performing crystallization purification by the method for purifying the crude epsilon-caprolactam product, and performing hydrogenation reaction on the epsilon-caprolactam crystal obtained after purification in the presence of a hydrogenation catalyst. By the method for purifying the crude epsilon-caprolactam product, the epsilon-caprolactam which meets the industrial product requirement can be obtained, and the phenomenon of scale formation in the crystallization process is avoided.
Description
Technical field
The present invention relates to a kind of method of purification of ε-Ji Neixianan and the preparation method of ε-Ji Neixianan.
Background technology
ε-Ji Neixianan is one of synthon and synthetic resins important material, is mainly used in to make tynex (nylon 6), resin and film etc.At present, the method for producing ε-Ji Neixianan in the industry is employing oleum acid as catalyst and solvent, OxiKhim-Styrol generation liquid phase Beckmann rearrangement.There are deficiencies such as etching apparatus, contaminate environment and economic benefit be undesirable in this technology, and can produce a large amount of ammonium sulfate.
Cyclohexanone-Oxime Gas Phase Beckmann Rearrangement on the solid acid catalyst is to realize that ε-Ji Neixianan does not have the novel process of sulphur ammoniumization; Have problems such as no equipment corrosion, non-environmental-pollution; The separation of product is purified and also will be simplified greatly, and the vapor phase beckmann rearrangement reaction novel process of therefore not having the sulphur ammonium has received great concern.
For development is applicable to the solid acid catalyst of vapor phase beckmann rearrangement reaction, the investigator carried out a large amount of research to two types of main catalyzer such as oxide compound (composite oxides), zeolite molecular sieves both at home and abroad, all can prepare ε-Ji Neixianan.
Yet the ε-Ji Neixianan that these methods obtain contains plurality of impurities.As everyone knows; ε-Ji Neixianan is the raw material that is used to prepare polymeric amide; ε-Ji Neixianan product to being used to prepare polymeric amide and further make synthon and synthetic resins has very high specification of quality; The impurity of μ g/g level all can influence the polyreaction of follow-up ε-Ji Neixianan, is difficult for forming long filament.Therefore; The method that adopts various separation to purify obtains crude epsi-caprolactam; Adopt various purified methods finally to make highly purified ε-Ji Neixianan then, highly purified like this ε-Ji Neixianan just can be used to make products such as synthon, synthetic resins and film.
CN 101070299A discloses a kind of separation method for purification of ε-Ji Neixianan, and this method is included in the step of crystallization ε-Ji Neixianan in the halohydrocarbon solution that contains crude epsi-caprolactam.Concrete, this patented claim discloses the methanol solution that will pass through the ε-Ji Neixianan that vapor phase beckmann rearrangement reaction obtains and has distilled, and removes methyl alcohol, lower-boiling impurity and high-boiling-point impurity, obtains crude epsi-caprolactam; This crude epsi-caprolactam is dissolved in the halohydrocarbon, obtains the mixing solutions of crude epsi-caprolactam-halohydrocarbon; This mixing solutions is carried out crystallisation by cooling and carries out spinning, obtain the ε-Ji Neixianan crystal; This ε-Ji Neixianan crystal is washed and carry out spinning with halohydrocarbon, obtain ε-Ji Neixianan; Then, make the ε-Ji Neixianan that obtains carry out hydrogenation reaction, thereby the extinction value, volatility base number and the potassium permanganate absorption value that obtain ε-Ji Neixianan meet the ε-Ji Neixianan product that Industrial products require.
Meet the ε-Ji Neixianan that Industrial products require though adopt the method for above-mentioned patented claim to prepare; Yet; In this method the mixing solutions of ε-Ji Neixianan-halohydrocarbon being carried out the crystalline mode is cooling crystallization method, in the crystalline process, wants heat release, therefore; Require to have the very big temperature difference between ε-Ji Neixianan and the heat-eliminating medium, and need enough heat interchanging areas.Simultaneously; Because the internal-external temperature difference of mold is big, cause ε-Ji Neixianan to be easy to stick to the wall of mold, therefore; In order to reduce scale formation; Need in mold, use scraper, perhaps use multi-stage mold to reduce the temperature difference between ε-Ji Neixianan and the heat-eliminating medium, yet can increase the cost and the production cost of mold greatly like this.
Summary of the invention
The objective of the invention is to overcome the defective that crystallisation by cooling process in the separating and purifying method of existing ε-Ji Neixianan is easy to generate scale formation; A kind of method of purification of new ε-Ji Neixianan is provided; Adopt this method can obtain to meet the ε-Ji Neixianan of Industrial products requirement, and can not produce scale formation in the crystallisation process.
The invention provides the method for purification of the thick product of a kind of ε-Ji Neixianan; This method comprises the thick product of ε-Ji Neixianan is dissolved in the halohydrocarbon; Obtain the halohydrocarbon solution of ε-Ji Neixianan; Under-10-50 ℃, this solution is carried out the reduction vaporization crystallization, isolate the ε-Ji Neixianan crystal, the thick product of said ε-Ji Neixianan contains ε-Ji Neixianan and is selected from least a in the isomers of OxiKhim-Styrol, octahydro azophenlyene, tetrahydroazepine-2-ketone and tetrahydroazepine-2-ketone.
The present invention also provides a kind of preparation method of ε-Ji Neixianan; This method is included under the existence of sieve catalyst of MFI structure; Make the OxiKhim-Styrol of gas phase carry out Beckman (Beckmann) rearrangement reaction; With obtaining the thick product of ε-Ji Neixianan after the reaction product distillation, then the thick product of this ε-Ji Neixianan is carried out crystallization and purification, and make the ε-Ji Neixianan crystal that obtains after the purification in the presence of hydrogenation catalyst, carry out hydrogenation reaction; The method of wherein, the thick product of said ε-Ji Neixianan being purified is the method for purification of the thick product of ε-Ji Neixianan provided by the invention.
The method of purification of the thick product of ε-Ji Neixianan according to the present invention; Halohydrocarbon solution through to ε-Ji Neixianan carries out the reduction vaporization crystallization; Make the ε-Ji Neixianan crystal that obtains carry out hydrogenation reaction afterwards; Can fully remove the impurity in the thick product of ε-Ji Neixianan, at least a as in the isomers of OxiKhim-Styrol, octahydro azophenlyene, tetrahydroazepine-2-ketone and tetrahydroazepine-2-ketone, thus obtain to meet the ε-Ji Neixianan product of Industrial products requirement; And; In the method for purification of the thick product of said ε-Ji Neixianan; Can in crystallizer, not produce scale formation in the reduction vaporization crystallisation process, therefore, the method for purification of the thick product of ε-Ji Neixianan according to the present invention; Need not use scraper equipment with the removal fouling, thereby can save production cost greatly.
Embodiment
Comprise according to the method for purification of the thick product of said ε-Ji Neixianan provided by the invention the thick product of ε-Ji Neixianan is dissolved in the halohydrocarbon; Obtain the halohydrocarbon solution of ε-Ji Neixianan; Under-10-50 ℃, this solution is carried out the reduction vaporization crystallization; Isolate the ε-Ji Neixianan crystal, the thick product of said ε-Ji Neixianan contains ε-Ji Neixianan and is selected from least a in the isomers of OxiKhim-Styrol, octahydro azophenlyene, tetrahydroazepine-2-ketone and tetrahydroazepine-2-ketone.
According to method provided by the invention, in order further to improve the ε-Ji Neixianan product gas purity of final preparation, said reduction vaporization crystalline temperature is preferably 5-40 ℃, more preferably 15-30 ℃.
According to method provided by the invention, said reduction vaporization crystalline pressure does not have strict requirement, as long as under reduced pressure can realize the object of the invention.Under the preferable case, said reduction vaporization crystalline pressure is 0.001-0.07MPa, more preferably 0.002-0.05MPa; The reduction vaporization crystalline time is 30-100 minute, more preferably 50-70 minute.In the present invention, said reduction vaporization crystalline pressure refers to absolute pressure.
According to method provided by the invention; The consumption of said halohydrocarbon can in very large range change, yet, in order to obtain the ε-Ji Neixianan of higher degree; And guarantee that the said reduction vaporization crystalline running time is unlikely long; With respect to the thick product of said ε-Ji Neixianan of 100 weight parts, the consumption of said halohydrocarbon is preferably the 180-1000 weight part, more preferably the 200-600 weight part.
According to method provided by the invention, said halohydrocarbon can be for various at normal temperatures for liquid and can dissolve the halohydrocarbon of ε-Ji Neixianan.Under preferable case, said halohydrocarbon is selected the lower halohydrocarbon of boiling point for use, thereby reduces in the reduction vaporization crystallisation process requirement to negative pressure.In the present invention, the boiling point of said halohydrocarbon is preferably 50-100 ℃, more preferably 60-90 ℃.
In the present invention, said halohydrocarbon is preferably at least a in positive chloropropane, different chloropropane, n-propylcarbinyl chloride, Sec-Butyl Chloride, different chlorobutane, tert-butyl chloride, positive N-PROPYLE BROMIDE, different N-PROPYLE BROMIDE, 1-NBB and the 2-NBB.
Further under the preferable case, said halohydrocarbon is at least two kinds a mixture in n-propylcarbinyl chloride, tert-butyl chloride, positive chloropropane, different chloropropane, positive N-PROPYLE BROMIDE and the 1-NBB.In this case, not only can obtain the ε-Ji Neixianan of higher degree and obtain the ε-Ji Neixianan product, but also can avoid producing in the crystallisation process phenomenon of fouling fully with higher yield.Further, when said halohydrocarbon was in n-propylcarbinyl chloride, tert-butyl chloride, positive chloropropane, positive N-PROPYLE BROMIDE and the 1-NBB at least two kinds mixture, the proportion of each halohydrocarbon in said mixture preferably was at least 20 weight %.
Under the most preferred situation, said halohydrocarbon is the mixture of n-propylcarbinyl chloride and tert-butyl chloride, and the weight ratio of n-propylcarbinyl chloride and tert-butyl chloride is 1: 0.25-4.
In the present invention, the thick product of said ε-Ji Neixianan can carry out the reaction product that Beckmann rearrangement obtains for making OxiKhim-Styrol.In this case; The thick product of said ε-Ji Neixianan can contain the isomers of ε-Ji Neixianan, OxiKhim-Styrol, octahydro azophenlyene and tetrahydroazepine-2-ketone and/or tetrahydroazepine-2-ketone usually; And the gross weight with the thick product of said ε-Ji Neixianan is a benchmark; The content of ε-Ji Neixianan can be 99-99.8 weight %; The content of OxiKhim-Styrol can be 0.01-0.5 weight %, and the content of octahydro azophenlyene can be 0.01-0.3 weight %, and the total content of the isomers of tetrahydroazepine-2-ketone and tetrahydroazepine-2-ketone can be 0.01-0.3 weight %.Said octahydro azophenlyene for example can be 1,2,3,4,6,7,8,9-octahydro azophenlyene, and said tetrahydroazepine-2-ketone for example can be 1,3,4,5-tetrahydroazepine-2-ketone.
In one embodiment, can also comprise according to method provided by the invention isolated ε-Ji Neixianan crystal after the reduction vaporization crystallization is washed, to obtain the higher ε-Ji Neixianan product of purity.The solvent that said ε-Ji Neixianan crystal is washed is preferably halohydrocarbon, more preferably with the identical halohydrocarbon of halohydrocarbon that dissolves the thick product of ε-Ji Neixianan.
The present invention also provides a kind of preparation method of ε-Ji Neixianan; This method is included under the existence of sieve catalyst of MFI structure; Make the OxiKhim-Styrol of gas phase carry out Beckmann rearrangement; With obtaining the thick product of ε-Ji Neixianan after the reaction product distillation, then the thick product of this ε-Ji Neixianan is carried out crystallization and purification, and make the ε-Ji Neixianan crystal that obtains after the purification in the presence of hydrogenation catalyst, carry out hydrogenation reaction; The method of wherein, the thick product of said ε-Ji Neixianan being carried out crystallization and purification is the method for purification of the thick product of said ε-Ji Neixianan provided by the invention.
According to the preparation method of said ε-Ji Neixianan provided by the invention, said Beckmann rearrangement is included under the existence of sieve catalyst of MFI structure, in the presence of carrier gas and solvent, the OxiKhim-Styrol of gas phase is reacted.The condition optimization of said Beckmann rearrangement comprises: temperature is 320-400 ℃, more preferably 365-385 ℃; Pressure is 0.07-0.13MPa, more preferably 0.08-0.12MPa; The dividing potential drop of OxiKhim-Styrol is 5.5-11.6kPa, and the dividing potential drop of solvent is 36.9-70.6kPa, and the dividing potential drop of carrier gas is 19.4-52.6kPa, and carrier gas flux is 1.0-5.0L/gcat/h, and the weight hourly space velocity of OxiKhim-Styrol is 1-5h
-1Said solvent can be low-carbon alcohol, for example can be methyl alcohol, ethanol etc.Said carrier gas can be all gases that under the Beckmann rearrangement condition, does not react with OxiKhim-Styrol and said solvent, and said carrier gas for example can be nitrogen and rare gas element.Said pressure and dividing potential drop all are meant absolute pressure.
Preparing method according to said ε-Ji Neixianan provided by the invention; The sieve catalyst of said MFI structure is that silica alumina ratio is at least greater than 5000; Be preferably greater than 10000 Si-Al molecular sieve catalyzer; The sieve catalyst of this MFI structure can be commercially available, and for example can build long company available from the Hunan; Also can adopt conventional method to prepare, the preparation method of the sieve catalyst of concrete MFI structure can be with reference to disclosed method among the CN 1600428A.
According to the preparation method of said ε-Ji Neixianan provided by the invention, mainly be in order from said reaction product, to remove solvent and water etc. to distilling through the reaction product that obtains behind the Beckmann rearrangement.Oneself is conventionally known to one of skill in the art for said distillatory method, repeats no more at this.
Preparing method according to said ε-Ji Neixianan provided by the invention; Through making ε-Ji Neixianan crystal and hydrogen generation hydrogenation reaction; On the one hand; Can the tetrahydroazepine-2-ketone and the isomers thereof that be difficult in the reduction vaporization crystallisation process fully remove be converted into ε-Ji Neixianan, thereby further improve the purity of the ε-Ji Neixianan of final preparation; On the other hand, can effectively improve the potassium permanganate absorption value of ε-Ji Neixianan product.
In the present invention; The condition of said hydrogenation reaction can suitably be selected in the hydrogenation conditions of routine; Yet; For the ε-Ji Neixianan product that guarantees final preparation has higher potassium permanganate absorption value and purity and less extinction value, the condition optimization of said hydrogenation reaction comprises: temperature is 80-150 ℃, more preferably 90-120 ℃; Pressure is 0.2-1.5MPa, more preferably 0.5-1.2MPa; Time is 0.5-3 hour, more preferably 1-2 hour; The weight ratio of said ε-Ji Neixianan crystal and hydrogenation catalyst is 1-100: 1, and 3-30 more preferably: 1.Said pressure refers to absolute pressure.
In the present invention, said hydrogenation reaction can be carried out in the presence of water.With respect to the ε-Ji Neixianan crystal of 100 weight parts, the consumption of said water can be the 100-500 weight part, is preferably the 200-400 weight part.
In the present invention, said hydrogenation catalyst can be the hydrogenation catalyst of various routines, and under the preferable case, said hydrogenation catalyst is the amorphous nickel catalyzer, and is concrete, and this amorphous nickel catalyzer for example can be referring to CN 1272490A and CN 1272491A.
According to method provided by the invention, said hydrogenation reaction can be carried out in slurry bed reactor, fixed-bed reactor or magnetically stabilized bed reactor.
In one embodiment; Also be included in after the hydrogenation reaction according to method provided by the invention; Collect the ε-Ji Neixianan product through triple effect evaporation and/or vacuum distillation method, thereby obtain to have higher potassium permanganate absorption value, less volatility base number and the ε-Ji Neixianan product of extinction value.
Below through embodiment the present invention is described further, but the present invention is not limited only to this.
In following examples, use following testing method to estimate the ε-Ji Neixianan crystal of preparation and the correlation parameter of ε-Ji Neixianan product:
(1) purity of ε-Ji Neixianan
Measure the purity of ε-Ji Neixianan with vapor-phase chromatography.
(2) the potassium permanganate absorption value (PM) of ε-Ji Neixianan
The ε-Ji Neixianan of 3.000 grams is poured in the tube comparison tubes of 100ml; Adding distil water is diluted to scale, shakes up, and puts into 20.0 ℃ constant temperature water bath; The concentration that in tube comparison tubes, adds 1ml is the potassium permanganate solution of 0.01N; Shake up immediately, start stopwatch simultaneously, the color of sample solution and standard color solution in tube comparison tubes (are got the pure Co (NO of 3.000 gram top grades
3)
26H
2O and 12 milligrams of pure K of top grade
2Cr
2O
7Water-soluble, be diluted to 1 liter, shake up) color stop stopwatch when identical, write down the time of being consumed (to calculate second), be the potassium permanganate absorption value.
(3) volatile alkali (V.B)
In alkaline medium, the low molecular impurity of the alkalescence in the sample is distilled, with the hydrochloric acid soln absorption of known quantity, excessive hydrochloric acid is used the standard solution of sodium hydroxide residual titration.With the mole number of the sour consumption of per kilogram sample measured value as volatile alkali.Calculation formula is following:
V.B(mmol/kg)＝[(V
0-V)×C
NaOH/M]×1000
In the formula: V
0The volume of the NaOH standardized solution that consumes for blank test, unit is ml;
V is the volume of the NaOH standardized solution of sample consumption, and unit is ml;
C
NaOHBe the accurate concentration of NaOH standardized solution, unit is mol/L;
M is a sample quality, and unit is g.
(4) extinction value E (at the 290nm wavelength)
In the 300ml Erlenmeyer flask, take by weighing the sample of 50 grams, add 50ml zero(ppm) water, shake up sample is dissolved fully, left standstill 10 minutes.Adopt spectrophotometer, under the wavelength of 290nm, detectable level is the extinction value of the sample of 50 weight % with respect to zero(ppm) water.
Embodiment 1
Present embodiment is used for explaining the method for purification of ε-Ji Neixianan provided by the invention and the preparation method of ε-Ji Neixianan.
Cyclohexanone-Oxime Gas Phase Beckmann Rearrangement is carried out in the fixed-bed reactor of 80ml; The internal diameter of this reactor drum is 28mm, and the loadings of the sieve catalyst of MFI structure (building long company available from the Hunan, trade mark RBS-1) is 9.45g; Reaction pressure is 0.1MPa; The catalyst bed reaction temperature is 375 ℃, and nitrogen (carrier gas) flow is 3.0L/gcat/hr, and the weight hourly space velocity of OxiKhim-Styrol is 2h
-1, the dividing potential drop of OxiKhim-Styrol is 8.6kPa, and the dividing potential drop of methyl alcohol (solvent) is 60.2kPa, and the dividing potential drop of nitrogen is 31.2kPa.
The product that obtains behind the Beckmann rearrangement is collected through-5 ℃ ethylene glycol solution circulation cooling, obtained containing the mixture of ε-Ji Neixianan, then this mixture is distilled, obtain the thick product of ε-Ji Neixianan.At Agilent GC6890 type gas chromatograph (flame ionization detector (FID); The OV-1 capillary chromatographic column; Column length 30m) upward the thick product of this ε-Ji Neixianan is analyzed, learnt that it mainly consists of: the ε-Ji Neixianan of 99.2 weight %, the OxiKhim-Styrol of 1225 μ g/g; The octahydro azophenlyene of 686 μ g/g, the tetrahydroazepine of 598 μ g/g-2-ketone.
Get the crude epsi-caprolactam that the aforesaid method of 2.0kg obtains; Be dissolved in the n-propylcarbinyl chloride of 2.0kg and be made into the solution that concentration is 50 weight %; Add volume and be in the there-necked flask of 10L as bed material, simultaneously above-mentioned ε-Ji Neixianan is mixed with the n-propylcarbinyl chloride solution that concentration is the hexanolactam of 30 weight %, and the speed of this solution with 1kg/h is added in the there-necked flask; Speed with 350r/min stirs; Temperature maintenance is at 20 ℃, and pressure is maintained 0.006MPa, carries out the reduction vaporization crystallization 60 minutes.The slurries of separating out behind the crystal are discharged with the speed of 1kg/h, and the slurries spinning of discharging is obtained crystal and mother liquor, reclaim mother liquor; The crystal that obtains is sent in the container of belt stirrer again, washs as cleaning solvent with n-propylcarbinyl chloride, and recentrifuge separates that to obtain purity be 99.94% ε-Ji Neixianan crystal; Reclaim washings, ε-Ji Neixianan crystalline yield is 90%, and the PM value is 150s; The V.B value is 0.45mmol/kg, and the E value is 0.1504.Continuous crystallisation is operated the there-necked flask inwall that makes discovery from observation after 100 hours and is not produced scale formation.Among the present invention, ε-Ji Neixianan crystalline yield calculates according to the weight * 100% of the hexanolactam raw material in all ε-Ji Neixianan crystalline weight/adding there-necked flasks that obtain in the certain hour.
Get the above-mentioned ε-Ji Neixianan crystal of 1.90kg, be added in the reaction kettle that volume is 10L, add water 4.4kg; Add the amorphous nickel catalyzer (the industrial trade mark is SRNA-4, builds long company available from the Hunan) of 190g again, be heated to about 100 ℃; Feed hydrogen then, hydrogen flowing quantity is controlled at 0.6L/min, and reaction pressure is maintained 0.7MPa; Make ε-Ji Neixianan and contacted with hydrogen, reacted 1 hour.Carry out dehydration by evaporation (condition of evaporation: temperature 60-85 ℃, pressure 0.005-0.01MPa) afterwards, after evaporation removes and anhydrates; Approximately carrying out underpressure distillation under the 1mmHg condition again; Obtain the ε-Ji Neixianan product, learn that through detection this ε-Ji Neixianan product gas purity is 99.99%, the PM value is 40000s; The V.B value is 0.15mmol/kg, and the E value is 0.0315.
Embodiment 2
Present embodiment is used for explaining the method for purification of ε-Ji Neixianan provided by the invention and the preparation method of ε-Ji Neixianan.
The thick product of ε-Ji Neixianan is purified and prepare the ε-Ji Neixianan product according to the method for embodiment 1; Different is; In the process that thick product is purified to ε-Ji Neixianan, using weight ratio is that the n-propylcarbinyl chloride of identical weight among 1: 1 the mixture replacement embodiment 1 of n-propylcarbinyl chloride and tert-butyl chloride is as recrystallisation solvent.The ε-Ji Neixianan crystalline yield that in purification process, obtains is 92%, and purity is 99.96%, and the PM value is 120s, and the V.B value is 0.40mmol/kg, and the E value is 0.18, and the there-necked flask inwall that makes discovery from observation does not produce scale formation.
In addition, the ε-Ji Neixianan product gas purity of final preparation is 99.98%, and the PM value is 43000s, and the V.B value is 0.16mmol/kg, and the E value is 0.0350.
Comparative Examples 1
The thick product of ε-Ji Neixianan is purified and prepare the ε-Ji Neixianan product according to the method for embodiment 1; Different is; The method that the thick product of ε-Ji Neixianan is purified is: get the thick product of ε-Ji Neixianan of 2.0kg, add the n-propylcarbinyl chloride of 2.0kg again, be heated to 70 ℃; Stirred 30 minutes, ε-Ji Neixianan is dissolved in the n-propylcarbinyl chloride fully.Continue cooling while stirring, temperature is cooled to 15 ℃ from 70 ℃, and the ε-Ji Neixianan crystal is separated out fully.Spinning obtains ε-Ji Neixianan crystal and mother liquor, reclaims mother liquor.So the ε-Ji Neixianan crystalline yield of preparation is 85%, and purity is 99.91%, and the PM value is 145s, and the V.B value is 0.45mmol/kg, and the E value is 0.2510, and the there-necked flask inwall that makes discovery from observation has produced fouling.
In addition, the ε-Ji Neixianan product gas purity of final preparation is 99.95%, and the PM value is 39000s, and the V.B value is 0.21mmol/kg, and the E value is 0.0423.
Embodiment 3
Present embodiment is used for explaining the method for purification of ε-Ji Neixianan provided by the invention and the preparation method of ε-Ji Neixianan.
Cyclohexanone-Oxime Gas Phase Beckmann Rearrangement is carried out in the fixed-bed reactor of 80ml; The internal diameter of this reactor drum is 28mm, and the loadings of the sieve catalyst of MFI structure (building long company available from the Hunan, trade mark RBS-1) is 9.45g; Reaction pressure is 0.1MPa; The catalyst bed reaction temperature is 365 ℃, and nitrogen (carrier gas) flow is 3.0L/gcat/hr, and the weight hourly space velocity of OxiKhim-Styrol is 3h
-1, the dividing potential drop of OxiKhim-Styrol is 5.5kPa, and the dividing potential drop of methyl alcohol (solvent) is 70.6kPa, and the dividing potential drop of nitrogen is 23.9kPa.
The product that obtains behind the Beckmann rearrangement is collected through-5 ℃ ethylene glycol solution circulation cooling, obtained containing the mixture of ε-Ji Neixianan, then this mixture is distilled, obtain the thick product of ε-Ji Neixianan.At Agilent GC6890 type gas chromatograph (flame ionization detector (FID); The OV-1 capillary chromatographic column; Column length 30m) upward the thick product of this ε-Ji Neixianan is analyzed, learnt that it mainly consists of: the ε-Ji Neixianan of 99.3 weight %, the OxiKhim-Styrol of 1205 μ g/g; The octahydro azophenlyene of 655 μ g/g, the tetrahydroazepine of 575 μ g/g-2-ketone.
Get the 2.0kg crude epsi-caprolactam; Be dissolved into and be made into the solution that concentration is 50 weight % in the 2.0kg tert-butyl chloride; Add volume and be in the there-necked flask of 10L as bed material, simultaneously above-mentioned ε-Ji Neixianan is mixed with the tert-butyl chloride solution that concentration is the ε-Ji Neixianan of 30 weight %, and the speed of this solution with 1kg/h is added in the there-necked flask; Speed with 350r/min stirs; Temperature maintenance is at 25 ℃, and pressure is maintained 0.02MPa, under this temperature and pressure, carries out the reduction vaporization crystallization 50 minutes.The crystal of separating out is discharged with the speed of 1kg/h, and the slurries spinning of discharging is obtained crystal and mother liquor, reclaim mother liquor; And crystal added in the container of belt stirrer, washing as cleaning solvent with tert-butyl chloride, recentrifuge separates that to obtain purity be 99.92% ε-Ji Neixianan crystal; Reclaim washings, ε-Ji Neixianan crystalline yield is 93%, and the PM value is 120s; The V.B value is 0.48mmol/kg, and the E value is 0.1608.Continuous crystallisation is operated the there-necked flask inwall that makes discovery from observation after 100 hours and is not produced scale formation.
Get the above-mentioned ε-Ji Neixianan crystal of 1.90kg, be added in the reaction kettle that volume is 10L, add water 4.4kg; Add the amorphous nickel catalyzer (the industrial trade mark is SRNA-4, builds long company available from the Hunan) of 190g again, be heated to about 120 ℃; Feed hydrogen then, hydrogen flowing quantity is controlled at 0.6L/min, and reaction pressure is maintained 1.0MPa; Make ε-Ji Neixianan and contacted with hydrogen, reacted 1.5 hours.Carry out dehydration by evaporation (condition of evaporation: temperature 60-85 ℃, pressure 0.005-0.01MPa) afterwards, after evaporation removes and anhydrates; Approximately carrying out underpressure distillation under the 1mmHg condition again; Obtain the ε-Ji Neixianan product, learn that through detection this ε-Ji Neixianan product gas purity is 99.99%, the PM value is 40500s; The V.B value is 0.20mmol/kg, and the E value is 0.0420.
Embodiment 4
Present embodiment is used for explaining the method for purification of ε-Ji Neixianan provided by the invention and the preparation method of ε-Ji Neixianan.
Cyclohexanone-Oxime Gas Phase Beckmann Rearrangement is carried out in the fixed-bed reactor of 80ml; The internal diameter of this reactor drum is 28mm, and the loadings of the sieve catalyst of MFI structure (building long company available from the Hunan, trade mark RBS-1) is 9.45g; Reaction pressure is 0.1MPa; The catalyst bed reaction temperature is 385 ℃, and nitrogen (carrier gas) flow is 3.0L/gcat/hr, and the weight hourly space velocity of OxiKhim-Styrol is 4h
-1, the dividing potential drop of OxiKhim-Styrol is 11.6kPa, and the dividing potential drop of methyl alcohol (solvent) is 36.9kPa, and the dividing potential drop of nitrogen is 51.5kPa.
The product that obtains behind the Beckmann rearrangement is collected through-5 ℃ ethylene glycol solution circulation cooling, obtained containing the mixture of ε-Ji Neixianan, then this mixture is distilled, obtain the thick product of ε-Ji Neixianan.At Agilent GC6890 type gas chromatograph (flame ionization detector (FID); The OV-1 capillary chromatographic column; Column length 30m) upward the thick product of this ε-Ji Neixianan is analyzed, learnt that it mainly consists of: the ε-Ji Neixianan of 99.2 weight %, the OxiKhim-Styrol of 1301 μ g/g; The octahydro azophenlyene of 690 μ g/g, the tetrahydroazepine of 601 μ g/g-2-ketone.
Get the 2.0kg crude epsi-caprolactam, be dissolved into and be made into the solution that concentration is 50 weight % in the positive chloropropane of 2.0kg, add volume and be in the there-necked flask of 10L as bed material; Simultaneously above-mentioned ε-Ji Neixianan is mixed with the positive chloropropane solution that concentration is the ε-Ji Neixianan of 30 weight %; And with in the speed adding there-necked flask of this solution with 1kg/h, with the speed stirring of 350r/min, temperature maintenance is at 30 ℃; Pressure is maintained 0.03MPa, under this temperature and pressure, carries out the reduction vaporization crystallization 70 minutes.The slurries of separating out behind the crystal are discharged with the speed of 1kg/h, and the slurries spinning of discharging is obtained crystal and mother liquor, reclaim mother liquor; And crystal added in the container of belt stirrer, washing as cleaning solvent with positive chloropropane, recentrifuge separates that to obtain purity be 99.85% ε-Ji Neixianan crystal; Reclaim washings, ε-Ji Neixianan crystalline yield is 93.56%, and the PM value is 100s; The V.B value is 0.34mmol/kg, and the E value is 0.1205.Continuous crystallisation is operated the there-necked flask inwall that makes discovery from observation after 100 hours and is not produced scale formation.
Get the above-mentioned ε-Ji Neixianan crystal of 1.90kg, be added in the reaction kettle that volume is 10L, add water 4.4kg; Add the amorphous nickel catalyzer (the industrial trade mark is SRNA-4, builds long company available from the Hunan) of 190g again, be heated to about 110 ℃; Feed hydrogen then, hydrogen flowing quantity is controlled at 0.6L/min, and reaction pressure is maintained 0.6MPa; Make ε-Ji Neixianan and contacted with hydrogen, reacted 2 hours.Carry out dehydration by evaporation (condition of evaporation: temperature 60-85 ℃, pressure 0.005-0.01MPa) afterwards, after evaporation removes and anhydrates; Approximately carrying out underpressure distillation under the 1mmHg condition again; Obtain the ε-Ji Neixianan product, learn that through detection this ε-Ji Neixianan product gas purity is 99.99%, the PM value is 41000s; The V.B value is 0.31mmol/kg, and the E value is 0.0480.
Claims (13)
1. the method for purification of the thick product of ε-Ji Neixianan; This method comprises the thick product of ε-Ji Neixianan is dissolved in the halohydrocarbon; Obtain the halohydrocarbon solution of ε-Ji Neixianan; Under-10 ℃ to 50 ℃, this solution is carried out the reduction vaporization crystallization, isolate the ε-Ji Neixianan crystal, the thick product of said ε-Ji Neixianan contains ε-Ji Neixianan and is selected from least a in the isomers of OxiKhim-Styrol, octahydro azophenlyene, tetrahydroazepine-2-ketone and tetrahydroazepine-2-ketone.
2. method according to claim 1, wherein, said reduction vaporization crystalline temperature is 5-40 ℃, and pressure is 0.001-0.07MPa, and the time is 30-100 minute.
3. method according to claim 2, wherein, said reduction vaporization crystalline temperature is 15-30 ℃, and pressure is 0.002-0.05MPa, and the time is 50-70 minute.
4. method according to claim 1, wherein, with respect to the thick product of said ε-Ji Neixianan of 100 weight parts, the consumption of said halohydrocarbon is the 180-1000 weight part.
5. method according to claim 4, wherein, with respect to the thick product of said ε-Ji Neixianan of 100 weight parts, the consumption of said halohydrocarbon is the 200-600 weight part.
6. according to claim 1,4 or 5 described methods, wherein, the boiling point of said halohydrocarbon is 50-100 ℃.
7. method according to claim 6, wherein, said halohydrocarbon is at least a in positive chloropropane, different chloropropane, n-propylcarbinyl chloride, Sec-Butyl Chloride, different chlorobutane, tert-butyl chloride, positive N-PROPYLE BROMIDE, different N-PROPYLE BROMIDE, 1-NBB and the 2-NBB.
8. method according to claim 7, wherein, said halohydrocarbon is at least two kinds a mixture in n-propylcarbinyl chloride, tert-butyl chloride, positive chloropropane, different chloropropane, positive N-PROPYLE BROMIDE and the 1-NBB.
9. according to claim 1,4 or 5 described methods; Wherein, The thick product of said ε-Ji Neixianan contains the isomers of ε-Ji Neixianan, OxiKhim-Styrol, octahydro azophenlyene and tetrahydroazepine-2-ketone and/or tetrahydroazepine-2-ketone; And the gross weight with the thick product of said ε-Ji Neixianan is a benchmark, and the content of ε-Ji Neixianan is 99-99.8 weight %, and the content of OxiKhim-Styrol is 0.01-0.5 weight %; The content of octahydro azophenlyene is 0.01-0.3 weight %, and the total content of the isomers of tetrahydroazepine-2-ketone and tetrahydroazepine-2-ketone is 0.01-0.3 weight %.
10. the preparation method of a ε-Ji Neixianan; This method is included under the existence of sieve catalyst of MFI structure; Make the OxiKhim-Styrol of gas phase carry out Beckmann rearrangement; With obtaining the thick product of ε-Ji Neixianan after the reaction product distillation, then the thick product of this ε-Ji Neixianan is carried out crystallization and purification, and make the ε-Ji Neixianan crystal that obtains after the purification in the presence of hydrogenation catalyst, carry out hydrogenation reaction; It is characterized in that the method for the thick product of said ε-Ji Neixianan being carried out crystallization and purification is any described method among the claim 1-9.
11. method according to claim 10, wherein, the condition of said Beckmann rearrangement comprises: temperature is 320-400 ℃; Pressure is 0.07-0.13MPa; The dividing potential drop of OxiKhim-Styrol is 5.5-11.6kPa, and the dividing potential drop of solvent is 36.9-70.6kPa, and the weight hourly space velocity of OxiKhim-Styrol is 1-5h
-1
12. method according to claim 10, wherein, the condition of said hydrogenation reaction comprises: temperature is 80-150 ℃, and pressure is 0.2-1.5MPa, and the time is 0.5-3 hour, and the weight ratio of said ε-Ji Neixianan crystal and hydrogenation catalyst is 1-100: 1.
13. according to claim 10 or 12 described methods, wherein, said hydrogenation catalyst is the amorphous nickel catalyzer.
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| CN103864689A (en) * | 2012-12-07 | 2014-06-18 | 帝斯曼知识产权资产管理有限公司 | Method for preparing caprolactam |
| CN104059018A (en) * | 2013-10-28 | 2014-09-24 | 中国石油化工股份有限公司 | Caprolactam purification method and device |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1293660A (en) * | 1998-03-20 | 2001-05-02 | Dsm有限公司 | Process for continuous purification of crude epsi-caprolactam |
| CN101070299A (en) * | 2006-05-12 | 2007-11-14 | 中国石油化工股份有限公司 | Method for purifying and refining epsi caprolactam |
-
2010
- 2010-10-15 CN CN201010516972.8A patent/CN102452982B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1293660A (en) * | 1998-03-20 | 2001-05-02 | Dsm有限公司 | Process for continuous purification of crude epsi-caprolactam |
| CN101070299A (en) * | 2006-05-12 | 2007-11-14 | 中国石油化工股份有限公司 | Method for purifying and refining epsi caprolactam |
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| CN103864689B (en) * | 2012-12-07 | 2017-12-22 | Cap Iii 有限公司 | A kind of method of the condensate liquid obtained in the evaporative crystallization steps of purification of aqueous ammonium sulfate phase |
| CN104557707A (en) * | 2013-10-28 | 2015-04-29 | 中国石油化工股份有限公司 | Caprolactam hydrofining method |
| CN104072419A (en) * | 2013-10-28 | 2014-10-01 | 中国石油化工股份有限公司 | Purification method and purification device of caprolactam |
| CN104557706A (en) * | 2013-10-28 | 2015-04-29 | 中国石油化工股份有限公司 | Caprolactam hydrofining method |
| CN104072419B (en) * | 2013-10-28 | 2016-11-02 | 中国石油化工股份有限公司 | The purification process of a kind of caprolactam and purification devices |
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| CN104059018A (en) * | 2013-10-28 | 2014-09-24 | 中国石油化工股份有限公司 | Caprolactam purification method and device |
| CN105017153A (en) * | 2014-04-24 | 2015-11-04 | 中国石油化工股份有限公司 | Method for refining caprolactam |
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