前苏联专利SU946400A3 Process for isolating epsilon-caprolactam

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专利摘要:
1430949 Lactams SNIA VISCOSA SOC NAZIONALE INDUSTRIA APPLICAZIONI VISCOSA SpA 27 June 1973 [28 June 1972] 30468/73 Heading C2C A lactam, e.g. caprolactam, is removed from solution in an organic first solvent by adding to the solution a second solvent which is miscible with the first solvent but which is not a solvent for the lactam so that the lactam is displaced from solution in the first solvent. Exemplified as the first solvent is a phenol containing at least one alkyl substituent which contains 3 or more carbon atoms and has a solubility in water of less than 0À5 g. per 100 g. of water at 25‹ C. and in sulphuric acid solution containing 50 g. of sulphuric acid per 50 g. of water has a solubility of less than 0À2 g. per 100 g. of acid solution at 25‹ C, the substituent groups of the phenol not hindering the activity of the OH group of the phenol. The second solvent may be an aliphatic, aromatic or chlorinated hydrocarbon. A third solvent, e.g. water which is immiscible with both the first and second solvents but which is a solvent for the lactam may also be added to the solution so that the displaced lactam forms a solution in the third solvent.
公开号:SU946400A3
申请号:SU731937627
申请日:1973-06-27
公开日:1982-07-23
发明作者:Маттоне Роберто；Столли Жанкарло；Жюфрэ Луиджи
申请人:Сниа Вискоза Сочиета Национале Индустриа Аппликациони Вискоза С.П.А. (Фирма)；
IPC主号:

专利说明:

(54) METHOD FOR ISOLATING g-CAPROLACTAM
one
The invention relates to the improvement of the method for the isolation of f-caprolactam.
A known method for the isolation of fi-caprolactam from the sulfuric acid reaction mixture obtained by rearranging cyclohexanone oxime by extracting g-caprolactam with alkylphenols followed by fractionation of the extract, yielding alkylphenol, -caprolactam and bottoms tl3.
The disadvantage of the known method is that & -caprolactam, thus obtained, has a rather significant amount of impurities. The excess amount of solvent that can be removed by distillation does not actually capture a significant amount of impurities that accumulate, contaminate the resulting product, and the accumulation of these contaminants can lead to unsuitable
caprolactam for industrial use.
The purpose of the invention is to increase the purity of the target product.
5 The goal is achieved
According to the method for isolating -caprolactam from the sulfuric acid reaction mixture obtained by rearranging cyclohexanone 10 oxime by extracting f-caprolactam with alkylphenols and fractionating the extract, to produce alkylphenol and -caprolactam, alkylphenols are fractionated
15 before the start of distilling off its mixture with -caprolactam, and water and a liquid saturated hydrocarbon, such as n-hexane or cyclohexane, are introduced into the residue and the desired product is isolated
20 of the aqueous layer.
Example 1: Pure caprolactam is removed from its solutions, visopropylphenol, which is obtained as a result of a preliminary extraction process carried out on
100 g of acidic lactam mass coming from the system of molecular rearrangement of cyclohexanone oxime (Beckmann) in a sulfuric acid medium and containing 5 wt.% Of E-caprolactam
Example 1, as well as other examples, concerns the preparation of a pure lactam from a phenolic solution, regardless of how this phenolic solution is obtained, if only the processors for obtaining the phenol solution are in accordance with the conventional method.
The solution of caprolactam in phenol, which is obtained by this method, is distilled in a 500-ml flask, in the upper part of which a short reflux condenser was installed, heated by means of an infrared radiation instrument. With an absolute pressure of 3 mm Hg. distills (at a constant temperature of 73 ° C) 225 g of ortho-isopropylphenol, which, as shown by the results of the analysis, has the same characteristics as the ortho-isopropylphenol used for extraction, and thus can be reused .
As soon as the temperature begins to rise (thus indicating the almost complete removal of ortho-isopropylphenol, which does not chemically interact with caprolactam), the distillation is stopped, and the mass that remains in the flask is cooled.
This mass is then mixed in a 500 ml dilution separating funnel with 100 ml of water and 10P ml of cyclohexane. Next, decantation is carried out, thus obtaining two phases one above the other: the lower layer is drained into the second Separating funnel and carried out fourfold extraction using 50 ml of cyclohexane ' for each extraction operation. The upper layer which remained in the first separating funnel is extracted four times, using 50 ml of water for each E1 $ stratification. All the aqueous phases thus obtained are combined, as well as all the cyclohexane phases. Cyclohexane is distilled from the combined cyclohexane phases to obtain a residual product in the amount of 31.5 g, which contains 25 g of ortho-isopropylphenol, 5 g of caprolactam and 1.5 g by-products with
Their combined aqueous phases are distilled water and a residual distillation product is obtained in an amount of 0.2 g which contains 39.7 g of caprolactam and 0.5 g of by-products.
Lumimeter 2. A solution of caprolactam in ortho-sec-butylphenol is obtained by extracting caprolactam from 100 g of the mass of the same type of composition as in Example T using 250 g of the mentioned phenol.
The solution of caprolactam in orthosecutyl butylphenol is first distilled under a pressure of 3 mm Hg. Distillation is carried out until 225 g of phenolzo is removed. The mass remaining in the flask is cooled and dissolved in 200 ml of n-hexane. Caprolactam is extracted in the white crystals that accumulate on the filter having a porous glass diaphragm. On this filter, the crystals are washed three times with N-hexane, dried in a vacuum at
Thus, AO g of caprolactam, containing negligible amounts of contaminants, is extracted. This Caprolactam ortho sec-butylphenol and by-product, which are not in quantitative balance with each other, are recovered by evaporation of ntexan from the filtrates combined together.
EXAMPLE 3 As a phenolic solution of caprolactam, a solution in p-isopropylphenol is used that does not contain and is obtained from the acidic lactam mass coming from the nitrosation system of hexahydrobenzoic acid with NaHSQ4 sulfate. The phenolic solution is distilled in a fractionation column including a 1000 ml preheater, heated by infrared radiation, and a section of a column with an internal diameter of 25 mm and ten foraminide plates, with a silver-coated lining vacuum jacket, controlled by a timer VI steam condensation device.

权利要求:
Claims (1)
[1]
When using apparatus in which an internal pressure of 3 mm Hg is maintained. and the reflux ratio is from 5 to 1, the passage of the ortho-isopropyl-vapor: vapor, which is the head fraction, takes place at 73 ° C. Distillation is stopped as soon as the temperature of the head fraction starts to rise and at this moment b7 g of isopropylphenol having the same degree of purity as the product used in the previous extraction of caprolactam from the acidic lactam mass coming from the nitrosation system. Thus, this isopropylphenol can immediately and completely be reused. The product remaining in the 1009-ml flask is transferred to a 200-mil lithium flask and combined with the product in the same distillation unit. After heating the installation, the pressure in it is adjusted to 1.2 mm Hg. and adjust so that the reflux ratio is from 3 to 1. In the head product, at a temperature of 97-98.0, a stream of steam is obtained which condenses in the condensate receiver, and distillation continues until the volume of condensate produced reaches 100 ml Distillate, obtained in an amount of 100.5 g, is a pure, transparent H1 bone, which tends to crystallize over time. As shown by chemical analysis, this distillate consists of kTa weightD of caprolactam and 30, .3 weightD of ortho-isopropylphenol, while koliches impurities of infusion / p co is negligible that they could not be measured. This distillate is poured into a separate 500 ml separatory funnel and shaken with 150 ml of water and 150 g of cyclohexane. This process is carried out under practically the conditions described in the previous example, the resulting product is decanted to form two phases, while the underlying phase is drank in the second separatory funnel and subjected to four times extraction with water, using 100 ml of water for each extraction. All aqueous as well as cyclohexane phases are combined. By distillation, cyclohexane is distilled from the cyclohexane phases and a residual distillation product is obtained, which contains 30.5 g of ortho-isopropyl phenol and 7.5 g of caprolactam. Water is removed from the aqueous phases by distillation. A residual product of distillation is obtained, which contains 62.5 g of crystalline caprolactam of high purity and white color. The residual product (g) of the secondary distillation is also subjected to distillation in a microdistillation apparatus, thereby obtaining an amount of g of distillate consisting of L g of caprolactam, 1.5 g of ortho-isopropylphenol and 0.5 g of by-products, while as a residual microdistillation product (7.5 g) consists of g of by-products and 0.5 g of caprolactam. In this way, a total removal of by-products is achieved with very low caprolactam loss. The yield of caprolactam at various stages of treatment is 98.6% of the initial amount, while the amount of regenerated ortho-isopropyphenol, under conditions of its reuse, is 99.7% of the initial amount. A continuous process is carried out in accordance with the proposed method, using apparatus consisting of separate structural units (assembly of which is carried out in the conventional manner) interconnected and connected to each other in accordance with the scheme shown in the drawing. In the drawing, along with an image of each structural unit of the plant, as well as some connecting elements between them, and outlet tubes, the flow rates of the various compounds undergoing treatment, expressed in g / h, are shown. , 01P ortho-isopropylphenol, SP is a by-product. The equipment must necessarily be provided with powering and conveying devices that provide the required flow rates of various compounds, as well as the device nical control, and in any case - the devices that are provided in conventional installations of this type. 1500 g of the solution obtained by extraction of S-caprolactam (CL) from the acidic reaction mass with ortho-isopropylphenol (01P). Containing 195 g of C1, 1290 g of H1P and 15 g of by-products (SP), mainly with a high boiling point continuously for each mas is fed to colo. 1 distillation with ten foramin plates 50 mm in diameter. In the head fraction, 1236 g / h of pure 01 P is removed, which is recycled to the CI extraction unit. Tail fractions are sent to the central part of the liquid-liquid extraction column, including rotating discs 2, into which 1000 g / h of water is fed from above and 441 from the bottom. , 5 g / h of cyclohexane (CES). 532 g / h of product containing 22.5 g of C, 54.0 g of OIP, 14.0 SP and 441.5 CES are recovered in the head fraction. 172.5 g CL 1.0 g SP and 1000 g Ni O are obtained in the tail fraction for each hour, which is further purified. The head product is sent to a stripper 3, which excludes the conventional distillation column preheater, at the top of which is a drip separator. All of the cylohexane in this column (CES) is recovered during the distillation in the amount of 441.5 g and returned to column 2, while the product released from the bottom of this column is sent to a stripping column 4, similar to the previous stripping column, but acting at a higher temperature. 74.5 g / head product is recovered from the column, containing 19.5 CI, 34.0 g 01P and 1.0 gram SP, which can be recycled to column 1, while the product coming out of the bottom of the stripping column, which contains all of the residual SP and 3.0 g of C1, can be removed from this system. The aqueous pacTBCip of caprolactam, which accumulates at the bottom of column 2, is dehydrated by distilling water in vacuo. The residual caprolactam, by simple distillation of which the first fraction is removed from the system, accounts for 5% of the initial quantity of the product, and the tail fraction, which is about 10 of the total amount of the product, gives a product having the following properties. The permanganate number is 7200 Color (APHA) 5 Acidity (as CHgCOOH) is 0.0005 m-vol. 1 Volatile 0, 1 m-eq 0.1n. , NaOH per 20 g of product A solution of caprolactam in alkylphenolic solvents has the following properties. Ortho-isopropylphenol (01P) Caprolactam lactam solution 12 wt.% Density at, g / cm, 1,036 Viscosity at 35 ° C, s1111.7 Ortho-sec-butylphenol (OSBP) Caprolactam solution 12 wt.% Density at,, 023 Viscosity at 35 s, SP Ortho-tert-butylphenol (SSRP) Caprolactam solution 12 wt.% Density at 35 ° C, .24 Viscosity at, cp 12.6 Alkylphenol solvents have different extraction capacity with respect to aromatic and chlorinated solvents, as can be seen from the following experiments. 100 g of a sulfuric acid solution of caprolactam, which is obtained after the Beckmanna rearrangement of cyclohexanone oxime, after diluting with water, contains 30 wt. caprolactam, 34% by weight of sulfuric acid, 2% by weight of by-products and 34% by weight of water. This mixture, using each time, five times, was extracted with 50 ml of ortoisopropylphenol. Analysis of this alkylphenol solution shows that 29.6 g (99) of caprolactam is extracted with alkylphenol. Another sample of the acidic solution is extracted five times with 50 ml of toluene each time. Analysis of the toluene extract shows that only 3.5 g (12%) of caprolactam is extracted with toluene. The extraction described is repeated under the same conditions using 5-h. 80 ml each ortho-tert-butylphenol. Analysis of the alkylphenol solution shows that 29.75 g of caprolactam was extracted. The same sample was extracted five times with chloroform, 80 ml each time. Analysis of the extract shows that only 5.8 g (19%) of caprolactam was extracted with chloroform. Claims method for isolating -caprolactam from a sulfuric acid reaction mixture obtained during the rearrangement of cyclohexane ionoxime by extraction of C-capropactam with alkylphenols, followed by fractionation by extraction
HfO 1000
f2.5
5, o 14.0
441.5
low to obtain alkylphenol and 5-caprolactam, characterized in that, in order to increase the purity of the target product, the alkylphenols are first fractionated before starting its mixture with caprolactam, and water and a liquid saturated hydrocarbon, for example n-hexane, is distilled or cyclohexane, and isolate the desired product from the aqueous layer. Sources of information taken into account during the examination 1. Patent of England No. 1021709, cl. C 2 C, pub. 196t.
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引用文献:

公开号 | 申请日 | 公开日 | 申请人 | 专利标题

US2737511A|1956-03-06|Extraction of lactam |

US3145198A|1964-08-18|piija|

FR1095772A|1953-03-19|1955-06-06|Stamicarbon|Process for purifying lactams|US4013640A|1974-04-11|1977-03-22|Union Carbide Corporation|Process for the recovery of amides|

IT1113404B|1979-02-28|1986-01-20|Snia Viscosa|INTERNATIONAL PATENTS S.R.L. VIA BRENTANO 2 MILAN|

IT7922250D0|1979-04-30|1979-04-30|Milano Snia Viscosa Societa Na|METHOD FOR THE PURIFICATION OF RAW CAPROLACTAM.|

US4328154A|1980-11-03|1982-05-04|Snia Viscosa Societa' Nazionale Industria Applicazioni Viscosa S.P.A.|Process for the purification of raw caprolactam|

法律状态:

优先权:

申请号 | 申请日 | 专利标题

IT26385/72A|IT956941B|1972-06-28|1972-06-28|PROCEDURE FOR THE PREPARATION OF PURE LACTAM FROM ITS PRIMARY SOLUTIONS IN ORGANIC SOLVENT|

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