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Method for catalytic synthesis of piperazine and triethylenediamine from ethylenediamine under solvent-free condition

A technology for the catalytic synthesis of piperazine and triethylenediamine catalyzed by ethylenediamine, which is applied in the direction of organic chemistry, can solve the problems of increased solvent recovery load, difficulty in azeotropic distillation separation, increased production costs, etc., and achieves the reduction of by-product yield, The separation process is simplified and the production cost is reduced

Active Publication Date: 2019-03-05
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The use of a large number of solvents or diluents will inevitably increase the solvent recovery load, bring a lot of power, heat and other cycle consumption, and increase production costs
What's more serious is that organic amines such as ethylenediamine, PIP, and TEDA can form azeotropes with various solvents, and only the azeotropic composition of the corresponding components can be obtained under conventional atmospheric distillation. Expensive special distillation methods such as azeotropic distillation, extractive distillation or pressurized distillation, etc., for dehydration and separation of azeotropes and near-boilers, the process operation is complicated, and the equipment investment is also large
Taking ethylenediamine as an example, in azeotropic distillation, hydrocarbons such as benzene, toluene, xylene, cyclohexane, and esters such as ethyl acetate, which are commonly used as entrainers, form binary azeotropes with ethylenediamine, and form binary azeotropes with water. -Ethylenediamine forms a ternary azeotrope, and azeotropic distillation separation is very difficult; for example, US3454645 and CN101723837A disclose the extraction and rectification process of the ethylenediamine-water system of strong basic extractant and ether extractant respectively, but because For the corrosion of equipment, and the introduction and accumulation of impurities in the extractant, the process operation is extremely complicated, and the equipment investment increases

Method used

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  • Method for catalytic synthesis of piperazine and triethylenediamine from ethylenediamine under solvent-free condition
  • Method for catalytic synthesis of piperazine and triethylenediamine from ethylenediamine under solvent-free condition

Examples

Experimental program
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Effect test

Embodiment 1

[0030] The catalyst used in this example is the hierarchically porous ZSM-5 molecular sieve disclosed in CN105712379A mentioned above, ion-exchanged with ammonium acetate and calcined in air at 500°C to obtain a hierarchically porous H-ZSM-5 molecular sieve catalyst. refer to figure 1 , the reaction process is: the feed mass space velocity of the raw material stream M is 0.5h -1 , after being preheated to 350°C, it enters the tube side of the reactor R with a tube-shell structure, and fills it with a multi-stage porous H-ZSM-5 molecular sieve catalyst. After the raw material stream M undergoes a contact reaction, the The product stream P obtained at the top extraction outlet was sampled for gas chromatography analysis, and the results obtained are shown in Table 1.

[0031] The product stream P from the reactor directly enters the rectification tower (it has a tower top and a bottom extraction outlet and an upper zone and a lower zone sideline extraction outlet; the number of...

Embodiment 2

[0033] The catalyst used in this embodiment is the mesoporous and microporous mordenite molecular sieve catalyst disclosed in CN106032281A mentioned above as the multi-level porous mordenite molecular sieve catalyst. refer to figure 1 , the reaction process is: the feed mass space velocity of the raw material stream M is 1.0h -1 , after being preheated to 300°C, it enters the tube side of the reactor R with a tube-shell structure, where it is filled with a multi-stage porous mordenite molecular sieve catalyst. The obtained product stream P was sampled and analyzed by gas chromatography, and the results obtained are shown in Table 1.

[0034] The product stream P from the reactor directly enters the rectification tower (it has a tower top and a tower bottom outlet and an upper zone and a lower zone sideline outlet; the number of theoretical plates is 30, the temperature of the tower bottom is 185 ° C, and the temperature of the tower top is 110 DEG C), through the rectifying ...

Embodiment 3

[0036] This embodiment uses the Beta molecular sieve with the hierarchical pore structure disclosed in CN104418348A mentioned above to undergo the ammonium acetate ion exchange and the hierarchically porous H-Beta molecular sieve obtained after roasting in air at 500°C as the hierarchically porous H-Beta molecular sieve catalyst . refer to figure 1 , the reaction process is: the feed mass space velocity of the raw material stream M is 2.0h -1 , after being preheated to 400°C, it enters the tube side of the tube-shell reactor R, where it is filled with a multi-stage porous H-Beta molecular sieve catalyst. The product stream P obtained at the outlet was sampled and analyzed by gas chromatography, and the results obtained are shown in Table 1.

[0037] The product stream P from the reactor directly enters the rectification tower (it has a tower top and a tower bottom outlet and an upper zone and a lower zone sideline outlet; the number of theoretical plates is 70, the temperatu...

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Abstract

The invention provides a method for catalytic synthesis of piperazine and triethylenediamine from ethylenediamine under a solvent-free condition. The method includes feeding pure ethylenediamine independently into a reactor, and performing catalytic conversion under a certain condition on a mesoporous / microporous composite multistage pore molecular sieve catalyst without any solvent to obtain a product needed. The piperazine and triethylenediamine are prepared by the method with high yields, a separation process is simple, energy consumption is lower, the production cost is reduced, and a difficult separation problem of azeotropes and compounds with close boiling points and a solvent recovery and purification problem are solved fundamentally. In addition, a part of or all product piperazine and a byproduct N-ethylpiperazine are recycled to increase the yield of triethylenediamine, flexible control of the yields of the piperazine and triethylenediamine is achieved while the yield of byproducts is reduced, and economic performance and competitiveness of the process are further enhanced.

Description

Technical field [0001] The invention belongs to the field of chemical engineering, and particularly relates to a method for synthesizing piperazine and triethylenediamine from ethylenediamine gas solid-phase catalysis under solvent-free conditions. Background technique [0002] Piperazine (abbreviated as PIP) is an important chemical intermediate with great utilization value in the chemical and pharmaceutical fields. It is also widely used as a surfactant and a chemical raw material for synthetic resins and synthetic fibers. In recent years, as the most widely used polyurethane catalyst, the demand for triethylenediamine (TEDA) has been increasing day by day. In addition, triethylenediamine can also be used as an ethylene polymerization and ethylene oxide polymerization catalyst. Its derivatives can be used as corrosion inhibitors and emulsifiers. As the scope of application becomes more and more extensive, the prices of PIP and TEDA have remained high for a long time, and ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D295/023C07D295/027C07D487/08C07D295/03
CPCC07D295/023C07D295/027C07D295/03C07D487/08
Inventor 王莹利刘中民袁翠峪朱书魁
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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