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A kind of synthetic method of 1,2-propanediamine

A synthetic method and technology of propylenediamine, applied in the first field, can solve problems such as unfavorable industrial production, difficult separation, difficult operation, etc., and achieve the effects of easy separation, high selectivity and simple operation

Active Publication Date: 2016-04-27
XIAN MODERN CHEM RES INST
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] Under normal pressure conditions, the boiling point of isopropanolamine is 159.4°C, and the boiling point of 2,5-dimethylpiperazine is 175.0°C. The by-product of 2,5-dimethylpiperazine and the raw material of isopropanolamine will form a minimum azeotrope Composition, the azeotropic temperature is 159.18°C, and the weight percentage is: 83.7% of isopropanolamine, 16.3% of 2,5-dimethylpiperazine, unreacted due to the existence of 2,5-dimethylpiperazine The raw material isopropanolamine is difficult to separate during rectification and recovery, and the operation is difficult, which is not conducive to industrial production

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  • A kind of synthetic method of 1,2-propanediamine

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preparation example Construction

[0028] The preparation of the metal-loaded catalyst in the present invention can be carried out using conventional catalyst steps, such as the following steps: the carrier is dried in a vacuum oven at 150° C. to 300° C. for 2 hours, and then mixed with a solution containing Ni or Co metal salt and a metal additive Re or non-metallic additive B, fully immersed in ultrasonic waves for 1.5h; filter off excess liquid to obtain a carrier with adsorbed metal ions, dry in a vacuum oven at 150°C to 300°C for 3h, and then continue to immerse in the remaining solution 2h; the carrier impregnated twice is calcined in a box-type resistance furnace at 300° C. to 400° C. for 6 hours to prepare a catalyst precursor.

[0029] The catalyst precursor is reductively activated in a tubular reactor, heated to 250°C to 300°C for about 4 hours and kept for 1 hour, while H 2 and N 2 6:1 (volume ratio) gas flow through the reaction tube, continue to heat to 350 ℃ ~ 350 ℃ and constant temperature acti...

Embodiment 1

[0034] The catalyst is a nickel-based supported catalyst, and the carrier is Al 2 o 3 , Ni is Al 2 o 3 15% of the mass of the carrier, and the non-metallic additive B is 3% of the mass of the carrier.

[0035] With 110g of isopropanolamine, 3.3g supported catalyst, 55g water, 0.55gNa 2 CO 3 The auxiliary agent is added into the autoclave, the air in the autoclave is replaced by hydrogen, and then evacuated, 42g of liquid ammonia is introduced, the hydrogen is continuously introduced to 2MPa, the temperature is raised to 185°C, and the reaction is carried out for 8h. After the reaction, the reaction solution was cooled to room temperature, and the reaction solution was filtered to recover the catalyst. Based on the consumption of isopropanolamine per unit weight, the conversion rate is 38.2%, and the selectivity of 1,2-propylenediamine is 99.6%. The reaction filtrate was analyzed by GC, and no 2,5-dimethylpiperazine was detected.

[0036] The reaction solution is distill...

Embodiment 2

[0038] The catalyst is a nickel-based supported catalyst, and the carrier is Al 2 o 3 , Ni is Al 2 o 3 20% of the mass of the carrier, and the metal additive Re is 1% of the mass of the carrier.

[0039] With 95g of isopropanolamine, 2.9g nickel-based supported catalyst, 95g water, 4.75gK 2 CO 3 The auxiliary agent is added into the autoclave, the air in the autoclave is replaced by hydrogen, and then vacuumized, 45g of liquid ammonia is introduced, the hydrogen is continuously introduced to 3MPa, the temperature is raised to 195°C, and the reaction is carried out for 8h. After the reaction, the reaction solution was cooled to room temperature, and the reaction solution was filtered to recover the catalyst. Based on the consumption of isopropanolamine per unit weight, the conversion rate is 59.5%, and the selectivity of 1,2-propylenediamine is 97.3%. The reaction solution was distilled to remove water, and further rectified to obtain the pure product of 1,2-propanediamin...

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Abstract

The invention relates to a synthesis method of 1,2-propane diamine. The method comprises the steps of preparing 1,2-propane diamine via reaction between isopropanolamine and liquid ammonia in the presence of hydrogen, a catalyst, an assistant and a reaction solvent. Compared with the prior art, since the reaction solvent is added, and due to solvation of the solvent and the reaction material, the probability of the reaction product 1,2-propane diamine continuing to participate in reaction to generate a cyclamine product is reduced; at the same time, the alkali metal and alkaline-earth metal assistant is added into a reaction system, and the base strength of the reaction system is changed, so that dehydrogenation of the catalyst to the reaction material is inhibited; and the selectivity of the product 1,2-propane diamine is improved.

Description

technical field [0001] The invention belongs to the field of catalytic synthesis, and in particular relates to a synthesis method of 1,2-propanediamine. Background technique [0002] 1,2-Propylenediamine is a raw material for the synthesis of important medicines or pharmaceutical intermediates such as 2,3,5-trimethylpyrazine, dexrazoxane, and tobacco. It is an important passivator in the oil industry. Epoxy resin curing accelerator and spandex chain extender can be used to modify shellac coatings, as well as raw materials for rubber and dyes, and can also be used as electroplating additives, or Cu 2+ 、Co 2+ , Ca 2+ Chelating agent for metal ions, ore dressing agent, etc. [0003] At present, 1,2-propanediamine is mainly continuously prepared from alcohol amine, alkylene oxide or diol as raw materials, using active metal or metal-supported catalysts, in the presence of hydrogen, in a high-pressure ammonia atmosphere, by reductive amination method The preparation is carrie...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C209/16C07C211/11
Inventor 杨建明余秦伟李亚妮王为强惠丰王伟袁俊张前吕剑
Owner XIAN MODERN CHEM RES INST