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A kind of production method of single nitrogen-containing heterocyclic compound

A technology of nitrogen heterocyclic compounds and heterocyclic compounds, which is applied in the field of production of single nitrogen heterocyclic compounds, can solve problems such as poor safety performance, low product yield, and rare raw materials, so as to reduce fugitive emissions, activity and High selectivity, process safety and environmental protection

Active Publication Date: 2020-11-27
北京恒瑞新霖科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0021] In order to overcome some difficulties faced by the existing single nitrogen-containing heterocyclic compounds: difficult environmental protection treatment, relatively rare raw materials, low product yield, low product purity and high moisture, poor safety performance and many other problems, the present invention provides a Preparation method of single nitrogen-containing heterocyclic compound

Method used

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  • A kind of production method of single nitrogen-containing heterocyclic compound
  • A kind of production method of single nitrogen-containing heterocyclic compound
  • A kind of production method of single nitrogen-containing heterocyclic compound

Examples

Experimental program
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Effect test

Embodiment 1

[0044] Take phthalide (another name o-hydroxymethylbenzoic acid lactone, content 99%) and dissolve it in water at 85°C according to the mass ratio of 1:1, and enter a continuous tubular reactor R101 (inner diameter 80mm, length 6m ) enters at 1m below the center, the internal catalyst is alumina containing 1.5wt% CaO, and the feed rate is 10L / h. Liquid ammonia enters from the lower part of the R101 reactor and reacts in reverse with the phthalide aqueous solution. The feed rate is 2.5L / h, and the converted molar ratio is about 2.2. The crude product (the amount of phthalide contained therein is 0.2wt%) enters the secondary flash tank, and the liquid is taken out in the lower part of the second flash tank, and subsequently obtains a compound containing 89 wt% indolinone (type I compound), wherein water Content 10wt%, phthalide 0.6wt%, free amine 2400ppm, the above-mentioned mixture containing indolinone is mixed with hot hydrogen by a metering pump and then enters the vaporizer...

Embodiment 2

[0046] γ-butyrolactone (content 99.5%) and liquid ammonia enter a continuous tubular reactor R101 (inner diameter 120mm, length 15m) according to the molar ratio of 1: 1.8 through metering pump, reaction temperature 260-270 ℃, reaction pressure 8.0MPa, The feed rate is 60L / h. The crude product (the gamma-butyrolactone amount contained therein is 0.4wt%) in the top of the outlet R101 enters the three-stage flash tank, and the liquid is taken out at the third-stage flash tank bottom, and subsequently obtains a product containing 95wt% 2-pyrrolidone (I type compound), wherein the water content is 4.5wt%, butyrolactone 0.4wt%, free amine 600ppm, the above-mentioned mixture containing 2-pyrrolidone is mixed with hot hydrogen by a metering pump and then enters the vaporizer, and the liquid feed rate is 5L / h, the hydrogen feed rate is 20NM3 / h, the equivalent hydrogen to 2-pyrrolidone molar ratio is 14.5, and after being overheated by a superheater (control temperature 230-250°C), it...

Embodiment 3

[0048] δ-valerolactone (content 99.8%) and monoethylamine aqueous solution (monoethylamine content 70wt%) enter a continuous stirred tank reactor R101 (2NM 3), the reaction temperature is 150°C, the reaction pressure is 2.5MPa, the catalyst is in powder form, the content is 2wt% of magnesium oxide, 45% of aluminum oxide, 53wt% of silicon oxide, and the amount of feed and output is 400L / h. The crude product (wherein containing δ-valerolactone amount is 1.5wt%) of the top of outlet R101 enters the first-stage flash tank, and the liquid is taken out at the bottom of the flash tank, and then obtained containing 93wt% 2-ethyl-piperidone ( Type I compound), wherein water content 1.2wt%, δ-valerolactone 0.8wt%, free amine 200ppm, the above-mentioned mixture containing 2-ethyl-piperidone is mixed with hot hydrogen by a metering pump and enters the vaporizer , the liquid feed rate is 10L / h, the hydrogen feed rate is 60NM 3 / h, the equivalent hydrogen to 2-ethyl-piperidone molar ratio ...

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Abstract

The invention discloses a production method of a single nitrogenous heterocyclic ring-containing compound. Lactone and fatty amine which are cheap and easy to obtain are used as raw materials for producing the single nitrogenous heterocyclic ring-containing compound; lactone and fatty amine are used for synthesis of amide, and hydrodeoxygenation is carried out in order to obtain the corresponding nitrogenous heterocyclic compound. The process has only two reaction steps, and has the advantages of low investment, high yield, simple separation for intermediate products, few by-products, and easy processing.

Description

technical field [0001] The invention relates to a production method of a single nitrogen-containing heterocyclic compound, more specifically, a method for producing a single nitrogen-containing heterocyclic compound by using cheap and easily available lactone and aliphatic amine as raw materials. Background technique [0002] Containing a single nitrogen heterocyclic compound is a large class in the heterocyclic compound, and the single nitrogen heterocyclic compound that the present invention relates to includes the following classes (R1, R2, R3, R4 in the following molecular formula (3)-(8) , R5 is selected from one of -H and alkane groups. [0003] (1) Heterocyclic compounds containing pyrrolidine structure, such as tetrahydropyrrole, N-methylpyrrolidine, N-ethylpyrrolidine, 4-methyl-N-ethylpyrrolidine, 2,3-dimethyl -N-Propylpyrrolidine, etc. [0004] [0005] (2) Heterocyclic compounds containing piperidine structure, such as piperidine, N-methylpiperidine, N-ethylp...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D209/44C07D207/04C07D211/10
Inventor 不公告发明人
Owner 北京恒瑞新霖科技有限公司
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