Dehydrogenation ammoniation method for producing pyrrolidine with 1,4butanediol

A technology of tetrahydropyrrole and butanediol, which is applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, organic chemistry, etc., can solve the problem of increasing the difficulty of product purification, high equipment requirements, and unfavorable large-scale Large-scale industrial production and other issues, to achieve the effect of reducing the difficulty of product purification and separation, high conversion rate and yield of raw materials, and easy sewage treatment

Inactive Publication Date: 2009-08-19
刘丽川
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These methods mainly react under the condition of hydrogen, have the disadvantages of harsh conditions, high equipment requirements, and difficult operation, and generally cannot react under normal pressure.
High pressure reaction requires high safety, equipment manufacturing and production costs are expensive, which is not conducive to increasing production capacity and large-scale industrial production
Most of the existing synthesis methods are medium and high pressure reactions. During the synthesis process, a large amount of water participates in the reaction, which wastes energy, increases the difficulty of product purification, and increases the difficulty and cost of sewage treatment.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0008] Embodiment 1: use gas phase fixed bed as reactor, add 3~5mm granular SO in gas phase fixed bed 4 2- / MxOy rare earth metal compound supported catalyst (for SO 4 2- / TiO 2 -SnO 2 -Al 2 o 3 Solid superacid catalyst) 150g; heat up to 280°C at a space velocity of 50-55cm 3 / min Input nitrogen into the reactor, so that the catalyst is always under the protection of nitrogen. Use a metering pump to feed 1,4-butanediol and water in a ratio (molar ratio) of 1:0.4, and feed the vapor of 1,4-butanediol and water into the reactor at a weight space velocity of 0.6g / min. At the same time, feed ammonia gas to make the molar ratio of 1,4-butanediol and ammonia 1:1.3, and make the molar ratio of 1,4-butanediol, ammonia and water 1:1.3:0.4. The reaction pressure is 0-0.1Mpa. The above-mentioned raw materials generate a mixture under the action of a catalyst, and the objects flowing out from the outlet of the reactor are condensed by a condensing device to obtain a mixture solve...

Embodiment 2

[0009] Embodiment 2: Different from Embodiment 1 is SO 4 2- / MxOy rare earth metal compound supported catalyst is SO 4 2- / CuO-ZnO-Al 2 o 3 Solid superacid catalyst; the molar ratio of 1,4-butanediol, ammonia and water is 1:1.5:1. The reaction temperature is 290°C. The conversion rate of 1,4-butanediol is 100%, the yield rate of tetrahydropyrrole is 91%, and the by-product is mainly water. The rest is the same. So I won't repeat it any more.

Embodiment 3

[0010] Embodiment 3: Different from Embodiment 1 is SO 4 2- / MxOy rare earth metal compound supported catalyst is SO 4 2- / TiO 2 -SnO 2 -Al 2 o 3 Solid superacid catalyst; the molar ratio of 1,4-butanediol, ammonia and water is 1:2:3. The steam of 1,4-butanediol and water is fed into the reactor at a weight space velocity of 0.7 g / min. The reaction temperature is 320°C. The conversion rate of 1,4-butanediol is 100%, the yield rate of tetrahydropyrrole is 90.5%, and the by-product is mainly water. The rest is the same. So I won't repeat it any more.

[0011] SO 4 2- / TiO 2 -SnO 2 -Al 2 o 3 Solid superacid catalyst and SO 4 2- / CuO-ZnO-Al 2 o 3 The solid superacid catalysts are all existing products.

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Abstract

The method belongs to a method for producing tetrahydropyrrole. The method comprises the following steps: taking 1,4-butyleneglycol, ammonia and water with the mol ratio of 1:1.3-2:0.4-3 as raw materials, heating and vaporizing to reach reaction temperature of 240-330 DEG C, introducing into a reactor at the weight space velocity of 0.6-0.7g / min under the protection of nitrogen, passing through a gas-phase fixed bed filled with an SO4 / MxOy rare earth compound supported catalyst, performing catalytic reaction at the reaction pressure of 0-0.1MPa, condensing a reactant to obtain a solvent mixture, distilling and purifying the solvent mixture, and collecting a distillate with the temperature of 86-90 DEG C to obtain crude tetrahydropyrrole. In the method, the tetrahydropyrrole is synthesized by reaction in a low pressure state, a little water is added in the synthesis process to reduce difficulty in purifying and separating the product, and the method has the advantages of safety and high efficiency, simple production process, low production cost, energy conservation, easy wastewater treatment, easy environmental protection, and high raw material conversion rate and yield.

Description

technical field [0001] The invention belongs to a method for producing tetrahydropyrrole. Background technique [0002] Tetrahydropyrrole is a cyclic secondary amine with pKb=2.9, which has the properties of a general amine. fields have a wide range of uses. [0003] Its preparation methods in the past mainly include: tetrahydrofuran and ammonia catalytic synthesis method, hydrogenation denitrogenation method, etc. The synthesis of tetrahydropyrrole compounds can also be carried out by other methods, among which the more representative ones are: 1,4-butanediamine catalytic hydrogenation denitrogenation method, 1,4-butanedinitrile hydrogenation method, pyrrole hydrogenation method , pyrrolidone hydrogenation method, etc. These methods mainly react under the condition of hydrogen, have the disadvantages of harsh conditions, high equipment requirements, and difficult operation, and generally cannot be reacted under normal pressure. The high-pressure reaction requires high s...

Claims

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Application Information

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IPC IPC(8): C07D295/023C07D295/027B01J27/053B01J23/14B01J23/80
Inventor 刘丽川
Owner 刘丽川
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