Method for preparing N-methylmorpholine through catalyst
A technology for the preparation of methylmorpholine and catalysis, which is applied in the chemical industry, can solve the problems of low conversion rate and cumbersome N-methylmorpholine method, and achieve the effects of high conversion rate, simple and feasible method, and reduced catalytic efficiency
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2017-02-01
- Estimated Expiration
- Not applicable · inactive patent
Abstract
Description
technical field
[0001] The invention belongs to the field of chemical industry and relates to chemical intermediates, in particular to a method for catalytically preparing N-methylmorpholine. Background technique
[0002] N-Methylmorpholine is a heterocyclic tertiary amine. The pure product is a colorless liquid with an ammonia smell. It is mainly used as a foaming catalyst, extraction agent, solvent, etc. for the synthesis of polyurethane plastics. It is also a synthetic medicine, pesticide, surface Important intermediates of active agents, etc.
[0003] The existing methods for synthesizing N-methylmorpholine are relatively cumbersome, or the conversion rate is low. Contents of the invention
[0004] The object of the present invention is to provide a kind of method that catalyzes the preparation of N-methylmorpholine.
[0005] Above-mentioned purpose of the present invention is achieved by following technical scheme:
[0006] A method for catalytically preparing N-me...
Examples
Embodiment 1
[0019] Embodiment 1: the method for catalytically preparing N-methylmorpholine
[0020] Including the preparation steps as described below:
[0021] Step S1, packing the rare earth-based solid catalyst into the tubular reactor;
[0022] In step S2, the liquid raw material N-methyldiethanolamine is placed in the raw material tank, and the sample is fed at a constant speed by a sampling pump. The raw material liquid passes through the rare earth-based solid catalyst in the tubular reactor for intramolecular dehydration reaction, and the liquid volume of the raw material liquid is Airspeed is 0.3h- 1 , the reactor temperature is 250°C;
[0023] Step S3, condensing and collecting the reaction solution obtained in step S2 through a condenser, adding caustic soda to separate the reaction solution, taking the upper liquid for atmospheric distillation, collecting fractions at 115-116°C, and obtaining the target product N-methylmorpholine; liter of reaction solution was added caust...
Embodiment 2
[0026] Embodiment 2: the method for catalytically preparing N-methylmorpholine
[0027] Including the preparation steps as described below:
[0028] Step S1, packing the rare earth-based solid catalyst into the tubular reactor;
[0029] In step S2, the liquid raw material N-methyldiethanolamine is placed in the raw material tank, and the sample is fed at a constant speed by a sampling pump. The raw material liquid passes through the rare earth-based solid catalyst in the tubular reactor for intramolecular dehydration reaction, and the liquid volume of the raw material liquid is The air speed is 0.1h -1 , the reactor temperature is 200°C;
[0030] Step S3, condensing and collecting the reaction solution obtained in step S2 through a condenser, adding caustic soda to separate the reaction solution, taking the upper liquid for atmospheric distillation, collecting fractions at 115-116°C, and obtaining the target product N-methylmorpholine; Add 2 g of caustic soda to the liter...
Embodiment 3
[0033] Embodiment 3: the method for catalytically preparing N-methylmorpholine
[0034] Including the preparation steps as described below:
[0035] Step S1, packing the rare earth-based solid catalyst into the tubular reactor;
[0036] In step S2, the liquid raw material N-methyldiethanolamine is placed in the raw material tank, and the sample is fed at a constant speed by a sampling pump. The raw material liquid passes through the rare earth-based solid catalyst in the tubular reactor for intramolecular dehydration reaction, and the liquid volume of the raw material liquid is Airspeed is 0.5h -1 , the reactor temperature is 300°C;
[0037] Step S3, condensing and collecting the reaction solution obtained in step S2 through a condenser, adding caustic soda to separate the reaction solution, taking the upper liquid for atmospheric distillation, collecting fractions at 115-116°C, and obtaining the target product N-methylmorpholine; Add caustic soda 4g to liter reaction sol...