CN204973830U

CN204973830U - Tower continuous production device of grignard reagent preparation

Info

Publication number: CN204973830U
Application number: CN201520705587.6U
Authority: CN
Inventors: 袁益中
Original assignee: ZHEJIANG HUAYI ENGINEERING DESIGN Co Ltd
Current assignee: Zhejiang Huayi engineering Tsukito design Inc
Priority date: 2015-09-14
Filing date: 2015-09-14
Publication date: 2016-01-20
Anticipated expiration: 2025-09-14

Abstract

The utility model discloses a tower continuous production device of grignard reagent preparation, including tower reactor, magnesium material feeding device, reactant and the leading -in pipeline of initiating agent, a reaction mixture circulation pipeline who has upper and lower zhi duan, magnesium material feeding device intercommunication is in the tower reactor upper end, tower reactor inside has multistage agitation roller and multistage heat exchanger, the tower reactor upper end has magnesium material filter screen, and it derives the pipeline to have a grignard reagent above above -mentioned magnesium material filter screen, props up the end on of the above -mentioned reaction mixture circulation pipeline of above -mentioned magnesium material filter screen below intercommunication, the circulating pump that passes through of the bottom suspension end of above -mentioned reaction mixture pipeline communicates with the tower reactor bottom. The utility model discloses can solve and how carry out continuous mass production to grignard reagent, need not the secondary and cause the process, can reduce simultaneously the technical problem of the required heat medium of required nitrogen gas of replacement air and dry reaction equipment.

Description

Tower continuous production device prepared by RMgBr

Technical field

The utility model relates to a kind of process units preparing grignard reagent.

Background technology

RMgBr is reacted by organohalogen compound and magnesium metal and forms organomagnesium reagent in absolute ether, is called " Grignard reagent ", is called for short " RMgBr ".Rear french chemist Nore awns obtains RMgBr using tetrahydrofuran as solvent in nineteen fifty-three.This improvement is called " Grignard-Nore awns reaction ".Now conventional halogenated hydrocarbons and magnesium powder react obtained in absolute ether or oxolane, and preparation process must have the material of active hydrogen without ethanol etc. without carbon dioxide at absolute, as: carry out under the conditions such as water, alcohol, ammonia NH3, hydrogen halides, end alkynes.Usually represent with general formula R MgX.Grignard reagent is a kind of active organic synthesis reagent, can carry out multiple reaction, mainly comprise: alkylated reaction, Carbonyl addition, conjugate addition, and halogenated hydrocarbons reduction etc.RMgBr generally has two kinds, 1: chlorobenzene class as benzyl chloride at ether as under oxolane and reactive magnesium, 2: bromocyclopentane at ether as under oxolane and magnesium or zinc reaction.

Please refer to Fig. 1, what Fig. 1 showed is traditional device be prepared grignard reagent, and this device mainly comprises a reactor, an initiator feed pipeline, reaction-ure feeding pipeline, a set of temperature of reaction kettle regulating system, an a set of cooling system; Wherein reactor is used for the reacting environment as various reactant, initiator feed pipeline is used for initator to import to reactor, reaction-ure feeding pipeline is used for reactant to put into reactor, humidity control system is for regulating the temperature of reactor, and the reactant that cooling system is used for reactor gasification or evaporation imports to reactor again.

Above-mentioned conventional design is prepared as intervalization production to RMgBr, the steps include: first dry reaction still, with the air of nitrogen replacement reaction kettle, the magnesium granules prepared in advance is dropped into reactor according to quantity, adds a certain amount of ethers organic matter and causes.To be triggeredly to complete, cooling limit, limit dropwise reaction thing halogenated hydrocarbons, to having reacted.

The shortcoming that above-mentioned conventional design has has: intermittent reaction, cannot continuous seepage, cannot realize Automated condtrol; And often a collection ofly all needing elicitation procedure, a large amount of heating agent needed for dry reaction still, the nitrogen needed for displacement tower reactor 2 air and initator of consuming is as ether compound etc.

Utility model content

The purpose of this utility model is to provide tower continuous production device prepared by a kind of RMgBr, solves and how to produce in enormous quantities continuously RMgBr, without the need to secondary elicitation procedure; The technical problem of the nitrogen needed for displaced air and the heating agent needed for dry reaction equipment can be reduced simultaneously.

Tower continuous production device prepared by RMgBr, comprises a tower reactor, magnesium material cast feeder, a reactant and an initator incoming line, a reactant mixture circulation line with upper and lower Zhi Duan; Magnesium material cast feeder is communicated with in tower reactor upper end; Tower reactor inside has Multi-stage stirring roller and multi-stage heat exchanger; Tower reactor upper end has magnesium material screen pack, and above above-mentioned magnesium material screen pack, have RMgBr derives pipeline, an end on be communicated with above-mentioned reactant mixture circulation line below above-mentioned magnesium material screen pack; The circulating pump that passes through of lower end of above-mentioned reactant mixture pipeline is communicated with tower reactor bottom; Reactant and initator incoming line are communicated with the bottom of tower reactor by a feed pump.

Described tower reactor inside has three grades of agitating rollers and three grades of heat exchangers, and above-mentioned each agitating roller becomes one-to-one relationship with each heat exchanger.

The beneficial effects of the utility model are: the utility model adopts magnesium material cast feeder quantitatively to feed intake to enter tower reactor inside and realizes feeding-in solid body, and initator of the present utility model and reactant realize liquid charging by feed pump, flowmeter, control valve from the bottom-up continous-stable charging of tower reactor; In tower reactor, magnesium material moves from top to bottom, and the liquefied mixture material that initator and reactant are formed, to lower and upper motion, can make solid liquid phase fully contact like this; Increase by a road reactant mixture circulation line simultaneously, by controlling the flow of this pipeline, not only can reduce the speed that magnesium material sinks, also can increase the solid-liquid phase reaction time, impel it fully to react; By aforesaid operations and layout, can guarantee like this to produce grignard reagent in enormous quantities; After once causing, without the need to secondary elicitation procedure; Also the nitrogen needed for displaced air and the heating agent needed for dry reaction equipment can be reduced; Automated condtrol process can be realized; Guarantee halogenated hydrocarbons complete reaction, and excessive magnesium grain is trapped within reactor, next reaction process can not be entered; If wherein it should be noted that, halogenated hydrocarbons is excessive, unstable when subsequent acidic Water Under solution, so preferentially guarantee halogenated hydrocarbons complete reaction.

Accompanying drawing explanation

Fig. 1 is the device that existing conventional form reagent is prepared;

Fig. 2 is the device that in specific embodiment, grignard reagent is prepared;

An end on 1. magnesium material cast feeders, 2. tower reactor in figure, 21. agitating rollers, 22. heat exchangers, 221. heat conductive oil inlets, 222. conduction oils outlets, 23. magnesium material screen packs, 3. reactant and initator incoming line, 4. reactant mixture circulation line, 41., 42. times ends, 5. RMgBr derive pipeline, 6. feed pump, 7. circulating pump.

Detailed description of the invention

Please refer to Fig. 2, tower continuous production device prepared by the RMgBr in figure, comprise the reactant mixture circulation line 4 that a magnesium material cast feeder 1, tower reactor 2, reactant and initator incoming line 3, have upper and lower Zhi Duan.

Magnesium material cast feeder 1 is mainly as inner in magnesium grain imports to tower reactor 2 by magnesium material, and the magnesium material cast feeder 1 in this figure has two introducing ports and is communicated with in tower reactor 2 upper end, and it conveniently carries out continuous dosing as required.

Tower reactor 2 is the core innovative point of the present embodiment, it adopts and is communicated to bottom it by reactant and initator incoming line 3 by built-in for heat exchanger 22 simultaneously, add reactant mixture circulation line 4, thus realize solid liquid phase and fully contact, after reaction completes, qualified RMgBr is derived pipeline 5 from RMgBr and is derived.Above-mentioned tower reactor 2 inside has three grades of agitating rollers 21 and three grades of heat exchangers 22, and each agitating roller 21 is arranged up and down with each 22 one-tenth, heat exchanger one-to-one relationship.Heat exchanger 22 mainly adopts conduction oil heat exchange, and each heat exchanger 22 has heat conductive oil inlet 221 and conduction oil outlet 222 outside tower reactor 2.Tower reactor 2 upper end has a magnesium material screen pack 23, and above above-mentioned magnesium material screen pack 23, have RMgBr derives pipeline 5, an end 41 on be communicated with above-mentioned reactant mixture circulation line 4 below above-mentioned magnesium material screen pack 23; The circulating pump 7 that passes through of lower end 42 of above-mentioned reactant mixture pipeline 4 is communicated with tower reactor 2 bottom; The mixture that such magnesium material, reactant, initator are formed just can at tower reactor 2 constantly circular response under the effect of circulating pump 7, and after reaction completes, qualified RMgBr is derived pipeline 5 from RMgBr and derived.

Reactant and initator incoming line 3 are communicated with reactant source and initator source, and this pipeline is communicated with the bottom of tower reactor 2 by a feed pump 6, reactant and initator are imported to tower reactor 2 like this under the effect of feed pump 6 inner.

Claims

1. the tower continuous production device prepared of RMgBr, is characterized in that: comprise a tower reactor, magnesium material cast feeder, a reactant and an initator incoming line, a reactant mixture circulation line with upper and lower Zhi Duan; Magnesium material cast feeder is communicated with in tower reactor upper end; Tower reactor inside has Multi-stage stirring roller and multi-stage heat exchanger; Tower reactor upper end has magnesium material screen pack, and above above-mentioned magnesium material screen pack, have RMgBr derives pipeline, an end on be communicated with above-mentioned reactant mixture circulation line below above-mentioned magnesium material screen pack; The circulating pump that passes through of lower end of above-mentioned reactant mixture pipeline is communicated with tower reactor bottom; Reactant and initator incoming line are communicated with the bottom of tower reactor by a feed pump.

2. according to tower continuous production device prepared by the RMgBr described in claim 1, it is characterized in that: described tower reactor inside has three grades of agitating rollers and three grades of heat exchangers, and above-mentioned each agitating roller becomes one-to-one relationship with each heat exchanger.