Background technology
Alkali metal 2-Pyrrolidone salt, mainly as catalyst, prepares vinylpyridine for 2-Pyrrolidone and acetylene reaction
The catalyst of pyrrolidone.
Patent No.:200810072060.9, describe 2-Pyrrolidone and the second of the potassium of pyrrolidones containing homogeneous catalyst
The method of alkyne reaction preparing ethylene base pyrrolidones, does not describe the preparation method of pyrrolidones potassium.
《Chemical science and technology market》2004 the 5th phases《The synthesis of NVP》One literary composition discusses 2-Pyrrolidone
Catalyst with acetylene reaction preparing ethylene base pyrrolidones is 2-Pyrrolidone sylvite, and the preparation method of 2-Pyrrolidone sylvite is 2-
Pyrrolidones and potassium hydroxide are dehydrated under vacuum or nitrogen bubble and prepare, Batch Process.
Patent No.:200880119517.5, the catalyst describing 2-pyrrolidones with acetylene reaction is alkali metal pyrrole
Pyrrolidone salt, is prepared with alkali metal hydroxide or reaction of alkali metal alkoxide by 2-pyrrolidones.
Patent No.:Two patents of 200410061451.2 and 201110354299.7 respectively describe a kind of by 2-pyrrole
Pyrrolidone hydrolysis produce the method for 4-Aminobutanoicacid after being acidified under alkalescence.
The reaction equation of 2-Pyrrolidone and potassium hydroxide is as shown in formula 3 and formula 4:
The product of formula 3 be 2-Pyrrolidone sylvite be purpose product, alkalescence is strong, and catalysis activity is good;The product of formula 4 is
4-Aminobutanoicacid sylvite, accessory substance, alkalescence is weak, catalytically inactive.Reduce the way that side reaction occurs and be generally fast dewatering, fast
Speed separates product.The growing amount of accessory substance 4-Aminobutanoicacid sylvite is generally 40-50%, can be entered by the method for constant-current titration
Row detection.
In the industrial production, in order to ensure catalysis activity, improve 2-Pyrrolidone potassium salts content, often take to increase hydrogen-oxygen
Change potassium inventory way realize, the increase of accessory substance when inevitably causing catalyst to manufacture, 2-Pyrrolidone and
Polymeric by-products during acetylene reaction increases, and yield is low, blocks reactor, frequently stops production.
Use alkali metal to react with 2-Pyrrolidone, prepare 2-Pyrrolidone sylvite catalyst, because the reaction time is short, reaction
Speed is fast, and side reaction is few, and catalysis activity is high, and yield is high, is a good selection.But a large amount of hydrogen can be produced at short notice
Gas, and release substantial amounts of heat, will cause the high safety requirements in commercial scale, in order to effectively carry out alkali-metal dispersion and
The removal of heat, the realization that industrial batch produces is deposited and is acquired a certain degree of difficulty.
Content of the invention
For the above-mentioned problems in the prior art, it is an object of the invention to design provides a kind of alkali metal 2-pyrroles
The technical scheme of the preparation method and its usage of the 2-Pyrrolidone solution of alkanone salt, can reduce unit reactor body accordingly
Long-pending alkali metal inventory, controls the rising of temperature and the generating capacity of hydrogen, can the repetition of simple microreactor quantity
Increasing and just can realizing gratifying commercial production scale, its production cost is low, and course of reaction is safe and reliable.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that include
Following steps:
1)By 2-Pyrrolidone feed containers, heater, filter, blender, microreactor, reactant liquor storage tank, alkali metal
Measuring tank and the displacement of connection system nitrogen, displacement to oxygen content is less than 0.5%;
2)Loading the 2-Pyrrolidone of q.s in 2-Pyrrolidone feed containers, in feed containers, the temperature of liquid controls
28 DEG C-35 DEG C, with the heated device of flow of 80-100ml/min, 2-Pyrrolidone is heated to 110-130 DEG C with pump, then passes through
Filter, blender, microreactor return 2-Pyrrolidone feed containers, 1.5-2.5 minute before throwing alkali metal, switch to reaction
In liquid storage tank so that 2-Pyrrolidone and alkali-metal reactant liquor are delivered in reactant liquor storage tank;
3)The alkali metal of q.s is entered in alkali metal measuring tank at the protection down of kerosene, the temperature of alkali metal amount pot liquid
Degree controls at 105-115 DEG C, and the nitrogen-sealed pressure of alkali metal measuring tank is set as 0.35-0.45MPa, then will be molten by pressure
The alkali metal melting extrudes feeding blender bottom alkali metal measuring tank and mixes laggard reactor reaction in a subtle way with 2-Pyrrolidone,
Alkali-metal inlet amount is 0.8-2.2 gram/min, and reacted liquid sends into reactant liquor storage tank after nitrogen displacement abjection hydrogen
In, obtaining the 2-Pyrrolidone solution of the alkali metal 2-Pyrrolidone salt of 0.1-10%, nitrogen-sealed preserves.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that described
Alkali metal be sodium, potassium or Na-K alloy.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that described
2-Pyrrolidone, its molecular structural formula is formula 1:
Have another name called:Pyrrolones, nitrogen penta cyclic ketones, butyrolactam.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that described
Alkali metal 2-Pyrrolidone salt, its molecular structural formula is formula 2:
M:Sodium, potassium, Na-K alloy.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that step
2)In:With the heated device of flow of 85-95ml/min, 2-Pyrrolidone is heated to 115-125 DEG C with pump, preferably with pump with 88-
2-Pyrrolidone is heated to 118-120 DEG C by the heated device of flow of 90ml/min.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that step
3)In:The nitrogen-sealed pressure of alkali metal measuring tank is set as 0.38-0.44MPa, preferably 0.40-0.42MPa.
The preparation method of the 2-Pyrrolidone solution of described a kind of alkali metal 2-Pyrrolidone salt, it is characterised in that step
3)In:Alkali-metal inlet amount is 0.9-1.8/min, preferably 1.2-1.5 gram/min.
2-Pyrrolidone solution for preparing the application in vinyl pyrrolidone with acetylene reaction.
In reaction, produced hydrogen simply can be deviate from degasser.
The microreactor system of this paper is continuous system, participates in the amount of material of reaction and is gram or milliliter level scope, reaction
The channel width of device is typically at 1-10000 m, between preferably 10-1000 m, more preferably 50-150 m.Material is stainless steel, also
The materials such as glass, pottery, plastics can be selected.
Alkali metal uses microporous barrier to mix with the mixing of 2-Pyrrolidone, before material enters reactor, first
Be introduced into a microporous barrier blender, the aperture of microporous barrier typically at 1-1000 m, preferably 10-800 m, more preferably 10-100
Between m.Material is stainless steel, it is also possible to select the material such as pottery, plastics.
The temperature of reaction is to be determined by the melt temperature of alkali metal, 2-Pyrrolidone, the temperature of microreactor system
Alkali metal to be guaranteed, 2-Pyrrolidone have mobility smoothly, and ordinary circumstance reaction temperature less than 2-Pyrrolidone boiling point is
Good.Reaction temperature general control, at 65-240 DEG C, is preferably:80-200 DEG C, more preferably 100-150 DEG C.
Reaction heat is to be taken away by excessive 2-Pyrrolidone, and alkali metal inventory is big, and reactant liquor is from starting to be reacted to
Temperature rise at the end of reaction is just big, and the amplitude that general control reaction temperature rises is 1-120 DEG C, preferably 1-80 DEG C, more preferably
For 1-50 DEG C.Also can select to remove heat with heat exchanger.
The concentration of alkali metal 2-Pyrrolidone salt is to be realized by the proportional quantity of control alkali metal and 2-Pyrrolidone, instead
In should, 2-Pyrrolidone be excessive relative to alkali metal, excessive number can be according to the presence or absence precipitation situation of solution and reactant liquor
Temperature rises situation and determines.
Reaction pressure is according to factor determinations such as blender, reactor resistance, reactant liquor temperature rises.
Alkali metal is carried out in the case of not having mechanical agitation with the reaction of 2-Pyrrolidone, reason be microreactor and
The mixed effect of preposition micropore blender is enough.
The preparation method and its usage of the 2-Pyrrolidone solution of above-mentioned a kind of alkali metal 2-Pyrrolidone salt, preparation process
In without other solvent or auxiliary agent, it is not necessary to process the second solvent, it is not necessary to catalyst, it is not necessary to auxiliary agent carries out disperseing and mixing, slightly
It higher than the relatively low reaction temperature of alkali metal fusing point, extremely low side reaction, is simple, economical on a manufacturing scale and safety
's.
Embodiment 1
2-Pyrrolidone container, heater, filter, blender, microreactor, reactant liquor storage tank and connection system nitrogen are put
Changing, displacement to oxygen content is less than 0.5%.
By the 2-Pyrrolidone of q.s(Fusing point be the boiling point under 24.6 DEG C, normal pressure be 245 DEG C, density 1.116(25/4
℃))Loading in feed containers, in feed containers, the temperature of liquid controls more than 28 DEG C, it is therefore an objective to keep at 2-Pyrrolidone
In liquid condition.With the heated device of flow of 90ml/min, 2-Pyrrolidone is heated to 120 DEG C with pump, then through filter, mixed
Clutch, microreactor return feed storage tank, are throwing metallic sodium first 2 minutes, are switching in reactant liquor storage tank so that 2-Pyrrolidone
Deliver in reactant liquor storage tank with the reactant liquor of sodium.
Replacing sodium measuring tank and sodium feeding line nitrogen, displacement to oxygen content is less than 0.5%.By the sodium of q.s(Fusing point
It is 97.82 DEG C, relative density (H2O)0.968)Protection down at kerosene enters in sodium measuring tank, the temperature of metering pot liquid
Control is more than 105 DEG C, it is therefore an objective to keep metallic sodium to be in molten condition.The nitrogen-sealed pressure of sodium measuring tank is set as
Melted metallic sodium, because melted sodium is than kerosene weight, can be extruded feeding by pressure mixed bottom sodium measuring tank by 0.4MPa
Clutch mixes laggard reactor reaction in a subtle way with 2-Pyrrolidone, and the inlet amount of metallic sodium is 1.0 grams/min, reacted liquid
Sending in reactant liquor storage tank after nitrogen displacement abjection hydrogen, the 2-Pyrrolidone obtaining about 4.6%2-pyrrolidones sodium salt is molten
Liquid, nitrogen-sealed preserves.