CN208389999U - Cooling device in a kind of 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction - Google Patents
Cooling device in a kind of 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction Download PDFInfo
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- CN208389999U CN208389999U CN201820570652.2U CN201820570652U CN208389999U CN 208389999 U CN208389999 U CN 208389999U CN 201820570652 U CN201820570652 U CN 201820570652U CN 208389999 U CN208389999 U CN 208389999U
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- reaction kettle
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- cooling liquid
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Abstract
Cooling device in one kind 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction, including reaction kettle, interlayer is equipped with outside reaction kettle, interlayer top is equipped with cooling liquid inlet, and lower part is equipped with cooling liquid outlet, and reaction kettle top is equipped with kettle cover, kettle cover is equipped with feed inlet, reaction kettle lower part is equipped with discharge port, is equipped with agitating shaft and coil pipe inside the reaction kettle, the coil pipe is in the shape of a spiral, the cooling liquid inlet of coil pipe is located at reaction kettle upper outside, and cooling liquid outlet is located at reaction kettle lower outside;Through the above technical solution, the utility model is attainable to have the beneficial effect that the utility model structure designs advantages of simple, it is easily operated, in addition to sandwich establishment carries out outside cooling other than reaction kettle, coil pipe also by being arranged in reaction kettle, coolant liquid directly cools down the material in reaction kettle, and spiral helicine coil pipe film-cooled heat increases, and can be quickly cooled down material;The external coolant circulation system of coil pipe simultaneously, improves production efficiency, ensure that product quality.
Description
Technical field
The utility model belongs to chemical industry equipment, and in particular in one kind 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction
Cooling device.
Background technique
In the production process of tropinone, the butanedial that 2,5- dimethoxy-tetrahydrofurans hydrolyze is synthesis tropinone
One of raw material, the capital equipment of 2,5- dimethoxy-tetrahydrofuran hydrolysis is reaction kettle, it is known that 2,5- dimethoxys four
The hydrolysis of hydrogen furans is exothermic reaction, if do not cooled down to material, will because temperature is excessively high influence product quality and
Yield, existing reaction kettle be mostly cooled down by being passed through brine ice in the collet that is arranged outside reaction kettle, but this
Kind reaction kettle cooling effect is general, is unable to satisfy the requirement that reaction system reduces temperature in reaction kettle.
Utility model content
For overcome the deficiencies in the prior art, the purpose of the utility model is to provide one kind 2,5- dimethoxy-tetrahydrofurans
Cooling device in hydrolysis reaction, to achieve the purpose that cool down to material in reactor rapidly.
To achieve the goals above, the technical solution adopted in the utility model is as follows:
Cooling device in one kind 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction, including reaction kettle, outside reaction kettle
Equipped with interlayer, interlayer top is equipped with cooling liquid inlet, and lower part is equipped with cooling liquid outlet, and reaction kettle top is equipped with kettle cover, on kettle cover
Equipped with feed inlet, reaction kettle lower part is equipped with discharge port, and agitating shaft is equipped with inside the reaction kettle, is equipped with inside the reaction kettle
Coil pipe, in the shape of a spiral, the cooling liquid inlet of coil pipe is located at reaction kettle upper outside to the coil pipe, and cooling liquid outlet is located at reaction
Kettle lower outside;Cooling liquid inlet is connect by pipeline with fluid reservoir, and pipeline is equipped with pump;Cooling liquid outlet by pipeline with it is cold
But device connects, and cooler is connect by pipeline with fluid reservoir;The first valve, cooling liquid outlet are equipped between cooling liquid inlet and pump
The second valve is equipped between cooler.
Bottom is additionally provided with fixed frame in the reaction kettle, and the coil pipe is fixed on fixed frame.
The kettle cover is equipped with temperature sensor.
The centerline direction of the coil pipe is consistent with stirring axis direction.
First valve and the second valve is solenoid valve.
The coil pipe is Stainless Steel Coil.
Coolant liquid in the coil pipe is brine ice.
Through the above technical solutions, the utility model is attainable to have the beneficial effect that the design of the utility model structure is simple
Rationally, easily operated, in addition to other than reaction kettle sandwich establishment carry out it is cooling outer, it is cold also by the coil pipe being arranged in reaction kettle
But liquid directly cools down the material in reaction kettle, and spiral helicine coil pipe film-cooled heat increases, and can be quickly cooled down material;Together
When the external coolant circulation system of coil pipe, improve production efficiency, ensure that product quality.
Detailed description of the invention
Fig. 1 is the schematic diagram of the utility model.
Specific embodiment
As shown in Fig. 1, cooling device in one kind 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction, including reaction kettle
1, interlayer 2 is equipped with outside reaction kettle 1,2 top of interlayer is equipped with cooling liquid inlet, and lower part is equipped with cooling liquid outlet, leads in interlayer cold
But liquid carries out cooling down to reaction kettle 1.1 top of reaction kettle is equipped with kettle cover, and kettle cover is equipped with feed inlet 3, will lead from feed inlet 3
Reaction mass 2 is wanted, 5- dimethoxy-tetrahydrofuran is passed through in kettle, and 1 lower part of reaction kettle is equipped with discharge port 4, in the reaction kettle 1
Portion is equipped with agitating shaft 5, guarantees that reaction mass is sufficiently mixed;2,5- dimethoxy-tetrahydrofuran hydrolysis are exothermic reaction, single
Temperature environment needed for not being able to satisfy reaction system is cooled down by interlayer 2, therefore coil pipe 6, coil pipe are set inside the reaction kettle 1
6 in the shape of a spiral, and helical form can effectively increase and reaction solution contact area.The cooling liquid inlet 61 of coil pipe 6 is located at 1 top of reaction kettle
Outside, cooling liquid outlet 62 are located at 1 lower outside of reaction kettle;Cooling liquid inlet 61 is connect by pipeline with fluid reservoir 7, on pipeline
Equipped with pump 8;Cooling liquid outlet 62 is connect by pipeline with cooler 9, and coolant liquid takes away the heat of reaction solution in kettle by coil pipe 6
Amount, the temperature of coolant liquid can increase, need to be cooled down the coolant liquid flowed out from coil outlets 62 with cooler 9, cold
But device 9 is connect by pipeline with fluid reservoir 7, coolant liquid after cooling will be delivered in fluid reservoir 7 again, by pumping 8 for liquid storage
Coolant liquid in tank 7 is pumped to 6 import of coil pipe;Cooling liquid inlet 61 and pump 8 between be equipped with the first valve 10, cooling liquid outlet 62 with
The second valve 11 is equipped between cooler 9, valve can control the size of coolant liquid burst size according to real reaction situation.
In order to avoid in cooling procedure, coil pipe 6 shakes, bottom is equipped with fixed frame 12 in reaction kettle, and coil pipe 6 is fixed
On fixed frame, coil pipe 6 is supported.
Kettle cover is equipped with temperature sensor 13, convenient for being measured in real time to temperature in the kettle, to control the disengaging of coolant liquid
The size of amount.
The centerline direction of coil pipe 6 is consistent with 5 direction of agitating shaft, prevents coil pipe 6 in whipping process from connecing with agitating shaft 5
Touching.
First valve 10 and the second valve 11 are solenoid valve, and solenoid valve more intelligently realizes the control to cooling liquid measure.
Coil pipe 6 is Stainless Steel Coil, and Stainless Steel Coil is at low cost, long service life.
Coolant liquid in coil pipe is brine ice, and brine ice is relative to good water cooling effect, while cost is also low.
The working process of the utility model is as follows: when starting reaction, reaction mixture is delivered to from the feed inlet on kettle cover
In reaction kettle, while leading to brine ice in interlayer and carrying out interlayer cooling, pump pumps the salt water in fluid reservoir into coil pipe, to anti-
Answer material in kettle to be cooled down, from coil outlets flow out salt water through cooler carry out secondary cooling then pass through pipeline to
In fluid reservoir, circulation is carried out according to this;The reaction temperature in temperature sensor detection kettle on reaction kettle, can pass through electromagnetism accordingly
Valve controls the conveying capacity of coolant liquid.
Above-described is only preferred embodiments of the present invention, it is noted that for those skilled in the art
For, under the premise of not departing from the utility model general idea, several changes and improvements can also be made, these also should be considered as
The protection scope of the utility model.
Claims (7)
1. one kind 2, cooling device in 5- dimethoxy-tetrahydrofuran hydrolysis reaction, including reaction kettle (1), reaction kettle (1)
Outside is equipped with interlayer (2), and interlayer (2) top is equipped with cooling liquid inlet, and lower part is equipped with cooling liquid outlet, and reaction kettle (1) top is set
There is kettle cover, kettle cover is equipped with feed inlet (3), and reaction kettle (1) lower part is equipped with discharge port (4), is equipped with inside the reaction kettle (1)
Agitating shaft (5), which is characterized in that be equipped with coil pipe (6) inside the reaction kettle (1), the coil pipe (6) in the shape of a spiral, coil pipe
(6) cooling liquid inlet (61) is located at reaction kettle (1) upper outside, and cooling liquid outlet (62) is located at reaction kettle (1) lower outside;
Cooling liquid inlet (61) is connect by pipeline with fluid reservoir (7), and pipeline is equipped with pump (8);Cooling liquid outlet (62) passes through pipeline
It is connect with cooler (9), cooler (9) is connect by pipeline with fluid reservoir (7);It is set between cooling liquid inlet (61) and pump (8)
There is the first valve, is equipped with the second valve (11) between cooling liquid outlet (62) and cooler (9).
2. cooling device in 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction according to claim 1, feature exist
In the interior bottom of the reaction kettle (1) is additionally provided with fixed frame (12), and the coil pipe (6) is fixed on fixed frame (12).
3. cooling device in 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction according to claim 1, feature exist
In the kettle cover is equipped with temperature sensor (13).
4. cooling device in 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction according to claim 1, feature exist
In the centerline direction of the coil pipe (6) is consistent with agitating shaft (5) direction.
5. cooling device in 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction according to claim 1, feature exist
In first valve (10) and the second valve (11) are solenoid valve.
6. cooling device in 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction according to claim 1, feature exist
In the coil pipe (6) is Stainless Steel Coil.
7. cooling device in 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction according to claim 1, feature exist
In the coolant liquid in the coil pipe (6) is brine ice.
Priority Applications (1)
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CN201820570652.2U CN208389999U (en) | 2018-04-20 | 2018-04-20 | Cooling device in a kind of 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction |
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CN201820570652.2U CN208389999U (en) | 2018-04-20 | 2018-04-20 | Cooling device in a kind of 2,5- dimethoxy-tetrahydrofuran hydrolysis reaction |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111013493A (en) * | 2019-12-28 | 2020-04-17 | 萧县新秀新材料有限公司 | Pipeline reaction system and method for preparing light stabilizer |
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2018
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111013493A (en) * | 2019-12-28 | 2020-04-17 | 萧县新秀新材料有限公司 | Pipeline reaction system and method for preparing light stabilizer |
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