CN205627901U - Whole oil bath formula pipeline reactor - Google Patents
Whole oil bath formula pipeline reactor Download PDFInfo
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- CN205627901U CN205627901U CN201620347106.3U CN201620347106U CN205627901U CN 205627901 U CN205627901 U CN 205627901U CN 201620347106 U CN201620347106 U CN 201620347106U CN 205627901 U CN205627901 U CN 205627901U
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- oil
- crossing current
- current pump
- reaction tube
- storage tank
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Abstract
The utility model discloses a whole oil bath formula pipeline reactor, whole oil bath formula pipeline reactor includes the inflation groove, leads oil pipe, oil groove heat preservation, oil storage tank, heating pipe, reaction tube, reaction tube support, oil groove crossing current pump, oil groove crossing current pump driving motor, oil groove crossing current pump magnetic transmission ware and conduction oil, the inflation groove communicates through leading oil pipe with the oil storage tank, oil storage tank outside parcel has the oil groove heat preservation, be full of the conduction oil in the oil storage tank, the utility model discloses whole oil bath formula pipeline reactor adopts integrated design, heats to conduct heat with the hot an organic whole that all integrates, avoids increasing unnecessary pipeline and flange connections, the while bulk reduction, square design is favorable to making the heat preservation, and the heat loss is few, and whole energy consumption is low.
Description
Technical field
This utility model relates to pipeline reactor field, is specifically related to a kind of overall oil-bath type pipeline
Reactor.
Background technology
Pipeline reactor is mainly used in gas phase, liquid phase, liquid phase tandem reaction sequence, by list
Continuous or many pipe arranged in parallel of root (straight tube or coil pipe) composition, be typically provided sleeve pipe or
Shell-tube type heat exchanger.During operation, material is continuously added to from one end, successive reaction in pipe,
Flow continually out from the other end, just reached the conversion ratio required.This kind of reactor have volume little,
The advantages such as specific surface is big, back-mixing is few, reactant mixture seriality changes, easily controllable.Along with
Chemical Manufacture increasingly tends to the pipe reaction of maximization, serialization, automatization, continuous operation
It is more and more that device is used in process of production, and some uses Autoclave the most always
Macromolecular polymerization reaction, currently also start to use instead the pipeline reactor of continuous operation.Pipeline is anti-
Answering another important indicator of device is exactly temperature control, accurately controls reaction temperature and is conducive to improving
Conversion ratio and selectivity.China Patent Publication No. CN102553512A and China Patent Publication No.
CN103349950A is the example of pipeline reactor, and its common drawback is, reacting pipe
Heat carrier need other equipment to provide, heat carrier is usually conduction oil, and equipment is usually led
Hot oil furnace, described heat-conducting oil furnace, by heat-conducting oil heating, is pipelined to reaction tube casing layer
Or container interlayer, it is back to circulation in heat-conducting oil furnace afterwards.Above-mentioned working method produces following asking
Topic: (1) heat transfer thermal release, it will produce a lot of pipeline, flange connector etc., this
A little connectors are the most all easy to break down, and its overall volume is the biggest, insulation
Technical difficulty big, its energy consumption is the biggest；(2) heat-conducting oil furnace typically must be equipped with conduction oil and follows
Ring pump, under the state that this heat conduction oil circulating pump is operated in High Temperature High Pressure, it seals, cooling is all difficult
To reach preferable effect, and its buy, maintenance cost the highest；(3) reaction tube sleeve pipe
Conduction oil flowing in layer or container interlayer is flowed and circulates by the pressure effect of pump, due to institute
State casing layer or container interlayer not in accordance with fluid-dynamic design, occur unavoidably flow dead with
And the problem of circulation, mixed flow, so will produce the problem that reaction tube temperature is uneven.
Utility model content
The purpose of this utility model is that the shortcoming overcoming prior art is with not enough, it is provided that a kind of whole
The design of body formula, heating heat transfer the most integrated hot overall oil-bath type pipeline reactor.
The purpose of this utility model is achieved through the following technical solutions:
A kind of overall oil-bath type pipeline reactor, described overall oil-bath type pipeline reactor includes swollen
Swollen groove, oil guide pipe, oil groove heat-insulation layer, oil storage tank, add heat pipe, reaction tube, reaction tube support,
Oil groove crossing current pump, oil groove crossing current pump drive motor, oil groove crossing current pump magnetic driver and conduction oil；
Described expansion slot is connected by oil guide pipe with oil storage tank, and the bottom of described expansion slot is higher than described storage
The top of oil groove；Oil groove heat-insulation layer it is enclosed with outside described oil storage tank；It is full of in described oil storage tank
Conduction oil；It is provided with in described oil storage tank and adds heat pipe, reaction tube, reaction tube support, oil groove crossing current
Pump, oil groove crossing current pump drives motor and oil groove crossing current pump magnetic driver；The described heat pipe that adds is positioned at
Below reaction tube support, described reaction tube is located on reaction tube support；Described oil groove crossing current pump drives
Galvanic electricity machine drives oil groove crossing current pump magnetic driver to rotate, described oil groove crossing current pump magnetic driver
Rotated by magnetically-actuated oil groove crossing current pump.
Preferably, described reaction tube is spirally wrapped around on reaction tube support；Described reaction tube
It is wound around the volume that can increase reaction tube in the shape of a spiral, improves work efficiency.
Preferably, described reaction tube is drawn by flange and is connected with extraneous pipeline.
Preferably, described oil groove crossing current pump drives the rotating speed of motor to be 10-100 rev/min.
Preferably, the temperature of described conduction oil is 100-350 DEG C.
Preferably, described reaction tube is two；Two reaction tubes are set and can improve work efficiency.
Preferably, described oil storage tank is square box；It is favourable that described oil storage tank is set to square structure
In making oil groove heat-insulation layer, thus it is few to reach heat loss, the effect that overall energy consumption is low.
Operation principle of the present utility model:
During room temperature, the conduction oil volume in expansion slot is minimum, and conduction oil liquid level is positioned at the bottom of expansion slot
Portion；Add heat pipe to begin to warm up, the volumetric expansion owing to temperature rises of the conduction oil in oil storage tank,
Described conduction oil flows into expansion slot along oil guide pipe, and described expansion slot has enough volumes to accommodate stream
The conduction oil entered；Oil groove crossing current pump drives motor to start to rotate, and drives oil groove crossing current pump magnetic force to pass
Dynamic device rotates, and oil groove crossing current pump magnetic driver is rotated by magnetically-actuated oil groove crossing current pump, oil
The conduction oil rotated in drive oil storage tank of groove crossing current pump circulates；Conduction oil in oil storage tank
Transfer thermal energy to reaction tube, after reaction tube reaches steady temperature, carry out pipe reaction operation.
This utility model compared with prior art has a following beneficial effect:
(1) this utility model entirety oil-bath type pipeline reactor uses integral design, heating to pass
Heat heat is the most integrated, it is to avoid increasing unnecessary pipeline and flange connector, volume subtracts simultaneously
Little, described squared design is conducive to making heat-insulation layer, and heat loss is few, and overall energy consumption is low.
(2) this utility model entirety oil-bath type pipeline reactor oil groove crossing current pump replacement high pressure is led
Circular-pump, uses magnetic driver transmission, improves global reliability, and cost is greatly reduced.
(3) type of flow of the conduction oil of this utility model entirety oil-bath type pipeline reactor is complete
Consider design by hydrodynamics, there is no flow dead and circulation, the problem of mixed flow, it is possible to
Ensure that the homogeneous temperature of reaction tube is consistent.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is generalized section of the present utility model；
Fig. 3 is that conduction oil of the present utility model circulates schematic diagram.
In figure, reference is: 1, expansion slot；2, oil guide pipe；3, oil groove heat-insulation layer；4、
Oil storage tank；5, heat pipe is added；6, reaction tube support；7, reaction tube；8, oil groove crossing current pump；9、
Oil groove crossing current pump drives motor；10, oil groove crossing current pump magnetic driver.
Detailed description of the invention
Below in conjunction with embodiment and accompanying drawing, this utility model is described in further detail, but this
The embodiment of utility model is not limited to this.
As shown in Figure 1 and Figure 2, this utility model is a kind of integral design, heating heat transfer use
The overall oil-bath type pipeline reactor that heat is the most integrated, it is to avoid increase unnecessary pipeline and flange
Connector, volume reduces simultaneously, described overall oil-bath type pipeline reactor include expansion slot 1,
Oil guide pipe 2, oil groove heat-insulation layer 3, oil storage tank 4, add heat pipe 5, reaction tube support 6, reaction
Pipe 7, oil groove crossing current pump 8, oil groove crossing current pump drive motor 9, oil groove crossing current pump magnetic driver
10 and conduction oil, described expansion slot 1 is connected by oil guide pipe 2 with oil storage tank 4, described expansion
The bottom of groove 1 is higher than the top of described oil storage tank 4, and described oil storage tank 4 is square box, the party
Shape is designed with beneficially making oil groove heat-insulation layer, thus it is few to reach heat loss, the effect that overall energy consumption is low
Really；It is enclosed with oil groove heat-insulation layer 3 outside described oil storage tank 4；It is full of in described oil storage tank 4 and leads
Deep fat；It is provided with in described oil storage tank 4 and adds heat pipe 5, reaction tube 7, reaction tube support 6, oil groove
Crossing current pump 8, oil groove crossing current pump drive motor 9 and oil groove crossing current pump magnetic driver 10；Described
Adding heat pipe 5 and be positioned at below reaction tube support 6, described reaction tube 7 is located on reaction tube support 6,
Described reaction tube 7 is spirally wrapped around on reaction tube support 6, simultaneously in order to improve work effect
Rate, described reaction tube 7 is set to two, and described reaction tube 7 is drawn and extraneous pipeline by flange
Connect；Described oil groove crossing current pump drives motor 9 to drive oil groove crossing current pump magnetic driver 10 to rotate,
Described oil groove crossing current pump drives the rotating speed of motor 9 to be 10-100 rev/min, described oil groove crossing current pump magnetic
Power driver 10 is rotated by magnetically-actuated oil groove crossing current pump 8.
As it is shown on figure 3, during room temperature, the conduction oil volume in expansion slot 1 is minimum, heat conduction fluid
Face is positioned at bottom expansion slot 1；Add heat pipe 5 to begin to warm up, the conduction oil in oil storage tank 4 due to
Temperature rises and volumetric expansion, and described conduction oil flows into expansion slot 1 along oil guide pipe 2, described
Expansion slot 1 has enough volumes to accommodate the conduction oil flowed into；Oil groove crossing current pump drives motor 9 to open
Begin to rotate, drive oil groove crossing current pump magnetic driver 10 to rotate, oil groove crossing current pump magnetic driver
10 are rotated by magnetically-actuated oil groove crossing current pump 8, and the rotation of oil groove crossing current pump 8 drives oil storage tank
Conduction oil in 4 circulates；Conduction oil in oil storage tank 4 transfers thermal energy to reaction tube 7,
The temperature of described conduction oil is 100-350 DEG C, after reaction tube 7 reaches steady temperature, manages
Formula operation.
The temperature that this utility model entirety oil-bath type pipeline reactor can accurately control pipe reaction is same
Shi Wendu is all also very good with property, and the reaction tube 7 any two points temperature difference is less than 0.5 DEG C, and overall
Formula structure assembly degree is high, low cost, and energy consumption is low, and reliability is high, and this reactor is applicable to multiple
Needing precise temperature control, reaction temperature is at the oil-bath type pipe reaction of 100-350 DEG C.This practicality is new
Type entirety oil-bath type pipeline reactor oil groove crossing current pump 8 substitutes high pressure heat conduction oil circulating pump, uses
Magnetic driver 10 transmission, improves global reliability, and cost is greatly reduced.This utility model
The type of flow of the conduction oil of overall oil-bath type pipeline reactor is considered to set by hydrodynamics completely
Meter, does not has flow dead and circulation, the problem of mixed flow, it is possible to ensure the temperature of reaction tube 7
Uniformity.This utility model entirety oil-bath type pipeline reactor can as a reaction module,
Also can carry out stacking, series, parallel mode forms bigger complicated system.
Above-mentioned for this utility model preferably embodiment, but embodiment of the present utility model is also
Do not limited by foregoing, other any without departing from spirit of the present utility model with former
Change that reason is lower to be made, modify, substitute, combine, simplify, all should be the substitute mode of equivalence,
Within being included in protection domain of the present utility model.
Claims (7)
1. an overall oil-bath type pipeline reactor, it is characterised in that described overall oil-bath type pipe
Road reactor includes expansion slot, oil guide pipe, oil groove heat-insulation layer, oil storage tank, adds heat pipe, reaction
Pipe, reaction tube support, oil groove crossing current pump, oil groove crossing current pump drive motor, oil groove crossing current pump magnetic
Power driver and conduction oil；Described expansion slot is connected by oil guide pipe with oil storage tank, described expansion
The bottom of groove is higher than the top of described oil storage tank；Oil groove heat-insulation layer it is enclosed with outside described oil storage tank；
Falling heat-transfer oil in described oil storage tank；It is provided with in described oil storage tank and adds heat pipe, reaction tube, reaction
Pipe holder, oil groove crossing current pump, oil groove crossing current pump drive motor and oil groove crossing current pump magnetic driver；
The described heat pipe that adds is positioned at below reaction tube support, and described reaction tube is located on reaction tube support；Institute
Stating oil groove crossing current pump drives motor to drive oil groove crossing current pump magnetic driver to rotate, and described oil groove is horizontal
Stream pump magnetic driver is rotated by magnetically-actuated oil groove crossing current pump.
Overall oil-bath type pipeline reactor the most according to claim 1, it is characterised in that
Described reaction tube is spirally wrapped around on reaction tube support.
Overall oil-bath type pipeline reactor the most according to claim 1, it is characterised in that
Described reaction tube is drawn by flange and is connected with extraneous pipeline.
Overall oil-bath type pipeline reactor the most according to claim 1, it is characterised in that
Described oil groove crossing current pump drives the rotating speed of motor to be 10-100 rev/min.
Overall oil-bath type pipeline reactor the most according to claim 1, it is characterised in that
The temperature of described conduction oil is 100-350 DEG C.
Overall oil-bath type pipeline reactor the most according to claim 1, it is characterised in that
Described reaction tube is two.
Overall oil-bath type pipeline reactor the most according to claim 1, it is characterised in that
Described oil storage tank is square box.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620347106.3U CN205627901U (en) | 2016-04-21 | 2016-04-21 | Whole oil bath formula pipeline reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620347106.3U CN205627901U (en) | 2016-04-21 | 2016-04-21 | Whole oil bath formula pipeline reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205627901U true CN205627901U (en) | 2016-10-12 |
Family
ID=57061942
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620347106.3U Withdrawn - After Issue CN205627901U (en) | 2016-04-21 | 2016-04-21 | Whole oil bath formula pipeline reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205627901U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817186A (en) * | 2016-04-21 | 2016-08-03 | 广东椰氏实业股份有限公司 | Integral oil bath type pipeline reactor and realization method thereof |
-
2016
- 2016-04-21 CN CN201620347106.3U patent/CN205627901U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817186A (en) * | 2016-04-21 | 2016-08-03 | 广东椰氏实业股份有限公司 | Integral oil bath type pipeline reactor and realization method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20161012 Effective date of abandoning: 20181019 |