CN205586983U - Produce production line of many color ring oxygen tree fat - Google Patents
Produce production line of many color ring oxygen tree fat Download PDFInfo
- Publication number
- CN205586983U CN205586983U CN201620312431.6U CN201620312431U CN205586983U CN 205586983 U CN205586983 U CN 205586983U CN 201620312431 U CN201620312431 U CN 201620312431U CN 205586983 U CN205586983 U CN 205586983U
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- China
- Prior art keywords
- oil
- production
- reactor
- production line
- epoxy resins
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
The embodiment of the utility model discloses produce production line of many color ring oxygen tree fat, this produce production line of many color ring oxygen tree fat all is provided with oil inlet, auxiliary agent entry and a plurality of feed inlet including a plurality of reation kettle that set up side by side, every reation kettle's cauldron top, is provided with discharge gate and oil -out at the bottom of the cauldron, multistage charge -in pipeline, one end is connected with raw material tank, and the other end is divided into the multistage pipeline with the reation kettle one -to -one, all is provided with the valve between per two multistage pipelines, and the branch road on the multistage pipeline is connected with reation kettle's feed inlet, and every all is provided with flow control valve on the road, heat conduction oil circulation pipeline, its both ends are connected with every reation kettle's oil inlet and oil -out respectively. The utility model discloses a produce production line of many color ring oxygen tree fat technological structure is simple, adopts the feeding of the mode controlled reaction cauldron that multistage charge -in pipeline and flow control valve combined together, not only makes every reation kettle feeding even, has saved the manpower moreover, has improved efficiency, has reduced manufacturing cost.
Description
Technical field
This utility model produces the production line of resin in relating to a kind of factory, particularly relate to a kind of production pleochroic halo ring
The production line of epoxy resins.
Background technology
In the factory producing epoxy resin, it will usually produce the epoxy resin of different colours on a production line,
In order to meet the different needs of client.In the workshop producing pleochroic halo ring epoxy resins, it is typically all and selects one
Reactor is by adding different coloring agent every time, thus produces the epoxy resin of different colours, this side
Method not only wastes manpower, and production efficiency is the highest.Additionally, also there are the multiple reactors of employing to give birth to simultaneously
Produce the factory of epoxy resin of multiple color, but owing to being all individually to carry out the work that feeds in each reactor
Sequence, causes the product quality difference of different colours.
Utility model content
This utility model embodiment technical problem to be solved is, for producing pleochroic halo ring in general factory
Epoxy resins not only waste of manpower, production efficiency is the highest, and the product quality of different colours also can difference
Problem, it is proposed that a kind of production line producing pleochroic halo ring epoxy resins.
In order to solve above-mentioned technical problem, this utility model embodiment provides a kind of production pleochroic halo ring epoxy resins
Production line, the production line of this production pleochroic halo ring epoxy resins includes: reactor, has been arranged side by side multiple, often
The still top of individual reactor is provided with oil-in, adjuvant entrance and multiple charging aperture, and bottom is provided with out
Material mouth and oil-out；Multistage feed pipe, its one end is connected with material box, and the other end is divided into and reactor one
The multi-stage pipeline of one correspondence, is provided with valve between every two multi-stage pipelines, and what multi-stage pipeline was arranged props up
Road is connected with the charging aperture of reactor, and every branch road is provided with flow control valve；Conduction oil circulating line,
Its two ends are connected with oil-in and the oil-out of each reactor respectively, conduction oil circulating line from oil-out to
Heat exchanger, oil oven and pressure alarm it is disposed with between oil-in.
Wherein, multistage feed pipe and material box are all correspondingly arranged on multiple, many for carrying in reactor
Plant raw materials for production.
Wherein, multistage feed pipe is provided with fluid pump.
Wherein, oil pump it is provided with between oil oven and pressure alarm.
Wherein, it is provided with agitator in reactor.
Wherein, reactor being provided with vacuum port, vacuum port is connected with evacuator.
Wherein, the bottom of reactor is provided with electric heater.
Implement this utility model embodiment, have the advantages that production polychrome epoxy of the present utility model
The production-line technique simple in construction of resin, uses the mode control that multistage feed pipe combines with flow control valve
The charging of reactor processed, not only makes the charging of each reactor uniformly, improves product quality, and save
Manpower, improves efficiency.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below by right
In embodiment or description of the prior art, the required accompanying drawing used is briefly described, it should be apparent that below,
Accompanying drawing in description is only embodiments more of the present utility model, comes for those of ordinary skill in the art
Say, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of the production line producing pleochroic halo ring epoxy resins that this utility model provides.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technical side in this utility model embodiment
Case is clearly and completely described, it is clear that described embodiment is only that this utility model part is real
Execute example rather than whole embodiments.Based on the embodiment in this utility model, ordinary skill people
The every other embodiment that member is obtained under not making creative work premise, broadly falls into this utility model
The scope of protection.
This utility model provides a kind of production line producing pleochroic halo ring epoxy resins, and referring to Fig. 1, Fig. 1 is this
The structural representation of the production line producing pleochroic halo ring epoxy resins that utility model provides.This production pleochroic halo ring oxygen tree
The production line of fat include reactor 10, multistage feed pipe 20, material box 30, conduction oil circulating line 40,
Evacuator 50 and electric heater 60.
Reactor 10 has been arranged side by side multiple, and the still top of each reactor 10 is provided with oil-in 11, auxiliary
Auxiliary agent entrance 12 and multiple charging aperture 13, bottom is provided with discharging opening 14 and oil-out 15.Reactor 10
Inside it is provided with agitator 16.Vacuum port 17, vacuum port 17 and evacuator 50 it is provided with on reactor 10
Connect.The bottom of reactor 10 is heated by electric heater 60.
Multistage feed pipe 20 one end is connected with material box 30, and the other end is divided into and reactor 10 one_to_one corresponding
Multi-stage pipeline 21, be provided with valve 22 between every two multi-stage pipelines 21.Arrange on multi-stage pipeline 21
Branch road 23 be connected with the charging aperture 13 of reactor 10, every branch road 23 is provided with flow control valve
24.It is provided with fluid pump 25 on multistage feed pipe 20.Multistage feed pipe 20 and material box 21 are the most corresponding
It is provided with multiple, multiple raw materials for production can be carried in reactor 10 simultaneously.
Conduction oil circulating line 40 two ends are respectively with the oil-in 11 of each reactor 10 and oil-out 15 even
Connect.Conduction oil circulating line 40 is disposed with heat exchanger 41, oil from oil-out 15 to oil-in 11
Stove 42, oil pump 44 and pressure alarm 43.
When the production line of this production pleochroic halo ring epoxy resins produces, the raw material of all fluids and adjuvant
Directly it is conveyed in reactor 10 by multistage feed pipe 20, and the inlet amount of each reactor 10 is led to
The combination crossing multi-stage pipeline 21 and flow control valve 24 controls to keep impartial.The adjuvant of powder can lead to
Cross adjuvant entrance 12 directly to pour in reactor 10.
Implement this utility model embodiment, have the advantages that production polychrome epoxy of the present utility model
The production-line technique simple in construction of resin, uses the mode control that multistage feed pipe combines with flow control valve
The charging of reactor processed, not only makes the charging of each reactor uniformly, improves product quality, and save
Manpower, improves efficiency.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model,
All within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, all
Within protection domain of the present utility model should be included in.
Claims (7)
1. the production line producing pleochroic halo ring epoxy resins, it is characterised in that described production pleochroic halo ring epoxy resins
Production line include:
Reactor, has been arranged side by side multiple, and the still top of each described reactor is provided with oil-in, auxiliary
Agent entrance and multiple charging aperture, bottom is provided with discharging opening and oil-out；
Multistage feed pipe, its one end is connected with material box, and the other end is divided into and described reactor one_to_one corresponding
Multi-stage pipeline, be provided with valve between every two described multi-stage pipelines, on described multi-stage pipeline arrange
Branch road is connected with the described charging aperture of described reactor, and every described branch road is provided with flow control valve；
Conduction oil circulating line, its two ends respectively with the described oil-in of each described reactor and described fuel-displaced
Mouth connects, and described conduction oil circulating line is disposed with heat exchange from described oil-out to described oil-in
Device, oil oven and pressure alarm.
The production line of production pleochroic halo ring epoxy resins the most according to claim 1, it is characterised in that described
Multistage feed pipe and described material box are all correspondingly arranged on multiple, multiple for carrying in described reactor
Raw materials for production.
The production line of production pleochroic halo ring epoxy resins the most according to claim 1, it is characterised in that described
Fluid pump it is provided with on multistage feed pipe.
The production line of production pleochroic halo ring epoxy resins the most according to claim 1, it is characterised in that described
It is provided with oil pump between oil oven and described pressure alarm.
The production line of production pleochroic halo ring epoxy resins the most according to claim 1, it is characterised in that described
Agitator it is provided with in reactor.
The production line of production pleochroic halo ring epoxy resins the most according to claim 5, it is characterised in that described
Being provided with vacuum port on reactor, described vacuum port is connected with evacuator.
The production line of production pleochroic halo ring epoxy resins the most according to claim 6, it is characterised in that described
The bottom of reactor is provided with electric heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620312431.6U CN205586983U (en) | 2016-04-14 | 2016-04-14 | Produce production line of many color ring oxygen tree fat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620312431.6U CN205586983U (en) | 2016-04-14 | 2016-04-14 | Produce production line of many color ring oxygen tree fat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205586983U true CN205586983U (en) | 2016-09-21 |
Family
ID=56923071
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620312431.6U Expired - Fee Related CN205586983U (en) | 2016-04-14 | 2016-04-14 | Produce production line of many color ring oxygen tree fat |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205586983U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107754999A (en) * | 2017-11-10 | 2018-03-06 | 江苏南方光纤科技有限公司 | Bare fibre reducing mechanism and bare fibre automatic recovery system |
| CN113457571A (en) * | 2020-03-30 | 2021-10-01 | 中石油吉林化工工程有限公司 | Polymerization inhibitor mechanism for MMA (methyl methacrylate) production device and polymerization inhibitor adding method |
-
2016
- 2016-04-14 CN CN201620312431.6U patent/CN205586983U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107754999A (en) * | 2017-11-10 | 2018-03-06 | 江苏南方光纤科技有限公司 | Bare fibre reducing mechanism and bare fibre automatic recovery system |
| CN113457571A (en) * | 2020-03-30 | 2021-10-01 | 中石油吉林化工工程有限公司 | Polymerization inhibitor mechanism for MMA (methyl methacrylate) production device and polymerization inhibitor adding method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160921 Termination date: 20210414 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |