CN206008109U - A kind of resin production plant - Google Patents
A kind of resin production plant Download PDFInfo
- Publication number
- CN206008109U CN206008109U CN201620921829.XU CN201620921829U CN206008109U CN 206008109 U CN206008109 U CN 206008109U CN 201620921829 U CN201620921829 U CN 201620921829U CN 206008109 U CN206008109 U CN 206008109U
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- horizontal
- condenser
- horizontal separator
- thinning vessel
- separator
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The utility model proposes a kind of resin production plant, including reactor, horizontal separator, thinning vessel, the reactor top gas outlet is connected with vertical condenser, and vertical condenser is connected by horizontal condenser with horizontal separator；Coalescence filter core is provided with the horizontal separator, the backflow of horizontal separator is back in reactor by desiccant box, the wastewater outlet of horizontal separator is connected with thinning vessel chuck water inlet, thinning vessel chuck outlet connects the water inlet of horizontal condenser by cooling tower, and the outlet of horizontal condenser is connected with thinning vessel chuck water inlet by pipeline；Rectifying column is provided between the horizontal separator and thinning vessel.Resin production plant can be in effectively utilizes production process waste water, realize recycling for waste water, reduce the consumption of water resource, reduce production cost, effectively improve feed purity.
Description
Technical field
This utility model belongs to resin technology production field, and in particular to a kind of resin production plant.
Background technology
Paint is made up of resin, solvent, color stuffing, auxiliary agent etc., and wherein played a crucial role is resin used,
It is the basic of paint chemistry classification.The production of resin is：First putting into reactant in reactor carries out polycondensation reaction, big through one
After the completion of section time response, then corresponding diluent and thixotropic agent, mix homogeneously will be added to obtain most in product input thinning vessel
Whole finished product.
Existing process units structure is relatively simple, reclaims not enough fully, can produce waste liquid, inadequate energy-conserving and environment-protective.In tree
The course of reaction of fat can produce a number of solid impurity, as reflux gas are entered in final storage tank, so be unfavorable for clear
Reason is also unfavorable for the raising of product quality.Current letdown tank chuck is connected with chilled water tank respectively with condenser chuck, latting drown
Tank cooling demand cooling water is less, and condenser chuck demand cooling water is more, is so unfavorable for saving cooling water resources.And point
The waste water that separates from device not only increases processing cost, is unfavorable for saving water resource frequently as wastewater treatment.
Adopting at present conventional separator production of resins process more, simple structure, but in high volume production process, equipment body
Product is big, and dispersed phase drop settling height is long, and separation efficiency and disposal ability are low, and more or less exist in Paint Production
Surfactant, is unfavorable for separating, strong inhibition disperse phase liquid drops in the coarse separation on interface.
Utility model content
This utility model provides a kind of resin production plant, solves above-mentioned resin and contains impurity effect paint quality
Problem, rationally using separator waste water, reduces water resources consumption, improves separation efficiency.
Realize that the technical solution of the utility model is：A kind of resin production plant, including reactor, horizontal separator, converts
Dilute kettle, the reactor top gas outlet are connected with vertical condenser, and vertical condenser is with horizontal separator by horizontal cold
Condenser is connected；Coalescence filter core is provided with the horizontal separator, and the backflow of horizontal separator is back to instead by desiccant box
Answer in kettle, the wastewater outlet of horizontal separator is connected with thinning vessel chuck water inlet, thinning vessel chuck outlet passes through cooling tower
The water inlet of connection horizontal condenser, the outlet of horizontal condenser are connected with thinning vessel chuck water inlet by pipeline；Described
Rectifying column is provided between horizontal separator and thinning vessel.
The rectifying column is hypergravity rectifier.
The beneficial effects of the utility model are：
（1）Using horizontal separator, the big liquid for needing sharp separation of volume of production is disclosure satisfy that, because horizontal liquid-liquid point
Big from interfacial area, separating rate is fast, and compared with the separator with size, treating capacity may be up to 2-5 times, improves production effect
Rate；And Coalescence filter core is provided with horizontal separator, water breakdown of emulsion, coalescence after Coalescence filter core of part emulsifying makes emulsifying shape
The water of state is separated, and further improves the purity of waste water；
（2）The wastewater outlet of horizontal separator is connected with thinning vessel chuck water inlet, chuck thinning vessel chuck outlet
The water of outflow enters horizontal condenser through cooling tower, and the water that horizontal condenser flows out reenters thinning vessel, forms a water
Stream circulation, substantially increases the utilization ratio of waste water, reduces the utilization of water resource, reduce production cost, energy-conserving and environment-protective；
（3）Increase hypergravity rectifier between thinning vessel and horizontal separator, horizontal separator point can be effectively improved
The water quality of the waste water for separating out, prevents the excessively multipair thinning vessel of organic substance in waste water and condenser from causing certain corrosion, and overweight
Power rectifier small volume, can effectively save place and space, reduce disposal of pollutants, pattern of improving management and administration, reduce production
Labor intensity, improves production security；
（4）The reflux pipeline of horizontal separator is provided with desiccant box, is provided with desiccant in desiccant box, and that isolated returns
After the drying agent such as flow liquid such as benzene are dried, the moisture in backflow can be effectively removed, improve the purity level of backflow, and then
Improve product quality.
Description of the drawings
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or accompanying drawing to be used is briefly described needed for description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise for not paying creative work
Under, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is structural representation of the present utility model.
Specific embodiment
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model, rather than whole
Embodiment.Embodiment in based on this utility model, those of ordinary skill in the art are not under the premise of creative work is paid
The every other embodiment for being obtained, belongs to the scope of this utility model protection.
As shown in figure 1, a kind of resin production plant, including reactor 1, horizontal separator 5, thinning vessel 8, the reactor
The outlet of 1 top gas is connected with vertical condenser 3, and vertical condenser 3 is connected by horizontal condenser 4 with horizontal separator 5；Institute
State in horizontal separator 5 and be provided with Coalescence filter core 5-1, the backflow of horizontal separator 5 is back to reactor 1 by desiccant box 6
Interior, the wastewater outlet of horizontal separator 5 is connected with 8 chuck water inlet of thinning vessel, and 8 chuck outlet of thinning vessel passes through cooling tower 2
The water inlet of connection horizontal condenser 4, the outlet of horizontal condenser 4 are connected with 8 chuck water inlet of thinning vessel by pipeline；Institute
State and between horizontal separator 5 and thinning vessel 8, be provided with rectifying column 7.
During production, material is entered in reactor 1, and heat kerosene enters the heat of the chuck of reactor 1 to be had in passage, to reach thing
Temperature needed for material reaction, during reaction, the gas outlet on reacted 1 top of kettle of gas phase gas enters be attached thereto vertical cool solidifying
Device 3, enters horizontal condenser 4 afterwards, and vertical condenser 3 is used in combination with horizontal condenser 4, more fully can be taken away in pipe
Heat, rapid condensation raw material liq and water prevent opposing steam flow to reactor 1.Raw material liq after condensation and water are entered
Horizontal separator 5, carries out the separation of organic faciess and water, in horizontal separator 5 due to the more general gravity of horizontal separator 5 point
Big from device separating interface area, the purpose of sharp separation can be reached, while the water of part emulsifying is in horizontal separator 5
Coalescence filter core 5-1, through breakdown of emulsion, coalescence, separates the water of emulsified state.The backflow that isolates contains some water
Point, desiccant box 6 is therefore provided with the pipeline outside horizontal separator 5, is provided with desiccant in desiccant box 6, backflow is passed through
After desiccant dryness, the moisture in backflow can be effectively removed, improve the purity of backflow.The waste water that horizontal separator 5 is discharged
Through 7 rectification of rectifying column, the waste water quality that horizontal separator 5 is isolated can be effectively improved, prevent organic substance mistake in waste water
Multipair thinning vessel and condenser cause certain corrosivity material arrival thinning vessel 8 by reactor 1 to be out diluted.
Preferably, the rectifying column 7 is hypergravity rectifier, and hypergravity rectifier small volume being capable of effectively save place
And space, disposal of pollutants is reduced, pattern of improving management and administration reduces productive labor intensity, improves production safety.
Preferred embodiment of the present utility model is the foregoing is only, not in order to limit this utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements that is made etc. should be included in this utility model
Protection domain within.
Claims (2)
1. a kind of resin production plant, including reactor（1）, horizontal separator（5）, thinning vessel（8）, it is characterised in that：Described
Reactor（1）Top gas outlet and vertical condenser（3）It is connected, vertical condenser（3）With horizontal separator（5）By horizontal
Condenser（4）It is connected；The horizontal separator（5）Coalescence filter core is inside provided with（5-1）, horizontal separator（5）Backflow pass through
Desiccant box（6）It is back to reactor（1）Interior, horizontal separator（5）Wastewater outlet and thinning vessel（8）Chuck water inlet phase
Even, thinning vessel（8）Chuck outlet passes through cooling tower（2）Connection horizontal condenser（4）Water inlet, horizontal condenser（4）'s
Outlet is by pipeline and thinning vessel（8）Chuck water inlet is connected；The horizontal separator（5）With thinning vessel（8）Between be provided with
Rectifying column（7）.
2. resin production plant according to claim 1, it is characterised in that：The rectifying column（7）For hypergravity rectifier.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620921829.XU CN206008109U (en) | 2016-08-23 | 2016-08-23 | A kind of resin production plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620921829.XU CN206008109U (en) | 2016-08-23 | 2016-08-23 | A kind of resin production plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206008109U true CN206008109U (en) | 2017-03-15 |
Family
ID=58250572
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620921829.XU Active CN206008109U (en) | 2016-08-23 | 2016-08-23 | A kind of resin production plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206008109U (en) |
-
2016
- 2016-08-23 CN CN201620921829.XU patent/CN206008109U/en active Active
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |