CN206027671U - Heating and thermal cycling device in softener production process - Google Patents
Heating and thermal cycling device in softener production process Download PDFInfo
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- CN206027671U CN206027671U CN201621056727.2U CN201621056727U CN206027671U CN 206027671 U CN206027671 U CN 206027671U CN 201621056727 U CN201621056727 U CN 201621056727U CN 206027671 U CN206027671 U CN 206027671U
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- heat
- heating
- exchanger tube
- heat exchanger
- softener
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Abstract
The utility model provides a heating and thermal cycling device in softener production process, including pyroreaction cauldron and low temperature reation kettle, the pyroreaction cauldron is equipped with first feed inlet and first discharge gate, the softener material is got into in the pyroreaction cauldron by first feed inlet, low temperature reation kettle is equipped with second feed inlet and second discharge gate, be equipped with material pumping pump between second feed inlet and the first discharge gate, be equipped with first heat exchange tube in the pyroreaction cauldron, be equipped with the second heat exchange tube in the low temperature reation kettle, the import of first heat exchange tube is connected in heating system through a heat conductive oil pipe, the export of first heat exchange tube is connected in the import of second heat exchange tube through the 2nd heat conductive oil pipe, the export of second heat exchange tube is connected in heating system through the 3rd heat conductive oil pipe, be equipped with the high temperature conduction oil in the heat conductive oil pipe. The utility model discloses utilize after waste heat and the heat exchange of reaction back material the heat of conduction oil to heat heat preservation low temperature reation kettle, can the make full use of heat, the heat conduction oil circulation heat exchange realizes heating and heat retaining cycle control.
Description
Technical field
This utility model is related to a kind of softener production equipment, the heating in more particularly to a kind of softener production process
With heat insulation circulating device.
Background technology
Need temperature-gradient method to be incubated in softener production process, be that material is positioned over into different reactors in prior art
In heated, heating-up temperature in different reactor is different, need to heat respectively, heats high energy consumption, and each reactor expends heat
Amount is more, and the temperature of each reactor need to be controlled, it is difficult to which control or control structure are complicated, in order to heat many reactors
Need to keep vacuum state, realize difficult.
Utility model content
For the problem that prior art is present, this utility model provides one kind and does not need vacuum condition, under low-temperature condition
Total overall reaction just can be completed the short period, simpler, accurate, saving time, and the softener production process of energy-conservation is operated
In heating and heat insulation circulating device.
To achieve these goals, this utility model is adopted the following technical scheme that：
Heating and heat insulation circulating device in a kind of softener production process, including pyroreaction kettle and low-temp reaction kettle,
The pyroreaction kettle is provided with first charging aperture and the first discharging opening, and softener material enters the height by the first charging aperture
In warm reactor, the low-temp reaction kettle is provided with second charging aperture and the second discharging opening, the second charging aperture and described first
Mateiral pump is provided between discharging opening, is provided with the first heat exchanger tube, is provided with second in the low-temp reaction kettle in the pyroreaction kettle
Heat exchanger tube, the import of first heat exchanger tube be connected to heating system by the first heat-conducting oil pipes, and first heat exchanger tube goes out
Mouth is connected to the import of second heat exchanger tube by the second heat-conducting oil pipes, and the outlet of second heat exchanger tube passes through the 3rd heat conduction
Oil pipe is connected to the heating system, is provided with high temperature heat conductive oil in first heat-conducting oil pipes.
Further, motor is additionally provided between first discharging opening and the second charging aperture, driven by the motor
The mateiral pump, by low-temp reaction kettle described in the softener material suction in the pyroreaction kettle.
Further, first heat-conducting oil pipes are provided with valve, for control into the heat conduction in first heat exchanger tube
The flow of oil.
Further, first heat exchanger tube or/and the second heat exchanger tube spiral be arranged at the pyroreaction kettle or/and
In the low-temp reaction kettle.
Further, the softener is with stearic acid, polyamines, emulsifying agent, cross-linking agent as raw material, through amidation process, season
Ammonium reaction and emulsion reaction are formed.
The beneficial effects of the utility model：
Softener material is incubated in being evacuated to low-temp reaction kettle after the completion of reacting in pyroreaction kettle by mateiral pump, meanwhile,
Conduction oil after first heat exchange intraductal heat exchange is entered in the second heat exchanger tube, more than reacting rear material by the second heat-conducting oil pipes
After heat and heat exchange, the heat of conduction oil carrys out heating and thermal insulation low-temp reaction kettle, can make full use of heat, and above-mentioned heating is not
Vacuum condition is needed, total overall reaction just can be completed under normal conditions the short period, heat conduction is oil circulation after the completion of reaction carries out hot friendship
Change, realize the loop control of heating and insulation, it is easy to control, it is simple to operate.
Description of the drawings
Fig. 1 is the heating in this utility model softener production process and the structural representation of heat insulation circulating device；
In figure, 1 pyroreaction kettle, 2 first charging apertures, 3 first discharging openings, 4 first heat exchanger tubes, 5 low temperature
Reactor, 6 second charging apertures, 7 second discharging openings, 8 second heat exchanger tubes, 9 mateiral pumps, 10 motors, 11 first
Heat-conducting oil pipes, 12 valves, 13 second heat-conducting oil pipes, 14 the 3rd heat-conducting oil pipes, 15 heating systems.
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 the present utility model, rather than all
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not making creative work premise
Lower obtained every other embodiment, belongs to the scope of this utility model protection.
Such as Fig. 1, this utility model provides the heating in a kind of softener production process and heat insulation circulating device, including high temperature
Reactor 1 and low-temp reaction kettle 5.The top of pyroreaction kettle 1 is provided with first charging aperture 2 and the first discharging opening 3, softener material
Entered in pyroreaction kettle 1 by first charging aperture 2, in pyroreaction kettle 1, be provided with the first heat exchanger tube 4,4 spiral of the first heat exchanger tube
It is arranged in pyroreaction kettle 1, the first heat exchanger tube 4 that spiral is arranged can increase heat exchange area.The entrance point of the first heat exchanger tube 4
The first heat-conducting oil pipes 11 are connected with, the first heat-conducting oil pipes 11 connect built with high temperature heat conductive oil, the other end of the first heat-conducting oil pipes 11
Heating system 15 is connected to, and by heating system 15 by heat-conducting oil heating, then first is flowed into through the first heat-conducting oil pipes 11 and is exchanged heat
In pipe 4, heat exchange is carried out with the softener material in pyroreaction kettle 1, so as to provide high temperature ring for the reaction of softener material
Border.Preferably, the first heat-conducting oil pipes 11 are provided with valve 12, the flow of the conduction oil entered in the first heat exchanger tube 4 for control,
So as to control the temperature in pyroreaction kettle 1.In the present embodiment, the temperature control of pyroreaction kettle 1 is at 180 DEG C or so.
The top of low-temp reaction kettle 5 is provided with second charging aperture 6 and the second discharging opening 7, second charging aperture 6 and the first discharging opening
Mateiral pump 9 and motor 10 is provided between 3, drives mateiral pump 9 to be evacuated to softener material by pyroreaction kettle 1 by motor 10 low
In warm reactor 5.Above-mentioned valve, mateiral pump and motor are all connected to electric-control system, automatically control conduction oil by electric-control system
Flow and mateiral pump and motor switch.It is provided with the second heat exchanger tube 8 in low-temp reaction kettle 5,8 spiral of the second heat exchanger tube sets
It is placed in pyroreaction kettle 5, the second heat exchanger tube 8 that spiral is arranged can increase heat exchange area.The import of the second heat exchanger tube 8 passes through
Second heat-conducting oil pipes 13 are connected to the outlet of the first heat exchanger tube 4, and the outlet of the second heat exchanger tube 8 is connected by the 3rd heat-conducting oil pipes 14
In heating system 15.The conduction oil in First Heat Exchanger 4 is introduced in the second heat exchanger tube 8 by the second heat-conducting oil pipes 13, utilized
After the waste heat of reacting rear material and heat exchange, the heat of conduction oil carrys out heating and thermal insulation low-temp reaction kettle 5, can make full use of heat
Amount.Temperature stabilization of the softener material in low-temp reaction kettle 5 now adds in low-temp reaction kettle 5 at 100 DEG C -110 DEG C or so
Enter cross-linking agent, temperature has a small amount of intensification, temperature control made at 110 DEG C -115 DEG C, until reaction terminates.Reaction is submissive after terminating
Agent material is discharged by the second discharging opening 7.After the completion of reaction, conduction oil is flow back into by the 3rd heat-conducting oil pipes 14 of 8 Jing of the second heat exchanger tube
Reheat in heating system 15, realize the loop control of heating and insulation, heat utilization ratio is high.
Softener of the present utility model with stearic acid, polyamines, emulsifying agent, cross-linking agent as raw material, through amidation process, season
Ammonium reaction and emulsion reaction are formed, it is not necessary to vacuum condition, under the heating of above-mentioned circulating device just can the short period it is complete
Into total overall reaction, operation is simpler, accurate, saves the time, so as to improve work efficiency, it is ensured that product quality.
Above example is only unrestricted to illustrate the technical solution of the utility model, although with reference to preferred embodiment pair
This utility model has been described in detail, it will be appreciated by those skilled in the art that can enter to the technical solution of the utility model
Row modification or equivalent, without deviating from the objective and scope of the technical program, which all should be covered in power of the present utility model
In sharp claimed range.
Claims (5)
1. the heating in a kind of softener production process and heat insulation circulating device, it is characterised in that include：Pyroreaction kettle and low
Warm reactor, the pyroreaction kettle are provided with first charging aperture and the first discharging opening, and softener material is by the first charging aperture
Into in the pyroreaction kettle, the low-temp reaction kettle is provided with second charging aperture and the second discharging opening, the second charging aperture
Mateiral pump is provided between first discharging opening, is provided with the first heat exchanger tube, the low-temp reaction kettle in the pyroreaction kettle
Second heat exchanger tube is provided with inside, the import of first heat exchanger tube is connected to heating system by the first heat-conducting oil pipes, described first
The outlet of heat exchanger tube is connected to the import of second heat exchanger tube by the second heat-conducting oil pipes, and the outlet of second heat exchanger tube is led to
Cross the 3rd heat-conducting oil pipes and be connected to the heating system, in first heat-conducting oil pipes, be provided with high temperature heat conductive oil.
2. the heating in softener production process according to claim 1 and heat insulation circulating device, it is characterised in that：It is described
Motor is additionally provided between first discharging opening and the second charging aperture, the mateiral pump is driven by the motor, will be described
In low-temp reaction kettle described in softener material suction in pyroreaction kettle.
3. the heating in softener production process according to claim 1 and heat insulation circulating device, it is characterised in that：It is described
First heat-conducting oil pipes are provided with valve, the flow of the conduction oil entered in first heat exchanger tube for control.
4. the heating in softener production process according to claim 1 and heat insulation circulating device, it is characterised in that：It is described
First heat exchanger tube or/and the second heat exchanger tube spiral are arranged in the pyroreaction kettle or/and the low-temp reaction kettle.
5. the heating in softener production process according to claim 1 and heat insulation circulating device, it is characterised in that：It is described
Softener with stearic acid, polyamines, emulsifying agent, cross-linking agent as raw material, through amidation process, quaterisation and emulsion reaction shape
Into.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621056727.2U CN206027671U (en) | 2016-09-14 | 2016-09-14 | Heating and thermal cycling device in softener production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621056727.2U CN206027671U (en) | 2016-09-14 | 2016-09-14 | Heating and thermal cycling device in softener production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206027671U true CN206027671U (en) | 2017-03-22 |
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ID=58297501
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621056727.2U Active CN206027671U (en) | 2016-09-14 | 2016-09-14 | Heating and thermal cycling device in softener production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206027671U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112047763A (en) * | 2020-09-14 | 2020-12-08 | 河南理工大学 | Device and process method for preparing fertilizer by utilizing kitchen waste |
| CN113521780A (en) * | 2021-09-02 | 2021-10-22 | 东营益盛化工有限公司 | Esterification tower for producing butyl acetate |
| CN114768574A (en) * | 2022-05-06 | 2022-07-22 | 沈慧 | System for producing cosmetic products |
-
2016
- 2016-09-14 CN CN201621056727.2U patent/CN206027671U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112047763A (en) * | 2020-09-14 | 2020-12-08 | 河南理工大学 | Device and process method for preparing fertilizer by utilizing kitchen waste |
| CN113521780A (en) * | 2021-09-02 | 2021-10-22 | 东营益盛化工有限公司 | Esterification tower for producing butyl acetate |
| CN114768574A (en) * | 2022-05-06 | 2022-07-22 | 沈慧 | System for producing cosmetic products |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 510000 Room 101, building 4, No. 23, sukeng street, Panyu District, Guangzhou City, Guangdong Province Patentee after: Guangzhou xieyanlai Industrial Co., Ltd Address before: Meishan village Panyu District Hualong Town Guangzhou Guangdong province 510000 City Gang of two face three four Patentee before: Guangzhou Panyu Xie Yun Lai Chemical Necessities Factory |