CN204429279U - A kind of reactor conduction oil induction system - Google Patents
A kind of reactor conduction oil induction system Download PDFInfo
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- CN204429279U CN204429279U CN201520037680.4U CN201520037680U CN204429279U CN 204429279 U CN204429279 U CN 204429279U CN 201520037680 U CN201520037680 U CN 201520037680U CN 204429279 U CN204429279 U CN 204429279U
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- reactor
- deep fat
- oil
- conduction oil
- fat still
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- 230000006698 induction Effects 0.000 title claims abstract description 9
- 239000000498 cooling water Substances 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 abstract description 7
- 238000009841 combustion method Methods 0.000 abstract description 2
- 239000000446 fuel Substances 0.000 abstract 1
- 230000001737 promoting effect Effects 0.000 abstract 1
- 239000003995 emulsifying agent Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000003763 carbonization Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
A kind of reactor conduction oil induction system, comprises reactor 9, deep fat still 4, repairing tank 7, connects to form reactor conduction oil conveying device successively by pipeline valve, Heat-transfer Oil Pump 5.Conduction oil in deep fat still is delivered in reacting kettle jacketing 13 by Heat-transfer Oil Pump 5, and the oil of repairing tank enters into deep fat still 4, and conduction oil is full of deep fat still 4 chuck, and conduction oil is at reacting kettle jacketing 13 Inner eycle heated material.React complete, stop circulation, the conduction oil in reacting kettle jacketing 13 is put to repairing tank 7, then steam, cooling water are entered in reactor by coil pipe and material is cooled.By hot oil pump to reacting kettle jacketing fuel feeding, ensure material evenly heat up and can cool fast, improve the quality of products, can also prevent the dry combustion method of deep fat still and conduction oil overheated.The utility model structure is simple, and small investment, can increase economic efficiency, and has larger promotional value.
Description
Technical field
The utility model relates to the production equipment of emulsifying agent, and particularly a kind of reactor conduction oil induction system system, is a kind of improved system.
Background technology
In process of production, conduction oil in deep fat still is entered reactor by pipeline by Heat-transfer Oil Pump, and in deep fat still, the liquid level of conduction oil declines, heater meeting dry combustion method; Conduction oil temperature often exceeds technological temperature, bad control; After having reacted due to high temperature heat conductive oil in reacting kettle jacketing, material cooling velocity is slow, efficiency is low, and affects emulsifying agent and normally produce and product quality.
Summary of the invention
The purpose of this utility model is in emulsifying agent production process, adopts the heater in deep fat still to heat conduction oil.The conduction oil of intensification is thrown in reacting kettle jacketing and is evenly heated up to material by recycling hot oil pump, the temperature of conduction oil is by temperature digital display transmitter, temperature signal is fed back on Central Control Room computer, when temperature exceeds technological temperature, several groups of heaters closed automatically by computer, allow conduction oil constant temperature at technological temperature; High temperature heat conductive oil after reacting completely in emptying reacting kettle jacketing, logical steam and cold water carry out fast cooling to emulsifying agent successively.
Solve the technical scheme of the utility model technical problem: a kind of reactor conduction oil conveying device, comprise reactor, deep fat still, repairing tank, reactor conduction oil conveying device is connected to form successively by pipeline, valve, Heat-transfer Oil Pump, reactor is connected with deep fat still by its oil-out pipeline, deep fat still is connected with repairing tank through conduction oil repairing pipe, deep fat still is connected with reactor bottom through Heat-transfer Oil Pump, reactor heat conductive oil inlet pipeline, is connected bottom reactor with repairing tank top.Side, described reactor top is provided with conduction oil outlet and steam, cooling water inlet; Described reactor bottom is provided with its heat conductive oil inlet pipeline, steam and cooling water outlet, heat conductive oil inlet and conduction oil drain, in described reactor, be provided with reacting kettle jacketing.Described deep fat still top is provided with deep fat still evacuation port and deep fat still oil-in, in deep fat still, is provided with deep fat kettle heater, is provided with deep fat still oil-out in deep fat still lower side.Described repairing tank 7 is provided with repairing tank oil-collecting hole above, has benefit tank nozzle, be provided with the oil-feed of repairing tank and evacuation port in repairing tank upper right side on the left of repairing tank.Conduction oil after intensification in deep fat still is delivered in reacting kettle jacketing by Heat-transfer Oil Pump, and the conduction oil in repairing tank flow into deep fat still, supplements deep fat still conduction oil and enters reacting kettle jacketing part, return deep fat still, circulating-heating emulsifying agent after being full of chuck; After reaction terminates, the high temperature heat conductive oil in emptying reacting kettle jacketing, passes into steam by coil pipe under vacuum conditions, cooling water comes to cool emulsifying agent fast successively, lower the temperature.
This technological improvement effectively solves that uneven, the local temperature of emulsifying agent heating is too high causes the problems such as the easy carbonization of conduction oil, easily decomposition, make reaction temperature accurate, adjustable, not only increase the reaction efficiency of esterification, and this mode of heating can ensure conduction oil constant temperature, extend the service life of conduction oil greatly; By the quick cooling of cooling water, effectively solve the problem that product oxidation color deepens, the utility model structure is simple, small investment.After installing this device, can raise labour efficiency, product quality reaches requirement, and increases.
Accompanying drawing explanation
Fig. 1 is the utility model assembling front view
Fig. 2 is the front view of the utility model reactor
Fig. 3 is the utility model deep fat still front view
Fig. 4 is the utility model repairing tank front view
In figure: 1 reactor conduction oil outlet, 2 conduction oil repairing pipes, 3 deep fat still evacuated tube, 4 deep fat stills, 5 Heat-transfer Oil Pump, 6 reactor conduction oil oil inlet pipes, 7 repairing tanks, 8 oil-feed of repairing tank and evacuated tube, 9 reactors, 10 reactor temperature digital display transmitters, 11 reactor conduction oil outlets, 12 steam and cooling water inlet, 13 reacting kettle jacketings, 14 steam and cooling water outlet, 15 reactor heat conductive oil inlets, 16 reactor conduction oil drains, 17 deep fat still temperature digital display transmitters, 18 deep fat kettle heaters, 19 deep fat still evacuation ports, 20 deep fat still oil-outs, 21 deep fat still oil-ins, 22 repairing tank oil-collecting holes, 23 mend tank nozzle, 24 oil-feed of repairing tank and evacuation ports.
Detailed description of the invention
With reference to accompanying drawing 1-4: a kind of reactor heat conduction induction system, comprise reactor 9, deep fat still 4, repairing tank 7, reactor conduction oil conveying device is connected to form successively by pipeline valve Heat-transfer Oil Pump 5, described reactor 9 is connected with deep fat still 4 by its oil-out 1 pipeline, deep fat still 4 is connected with repairing tank 7 through conduction oil repairing pipe 2, deep fat still 4 is connected with reactor 4 bottom through Heat-transfer Oil Pump 5 reactor conduction oil oil inlet pipe 6, is connected bottom reactor 9 with repairing tank 7 top.Side, described reactor 9 top is provided with reactor temperature digital display transmitter 10, conduction oil outlet 11 and steam cooling water inlet 12; Described reactor 9 bottom is provided with its conduction oil oil inlet pipe 6, steam and cooling water outlet 14, reactor heat conductive oil inlet 15 and reactor conduction oil drain 16, in described reactor 9, be provided with reacting kettle jacketing 13.Described deep fat still 4 top is provided with deep fat still temperature digital display transmitter 17, and deep fat still evacuation port 19 and deep fat still oil-in 21, be provided with deep fat kettle heater 18 in deep fat still, is provided with deep fat still oil-out 20 in deep fat still lower side.Described repairing tank 7 is provided with repairing tank oil-collecting hole 22 above, has and mends tank nozzle 23, be provided with the oil-feed of repairing tank and evacuation port 24 in repairing tank upper right side on the left of repairing tank.
Conduction oil in deep fat still is delivered in reacting kettle jacketing 13 by Heat-transfer Oil Pump 5, and at this moment the oil of repairing tank enters into deep fat still 4, and ensure that conduction oil is full of deep fat still 4 all the time, conduction oil is at reacting kettle jacketing 13 Inner eycle heated material.React complete, stop circulation, the conduction oil in reacting kettle jacketing 13 is put to repairing tank 7, then steam, cooling water are entered in reactor by coil pipe and material is cooled.
Claims (4)
1. a reactor conduction oil induction system, comprise reactor (9), deep fat still (4), repairing tank (7), pass through pipeline, valve, Heat-transfer Oil Pump (5) connects to form reactor conduction oil conveying device successively, it is characterized in that: described reactor (9) is connected with deep fat still (4) by its oil-out (1) pipeline, deep fat still (4) is connected with repairing tank (7) through conduction oil repairing pipe (2), deep fat still (4) is through Heat-transfer Oil Pump (5), reactor conduction oil inflow pipeline (6) is connected with reactor (4) bottom, reactor (9) bottom is connected with repairing tank (7) top, . described reactor (9) side, top is provided with conduction oil outlet (11) and steam cooling water inlet (12), described reactor (9) bottom is provided with its conduction oil oil inlet pipe (6), steam and cooling water outlet (14), reactor heat conductive oil inlet (15) and reactor conduction oil drain (16).
2. a kind of reactor conduction oil induction system as claimed in claim 1, is characterized in that
:reactor temperature digital display transmitter (10), reacting kettle jacketing (13) is provided with in described reactor (9).
3. a kind of reactor conduction oil induction system as claimed in claim 2, is characterized in that
:described deep fat still (4) top is provided with deep fat still temperature digital display transmitter (17) deep fat still evacuation port (19) and deep fat still oil-in (21); Deep fat kettle heater (18) is provided with in deep fat still; Deep fat still oil-out (20) is provided with in deep fat still lower side.
4. a kind of reactor conduction oil induction system as claimed in claim 3, is characterized in that
:described repairing tank (7) is provided with repairing tank oil-collecting hole (22) above, has and mends tank nozzle (23), be provided with the oil-feed of repairing tank and evacuation port (24) in repairing tank upper right side on the left of repairing tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520037680.4U CN204429279U (en) | 2015-01-20 | 2015-01-20 | A kind of reactor conduction oil induction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520037680.4U CN204429279U (en) | 2015-01-20 | 2015-01-20 | A kind of reactor conduction oil induction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204429279U true CN204429279U (en) | 2015-07-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520037680.4U Expired - Fee Related CN204429279U (en) | 2015-01-20 | 2015-01-20 | A kind of reactor conduction oil induction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204429279U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104667855A (en) * | 2015-01-20 | 2015-06-03 | 湖南省南岭化工集团有限责任公司 | Heat-conducting oil transport system for reaction kettle |
| CN111569658A (en) * | 2020-04-22 | 2020-08-25 | 中国工程物理研究院材料研究所 | High-low temperature circulating device for thermal cycle adsorption separation device |
-
2015
- 2015-01-20 CN CN201520037680.4U patent/CN204429279U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104667855A (en) * | 2015-01-20 | 2015-06-03 | 湖南省南岭化工集团有限责任公司 | Heat-conducting oil transport system for reaction kettle |
| CN111569658A (en) * | 2020-04-22 | 2020-08-25 | 中国工程物理研究院材料研究所 | High-low temperature circulating device for thermal cycle adsorption separation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180716 Address after: 425200 No. 6 Shuangbei Road, Yupo Town, Shuangpai County, Yongzhou City, Hunan Province Patentee after: Hunan Nanling Fine Chemical Co., Ltd. Address before: 425200 No. 6 Shuangbei Road, Yupo Town, Shuangpai County, Yongzhou City, Hunan Province Patentee before: Hunan Nanling Chemical Group Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150701 Termination date: 20210120 |
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| CF01 | Termination of patent right due to non-payment of annual fee |