CN107166982A - A kind of emulsion steam-heating system - Google Patents
A kind of emulsion steam-heating system Download PDFInfo
- Publication number
- CN107166982A CN107166982A CN201710517225.8A CN201710517225A CN107166982A CN 107166982 A CN107166982 A CN 107166982A CN 201710517225 A CN201710517225 A CN 201710517225A CN 107166982 A CN107166982 A CN 107166982A
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- China
- Prior art keywords
- emulsion
- steam
- heating system
- heater box
- pipe
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/08—Auxiliary systems, arrangements, or devices for collecting and removing condensate
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
The invention discloses a kind of emulsion steam-heating system, including:Heater box, heating tube, reheating pipe.Wherein, heating tube is used to once heat the emulsion in heater box, and the emulsion after reheating pipe is used for once heating carries out reheating.In the running, steam enters heater box from heating tube, carries out heat exchange with emulsion, completes the steam after heat exchange and enters reheating pipe and carry out secondary heat exchange with emulsion.The setting can be heated further using the heat in steam to emulsion, raise the temperature of emulsion;Reduce the usage amount of source steam and the growing amount of condensed water simultaneously.Therefore, emulsion steam-heating system proposed by the present invention can reduce the usage amount of steam, reduce the growing amount of condensed water, improve the temperature of emulsion, it is ensured that being smoothed out for cold-rolling process, solve the problem in the field at this stage.
Description
Technical field
The present invention relates to emulsion domain of control temperature, more specifically to a kind of emulsion steam-heating system.
Background technology
Emulsion is a kind of high performance semi-synthetic metal working fluid, the effect with lubrication synergy, for improving processing
Surface quality of part etc., is commonly used for the lubricant of cold-rolling process.In use, emulsion ability within the scope of certain temperature
Good effect is played, it is too high or too low for temperature, it can influence its service behaviour.Therefore, it is necessary to emulsion in actual production
Temperature carry out strict control, it is possessed higher activity, it is ensured that cold-rolling process process is smoothed out.
In actual production, generally steam is used to heat emulsion, to meet the temperature parameter that emulsion is optimal;I.e.
Steam enters the heater box 1 equipped with emulsion, completes the steam of heat exchange because condensation forms steam water interface, a part is straight
Run in and stored into cesspool 9, another part into boiler 8.It please specifically refer to Fig. 2.
For prior art, because the temperature of emulsion is relatively low, have to enter control steam during heat exchange
Bypass pipe 10 valve 11 open and be transferred to maximum aperture, to be heated to emulsion, nonetheless, remain difficult to expire
The optimum working temperature of sufficient emulsion, while so that the waste of steam in source is serious;Also, because steam endlessly enters
Enter, more condensed water is formed after causing heat exchange, and because of the limited storage space of boiler 8 so that unnecessary condensed water is straight
Run in into cesspool 9, cause to waste.
Therefore, the usage amount of steam how is reduced, the growing amount of condensed water is reduced, and improves the temperature of emulsion, is made cold
Roll process is smoothed out, and is field problem urgently to be resolved hurrily at this stage.
The content of the invention
In view of this, it is an object of the invention to provide a kind of emulsion steam-heating system, the system can reduce steaming
The usage amount of vapour, reduces the growing amount of condensed water, and improves the temperature of emulsion, is smoothed out cold-rolling process, solves existing
The problem in the stage field.
A kind of emulsion steam-heating system, including:
Emulsion is provided with heater box, the heater box;
Heating tube, the heating tube is through the heater box, for heating the emulsion, the two ends point of the heating tube
Wei not first entrance and first outlet;
Reheating pipe, the reheating pipe is through the heater box, for being reheated to the emulsion, the reheating pipe
Two ends be respectively second entrance and second outlet, and the second entrance is connected with the first outlet;
Steam enter from the first entrance and with the emulsion carry out heat exchange, complete heat exchange after formed steam with
The steam water interface of condensed water is simultaneously discharged from the second outlet.
It is preferred that, described emulsion steam-heating system, in addition to:
Boiler, the boiler is used to reclaim the steam water interface;
Cesspool, the cesspool is used to reclaim the condensed water that the steam water interface and the boiler overflow.
It is preferred that, described emulsion steam-heating system, in addition to bypass pipe and valve, the bypass pipe be it is multiple,
It is separately positioned on the first access point, at the first outlet and at the second outlet, and on each described bypass pipe
Provided with the valve.
It is preferred that, described emulsion steam-heating system, the part that the heating tube is placed in the heater box is snake
Shape pipe.
It is preferred that, described emulsion steam-heating system, the part that the reheating pipe is placed in the heater box is snake
Shape pipe.
It is preferred that, described emulsion steam-heating system, at the first outlet temperature of steam water interface 80 DEG C-
Between 100 DEG C.
It is preferred that, described emulsion steam-heating system, emulsion temperature after being heated through the reheating pipe 52 DEG C-
Between 65 DEG C.
Emulsion steam-heating system proposed by the present invention, including:Heater box, heating tube, reheating pipe.Wherein, heating tube
For once being heated to the emulsion in heater box, the emulsion after reheating pipe is used for once heating carries out secondary add
Heat.In the running, steam enters heater box from heating tube, carries out heat exchange with emulsion, completes after heat exchange
Steam enters reheating pipe and carries out secondary heat exchange with emulsion.The setting can further utilize the heat in steam to emulsification
Liquid is heated, and raises the temperature of emulsion;Reduce the usage amount of source steam and the growing amount of condensed water simultaneously.Cause
This, emulsion steam-heating system proposed by the present invention can reduce the usage amount of steam, reduce the growing amount of condensed water, improve
The temperature of emulsion, it is ensured that being smoothed out for cold-rolling process, solves the problem in the field at this stage.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
There is the accompanying drawing used required in technology description to be briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the schematic diagram of emulsion steam-heating system in the specific embodiment of the invention;
Fig. 2 is the schematic diagram of emulsion steam-heating system in background of invention.
In Fig. 1-Fig. 2:
Heater box -1, heating tube -2, reheating pipe -3, first entrance -4, first outlet -5, second entrance -6,
Two outlets -7, boiler -8, cesspool -9, bypass pipe -10, valve -11.
Embodiment
The core of present embodiment is to provide a kind of emulsion steam-heating system, and the system can reduce steam
Usage amount, reduce the growing amount of condensed water, and improve the temperature of emulsion, be smoothed out cold-rolling process, solve existing rank
The problem in the section field.
Hereinafter, embodiment is illustrated referring to the drawings.In addition, embodiments illustrated below is not to described in claim
The content of the invention rise any restriction effect.In addition, the full content of the composition represented by example below is not limited to as right
It is required that necessary to the solution of described invention.
The emulsion steam-heating system that present embodiment is provided, mainly includes:Heater box 1, heating tube 2, reheating
Pipe 3.Wherein, there is emulsion to be heated in heater box 1;Heating tube 2 is through heater box 1, for the emulsification inside heater box 1
Liquid is once heated, and its two ends is respectively the first entrance 4 and first outlet 5 flowed through for steam;Reheating pipe 3, which is passed through, to be added
Hot tank 1, for carrying out reheating to emulsion, and its two ends is respectively second entrance 6 and second outlet 7, and second entrance 6
It is connected with above-mentioned first outlet 5, i.e., the steam after once exchanging heat is directly entered reheating pipe 3, and secondary with emulsion progress
Heat exchange, makes full use of the after-heat in steam.Steam enters from first entrance 4 and carries out heat exchange twice with emulsion, complete
Steam into heat exchange forms the steam water interface of steam and condensed water and discharged from second outlet 7.It please specifically refer to Fig. 1.
The emulsion steam-heating system that present embodiment is provided, in the running, steam is from heating
Pipe 2 enter heater box 1, with emulsion carry out heat exchange, complete heat exchange after steam enter reheating pipe 3 and with heater box 1
Emulsion carries out secondary heat exchange.The setting can be heated further using the heat in steam to emulsion, make emulsification
The temperature rise of liquid;Reduce the usage amount of source steam and the growing amount of condensed water simultaneously.Therefore, emulsification proposed by the present invention
Liquid steam-heating system can reduce the usage amount of steam, reduce the growing amount of condensed water, and improve the temperature of emulsion, make cold
Roll process is smoothed out, and solves the problem in the field at this stage.
The emulsion steam-heating system that present embodiment is provided, can also include:Boiler 8, cesspool 9.Its
In, boiler 8 is used to reclaim the steam water interface completed after heat exchange;Cesspool 9 is used to reclaim the steam-water mixing completed after heat exchange
Thing, and the unnecessary condensed water that boiler 8 overflows.This is designed to further collect the steam for completing heat exchange, and many
Remaining condensed water then drains into cesspool 9 in case he uses.It please specifically refer to Fig. 1.
The emulsion steam-heating system that present embodiment is provided, can also include bypass pipe 10 and be arranged on bypass
Valve 11 on pipe 10.Bypass pipe 10 to be multiple, can be separately positioned at first entrance 4, at first outlet 5, second outlet 7
Place, and be equipped with each bypass pipe 10 for controlling its through-flow valve 11.The setting can be when steam be not enough as standby
With can further expand the inlet of steam, emulsion is sufficiently heated, to meet the temperature model that emulsion is optimal
Enclose.It please specifically refer to Fig. 1.
The emulsion steam-heating system that present embodiment is provided, in order to increase the contact of emulsion and heating tube 2
Heating tube 2 inside heater box 1, can be designed as the coiled pipe of bending by area, the efficiency of increase heat exchange;Similarly, also
Reheating pipe 3 inside heater box 1 can be set to coiled pipe.It please specifically refer to Fig. 1.
The emulsion steam-heating system that present embodiment is provided, the system can exist the temperature control of emulsion
Its optimal operating temperature range, complete once exchange heat after, at first outlet 5 steam water interface temperature range at 80 DEG C -100
Between DEG C;After secondary heat exchange, the temperature of emulsion can be controlled between 52 DEG C -65 DEG C, the temperature of emulsion in the design
Degree is benefit with 55 DEG C;This is designed to the activation plays of emulsion to optimal, can preferably ensure the smooth of cold-rolling process
Carry out.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or using the present invention.
A variety of modifications to these embodiments will be apparent for those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, it is of the invention
The embodiments shown herein is not intended to be limited to, and is to fit to and principles disclosed herein and features of novelty phase one
The most wide scope caused.
Claims (7)
1. a kind of emulsion steam-heating system, it is characterised in that including:
Emulsion is provided with heater box (1), the heater box (1);
Heating tube (2), the heating tube (2) is through the heater box (1), for heating the emulsion, the heating tube (2)
Two ends be respectively first entrance (4) and first outlet (5);
Reheating pipe (3), the reheating pipe (3) is described through the heater box (1), for being reheated to the emulsion
The two ends of reheating pipe (3) are respectively second entrance (6) and second outlet (7), and the second entrance (6) and the first outlet
(5) it is connected;
Steam from the first entrance (4) enter and with the emulsion carry out heat exchange, complete heat exchange after formed steam with it is cold
The steam water interface of solidifying water is simultaneously discharged from the second outlet (7).
2. emulsion steam-heating system according to claim 1, it is characterised in that also include:
Boiler (8), the boiler (8) is used to reclaim the steam water interface;
Cesspool (9), the cesspool (9) is used to reclaim the condensation that the steam water interface and the boiler (8) overflow
Water.
3. emulsion steam-heating system according to claim 1, it is characterised in that also including bypass pipe (10) and valve
(11), the bypass pipe (10) is multiple, is separately positioned on the first entrance (4) place, the first outlet (5) place and described
The valve (11) is equipped with second outlet (7) place, and each described bypass pipe (10).
4. emulsion steam-heating system according to claim 1, it is characterised in that the heating tube (2) is placed in described
Part in heater box (1) is coiled pipe.
5. emulsion steam-heating system according to claim 1, it is characterised in that the reheating pipe (3) is placed in described
Part in heater box (1) is coiled pipe.
6. emulsion steam-heating system according to claim 1, it is characterised in that first outlet (5) place carbonated drink
The temperature of mixture is between 80 DEG C -100 DEG C.
7. emulsion steam-heating system according to claim 1, it is characterised in that after being heated through the reheating pipe (3)
Emulsion temperature between 52 DEG C -65 DEG C.
Priority Applications (1)
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CN201710517225.8A CN107166982A (en) | 2017-06-29 | 2017-06-29 | A kind of emulsion steam-heating system |
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CN201710517225.8A CN107166982A (en) | 2017-06-29 | 2017-06-29 | A kind of emulsion steam-heating system |
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CN107166982A true CN107166982A (en) | 2017-09-15 |
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CN201710517225.8A Pending CN107166982A (en) | 2017-06-29 | 2017-06-29 | A kind of emulsion steam-heating system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109482657A (en) * | 2018-12-26 | 2019-03-19 | 西南铝业(集团)有限责任公司 | A kind of milling train emulsion temperature control system and hot finishing mill |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1990588A2 (en) * | 2007-05-11 | 2008-11-12 | Mecoswiss Mechanische Componenten GmbH & Co. KG | Household machine with a cooling device |
CN101575044A (en) * | 2009-06-11 | 2009-11-11 | 上海宝钢工程技术有限公司 | Method for controlling temperature of crude oil for emulsion of rolling mill and control device |
CN101852557A (en) * | 2010-06-12 | 2010-10-06 | 沈阳石蜡化工有限公司 | Decoking method of tubular heater of urea dewaxing device |
CN101912883A (en) * | 2010-08-12 | 2010-12-15 | 宝钢工程技术集团有限公司 | Circulation heating system for steam heater |
CN102767972A (en) * | 2012-06-18 | 2012-11-07 | 中冶南方工程技术有限公司 | Method and device for recovering condensate water in steam heating system |
-
2017
- 2017-06-29 CN CN201710517225.8A patent/CN107166982A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1990588A2 (en) * | 2007-05-11 | 2008-11-12 | Mecoswiss Mechanische Componenten GmbH & Co. KG | Household machine with a cooling device |
CN101575044A (en) * | 2009-06-11 | 2009-11-11 | 上海宝钢工程技术有限公司 | Method for controlling temperature of crude oil for emulsion of rolling mill and control device |
CN101852557A (en) * | 2010-06-12 | 2010-10-06 | 沈阳石蜡化工有限公司 | Decoking method of tubular heater of urea dewaxing device |
CN101912883A (en) * | 2010-08-12 | 2010-12-15 | 宝钢工程技术集团有限公司 | Circulation heating system for steam heater |
CN102767972A (en) * | 2012-06-18 | 2012-11-07 | 中冶南方工程技术有限公司 | Method and device for recovering condensate water in steam heating system |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109482657A (en) * | 2018-12-26 | 2019-03-19 | 西南铝业(集团)有限责任公司 | A kind of milling train emulsion temperature control system and hot finishing mill |
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Application publication date: 20170915 |