CN108518670A - A kind of vapour system - Google Patents
A kind of vapour system Download PDFInfo
- Publication number
- CN108518670A CN108518670A CN201810436528.1A CN201810436528A CN108518670A CN 108518670 A CN108518670 A CN 108518670A CN 201810436528 A CN201810436528 A CN 201810436528A CN 108518670 A CN108518670 A CN 108518670A
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- CN
- China
- Prior art keywords
- steam
- pipeline
- optionally
- vapour
- moist
- Prior art date
- 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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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/32—Feed-water heaters, i.e. economisers or like preheaters arranged to be heated by steam, e.g. bled from turbines
- F22D1/34—Feed-water heaters, i.e. economisers or like preheaters arranged to be heated by steam, e.g. bled from turbines and returning condensate to boiler with main feed supply
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/02—Pipe-line systems for gases or vapours
- F17D1/06—Pipe-line systems for gases or vapours for steam
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D3/00—Arrangements for supervising or controlling working operations
- F17D3/14—Arrangements for supervising or controlling working operations for eliminating water
- F17D3/145—Arrangements for supervising or controlling working operations for eliminating water in gas pipelines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/26—Steam-separating arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D5/00—Controlling water feed or water level; Automatic water feeding or water-level regulators
- F22D5/08—Controlling water feed or water level; Automatic water feeding or water-level regulators with float-actuated valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D5/00—Controlling water feed or water level; Automatic water feeding or water-level regulators
- F22D5/26—Automatic feed-control systems
- F22D5/34—Applications of valves
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The present invention discloses a kind of vapour system, is related to Garment Technology field, and primary structure includes boiler, steam inlet pipe road, aerated water purification separator, steam exhaust piping and recovery tank, and steam inlet pipe road includes moist steam pipeline, and dry blowing vapor pipeline is arranged on moist steam pipeline；Water from recovery tank is heated into moist steam by boiler, pass through moist steam Pipeline transport to aerated water purification separator, aerated water purification separator removes moisture extra in moist steam, and moist steam is made to become dry saturated steam, and dry saturated steam enters dry blowing vapor pipeline, the heat of moist steam can heat dry saturated steam, make dry saturated steam that higher temperature be kept to increase the utilization rate of steam to reduce the water droplet in dry saturated steam, the utilization rate for improving boiler heat, reaches energy-saving and environment-friendly purpose.
Description
Technical field
The present invention relates to Garment Technology fields, more particularly to a kind of vapour system.
Background technology
Many enterprises all can carry out manufacture production using steam at present, mainly by the way that tap water to be passed into boiler
Water is heated into gaseous state by portion, boiler, is then connected to each gas utilization unit by steam (vapor) outlet.
Heat source is used steam as indirectly to the heater of material, is reduced by discharging latent heat condensation after steam heat-exchanging
The saturation condensed water of temperature, this saturation condensed water is preferable distilled water, most suitable to be used as boiler feedwater, but this saturation condenses
Water is with open recycling or is directly excluded by drain valve, not only waste of energy but also increases cost.
Although a part of device in the prior art forms the access of steam circulation, but steam passes through steam drying machine
Retracting device just is flowed to from exit afterwards, most steam is not condensed into water fully and just dried via steam
The outlet of dry machine is flowed out, and the utilization rate of steam is very low.And the production cost of clothes production enterprise is higher and higher now, energy of getting a profit
Power is more and more weaker, and therefore, it is urgent to provide a kind of vapour systems that can improve clothing factory's steam utilization.
Invention content
In order to solve the above technical problems, the present invention provides a kind of vapour system, can improve the utilization rate of steam, reduces clothes
Fill the production cost of manufacturing enterprise.
To achieve the above object, the present invention provides following schemes：
The present invention provides a kind of vapour system, including boiler, steam inlet pipe road, aerated water purification separator, steam exhaust piping and returns
Water tank；The steam inlet pipe road is set between the boiler and the aerated water purification separator, and the steam exhaust piping is set to institute
It states between the discharge outlet of aerated water purification separator and the recovery tank, moisturizing is provided between the recovery tank and the boiler
It pumps, multiple vapour interfaces is provided on the steam inlet pipe road, multiple back-steam interfaces are provided in the steam exhaust piping；It is described into vapour
Pipeline includes moist steam pipeline, is arranged with dry blowing vapor pipeline on the moist steam pipeline, moist steam pipeline one end with it is described
The steam (vapor) outlet of boiler is connected, and the other end of the moist steam pipeline is connected with the import of the aerated water purification separator,
The dry blowing vapor pipeline is connected with the outlet of the aerated water purification separator.
Optionally, the recovery tank includes babinet, and coil pipe, described coil pipe one end and the back-steam are provided in the babinet
Pipeline is connected, and the other end of the coil pipe is connected to one end of an escape pipe, and the other end of the escape pipe is connected to the babinet
It is internal；
Optionally, the top of the box is provided with manhole；
Optionally, it is provided with removable cover on the manhole；
Optionally, the babinet top is provided with gas vent；
Optionally, the babinet top is provided with ball-cock assembly；
Optionally, the lower box is provided with water outlet；
Optionally, the water outlet is connected with the water inlet of the small pump；
Optionally, the axis direction on the coil pipe perpendicular to the coil pipe is provided with multiple branch pipes；
Optionally, the multiple branch pipe is set to the top and bottom of the coil pipe.
Optionally, the multiple to be set on the dry blowing vapor pipeline with vapour interface；
Optionally, the multiple top that the dry blowing vapor pipeline is set to vapour interface；
Optionally, the water out of the aerated water purification separator is connected by the back-steam pipeline with the recovery tank；
Optionally, it is arranged with insulating layer on the dry blowing vapor pipeline；
Optionally, the return tube road is arranged with insulating layer；
Optionally, the back-steam interface is set to the top of the back-steam pipeline.
Optionally, the steam inlet pipe road and the steam exhaust piping, which are arranged in parallel in, needs on the operation position using steam
Side.
Optionally, the steam inlet pipe road and the steam exhaust piping, which are arranged in parallel in, needs under the operation position using steam
Side.
Optionally, multiple described with being provided with the first valve on vapour interface.
Optionally, it is provided with the second valve on multiple back-steam interfaces.
Optionally, multiple described to be connected with gas utilization unit by hose with vapour interface.
Optionally, multiple back-steam interfaces are connected by hose with gas utilization unit.
The present invention achieves following technique effect compared with the existing technology：
Vapour system primary structure in the present invention include boiler, steam inlet pipe road, aerated water purification separator, steam exhaust piping and
Recovery tank, steam inlet pipe road include moist steam pipeline, and dry blowing vapor pipeline is arranged on moist steam pipeline；Boiler will be from recovery tank
Water is heated into moist steam, and by moist steam Pipeline transport to aerated water purification separator, aerated water purification separator removes in moist steam
Extra moisture makes moist steam become dry saturated steam, and dry saturated steam enters dry blowing vapor pipeline, and the heat of moist steam can heat dry blowing
Vapour makes dry saturated steam that higher temperature be kept to increase the utilization rate of steam to reduce the water droplet in dry saturated steam, improve boiler heat
Utilization rate reaches energy-saving and environment-friendly purpose.
Description of the drawings
It in order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only some implementations of the present invention
Example, for those of ordinary skill in the art, without having to pay creative labor, can also be according to these attached drawings
Obtain other attached drawings.
Fig. 1 is the structural schematic diagram of vapour system in the present invention；
Fig. 2 is the structural schematic diagram of recovery tank in vapour system of the present invention；
Fig. 3 is the overlooking structure diagram of recovery tank in vapour system of the present invention；
Fig. 4 is the coil arrangement schematic diagram of recovery tank in vapour system of the present invention；
Fig. 5 is the schematic cross-sectional view in steam inlet pipe road in vapour system of the present invention；
Fig. 6 is the structural schematic diagram of one embodiment of vapour system in the present invention；
Fig. 7 is the overlooking structure diagram of one embodiment of vapour system in the present invention；
Fig. 8 is the overlooking structure diagram of second embodiment of vapour system in the present invention.
Reference sign：1, recovery tank；1-1, water outlet；1-2, gas vent；1-3, removable cover；1-4, ball-cock assembly；
1-5, babinet；2, small pump；3, boiler；4, back-steam interface；5, the second valve；6, the first valve；7, with vapour interface；8, steam inlet pipe
Road；8-1, moist steam pipeline；8-2, dry blowing vapor pipeline；8-3, insulating layer；9, aerated water purification separator；10, operation position；11、
Steam exhaust piping；12, coil pipe；12-1, escape pipe；12-2, branch pipe；13, the second operation position.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Embodiment one：
As shown in Figure 1, the present embodiment provides a kind of vapour system, including boiler 3, steam inlet pipe road 8, aerated water purification separator
9, steam exhaust piping 11 and recovery tank 1；The steam inlet pipe road 8 is set between the boiler 3 and the aerated water purification separator 9,
The steam exhaust piping 11 is set between the discharge outlet of the aerated water purification separator 9 and the recovery tank 1, the recovery tank 1
It is provided with small pump 2 between the boiler 3, multiple vapour interface 7, the steam exhaust piping are provided on the steam inlet pipe road 8
Multiple back-steam interfaces 4 are provided on 11；The steam inlet pipe road 8 includes being covered on moist steam pipeline 8-1, the moist steam pipeline 8-1
Equipped with dry blowing vapor pipeline 8-2, described one end moist steam pipeline 8-1 is connected with the steam (vapor) outlet of the boiler 3, the moist steam
The other end of pipeline 8-1 is connected with the import of the aerated water purification separator 9, the dry blowing vapor pipeline 8-2 and the carbonated drink
The outlet of decontaminating separator 9 is connected.
In this specific embodiment, as shown in Figs. 1-5, to improve the utilization rate of the energy, the recovery tank 1 includes babinet 1-
Coil pipe 12 is provided in 5, the babinet 1-5,12 one end of the coil pipe is connected with the steam exhaust piping 11, the coil pipe 12
The other end is connected to one end of an escape pipe 12-1, and the other end of the escape pipe 12-1 is connected to inside the babinet 1-5, by returning
The steam that steam pipe road 11 flows back flows into coil pipe 12, escape pipe 12-1 is flowed to through coil pipe 12, in flow process, in coil pipe 12
Steam is by the water cooling in babinet 1-5, and the steam in coil pipe 12 is flowed by escape pipe 12-1 in babinet 1-5, in babinet 1-5
Water converge, be heated into steam can continue to be delivered to boiler 3 by small pump 2；It is provided with manhole at the top of the babinet 1-5；
Removable cover 1-3 is provided on the manhole, in order to periodically to carrying out repair and maintenance work in babinet 1-5；The babinet 1-5
Top is provided with gas vent 1-2, with the pressure in balance box 1-5, makes the pressure in babinet 1-5 close to external atmosphere pressure, makes
Steam in steam exhaust piping 11 can smoothly flow into babinet 1-5；The tops the babinet 1-5 are provided with ball-cock assembly 1-4, in babinet
In 1-5 after water level decreasing to predeterminated position, ball-cock assembly 1-4 is opened, and to carrying out moisturizing in babinet 1-5, makes the water level in babinet 1-5
It keeps within a preset range；The lower parts the babinet 1-5 are provided with water outlet 1-1；The water outlet 1-1 and the small pump 2
Water inlet is connected, and the water in babinet 1-5 is delivered to boiler 3 by small pump 2, steam is thermally formed by boiler 3；The disk
Axis direction on pipe 12 perpendicular to the coil pipe 12 is provided with multiple branch pipe 12-2；The multiple branch pipe 12-2 is set to described
The top and bottom of coil pipe 12, branch pipe 12-2 can increase residence time of the steam in coil pipe 12, so that steam in coil pipe 12
Pressure further declines, and increases the heat exchange between the moisture in the steam and babinet 1-5 in coil pipe 12, avoids the wave of heat
Take.
It is the multiple to be set on the dry blowing vapor pipeline 8-2 with vapour interface 7；It is the multiple to be set to institute with vapour interface 7
The top for stating dry blowing vapor pipeline 8-2 is connected with the air inlet of vapour iron by hose with vapour interface 7, is carried for vapour iron
For dry saturated steam；The water out of the aerated water purification separator 9 is connected by the back-steam pipeline with the recovery tank 1；It is described
It is arranged with insulating layer 8-3 on dry blowing vapor pipeline 8-2；The return tube road is arranged with insulating layer 8-3；The back-steam interface 4 is set
It is placed in the top of the back-steam pipeline, back-steam interface 4 is used to send the steam that the gas outlet of vapour iron returns back to back-steam pipeline.
It is multiple described with being provided with the first valve 6 on vapour interface 7.It is provided with the second valve on multiple back-steam interfaces 4
5.It is multiple described to be connected with gas utilization unit by hose with vapour interface 7.Multiple back-steam interfaces 4 are set by hose with vapour
It is standby to be connected.
In this specific embodiment, as shown in Figure 6 and Figure 7, when operation position is located at second floor, and Stall is the places such as storehouse
When, the steam inlet pipe road 8 and the steam exhaust piping 11 are arranged in parallel in 13 lower section of the second operation position, can either make the second operation
Station 13 does not see the steam inlet pipe road 8 and the steam exhaust piping 11, makes 13 local environment neat and tidy of the second operation position, also
It is avoided that the environment temperature in the second operation position 13 caused by the steam inlet pipe road 8 and the steam exhaust piping 11 distribute heat
It is excessively high, part refrigeration expense can be saved, and outflow of the steam in steam inlet pipe road 8 and the stream in steam exhaust piping 11 can be made
Enter more smooth, avoids the moisture in steam from accumulating, influence the normal use of vapour iron.
In another specific embodiment, as shown in figure 8, the steam inlet pipe road 8 and the steam exhaust piping 11 are arranged in parallel in
10 top of operation position using steam is needed, the arranged direction and station of the steam inlet pipe road 8 and the steam exhaust piping 11
Arranged direction is perpendicular, this arrangement can greatly reduce the total length in the steam inlet pipe road 8 and the steam exhaust piping 11,
Save construction cost.
In still another embodiment, the vapour system in the present embodiment is reversed steam-supplying system, i.e. recovery tank 1, benefit
Water pump 2 and boiler 3 are arranged in one end of production line, and aerated water purification separator 9 is arranged in the other end of production line, steam inlet pipe road 8
The direction that production line is parallel to steam exhaust piping 11 is arranged, in this specific embodiment, a vapour system is only a production
Line provides steam.
Specific case is applied in this specification, and principle and implementation of the present invention are described, above example
Explanation be merely used to help understand the present invention method and its core concept；Meanwhile for those of ordinary skill in the art,
According to the thought of the present invention, there will be changes in the specific implementation manner and application range.In conclusion in this specification
Appearance should not be construed as limiting the invention.
Claims (9)
1. a kind of vapour system, which is characterized in that including boiler, steam inlet pipe road, aerated water purification separator, steam exhaust piping and return water
Case；The steam inlet pipe road is set between the boiler and the aerated water purification separator, and the steam exhaust piping is set to described
Between the discharge outlet of aerated water purification separator and the recovery tank, it is provided with small pump between the recovery tank and the boiler,
It is provided with multiple vapour interfaces on the steam inlet pipe road, multiple back-steam interfaces are provided in the steam exhaust piping；The steam inlet pipe
Road includes moist steam pipeline, and dry blowing vapor pipeline, moist steam pipeline one end and the pot are arranged on the moist steam pipeline
The steam (vapor) outlet of stove is connected, and the other end of the moist steam pipeline is connected with the import of the aerated water purification separator, institute
Dry blowing vapor pipeline is stated with the outlet of the aerated water purification separator to be connected.
2. vapour system according to claim 1, which is characterized in that the recovery tank includes babinet, is set in the babinet
It is equipped with coil pipe, described coil pipe one end is connected with the steam exhaust piping, and the other end of the coil pipe is connected to one end of an escape pipe,
The other end of the escape pipe is connected to the box house；Optionally, the top of the box is provided with manhole；Optionally, described
Removable cover is provided on manhole；Optionally, the babinet top is provided with gas vent；Optionally, the babinet top setting
There is ball-cock assembly；Optionally, the lower box is provided with water outlet；Optionally, the water inlet of the water outlet and the small pump
Mouth is connected；Optionally, the axis direction on the coil pipe perpendicular to the coil pipe is provided with multiple branch pipes；Optionally, described
Multiple branch pipes are set to the top and bottom of the coil pipe.
3. vapour system according to claim 1, which is characterized in that the multiple to be set to the dry saturated steam with vapour interface
On pipeline；Optionally, the multiple top that the dry blowing vapor pipeline is set to vapour interface；Optionally, the carbonated drink purification
The water out of separator is connected by the back-steam pipeline with the recovery tank；Optionally, it is arranged on the dry blowing vapor pipeline
There is insulating layer；Optionally, the return tube road is arranged with insulating layer；Optionally, the back-steam interface is set to the back-steam
The top of pipeline.
4. vapour system according to claim 1, which is characterized in that the steam inlet pipe road is parallel with the steam exhaust piping to be set
It is placed in and needs above the operation position using steam.
5. vapour system according to claim 1, which is characterized in that the steam inlet pipe road is parallel with the steam exhaust piping to be set
It is placed in and needs below the operation position using steam.
6. vapour system according to claim 1, which is characterized in that multiple described with being provided with the first valve on vapour interface
Door.
7. vapour system according to claim 1, which is characterized in that be provided with the second valve on multiple back-steam interfaces
Door.
8. vapour system according to claim 1, which is characterized in that multiple described to be set with vapour by hose with vapour interface
It is standby to be connected.
9. vapour system according to claim 1, which is characterized in that multiple back-steam interfaces are set by hose with vapour
It is standby to be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810436528.1A CN108518670A (en) | 2018-05-09 | 2018-05-09 | A kind of vapour system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810436528.1A CN108518670A (en) | 2018-05-09 | 2018-05-09 | A kind of vapour system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108518670A true CN108518670A (en) | 2018-09-11 |
Family
ID=63430062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810436528.1A Pending CN108518670A (en) | 2018-05-09 | 2018-05-09 | A kind of vapour system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108518670A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2539904Y (en) * | 2002-04-27 | 2003-03-12 | 薛植深 | Hot water reverse-flow device for steam boiler |
| KR101287035B1 (en) * | 2013-05-07 | 2013-07-17 | 호용종합건설주식회사 | Boiler system of providing dry steam for renewed pipe |
| CN103590228A (en) * | 2013-11-07 | 2014-02-19 | 周文彪 | Steam energy saver |
| CN106835659A (en) * | 2017-03-24 | 2017-06-13 | 北京市帅风科技有限公司 | A kind of evaporated condensation water energy-saving steam pipe-line system |
| CN208546967U (en) * | 2018-05-09 | 2019-02-26 | 张月文 | A kind of vapour system |
-
2018
- 2018-05-09 CN CN201810436528.1A patent/CN108518670A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2539904Y (en) * | 2002-04-27 | 2003-03-12 | 薛植深 | Hot water reverse-flow device for steam boiler |
| KR101287035B1 (en) * | 2013-05-07 | 2013-07-17 | 호용종합건설주식회사 | Boiler system of providing dry steam for renewed pipe |
| CN103590228A (en) * | 2013-11-07 | 2014-02-19 | 周文彪 | Steam energy saver |
| CN106835659A (en) * | 2017-03-24 | 2017-06-13 | 北京市帅风科技有限公司 | A kind of evaporated condensation water energy-saving steam pipe-line system |
| CN208546967U (en) * | 2018-05-09 | 2019-02-26 | 张月文 | A kind of vapour system |
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