CN108613016A - A kind of U-shaped pipe vapour system - Google Patents
A kind of U-shaped pipe vapour system Download PDFInfo
- Publication number
- CN108613016A CN108613016A CN201810436090.7A CN201810436090A CN108613016A CN 108613016 A CN108613016 A CN 108613016A CN 201810436090 A CN201810436090 A CN 201810436090A CN 108613016 A CN108613016 A CN 108613016A
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- CN
- China
- Prior art keywords
- steam
- pipeline
- optionally
- pipe
- vapour
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000000746 purification Methods 0.000 claims abstract description 27
- 238000011084 recovery Methods 0.000 claims abstract description 26
- 238000007664 blowing Methods 0.000 claims abstract description 21
- 230000008676 import Effects 0.000 claims description 3
- 238000001727 in vivo Methods 0.000 claims 1
- 229920006395 saturated elastomer Polymers 0.000 abstract description 10
- 238000005516 engineering process Methods 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 235000014171 carbonated beverage Nutrition 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D49/00—Separating dispersed particles from gases, air or vapours by other methods
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices For Medical Bathing And Washing (AREA)
Abstract
The present invention discloses a kind of U-shaped pipe vapour system, it is related to Garment Technology field, 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 U-shaped pipe 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 U-shaped pipe vapour system, can improve the utilization of steam
Rate reduces the production cost of clothes production enterprise.
To achieve the above object, the present invention provides following schemes：
The present invention provides a kind of U-shaped pipe vapour system, including boiler, steam inlet pipe road, aerated water purification separator, return tube
Road and recovery tank；The steam inlet pipe road is set between the boiler and the aerated water purification separator, and the steam exhaust piping is set
It is placed between the discharge outlet of the aerated water purification separator and the recovery tank, is provided between the recovery tank and the boiler
Small pump, be provided on the steam inlet pipe road it is multiple use vapour interfaces, be provided with multiple back-steam interfaces in the steam exhaust piping；It is described
Steam inlet pipe road includes moist steam pipeline, is arranged with dry blowing vapor pipeline on the moist steam pipeline, moist steam pipeline one end with
The steam (vapor) outlet of the boiler is connected, and the other end of the moist steam pipeline is connected with the import of the aerated water purification separator
Logical, the dry blowing vapor pipeline is connected with the outlet of the aerated water purification separator；
The boiler and the recovery tank are set to the side of operation position, and the aerated water purification separator is set to described
The other side of operation position, the steam inlet pipe road and the steam exhaust piping are set to above or below the operation position.
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.
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 U-shaped pipe vapour system, including boiler 3, steam inlet pipe road 8, carbonated drink are net
Separator 9, steam exhaust piping 11 and recovery tank 1；The steam inlet pipe road 8 is set to the boiler 3 and the carbonated drink purification separation
Between device 9, the steam exhaust piping 11 is set between the discharge outlet of the aerated water purification separator 9 and the recovery tank 1, described
It is provided with small pump 2 between recovery tank 1 and the boiler 3, is provided with multiple vapour interfaces 7 on the steam inlet pipe road 8, described time
Multiple back-steam interfaces 4 are provided on steam pipe road 11；The steam inlet pipe road 8 includes moist steam pipeline 8-1, the moist steam pipeline 8-
Dry blowing vapor pipeline 8-2 is arranged on 1, described one end moist steam pipeline 8-1 is connected with the steam (vapor) outlet of the boiler 3, described
The other end of moist steam pipeline 8-1 is connected with the import of the aerated water purification separator 9, the dry blowing vapor pipeline 8-2 and institute
The outlet for stating aerated water purification separator 9 is connected；
The boiler 3 and the recovery tank 1 are set to the side of operation position 10, and the aerated water purification separator 9 is arranged
The other side in the operation position 10, the steam inlet pipe road 8 and the steam exhaust piping 11 are set to the top of operation position 10,
The steam inlet pipe road 8 and 11 top of the steam exhaust piping are provided with the second operation position 13.
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.
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 U-shaped pipe vapour system, which is characterized in that including boiler, steam inlet pipe road, aerated water purification separator, return tube
Road and recovery tank；The steam inlet pipe road is set between the boiler and the aerated water purification separator, and the steam exhaust piping is set
It is placed between the discharge outlet of the aerated water purification separator and the recovery tank, is provided between the recovery tank and the boiler
Small pump, be provided on the steam inlet pipe road it is multiple use vapour interfaces, be provided with multiple back-steam interfaces in the steam exhaust piping；It is described
Steam inlet pipe road includes moist steam pipeline, is arranged with dry blowing vapor pipeline on the moist steam pipeline, moist steam pipeline one end with
The steam (vapor) outlet of the boiler is connected, and the other end of the moist steam pipeline is connected with the import of the aerated water purification separator
Logical, the dry blowing vapor pipeline is connected with the outlet of the aerated water purification separator；
The boiler and the recovery tank are set to the side of operation position, and the aerated water purification separator is set to the operation
The other side of station, the steam inlet pipe road and the steam exhaust piping are set to above or below the operation position.
2. U-shaped pipe vapour system according to claim 1, which is characterized in that the recovery tank includes babinet, the case
It is provided with coil pipe in vivo, described coil pipe one end is connected with the steam exhaust piping, and the other end of the coil pipe is connected to an escape pipe
One end, the other end of the escape pipe is connected to the box house；Optionally, the top of the box is provided with manhole；It is optional
, it is provided with removable cover on the manhole；Optionally, the babinet top is provided with gas vent；Optionally, on the babinet
Portion is provided with ball-cock assembly；Optionally, the lower box is provided with water outlet；Optionally, the water outlet and the small pump
Water inlet be connected；Optionally, the axis direction on the coil pipe perpendicular to the coil pipe is provided with multiple branch pipes；It is optional
, the multiple branch pipe is set to the top and bottom of the coil pipe.
3. U-shaped pipe vapour system according to claim 1, which is characterized in that the multiple to be set to institute with vapour interface
It states on dry blowing vapor pipeline；Optionally, the multiple top that the dry blowing vapor pipeline is set to vapour interface；Optionally, described
The water out of aerated water purification separator is connected by the back-steam pipeline with the recovery tank；Optionally, the dry blowing steam pipe
Road is arranged with insulating layer；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.
4. U-shaped pipe vapour system according to claim 1, which is characterized in that the steam inlet pipe road and the return tube
Road, which is arranged in parallel in, to be needed above the operation position using steam.
5. U-shaped pipe vapour system according to claim 1, which is characterized in that the steam inlet pipe road and the return tube
Road, which is arranged in parallel in, to be needed below the operation position using steam.
6. U-shaped pipe vapour system according to claim 1, which is characterized in that multiple described to be provided with on vapour interface
First valve.
7. U-shaped pipe vapour system according to claim 1, which is characterized in that be provided on multiple back-steam interfaces
Second valve.
8. U-shaped pipe vapour system according to claim 1, which is characterized in that multiple described to pass through hose with vapour interface
It is connected with gas utilization unit.
9. U-shaped pipe vapour system according to claim 1, which is characterized in that multiple back-steam interfaces pass through hose
It is connected with gas utilization unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810436090.7A CN108613016A (en) | 2018-05-09 | 2018-05-09 | A kind of U-shaped pipe vapour system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810436090.7A CN108613016A (en) | 2018-05-09 | 2018-05-09 | A kind of U-shaped pipe vapour system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108613016A true CN108613016A (en) | 2018-10-02 |
Family
ID=63662472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810436090.7A Pending CN108613016A (en) | 2018-05-09 | 2018-05-09 | A kind of U-shaped pipe vapour system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108613016A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109595404A (en) * | 2019-01-25 | 2019-04-09 | 张月文 | A kind of three-in-one pipeline for vapour system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011145040A (en) * | 2010-01-18 | 2011-07-28 | Miura Co Ltd | Steam boiler device and operation method therefor |
| CN202220307U (en) * | 2011-07-16 | 2012-05-16 | 天津市大港巨龙造纸厂 | Adjustable heat pump air feed system |
| CN203215660U (en) * | 2013-05-03 | 2013-09-25 | 青岛亿通达新能源有限公司 | Steam heat energy closed cycling device |
| 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 |
| CN108006437A (en) * | 2017-10-31 | 2018-05-08 | 河南中烟工业有限责任公司 | A kind of system for improving steam quality |
-
2018
- 2018-05-09 CN CN201810436090.7A patent/CN108613016A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011145040A (en) * | 2010-01-18 | 2011-07-28 | Miura Co Ltd | Steam boiler device and operation method therefor |
| CN202220307U (en) * | 2011-07-16 | 2012-05-16 | 天津市大港巨龙造纸厂 | Adjustable heat pump air feed system |
| CN203215660U (en) * | 2013-05-03 | 2013-09-25 | 青岛亿通达新能源有限公司 | Steam heat energy closed cycling device |
| 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 |
| CN108006437A (en) * | 2017-10-31 | 2018-05-08 | 河南中烟工业有限责任公司 | A kind of system for improving steam quality |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109595404A (en) * | 2019-01-25 | 2019-04-09 | 张月文 | A kind of three-in-one pipeline for vapour system |
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Application publication date: 20181002 |