CN203451847U - Steam heating device of fiber feeding groove in viscose staple fiber post-treatment - Google Patents
Steam heating device of fiber feeding groove in viscose staple fiber post-treatment Download PDFInfo
- Publication number
- CN203451847U CN203451847U CN201320531736.2U CN201320531736U CN203451847U CN 203451847 U CN203451847 U CN 203451847U CN 201320531736 U CN201320531736 U CN 201320531736U CN 203451847 U CN203451847 U CN 203451847U
- Authority
- CN
- China
- Prior art keywords
- steam
- fine groove
- give
- viscose staple
- aperture
- 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.)
- Expired - Fee Related
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 63
- 229920000297 Rayon Polymers 0.000 title claims abstract description 38
- 238000010438 heat treatment Methods 0.000 title abstract 2
- 210000005056 cell body Anatomy 0.000 claims abstract description 22
- 238000012805 post-processing Methods 0.000 claims description 26
- 238000007664 blowing Methods 0.000 claims description 10
- 238000005265 energy consumption Methods 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000007921 spray Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 11
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 6
- 238000009826 distribution Methods 0.000 description 4
- 239000003292 glue Substances 0.000 description 4
- 238000005520 cutting process Methods 0.000 description 3
- 239000002964 rayon Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Nonwoven Fabrics (AREA)
- Treatment Of Fiber Materials (AREA)
Abstract
The utility model relates to a viscose staple fiber machinery technical field, concretely relates to give the steam heating device in fine groove among the viscose staple fiber aftertreatment, give 12 steam spray tubes that have a aperture of fine groove cell body bottom align to grid, be applicable to wide, high yield give fine groove, when satisfying 10 ten thousand tons of viscose production line demands of annual output, with energy consumption control at the minimum, increase of production effectively, reduce the energy consumption, practice thrift the cost.
Description
Technical field
The utility model relates to viscose staple fibre field of mechanical technique, is specifically related in a kind of viscose staple fibre post processing the steam heater to fine groove.
Background technology
Belong to viscose staple fibre post processing equipment to fine groove, for the viscose staple fibre that cutting machine is cut off, through distribution plate, divide and be paved into uniform fibrage, flow to fourdrinier wire scouring machine.Under the effect of steam, the carbon disulfide evaporation in fiber, and reach the object that makes fiber opening.Give the quality of fine groove paving capillary effect fruit, directly affect later process washing, mesohigh padding machine dries the effect of fiber, and then affects the consumption of drying plant steam.
During equipment operation, the viscose staple fibre cutting off from cutting machine is under the drive of current, on defeated hollow billet road enters to fine fibre distributor, by Motor Drive crank and rocker mechanism, drive distributor reciprocally swinging, fiber is spread out equably in groove, the steam that is laid on the steam jet ejection of cell body bottom remains in carbon disulfide in fiber by fiber opening discharge, is conducive to completing of follow-up desulfurization, bleaching, washing and the operation that oils.
201220643434.X, the utility model patent that denomination of invention is " be applicable to short rayon fiber post processing equipment give fine slot device ", a kind of fine slot device of giving that is applicable to short rayon fiber post processing equipment is disclosed, this device comprises rack-mounted cell body successively, steam heater, be arranged on the steam discharge cover of steam heater top, be arranged on the fiber distribution groove being connected with charging aperture in cell body inner chamber, be arranged on frame below for driving the transmission device of fiber distribution groove, at cell body top, away from steam heater one side, be provided with fiber collector groove, the charging aperture of fiber collector groove is arranged on upper lateral part, discharging opening is connected with the feed end of fiber distribution groove, at the cell body intracavity bottom being positioned at below fiber collector groove present position, be provided with over flow rinse groove, and the frid indention structure of overflow launder, on the inclined-plane, cell body bottom between over flow rinse groove and steam heater, be provided with buffer board, and buffer board is two arcs.The steam heater of giving fine groove of this patent is not suitable for the production of wide cut high yield, cannot meet the demand of producing 100000 tons of viscose glue production lines per year.
Utility model content
In order to solve the demand of 100,000 tons of viscose glue production lines, the utility model provides in a kind of short rayon fiber post processing the steam heater to fine groove.Steam heater is for arranging and be with foraminate steam jet to the cell body bottom even of fine groove, when meeting and producing 100000 tons of viscose glue production line demands per year, energy consumption is controlled at minimum, effectively improves output, reduces energy consumption, cost-saving.
For achieving the above object, the utility model adopts following technical scheme:
In viscose staple fibre post processing, give the steam heater of fine groove, it is characterized in that: to the cell body bottom even of fine groove, arrange 12 and be with foraminate steam jet.
Perforate on described steam jet and level are 30 ~ 60 degree straight angles.
The spacing of described steam jet is 200mm, can well make fibrage swim on the water surface.
On described steam jet, the pitch of holes of aperture is 50 ~ 55mm, and pitch of holes is excessive, and fiber opening is inhomogeneous; Pitch of holes is too small, need to increase quantity of steam, increases energy consumption.The pitch of holes of 50 ~ 55mm can make uperize cover fibrage bottom completely, makes the complete shredding of fiber, reaches optimum efficiency.
The internal diameter of described steam jet is 50mm, when guaranteeing fiber opening effect, has reduced again energy resource consumption.
Adjacent aperture on described different steam jets is cross arrangement, is conducive to shorten pitch-row, makes fiber obtain abundant shredding.
The pitch of holes of the adjacent aperture on described different steam jets is 25mm, more fully fiber is charged and attacked to shredding.
The aperture of described aperture is Φ 1 ~ 3mm, and aperture is crossed conference and increased steam consumption, and affects fibrage laying effect; The too small meeting in aperture affect steam and charge and attack fibrage ability, thereby cause fiber to kink, reduces shredding effect.
The beneficial effects of the utility model are:
1, the cell body bottom even of giving fine groove of the present utility model is arranged 12 and is with foraminate steam jet, when meeting and producing 100000 tons of viscose glue production line demands per year, energy consumption is controlled at minimum, effectively improves output, reduces energy consumption, cost-saving.
2, be of the present utility modelly 30 ~ 60 with level to perforate on fine groove steam jet to spend the straight angles, played the effect that changes fibrage flow velocity, guiding fiber flow direction and opening fiber, thereby make fiber lay down blanket more even, be conducive to completing of follow-up desulfurization, bleaching, washing and the operation that oils.
3, on the utility model steam jet, the pitch of holes of aperture is 50 ~ 55mm, and pitch of holes is excessive, and fiber opening is inhomogeneous; Pitch of holes is too small, need to increase quantity of steam, increases energy consumption.The pitch of holes of 50 ~ 55mm can make uperize cover fibrage bottom completely, makes the complete shredding of fiber, reaches optimum efficiency.
4, the adjacent aperture on the different steam jets of the utility model is cross arrangement, is conducive to shorten pitch-row, makes fiber obtain abundant shredding, has further guaranteed the shredding effect of fiber.
5, the aperture of the utility model aperture is Φ 1 ~ 3mm, and aperture is crossed conference and increased steam consumption, and affects fibrage laying effect; The too small meeting in aperture affect steam and charge and attack fibrage ability, thereby cause fiber to kink, reduces shredding effect.Energy consumption, when guaranteeing opening fiber, has been saved again in 1 ~ 3mm aperture, has strengthened the energy-saving effect of device.
Accompanying drawing explanation
Fig. 1 is the structural representation of giving fine groove steam heater in the post processing of the utility model viscose staple fibre.
Fig. 2 is the fine groove structural representation of giving of viscose staple fibre aftertreatment technology of the present utility model.
In figure, be labeled as: 1, main steam header, 2, steam jet, 3, frame, 4, cell body, 5, feed hopper, 6, fibre distributor, 7, transmission device, 8, buffer board, 9, steam heater, 10, steam discharge cover, 11, transport, 12, gas block panel.
The specific embodiment
Below in conjunction with the specific embodiment, essentiality content of the present utility model is described in further detail.
Embodiment 1
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
Equipment total installed capacity power of the present utility model is reduced to 4509KW from 5253Kw, has fallen 744KW.Explanation thus, the utility model can not only be applicable to 100,000 tons of production lines, can also effectively reduce costs, and saves energy consumption.
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 30 degree angles.
Embodiment 3
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 60 degree angles.
The spacing of described steam jet 2 is 200mm.
Embodiment 4
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 45 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 50mm.
Embodiment 5
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 50 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 55mm.
The internal diameter of described steam jet 2 is 50mm.
Embodiment 6
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 40 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 53mm.
The internal diameter of described steam jet 2 is 50mm.
Adjacent aperture on described different steam jets 2 is cross arrangement.
Embodiment 7
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 35 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 51mm.
The internal diameter of described steam jet 2 is 50mm.
Adjacent aperture on described different steam jets 2 is cross arrangement.
The pitch of holes of the adjacent aperture on described different steam jets 2 is 25mm.
Embodiment 8
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 43 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 54mm.
The internal diameter of described steam jet 2 is 50mm.
Adjacent aperture on described different steam jets 2 is cross arrangement.
The pitch of holes of the adjacent aperture on described different steam jets 2 is 25mm.
The aperture of described aperture is Φ 1mm.
Embodiment 9
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 43 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 54mm.
The internal diameter of described steam jet 2 is 50mm.
Adjacent aperture on described different steam jets 2 is cross arrangement.
The pitch of holes of the adjacent aperture on described different steam jets 2 is 25mm.
The aperture of described aperture is Φ 2mm.
In viscose staple fibre post processing, give the steam heater of fine groove, arrange 12 to fine groove cell body 4 bottom evens and be with foraminate steam jet 2.
The blowing angle of steam jet 2 and level are 43 degree angles.
The spacing of described steam jet 2 is 200mm.
On described steam jet 2, the pitch of holes of aperture is 54mm.
The internal diameter of described steam jet 2 is 50mm.
Adjacent aperture on described different steam jets 2 is cross arrangement.
The pitch of holes of the adjacent aperture on described different steam jets 2 is 25mm.
The aperture of described aperture is Φ 3mm.
Claims (8)
1. in viscose staple fibre post processing, give the steam heater of fine groove, it is characterized in that: to cell body (4) bottom even of fine groove, arrange 12 and be with foraminate steam jet (2).
2. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the blowing angle of described steam jet (2) and level are 30 ~ 60 degree angles.
3. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the spacing of described steam jet (2) is 200mm.
4. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the pitch of holes of the upper aperture of described steam jet (2) is 50 ~ 55mm.
5. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the internal diameter of described steam jet (2) is 50mm.
6. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the adjacent aperture on described different steam jets (2) is cross arrangement.
7. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the pitch of holes of the adjacent aperture on described different steam jets (2) is 25mm.
8. in viscose staple fibre post processing according to claim 1, give the steam heater of fine groove, it is characterized in that: the aperture of described aperture is Φ 1 ~ 3mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320531736.2U CN203451847U (en) | 2013-08-29 | 2013-08-29 | Steam heating device of fiber feeding groove in viscose staple fiber post-treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320531736.2U CN203451847U (en) | 2013-08-29 | 2013-08-29 | Steam heating device of fiber feeding groove in viscose staple fiber post-treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203451847U true CN203451847U (en) | 2014-02-26 |
Family
ID=50131740
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320531736.2U Expired - Fee Related CN203451847U (en) | 2013-08-29 | 2013-08-29 | Steam heating device of fiber feeding groove in viscose staple fiber post-treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203451847U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103993450A (en) * | 2014-05-26 | 2014-08-20 | 江苏双盈纺织科技有限公司 | Dyeing jar heating device |
-
2013
- 2013-08-29 CN CN201320531736.2U patent/CN203451847U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103993450A (en) * | 2014-05-26 | 2014-08-20 | 江苏双盈纺织科技有限公司 | Dyeing jar heating device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203391130U (en) | Silicon chip cutting device | |
| CN103453785B (en) | Runoff type electrostatic water collection device and there is the cooling tower of runoff type electrostatic water collection device | |
| CN203007636U (en) | Poly-p-phenylene benzobisthiazole (PBO) stepping washing device | |
| CN206542802U (en) | Cellular-type feeding trough is used in the cultivation of one boar | |
| CN203451847U (en) | Steam heating device of fiber feeding groove in viscose staple fiber post-treatment | |
| CN2763003Y (en) | Cooling and transferring equipment for injection products | |
| CN203772056U (en) | Runoff type static water collecting device and cooling tower provided with same | |
| CN203514027U (en) | Fiber feeding groove for viscose staple fiber post-treatment process | |
| CN201447627U (en) | High-concentration hydraulic pulper | |
| CN208548197U (en) | Cooling and drying device is used in a kind of production of cable | |
| CN102660785A (en) | Bubble electrostatic spinning device | |
| CN103437088B (en) | Wool paving process in viscose staple fiber post-treatment | |
| CN207362452U (en) | A kind of non-woven fabrics spun-laced machine | |
| CN216445511U (en) | Curved surface electrostatic spinning device | |
| CN201862280U (en) | Distributor for plate type falling film evaporator | |
| CN202989539U (en) | Fiber supply groove device applied for viscose staple fiber post treatment equipment | |
| CN106139858B (en) | A kind of High-efficiency carbon-absorbing tower | |
| CN202666978U (en) | Pulp plug guide rod locating structure in ore distribution box | |
| CN114214738A (en) | Curved surface electrostatic spinning device | |
| CN209743163U (en) | Special rotary vane vacuum pump for producing cellosilk | |
| CN102359004B (en) | Square extending type cloth conveying tube | |
| CN207698684U (en) | A kind of row is to machine separating screen device | |
| CN207031386U (en) | A kind of oil expression disintegrating machine | |
| CN2905855Y (en) | Steam spraying tube type floss forming groove | |
| CN212270524U (en) | Pulp distributor for head box |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140226 Termination date: 20160829 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |