CN203904687U - Hot air drying room - Google Patents
Hot air drying room Download PDFInfo
- Publication number
- CN203904687U CN203904687U CN201420314625.0U CN201420314625U CN203904687U CN 203904687 U CN203904687 U CN 203904687U CN 201420314625 U CN201420314625 U CN 201420314625U CN 203904687 U CN203904687 U CN 203904687U
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- CN
- China
- Prior art keywords
- hot air
- moisture absorption
- desiccator
- absorption apparatus
- cylindricality
- 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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Abstract
The utility model relates to a wet sized yarn drying device, in particular to a hot air drying room. The hot air drying room comprises an outer shell, a sized yarn roller, air plates, a first electric heating device, a centrifugal fan, a second electric heating device, a moisture absorbing device and a hot air circulating pipeline. The sized yarn roller is arranged between the air plates in parallel, one side, facing the sized yarn roller, of each air plate is provided with an air port, and the air plates are communicated with an air outlet of the hot air circulating pipeline; the moisture absorbing device, the centrifugal fan and the electric heating devices are sequentially arranged in the hot air circulating pipeline, and the moisture absorbing device is arranged on an inlet of the hot air circulating pipeline. The drying room is good in effect of drying wet sized yarn.
Description
Technical field
The utility model relates to a kind of wet pulp yarn drying unit, is specifically related to a kind of hot air baking room.
Background technology
The sizing drying of weaving loom preparatory process adopts the drying mode of steam drying or oil heating.
Existing equipment, for cost-saving, reduction energy consumption, adopts the drying mode of electric heating circulating blowing more.
Drying process is exactly the excessive moisture of removing on wet pulp yarn, reaches the regain of technological requirement, solidifies the glutinous slurries that cover on sizing, makes it form bonding internal fiber, pastes the serous coat of volt surface hairiness.
The drying mode of existing electric heating circulating blowing, due to what adopt, be the mode of hot air circulation, although indoor temperature is higher than in the past, do not have a kind of effective moisture-catcher, humidity in drying room does not decline, and the result causing is that wet pulp yarn regain after drying room does not reach technological requirement.
Utility model content
The purpose of this utility model is to provide a kind of drying room that improves drying wet pulp yarn efficiency.
The utility model is achieved through the following technical solutions: hot air baking room, comprises shell, sizing cylinder, aerofoil, electric calorifie installation, centrifugal blower, electric calorifie installation, moisture absorption apparatus and hot air circulation pipeline; Sizing cylinder is arranged between parallel aerofoil, aerofoil is provided with air port towards sizing cylinder one side, aerofoil is tangent with the side of sizing cylinder towards sizing cylinder one side, aerofoil is communicated with the air outlet of hot air circulation pipeline, wherein, in hot air circulation pipeline, be provided with in turn moisture absorption apparatus, centrifugal blower and electric calorifie installation, moisture absorption apparatus is arranged on the porch of hot air circulation pipeline.
The beneficial effects of the utility model are: in prior art, in the drying room of majority, moisture absorption apparatus is not installed, or the position that moisture absorption apparatus is installed be not drying room inner air flow must be through part, it is high that the result causing is exactly the interior humidity of drying room, the poor effect of the drying of wet pulp yarn.Although heater is housed in prior art, the rear still steam of steam heating, does not have effect to the decline of humidity.In technical scheme in the application, be to install moisture absorption apparatus additional at the air inlet place of hot air circulation pipeline, air in drying room must pass through moisture absorption apparatus, air-flow is through primary dewatering, pass through again the heating of electric calorifie installation, the water vapour content of air reduces and temperature rising, stimulated the menstrual flow aerofoil, air port of air blows to the wet pulp yarn on sizing cylinder, fast by the oven dry of wet pulp yarn.This equipment can significantly be accelerated the dry efficiency of wet pulp yarn.
Further, the high both sides of the crown center of the inwall of shell are low, and the inwall bottom of shell is provided with water discharge outlet; Steam inwall meet after cold liquefaction along with water discharge outlet flows out hot air baking room, reduce airborne water vapour content.
Further, institute's moisture absorption apparatus is cylindricality desiccator, and spherical Kiselgel A is housed in cylindricality desiccator, and the both ends of the surface of cylindricality desiccator all offer passage; Spherical Kiselgel A has good moisture sorption effect, and cylindricality desiccator is removable, avoids the water suction of cylindricality desiccator full rear ineffective.
Further, moisture absorption apparatus is wheeling disk structure, in the middle of moisture absorption apparatus, be provided with wheel shaft, moisture absorption apparatus is hinged on shell by wheel shaft, on the end face of moisture absorption apparatus, prolong wheel shaft extension uniform one group of through hole, in through hole, be connected with cylindricality desiccator, the caliber of the diameter of cylindricality desiccator coupling hot air circulation pipeline, spherical Kiselgel A is housed in cylindricality desiccator, and the both ends of the surface of cylindricality desiccator are evenly equipped with passage; Use wheeling disk structure can switch fast cylindricality desiccator, avoid stopping whole drying work because changing moisture absorption apparatus, after the cylindricality desiccator that loads different moisture sorption effects, also can meet the different requirements of different process to air humidity simultaneously.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail:
Fig. 1 is the structural representation of the utility model structure hot air baking room embodiment;
Fig. 2 is the perspective view of moisture absorption apparatus in Fig. 1;
Reference numeral: shell 1, deflector roll 2, sizing cylinder 3, moisture absorption apparatus 4, wheel shaft 41, centrifugal blower 5, electric calorifie installation 6, hot air circulation pipeline 7, aerofoil 8, air port 81, water discharge outlet 9.
The specific embodiment
Hot air baking room shown in 1, comprises shell 1, sizing cylinder 3, aerofoil 8, electric calorifie installation, centrifugal blower 5, electric calorifie installation 6, moisture absorption apparatus 4, hot air circulation pipeline 7 by reference to the accompanying drawings; Sizing cylinder 3 has four, four sizing cylinders 3 are between two aerofoils 8, aerofoil 8 is provided with air port 81, aerofoil 8 is communicated with hot air circulation pipeline 7, wherein, in hot air circulation pipeline 7, in the direction of arrow as shown in Figure 1, being provided with in turn moisture absorption apparatus 4, centrifugal blower 5 and electric calorifie installation 6, is the interface of circulating line and aerofoil 8 after electric calorifie installation 6.
The interior wall construction of shell 1 is illustrated in figure 1 house shape, and the both sides lowest part of the inwall of shell 1 is equipped with water discharge outlet 9, steam inwall meet after cold liquefaction along with water discharge outlet 9 flows out hot air baking rooms.
During operation, deflector roll 2 is for guiding the direction of advance of wet pulp yarn, and wet pulp yarn enters from the porch of shell 1, and wet pulp yarn is wound on four sizing cylinders 3 successively, sizing cylinder 3 operation guiding wet pulp yarns are through each air port 81, and the hot blast blowing out by air port 81 is realized the object of drying wet pulp yarn; The inevitable a large amount of steam of generation in the process of oven dry wet pulp yarn, steam enters hot air circulation pipeline 7 under the effect of centrifugal blower 5, the air that contains large quantity of moisture is removed airborne moisture by moisture absorption apparatus 4, through centrifugal blower 5, accelerate, by electric calorifie installation 6, heat again, prolong hot air circulation pipeline 7 and be delivered to aerofoil 8.In this process, the air in drying room nearly all will pass through moisture absorption apparatus 4, and this has improved air dried efficiency.Final high temperature, dry air have accelerated to dry the efficiency of wet pulp yarn.
Moisture absorption apparatus 4 wheeling disk structure as shown in Figure 2, centre is wheel shaft 41, moisture absorption apparatus 4 is hinged on shell 1 by wheel shaft 41, wheel shaft 41 is uniform four through holes around, can clamping cylindricality desiccator in through hole, spherical Kiselgel A is housed in cylindricality desiccator, the both ends of the surface of cylindricality desiccator are evenly equipped with passage, use wheeling disk structure can change fast desiccator, conveniently can the new desiccator of quick-replaceable after water suction is full at desiccator.
Above-described is only preferred embodiment of the present utility model; should be understood that; for a person skilled in the art; do not departing under the prerequisite of the utility model structure; can also make some distortion and improvement; these also should be considered as protection domain of the present utility model, and these can not affect effect and practical applicability that the utility model is implemented.
Claims (4)
1. hot air baking room, comprises shell (1), sizing cylinder (3), aerofoil (8), electric calorifie installation (6), centrifugal blower (5), electric calorifie installation (6), moisture absorption apparatus (4) and hot air circulation pipeline (7); Described sizing cylinder (3) is arranged between parallel aerofoil (8), described aerofoil (8) is provided with air port (81) towards sizing cylinder (3) one sides, described aerofoil (8) is tangent with the side of sizing cylinder (3) towards sizing cylinder (3) one side, described aerofoil (8) is communicated with the air outlet of hot air circulation pipeline (7), it is characterized in that, in described hot air circulation pipeline (7), be provided with in turn moisture absorption apparatus (4), centrifugal blower (5) and electric calorifie installation (6), described moisture absorption apparatus (4) is arranged on the porch of hot air circulation pipeline (7).
2. hot air baking room as claimed in claim 1, is characterized in that, the high both sides of crown center of the inwall of described shell (1) are low, and the inwall bottom of shell (1) is provided with water discharge outlet (9).
3. hot air baking room as claimed in claim 1, is characterized in that, institute's moisture absorption apparatus (4) is cylindricality desiccator, in described cylindricality desiccator, spherical Kiselgel A is housed, and the both ends of the surface of cylindricality desiccator all offer passage.
4. hot air baking room as claimed in claim 1, it is characterized in that, described moisture absorption apparatus (4) is wheeling disk structure, in the middle of described moisture absorption apparatus (4), be provided with wheel shaft (41), described moisture absorption apparatus (4) is hinged on shell (1) by wheel shaft (41), on the end face of described moisture absorption apparatus (4), prolong wheel shaft (41) extension uniform one group of through hole, in through hole, be connected with cylindricality desiccator, the caliber of the diameter coupling hot air circulation pipeline (7) of described cylindricality desiccator, spherical Kiselgel A is housed in cylindricality desiccator, and the both ends of the surface of cylindricality desiccator are evenly equipped with passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420314625.0U CN203904687U (en) | 2014-06-13 | 2014-06-13 | Hot air drying room |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420314625.0U CN203904687U (en) | 2014-06-13 | 2014-06-13 | Hot air drying room |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203904687U true CN203904687U (en) | 2014-10-29 |
Family
ID=51778978
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420314625.0U Expired - Fee Related CN203904687U (en) | 2014-06-13 | 2014-06-13 | Hot air drying room |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203904687U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104005195A (en) * | 2014-06-13 | 2014-08-27 | 潼南县炫吉中绸有限公司 | Hot-air drying room |
-
2014
- 2014-06-13 CN CN201420314625.0U patent/CN203904687U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104005195A (en) * | 2014-06-13 | 2014-08-27 | 潼南县炫吉中绸有限公司 | Hot-air drying room |
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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: 20141029 Termination date: 20150613 |
|
| EXPY | Termination of patent right or utility model |