CN202136844U - Multistage-separation continuous rosin dreg removal device - Google Patents
Multistage-separation continuous rosin dreg removal device Download PDFInfo
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- CN202136844U CN202136844U CN201120237874U CN201120237874U CN202136844U CN 202136844 U CN202136844 U CN 202136844U CN 201120237874 U CN201120237874 U CN 201120237874U CN 201120237874 U CN201120237874 U CN 201120237874U CN 202136844 U CN202136844 U CN 202136844U
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- rosin
- separation
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- filter plate
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Abstract
The utility model discloses a multistage-separation continuous rosin dreg removal device, which consists of a spiral conveying blade (4), a U-shaped body (3), filter plates (8, 9), separation plates (6, 10), a feeding hole (12), a discharging hole (11) and a dreg discharging hole (7). The multistage-separation continuous rosin dreg removal device is characterized in that a certain angle is formed between the U-shaped body (3) and the horizontal plane; the feeding hole (12) is lower than the dreg discharging hole (7); the separation plates (6, 10) consist of a first-stage separation plate (10) and a second-stage separation plate (6) and are covered by dense iron wire filter screens; and a first-stage filter plate (8) and a second-stage filter plate (9) are arranged inside the U-shaped body (3) at the periphery of the spiral conveying blade (4). The advantages of the multistage-separation continuous rosin dreg removal device are that: fine impurities can be separated; a range of application is wide; and the multistage-separation continuous rosin dreg removal device can be used for removing dregs in a rosin solution produced by high-efficiency continuous rosin.
Description
Technical field
The utility model relates to the continuous rosin deslagging device of rosin liquid multi-stage separation that forest chemical rosin is produced.
Background technology
With rosin is the rosin processing that raw material carries out, and technological process is long, the operation that needs rosin dissolving, rosin slagging-off, turpentine oil separated form water, rosin to distill the hot packing of rosin.Because climbing up and up of domestic human cost causes the purchasing price with rosin at the rosin upper reaches significantly to improve accordingly, illegal rosin dealer merchant is in order to improve bigger profit; The interpolation fine impurities as much as possible in the rosin the inside; Improve the weight of rosin, contain a large amount of impurity in the rosin, brought adverse effect to rosin slagging-off operation; Influence carrying out continuously of rosin processing, increased the weight of working strength of workers.
In order to improve rosin slagging-off efficient; Like patent CN201848163U a kind of high-efficiency and continuous rosin scummer is provided; A kind of spiral conveying blade, U-shaped body, filter plate, separating plate have been adopted; Reach the purpose of rosin liquid slagging-off through the running of drive of motor high-efficiency and continuous rosin scummer, but also have following defective simultaneously: sneak into natural impuritys such as bark wooden unit in the rosin that (1) can only separate, the fine impurities of adding for rosin dealer merchant is difficult to separate; (2) when the rosin liquid inlet flow rate is bigger, rosin liquid has little time to separate and is promptly taken to slag-drip opening by spiral conveying blade, thereby has caused the loss of rosin liquid.Because above defective, a kind of high-efficiency and continuous rosin scummer that patent CN201848163U provides can only use and contain natural bark impurity, and under the less situation of rosin liquid flow-rate ratio; The big situation of more fine impurities and rosin liquid flow-rate ratio is of non-ideal use for containing.
In order to address the above problem; The continuous rosin deslagging device of the multi-stage separation that the utility model provides adopts multistage filter plate to carry out the separation of rosin liquid; Thereby can effectively solve above defective, realize separating the big still purpose of high efficiency separation of fine impurities, rosin liquid flow-rate ratio.
Summary of the invention
The continuous rosin deslagging device of the utility model multi-stage separation to solve and contain the rosin slagging-off that the big situation high-efficiency and continuous rosin of more fine impurities and rosin liquid flow-rate ratio is produced.
The utility model solves the problems of the technologies described above and adopts multistage filter plate, is characterized in: be made up of spiral conveying blade, U-shaped body, filter plate, separating plate, charging aperture, discharging opening, slag-drip opening, it is characterized in that U-shaped body and level are certain angle; And the charging aperture height is below slag-drip opening; Separating plate is made up of 1 grade of separating plate and 2 grades of separating plates, and every grade of separating plate is formed by fine and close iron wire filter screen parcel, and rosin liquid separates impurity and fat liquid major part through 1,2 grade of separation on this separating plate; Impurity is under the drive of helical feed leaf simultaneously; Carry to slag-drip opening from the bottom up, in the peripheral U-shaped body inboard of spiral conveying blade 1 grade of filter plate, 2 grades of filter plates are set, the pore size of 1 grade of filter board hole is 4~6mm; The rosin liquid of separating gets into 2 grades of filter plates through 1 grade of filter plate; The big impurity of separating is in up slag-drip opening conveying of spiral conveying blade, and the rosin liquid of being carried secretly by impurity on a small quantity thoroughly separates through 1 grade of filter plate under the gravity effect once more, and impurity is discharged by slag-drip opening; The rosin liquid of initial gross separation further separates through 2 grades of filter plates, and the rosin liquid of 2 grades of separation send subsequent processing by discharging opening.
The utility model is compared with patent CN201848163U, on the basis of filter plate, has increased to change 2 grades of filter plates, and U-shaped body and level can be regulated the angle that is certain, has structurally improved rosin liquid slagging-off efficient greatly.U-shaped body and level are 10 °~20 ° angles; Can regulate according to demand of practical production; The charging aperture height is below slag-drip opening; Utilize the gravity effect of liquid, the slag-drip opening above having avoided when the rosin liquid flow-rate ratio is big being scraped by spiral conveying blade has improved the slagging-off ability of rosin liquid.Described 2 grades of filter plates are positioned at the outside of 1 grade of filter plate, in the middle of U-shaped body bottom and 1 grade of filter plate; Fix at U-shaped body two ends, open U-shaped body feed end after use a period of time and change, its pore size is 1~2mm; 1 grade of filter plate and the bigger impurity such as bark wooden unit of the main separated volume of separating plate; 2 grades of filter plates then on the basis that 1 grade of filter plate separates, the further smaller impurity of separating particles, thus can reach the purpose of thorough removing impurities.
The utility model is easy to use, can adapt to existing rosin liquid impurity more and separate, and the scope of application is extensive, under different occasions, can realize the rosin liquid slagging-off that high-efficiency and continuous rosin is produced.
Description of drawings
Below in conjunction with accompanying drawing the continuous rosin deslagging device of the utility model multi-stage separation is described.
Fig. 1: patent CN201848163U high-efficiency and continuous rosin scummer.
Fig. 2: the continuous rosin deslagging device of multi-stage separation.
Fig. 3: the continuous rosin deslagging device of multi-stage separation A-A figure.
Wherein, Fig. 1,1 ' belt pulley, 2 ' bearing block, 3 ' U-shaped body, 4 ' ' 2 grades of separating plate, 7 '-slag-drip openings, 8 of spiral conveying blade, 5 '-helical axis, 6 ' filter plate, 9 '-1 grade separating plate, 10 ' discharging openings, 11 '-charging aperture.
Fig. 2,1-belt pulley, 2-bearing block, 3-U body, 4-spiral conveying blade, 5-helical axis, 6-2 level separating plate, 7-slag-drip opening, 8-1 level filter plate, 9-2 level filter plate, 10-1 level separating plate, 11-discharging opening, 12-charging aperture.
The specific embodiment
When the continuous rosin deslagging device of multi-stage separation moves, regulate U-shaped body and level angle according to demand of practical production, angle is controlled between 10 °~20 °; Change 2 grades of clean filter plates, start rosin scummer electric motor starting switch, the entry into service of rosin deslagging device; Open the charging valve; Rosin fat liquid gets into the scummer device by charging aperture, through impurity such as bark wooden units in the scummer spiral conveying blade rotation removing fat liquid, carries rosin separating plate high efficiency separation on the overwinding conveying blade secretly in the impurity such as bark wooden unit; Fat liquid separates through 1 grade of filter plate and 2 grades of filter plates, send subsequent processing by discharging opening.The impurity of 1 grade of filter plate separation is discharged by slag-drip opening, and the impurity of 2 grades of separation is then through regularly replacing the purpose that 2 grades of filter plates reach removal of contamination.
Used 2 grades of filter plates can continue to use through after cleaning, drying.
General, its angle of U-shaped body and level angle is arranged on 15 °.
Claims (5)
1. the continuous rosin deslagging device of multi-stage separation is made up of spiral conveying blade (4), U-shaped body (3), filter plate (8,9), separating plate (6,10), charging aperture (12), discharging opening (11), slag-drip opening (7); It is characterized in that: U-shaped body (3) is certain angle with level; And charging aperture (12) height is below slag-drip opening (7); Separating plate is made up of 1 grade of separating plate (10) and 2 grades of separating plates (6); Every grade of separating plate (6,10) is formed by fine and close iron wire filter screen parcel, in peripheral U-shaped body (3) inboard of spiral conveying blade (4) 1 grade of filter plate (8), 2 grades of filter plates (9) is set.
2. according to the continuous rosin deslagging device of the said multi-stage separation of claim 1, it is characterized in that: U-shaped body (3) is 10 °~20 ° angles with level.
3. according to the continuous rosin deslagging device of the said multi-stage separation of claim 1, it is characterized in that: 1 grade of filter plate (8) filter plate pore size is 4~6mm.
4. according to the continuous rosin deslagging device of the said multi-stage separation of claim 1, it is characterized in that: 2 grades of filter plates (9) are positioned at the outside of 1 grade of filter plate (8), in the middle of U-shaped body (3) bottom and 1 grade of filter plate (8), fix at U-shaped body (3) two ends.
5. according to the continuous rosin deslagging device of the said multi-stage separation of claim 1, it is characterized in that: 2 grades of filter plates (9) filter plate pore size is 1~2mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201120237874U CN202136844U (en) | 2011-06-29 | 2011-06-29 | Multistage-separation continuous rosin dreg removal device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201120237874U CN202136844U (en) | 2011-06-29 | 2011-06-29 | Multistage-separation continuous rosin dreg removal device |
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CN202136844U true CN202136844U (en) | 2012-02-08 |
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CN201120237874U Expired - Fee Related CN202136844U (en) | 2011-06-29 | 2011-06-29 | Multistage-separation continuous rosin dreg removal device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102643611A (en) * | 2012-04-24 | 2012-08-22 | 桂林兴松林化有限责任公司 | High-efficiency energy-saving low-cost high-quality rosin production process and production line equipment |
CN102787012A (en) * | 2012-08-21 | 2012-11-21 | 无锡市华立石化工程有限公司 | Turpentine deslagging kettle with conical net |
CN111561662A (en) * | 2020-05-12 | 2020-08-21 | 江西吉仁林化实业有限公司 | Conveying equipment for rosin |
-
2011
- 2011-06-29 CN CN201120237874U patent/CN202136844U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102643611A (en) * | 2012-04-24 | 2012-08-22 | 桂林兴松林化有限责任公司 | High-efficiency energy-saving low-cost high-quality rosin production process and production line equipment |
CN102643611B (en) * | 2012-04-24 | 2013-11-27 | 桂林兴松林化有限责任公司 | High-efficiency energy-saving low-cost high-quality rosin production process and production line equipment |
CN102787012A (en) * | 2012-08-21 | 2012-11-21 | 无锡市华立石化工程有限公司 | Turpentine deslagging kettle with conical net |
CN111561662A (en) * | 2020-05-12 | 2020-08-21 | 江西吉仁林化实业有限公司 | Conveying equipment for rosin |
CN111561662B (en) * | 2020-05-12 | 2021-10-15 | 江西吉仁林化实业有限公司 | Conveying equipment for rosin |
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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: 20120208 Termination date: 20140629 |
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EXPY | Termination of patent right or utility model |