CN205925188U - Automatic high -efficient deslagging box of rosin continuous production - Google Patents

Automatic high -efficient deslagging box of rosin continuous production Download PDF

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Publication number
CN205925188U
CN205925188U CN201620843128.9U CN201620843128U CN205925188U CN 205925188 U CN205925188 U CN 205925188U CN 201620843128 U CN201620843128 U CN 201620843128U CN 205925188 U CN205925188 U CN 205925188U
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CN
China
Prior art keywords
rosin
rotating cylinder
shower nozzle
main body
capstan
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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
Application number
CN201620843128.9U
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Chinese (zh)
Inventor
黄荣全
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Weishan Silver Billion Forest Chemical Industry LLC
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Weishan Silver Billion Forest Chemical Industry LLC
Priority date (The priority date 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 date listed.)
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Publication date
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Priority to CN201620843128.9U priority Critical patent/CN205925188U/en
Application granted granted Critical
Publication of CN205925188U publication Critical patent/CN205925188U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a rosin processing field. Aim at provides an automatic high -efficient deslagging box of rosin continuous production who has high slagging -off performance. The utility model provides a: an automatic high -efficient deslagging box of rosin continuous production, includes the deslagging box main part, the rotary drum top sets up the filter screen of slope, and the main part side middle part row of setting cinder notch, the lower of arranging cinder notch and filter screen is relative. Charge -in pipeline is last to set up the pressurization box, and the bottom surface of pressurization box is the infundibulate, and the main part top sets up air compressor, and air compressor passes through the flow divider and is connected with a pressurizing pipeline and the 2nd pressurizing pipeline respectively, and a pressurizing pipeline is connected with the upper portion of pressurization box, the 2nd pressurizing pipeline and charge -in pipeline near the one end of shower nozzle be connected just lie in the junction the 2nd pressurizing pipeline to one side towards the export of shower nozzle. The utility model discloses can be quicker, thorough with the separation of impurities in the rosin fat liquid, have high slagging -off performance.

Description

A kind of rosin continuously produces automatical and efficient slag removal tank
Technical field
The utility model is related to rosin manufacture field, specifically related to slag removal tank.
Background technology
The production process of rosin mainly includes resin tapping, dissolving, clarification, distillation.Resin tapping be rosin is gathered from pine tree and The whole process of transport;Dissolving is dissolved oil, oxalic acid, water etc. will to be added in the rosin collecting so that rosin is dissolved;After dissolving Solution is passed through in defecator and is clarified, and finally sends in destilling tower and is distilled, the solid obtaining after distillation is rosin.Steam Evaporate the oil of generation, vapour mixture condenses and separates in oil water separator through condenser and turpentine oil is obtained.
Rosin due to collecting has more impurity, such as bark, leaf etc..In order to improve the quality of rosin product, Typically require and first the impurity in rosin liquid is purged, the existing deslagging device structure for rosin production is more simple Single, typically screen pack is set in a tank interior, impurity is taken out after screen pack by rosin solution.But due to rosin Fat liquid viscosity is larger, and mobility is weaker, and usually occurring that impurity is wrapped in inside rosin liquid cannot detached situation.Passing through During filter screen, the rosin liquid that whole group is enclosed with impurity all cannot pass through screen pack, result in blockage, reduce the effect of slagging-off.
Content of the invention
The purpose of this utility model is to provide a kind of rosin with high residue eliminating performance continuously to produce automatical and efficient slagging-off Case.
For achieving the above object, the utility model be employed technical scheme comprise that:A kind of rosin is continuous to be produced automatically Efficiently slag removal tank, including support and the slagging-off box main body being arranged on support, described body floor arranges grease outlet, sets in main body Put rotating cylinder, described rotating cylinder is located at lower body part and is driven by reducing motor, cylinder sidewall arranges some degreasing holes.Above rotating cylinder The screen pack that setting tilts, arranges slag-drip opening in the middle part of described body side, described slag-drip opening is relative with the lowest part of screen pack.Institute State above screen pack setting shower nozzle, described shower nozzle towards main body away from slag-drip opening side, shower nozzle is connected with feed pipe.Described Pressurized cassette is arranged on feed pipe, the bottom surface of described pressurized cassette is in infundibulate, and described body top arranges air compressor, described Air compressor is connected with the first capstan and the second capstan respectively by flow divider, described first capstan with plus The top of pressure box connects, and described second capstan is connected near one end of shower nozzle with feed pipe and is located at the second of junction Capstan is tiltedly towards the outlet of shower nozzle.
Preferably, kuppe is set between described rotating cylinder and screen pack, and the outlet of described kuppe is located at directly over rotating cylinder.
Preferably, described rotating cylinder is in back taper.
Preferably, the outlet of described shower nozzle is in horn-like and is provided with multiple demarcation strips.
The beneficial effects of the utility model embody a concentrated reflection of, can more quick, thoroughly by the impurity in rosin liquid Separate, there is high residue eliminating performance.Specifically, the utility model, when using, is conveyed into main body by feed pipe Rosin liquid, air compressor squeezes into forced air into pressurized cassette and feed pipe.Rosin liquid by spray outlet quick, point Scattered ejection, after impinging upon body side, the inwall along body side glides.Due to rosin liquid glide during relatively For dispersion and thinner thickness, the impurity of its internal package fully can be exposed.Thus when through screen pack, impurity can be had The filtration of effect, it is to avoid impurity is wrapped in blocking screen pack in rosin liquid.The impurity staying after filtration can be discharged along slag-drip opening.And Rosin liquid then falls in rotating cylinder, and reducing motor drives drum rotation, carries out secondary sieving to the rosin liquid in rotating cylinder, finally The rosin liquid of high-quality is discharged through grease outlet.Compare with the deslagging device being traditionally used for rosin production, the utility model is not only The speed of slagging-off is fast, and the effect removing the gred is fabulous.
Brief description
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the scheme of installation of demarcation strip.
Specific embodiment
Continuously produce automatical and efficient slag removal tank in conjunction with a kind of rosin shown in Fig. 1 and 2, include support 1 and be arranged on support 1 On slagging-off box main body 2, described main body 2 and support 1 are fixed using modes such as bolts or welding.Described main body 2 bottom surface sets Put grease outlet 3, setting rotating cylinder 4 in main body 2, described rotating cylinder 4 is located at main body 2 bottom and is driven by reducing motor 5, rotating cylinder 4 side Wall arranges some degreasing holes, and described degreasing hole is in the through hole on rotating cylinder 4 side wall, when rotating cylinder 4 rotates, rosin liquid Flowed out by degreasing in the hole, enter the grease outlet 3 being located at bottom.The screen pack 6 that rotating cylinder 4 top setting tilts, described main body 2 side Middle part setting slag-drip opening 7, described slag-drip opening 7 is relative with the lowest part of screen pack 6.Described screen pack 6 top setting shower nozzle 8, institute State shower nozzle 8 towards main body 2 away from slag-drip opening 7 side, as shown in figure 1, slag-drip opening 7 is in the left surface of main body 2, then shower nozzle 8 court Right flank to main body 2.Shower nozzle 8 is connected with feed pipe 9, and described feed pipe 9 arranges pressurized cassette 10, described pressurized cassette 10 It is the box body of a closing, can be by squeezing into air into pressurized cassette 10, thus improving the pressure within pressurized cassette 10.Described The bottom surface of pressurized cassette 10 is in the infundibulate being easy to the discharge of rosin liquid, and described main body 2 top arranges air compressor 11, described sky Air compressor 11 is connected with the first capstan 13 and the second capstan 14 respectively by flow divider 12, described first forcing pipe Road 13 is connected with the top of pressurized cassette 10, and described second capstan 14 is connected and position near one end of shower nozzle 8 with feed pipe 9 In the oblique outlet towards shower nozzle 8 of the second capstan 14 of junction, as shown in Fig. 2 namely described second capstan 14 With feed pipe 9 oblique, and guarantee that the forced air discharge direction discharged in the second capstan 14 is partial to the going out of shower nozzle 8 Mouthful, the outlet of shower nozzle 8 is located at right side, then the second capstan 14 tilts from upper left to bottom right.
The utility model use when, rosin liquid is conveyed into main body 2 by feed pipe 9, air compressor 11 to Forced air is squeezed in pressurized cassette 10 and feed pipe 9.Rosin liquid exports quick, scattered ejection by shower nozzle 8, impinges upon master Behind body 2 side, the inwall along main body 2 side glides.Due to rosin liquid glide during more dispersion and thickness relatively Thin, the impurity of its internal package fully can be exposed.Thus when through screen pack 6, impurity can effectively be filtered, it is to avoid Impurity is wrapped in blocking screen pack 6 in rosin liquid.The impurity staying after filtration can be discharged along slag-drip opening 7.And rosin liquid is then Fall in rotating cylinder 4, reducing motor 5 drives rotating cylinder 4 to rotate, and carries out secondary sieving to the rosin liquid in rotating cylinder 4, last high-quality Rosin liquid is discharged through grease outlet 3.Compare with the deslagging device being traditionally used for rosin production, the utility model not only removes the gred Speed is fast, and the effect removing the gred is fabulous.
In order to improve performance of the present utility model further, water conservancy diversion can also be set between described rotating cylinder 4 and screen pack 6 Cover 15, the outlet of described kuppe 15 is located at directly over rotating cylinder 4.Described kuppe 15 shape is matched with screen pack 6 and rotating cylinder 4 Close, kuppe 15 is easy to import completely inside rotating cylinder 4 through the rosin liquid that screen pack 6 filters.In order to improve the sieve of rotating cylinder 4 Divide effect, it is also possible that state rotating cylinder 4 being set in back taper, facilitating heavier impurity and converging in rotating cylinder 4 bottom, in accumulation To more when so that it may open maintenance door, impurity is discharged, usual maintenance door be located at main body 2 side.The rotating cylinder 4 of back taper Due to being inclined-plane, when rotating cylinder 4 rotates, lighter rosin liquid can be up along the side of rotating cylinder 4, makes rotating cylinder 4 for the side on top Filter effect more preferably.As shown in Fig. 2 can also be in horn-like and be provided with multiple demarcation strips 16 in the outlet of described shower nozzle 8, The rosin liquid exporting ejection from shower nozzle 8 can be disperseed by demarcation strip 16 further, makes impurity be easier to expose.For the ease of main body 2 cleaning, can also be arranged steam pipework in main body 2, by steam pipework, rosin liquid be heated, can be effective Improve the mobility of rosin liquid.

Claims (4)

1. a kind of rosin continuously produce automatical and efficient slag removal tank it is characterised in that:Including support(1)Be arranged on support(1)On Slagging-off box main body(2), described main body(2)Bottom surface arranges grease outlet(3), main body(2)Interior setting rotating cylinder(4), described rotating cylinder(4) Positioned at main body(2)Reducing motor is simultaneously passed through in bottom(5)Drive, rotating cylinder(4)Side wall arranges some degreasing holes;Rotating cylinder(4)Top sets Put the screen pack of inclination(6), described main body(2)Slag-drip opening is set in the middle part of side(7), described slag-drip opening(7)With screen pack(6)'s Lowest part is relatively;Described screen pack(6)Top setting shower nozzle(8), described shower nozzle(8)Towards main body(2)Away from slag-drip opening(7)'s Side, shower nozzle(8)With feed pipe(9)Connect;Described feed pipe(9)Upper setting pressurized cassette(10), described pressurized cassette(10) Bottom surface be in infundibulate, described main body(2)Top arranges air compressor(11), described air compressor(11)By flow divider (12)Respectively with the first capstan(13)With the second capstan(14)Connect, described first capstan(13)With pressurized cassette (10)Top connect, described second capstan(14)With feed pipe(9)Near shower nozzle(8)One end connect and be located at even Connect second capstan at place(14)Tiltedly towards shower nozzle(8)Outlet.
2. rosin according to claim 1 continuously produce automatical and efficient slag removal tank it is characterised in that:Described rotating cylinder(4)With Screen pack(6)Between arrange kuppe(15), described kuppe(15)Outlet be located at rotating cylinder(4)Surface.
3. rosin according to claim 2 continuously produce automatical and efficient slag removal tank it is characterised in that:Described rotating cylinder(4)It is in Back taper.
4. rosin according to claim 3 continuously produce automatical and efficient slag removal tank it is characterised in that:Described shower nozzle(8)'s Outlet is in horn-like and is provided with multiple demarcation strips(16).
CN201620843128.9U 2016-08-05 2016-08-05 Automatic high -efficient deslagging box of rosin continuous production Expired - Fee Related CN205925188U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620843128.9U CN205925188U (en) 2016-08-05 2016-08-05 Automatic high -efficient deslagging box of rosin continuous production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620843128.9U CN205925188U (en) 2016-08-05 2016-08-05 Automatic high -efficient deslagging box of rosin continuous production

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Publication Number Publication Date
CN205925188U true CN205925188U (en) 2017-02-08

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108193294A (en) * 2018-01-17 2018-06-22 泰兴市恒信特种耐火材料有限公司 Low slag ball aluminosilicate refractory fiber needle punched blanket production line

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108193294A (en) * 2018-01-17 2018-06-22 泰兴市恒信特种耐火材料有限公司 Low slag ball aluminosilicate refractory fiber needle punched blanket production line

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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
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170208

Termination date: 20170805