CN103352390A - High-concentration slag separator - Google Patents
High-concentration slag separator Download PDFInfo
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- CN103352390A CN103352390A CN2013102395792A CN201310239579A CN103352390A CN 103352390 A CN103352390 A CN 103352390A CN 2013102395792 A CN2013102395792 A CN 2013102395792A CN 201310239579 A CN201310239579 A CN 201310239579A CN 103352390 A CN103352390 A CN 103352390A
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- slag
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- cylinder body
- sediment pot
- deslagging device
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Abstract
The invention discloses a high-concentration slag separator which is characterized by comprising a feeding cylinder body, a primary slag separation device, a secondary slag separation device, a slag settlement tank and a supporting frame, wherein a good pulp opening is formed in the top of the feeding cylinder body, a spiral feeding pipeline is arranged on one side wall at the top of the feeding cylinder body, a pulp inlet is formed in a feeding end of the spiral feeding pipeline, the primary slag separation device and the second slag separation device are arranged at the bottom of the feeding cylinder body in sequence, the bottom of the second slag separation device is connected with a feeding end of the slag settlement tank, a slag discharge opening is formed in the bottom of the slag settlement tank, the slag settlement tank is fixed on the supporting frame, and valves are arranged on the feeding end of the slag settlement tank and the slag discharge opening. The high-concentration slag separator has the advantages that the slag discharging effect is good, various impurities can be removed at the same time, the working efficiency is high, the production capacity of high-concentration cotton pulp can reach 55 t/d, the structure is simple, and the operation is convenient.
Description
Technical field
The present invention relates to a kind of HC Cleaner, belong to purified cotton slag removal equipment field.
Background technology
In the during refined cotton production, through thermophilic digestion, contain a small amount of cotton slag, the end of a thread and other impurity in the cotton pulp after bleaching, the washing, if these cotton slags and impurity can not get cleaning or clears up endless, can seriously affect the quality of product, even have influence on the result of use of product.And present manner of cleaning up is by manually picking, the impurity such as the cotton slag in the cotton pulp, the end of a thread are picked out mostly, and this mode not only workload is large, and picks untotally, greatly reduces production efficiency and product quality.Therefore, need a kind of new technical scheme to solve above-mentioned technical problem.
Summary of the invention
The purpose of this invention is to provide a kind of high efficiency, the effective HC Cleaner of slagging-off.
The technical scheme that the present invention solves the problems of the technologies described above employing is:
A kind of HC Cleaner, comprise feed barrel, the one-level deslagging device, the secondary deslagging device, sediment pot and bracing frame, the top of described feed barrel is provided with good slurry mouth, be provided with the spiral feed pipe on the sidewall of described feed barrel top, be provided with stock inlet on the feed end of described spiral feed pipe, described one-level deslagging device, the secondary deslagging device is set in turn in the bottom of feed barrel, the bottom of described secondary deslagging device is connected with the feed end of sediment pot, described bottom except sediment pot is provided with slag-drip opening, described sediment pot is fixed on the bracing frame, is provided with valve on the feed end of described sediment pot and on the slag-drip opening.
The taper courage I that described one-level deslagging device comprises the outer cylinder body I that top and feed barrel are fixedly connected with and is connected with feed barrel; Described secondary deslagging device comprises the outer cylinder body II that top and outer cylinder body I are fixedly connected with and the taper courage II that is connected with taper courage I, and the bottom of described outer cylinder body II is fixed on the bracing frame, and the bottom of described taper courage II is connected with the feed end of sediment pot.
Described stock inlet is pyramidal structure, and the osculum end of described stock inlet links to each other with the spiral feed pipe.
Be provided with recoil on the top of described feed barrel and the sediment pot and clean water pipe.
Be provided with the capacity observation panel on the sidewall of described sediment pot.
Be provided with strong magnets on the inwall of described sediment pot.
Advantage of the present invention is: slag tap effective, can remove simultaneously plurality of impurities,, high efficiency, high concentration cotton pulp production capacity can reach 55t/d, and is simple in structure, easy to operate.
Description of drawings
Fig. 1 is overall structure schematic diagram of the present invention.
Fig. 2 is the plan structure schematic diagram of Fig. 1.
Wherein: 1, feed barrel, 2, the one-level deslagging device, 3, the secondary deslagging device, 4, sediment pot, 5, bracing frame, 6, good slurry mouthful, 7, spiral feed pipe, 8, stock inlet, 9, slag-drip opening, 10, valve, 11, outer cylinder body I, 12, taper courage I, 13, outer cylinder body II, 14, taper courage II, 15, recoil cleans water pipe, 16, capacity observation panel, 17, strong magnets.
The specific embodiment
As depicted in figs. 1 and 2, a kind of HC Cleaner, comprise feed barrel 1, one-level deslagging device 2, secondary deslagging device 3, sediment pot 4 and bracing frame 5, be provided with good slurry mouth 6 at the top of feed barrel 1, be provided with spiral feed pipe 7 at feed barrel 1 top sidewall, feed end at the spiral feed pipe is provided with stock inlet 8, and one-level deslagging device 22, secondary deslagging device 3 are set in turn in the bottom of feed barrel 1.The taper courage I12 that one-level deslagging device 2 comprises the outer cylinder body I11 that top and feed barrel are fixedly connected with and is connected with feed barrel; Secondary deslagging device 3 comprises the outer cylinder body II13 that top and outer cylinder body I11 are fixedly connected with and the taper courage II14 that is connected with taper courage I12, the bottom of outer cylinder body II13 is fixed on the bracing frame 5, the bottom of taper courage II14 is connected with the feed end of sediment pot 4, be provided with slag-drip opening 9 in the bottom of sediment pot 4, sediment pot 4 is fixed on the bracing frame 5, on the feed end of sediment pot 4 and slag-drip opening 9 be provided with valve 10.
During use, the cotton pulp of high concentration enters from stock inlet 8, entered in the feed barrel 1 by spiral feed pipe 7, cotton pulp is down motion twist, cotton slag, the end of a thread etc. drop on taper courage I12 in the motion process, the motion that enters along with cotton pulp, the impurity such as cotton pulp and cotton slag, the end of a thread continue down motion, form cutout after in entering into taper courage II14, the impurity such as cotton slag, the end of a thread drop in the sediment pot 4, and the slurry after the slagging-off begins up to move, and the slurry mouth 6 of getting married and start a new life transfers out and enter subsequent processing.And the impurity such as cotton slag fall behind the full sediment pot 4, close the valve 10 on the charging aperture of sediment pot, open simultaneously the valve 10 on the slag-drip opening 9, and the impurity such as cotton slag are discharged from slag-drip opening.Enter speed and the spiral effect of stock inlet 8 in order to strengthen the high concentration cotton pulp, stock inlet 8 is related to pyramidal structure, and the osculum end of stock inlet links to each other with spiral feed pipe 7.For the iron ion in the dedusting cotton pulp better, be provided with strong magnets 17 at the inwall of sediment pot, simultaneously in order to observe in time the situation in the sediment pot 4, be provided with capacity observation panel 16 at the sidewall of sediment pot.The impurity that adheres in order to clean well the scummer inwall, at the top of feed barrel 1 and sediment pot 4 be provided with recoil and clean water pipe 15, clean in water pipe 15 net scummers by this recoil and pour clear water, to reach the effect of cleaning inwall.
Claims (6)
1. HC Cleaner, it is characterized in that: comprise feed barrel, the one-level deslagging device, the secondary deslagging device, sediment pot and bracing frame, the top of described feed barrel is provided with good slurry mouth, be provided with the spiral feed pipe on the sidewall of described feed barrel top, be provided with stock inlet on the feed end of described spiral feed pipe, described one-level deslagging device, the secondary deslagging device is set in turn in the bottom of feed barrel, the bottom of described secondary deslagging device is connected with the feed end of sediment pot, the bottom of described sediment pot is provided with slag-drip opening, described sediment pot is fixed on the bracing frame, is provided with valve on the feed end of described sediment pot and on the slag-drip opening.
2. a kind of HC Cleaner according to claim 1 is characterized in that: the taper courage I that described one-level deslagging device comprises the outer cylinder body I that top and feed barrel are fixedly connected with and is connected with feed barrel; Described secondary deslagging device comprises the outer cylinder body II that top and outer cylinder body I are fixedly connected with and the taper courage II that is connected with taper courage I, and the bottom of described outer cylinder body II is fixed on the bracing frame, and the bottom of described taper courage II is connected with the feed end of sediment pot.
3. a kind of HC Cleaner according to claim 1 and 2, it is characterized in that: described stock inlet is pyramidal structure, the osculum end of described stock inlet links to each other with the spiral feed pipe.
4. a kind of HC Cleaner according to claim 1 and 2 is characterized in that: be provided with recoil on the top of described feed barrel and the sediment pot and clean water pipe.
5. a kind of HC Cleaner according to claim 1 and 2 is characterized in that: be provided with the capacity observation panel on the sidewall of described sediment pot.
6. a kind of HC Cleaner according to claim 1 and 2 is characterized in that: be provided with strong magnets on the inwall of described sediment pot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013102395792A CN103352390A (en) | 2013-06-17 | 2013-06-17 | High-concentration slag separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013102395792A CN103352390A (en) | 2013-06-17 | 2013-06-17 | High-concentration slag separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103352390A true CN103352390A (en) | 2013-10-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013102395792A Pending CN103352390A (en) | 2013-06-17 | 2013-06-17 | High-concentration slag separator |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105198037A (en) * | 2015-11-12 | 2015-12-30 | 南京林业大学 | Dissolved-air injection water pulp purification principle-based hydrocyclone system and slurry-residue separation method |
| CN110592730A (en) * | 2019-09-27 | 2019-12-20 | 山东恒联新材料股份有限公司 | Recovery equipment and recovery method for waste glue generated in cellulose viscose production process |
| CN111778756A (en) * | 2020-07-01 | 2020-10-16 | 淄博云峰工业陶瓷有限公司 | Novel purify high concentration scummer for waste paper pulp |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4107033A (en) * | 1976-03-20 | 1978-08-15 | Hermann Finckh Maschinenfabrik | Apparatus for cleaning fibrous suspensions of low stock consistency |
| CN2659548Y (en) * | 2003-12-01 | 2004-12-01 | 徐斌 | Skim gate for pipeline |
| CN201738182U (en) * | 2010-06-02 | 2011-02-09 | 安丘市天利机械制造有限公司 | Double-cone slag removal separation device |
| CN201817735U (en) * | 2010-10-12 | 2011-05-04 | 山东杰锋机械制造有限公司 | Eddy slag remover |
| CN202187244U (en) * | 2011-07-05 | 2012-04-11 | 张祺翔 | Pulp inlet chamber of high concentration slag desledger separator for papermaking |
| CN203420171U (en) * | 2013-06-17 | 2014-02-05 | 如东县海宇纤维制品有限公司 | High-concentration slag remover |
-
2013
- 2013-06-17 CN CN2013102395792A patent/CN103352390A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4107033A (en) * | 1976-03-20 | 1978-08-15 | Hermann Finckh Maschinenfabrik | Apparatus for cleaning fibrous suspensions of low stock consistency |
| CN2659548Y (en) * | 2003-12-01 | 2004-12-01 | 徐斌 | Skim gate for pipeline |
| CN201738182U (en) * | 2010-06-02 | 2011-02-09 | 安丘市天利机械制造有限公司 | Double-cone slag removal separation device |
| CN201817735U (en) * | 2010-10-12 | 2011-05-04 | 山东杰锋机械制造有限公司 | Eddy slag remover |
| CN202187244U (en) * | 2011-07-05 | 2012-04-11 | 张祺翔 | Pulp inlet chamber of high concentration slag desledger separator for papermaking |
| CN203420171U (en) * | 2013-06-17 | 2014-02-05 | 如东县海宇纤维制品有限公司 | High-concentration slag remover |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105198037A (en) * | 2015-11-12 | 2015-12-30 | 南京林业大学 | Dissolved-air injection water pulp purification principle-based hydrocyclone system and slurry-residue separation method |
| CN105198037B (en) * | 2015-11-12 | 2016-10-12 | 南京林业大学 | Based on the hydrocyclone system and the screenings separation method that inject dissolved air water formula pulp purifiation principle |
| CN110592730A (en) * | 2019-09-27 | 2019-12-20 | 山东恒联新材料股份有限公司 | Recovery equipment and recovery method for waste glue generated in cellulose viscose production process |
| CN111778756A (en) * | 2020-07-01 | 2020-10-16 | 淄博云峰工业陶瓷有限公司 | Novel purify high concentration scummer for waste paper pulp |
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Application publication date: 20131016 |