CN203420171U - High-concentration slag remover - Google Patents
High-concentration slag remover Download PDFInfo
- Publication number
- CN203420171U CN203420171U CN201320346532.1U CN201320346532U CN203420171U CN 203420171 U CN203420171 U CN 203420171U CN 201320346532 U CN201320346532 U CN 201320346532U CN 203420171 U CN203420171 U CN 203420171U
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- CN
- China
- Prior art keywords
- slag
- feed
- sediment pot
- deslagging device
- sediment
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- Expired - Fee Related
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Abstract
The utility model discloses a high-concentration slag remover. The high-concentration slag remover is characterized by comprising a feeding barrel body, a first-stage slag-removing device, a second-stage slag-removing device, a slag sediment tank and a supporting frame, wherein an accepts port is formed in the top of the feeding barrel body, a spiral feeding pipeline is arranged on the lateral wall of the top of the feeding barrel body, a pulp inlet is formed in a feeding end of the spiral feeding pipeline, the first-stage slag-removing device and the second-stage slag-removing device are sequentially arranged at the bottom of the feeding barrel body, the bottom of the second-stage slag-removing device is connected with a feeding end of the slag sediment tank, a slag discharging port is formed in the bottom of the slag sediment tank, the slag sediment is fixed to the supporting frame, and valves are arranged on the feeding end of the slag sediment tank and the slag discharging port respectively. The high-concentration slag remover has the advantages of being good in slag outlet effect, capable of simultaneously removing various impurities, high in work efficiency, simple in structure and convenient to operate, and the production capacity of high-concentration cotton pulp can reach 55t/d.
Description
Technical field
The utility model relates to a kind of HC Cleaner, belongs to purified cotton slag removal equipment field.
Background technology
During refined cotton production, through thermophilic digestion, in the cotton pulp after bleaching, washing, contain a small amount of cotton slag, the end of a thread and other impurity, 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 current manner of cleaning up is by manually picking mostly, the impurity such as the cotton slag in cotton pulp, the end of a thread to be picked out, 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.
Utility model content
The purpose of this utility model is to provide that a kind of operating efficiency is high, effective HC Cleaner removes the gred.
The technical scheme in the invention for solving the above technical problem is:
A kind of HC Cleaner, comprise feed barrel, one-level deslagging device, secondary deslagging device, sediment pot and bracing frame, the top of described feed barrel is provided with good slurry mouthful, on the sidewall of described feed barrel top, be provided with spiral feed pipe, on the feed end of described spiral feed pipe, be provided with stock inlet, described one-level deslagging device, 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 described bottom except sediment pot is provided with slag-drip opening, described sediment pot is fixed on bracing frame, on the feed end of described sediment pot and on slag-drip opening, be provided with valve.
The taper courage I that described one-level deslagging device comprises the outer cylinder body I that top is fixedly connected with feed barrel and is connected with feed barrel; Described secondary deslagging device comprises the outer cylinder body II that top is fixedly connected with outer cylinder body I and the taper courage II being connected with taper courage I, and the bottom of described outer cylinder body II is fixed on 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 is connected with spiral feed pipe.
On the top of described feed barrel and sediment pot, be provided with recoil and clean water pipe.
On the sidewall of described sediment pot, be provided with capacity observation panel.
On the inwall of described sediment pot, be provided with strong magnets.
The utility model has the advantages that: slag tap effective, can remove plurality of impurities simultaneously, operating efficiency is high, high concentration cotton pulp production capacity can reach 55t/d, simple in structure, easy to operate.
Accompanying drawing explanation
Fig. 1 is overall structure schematic diagram of the present utility model.
Fig. 2 is the plan structure schematic diagram of Fig. 1.
Wherein: 1, feed barrel, 2, one-level deslagging device, 3, 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, at the top of feed barrel 1, be provided with good slurry mouth 6, on feed barrel 1 top sidewall, be provided with spiral feed pipe 7, on the feed end of spiral feed pipe, be provided with stock inlet 8, 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 is fixedly connected with feed barrel and is connected with feed barrel; Secondary deslagging device 3 comprises the outer cylinder body II13 that top is fixedly connected with outer cylinder body I11 and the taper courage II14 being connected with taper courage I12, the bottom of outer cylinder body II13 is fixed on bracing frame 5, the bottom of taper courage II14 is connected with the feed end of sediment pot 4, in the bottom of sediment pot 4, be provided with slag-drip opening 9, sediment pot 4 is fixed on bracing frame 5, is provided with valve 10 on the feed end of sediment pot 4 and on slag-drip opening 9.
During use, the cotton pulp of high concentration enters from stock inlet 8, by spiral feed pipe 7, entered in feed barrel 1, cotton pulp is down motion twist, in motion process, cotton slag, the end of a thread etc. drop on taper courage I12, 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, after in entering into taper courage II14, form cutout, the impurity such as cotton slag, the end of a thread drop in sediment pot 4, and slurry after slagging-off starts up to move, the slurry mouthfuls 6 of getting married and start a new life transfers out and enters subsequent processing.And the impurity such as cotton slag fall after full sediment pot 4, close the valve 10 on the charging aperture of sediment pot, open the valve 10 on slag-drip opening 9 simultaneously, the impurity such as cotton slag are discharged from slag-drip opening.The speed and the spiral effect that in order to strengthen high concentration cotton pulp, enter stock inlet 8, be related to pyramidal structure by stock inlet 8, and the osculum end of stock inlet is connected with spiral feed pipe 7.Iron ion in dedusting cotton pulp is better provided with strong magnets 17 on the inwall of sediment pot, simultaneously in order to observe in time the situation in sediment pot 4, is provided with capacity observation panel 16 on the sidewall of sediment pot.The impurity adhering in order to clean well scummer inwall is provided with recoil and cleans water pipe 15 on the top of feed barrel 1 and sediment pot 4, is cleaned in water pipe 15 net scummers and is poured clear water, to reach the effect of cleaning inwall by this recoil.
Claims (6)
1. a HC Cleaner, it is characterized in that: comprise feed barrel, one-level deslagging device, secondary deslagging device, sediment pot and bracing frame, the top of described feed barrel is provided with good slurry mouthful, on the sidewall of described feed barrel top, be provided with spiral feed pipe, on the feed end of described spiral feed pipe, be provided with stock inlet, described one-level deslagging device, 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 bracing frame, on the feed end of described sediment pot and on slag-drip opening, be provided with valve.
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 is fixedly connected with feed barrel and is connected with feed barrel; Described secondary deslagging device comprises the outer cylinder body II that top is fixedly connected with outer cylinder body I and the taper courage II being connected with taper courage I, and the bottom of described outer cylinder body II is fixed on 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, is characterized in that: described stock inlet is pyramidal structure, and the osculum end of described stock inlet is connected with spiral feed pipe.
4. a kind of HC Cleaner according to claim 1 and 2, is characterized in that: on the top of described feed barrel and sediment pot, be provided with recoil and clean water pipe.
5. a kind of HC Cleaner according to claim 1 and 2, is characterized in that: on the sidewall of described sediment pot, be provided with capacity observation panel.
6. a kind of HC Cleaner according to claim 1 and 2, is characterized in that: on the inwall of described sediment pot, be provided with strong magnets.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320346532.1U CN203420171U (en) | 2013-06-17 | 2013-06-17 | High-concentration slag remover |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320346532.1U CN203420171U (en) | 2013-06-17 | 2013-06-17 | High-concentration slag remover |
Publications (1)
Publication Number | Publication Date |
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CN203420171U true CN203420171U (en) | 2014-02-05 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201320346532.1U Expired - Fee Related CN203420171U (en) | 2013-06-17 | 2013-06-17 | High-concentration slag remover |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103352390A (en) * | 2013-06-17 | 2013-10-16 | 如东县海宇纤维制品有限公司 | High-concentration slag separator |
-
2013
- 2013-06-17 CN CN201320346532.1U patent/CN203420171U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103352390A (en) * | 2013-06-17 | 2013-10-16 | 如东县海宇纤维制品有限公司 | High-concentration slag separator |
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Legal Events
Date | Code | Title | Description |
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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: 20140205 Termination date: 20160617 |
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CF01 | Termination of patent right due to non-payment of annual fee |