CN204238065U - Cotton starch plate is produced with refinement concentration equipment - Google Patents
Cotton starch plate is produced with refinement concentration equipment Download PDFInfo
- Publication number
- CN204238065U CN204238065U CN201420732542.3U CN201420732542U CN204238065U CN 204238065 U CN204238065 U CN 204238065U CN 201420732542 U CN201420732542 U CN 201420732542U CN 204238065 U CN204238065 U CN 204238065U
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- CN
- China
- Prior art keywords
- tailings
- recovery device
- stage
- slurry
- tailings recovery
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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 - Lifetime
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- 229920000742 Cotton Polymers 0.000 title claims abstract description 19
- 229920002472 Starch Polymers 0.000 title description 10
- 235000019698 starch Nutrition 0.000 title description 10
- 239000008107 starch Substances 0.000 title description 10
- 238000011084 recovery Methods 0.000 claims abstract description 63
- 239000002002 slurry Substances 0.000 claims abstract description 51
- 239000012535 impurity Substances 0.000 claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 claims abstract description 11
- 239000004576 sand Substances 0.000 claims abstract description 10
- 238000007670 refining Methods 0.000 claims 2
- 238000004537 pulping Methods 0.000 claims 1
- 239000002893 slag Substances 0.000 claims 1
- 230000008719 thickening Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 5
- 239000000428 dust Substances 0.000 abstract description 4
- 239000000835 fiber Substances 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 3
- 230000008676 import Effects 0.000 description 10
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 235000006662 Lansium Nutrition 0.000 description 2
- 241001156382 Lansium Species 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
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- Paper (AREA)
Abstract
本实用新型公开了一种棉浆板生产用细化浓缩处理设备，包括一、二级除砂装置，一、二级除砂装置的尾渣排出口分别与二段尾渣回收装置相连接，二段尾渣回收装置回收的良浆排出口与二级除砂装置的浆料进口相连接，二段尾渣回收装置的尾渣排出口与三段尾渣回收装置的浆料进口相连接，三段尾渣回收装置的尾渣排出口与四段尾渣回收装置的浆料进口相连接，四段尾渣回收装置的尾渣排出口与尾渣收集装置相连接，采用上述细化浓缩处理设备对浆料进行除杂，较传统工艺，除砂净化率由64％-76％提升至80％-90％；尾渣纤维总损失率由1.5％-2.0％降至0.1％-0.5％，净化后浆料符合客户对尘埃指标的高标准要求。
The utility model discloses a refinement and concentration treatment equipment for cotton pulp board production, which comprises primary and secondary desanding devices, the tailings discharge ports of the primary and secondary desandering devices are respectively connected with the secondary tailings recovery device, The good pulp outlet recovered by the second-stage tailings recovery device is connected to the slurry inlet of the second-stage sand removal device, and the tailings outlet of the second-stage tailings recovery device is connected to the slurry inlet of the third-stage tailings recovery device. The tailings discharge port of the third-stage tailings recovery device is connected to the slurry inlet of the fourth-stage tailings recovery device, and the tailings discharge port of the fourth-stage tailings recovery device is connected to the tailings collection device, and the above-mentioned refinement and concentration treatment is adopted The equipment removes impurities from the slurry. Compared with the traditional process, the sand removal and purification rate is increased from 64%-76% to 80%-90%; the total loss rate of tailing fiber is reduced from 1.5%-2.0% to 0.1%-0.5%. The purified slurry meets the customer's high standard requirements for dust indicators.
Description
Technical field
The utility model relates to cotton starch plate production field, is specifically related to a kind of cotton starch plate production refinement concentration equipment.
Background technology
The paper that our people's coin is adopted is rag paper, and the raw materials for production of rag paper are cotton, is that cotton is processed into cotton starch plate at the production initial stage, and then cracks cotton starch plate and be processed into rag paper and follow-up printing operation.In traditional processing technology, the technique of one-level two sections of desanding is adopted to carry out desanding removal of impurities to the cotton pulp after boiling.One-level two sections of sand removing processs effectively cannot remove the non-fiber impurity such as the Calusena lansium in slurry, and tailings amount is comparatively large simultaneously, and cause wastage of material, product quality is difficult to reach producer's requirement, and dust detects not up to standard.
Utility model content
The purpose of this utility model is to provide a kind of cotton starch plate production refinement concentration equipment, and it effectively can remove the impurity such as cotton seed hulls, Calusena lansium in slurry, and can process further tailings, improves the rate of recovery of slurry, reduces production cost.
For achieving the above object, the utility model adopts following technical scheme to implement:
A kind of cotton starch plate is produced with refinement concentration equipment, it is characterized in that: the one-level desanding device set gradually before and after comprising and secondary desanding device, one, the tailings outlet of secondary desanding device is connected with two sections of recovery device for tailings respectively, the good slurry outlet of two sections of recovery device for tailings recovery is connected with the slurry import of secondary desanding device, the tailings outlet of two sections of recovery device for tailings is connected with the slurry import of three sections of recovery device for tailings, the good slurry outlet of three sections of recovery device for tailings recovery is connected with the slurry import of two sections of recovery device for tailings, the tailings outlet of three sections of recovery device for tailings is connected with the slurry import of four sections of recovery device for tailings, the good slurry outlet of four sections of recovery device for tailings recovery is connected with the slurry import of three sections of recovery device for tailings, the tailings outlet of four sections of recovery device for tailings is connected with tailings gathering-device, one-level desanding device is that 26 606 desanders are in series, secondary desanding device is that 24 606 desanders are in series, two sections of recovery device for tailings are that 14 606 desanders are in series, three sections of recovery device for tailings are that 3 606 desanders are in series, four sections of recovery device for tailings are that 2 606 desanders are in series.
Concrete scheme is:
The front portion of one-level desanding device arranges the one-level middle tone stock tank regulated slurry concentration, arranges the secondary middle tone stock tank regulated slurry concentration between I and II desanding device.The good slurry outlet of secondary desanding device is connected with cylinder enrichment facility.Refinement concentration equipment also comprises stuff box, is provided with the desilting ditch for tentatively removing impurity in slurry between stuff box and one-level middle tone stock tank.
The beneficial effects of the utility model are: adopt above-mentioned refinement concentration equipment to carry out removal of impurities to slurry, comparatively traditional handicraft, desanding purifying rate is promoted to 80%-90% by 64%-76%; Tailings fiber total loss rate is down to 0.1%-0.5% by 1.5%-2.0%, and purification disposed slurry meets the high standard requirement of client to dust index.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
In order to make the purpose of this utility model and advantage clearly understand, below in conjunction with embodiment, the utility model is specifically described.Should be appreciated that following word only in order to describe one or more concrete embodiments of the present utility model, considered critical is not carried out to the protection domain that the utility model is specifically asked.
The technical scheme that the utility model is taked as shown in Figure 1, a kind of cotton starch plate is produced with refinement concentration equipment, the one-level desanding device 11 set gradually before and after comprising and secondary desanding device 12, one, the tailings outlet of secondary desanding device 12 is connected with two sections of recovery device for tailings 18 respectively, the good slurry outlet of two sections of recovery device for tailings 18 recovery is connected with the slurry import of secondary desanding device 12, the tailings outlet of two sections of recovery device for tailings 18 is connected with the slurry import of three sections of recovery device for tailings 19, the good slurry outlet of three sections of recovery device for tailings 19 recovery is connected with the slurry import of two sections of recovery device for tailings 18, the tailings outlet of three sections of recovery device for tailings 19 is connected with the slurry import of four sections of recovery device for tailings 20, the good slurry outlet of four sections of recovery device for tailings 20 recovery is connected with the slurry import of three sections of recovery device for tailings 19, the tailings outlet of four sections of recovery device for tailings 20 is connected with tailings gathering-device 21, one-level desanding device 11 is that 26 606 desanders (606 II X desander) are in series, secondary desanding device 12 is that 24 606 desanders are in series, two sections of recovery device for tailings 18 are that 14 606 desanders are in series, three sections of recovery device for tailings 19 are that 3 606 desanders are in series, four sections of recovery device for tailings 20 are that 2 606 desanders are in series.The technique of secondary four sections is adopted to carry out removal of impurities to cotton pulp material in the utility model, in order to improve the efficiency of removal of impurities and to improve the rate of recovery of slurry.
Concrete is operating as: the front portion of one-level desanding device 11 arranges the one-level middle tone stock tank 13 regulated slurry concentration, arranges the secondary middle tone stock tank 14 regulated slurry concentration between I and II desanding device 12.The good slurry outlet of secondary desanding device 12 is connected with cylinder enrichment facility 17 (decker).Refinement concentration equipment also comprises stuff box 15, is provided with the desilting ditch 16 for tentatively removing impurity in slurry between stuff box 15 and one-level middle tone stock tank 13.Desilting ditch is a segment length 1000mm wide 75mm height 60mm groove, and in groove, the calcium-plastic board of oblique cutting 6 tile height 20mm is formed and cuts off, and slurry is slowly flowed in desilting ditch, heavy foreign material natural sediment.
In stuff box, first regulate slurry dense to 0.5% before desanding, utilize sand setting ditch precipitated impurities, slurry enters and enters one-level desanding device 11 after one-level middle tone stock tank is sized mixing again and carry out one-level desanding, the good slurry that one-level desanding device 11 reclaims enters and enters secondary desanding device 12 again after secondary middle tone stock tank regulates and carry out desanding, and desanding terminates rear good slurry and is delivered to cylinder enrichment facility and concentrates laggard reserve pit.The tailings that I and II desanding device 12 is separated enters two, three, four sections of recovery device for tailings 20 and recycles, and every section of good slurry reclaimed from tailings enters the preceding paragraph recovery device for tailings, and final stage tailings is discharged to collect to reclaim and is used for other utilization.
In the utility model, each device is all supporting stock pump, and desanding at different levels enters to starch pressure >=0.35MPa, pulp pressure 0.05-0.07MPa.
Detailed is:
One-level desanding device 11: motor 110KW, stock pump lift 35M, flow 700M/H
Secondary desanding device 12: motor 90KW, stock pump lift 35M, flow 650M/H
Two sections of recovery device for tailings 18: motor 45KW, stock pump lift 32M, flow 350M/H
Three sections of recovery device for tailings 19: motor 11KW, stock pump lift 32M, flow 90M/H
Four sections of recovery device for tailings 20: motor 5.5KW, stock pump lift 27M, flow 30M/H
The beneficial effects of the utility model are: adopt above-mentioned refinement concentration equipment to carry out removal of impurities to slurry, comparatively traditional handicraft, desanding purifying rate is promoted to 80%-90% by 64%-76%; Tailings fiber total loss rate is down to 0.1%-0.5% by 1.5%-2.0%, and purification disposed slurry meets the high standard requirement of client to dust index.
The above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art; to know in the utility model after contents; under the prerequisite not departing from the utility model principle; can also make some equal conversion to it and substitute, these convert on an equal basis and substitute and also should be considered as belonging to protection domain of the present utility model.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420732542.3U CN204238065U (en) | 2014-11-27 | 2014-11-27 | Cotton starch plate is produced with refinement concentration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420732542.3U CN204238065U (en) | 2014-11-27 | 2014-11-27 | Cotton starch plate is produced with refinement concentration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204238065U true CN204238065U (en) | 2015-04-01 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420732542.3U Expired - Lifetime CN204238065U (en) | 2014-11-27 | 2014-11-27 | Cotton starch plate is produced with refinement concentration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204238065U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106192508A (en) * | 2016-07-07 | 2016-12-07 | 合肥银山棉麻股份有限公司 | Four sections of desanding new technologies of two-stage |
| CN111395027A (en) * | 2019-01-03 | 2020-07-10 | 安徽雪龙纤维科技股份有限公司 | Material preparation method for cotton pulp production |
-
2014
- 2014-11-27 CN CN201420732542.3U patent/CN204238065U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106192508A (en) * | 2016-07-07 | 2016-12-07 | 合肥银山棉麻股份有限公司 | Four sections of desanding new technologies of two-stage |
| CN106192508B (en) * | 2016-07-07 | 2018-05-08 | 合肥银山棉麻股份有限公司 | Four sections of desanding new processes of two-stage |
| CN111395027A (en) * | 2019-01-03 | 2020-07-10 | 安徽雪龙纤维科技股份有限公司 | Material preparation method for cotton pulp production |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20150401 |