CN204238065U - Cotton starch plate is produced with refinement concentration equipment - Google Patents
Cotton starch plate is produced with refinement concentration equipment Download PDFInfo
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- 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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Abstract
The utility model discloses a kind of cotton starch plate production refinement concentration equipment, comprise one, 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 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 tailings outlet of four sections of recovery device for tailings is connected with tailings gathering-device, above-mentioned refinement concentration equipment is adopted 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.
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)
1. a 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.
2. cotton starch plate production refinement concentration equipment according to claim 1, it is characterized in that: 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.
3. cotton starch plate production refinement concentration equipment according to claim 1 and 2, is characterized in that: the good slurry outlet of secondary desanding device is connected with cylinder enrichment facility.
4. cotton starch plate production refinement concentration equipment according to claim 2, is characterized in that: refinement concentration equipment also comprises stuff box, being provided with the desilting ditch for tentatively removing impurity in slurry between stuff box and one-level middle tone stock tank.
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CN201420732542.3U CN204238065U (en) | 2014-11-27 | 2014-11-27 | Cotton starch plate is produced with refinement concentration equipment |
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CN201420732542.3U CN204238065U (en) | 2014-11-27 | 2014-11-27 | Cotton starch plate is produced with refinement concentration equipment |
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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 active Active
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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