CN212404124U - Device for removing sucrose starch and acidic flocculate - Google Patents
Device for removing sucrose starch and acidic flocculate Download PDFInfo
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- CN212404124U CN212404124U CN202021482596.0U CN202021482596U CN212404124U CN 212404124 U CN212404124 U CN 212404124U CN 202021482596 U CN202021482596 U CN 202021482596U CN 212404124 U CN212404124 U CN 212404124U
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Abstract
The utility model discloses a device for getting rid of sucrose starch and acid flocculation thing, get rid of the jar including starch, be equipped with overflow pipe and import pipe on the outer wall of starch removal jar upper end, the buffer bin intercommunication of a set of order connection that is equipped with in import pipe and the starch removal jar, be equipped with annular overflow launder in the starch removal jar, buffer bin export and annular overflow launder intercommunication, starch is equipped with the sediment of scraping of taking first gear motor in getting rid of the jar and is scraped bubble device, starch removal tank bottoms portion is equipped with and gets rid of the leakage pipe and a set of first blow-off pipe of jar intercommunication with starch, starch is got rid of and is equipped with the play juice groove that starch was got rid of the jar respectively in the jar both ends end, the one end that goes out the juice groove and wear out the starch removal jar is equipped with and goes out. The device can remove the starch content in the cane sugar, reduce the adverse effect of the starch and the acidic flocculate on the cane sugar making process and the obtained sugar products, and avoid scale formation in the evaporating pot and the sugar boiling pot caused by acid-base reaction lag.
Description
Technical Field
The utility model relates to an industrial sugar-making equipment, in particular to a device for removing sucrose starch and acidic flocculate in the production process of a sugar-making one-step method and a sugar-making two-step method.
Background
During the growth of sugar cane, both starch and sucrose are present in sugar cane as a storage component and starch content is strongly related to planting area, climate, sugar cane variety and harvest time. Starch is a high molecular condensate of glucose, with molecular weights ranging from tens of thousands to millions. The natural starch exists in a granular state, is insoluble in cold water and is in a suspension state, the natural starch absorbs water to expand when being heated, the natural starch is gelatinized to form a viscous paste when exceeding a certain temperature, and the gelatinized starch is a typical hydrophilic colloidal substance and has stable chemical properties and can not be coagulated or precipitated by a common method. The research shows that the starch in the cane juice is heated and dissolved to form sticky paste, so that the viscosity of the cane juice is increased, the filtering performance of the cane juice is influenced, the sedimentation efficiency is reduced, the crystallization of cane sugar is further hindered, the sugar boiling time is increased, the product color value and the yield of waste honey are increased, and the loss of cane sugar is caused and the quality of sugar products is influenced. In addition, the excessive content of starch in the white granulated sugar can also increase the turbidity of downstream products, generate acidic flocculate, influence the product quality and prevent sugar products from entering high-end food fields such as beverages, pharmacy and the like.
The sugarcane inevitably carries a lot of sugarcane tips and sugarcane leaves in the harvesting process, particularly after the sugarcane is mechanically harvested, the content of the sugarcane tips and the sugarcane leaves in the sugarcane is larger, starch is mainly concentrated in the sugarcane tips and the sugarcane leaves, the content of the starch in sugarcane juice is greatly increased, and the adverse effect on the sugarcane sugar manufacturing process and the obtained sugar products is generated if the starch is not removed. In the prior sugar production, starch content is usually removed by adding complex enzyme clarifiers of sugar industry such as alpha-glucanase, pectinase, amylase and the like, which are influenced by unbalanced production and operation and the like, the removal rate is not high, the complex enzyme clarifiers cannot be completely removed, the cost is high, and the production cost, the operation and maintenance cost and the like are increased; and residual amylase can have certain influence on downstream products, so that the starch content in the downstream products is changed, and the stability of the properties of the downstream products is influenced, such as the viscosity of yoghourt or starch pudding products. Therefore, when applying amylase in sugar industry of sugarcane, not only the starch removal rate is ensured, but also the residual problem of amylase in sugar products is concerned, and the extra addition of amylase is not a very ideal way for removing starch.
If a complex enzyme clarifying agent is not required to be added in the sugar production, the quality of sugar products is not influenced due to the residue problem caused by amylase, but the starch can be effectively removed through a clarifying container, the starch content in the cane sugar is reduced, the adverse influence of the starch on the sugar making process of the cane sugar and the obtained sugar products is reduced, the investment is low, the production cost is not increased, and the method is equipment urgently needed by the mechanized process of the sugar industry at present and in the future.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a device for removing sucrose starch and acidic flocculate aiming at the defects existing in the prior art. The device can remove the starch content in cane sugar in a one-step method or a two-step method for sugar production, reduce the adverse effect of starch and acid floc on a cane sugar production process and obtained sugar products, and avoid scale formation in an evaporating pot and a sugar boiling pot caused by acid-base reaction lag.
Realize the utility model discloses the technical scheme of purpose is:
a device for removing sucrose starch and acidic flocs comprises a starch removing tank, wherein an overflow pipe and an inlet pipe are arranged on the outer wall of the upper end part of the starch removing tank, the overflow pipe is communicated with the cylinder of the starch removing tank, the inlet pipe is communicated with a group of sequentially connected buffer tanks arranged in the starch removing tank, an annular overflow tank is arranged in the starch removing tank, the outlet of the buffer tank is communicated with the annular overflow tank, a slag and bubble scraping device with a first speed reducing motor is arranged in the starch removing tank, the first speed reducing motor is positioned on the outer wall of the starch removing tank, a first exhaust pipe and a group of first manholes which are communicated with the starch removing tank are arranged on the outer wall of the upper end part of the starch removing tank, an outer leakage pipe and a group of first drainage pipes which are communicated with the starch removing tank are arranged at the bottom part of the starch removing tank, end heads of the starch removing tank are respectively penetrated out, a first juice outlet pipe communicated with the juice outlet, the other end of the slag scraping and foaming device is communicated with the external drainage pipe, and slag in the slag scraping and foaming device is used for scraping and stirring the sediment in the annular overflow groove to avoid the sediment from accumulating in the groove; scrape and scrape among the bubble device scrape the bubble and be used for scraping starch and get rid of the dross and the foam on jar internal mixed cane juice surface, discharge dross and foam through going out the juice groove, first manhole is used for examining starch and gets rid of the jar interior condition.
The starch removing tank body is cylindrical, the upper end of the starch removing tank body is outwards conical or flat, the lower end of the starch removing tank body is outwards conical or flat, and the inclination of the conical shape is 10-45 degrees.
The connecting part of the leakage pipe and the juice outlet groove is provided with a cylindrical control valve, and the juice outlet amount is adjusted through the cylindrical control valve.
According to the technical scheme, in the sugar-making one-step method, the output ends of the first juice outlet pipe and the overflow pipe extend into the mixed juice box.
In the two-step sugar-making method, the output end of the first juice outlet pipe is communicated with the lower end part of the lime mixing tank, the end part of the juice outlet groove connected with the first juice outlet pipe is provided with a lime or calcium saccharified adding pipe, and the rest structures are the same as the one-step sugar-making method.
The lime blending tank upper end outer wall is equipped with the second play juice pipe with intercommunication in the lime blending tank, be equipped with on the lime blending tank upper end outer wall with the second blast pipe and the second manhole of intercommunication in the lime blending tank, be equipped with the agitator of taking second gear motor in the lime blending tank, second gear motor is located the lime blending tank outer wall, the second goes out the juice pipe and stretches into main ash bin with the output of overflow pipe.
And a second sewage discharge pipe is arranged at the bottom of the lime mixing tank.
The diameter of the starch removing tank is 3000 mm-8000 mm, and the height of the starch removing tank is 3000 mm-12000 mm.
The second exhaust pipe is the same as the first exhaust pipe in specification, the diameter of the first exhaust pipe is larger than or equal to 100mm, the length of the first exhaust pipe is 1000 mm-4000 mm, the diameter of the first juice outlet pipe is 100 mm-600 mm, and the diameter of the overflow pipe is larger than or equal to 200mm in the middle.
The diameter of the leakage pipe is 100 mm-800 mm, the diameter of the cylindrical control valve is more than or equal to 100mm in the middle and 100 mm-800 mm in height.
The capacity of the buffer tank is more than or equal to 0.5m3。
The width of the annular overflow groove is larger than or equal to 100mm, the height of the annular overflow groove is larger than or equal to 100mm, the width of the juice outlet groove is larger than or equal to 100mm, the height of the juice outlet groove is larger than or equal to 100mm, the end part of the juice outlet groove connected with the leakage pipe inclines towards the end part connected with the first juice outlet pipe, and the inclination angle is 0-45 degrees.
The lime mixing tank body is cylindrical, the diameter of the lime mixing tank body is 1000 mm-6000 mm, the height of the lime mixing tank body is 1000 mm-12000 mm, the upper end of the lime mixing tank body is outwards conical or flat, the lower end of the lime mixing tank body is outwards conical or flat, and the inclination of the conical shape is 10-45 degrees.
The diameter of the second juice outlet pipe is 50 mm-600 mm.
The diameter of the blow-off pipe is 20 mm-500 mm.
The device in the technical scheme is made of carbon steel or stainless steel.
In the process flow of the sugar making one-step method, the starch removing tank is assembled in front of the juice mixing box after the mixed juice is heated for one time, the device of the technical scheme can efficiently remove the starch content, improve the clarification process effect and reduce the scale formation in the evaporating tank and the sugar boiling tank after the acid-base reaction lag.
In the raw sugar production process flow of the sugar making two-step method, the starch removal tank and the lime mixing tank of the technical scheme are assembled in front of the main ash box after the mixed juice is heated for one time, and the neutralization main ash (lime milk) is added into the device of the technical scheme.
The device can remove the starch content in the cane sugar, reduce the adverse effect of the starch and the acidic flocculate on the cane sugar making process and the obtained sugar products, and avoid scale formation in the evaporating pot and the sugar boiling pot caused by acid-base reaction lag.
Drawings
FIG. 1 is a schematic diagram of a structure in a sugar production one-step process according to an embodiment;
FIG. 2 is a top view of FIG. 1;
FIG. 3 is a schematic diagram of the structure of a two-step process for sugar production according to an embodiment;
FIG. 4 is a top view of FIG. 3;
FIG. 5 is a schematic view of a process flow of a sugar-making one-step method;
FIG. 6 is a schematic process flow diagram of a two-step sugar manufacturing process.
In the figure, 1, a starch removal tank 2, an overflow pipe 3, a first juice outlet pipe 4, an inlet pipe 5, a buffer tank 6, an annular overflow tank 7, a slag scraping and bubble scraping device 71, a first speed reduction motor 8, a first exhaust pipe 9, a first manhole 10, an outer discharge pipe 11, a cylinder control valve 12, a juice outlet tank 13, a mixed juice tank 14, a lime mixing tank 15, a lime or calcium saccharate adding pipe 16, a second juice outlet pipe 17, a second manhole 18, a stirrer 181, a second speed reduction motor 19, a main ash tank 20, a first sewage discharge pipe 21, a second sewage discharge pipe 22 and a second exhaust pipe.
Detailed Description
The present invention will be described in further detail with reference to the following drawings and specific embodiments, but the present invention is not limited thereto.
Example (b):
a device for removing sucrose starch and acidic flocculate comprises a starch removing tank 1, an overflow pipe 2 and an inlet pipe 4 are arranged on the outer wall of the upper end part of the starch removing tank 1, the overflow pipe 2 is communicated with a barrel of the starch removing tank 2, the inlet pipe 4 is communicated with a group of sequentially connected buffer tanks 5 arranged in the starch removing tank 1, annular overflow tanks 6 are arranged in the starch removing tank 1, outlets of the buffer tanks 5 are communicated with the annular overflow tanks 6, a slag scraping and bubble scraping device 7 with a first speed reducing motor 71 is arranged in the starch removing tank 1, the first speed reducing motor 71 is positioned on the outer wall of the starch removing tank 1, a first exhaust pipe 8 and a group of first manhole 9 which are communicated with the starch removing tank 1 are arranged on the outer wall of the upper end part of the starch removing tank 1, an outer drainage pipe 10 and a group of first drainage pipe 20 which are communicated with the starch removing tank 1 are arranged at the bottom of the starch removing tank 1, and a juice outlet groove 12, one end of the juice outlet groove 12, which penetrates out of the starch removal tank 1, is provided with a first juice outlet pipe 3 communicated with the juice outlet groove 12, the other end of the juice outlet groove is communicated with an external drainage pipe 10, and the slag in the slag scraping and foaming device 7 is used for scraping and stirring the sediment in the annular overflow groove 6 to prevent the sediment from being accumulated in the annular overflow groove 6; the scum scraping and foaming device 7 is used for scraping scum and foam on the surface of the mixed cane juice in the starch removing tank 1 and discharging the scum and the foam through the juice outlet tank 12 and the first juice outlet pipe 3.
The starch removing tank 1 is cylindrical, the upper end of the starch removing tank is outward conical or flat, the lower end of the starch removing tank is outward conical or flat, the inclination of the conical shape is 10-45 degrees, the angle of the conical shape of the upper end of the starch removing tank 1 is 15 degrees, the lower end of the starch removing tank is outward conical, and the inclination of the conical shape is 45 degrees.
A cylinder control valve 11 is arranged at the connecting part of the leakage pipe 10 and the juice outlet groove 12, and the juice outlet amount is adjusted through the cylinder control valve 11.
In the sugar-making one-step method of the device, the output ends of the first juice outlet pipe 3 and the overflow pipe 2 extend into the mixed juice box 13.
In the two-step sugar-making method, the output end of the first juice outlet pipe 3 is communicated with the lower end part of a lime mixing tank 14, the end part of the juice outlet groove 11 connected with the first juice outlet pipe 3 is provided with a lime or calcium saccharified adding pipe 15, and the rest structures are the same as the one-step sugar-making method.
The outer wall of the upper end of the lime mixing tank 14 is provided with a second juice outlet pipe 16 communicated with the lime mixing tank 14, the outer wall of the upper end of the lime mixing tank 14 is provided with a second exhaust pipe 22 and a second manhole 17 communicated with the lime mixing tank 14, the lime mixing tank 14 is internally provided with a stirrer 18 with a second speed reducing motor 181, the second speed reducing motor 181 is positioned on the outer wall of the lime mixing tank 14, and the output ends of the second juice outlet pipe 16 and the overflow pipe 2 extend into the main ash box 19.
And a second sewage draining pipe 21 is arranged at the bottom of the lime mixing tank 14.
The diameter of the starch removing tank 1 is 3000 mm-8000 mm, the height is 3000 mm-12000 mm, the diameter of the starch removing tank 1 is 6500mm, and the height is 9000 mm.
The second exhaust pipe 22 and the first exhaust pipe 8 are identical in specification, the diameter of the first exhaust pipe 8 is larger than or equal to 100mm, the length of the first exhaust pipe 8 is 1000 mm-4000 mm, the diameter of the first exhaust pipe 8 is 400mm, the length of the first exhaust pipe is 2000mm, the diameter of the first juice outlet pipe 3 is 100 mm-600 mm, the diameter of the overflow pipe 2 is larger than or equal to 200mm, the diameter of the first juice outlet pipe 3 is 600mm, and the diameter of the overflow pipe 2 is 650 mm.
The diameter of the leakage pipe 10 is 100 mm-800 mm, the diameter of the leakage pipe 10 is 500mm, the diameter of the cylinder control valve 11 is more than or equal to 100mm in the front and 100 mm-800 mm in the height, and the diameter of the cylinder control valve 11 is 480mm and 700mm in the height.
The capacity of the buffer box 5 is more than or equal to 0.5m3The buffer tank 5 of this example has a capacity of 1.9 m3。
The width of the annular overflow groove 6 is more than or equal to 100mm, the height of the annular overflow groove 6 is more than or equal to 100mm, the width of the juice outlet groove 12 is more than or equal to 100mm, the height of the juice outlet groove 12 is more than or equal to 100mm, the width of the juice outlet groove 12 is 750mm, the height of the juice outlet groove is 1000mm, the end part of the juice outlet groove 12 communicated with the outer leakage pipe 10 is inclined towards the end part communicated with the first juice outlet pipe 3, the inclination angle is 0-45 degrees, and the inclination angle is 15 degrees in the embodiment.
The lime mixing tank 14 is cylindrical, the diameter is 1000 mm-6000 mm, the height is 1000 mm-12000 mm, the upper end is outward conical or flat, the lower end is outward conical or flat, the conical inclination is 10-45 degrees, the diameter of the lime mixing tank 14 is 2500mm, the height is 5000mm, the inclination of the upper end outward conical is 15 degrees, and the lower end is flat.
The diameter of the second juice outlet pipe 16 is 50 mm-600 mm, and the diameter of the second juice outlet pipe 16 is 600 mm.
The diameter of the second sewage discharge pipe 21 is 20 mm-500 mm, and the diameter of the second sewage discharge pipe 21 is 150 mm.
The material of the device is carbon steel or stainless steel.
In the process flow of the sugar making one-step method, the starch removing tank 1 of the device is assembled in front of the mixed juice box 13 after the mixed juice is heated for one time, the device can efficiently remove the starch content, improve the clarification process effect, reduce the scale formation in the evaporating tank and the sugar boiling tank after the acid-base reaction lag, and the process flow of the sugar making one-step method is shown in figure 5.
In the process flow of the raw sugar production of the two-step sugar making method, the starch removing tank 1 and the lime mixing tank 14 of the device of the embodiment are assembled in front of the main ash box 19 after the mixed juice is heated for one time, and the neutralization main ash (lime milk) is added into the device of the embodiment, the device of the embodiment has the function of efficiently removing the starch content, and can also ensure that the added lime milk and the pre-ash cane juice are mixed more uniformly, the mixed flow is controlled by liquid level, so that the lime milk and the pre-ash cane juice have sufficient reaction time, the process index PH value is ensured to be balanced and stable, the cane juice reacts more fully and completely, the clarification process effect and the filtering performance of mud juice are improved, the scale formation in the evaporating tank and the sugar boiling tank due to acid-base reaction lag is reduced, and the process flow of the two-step sugar making method is shown in.
The capacity of the device is different according to different daily squeezing amounts, the starch removing tank 1 is designed according to the squeezing amount, sugarcane growth areas, starch content and the like, and the capacity is about 50% -70% of the sugarcane squeezing amount per hour; the lime mixing tanks 14 are designed to control the amount of squeezed sugar cane and the effective content of calcium oxide in lime milk or calcium saccharified, and the amount of squeezed sugar cane is about 3% of the amount of squeezed sugar cane per hour. The main body of the starch removing tank 1 is a cylinder, the bottom of the starch removing tank is conical, so that amylase is activated and starch is degraded more completely under the dynamic and static combined states of 'torrent, turbulence, advection' and the like of cane juice. The lime mixing tank 14 is a cylinder, the lower part of the lime mixing tank can be flat-bottomed or conical-bottomed, a stirrer 18 is arranged in the lime mixing tank, so that cane juice and lime are mixed more fully, the reaction is more complete, the pH value is more stable, the fluctuation peak value is smaller, and the lime lag reaction caused by uneven lime adding or incomplete reaction is reduced.
The following is further illustrated by the two-step method for sugar production:
the two-step method for preparing sugar comprises the following working steps:
the first step is as follows: mixing, squeezing juice, pre-ashing, adding phosphorus, feeding the primarily heated mixed juice into a buffer tank 5 through an inlet pipe 4 under the pressure action of a delivery pump, decompressing the mixed juice into advection, fully mixing the mixed juice, feeding the mixed juice into an annular overflow tank 6, and slowly flowing the mixed juice into the bottom of a starch removal tank 1 from the upper part;
the second step is that: performing reaction degradation, uniformly distributing the mixed juice flowing into the starch removal tank 1, slowly flowing into the bottom of the starch removal tank 1 from the annular overflow groove 6, and standing for 30 minutes through reaction, degradation, separation and the like to activate amylase and degrade starch;
the third step: adding lime, namely adjusting the mixed juice flowing out of an outlet pipe 10 at the bottom of the starch removing tank 1 through a cylinder control valve 11 to enter a juice outlet tank 12, adding lime or calcium saccharate into the juice outlet tank 12 through a lime or calcium saccharate adding pipe 15, wherein the pH value of the lime or calcium saccharate is 7.6-8.4, and then flowing into a lime mixing tank 14;
the fourth step: the lime and the mixed juice enter the lime mixing tank 14 from the lower part of the lime mixing tank 14 for complete reaction, and are fully mixed and completely reacted in the lime mixing tank 14 to meet the process index requirements, so that the starch is degraded again, and meanwhile, the lime lag reaction caused by uneven lime feeding or incomplete reaction is reduced;
the fifth step: the cane juice, which is well mixed and fully reacted by the lime mixing tank 14, flows out of the second juice outlet pipe 16 into the main ash bin 19.
Claims (7)
1. A device for removing sucrose starch and acidic flocs is characterized by comprising a starch removing tank, wherein an overflow pipe and an inlet pipe are arranged on the outer wall of the upper end part of the starch removing tank, the overflow pipe is communicated with the cylinder of the starch removing tank, the inlet pipe is communicated with a group of sequentially connected buffer tanks arranged in the starch removing tank, an annular overflow tank is arranged in the starch removing tank, the outlet of the buffer tank is communicated with the annular overflow tank, a slag scraping and foaming device with a first speed reducing motor is arranged in the starch removing tank, the first speed reducing motor is positioned on the outer wall of the starch removing tank, a first exhaust pipe and a group of first manholes which are communicated with the starch removing tank are arranged on the outer wall of the upper end part of the starch removing tank, an outer leakage pipe and a group of first drainage pipes which are communicated with the starch removing tank are arranged at the bottom of the starch removing tank, and juice, one end of the juice outlet groove penetrating through the starch removing tank is provided with a first juice outlet pipe communicated with the juice outlet groove, and the other end of the juice outlet groove is communicated with the leakage pipe.
2. The apparatus of claim 1 wherein the starch removal tank body is cylindrical, has an upper end tapered or flat outwardly and a lower end tapered or flat outwardly.
3. The apparatus as claimed in claim 1, wherein the connection between the drain and the juice outlet tank is provided with a cylinder control valve.
4. The apparatus of claim 1, wherein the first juice outlet pipe and the overflow pipe extend into the mixing tank at the output end of the first juice outlet pipe and the overflow pipe in the sugar manufacturing one-step method.
5. The apparatus of claim 1, wherein the first juice outlet pipe has an outlet end connected to the lower end of the lime mixing tank, and the lime or calcium saccharified solution inlet pipe is provided at the end of the juice outlet tank connected to the first juice outlet pipe.
6. The apparatus as claimed in claim 5, wherein the lime mixing tank has a second juice outlet pipe on the outer wall of the upper end thereof, the second outlet pipe is connected to the lime mixing tank, the lime mixing tank has a second air outlet pipe and a second manhole on the outer wall of the upper end thereof, the lime mixing tank has a stirrer with a second speed reduction motor on the outer wall thereof, and the second juice outlet pipe and the outlet of the overflow pipe extend into the main dust box.
7. The apparatus for removing sucrose starch and acidic floes as in claim 5, wherein a second blowdown is provided at the bottom of the lime mixing tank.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202021482596.0U CN212404124U (en) | 2020-07-24 | 2020-07-24 | Device for removing sucrose starch and acidic flocculate |
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| CN202021482596.0U CN212404124U (en) | 2020-07-24 | 2020-07-24 | Device for removing sucrose starch and acidic flocculate |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111690779A (en) * | 2020-07-24 | 2020-09-22 | 广西飞鹏节能环保科技有限公司 | Device for removing sucrose starch and acidic flocculate |
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2020
- 2020-07-24 CN CN202021482596.0U patent/CN212404124U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111690779A (en) * | 2020-07-24 | 2020-09-22 | 广西飞鹏节能环保科技有限公司 | Device for removing sucrose starch and acidic flocculate |
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