CN213335438U - Calcium citrate suspension drying and separating system - Google Patents
Calcium citrate suspension drying and separating system Download PDFInfo
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- CN213335438U CN213335438U CN202021561024.1U CN202021561024U CN213335438U CN 213335438 U CN213335438 U CN 213335438U CN 202021561024 U CN202021561024 U CN 202021561024U CN 213335438 U CN213335438 U CN 213335438U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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Abstract
The utility model relates to a calcium citrate suspension dry separation system, its characterized in that: comprises a feed hopper, a centrifugal kettle, a conveying auger module and a drying module; the structure of the conveying auger is arranged between the centrifugal kettle and the drying module, and the amount of calcium citrate falling into the drying module at each time is ensured by uniform conveying of the conveying auger, so that the drying with controllable flow is realized, and the problem of uneven drying of the calcium citrate is avoided; in addition, the hot air pipeline and the drying cylinder body are heated and dried by adopting an interlayer, so that a direct hot air blowing mode is avoided, and the loss of calcium citrate crystals in the drying process is avoided; and the smoke exhaust pipeline is connected with the combustor, so that the waste heat generated by combustion can be fully utilized for drying, and the energy is saved.
Description
Technical Field
The utility model relates to a calcium citrate suspension dry separation technical field especially relates to a calcium citrate suspension dry separation system.
Background
The calcium citrate is white crystalline powder, has no odor and slight hygroscopicity, is slightly soluble in water, can be dissolved in acid and is almost insoluble in ethanol, the crystalline water gradually loses water when heated to 100 ℃, and the crystalline water is completely dehydrated at 120 ℃; the calcium citrate is a food calcium enhancer, and the absorption effect is better than that of inorganic calcium; can be used for fortifying various foods, including infant formula, fruit juice, dairy products, solid beverage, sport beverage, milk, soybean milk, health products and grain products
Calcium citrate crystal can be obtained through a separation and drying mode to a calcium citrate suspension, after the common suspension is centrifugally dehydrated, the suspension is directly poured into a drying module to be dried, and the calcium citrate is easy to gather, so that the problem that the edge part is easy to transit, dry and deteriorate in a subsequent drying system, and the middle part is still very wet is caused, and the calcium citrate crystal is directly blown by hot air directly adopting heat exchange in the drying process, so that part of the crystal can be taken away along with the hot air to cause material waste.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is to provide a calcium citrate suspension dry separation system, can solve calcium citrate and directly empty the problem that gets into dry module and lead to drying inhomogeneously and carrying calcium citrate crystal to run off through hot-blast blowing after accomplishing centrifugal separation.
In order to solve the technical problem, the utility model adopts the technical scheme that: the novel point of a calcium citrate suspension drying and separating system is that: comprises a feed hopper, a centrifugal kettle, a conveying auger module and a drying module;
the feed hopper is arranged above the centrifugal kettle through a support frame, the outer wall of the feed hopper is hinged with the support frame, and the calcium citrate suspension in the feed hopper is poured into the centrifugal kettle by turning over the feed hopper;
the centrifugal kettle comprises a kettle cover, an outer barrel body, an inner net barrel, a transmission shaft and a driving motor; the kettle cover is arranged at the top end of the outer cylinder; a through hole for accommodating the transmission shaft to pass through is formed in the center of the bottom end of the outer cylinder body; a water outlet is formed in the bottom end of the side edge of the outer cylinder body; the inner net barrel is coaxially arranged in the outer barrel, the bottom end of the inner net barrel is closed and is coaxially provided with a transmission shaft, and the transmission shaft is connected to the bottom end of the outer barrel through a slewing bearing to realize that the inner net barrel rotates around the outer barrel; a transmission gear is arranged on the transmission shaft and positioned on the outer side of the outer cylinder body, and the transmission gear is connected to the output end of a driving motor through a transmission chain and drives the inner net cylinder to rotate through the driving motor;
the conveying auger module is positioned on one side of the centrifugal kettle, the conveying auger module is obliquely arranged on a support frame, the conveying auger module comprises an auger cover and a conveying auger, an input material port is formed in one end of the top of the auger cover, and an output material port is formed in one end of the bottom of the auger cover; two ends of the conveying auger are connected to the auger cover through a rotary bearing, and one end of the conveying auger extends out of the auger cover and is connected with the output end of an auger motor arranged on the support frame through a transmission chain to realize the driving of the conveying auger;
the drying module is provided with an output end of the conveying auger and comprises a drying cylinder, a hot air pipeline and a burner; the drying cylinder is provided with a feed inlet, a discharge outlet and a moisture discharge outlet, and the feed inlet is butted with an output material outlet of the conveying auger module; the drying cylinder is arranged in the hot air pipeline, a feed inlet and a discharge outlet of the drying cylinder respectively penetrate out of the hot air pipeline, and a drying interlayer is formed between the inner wall of the hot air pipeline and the outer wall of the drying cylinder; one end of the hot air pipeline is communicated with the atmosphere, the other end of the hot air pipeline is connected to a smoke exhaust pipeline of the combustor, and the calcium citrate in the drying cylinder is heated and dried through waste heat of the smoke exhaust pipeline.
Furthermore, the middle of the bottom end of the outer cylinder body is inwards sunken to form a groove structure.
The utility model has the advantages that:
1) the structure of the conveying auger is arranged between the centrifugal kettle and the drying module, and the amount of calcium citrate falling into the drying module at each time is ensured by uniform conveying of the conveying auger, so that the drying with controllable flow is realized, and the problem of uneven drying of the calcium citrate is avoided; in addition, the hot air pipeline and the drying cylinder body are heated and dried by adopting an interlayer, so that a direct hot air blowing mode is avoided, and the loss of calcium citrate crystals in the drying process is avoided; and the smoke exhaust pipeline is connected with the combustor, so that the waste heat generated by combustion can be fully utilized for drying, and the energy is saved.
Drawings
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
Fig. 1 is a structural diagram of a calcium citrate suspension drying and separating system of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention, as generally described and illustrated in the figures herein, may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the present invention, presented in the accompanying drawings, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like indicate the position or positional relationship based on the position or positional relationship shown in the drawings, or the position or positional relationship which is usually placed when the product of the present invention is used, and are only for convenience of description and simplification of the description, but do not indicate or imply that the device or element referred to must have a specific position, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," "third," and the like are used solely to distinguish one from another and are not to be construed as indicating or implying relative importance.
Furthermore, the terms "horizontal", "vertical" and the like do not imply that the components are required to be absolutely horizontal or pendant, but rather may be slightly inclined. For example, "horizontal" merely means that the direction is more horizontal than "vertical" and does not mean that the structure must be perfectly horizontal, but may be slightly inclined.
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The drying and separating system for the calcium citrate suspension shown in figure 1 comprises a feed hopper 1, a centrifugal kettle 2, a conveying auger module 3 and a drying module 4.
Feed hopper 1 passes through the support frame setting in the top of centrifugation cauldron 2, and the outer wall of feed hopper 1 is articulated with a support frame, realizes empting the calcium citrate suspension in the feed hopper 1 into in the centrifugation cauldron 2 through upset feed hopper 1.
The centrifugal kettle 2 comprises a kettle cover 21, an outer cylinder 22, an inner net cylinder 23, a transmission shaft 24 and a driving motor 25; the kettle cover 21 is arranged at the top end of the outer cylinder 22; a through hole for allowing the transmission shaft 24 to pass through is formed in the center of the bottom end of the outer cylinder 22, and the middle of the bottom end of the outer cylinder 22 is sunken inwards to form a groove structure, so that water drainage is facilitated; a water outlet is arranged at the bottom end of the side edge of the outer cylinder body 22; the inner net cylinder 23 is coaxially arranged in the outer cylinder 22, the bottom end of the inner net cylinder 23 is closed and is coaxially provided with the transmission shaft 24, and the transmission shaft 24 is connected to the bottom end of the outer cylinder 22 through a rotary bearing to realize that the inner net cylinder 23 rotates around the outer cylinder 22; the transmission shaft 24 is provided with a transmission gear on the outer side of the outer cylinder 22, and the transmission gear is connected to the output end of the driving motor 25 through a transmission chain, and the driving motor 25 drives the inner net cylinder 23 to rotate.
The conveying auger module 3 is positioned at one side of the centrifugal kettle 2, the conveying auger module 3 is obliquely arranged on a support frame, the conveying auger module 3 comprises an auger cover 31 and a conveying auger 32, an input port is formed at one end of the top of the auger cover 31, and an output port is formed at one end of the bottom of the auger cover 31; two ends of the conveying auger 32 are connected to the auger cover 31 through a rotary bearing, and one end of the conveying auger 32 extends out of the auger cover 31 and is connected with the output end of an auger motor arranged on the support frame through a transmission chain to realize the driving of the conveying auger 32.
The drying module 4 is provided with an output end of the conveying auger 32, and the drying module 4 comprises a drying cylinder 41, a hot air pipeline 42 and a burner 43; a feed inlet, a discharge outlet and a moisture discharge outlet are formed in the drying cylinder 41, and the feed inlet is butted with an output material outlet of the conveying auger module 3; the drying cylinder 41 is arranged in the hot air pipeline 42, a feed inlet and a discharge outlet of the drying cylinder 41 respectively penetrate out of the hot air pipeline 42, and a drying interlayer is formed between the inner wall of the hot air pipeline 42 and the outer wall of the drying cylinder 41; one end of the hot air pipeline 42 is communicated with the atmosphere, the other end of the hot air pipeline 42 is connected to a smoke exhaust pipeline of the burner 43, and the calcium citrate in the drying cylinder 41 is heated and dried through the waste heat of the smoke exhaust pipeline.
The utility model discloses a theory of operation is: pouring the calcium citrate suspension into a centrifugal kettle through a feed hopper, rotating a mesh drum under the drive of a drive motor to separate suspended calcium citrate from water, and discharging the water through a water outlet; moist calcium citrate is taken out and is stably and uniformly conveyed through the conveying auger module to enter the drying cylinder, the exhaust pipe residual heat of the combustor heats the drying cylinder, the drying of the calcium citrate is realized, and generated moisture is discharged out of the drying cylinder through the moisture discharging port.
It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (2)
1. A calcium citrate suspension drying and separating system is characterized in that: comprises a feed hopper, a centrifugal kettle, a conveying auger module and a drying module;
the feed hopper is arranged above the centrifugal kettle through a support frame, the support frame is hinged to the outer wall of the feed hopper, and the calcium citrate suspension in the feed hopper is poured into the centrifugal kettle by turning over the feed hopper;
the centrifugal kettle comprises a kettle cover, an outer barrel body, an inner net barrel, a transmission shaft and a driving motor; the kettle cover is arranged at the top end of the outer cylinder; a through hole for accommodating the transmission shaft to pass through is formed in the center of the bottom end of the outer cylinder body; a water outlet is formed in the bottom end of the side edge of the outer cylinder body; the inner net barrel is coaxially arranged in the outer barrel, the bottom end of the inner net barrel is closed and is coaxially provided with a transmission shaft, and the transmission shaft is connected to the bottom end of the outer barrel through a slewing bearing to realize that the inner net barrel rotates around the outer barrel; a transmission gear is arranged on the transmission shaft and positioned on the outer side of the outer cylinder body, and the transmission gear is connected to the output end of a driving motor through a transmission chain and drives the inner net cylinder to rotate through the driving motor;
the conveying auger module is positioned on one side of the centrifugal kettle, the conveying auger module is obliquely arranged on a support frame, the conveying auger module comprises an auger cover and a conveying auger, an input material port is formed in one end of the top of the auger cover, and an output material port is formed in one end of the bottom of the auger cover; two ends of the conveying auger are connected to the auger cover through a rotary bearing, and one end of the conveying auger extends out of the auger cover and is connected with the output end of an auger motor arranged on the support frame through a transmission chain to realize the driving of the conveying auger;
the drying module is provided with an output end of the conveying auger and comprises a drying cylinder, a hot air pipeline and a burner; the drying cylinder is provided with a feed inlet, a discharge outlet and a moisture discharge outlet, and the feed inlet is butted with an output material outlet of the conveying auger module; the drying cylinder is arranged in the hot air pipeline, a feed inlet and a discharge outlet of the drying cylinder respectively penetrate out of the hot air pipeline, and a drying interlayer is formed between the inner wall of the hot air pipeline and the outer wall of the drying cylinder; one end of the hot air pipeline is communicated with the atmosphere, the other end of the hot air pipeline is connected to a smoke exhaust pipeline of the combustor, and the calcium citrate in the drying cylinder is heated and dried through waste heat of the smoke exhaust pipeline.
2. The system for drying and separating a calcium citrate suspension according to claim 1, wherein: the middle of the bottom end of the outer cylinder body is inwards sunken to form a groove structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021561024.1U CN213335438U (en) | 2020-07-31 | 2020-07-31 | Calcium citrate suspension drying and separating system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021561024.1U CN213335438U (en) | 2020-07-31 | 2020-07-31 | Calcium citrate suspension drying and separating system |
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| CN213335438U true CN213335438U (en) | 2021-06-01 |
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| CN202021561024.1U Active CN213335438U (en) | 2020-07-31 | 2020-07-31 | Calcium citrate suspension drying and separating system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228180A (en) * | 2022-06-28 | 2022-10-25 | 山东信科环化有限责任公司 | High-efficient separator of barium chloride crystallization |
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2020
- 2020-07-31 CN CN202021561024.1U patent/CN213335438U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228180A (en) * | 2022-06-28 | 2022-10-25 | 山东信科环化有限责任公司 | High-efficient separator of barium chloride crystallization |
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