CN212914644U - Humic acid liquid continuous high-efficiency dynamic settler - Google Patents
Humic acid liquid continuous high-efficiency dynamic settler Download PDFInfo
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- CN212914644U CN212914644U CN202021271250.6U CN202021271250U CN212914644U CN 212914644 U CN212914644 U CN 212914644U CN 202021271250 U CN202021271250 U CN 202021271250U CN 212914644 U CN212914644 U CN 212914644U
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Abstract
The utility model discloses a continuous high-efficient dynamic settler of humic acid liquid, including the settler main part, the inside central authorities pipe that is equipped with of settler main part, central authorities 'pipe is located settler main part middle part, central authorities' pipe below is equipped with the cone and returns the radials, the cone returns the radials bottom and is equipped with the radiant panel, be equipped with one-level heater, secondary heater and tertiary heater in the settler main part, tertiary heater, secondary heater and one-level heater from the top down are arranged the setting in proper order inside the settler main part, the inside top of settler main part is equipped with the annular and gathers the groove. The utility model discloses an adopt the heating, subside, separation integral type structure, the heater does not have area, and rotten liquid pipe need not to increase the heat preservation, has correspondingly reduced the heat loss, and the operating personnel centralized management of being convenient for adopts tertiary heating method, reduces solution viscosity, shortens the settling time, and the sediment is thorough, and the sediment is discharged through the scum pipe, avoids the sedimentation tank clearance difficulty.
Description
Technical Field
The utility model relates to a fertilizer production correlation technique field specifically is a high-efficient dynamic settler in succession of humic acid liquid.
Background
Humic acid is a slow release agent and a stabilizer of a nitrogen fertilizer, a synergist of a phosphate fertilizer and a protector of a potassium fertilizer, is a blending agent and a chelating agent of medium and trace elements, and has obvious synergistic effect on a chemical fertilizer; preparing a product containing a large amount of humic acid, nitrogen, phosphorus, potassium and certain trace elements required by the growth and development of crops, wherein the lignite contains rich humic acid, and the humic acid has the highest organic matter content and is a soil conditioner and a synergistic sustained-release agent of a fertilizer; the humic acid is combined with the fertilizer to realize the integrated effect of soil nutrients, which is a specific effect that any fertilizer does not have, and can inhibit the volatilization and loss of the active ingredients of the fertilizer. Humic acid can improve soil, regulate plant growth and activate plant cell activity, and the clear liquid of humic acid after sedimentation treatment can be combined with traditional inorganic fertilizer, compound fertilizer and urea to prepare fertilizer with better water solubility, and has obvious advantages. The fertilizer is a quick-acting fertilizer, has good water solubility and no residue, can be completely dissolved in water, has higher effective absorption efficiency than the common fertilizer, has quick fertilizer efficiency, and can meet the nutritional requirement of high-yield crops in a quick growth period. Can cooperate drip irrigation, sprinkler irrigation system to realize water, fertile with exerting to the hosepipe is fertile, and the operation of fertilizeing can need not artifically, practices thrift the hand labor cost greatly, has been realized the importance of humic acid fertilizer by more and more soil expert, fertilizer expert, agricultural technology popularization expert, agricultural fund distributor, agricultural science and technology personnel, crop farming, peasant realization.
The existing humic acid liquid is high in concentration and viscosity, so that the sedimentation speed is low, a heater is used for heating the humic acid liquid to a temperature below the boiling point to reduce the viscosity of the humic acid liquid, and then the humic acid liquid enters a settler to accelerate the sedimentation speed of the humic acid liquid.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a high-efficient dynamic settler in succession of humic acid liquid, because concentration is high with the present humic acid liquid that mentions in solving above-mentioned background art, viscosity is high, consequently, the settling rate is slow, so use the heater at first to heat it to the temperature below the boiling point, reduce its viscosity, then get into the settler, can accelerate its settling rate, nevertheless owing to increased one set of heater, consequently, the investment is big, area is big, also convenient centralized management, and when present humic acid liquid adopts the sedimentation tank to deposit, can not accomplish continuous sedimentation, and deposit the impurity that produces many, the sedimentation tank clearance difficulty, the problem that intensity of labour is big.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a continuous high-efficient dynamic settler of humic acid liquid, includes the settler main part, the inside central authorities pipe that is equipped with of settler main part, central authorities pipe is located settler main part middle part, central authorities pipe below is equipped with the cone and returns the radials, the cone returns the radials bottom and is equipped with the radiant panel, be equipped with primary heater, secondary heater and tertiary heater in the settler main part, tertiary heater, secondary heater and primary heater from the top down arrange in proper order and set up inside the settler main part, the inside top of settler main part is equipped with the annular and gathers the groove, the annular is gathered and is equipped with the outage on the groove lateral wall, the inside scum pipe that is equipped with of settler main part, the scum pipe is located central authorities pipe one side.
Preferably, the primary heater, the secondary heater and the tertiary heater are all arranged by adopting disc pipes, and the primary heater, the secondary heater and the tertiary heater are communicated in sequence.
Preferably, a lower cone is arranged below the settler main body, the lower cone and the settler main body are integrally arranged, and one end of the slag discharge pipe extends to the bottom end inside the lower cone.
Preferably, one side of the lower cone is connected with a steam connecting pipe, and one end of the steam connecting pipe extends into the lower cone and is connected with the primary heater.
Preferably, the bottom end in the lower cone is provided with a collecting port, and the collecting port is positioned at the bottom end of the slag discharge pipe.
Preferably, the liquid discharge holes are provided with a plurality of groups, and the plurality of groups of liquid discharge holes are circumferentially distributed on the side wall of the annular collecting groove.
Preferably, the settler main body, the primary heater, the secondary heater and the tertiary heater are all made of steel.
The utility model provides a high-efficient dynamic settler in succession of humic acid liquid possesses following beneficial effect:
(1) the utility model discloses an adopt the heating, subside, separate integral type structure, the heater does not have area, and rotten liquid pipe need not to increase the heat preservation, has correspondingly reduced the heat loss, and the operating personnel centralized management of being convenient for invests in for a short time, convenient to use.
(2) The utility model discloses an adopt tertiary heating method, reduce solution viscosity, shorten the settling time, deposit thoroughly, the investment is little, take up an area of fewly, the processing ease, and the precipitate is by discharging, avoids the sedimentation tank to clear up the difficulty, greatly reduced intensity of labour.
(3) The utility model discloses an adopt continuous feeding, the ejection of compact in succession, arrange the sediment mode in succession, reach continuous sedimentation, realize continuous production, do benefit to and increase substantially the production scale to effectual improvement production efficiency.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
In the figure: 1. a settler body; 2. a central tube; 3. a cone returns to the web; 4. a radiation plate; 5. a secondary heater; 6. a tertiary heater; 7. an annular collection groove; 8. a slag discharge pipe; 9. a primary heater; 10. a lower cone; 11. a steam connecting pipe; 12. a collection port; 13. and a liquid discharge hole.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention will be further described in detail with reference to the following embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
As shown in fig. 1, a continuous high-efficient dynamic settler of humic acid liquid, including settler main part 1, the inside central authorities pipe 2 that is equipped with of settler main part 1, central authorities pipe 2 is located settler main part 1 middle part, 2 below of central authorities pipe are equipped with the cone and return radials 3, the cone returns radials 3 bottom and is equipped with radiant panel 4, be equipped with primary heater 9, secondary heater 5 and tertiary heater 6 in the settler main part 1, tertiary heater 6, secondary heater 5 and primary heater 9 from the top down arrange in proper order and set up inside settler main part 1, the inside top of settler main part 1 is equipped with annular collection groove 7, be equipped with outage 13 on the annular collection groove 7 lateral wall, the inside sediment pipe 8 that is equipped with of settler main part 1, sediment pipe 8 is located central authorities pipe 2 one side.
The primary heater 9, the secondary heater 5 and the tertiary heater 6 are all arranged by adopting disc pipes, the primary heater 9, the secondary heater 5 and the tertiary heater 6 are sequentially communicated, and steam for heating can sequentially enter the primary heater 9, the secondary heater 5 and the tertiary heater 6 through the steam connecting pipe 11, so that the heat of the steam is fully utilized and finally discharged from a discharge port of the tertiary heater 6.
The lower cone 10 is arranged below the settler main body 1, the lower cone 10 and the settler main body 1 are integrally arranged, one end of the slag discharging pipe 8 extends to the bottom end inside the lower cone 10, impurities and sediments in the lower cone 10 can enter the slag discharging pipe 8 through the slag discharging pipe 8 and ascend along with clear liquid, and the impurities and sediments are discharged through the slag discharging pipe 8 at the liquid level.
One side of the lower cone 10 is connected with a steam connecting pipe 11, one end of the steam connecting pipe 11 extends into the lower cone 10 and is connected with the primary heater 9, steam for heating can be sent into the primary heater 9 through the steam connecting pipe 11, and then the steam enters the secondary heater 5 and the tertiary heater 6 in sequence through the primary heater 9 to be heated.
The bottom end in the lower cone 10 is provided with a collection port 12, the collection port 12 is positioned at the bottom end of the slag discharge pipe 8, impurities collected at the collection port 12 can enter the slag discharge pipe 8 from an inlet at the bottom end of the slag discharge pipe 8, the impurities in the slag discharge pipe 8 rise along with clear liquid, and the impurities are discharged from the slag discharge pipe 8 at the liquid level.
The liquid discharge holes 13 are provided with a plurality of groups, the plurality of groups of liquid discharge holes 13 are circumferentially distributed on the side wall of the annular collection groove 7, and qualified humic acid clear liquid which rises to the top can be discharged through the liquid discharge holes 13 of the annular collection groove 7 and sent to use working sections such as water-soluble fertilizers.
The settler main body 1, the primary heater 9, the secondary heater 5 and the tertiary heater 6 are all made of steel, so that the settler main body 1 is high in strength and long in service life.
The humic acid liquid continuous high-efficiency dynamic settler is characterized in that when the humic acid liquid continuous high-temperature dynamic settler works, humic acid stock solution containing impurities and precipitates enters a central tube 2 from the top of a humic acid liquid continuous high-temperature dynamic settler main body 1 in a tangential manner, the humic acid stock solution is lowered in descending speed in the central tube 2, is subjected to primary preheating after heat exchange with solution in a container, the concentration and the viscosity of the solution are lowered along with the rise of temperature, the descending speed of the stock solution is reduced through a cone returning radial plate 3 at the lower part of the central tube 2, the primary cleaning and turbidity separation is achieved on a radiation plate 4, clear solution is swirled upwards, the turbid solution is smooth downwards, the upwards clear solution is heated through a secondary heater 5, the concentration and the viscosity are lowered continuously, the impurities and the precipitates carried in the clear solution are settled downwards, the clear solution is continuously upwards heated further through a tertiary heater 6, the concentration and the viscosity are reduced continuously, and the impurities carried in the, The precipitate continues to settle, the clear liquid continues to go up, the clear liquid further separates and settles through the space section at the upper part, the qualified humic acid clear liquid at the top flows out through the hole of the annular collecting groove 7 and is sent to the use working sections of water soluble fertilizer and the like, the precipitate and the impurities with large specific gravity descend through the radiation plate 4, the temperature is further raised through the primary heater 9, the concentration and the viscosity of the solution are reduced, the separated clear liquid rises upwards, the precipitate and the impurities continue to descend, the precipitate and the impurities are collected at the collecting port 12 of the lower cone 10, and then enter the slag discharging pipe 8 from the bottom end of the slag discharging pipe 8, the suspended matters rise along with the clear liquid in the slag discharging pipe 8, are discharged through the slag discharging pipe 8 at the liquid level, the steam used in the heating process enters from the steam connecting pipe 11 at one side of the lower cone 10 and passes through the primary heater 9, the secondary heater 5 and the tertiary heater 6 in sequence, so that the, discharging from the outlet of the tertiary heater 6; the utility model discloses an adopt the heating, subside, separation integral type structure, the heater does not have area, rotten liquid pipe need not to increase the heat preservation, the heat loss has correspondingly been reduced, the operating personnel centralized management of being convenient for, the investment is little, and adopt tertiary heating method, reduce solution viscosity, shorten the settling time, deposit thoroughly, the investment is little, take up an area of for a short time, easy operation, the precipitate discharges through scum pipe 8, avoid the sedimentation tank clearance difficulty, greatly reduced intensity of labour, through adopting continuous feeding, the continuous ejection of compact, arrange the sediment mode in succession, reach continuous sedimentation, realize continuous production, do benefit to and increase substantially the production scale, thereby effectual improvement production efficiency, facilitate promotion and use.
In the description of the present invention, it should be understood that the indicated orientation or positional relationship is based on the orientation or positional relationship shown in the drawings, and is only for convenience of description and simplification of description, and does not indicate or imply that the indicated device or element must have a particular orientation, be constructed and operated in a particular orientation, and thus should not be construed as limiting the present invention.
In the present invention, unless otherwise explicitly specified or limited, for example, it may be fixedly connected, detachably connected, or integrated; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, can be connected inside two elements or can be in an interaction relationship between the two elements, and unless otherwise specifically limited, the specific meaning of the terms in the present invention can be understood by those skilled in the art according to specific situations
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. The utility model provides a continuous high-efficient dynamic settler of humic acid liquid, its characterized in that, including settler main part (1), inside central authorities pipe (2) of being equipped with of settler main part (1), central authorities pipe (2) are located settler main part (1) middle part, central authorities pipe (2) below is equipped with the cone and returns radials (3), the cone returns radials (3) bottom and is equipped with radiant panel (4), be equipped with one-level heater (9), secondary heater (5) and tertiary heater (6) in settler main part (1), tertiary heater (6), secondary heater (5) and primary heater (9) from the top down arrange in proper order and set up inside settler main part (1), the inside top of settler main part (1) is equipped with annular collection groove (7), be equipped with outage (13) on annular collection groove (7) lateral wall, the inside slag pipe (8) that is equipped with of settler main part (1), the slag discharge pipe (8) is positioned at one side of the central pipe (2).
2. The humic acid liquid continuous high-efficiency dynamic settler according to claim 1, wherein the primary heater (9), the secondary heater (5) and the tertiary heater (6) are all arranged by adopting disc tubes, and the primary heater (9), the secondary heater (5) and the tertiary heater (6) are communicated in sequence.
3. The continuous high-efficiency dynamic settler of humic acid liquid according to claim 1, wherein a lower cone (10) is arranged below the settler main body (1), the lower cone (10) is integrated with the settler main body (1), and one end of the slag discharge pipe (8) extends to the bottom end inside the lower cone (10).
4. A continuous high-efficiency dynamic settler of humic acid liquid according to claim 3 wherein one side of the lower cone (10) is connected with a steam connecting pipe (11), and one end of the steam connecting pipe (11) extends to the inside of the lower cone (10) and is connected with the primary heater (9).
5. A high-efficiency continuous dynamic settler of humic acid liquid according to claim 3, wherein the bottom end of the inside of the lower cone (10) is provided with a collection port (12), and the collection port (12) is positioned at the bottom end of the slag discharge pipe (8).
6. The continuous high-efficiency dynamic settler of humic acid liquid according to claim 1, wherein the liquid drainage holes (13) are provided with a plurality of groups, and the plurality of groups of liquid drainage holes (13) are circumferentially distributed on the side wall of the annular collection tank (7).
7. The continuous high-efficiency dynamic settler of humic acid liquid according to claim 1, wherein the settler body (1), the primary heater (9), the secondary heater (5) and the tertiary heater (6) are all made of steel.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021271250.6U CN212914644U (en) | 2020-06-29 | 2020-06-29 | Humic acid liquid continuous high-efficiency dynamic settler |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202021271250.6U CN212914644U (en) | 2020-06-29 | 2020-06-29 | Humic acid liquid continuous high-efficiency dynamic settler |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113926220A (en) * | 2020-06-29 | 2022-01-14 | 红河锦东化工股份有限公司 | Humic acid liquid continuous high-efficiency dynamic settler |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113926220A (en) * | 2020-06-29 | 2022-01-14 | 红河锦东化工股份有限公司 | Humic acid liquid continuous high-efficiency dynamic settler |
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