CN218076870U - A high-efficient settling chamber for zinc oxide powder preparation - Google Patents

A high-efficient settling chamber for zinc oxide powder preparation Download PDF

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Publication number
CN218076870U
CN218076870U CN202222302652.3U CN202222302652U CN218076870U CN 218076870 U CN218076870 U CN 218076870U CN 202222302652 U CN202222302652 U CN 202222302652U CN 218076870 U CN218076870 U CN 218076870U
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cooling
cooling thin
thin plate
settling chamber
chamber
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张静冰
覃庶宏
王盛强
郭朝东
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Wuxuan Huifeng Industrial Co ltd
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Wuxuan Huifeng Industrial Co ltd
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Abstract

The utility model relates to the technical field of zinc oxide powder preparation, in particular to a high-efficiency settling chamber for zinc oxide powder preparation, which comprises a settling chamber body, wherein a cooling device is also arranged at the middle lower part of the settling chamber, the cooling device comprises a cooling thin plate, a cavity is arranged inside the cooling thin plate, and the lower part of the cooling thin plate is provided with an air inlet and/or a liquid inlet; the upper part of the cooling thin plate is provided with an air outlet and/or a liquid outlet; and a plurality of cooling thin plates are distributed in the middle lower part of the settling chamber at intervals in parallel. Adopt the utility model has the advantages of the radiating efficiency is good, can not reduce product yield, excellent in use effect.

Description

A high-efficient settling chamber for preparation of zinc oxide powder
Technical Field
The utility model relates to a zinc oxide powder preparation technical field, concretely relates to high-efficient settling chamber for preparation of zinc oxide powder.
Background
The most current advanced zinc-oxygen powder production process of a zinc oxide rotary kiln production line has the technical principle that zinc powder, coke and the like are mixed according to a certain proportion and then conveyed to the kiln tail of a rotary kiln through a conveying belt, then under the continuous rotation of the rotary kiln, raw materials sequentially pass through a drying section, a preheating section, a middle-temperature section and a high-temperature section, finally, various metal steam such as zinc steam and high-temperature steam-solid mixtures such as coal dust and the like are generated in the high-temperature section, after the high-temperature steam-solid mixtures are generated, under the action of strong induced air and blast air in the kiln, the high-temperature steam-solid mixtures reversely enter the middle-temperature section, the preheating section and the drying section, and finally enter a settling chamber, and the settling chamber has the functions of: separating, radiating and continuously oxidizing various oxides, dust and the like contained in the high-temperature gas-solid mixture; the impurities that are not oxidized are removed by falling from the lower end of the settling chamber by settling (the impurities fall out of the settling chamber and are then returned to the kiln for use), while the light gaseous oxides enter the baghouse. The problems with the settling chambers currently used are: generally, the temperature of a settling chamber is reduced mainly by the heat transfer between the body of the settling chamber and the surrounding air, and a water cooling system is designed at the upper part of the settling chamber; generally, the temperature of the gaseous oxide before entering the bag-type chamber can be ensured not to exceed 160 ℃ through the above mode, however, if the outside air temperature is high in summer, high temperature in a plant is difficult to diffuse quickly, the situation that the heat dissipation effect of the body of the settling chamber is not good can occur, at this time, although the circulation of the water cooling system can be slightly accelerated to improve the temperature reduction, the regulation effect of the water cooling system is limited, and how the water cooling circulation is too fast, the temperature at the front section of the settling chamber is too low, so that the metal gaseous oxide (zinc oxide steam) is cooled excessively, and the metal gaseous oxide falls off as impurities are settled, so that the yield of the end product of the production line is reduced, but if the outside environment is at high temperature, the temperature entering the bag-type chamber is too high, so that the bag-type chamber burns out, which is a contradictory process. However, according to the observation and research, it is found that a part of the high temperature in the settling chamber is caused by too high temperature of the mixture settled in the lower part of the settling chamber, because the settled mixture contains a large amount of coal dust, and the mixture pumped into the settling chamber through the rotary kiln contains a part of the coal dust in a high temperature state besides the metal gaseous oxides, and the high temperature of the mixture settled in the lower part of the settling chamber has no effect and can affect heat dissipation, so that the temperature in the settling chamber is high, therefore, the cooling device additionally arranged on the lower part of the settling chamber provides an effective idea for solving the technical problems, but the cooling device arranged on the lower part of the settling chamber can encounter the following problems: firstly, the lower part of the existing settling chamber is funnel-shaped (the lower part structure of the existing settling chamber is basically similar to the attached drawing disclosed by the following patent documents and is named as a secondary zinc oxide settling chamber with high settling efficiency, the application (patent) No. 202010828678.4, the publication (announcement) No. CN112023530B, or a product of the settling chamber in zinc oxide rotary kiln production line equipment produced by the brand such as Henan Huaguan and the like sold at present), the space of the lower part is limited, and the existing cooling device with large volume cannot be used, so that the aggregation effect and falling of particle mixtures can be influenced, other new problems such as blockage and the like are caused, and the normal production is disturbed; however, if only a few water pipes are inserted, the contact area between the water pipes and the middle lower part of the settling chamber is insufficient, the adjusting effect is very limited, and the water pipes do not play an effective role.
Disclosure of Invention
The utility model provides a high-efficient deposit room for preparation of zinc oxide powder that excellent in use effect to above-mentioned technical problem.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a high-efficiency settling chamber for preparing zinc oxide powder comprises a settling chamber body, wherein a cooling device is further arranged at the middle lower part of the settling chamber; the cooling device comprises a cooling thin plate, a cavity is arranged in the cooling thin plate, and an air inlet and/or a liquid inlet are/is formed in the lower part of the cooling thin plate; the upper part of the cooling thin plate is provided with an air outlet and/or a liquid outlet; and a plurality of cooling thin plates are distributed in the middle lower part of the settling chamber at intervals in parallel.
Optionally, one side of the lower part of the cooling thin plate is sequentially provided with a liquid inlet and a gas inlet from bottom to top, and the other side of the upper part of the cooling thin plate is also provided with a gas outlet and/or a liquid outlet.
Optionally, the air inlets of a plurality of cooling thin plates are communicated with a total air inlet chamber; liquid inlets of the plurality of cooling thin plates are communicated with a total liquid inlet chamber; the air outlets of the plurality of cooling thin plates are communicated with a main air outlet chamber; the liquid outlets of the plurality of cooling thin plates are communicated with a total liquid outlet chamber. Optionally, the outer surface of the cooling thin plate is further provided with a plurality of longitudinal ribs.
Optionally, the cooling device includes a cooling thin plate, a cavity is provided in the cooling thin plate, and a plurality of cooling thin plates are distributed in the middle lower part of the settling chamber at intervals in parallel; an intermediate plate is connected between two adjacent cooling thin plates, and a second cavity is formed in the intermediate plate; the second cavity is communicated with the cavities of the two cooling thin plates; and two sides of the lower part of one cooling thin plate are provided with air inlets, one side of the lower part of the cooling thin plate is provided with a liquid inlet, and one side or two sides of the upper part of the other cooling thin plate are respectively provided with an air outlet and/or a liquid outlet.
Optionally, the cooling device includes a cooling thin plate, a cavity is provided in the cooling thin plate, and a plurality of cooling thin plates are distributed in the middle lower part of the settling chamber at intervals in parallel; a plurality of communicating pipes are connected between two adjacent cooling thin plates; both sides of the lower part of one of the cooling thin plates are provided with air inlets, one side of the lower part is provided with a liquid inlet, and one side or both sides of the upper part of the other cooling thin plate are respectively provided with an air outlet and/or a liquid outlet.
The utility model has the advantages of compared with the prior art:
1. the utility model discloses a well lower part at the deposit room body is equipped with cooling device, high temperature impurity to subsiding the unable oxidation such as high temperature coal ash of well lower part cools down, realize cooling down in whole deposit room, ensure deposit room exit temperature control below 160 degrees, and cool down to the well lower part of deposit room, can not directly influence "main part product steam layer" on deposit room upper portion, metal steam too much subsides and influence the drawback of final yield can not appear, and simultaneously, cool down to the impurity region of well lower part, still be favorable to improving the settling velocity of impurity, finally realize high-efficient cooling, high-efficient settlement and do not influence the beneficial effect of product yield.
2. The cooling sheet that is equipped with not only can satisfy thin requirement, adopts the mode that the gas-liquid mixture flows to realize high-efficient cooling simultaneously, excellent in use effect.
Drawings
Fig. 1 is a front sectional view of the present invention;
fig. 2 is a side sectional view of the present invention;
fig. 3 is an external side partial cross-sectional view of the present invention;
fig. 4 is an external side partial cross-sectional view of the present invention;
FIG. 5 is a schematic perspective view of the cooling sheet of the present invention;
FIG. 6 is a schematic view of another embodiment of the cooling sheet of the present invention;
FIG. 7 is a schematic view of a combination structure of the cooling sheet of the present invention;
fig. 8 is a schematic view of another combination structure of the cooling thin plate of the present invention.
Detailed Description
The present invention will be described in detail with reference to the accompanying drawings and specific embodiments:
in the following embodiments, "left, right", "front, back" and "inner" are directions determined only for convenience of the descriptors, and do not limit the structure of the present invention.
As shown in fig. 1 to 8, the high-efficiency settling chamber for preparing zinc oxide powder comprises a settling chamber body 1, wherein a cooling device is arranged at the middle lower part of the settling chamber.
Optionally, the cooling device includes a cooling thin plate 2, a cavity is disposed inside the cooling thin plate 2, an air inlet 4 and/or a liquid inlet 5 are disposed on one side of a lower portion of the cooling thin plate 2, in this embodiment, the air inlet 4 is disposed at a middle lower portion of the cooling thin plate 2, then the liquid inlet 5 is disposed at a lower portion of the cooling thin plate 2, when in use, cooling water enters the bottom of an inner cavity of the cooling thin plate 2 from the liquid inlet 5, and then the air inlet 4 is used for communicating with an air source; an air outlet 3 and/or a liquid outlet are/is arranged at the upper part of the cooling thin plate 2, and only the air outlet 3 is arranged at the other side of the cooling thin plate 2 in the embodiment; a plurality of cooling thin plates 2 are distributed in parallel at intervals at the middle lower part of the settling chamber 1. Then the air inlets 4 of a plurality of cooling thin plates 2 are communicated with a total air inlet chamber 8, and the total air inlet chamber 8 is provided with a total air inlet pipe 9; the liquid inlets 5 of the plurality of cooling thin plates 2 are communicated with a total liquid inlet chamber 10, and the total liquid inlet chamber 10 is provided with a total liquid inlet pipe 11; the air outlets 3 of the plurality of cooling thin plates 2 are communicated with a main air outlet chamber 6, and the main air outlet chamber 6 is provided with a main air outlet pipe 7; in some embodiments, if liquid outlets are further provided, a plurality of liquid outlets of the cooling thin plates can be communicated with a total liquid outlet chamber. When the cooling device is used, as shown in fig. 1, cooling water enters the bottom of the inner cavity (i.e., the W region) of the cooling thin plate 2 from the liquid inlet 5, then high-temperature impurities settled at the middle lower part of the settling chamber body 1 transfer heat to the cooling thin plate 2, the cooling water absorbs the high temperature of the cooling thin plate 2 and forms steam at the same time, then the evaporated steam enters the steam layer E region, then high-speed airflow is introduced from the gas inlet 4, the high-speed airflow is mixed with the steam layer E region and enters the upper mixing region M region, the high-speed airflow and the steam further carry away heat of the cooling thin plate 2 in the M region and finally are extracted from the gas outlet 3, and during assembly, the total gas outlet pipe 7 is communicated with a negative pressure pipeline to transfer the heat to a required working section for utilization or drainage treatment.
Optionally, as shown in fig. 6, the outer surface of the cooling sheet 2 of some embodiments is further provided with a plurality of longitudinal ribs 12, and the longitudinal ribs 12 are provided to increase the contact area between the cooling sheet 2 and the outside.
Alternatively, the cooling device of some embodiments may also be configured as follows: as shown in fig. 7, the cooling device comprises a cooling thin plate 2, a cavity is arranged in the cooling thin plate 2, and a plurality of cooling thin plates are distributed in the middle lower part of the settling chamber at intervals in parallel; an intermediate plate 13 is further connected between two adjacent cooling thin plates, and the intermediate plate 13 is provided with a second cavity; the second cavity is communicated with the cavities of the two cooling thin plates 2; wherein, both sides of the lower part of one of the cooling thin plates are provided with an air inlet 4, one side of the lower part is provided with a liquid inlet 5, and one side or both sides of the upper part of the other cooling thin plate 2 are respectively provided with an air outlet and/or a liquid outlet, in this embodiment, preferably, only 2 air outlets 3 are provided, and two air outlets 3 are arranged on both sides of the upper part of the cooling thin plate 2. The combination mode of the structure has similar technical effects with other structures, and also belongs to the technical problems to be solved by the application.
Alternatively, the cooling device of some embodiments may also use a configuration similar to the configuration in fig. 7, as shown in fig. 8, which includes a cooling thin plate 2, a cavity is provided inside the cooling thin plate 2, and a plurality of cooling thin plates 2 are distributed in parallel and at intervals in the middle and lower part of the settling chamber; a plurality of communicating pipes 14 are further connected between two adjacent cooling thin plates 2, wherein both sides of the lower part of one cooling thin plate 2 are provided with air inlets, one side of the lower part is provided with a liquid inlet, and one side or both sides of the upper part of the other cooling thin plate are respectively provided with an air outlet and/or a liquid outlet. In this embodiment, a plurality of said communicating pipes 14 are disposed in the mixing area M, and the purpose of this design is: the air flow of one cooling thin plate 2 is mixed with the steam to absorb heat and then is conveyed to the other cooling thin plate 2, and the heat absorption effect of the mixed air flow is improved.
The principles and embodiments of the present invention have been explained herein using specific examples, which are presented only to assist in understanding the methods and their core concepts. It should be noted that there are infinite specific structures due to the limited character expressions, and it will be apparent to those skilled in the art that various improvements, decorations or changes can be made without departing from the principles of the present invention, and the technical features can be combined in a suitable manner; the application of the concepts and technical solutions of the present invention to other applications, with or without any modifications, shall be considered as the scope of the present invention.

Claims (6)

1. A high-efficient settling chamber for preparation of zinc oxide powder which characterized in that: the sedimentation chamber comprises a sedimentation chamber body, wherein a cooling device is also arranged at the middle lower part of the sedimentation chamber; the cooling device comprises a cooling thin plate, a cavity is arranged in the cooling thin plate, and an air inlet and/or a liquid inlet are/is formed in the lower part of the cooling thin plate; the upper part of the cooling thin plate is provided with an air outlet and/or a liquid outlet; and a plurality of cooling thin plates are distributed in the middle lower part of the settling chamber at intervals in parallel.
2. The high-efficiency settling chamber for preparing zinc oxide powder as claimed in claim 1, wherein: one side of the lower part of the cooling thin plate is sequentially provided with a liquid inlet and a gas inlet from bottom to top, and the other side of the upper part of the cooling thin plate is also provided with a gas outlet and/or a liquid outlet.
3. The high-efficiency settling chamber for preparing zinc oxide powder as claimed in claim 1, wherein: the air inlets of the plurality of cooling thin plates are communicated with a total air inlet chamber; liquid inlets of the plurality of cooling thin plates are communicated with a total liquid inlet chamber; the air outlets of the plurality of cooling thin plates are communicated with a main air outlet chamber; the liquid outlets of the plurality of cooling thin plates are communicated with a total liquid outlet chamber.
4. The high-efficiency settling chamber for preparing zinc oxide powder as claimed in claim 1, wherein: and the outer surface of the cooling thin plate is also provided with a plurality of longitudinal raised lines.
5. The high-efficiency settling chamber for preparing zinc oxide powder as claimed in claim 1, which is characterized in that: the cooling device comprises cooling thin plates, a cavity is arranged in each cooling thin plate, and the cooling thin plates are distributed at the middle lower part of the settling chamber at intervals in parallel; an intermediate plate is connected between two adjacent cooling thin plates, and a second cavity is formed in the intermediate plate; the second cavity is communicated with the cavities of the two cooling thin plates; and two sides of the lower part of one cooling thin plate are provided with air inlets, one side of the lower part of the cooling thin plate is provided with a liquid inlet, and one side or two sides of the upper part of the other cooling thin plate are respectively provided with an air outlet and/or a liquid outlet.
6. The high-efficiency settling chamber for preparing zinc oxide powder as claimed in claim 1, which is characterized in that: the cooling device comprises cooling thin plates, a cavity is arranged in each cooling thin plate, and the cooling thin plates are distributed at the middle lower part of the settling chamber at intervals in parallel; a plurality of communicating pipes are connected between two adjacent cooling thin plates; both sides of the lower part of one of the cooling thin plates are provided with air inlets, one side of the lower part is provided with a liquid inlet, and one side or both sides of the upper part of the other cooling thin plate are respectively provided with an air outlet and/or a liquid outlet.
CN202222302652.3U 2022-08-31 2022-08-31 A high-efficient settling chamber for zinc oxide powder preparation Active CN218076870U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202222302652.3U CN218076870U (en) 2022-08-31 2022-08-31 A high-efficient settling chamber for zinc oxide powder preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202222302652.3U CN218076870U (en) 2022-08-31 2022-08-31 A high-efficient settling chamber for zinc oxide powder preparation

Publications (1)

Publication Number Publication Date
CN218076870U true CN218076870U (en) 2022-12-20

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CN202222302652.3U Active CN218076870U (en) 2022-08-31 2022-08-31 A high-efficient settling chamber for zinc oxide powder preparation

Country Status (1)

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CN (1) CN218076870U (en)

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