CN210583808U - Barium sulfide solution heating clarifying tank - Google Patents

Barium sulfide solution heating clarifying tank Download PDF

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Publication number
CN210583808U
CN210583808U CN201920991470.7U CN201920991470U CN210583808U CN 210583808 U CN210583808 U CN 210583808U CN 201920991470 U CN201920991470 U CN 201920991470U CN 210583808 U CN210583808 U CN 210583808U
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fixedly connected
tank body
heating
tank
barium sulfide
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CN201920991470.7U
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Chinese (zh)
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张启
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Hubei Jingshan Chutianbeiyan LLC
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Hubei Jingshan Chutianbeiyan LLC
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Abstract

The utility model discloses a barium sulfide solution heating clarification tank, which comprises a tank body, the central authorities at jar body top are pegged graft and are had the feed liquor section of thick bamboo that extends to jar internal chamber, the trapezoidal fill of bottom fixedly connected with of feed liquor section of thick bamboo, the top of jar body is rabbeted about feed liquor section of thick bamboo symmetry and is had the steam pipe, the seal cover has been cup jointed to the feed liquor section of thick bamboo part of jar internal chamber, the equal fixed joint in the left and right sides of seal cover has a plurality of steam heads. The utility model relates to a chemical industry equipment technical field, this barium sulfide solution heating clarification tank, through setting up steam heating and the dual heating mechanism of electrical heating, can heat barium sulfide solution, solution after the heating can clarify fast, impurity subsides jar body bottom fast, solution after the heating is from bottom to top outside the feed liquor section of thick bamboo because of the sectional area high velocity of flow down, the undisturbed, reach the effect that continuous heating nature subsides the purification, impurity after the clarification is through the automatic discharge of the sediment thick liquid export of slope, prevent that impurity from gluing, thereby clarification efficiency has been improved.

Description

Barium sulfide solution heating clarifying tank
Technical Field
The utility model relates to the technical field of chemical equipment, in particular to a barium sulfide solution heating and clarifying tank.
Background
Barium sulfide is an important intermediate product in the production process of precipitated barium carbonate, and impurities in the solution must be clarified before entering the carbonization reaction.
The existing clarifying tank mostly adopts a natural clarifying mode, which needs to consume a large amount of time and has poor clarifying effect.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
The utility model provides a barium sulfide solution heating clarification tank, which solves the problems of time consuming and poor effect of the prior clarification tank.
(II) technical scheme
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a barium sulfide solution heating clarification tank, includes a jar body, the central authorities at jar body top are pegged graft and are had the feed liquor section of thick bamboo that extends to jar body inner chamber, the trapezoidal fill of the bottom fixedly connected with of feed liquor section of thick bamboo, the top of jar body is rabbeted about feed liquor section of thick bamboo symmetry and is had the steam pipe, the feed liquor section of thick bamboo part of jar body inner chamber has cup jointed the sealed cowling, the equal fixed joint in the left and right sides of sealed cowling has a plurality of steam heads, a plurality of steam heads all with steam pipe fixed connection.
The inner side wall of the trapezoidal hopper is fixedly connected with a clamp, the inner side of the clamp is fixedly connected with a first electric heating pipe, the bottom of the inner wall of the tank body is fixedly connected with a filter screen plate, and one side of the filter screen plate is fixedly connected to the bottom of the liquid inlet cylinder.
The left side and the right side of the tank body are fixedly connected with liquid discharge ports, the inner wall of the tank body is fixedly connected with a pump machine corresponding to the liquid discharge ports, the water outlet end of the pump machine is connected with the liquid discharge ports through a guide pipe, and the water inlet end of the pump machine is fixedly connected with a water inlet pipe.
The central authorities fixedly connected with sediment thick liquid export of jar body bottom, the bottom threaded connection of sediment thick liquid export has the waste residue to collect the box, all seted up the camera apron about the bottom of jar internal wall, fixedly connected with second electric heating pipe in the camera apron.
The bottom of the tank body is fixedly connected with a base.
Preferably, the inner wall of the waste residue collection box is attached with an adsorption pad.
Preferably, the top of the tank body is fixedly connected with an access hole.
Preferably, the number of the steam heads is 15-20, and the distances between two adjacent steam heads are equal.
Preferably, the water inlet pipe is positioned above the screen plate.
Preferably, the bottom of the inner wall of the tank body is obliquely arranged.
(III) advantageous effects
The utility model provides a barium sulfide solution heating clarification tank. The method has the following beneficial effects:
this barium sulfide solution heating clarification tank through setting up steam heating and the dual heating mechanism of electrical heating, can heat barium sulfide solution, and solution after the heating can be clarified fast, and impurity subsides jar body bottom fast, and solution after the heating is from bottom to top outside the feed liquor section of thick bamboo because of the sectional area high velocity of flow down, and no disturbance reaches the effect that the continuous heating subsides the purification naturally, and impurity after the clarification is through the automatic discharge of the sediment thick liquid export of slope, prevents that impurity from gluing to clarification efficiency has been improved.
Drawings
FIG. 1 is a front sectional view of the structure of the present invention;
FIG. 2 is a bottom view of the ladder-shaped bucket of the present invention;
FIG. 3 is a sectional view of the waste residue collecting box of the present invention;
fig. 4 is the utility model discloses a screen plate structure plan view.
In the figure: 1. a tank body; 2. a liquid inlet cylinder; 3. a trapezoidal hopper; 4. a steam pipe; 5. a sealing cover; 6. a steam head; 7. clamping; 8. a first electric heating tube; 9. a filter screen plate; 10. a liquid discharge port; 11. a pump machine; 12. a water inlet pipe; 13. a slurry outlet; 14. a waste residue collection box; 15. a hidden groove; 16. a second electric heating tube; 17. a base; 18. an adsorption pad; 19. and (6) an access hole.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. 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. 1-4, the utility model provides a technical solution: the utility model provides a barium sulfide solution heating clarification tank, the top fixedly connected with access hole 19 of jar body 1 sets up access hole 19, makes things convenient for the maintenance personal to regularly overhaul. The device comprises a tank body 1, a liquid inlet cylinder 2 extending to an inner cavity of the tank body 1 is inserted in the center of the top of the tank body 1, and a trapezoidal hopper 3 is fixedly connected to the bottom of the liquid inlet cylinder 2. The steam pipes 4 are symmetrically embedded in the top of the tank body 1 about the liquid inlet barrel 2, the sealing cover 5 is sleeved on the liquid inlet barrel 2 in the inner cavity of the tank body 1, the left side and the right side of the sealing cover 5 are fixedly clamped with the plurality of steam heads 6, the plurality of steam heads 6 are fixedly connected with the steam pipes 4, the number of the steam heads 6 is 15-20, and the distance between every two adjacent steam heads 6 is equal.
The inner side wall of the trapezoidal hopper 3 is fixedly connected with a clamp 7, and the inner side of the clamp 7 is fixedly connected with a first electric heating pipe 8. The bottom of the inner wall of the tank body 1 is fixedly connected with a filter screen plate 9, the aperture of the filter screen plate 9 is smaller than the radius of impurities, and one side of the filter screen plate 9 is fixedly connected with the bottom of the liquid inlet cylinder 2.
The left side and the right side of the tank body 1 are fixedly connected with a liquid discharge port 10, the inner wall of the tank body 1 is fixedly connected with a pump 11 corresponding to the liquid discharge port 10, the pump 11 adopts a 20ISF10-20 model, the water outlet end of the pump 11 is connected with the liquid discharge port 10 through a guide pipe, the water inlet end of the pump 11 is fixedly connected with a water inlet pipe 12, and the water inlet pipe 12 is positioned above the filter screen plate 9.
The bottom of the 1 inner wall of jar body is the slope setting, and the central fixedly connected with sediment thick liquid export 13 of the 1 bottom of jar body, the bottom threaded connection of sediment thick liquid export 13 has the waste residue to collect box 14, and the inner wall laminating of waste residue collection box 14 has adsorption pad 18, sets up adsorption pad 18, conveniently adsorbs impurity to regularly pull down waste residue collection box 14, clear away impurity. The hidden grooves 15 are formed in the left and right sides of the bottom of the inner wall of the tank body 1, the second electric heating pipes 16 are fixedly connected in the hidden grooves 15, and the first electric heating pipes 8 and the second electric heating pipes 16 are of HHD-FB009 models.
The bottom of the tank body 1 is fixedly connected with a base 17.
During the use, barium sulfide liquid is poured into through advancing liquid cylinder 2, then switches on hot steam with steam pipe 4, and steam passes through in steam pipe 4 gets into steam head 6, heats the liquid cylinder 2 that advances in the sealed cowling 5 then to the solution that the messenger flowed into in the liquid cylinder 2 heaies up, and solution is fought 3 through trapezoidal and is flowed out, is equipped with first electric heating pipe 8 in the trapezoidal fill 3, opens first electric heating pipe 8, can heat solution once more.
The solution finally falls to the bottom of the tank body 1, the solution can be further heated by opening the second electric heating pipe 16, the clarification speed can be increased by continuous heating, and clarified impurities flow into the slag slurry outlet 13 along the inner wall of the inclined tank body 1 and then enter the waste residue collecting box 14 to be stored.
The pump 11 is started to pump the clarified liquid through the inlet pipe 12 and discharge it through the discharge port 10, while the impurities are blocked by the screen plate 9 and thus cannot pass through, thereby completing the separation of the impurities from the clarified liquid.
To sum up, this barium sulfide solution heating clarification tank through setting up steam heating and the dual heating mechanism of electrical heating, can heat the barium sulfide solution, the solution after the heating can be clarified fast, impurity subsides to jar body 1 bottom fast, the solution after the heating is from bottom to top under the inlet cylinder 2 is outer because of the sectional area big velocity of flow, no disturbance reaches the effect of continuous heating nature settlement purification, impurity after the clarification is through the automatic discharge of the sediment thick liquid export 13 of slope, prevent that impurity from gluing, thereby clarification efficiency has been improved.
It should be noted that the electrical components shown in this document are all electrically connected to an external master controller and 220V mains, and the master controller may be a conventional known device such as a computer for controlling, and the control principle, internal structure, and control switching manner of the device are conventional means in the prior art, and are directly referred to herein without further description. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
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 (6)

1. A barium sulfide solution heating clarification tank is characterized in that: the steam-feeding tank comprises a tank body (1), wherein a liquid inlet cylinder (2) extending to an inner cavity of the tank body (1) is inserted in the center of the top of the tank body (1), a trapezoidal hopper (3) is fixedly connected to the bottom of the liquid inlet cylinder (2), steam pipes (4) are symmetrically embedded in the top of the tank body (1) relative to the liquid inlet cylinder (2), a sealing cover (5) is sleeved on the part of the liquid inlet cylinder (2) in the inner cavity of the tank body (1), a plurality of steam heads (6) are fixedly clamped on the left side and the right side of the sealing cover (5), and the steam heads (6) are fixedly connected with the steam pipes (4);
the inner side wall of the trapezoidal hopper (3) is fixedly connected with a clamp (7), the inner side of the clamp (7) is fixedly connected with a first electric heating pipe (8), the bottom of the inner wall of the tank body (1) is fixedly connected with a filter screen plate (9), and one side of the filter screen plate (9) is fixedly connected with the bottom of the liquid inlet cylinder (2);
the left side and the right side of the tank body (1) are fixedly connected with a liquid outlet (10), the inner wall of the tank body (1) is fixedly connected with a pump (11) corresponding to the liquid outlet (10), the water outlet end of the pump (11) is connected with the liquid outlet (10) through a guide pipe, and the water inlet end of the pump (11) is fixedly connected with a water inlet pipe (12);
a slag slurry outlet (13) is fixedly connected to the center of the bottom of the tank body (1), a waste slag collecting box (14) is in threaded connection with the bottom of the slag slurry outlet (13), blind grooves (15) are formed in the left side and the right side of the bottom of the inner wall of the tank body (1), and second electric heating pipes (16) are fixedly connected in the blind grooves (15);
the bottom of the tank body (1) is fixedly connected with a base (17).
2. The barium sulfide solution heating and clarifying tank as set forth in claim 1, wherein: the inner wall of the waste residue collecting box (14) is attached with an adsorption pad (18).
3. The barium sulfide solution heating and clarifying tank as set forth in claim 1, wherein: the top of the tank body (1) is fixedly connected with an access hole (19).
4. The barium sulfide solution heating and clarifying tank as set forth in claim 1, wherein: the number of the steam heads (6) is 15-20, and the distances between two adjacent steam heads (6) are equal.
5. The barium sulfide solution heating and clarifying tank as set forth in claim 1, wherein: the water inlet pipe (12) is positioned above the filter screen plate (9).
6. The barium sulfide solution heating and clarifying tank as set forth in claim 1, wherein: the bottom of the inner wall of the tank body (1) is obliquely arranged.
CN201920991470.7U 2019-06-27 2019-06-27 Barium sulfide solution heating clarifying tank Active CN210583808U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920991470.7U CN210583808U (en) 2019-06-27 2019-06-27 Barium sulfide solution heating clarifying tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920991470.7U CN210583808U (en) 2019-06-27 2019-06-27 Barium sulfide solution heating clarifying tank

Publications (1)

Publication Number Publication Date
CN210583808U true CN210583808U (en) 2020-05-22

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CN201920991470.7U Active CN210583808U (en) 2019-06-27 2019-06-27 Barium sulfide solution heating clarifying tank

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112999984A (en) * 2021-03-25 2021-06-22 沧州信联化工有限公司 Decomposition device of tetramethylammonium hydroxide solution and use method thereof
CN113277535A (en) * 2021-05-20 2021-08-20 萍乡市华顺环保化工填料有限公司 Novel subsider heating is used in aluminium oxide production device
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

Cited By (4)

* Cited by examiner, † Cited by third party
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
CN112999984A (en) * 2021-03-25 2021-06-22 沧州信联化工有限公司 Decomposition device of tetramethylammonium hydroxide solution and use method thereof
CN113277535A (en) * 2021-05-20 2021-08-20 萍乡市华顺环保化工填料有限公司 Novel subsider heating is used in aluminium oxide production device
CN113277535B (en) * 2021-05-20 2022-11-18 萍乡市华顺环保化工填料有限公司 Novel subsider heating is used in aluminium oxide production device

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