CN215995702U - Emulsion is handled and is used precipitation equipment with edulcoration structure - Google Patents

Abstract

The utility model discloses a precipitation device with an impurity removal structure for emulsion treatment, which comprises an impurity removal main body, an aerosol impurity removal mechanism, a precipitation impurity removal mechanism and a track, wherein the aerosol impurity removal mechanism comprises a gas inlet pipe, a gas outlet pipe and a gas inlet pipe; the spout, it is seted up in the track bottom, the deflector is installed on the spout right side, spout internally mounted has the sliding seat, the telescopic link is installed to sliding seat left side input, the short connecting rod is installed to the sliding seat right side terminal surface, the short connecting rod is kept away from the slider is installed to sliding seat one end. The problem of the unable fine multiple impurity of dispelling in the emulsion of prior art, the emulsion after using is directly scrapped to the general selection of enterprise, the emission of emulsion can lead to the technical problem of the pollution of soil and lake when causing manufacturing cost to increase, provides an emulsion for processing precipitation equipment with edulcoration structure, and what have pertinence is categorised to different density impurity and is dispeled, keeps in the edulcoration mechanism clean when the effect is dispelled to the guarantee impurity, effectively reduces edulcoration mechanism maintenance frequency.

Description

Emulsion is handled and is used precipitation equipment with edulcoration structure

Technical Field

The utility model relates to the technical field of emulsion treatment, in particular to a precipitation device with an impurity removal structure for emulsion treatment.

Background

When a continuous rolling mill in a production system works, a plurality of parts need to be cooled or lubricated by emulsion, the emulsion can contain impurities after being used by the continuous rolling mill, if the emulsion is directly recycled without being treated, the continuous rolling mill can be damaged, and the impurity components are complex and are obviously layered in the emulsion.

The common problems of the existing emulsion treatment equipment are as follows: in the prior art, various impurities in the emulsion cannot be well removed, and enterprises generally choose to directly discard the used emulsion, so that the production cost is increased, and the emission of the emulsion can cause the pollution to land and lakes.

SUMMERY OF THE UTILITY MODEL

The utility model aims to provide a precipitation device with an impurity removal structure for emulsion treatment, which aims to solve the problem that various impurities in emulsion cannot be well removed in the prior art proposed in the background art, and enterprises generally choose to scrap the used emulsion directly, so that the production cost is increased, and the emission of the emulsion can cause the pollution to land and lakes.

In order to achieve the purpose, the utility model provides the following technical scheme: a precipitation equipment with edulcoration structure for emulsion is handled includes:

removing impurities from the main body;

further comprising:

the aerosol impurity removal mechanism is movably arranged inside the impurity removal main body;

the aerosol edulcoration mechanism includes:

a track;

the slide way, it sets up in the track bottom, the deflector is installed on the spout right side, spout internally mounted has the sliding seat, the telescopic link is installed to sliding seat left side input, the short connecting rod is installed to sliding seat right side terminal surface, the short connecting rod is kept away from the slider is installed to sliding seat one end, long connecting rod is installed to sliding seat left side terminal surface, the filter plate is installed to slider top terminal surface, the down tube is installed at the filter plate top, the outside cover of down tube is equipped with the scraper blade.

Preferably, the guide plate is fixedly installed on the end face of the right side of the sliding groove, the top of the guide plate inclines rightwards, and the sliding seat is movably installed inside the sliding groove.

Preferably, the sliding seat right side terminal surface rotates and installs the short connecting rod, and the telescopic link passes through the sliding seat and constitutes transmission structure with the short connecting rod, the sliding seat left side terminal surface rotates and installs long connecting rod, and long connecting rod keeps away from sliding seat one end and rotates and install the slider.

Preferably, the slide block is movably mounted inside the track, the length of the slide block is smaller than that of the filter plate fixedly mounted on the top end face, an inclined rod inclined to the left is fixedly mounted on the top end face of the filter plate, and a scraper plate is movably mounted at the surface end of the inclined rod.

Preferably, the edulcoration main part includes:

the inner side of the top of the box body is fixedly provided with a track;

the aerosol cavity is arranged on the right side of the inner cavity of the box body, and a fluid infusion port is formed in the end face of the bottom of the aerosol cavity.

Preferably, the edulcoration main part still includes:

the liquid level meter is attached to the inner bottom of the aerosol cavity, and an impurity outlet is formed in the end face of the top of the aerosol cavity;

the turning plate is rotatably installed on the inner side of the bottom of the box body, the liquid level meter is electrically connected with the turning plate and the telescopic rod respectively, a settling chamber is formed in the left side of the inner cavity of the box body, and the cross section of the settling chamber is V-shaped.

Preferably, the bottom of the precipitation cavity is movably provided with a precipitation and impurity removal mechanism;

deposit edulcoration mechanism includes:

the discharge opening is formed in the end face of the bottom of the precipitation cavity with the V-shaped section;

the pipeline is arranged at the bottom of the discharge opening, and a boss is fixedly arranged in the pipeline.

Preferably, the precipitation and impurity removal mechanism further comprises:

the valve body is fixedly arranged at the bottom of the boss, one side of the valve body surface, opposite to the inner cavity of the pipeline, is in a transparent state, one side of the valve body, opposite to the inner cavity of the pipeline, is in a closed state, the valve body is obliquely arranged inside the pipeline, and a threaded end is arranged on the end surface of the bottom of the valve body.

Preferably, the precipitation and impurity removal mechanism further comprises:

the filter cartridge is movably arranged inside the valve body, the end face of the filter cartridge is attached to the inner wall of the valve body, a threaded sleeve is fixedly arranged at the bottom of the filter cartridge, the threaded sleeve is arranged on the end face of the bottom of the valve body, and a recovery tank is arranged on one side, away from the discharge opening, of the pipeline.

Compared with the prior art, the utility model has the beneficial effects that: the problem of the unable fine multiple impurity of dispelling in the emulsion of prior art, the emulsion after using is directly scrapped to the general selection of enterprise, the emission of emulsion can lead to the technical problem of the pollution of soil and lake when causing manufacturing cost to increase, provides an emulsion for processing precipitation equipment with edulcoration structure, and what have pertinence is categorised to different density impurity and is dispeled, keeps in the edulcoration mechanism clean when the effect is dispelled to the guarantee impurity, effectively reduces edulcoration mechanism maintenance frequency.

1. The utility model is characterized in that through the arrangement of a floating impurity removal mechanism, a liquid level meter is electrically connected with a telescopic rod, the telescopic rod is started and pushes a sliding seat to slide in a sliding chute, the sliding seat drives a sliding block to slide in a track through a short connecting rod and a long connecting rod, when a filter plate at the top of the sliding block is contacted with a guide plate at the right end face of the sliding chute, the sliding block stops transverse displacement, the sliding seat is pushed by the telescopic rod to continue to slide towards the guide plate, under the jacking action of the short connecting rod and the long connecting rod, the filter plate is positioned in a floating cavity to be lifted and finally inclines rightwards under the action of the length difference of the connecting rods at two sides, low-density suspended impurities in emulsion can be completely filtered by the filter plate and are attached to the inside of the filter plate, then a scraper plate sleeved on the left end face of an inclined rod at the top of the filter plate under the action of gravity starts to slide rightwards, and impurities attached to the end face of the filter plate all flow along the guide of the top end face of the guide plate in the sliding stroke of the left box body and finally flow along the guide plate Discharging impurities through an impurity outlet which is arranged on the side;

2. the utility model opens the discharge opening after a period of time for precipitation through the arrangement of the precipitation and impurity removal mechanism, emulsion flows into the pipeline through the discharge opening, the boss arranged in the pipeline plays a role of intercepting, the emulsion level changes the way at the boss and flows through the interior of the valve body, the valve body is arranged in a structure that one side of the interior of the pipeline is through and the exterior of the pipeline is sealed, so that the emulsion has to pass through one end surface of the valve body to the other side pipeline, high-density sediment impurities in the emulsion can be retained in the filter cylinder under the filtering action of the filter cylinder attached to the inner wall of the valve body, and then a user rotates the threaded sleeve, the thread sleeve which is arranged on the end face of the bottom of the valve body and is engaged with the thread drives the filter cylinder to be separated from the interior of the valve body, so that the accumulated impurities in the filter cylinder are removed, and the emulsion filtered by the valve body finally flows into a recovery tank to be recycled;

3. according to the utility model, through the arrangement of the impurity removal main body, the turning plate at the position of the passage from the aerosol cavity at the bottom of the box body to the precipitation cavity is closed, a user introduces used emulsion into the aerosol cavity through the liquid supplementing port, the filling stroke of the emulsion in the aerosol cavity is monitored by the liquid level meter, the input of the liquid supplementing port is stopped when the preset liquid height is reached, after the aerosol removing process suspended in the emulsion is completed, the turning plate is opened and is finally closed by the liquid level meter along with the reduction of the emulsion height, the emulsion enters the precipitation cavity, and because of the V-shaped structure of the precipitation cavity, high-density sediment impurities in the emulsion are gathered at the bottom of the V-shaped structure of the precipitation cavity, so that the cleanness of the inner wall of the precipitation cavity is favorably kept while the impurities are removed.

Drawings

FIG. 1 is a schematic view of a front view of an impurity removing main body according to the present invention;

FIG. 2 is a schematic diagram of a front view of an aerosol impurity removal mechanism according to the present invention;

FIG. 3 is a schematic view of a front view of a precipitation and impurity removal mechanism according to the present invention;

fig. 4 is a schematic perspective view of the thread bushing of the present invention.

In the figure: 1. removing impurities from the main body; 101. a box body; 102. an aerosol chamber; 103. a fluid infusion port; 104. a liquid level meter; 105. an impurity outlet; 106. turning over a plate; 107. a sedimentation chamber; 2. an aerosol impurity removal mechanism; 201. a track; 202. a chute; 203. a guide plate; 204. a sliding seat; 205. a telescopic rod; 206. a short connecting rod; 207. a slider; 208. a long connecting rod; 209. filtering the plate; 210. a diagonal bar; 211. a squeegee; 3. a precipitation and impurity removal mechanism; 301. a discharge opening; 302. a pipeline; 303. a boss; 304. a valve body; 305. a threaded end; 306. a filter cartridge; 307. a threaded sleeve; 308. and (5) a recovery tank.

Detailed Description

As shown in fig. 1, a precipitation apparatus for emulsion treatment having an impurity removing structure includes: impurity removal main body 1; the device comprises a box body 101, wherein a track 201 is fixedly arranged on the inner side of the top of the box body 101; the device comprises an aerosol cavity 102, a liquid level meter 104 and a liquid level meter, wherein the aerosol cavity 102 is arranged on the right side of an inner cavity of a box body 101, a liquid replenishing port 103 is formed in the end face of the bottom of the aerosol cavity 102, the liquid level meter is attached to the bottom of the inner side of the aerosol cavity 102 and closes a turning plate 106 at the position of a channel from the aerosol cavity 102 to a settling cavity 107 at the bottom of the box body 101, a user introduces used emulsion into the aerosol cavity 102 through the liquid replenishing port 103, the filling stroke of the emulsion in the aerosol cavity 102 is monitored by the liquid level meter 104, the input of the liquid replenishing port 103 is stopped when the preset liquid level is reached, and an impurity outlet 105 is formed in the end face of the top of the aerosol cavity 102; turn over board 106, it rotates to install in box 101 bottom inboardly, level gauge 104 constitutes electric connection with turning over board 106 and telescopic link 205 respectively, sedimentation chamber 107 has been seted up on box 101 inner chamber left side, sedimentation chamber 107 cross-section is the V font, after the process is dispeled to the aerosol of suspension in accomplishing the emulsion, turn over board 106 and open and finally turn over board 106 and close by level gauge 104 control along with the decline of emulsion height, the emulsion has got into sedimentation chamber 107, because sedimentation chamber 107's V font structure, high density heavy end impurity gathers in sedimentation chamber 107's V font structure's bottom in the emulsion, do benefit to impurity removal and keep the clean and tidy of sedimentation chamber 107 inner wall simultaneously.

As shown in fig. 2, the aerosol impurity removing mechanism 2 is movably arranged inside the impurity removing main body 1; a rail 201; a sliding chute 202 which is arranged at the bottom of the track 201, a guide plate 203 is arranged at the right side of the sliding chute 202, a sliding seat 204 is arranged inside the sliding chute 202, the guide plate 203 is fixedly arranged at the right side end face of the sliding chute 202, the top of the guide plate 203 inclines to the right, the sliding seat 204 is movably arranged inside the sliding chute 202, the sliding seat is electrically connected with a telescopic rod 205 through a liquid level meter 104, the telescopic rod 205 is started and pushes the sliding seat 204 to slide in the sliding chute 202, the sliding seat 204 drives a sliding block 207 to slide in the track 201 through a short connecting rod 206 and a long connecting rod 208, the telescopic rod 205 is arranged at the left side input end of the sliding seat 204, the short connecting rod 206 is arranged at the right side end face of the sliding seat 204, the sliding block 207 is arranged at one end of the short connecting rod 206 far away from the sliding seat 204, the long connecting rod 208 is arranged at the left side end face of the sliding seat 204, the short connecting rod 206 is rotatably arranged at the right side end face of the sliding seat 204, and the telescopic rod 205 and the telescopic rod 206 form a transmission structure through the sliding seat 204 and the short connecting rod 206, a long connecting rod 208 is rotatably mounted on the left end face of the sliding seat 204, a sliding block 207 is rotatably mounted on one end of the long connecting rod 208, which is far away from the sliding seat 204, a filter plate 209 is mounted on the top end face of the sliding block 207, when the filter plate 209 on the top of the sliding block 207 contacts with the guide plate 203 on the right end face of the sliding chute 202, the sliding block 207 stops lateral displacement, at this time, the sliding seat 204 continues to slide towards the guide plate 203 under the pushing of the telescopic rod 205, under the pushing and extending action of the short connecting rod 206 and the long connecting rod 208, the filter plate 209 is lifted in the aerosol cavity 102 and finally inclines rightwards under the action of the length difference of the connecting rods on the two sides, an inclined rod 210 is mounted on the top of the filter plate 209, a scraper 211 is sleeved outside the inclined rod 210, the sliding block 207 is movably mounted inside the track 201, the length of the sliding block 207 is smaller than the filter plate 209 fixedly mounted on the top end face of the filter plate 209, the inclined rod 210 inclining leftwards is fixedly mounted on the top end face of the filter plate 209, and the surface of the inclined rod 210 is movably mounted with the scraper 211, the low-density suspended impurities in the emulsion are all filtered by the filter plate 209 and attached to the end face of the filter plate, then the scraper 211 sleeved on the left end face of the inclined rod 210 inclined to the left at the top of the filter plate 209 under the action of gravity starts to slide to the right, and the impurities attached to the end face of the filter plate 209 in the sliding stroke of the scraper 211 all flow along the guide of the top end face of the guide plate 203 and are finally discharged from the impurity outlet 105 formed in the left side of the box 101.

As shown in fig. 3-4, the bottom of the precipitation cavity 107 is movably provided with a precipitation and impurity removal mechanism 3; the discharge opening 301 is formed in the end face of the bottom of the sedimentation chamber 107 with the V-shaped section; a pipeline 302 which is arranged at the bottom of the discharge port 301, a boss 303 is fixedly arranged in the pipeline 302, a valve body 304 which is fixedly arranged at the bottom of the boss 303, the surface of the valve body 304 is in a transparent state relative to one side of the inner cavity of the pipeline 302, the valve body 304 is in a closed state relative to the side of the inner cavity of the pipeline 302, the valve body 304 is obliquely arranged in the pipeline 302, the discharge port 301 is opened after one end time of sedimentation, emulsion flows into the pipeline 302 through the discharge port 301, the boss 303 arranged in the pipeline 302 plays a role of intercepting, the emulsion is redirected at the boss 303 and flows through the inside of the valve body 304, the surface of the valve body 304 is transparent relative to one side of the inside of the pipeline 302 and is in a structure which the outside of the pipeline 302 is closed, so that the emulsion is led to the pipeline 302 at the other side through the end surface of the inside of the valve body 304, a threaded end 305 is arranged on the bottom end surface of the valve body 304, a filter cartridge 306 which is movably arranged in the valve body 304, and the end surface of the filter cartridge 306 is jointed with the inner wall of the valve body 304, the bottom of the filter cylinder 306 is fixedly provided with a threaded sleeve 307, the threaded sleeve 307 is arranged on the end face of the bottom of the valve body 304, a recovery tank 308 is arranged on one side, away from the discharge port 301, of the pipeline 302, high-density bottom-sinking impurities in the emulsion can be retained inside the filter cylinder 306 under the filtering action of the filter cylinder 306 attached to the inner wall of the valve body 304, and then a user can drive the filter cylinder 306 to be separated from the valve body 304 by rotating the threaded sleeve 307 which is arranged on the end face of the bottom of the valve body 304 and meshed with the threaded end 305, so that the impurities accumulated in the filter cylinder 306 can be removed, and the emulsion filtered by the valve body 304 finally flows into the recovery tank 308 to be recovered and utilized.

The working principle is as follows: when the sedimentation equipment with the impurity removing structure for emulsion treatment is used, the turning plate 106 at the passage of the aerosol cavity 102 at the bottom of the box body 101 to the sedimentation cavity 107 is closed, a user introduces used emulsion into the aerosol cavity 102 through the liquid supplementing port 103, the filling stroke of the emulsion in the aerosol cavity 102 is monitored by the liquid level meter 104, the input of the liquid supplementing port 103 is stopped when the preset liquid height is reached, the telescopic rod 205 is electrically connected with the telescopic rod 205, the telescopic rod 205 is started and pushes the sliding seat 204 to slide in the sliding chute 202, the sliding seat 204 drives the sliding block 207 to slide in the track 201 through the short connecting rod 206 and the long connecting rod 208, when the filter plate 209 at the top of the sliding block 207 is contacted with the guide plate 203 at the right end face of the sliding chute 202, the sliding block 207 stops the transverse displacement, at the moment, the sliding seat 204 continues to slide towards the guide plate 203 under the pushing of the telescopic rod 205, under the pushing action of the short connecting rod 206 and the long connecting rod 208, the filter plate 209 is lifted in the aerosol cavity 102 and finally inclines to the right under the action of the length difference of the connecting rods at two sides, all suspended impurities with low density in the emulsion can be filtered by the filter plate 209 and are attached to the end surface of the filter plate, then the scraper 211 originally sleeved on the left end surface of the inclined rod 210 inclining to the left at the top of the filter plate 209 under the action of gravity starts to slide to the right, all the impurities attached to the end surface of the filter plate 209 flow along the guide of the top end surface of the guide plate 203 in the sliding process of the scraper 211 and are finally discharged from the impurity outlet 105 arranged at the left side of the box body 101, after the suspended aerosol removing process in the emulsion is completed, the turning plate 106 is opened and is finally controlled to be closed by the liquid level meter 104 along with the descending of the height of the emulsion, the emulsion enters the settling cavity 107, because of the V-shaped structure of the settling cavity 107, the high-density settled impurities in the emulsion are gathered at the bottom of the V-shaped structure of the settling cavity 107, the inner wall of the precipitation cavity 107 is kept clean while impurities are removed, the discharge opening 301 is opened after a period of time for precipitation, emulsion flows into the pipeline 302 through the discharge opening 301, the boss 303 arranged in the pipeline 302 plays a role in intercepting, the emulsion is redirected at the boss 303 and flows through the interior of the valve body 304, the through side of the interior of the surface of the valve body 304 is communicated with the pipeline 302, the exterior of the surface of the valve body 304 is sealed, the emulsion has to be communicated to the pipeline 302 at the other side through the through side end surface of the interior of the valve body 304, high-density bottom impurities in the emulsion can be retained in the filter cartridge 306 under the filtering action of the filter cartridge 306 attached to the inner wall of the valve body 304, and then a user drives the filter cartridge 306 to be separated from the interior of the valve body 304 by rotating the threaded sleeve 307 arranged on the bottom end surface of the valve body 304 and meshed with the threaded end 305, so as to remove the accumulated impurities in the filter cartridge 306, the emulsion filtered by the valve body 304 finally flows into the recovery tank 308 to be recycled.

Claims (9)

1. A precipitation equipment with edulcoration structure for emulsion is handled includes:

an impurity removal main body (1);

it is characterized by also comprising:

the aerosol impurity removal mechanism (2) is movably arranged inside the impurity removal main body (1);

the aerosol impurity removal mechanism (2) comprises:

a track (201);

spout (202), it sets up in track (201) bottom, deflector (203) are installed on spout (202) right side, spout (202) internally mounted has sliding seat (204), telescopic link (205) are installed to sliding seat (204) left side input, short connecting rod (206) are installed to sliding seat (204) right side terminal surface, short connecting rod (206) are kept away from sliding seat (204) one end is installed slider (207), long connecting rod (208) are installed to sliding seat (204) left side terminal surface, filter plate (209) are installed to slider (207) top terminal surface, down tube (210) are installed at filter plate (209) top, down tube (210) outside cover is equipped with scraper blade (211).

2. The emulsion processing sedimentation apparatus with an impurity removing structure according to claim 1, wherein the guide plate (203) is fixedly installed on the right end face of the chute (202), the top of the guide plate (203) is inclined to the right, and the sliding seat (204) is movably installed inside the chute (202).

3. The emulsion processing sedimentation equipment with an impurity removing structure is characterized in that a short connecting rod (206) is rotatably installed on the right end face of the sliding seat (204), a telescopic rod (205) and the short connecting rod (206) form a transmission structure through the sliding seat (204), a long connecting rod (208) is rotatably installed on the left end face of the sliding seat (204), and a sliding block (207) is rotatably installed at one end, far away from the sliding seat (204), of the long connecting rod (208).

4. The emulsion processing sedimentation device with the impurity removing structure is characterized in that the slide block (207) is movably mounted inside the track (201), the length of the slide block (207) is smaller than that of the filter plate (209) fixedly mounted on the top end face, an inclined rod (210) inclined to the left is fixedly mounted on the top end face of the filter plate (209), and a scraper (211) is movably mounted on the surface end of the inclined rod (210).

5. The precipitation apparatus for emulsion treatment with edulcoration structure according to claim 1, wherein the edulcoration body (1) comprises:

the device comprises a box body (101), wherein a track (201) is fixedly arranged on the inner side of the top of the box body (101);

the aerosol cavity (102) is arranged on the right side of the inner cavity of the box body (101), and a liquid supplementing port (103) is formed in the end face of the bottom of the aerosol cavity (102).

6. The precipitation apparatus for emulsion treatment with edulcoration structure according to claim 5, wherein the edulcoration main body (1) further comprises:

the liquid level meter (104) is attached to the bottom of the inner side of the aerosol cavity (102), and an impurity outlet (105) is formed in the top end face of the aerosol cavity (102);

the turning plate (106) is rotatably installed on the inner side of the bottom of the box body (101), the liquid level meter (104) is electrically connected with the turning plate (106) and the telescopic rod (205) respectively, a settling chamber (107) is formed in the left side of the inner cavity of the box body (101), and the cross section of the settling chamber (107) is V-shaped.

7. The emulsion processing sedimentation equipment with an impurity removal structure as claimed in claim 6, wherein a sedimentation impurity removal mechanism (3) is movably mounted at the bottom of the sedimentation cavity (107);

the precipitation impurity removal mechanism (3) comprises:

the discharge opening (301) is formed in the end face of the bottom of the sedimentation cavity (107) with the V-shaped section;

the pipeline (302) is arranged at the bottom of the discharge opening (301), and a boss (303) is fixedly arranged in the pipeline (302).

8. The emulsion processing precipitation apparatus with impurity removing structure as claimed in claim 7, wherein said precipitation impurity removing mechanism (3) further comprises:

the valve body (304) is fixedly installed at the bottom of the boss (303), one side of the inner cavity of the surface-phase pipeline (302) of the valve body (304) is in a transparent state, one side of the valve body (304) departing from the inner cavity of the pipeline (302) is in a closed state, the valve body (304) is obliquely installed inside the pipeline (302), and a threaded end (305) is formed in the end face of the bottom of the valve body (304).

9. The emulsion processing precipitation apparatus with impurity removing structure as claimed in claim 8, wherein said precipitation impurity removing mechanism (3) further comprises:

the filter cartridge (306) is movably mounted inside the valve body (304), the end face of the filter cartridge (306) is attached to the inner wall of the valve body (304), a threaded sleeve (307) is fixedly mounted at the bottom of the filter cartridge (306), the threaded sleeve (307) is mounted on the end face of the bottom of the valve body (304), and a recovery tank (308) is mounted on one side, far away from the discharge opening (301), of the pipeline (302).

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