Efficient emulsion breaking and separating device

Abstract

The invention discloses an efficient emulsion breaking and separating device which comprises an extraction bin and a bidirectional stirring mechanism, the rear end of the extraction bin is communicated with the upper end of the solution recycling bin through a first connecting pipe, the rear end of the solution recycling bin is communicated with the rear end of the supplementing bin through a second connecting pipe, the front end of the supplementing bin is communicated with the upper end of the extraction bin through a third connecting pipe, a driving bin is arranged at the upper end of the extraction bin, and a feeding pipe is arranged at the lower end of the extraction bin; the bidirectional stirring mechanism is arranged between the driving bin and the extraction bin, a control box is arranged on the right side of the extraction bin, a control switch group is arranged in the control box, and the input end of the control switch group is electrically connected with an external power source. The extraction efficiency of chlorobenzene is effectively improved, meanwhile, the chlorobenzene solvent in the emulsion can be effectively recovered and recycled, the energy consumption in the recovery process is greatly reduced, and the economic benefit is remarkable.

Description

Technical Field

[0001] The invention relates to the technical field of chlorobenzene recovery, in particular to an emulsion high-efficiency demulsification and separation device. Background Art

[0002] The design of the emulsion high-efficiency demulsification and separation device is to effectively separate the oil and water phases in the emulsion by physical or chemical methods. Chlorobenzene extraction refers to the use of chlorobenzene as an extractant to selectively dissolve certain components from the mixture, thereby separating these components from other components. Based on the difference in solubility of different substances in chlorobenzene, the selective solubility of chlorobenzene is used to achieve separation and purification;

[0003] Some of the existing emulsion high-efficiency demulsification and separation devices use a single-axis unidirectional stirring method to mix the chlorobenzene emulsion and the acetone extractant, and some of the emulsion high-efficiency demulsification and separation devices use a distillation method to recover chlorobenzene.

[0004] There are some problems with this type of traditional high-efficiency emulsion demulsification and separation device. For example, the use of a single-axis unidirectional stirring method may affect the mixing efficiency of the chlorobenzene emulsion and the acetone extractant. The use of distillation may require multiple distillation recovery, which may increase the energy consumption of the high-efficiency emulsion demulsification and separation device. Summary of the invention

[0005] The technical problem to be solved by the present invention is to overcome the existing defects and provide an emulsion high-efficiency demulsification and separation device, which can realize high-efficiency stirring and mixing of chlorobenzene emulsion and acetone extractant, effectively improve the extraction efficiency of chlorobenzene, and at the same time can effectively recover the chlorobenzene solvent in the emulsion and recycle it, greatly reducing the energy consumption in the recovery process, with significant economic benefits, and can effectively solve the problems in the background technology.

[0006] To achieve the above-mentioned object, the present invention provides the following technical solutions: an emulsion efficient demulsification and separation device, comprising an extraction chamber and a bidirectional stirring mechanism;

[0007] Extraction chamber: its rear end is connected with the upper end of the solution recovery chamber through connecting pipe 1, the rear end of the solution recovery chamber is connected with the rear end of the supplement chamber through connecting pipe 2, the front end of the supplement chamber is connected with the upper end of the extraction chamber through connecting pipe 3, the upper end of the extraction chamber is provided with a driving chamber, and the lower end of the extraction chamber is provided with a feeding pipe;

[0008] Bidirectional stirring mechanism: It is arranged between the driving chamber and the extraction chamber, and can realize efficient stirring and mixing of chlorobenzene emulsion and acetone extractant, effectively improving the extraction efficiency of chlorobenzene. At the same time, it can effectively recover the chlorobenzene solvent in the emulsion and recycle it, greatly reducing the energy consumption in the recovery process, and achieving significant economic benefits.

[0009] Furthermore, a control box is provided on the right side of the extraction chamber, and a control switch group is provided inside the control box. The input end of the control switch group is electrically connected to an external power supply to control various electrical appliances.

[0010] Furthermore, the bidirectional stirring mechanism includes a rotating column, a rotating drum, a passive gear, a driving handle, a gear, an inner gear ring and a stirring rod. The rotating column is rotatably connected between the driving chamber and the extraction chamber, the lower end of the rotating column is fixedly connected with a propeller blade, the lower end of the rotating column is fixedly connected with a passive gear, the outer surface of the rotating column is sleeved with a rotating drum, the middle part of the outer surface of the rotating drum is rotatably connected to the upper end of the extraction chamber, the lower end of the rotating drum is fixedly connected with a driving handle, the end of the driving handle away from the center of the rotating drum is rotatably connected with a stirring rod, the lower end of the stirring rod is fixedly connected with evenly distributed stirring blades, the upper end of the stirring rod is fixedly connected with a gear, the gears are meshed with the passive gear, the inner gear ring is fixedly connected to the upper end of the inner wall of the extraction chamber, and the gears are meshed with the inner gear ring to achieve bidirectional stirring and mixing of chlorobenzene emulsion and acetone reagent.

[0011] Furthermore, the bidirectional stirring mechanism also includes a motor and a worm, the worm is rotatably connected between two symmetrically distributed supports at the right end of the driving bin, the upper end of the rotating drum is fixedly connected to a worm wheel, the worm is meshingly connected to the worm wheel, and a motor is arranged at the rear end of the rear support, the output shaft of the motor is fixedly connected to the rear end of the worm, and the input end of the motor is electrically connected to the output end of the control switch group, so as to provide driving force for bidirectional stirring and mixing of the chlorobenzene emulsion and the acetone reagent.

[0012] Furthermore, a mounting plate is fixedly connected to the lower end of the inner wall of the solution recovery bin, a branch sieve barrel is arranged at the upper end of the mounting plate, two heating tubes are arranged at the lower end of the inner wall of the solution recovery bin, the input ends of the heating tubes are electrically connected to the output ends of the control switch group, and the upper end of the solution recovery bin is connected to a bin cover by bolts to provide heat for chlorobenzene to separate from the molecular sieve barrel.

[0013] Furthermore, infusion pumps are provided inside the connecting tube 1 and the connecting tube 2, and the input ends of the infusion pumps are electrically connected to the output ends of the control switch group to provide driving force for the movement of chlorobenzene and acetone.

[0014] Furthermore, a cooling bin is provided inside the inner wall of the solution recovery bin, a spiral sheet is fixedly connected inside the cooling bin, a water inlet pipe is provided at the upper end of the cooling bin, and a water outlet pipe is provided at the lower end of the cold water bin to facilitate cooling of the molecular sieve barrel.

[0015] Furthermore, the lower ends of the extraction chamber and the solution recovery chamber are both provided with discharge pipes, the middle parts of the discharge pipes are both provided with electric valves, the input ends of the electric valves are both electrically connected to the output ends of the control switch group to control the removal of water and chlorobenzene.

[0016] Furthermore, the lower ends of the extraction bin and the solution recovery bin are fixedly connected with evenly distributed leg one, the lower end of the replenishment bin is fixedly connected with symmetrically distributed leg two, and the lower ends of leg one and leg two are provided with evenly distributed mounting holes, which effectively ensures the smooth demulsification of the chlorobenzene emulsion.

[0017] Compared with the prior art, the beneficial effects of the present invention are: the high-efficiency emulsion demulsification and separation device has the following advantages:

[0018] 1. Personnel realize the operation of the motor by controlling the switch group. The output shaft of the motor rotates to drive the worm, and then drives the worm wheel to rotate. The rotation of the worm wheel drives the drum to rotate. The rotation of the drum drives the three stirring rods to rotate around the central axis of the drum. The rotation of the stirring rods drives the vertically adjacent gears to rotate around the central axis of the drum. The gears rotate under the action of the inner gear ring. The rotation of the gears drives the vertically adjacent stirring rods to rotate, thereby realizing the stirring of the outer layer inside the extraction chamber. At the same time, the rotation of the three gears causes the passive gear to rotate. The rotation of the passive gear drives the rotating column to rotate. The rotation of the rotating column drives the propeller blades to rotate, realizing the stirring of the inner layer inside the extraction chamber, which can realize the efficient stirring and mixing of chlorobenzene emulsion and acetone extractant, and effectively improve the extraction efficiency of chlorobenzene.

[0019] 2. When the chlorobenzene emulsion and the acetone extractant are mixed to a certain degree, the personnel turn off the motor by controlling the switch group, so that the extraction phase and the residual phase are statically separated. After the static state is completed, the personnel realize the operation of the electric valve on the front side by controlling the switch group. The electric valve on the front side is opened, and the extracted water is removed through the discharge pipe on the front side and enters the external wastewater treatment unit. After the water is removed, the personnel close the electric valve on the front side by controlling the switch group and realize the operation of the infusion pump on the front side. The infusion pump pumps the extraction phase into the solution recovery bin through the connecting pipe 1, and the mixture of chlorobenzene and acetone falls into the molecular sieve barrel. The chlorobenzene molecules will interact with the molecular sieve barrel material. According to the pore size and surface properties of the molecular sieve, the chlorobenzene molecules are adsorbed on the surface of the molecular sieve barrel, thereby realizing separation from acetone. At the same time, the personnel realize the operation of the infusion pump on the rear side by controlling the switch group. The separated acetone is pumped into the interior of the replenishing bin through the connecting pipe 2, thereby realizing the recovery of acetone. After the molecular sieve barrel is adsorbed, the personnel closes the infusion pump on the rear side by controlling the switch group, and realizes the operation of the heating pipe and the electric valve on the rear side. The heating pipe provides heat to make the chlorobenzene molecules separate from the molecular sieve barrel and enter the external chlorobenzene recovery tank through the discharge pipe on the rear side. After the chlorobenzene is removed, the personnel closes the heating pipe by controlling the switch group, and injects cooling water into the cooling bin through the water inlet pipe. The cooling water spirally descends slowly under the action of the spiral blades, thereby realizing the cooling of the molecular sieve barrel, and then waiting for the next adsorption of chlorobenzene molecules, which greatly reduces the energy consumption in the process of chlorobenzene solvent recovery, treatment and recycling, effectively improves the economic benefits, can effectively recover the chlorobenzene solvent in the emulsion and recycle it, greatly reduces the energy consumption in the recovery process, and has significant economic benefits. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 It is a schematic diagram of the structure of the present invention;

[0021] Figure 2 It is a schematic diagram of the cross-sectional structure inside the present invention;

[0022] Figure 3 It is a structural schematic diagram of the rear side of the present invention;

[0023] Figure 4 It is a schematic diagram of the enlarged structure of point A of the present invention.

[0024] In the figure: 1 extraction chamber, 2 solution recovery chamber, 3 replenishment chamber, 4 drive chamber, 5 two-way stirring mechanism, 51 motor, 52 worm, 53 rotating column, 54 drum, 55 passive gear, 56 driving handle, 57 gear, 58 internal gear ring, 59 stirring rod, 6 connecting pipe 1, 7 heating pipe, 8 cooling chamber, 9 spiral sheet, 10 water inlet pipe, 11 water outlet pipe, 12 infusion pump, 13 connecting pipe 2, 14 molecular sieve barrel, 15 chamber cover, 16 electric valve, 17 connecting pipe 3, 18 feeding pipe, 19 supporting leg 1, 20 control box, 21 control switch group, 22 supporting leg 2. DETAILED DESCRIPTION

[0025] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0026] See also Figure 1-4 , this embodiment provides a technical solution: an emulsion efficient demulsification and separation device, comprising an extraction chamber 1 and a bidirectional stirring mechanism 5;

[0027] Extraction chamber 1: its rear end is connected with the upper end of solution recovery chamber 2 through connection pipe 1 6, the rear end of solution recovery chamber 2 is connected with the rear end of supplement chamber 3 through connection pipe 2 13, the front end of supplement chamber 3 is connected with the upper end of extraction chamber 1 through connection pipe 3 17, the upper end of extraction chamber 1 is provided with driving chamber 4, the lower end of extraction chamber 1 is provided with feeding pipe 18, the right side of extraction chamber 1 is provided with control box 20, the interior of control box 20 is provided with control switch group 21, the input end of control switch group 21 is electrically connected with external power supply, the lower ends of extraction chamber 1 and solution recovery chamber 2 are fixedly connected with evenly distributed support legs 1 19, the lower end of supplement chamber 3 is fixedly connected with symmetrically distributed support legs 22, the lower ends of support legs 19 and support legs 2 22 are provided with evenly distributed mounting holes;

[0028] Bidirectional stirring mechanism 5: It is arranged between driving chamber 4 and extraction chamber 1, and comprises rotating column 53, rotating drum 54, passive gear 55, driving handle 56, gear 57, inner gear ring 58 and stirring rod 59. Rotating column 53 is rotatably connected between driving chamber 4 and extraction chamber 1, and the lower end of rotating column 53 is fixedly connected with propeller blade, and the lower end of rotating column 53 is fixedly connected with passive gear 55. The outer surface of rotating column 53 is sleeved with rotating drum 54, and the central axis of rotating column 53, rotating drum 54 and extraction chamber 1 coincides, and the middle part of the outer surface of rotating drum 54 coincides with the central axis of extraction chamber 1. The upper end of the extraction chamber 1 is rotatably connected, and the lower end of the rotating drum 54 is fixedly connected to a driving handle 56. The end of the driving handle 56 away from the center of the rotating drum 54 is rotatably connected to a stirring rod 59. The lower end of the stirring rod 59 is fixedly connected to a stirring blade evenly distributed. The upper end of the stirring rod 59 is fixedly connected to a gear 57. The gear 57 is meshed with the passive gear 55. The inner gear ring 58 is fixedly connected to the upper end of the inner wall of the extraction chamber 1. The gear 57 is meshed with the inner gear ring 58. The bidirectional stirring mechanism 5 also includes a motor 51 and a worm 52. The worm 52 is rotatably connected to the driving chamber 4, a worm wheel is fixedly connected to the upper end of the rotating drum 54, and the worm 52 is meshed with the worm wheel. A motor 51 is arranged at the rear end of the rear support, and the output shaft of the motor 51 is fixedly connected to the rear end of the worm 52. The input end of the motor 51 is electrically connected to the output end of the control switch group 21. The motor 41 is operated by the control switch group 21. The output shaft of the motor 41 rotates to drive the worm 52 to rotate, and then drives the worm wheel to rotate. The rotation of the worm wheel drives the rotating drum 54 to rotate. The rotation of the rotating drum 54 drives the three stirring rods 59 to rotate around the center of the rotating drum 54. The central axis rotates, and the stirring rod 59 rotates to drive the vertically adjacent gears 57 to rotate around the central axis of the rotating drum 54. The gears 57 rotate under the action of the inner gear ring 58. The rotation of the gears 57 drives the vertically adjacent stirring rods 59 to rotate, thereby achieving stirring of the outer layer inside the extraction chamber 1. At the same time, the three gears 57 rotate to rotate the passive gear 55. The rotation of the passive gear 55 drives the rotating column 53 to rotate. The rotation of the rotating column 53 drives the propeller blades to rotate, thereby achieving stirring of the inner layer inside the extraction chamber 1, thereby achieving efficient stirring and mixing of the chlorobenzene emulsion and the acetone extractant.

[0029] Wherein: the lower end of the inner wall of the solution recovery bin 3 is fixedly connected with a mounting plate, the upper end of the mounting plate is provided with a branch screen barrel 14, the lower end of the inner wall of the solution recovery bin 3 is provided with two heating tubes 7, the input ends of the heating tubes 7 are electrically connected to the output ends of the control switch group 21, the upper end of the solution recovery bin 3 is connected with a bin cover 15 by bolts, the inner wall of the solution recovery bin 1 is provided with a cooling bin 8, the inner part of the cooling bin 8 is fixedly connected with a spiral sheet 9, the upper end of the cooling bin 8 is provided with a water inlet pipe 10, and the lower end of the cold water bin 8 is provided with a water outlet pipe 11, and the chlorobenzene emulsion and acetone are heated to 1000 ℃. The extractant is mixed to a certain degree, and the motor 51 is turned off by controlling the switch group 21, so that the extraction phase and the residual phase are statically separated. After the static state is completed, the electric valve 16 on the front side is operated by controlling the switch group 21, and the electric valve 16 on the front side is opened. The extracted water is removed through the discharge pipe on the front side and enters the external wastewater treatment unit. After the water is removed, the electric valve 16 on the front side is closed by controlling the switch group 21 and the infusion pump 12 on the front side is operated. The infusion pump 12 pumps the extraction phase into the solution recovery bin 2 through the connecting pipe 6, and chlorobenzene and propylene are removed. The mixture of ketones falls into the interior of the molecular sieve barrel 14, and the chlorobenzene molecules interact with the material of the molecular sieve barrel 14. According to the pore size and surface properties of the molecular sieve, the chlorobenzene molecules are adsorbed on the surface of the molecular sieve barrel 14, thereby achieving separation from acetone. At the same time, the infusion pump 12 on the rear side is operated by controlling the switch group 21, and the separated acetone is pumped into the interior of the replenishment bin 3 through the connecting pipe 2 13, thereby achieving acetone recovery. After the molecular sieve barrel 7 is adsorbed, the infusion pump 12 on the rear side is turned off by controlling the switch group 21, and the heating pipe 7 and the rear side are heated. The electric valve 16 is in operation, and the heating tube 7 provides heat, so that the chlorobenzene molecules are separated from the molecular sieve barrel 14 and enter the external chlorobenzene recovery tank through the discharge pipe on the rear side. After the chlorobenzene is removed, the heating tube 7 is turned off by controlling the switch group 21, and cooling water is injected into the cooling bin 8 through the water inlet pipe 10. The cooling water spirally descends slowly under the action of the spiral sheet 9, thereby cooling the molecular sieve barrel 14, and then waiting for the next adsorption of chlorobenzene molecules, which greatly reduces the energy consumption in the process of chlorobenzene solvent recovery and recycling, and effectively improves the economic benefits;

[0030] Wherein: the interior of the connecting tube 1 6 and the connecting tube 2 13 are both provided with an infusion pump 12, and the input end of the infusion pump 12 is electrically connected to the output end of the control switch group 21;

[0031] The lower ends of the extraction chamber 1 and the solution recovery chamber 2 are both provided with discharge pipes, the middle parts of the discharge pipes are both provided with electric valves 16 , and the input ends of the electric valves 16 are both electrically connected to the output ends of the control switch group 21 .

[0032] The working principle of an emulsion efficient demulsification and separation device provided by the present invention is as follows: during operation, personnel use mounting bolts to stably connect the mounting holes at the lower ends of the support legs 19 and the support legs 22 with the threaded holes in the horizontal working area, thereby realizing the stable installation of the extraction chamber 1, the solution recovery chamber 2, the replenishment chamber 3 and other mechanisms. After the installation is stable, personnel add chlorobenzene emulsion through the inside of the feed pipe 18, and at the same time add the acetone extractant in the replenishment chamber 3 to the inside of the extraction chamber 1 through the connecting pipe 3 17. Then, personnel realize the operation of the motor 41 by controlling the switch group 21. The output shaft of the motor 41 rotates to drive the worm 52 to rotate, thereby driving the worm wheel to rotate. The rotation of the worm wheel drives the rotating drum 54 to rotate. The rotation of the rotating drum 54 drives the three stirring rods 59 to rotate around the rotating drum 54. The central axis rotates, and the stirring rod 59 rotates to drive the vertically adjacent gears 57 to rotate around the central axis of the rotating drum 54. The gears 57 rotate under the action of the inner gear ring 58. The rotation of the gears 57 drives the vertically adjacent stirring rods 59 to rotate, thereby achieving the stirring of the inner and outer layers of the extraction chamber 1. At the same time, the rotation of the three gears 57 causes the passive gear 55 to rotate, and the rotation of the passive gear 55 drives the rotating column 53 to rotate. The rotation of the rotating column 53 drives the propeller blades to rotate, thereby achieving the stirring of the inner layer of the extraction chamber 1, thereby achieving efficient stirring and mixing of the chlorobenzene emulsion and the acetone extractant. When the chlorobenzene emulsion and the acetone extractant are mixed to a certain extent, the personnel turn off the motor 51 by controlling the switch group 21, so that the extraction phase and the residual phase are statically separated. After the static state is completed, the personnel pass The control switch group 21 realizes the operation of the electric valve 16 on the front side. The electric valve 16 on the front side is opened, and the extracted water is removed through the discharge pipe on the front side and enters the external wastewater treatment unit. After the water is removed, the personnel closes the electric valve 16 on the front side and realizes the operation of the infusion pump 12 on the front side through the control switch group 21. The infusion pump 12 pumps the extraction phase into the solution recovery bin 2 through the connecting pipe 16. The mixture of chlorobenzene and acetone falls into the molecular sieve barrel 14. The chlorobenzene molecules interact with the material of the molecular sieve barrel 14. According to the pore size and surface properties of the molecular sieve, the chlorobenzene molecules are adsorbed on the surface of the molecular sieve barrel 14, thereby realizing separation from the acetone. At the same time, the personnel realizes the operation of the infusion pump 12 on the rear side through the control switch group 21 to separate the separated Acetone is pumped into the interior of the replenishing bin 3 through the connecting pipe 2 13, thereby realizing the recovery of acetone. After the molecular sieve barrel 7 is adsorbed, the personnel closes the infusion pump 12 on the rear side by controlling the switch group 21, and realizes the operation of the heating pipe 7 and the electric valve 16 on the rear side. The heating pipe 7 provides heat to make the chlorobenzene molecules separate from the molecular sieve barrel 14 and enter the external chlorobenzene recovery tank through the discharge pipe on the rear side. After the chlorobenzene is removed, the personnel closes the heating pipe 7 by controlling the switch group 21, and injects cooling water into the interior of the cooling bin 8 through the water inlet pipe 10. The cooling water spirally descends slowly under the action of the spiral sheet 9, thereby realizing the cooling of the molecular sieve barrel 14, and then waiting for the next adsorption of chlorobenzene molecules, which greatly reduces the energy consumption in the process of chlorobenzene solvent recovery, treatment and recycling.Effectively improve economic benefits.

[0033] It is worth noting that the motor 51 disclosed in the above embodiment can use a YE3-225M-4P 45KW three-phase asynchronous motor, the heating tube 7 can use a DN50 heating tube, the infusion pump 12 can use an MDS stainless steel vortex magnetic pump, the electric valve 16 can use a JG90-D3-DQ-MF7 electric butterfly valve, and the control switch group 21 is provided with control buttons corresponding to the motor 51, the heating tube 7, the infusion pump 12 and the electric valve 16.

[0034] The above descriptions are merely embodiments of the present invention and are not intended to limit the patent scope of the present invention. Any equivalent structure or equivalent process transformation made using the contents of the present invention specification and drawings, or directly or indirectly applied in other related technical fields, are also included in the patent protection scope of the present invention.

Claims

1. An emulsion efficient demulsification and separation device, characterized in that: It comprises an extraction chamber (1) and a bidirectional stirring mechanism (5); The extraction chamber (1) has a rear end connected to the upper end of the solution recovery chamber (2) through a connecting pipe 1 (6), the rear end of the solution recovery chamber (2) is connected to the rear end of the supplement chamber (3) through a connecting pipe 2 (13), the front end of the supplement chamber (3) is connected to the upper end of the extraction chamber (1) through a connecting pipe 3 (17), the upper end of the extraction chamber (1) is provided with a driving chamber (4), and the lower end of the extraction chamber (1) is provided with a feeding pipe (18); Bidirectional stirring mechanism (5): It is arranged between the driving chamber (4) and the extraction chamber (1).

2. The emulsion efficient demulsification and separation device according to claim 1, characterized in that: A control box (20) is arranged on the right side of the extraction chamber (1), a control switch group (21) is arranged inside the control box (20), and an input end of the control switch group (21) is electrically connected to an external power supply.

3. The emulsion efficient demulsification and separation device according to claim 2, characterized in that: The bidirectional stirring mechanism (5) comprises a rotating column (53), a rotating drum (54), a passive gear (55), a driving handle (56), a gear (57), an inner gear ring (58) and a stirring rod (59); the rotating column (53) is rotatably connected between the driving chamber (4) and the extraction chamber (1); a propeller blade is fixedly connected to the lower end of the rotating column (53); the passive gear (55) is fixedly connected to the lower end of the rotating column (53); the rotating drum (54) is sleeved on the outer surface of the rotating column (53); the middle part of the outer surface of the rotating drum (54) is in contact with the extraction chamber (1); The upper end of the rotating drum (54) is rotatably connected to the upper end of the rotating drum (1), the lower end of the rotating drum (54) is fixedly connected to a driving handle (56), one end of the driving handle (56) away from the center of the rotating drum (54) is rotatably connected to a stirring rod (59), the lower end of the stirring rod (59) is fixedly connected to stirring blades evenly distributed, the upper end of the stirring rod (59) is fixedly connected to a gear (57), the gear (57) is meshed with the driven gear (55), the inner gear ring (58) is fixedly connected to the upper end of the inner wall of the extraction chamber (1), and the gear (57) is meshed with the inner gear ring (58).

4. The emulsion efficient demulsification and separation device according to claim 3, characterized in that: The bidirectional stirring mechanism (5) further comprises a motor (51) and a worm (52); the worm (52) is rotatably connected between two symmetrically distributed supports at the right end of the driving chamber (4); a worm wheel is fixedly connected to the upper end of the rotating drum (54); the worm wheel (52) is meshingly connected to the worm wheel; a motor (51) is arranged at the rear end of the rear support; an output shaft of the motor (51) is fixedly connected to the rear end of the worm wheel (52); and an input end of the motor (51) is electrically connected to an output end of the control switch group (21).

5. The high-efficiency emulsion demulsification and separation device according to claim 1, characterized in that: The lower end of the inner wall of the solution recovery bin (3) is fixedly connected to a mounting plate, the upper end of the mounting plate is provided with a branch screen barrel (14), the lower end of the inner wall of the solution recovery bin (3) is provided with two heating tubes (7), the input ends of the heating tubes (7) are electrically connected to the output ends of the control switch group (21), and the upper end of the solution recovery bin (3) is connected to a bin cover (15) by bolts.

6. The high-efficiency emulsion demulsification and separation device according to claim 2, characterized in that: The connecting tube 1 (6) and the connecting tube 2 (13) are both provided with an infusion pump (12), and the input end of the infusion pump (12) is electrically connected to the output end of the control switch group (21).

7. The high-efficiency emulsion demulsification and separation device according to claim 1, characterized in that: A cooling bin (8) is arranged inside the inner wall of the solution recovery bin (1), a spiral blade (9) is fixedly connected inside the cooling bin (8), a water inlet pipe (10) is arranged at the upper end of the cooling bin (8), and a water outlet pipe (11) is arranged at the lower end of the cold water bin (8).

8. The high-efficiency emulsion demulsification and separation device according to claim 2, characterized in that: The lower ends of the extraction chamber (1) and the solution recovery chamber (2) are both provided with discharge pipes, the middle parts of the discharge pipes are both provided with electric valves (16), and the input ends of the electric valves (16) are both electrically connected to the output ends of the control switch group (21).

9. The high-efficiency emulsion demulsification and separation device according to claim 1, characterized in that: The lower ends of the extraction chamber (1) and the solution recovery chamber (2) are fixedly connected with evenly distributed support legs (19), the lower end of the replenishment chamber (3) is fixedly connected with symmetrically distributed support legs (22), and the lower ends of the support legs (19) and the support legs (22) are both provided with evenly distributed mounting holes.

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