A grease recovery mechanism based on carbonized wool wastewater treatment
By combining rotary permeation and dynamic water pressure, and utilizing the synergistic effect of an anti-grease permeation membrane and a water-permeable filter, the problem of low grease concentration in carbonized wool wastewater was solved, thus improving the recovery efficiency of lanolin.
Patent Information
- Application Number
- CN202511494662.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-10-20
- Publication Date
- 2026-02-27
- Estimated Expiration
- 2045-10-20
AI Technical Summary
In existing technologies, the concentration of grease in carbonized wool wastewater is low, which leads to a reduced grease recovery rate and requires multiple heating separations, affecting the recovery efficiency.
By combining rotary effusion and dynamic water pressure, and through the synergistic effect of the anti-grease permeation membrane and the water-permeable filter, the grease concentration in wastewater is increased, the number of centrifugation separations is reduced, and the lanolin recovery rate is improved.
It significantly improves the recovery efficiency of lanolin, reduces the number of centrifugation separations, avoids multiple heating separations, and enhances recovery efficiency.
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Figure CN120965046B_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The present application relates to the technical field of wastewater treatment, and particularly relates to a grease recovery mechanism based on carbonized wool wastewater treatment. BACKGROUND
[0002] Carbonized wool is a process of removing plant cellulose substances in wool by chemical method combined with mechanical treatment according to the characteristics that wool is acid-resistant and plant matter is not acid-resistant. In the processing of carbonized wool, wool also needs to go through the process of washing wool. Wool grease is a kind of secreted grease attached to wool, which is a soft paste of light yellow or brown yellow, has viscosity and smoothness, has weak and specific smell, and will melt into wastewater during washing wool.
[0003] After the completion of washing wool and discharge, wool grease will be recovered from wastewater. At present, the traditional centrifugal separation method and extraction method are commonly used at home and abroad.
[0004] The centrifugal separation method is to separate wool grease from wastewater by using a high-speed centrifuge. At present, the separation is mainly performed by a disc centrifuge. Before centrifugal separation, the washing wool wastewater needs to be treated and heated.
[0005] Before entering the separator for separation, the washing wool wastewater needs to remove larger suspended particles by sedimentation and then be heated to enter the centrifuge to complete centrifugal separation to separate water phase, oil phase and residue phase. However, since the grease concentration suitable for centrifugal separation is generally above 15 g / L, when the concentration is lower than 10 g / L, the recovery rate of wool grease will be reduced. In general, the treatment process of wool grease-containing wastewater cannot help to increase the grease concentration in the waste liquid, so that the separated oil phase needs to be heated again for oil-water separation to obtain crude wool grease after recovery, which affects the wool grease recovery efficiency. SUMMARY
[0006] The present application provides a grease recovery mechanism based on carbonized wool wastewater treatment, which can increase the grease concentration of wastewater by removing water in wastewater through rotary exudation after the completion of the sedimentation step, thereby solving the problems in the background art, that is:
[0007] When the waste liquid with low grease concentration is separated, the recovery rate of wool grease will be reduced, so that the separated oil phase needs to be heated again for oil-water separation to obtain crude wool grease after recovery, which has low recovery efficiency.
[0008] In order to achieve the above object, the present application provides a grease recovery mechanism based on carbonized wool wastewater treatment, which comprises a centrifugal separator and a heating tank connected to the feed inlet of the centrifugal separator, and further comprises a wastewater water removal mechanism connected to the feed inlet of the heating tank, wherein the wastewater water removal mechanism comprises an outer tank, an inner tank for introducing wastewater, and a water removal assembly, the outer tank comprises a support frame, a metal shielding tank, and an inner heating element arranged on the inner wall of the shielding tank, and the inner tank is arranged inside the shielding tank;
[0009] The water removal assembly comprises a rotating dewatering assembly and a guided stirring assembly.
[0010] The rotating dewatering assembly comprises a water-permeable filter arranged along the central axis of the inner tank and a driving element for driving the rotation of the water-permeable filter, the water-permeable filter comprises an oil-proof permeable membrane and a water-permeable filter screen arranged around the water-permeable filter, and an annular water body exosmosis area is formed inside the inner tank.
[0011] The guided stirring assembly is arranged below the inner tank and acts on the water body exosmosis area of the oil-proof permeable membrane to form multiple guided exosmosis and static liquid stirring of the wastewater.
[0012] The water-permeable filter further comprises a shaped mounting frame, the shaped mounting frame is mounted at the center inside the inner tank, and a wastewater outlet pipeline is arranged at the connection between the bottom end of the shaped mounting frame and the inner tank, the wastewater outlet pipeline is connected to the feed inlet of the heating tank, the shaped mounting frame is an annular frame body, the top end of the shaped mounting frame is provided with a rubber ring, and the bottom end of the shaped mounting frame is a concave metal bottom ring, and the oil-proof permeable membrane and the water-permeable filter screen are arranged around the outer side of the shaped mounting frame.
[0013] The water-permeable filter screen is an annular pleated filter screen, the inner side of the water-permeable filter screen is attached to the oil-proof permeable membrane, the wastewater guide inlet of the top wall of the inner tank is located at the center of the oil-proof permeable membrane, and the bottom of the inner tank is provided with a drain hole corresponding to the water-permeable filter screen.
[0014] The driving element is arranged at the end of the shielding tank, the output end of the driving element penetrates through the shielding tank and the top wall of the inner tank and is provided with a driving vane, and the driving vane is tightly attached to the rubber ring at the top end of the shaped mounting frame to transmit rotary power.
[0015] In this technical solution, through the synergistic effect of the oil-proof permeable membrane and the water-permeable filter screen, combined with the rotating centrifugal force and dynamic water pressure, the wastewater passing through the inner tank removes part of the water body, significantly reduces the water content of the wastewater, improves the grease concentration, reduces the number of subsequent centrifugal separations, and improves the wool grease recovery efficiency.
[0016] As a further improvement of the present technical solution, the guided stirring assembly comprises a guide cone, a shielding table, a control element, and a stirring element.
[0017] The shielding table is arranged above the connection between the wastewater leading pipe and the shaping mounting frame, the top surface of the shielding table is a conical surface, the lower half is a cylinder, the edge of the cylinder is attached to the inner wall of the grease-proof permeable membrane, the control member is arranged at the bottom end of the inner layer tank body, and the control end of the control member is connected to the shielding table, so that the shielding table can be controlled to rise and fall to open and close the wastewater leading pipe;
[0018] The stirring member is installed on the top of the shielding table, the guide cone is fixed to the top end of the stirring member and is attached to the inner wall of the grease-proof permeable membrane, the stirring member comprises a driving motor, a sealing ring and a stirring frame, the driving motor is arranged inside the hollow shielding table, the stirring frame is vertically rotatably installed on the top of the shielding table and is driven by the driving motor, the sealing ring is arranged at the connection between the stirring frame and the shielding table, and the guide cone is fixedly arranged at the end of the stirring frame.
[0019] The stirring frame comprises a rotating shaft connected with the driving motor and a stirring inclined rod arranged outside the rotating shaft, and the stirring inclined rod is located between the shielding table and the guide cone.
[0020] In the technical solution, the static water pressure dewatering and the dynamic extrusion dewatering steps are combined, when the wastewater stays, water is exuded by the static pressure of the liquid level, when the shielding table is controlled to move upward by the control member, the narrow channel between the shielding table and the grease-proof permeable membrane utilizes the flow resistance to form a local high pressure, further extruding the wastewater, realizing deep dewatering, and the dynamic design of the rotating grease-proof permeable membrane and the stirring assembly effectively avoids the accumulation of grease on the membrane surface, forms multiple guided exosmosis and static liquid stirring of the wastewater.
[0021] Compared with the prior art, the grease recovery mechanism based on carbonized wool wastewater treatment has the following beneficial effects:
[0022] In the technical solution, the wastewater flows into the inside of the grease-proof permeable membrane, through the cooperation of the grease-proof permeable membrane and the water-permeable filter screen, when the wastewater stays, water is exuded by the static pressure of the liquid level, when the shielding table is controlled to move upward by the control member, the narrow channel between the shielding table and the grease-proof permeable membrane utilizes the flow resistance to form a local high pressure, further extruding the wastewater, realizing deep dewatering, and the dynamic water pressure and the rotating centrifugal force are combined to remove part of the water in the wastewater through the inner layer tank body, significantly reducing the water content of the wastewater, improving the grease concentration, reducing the number of subsequent centrifugal separations, and improving the wool grease recovery efficiency.
[0023] In addition, the cooperation of the rotating grease-proof permeable membrane, the guide cone and the stirring member can avoid the accumulation of grease on the membrane surface, and ensure the efficiency of water exosmosis. BRIEF DESCRIPTION OF DRAWINGS
[0024] Figure 1 It is a schematic diagram of the overall structure of the present application;
[0025] Figure 2The overall structure schematic view of another aspect of the present application;
[0026] Figure 3 The structure schematic view of the wastewater removing mechanism in the present application;
[0027] Figure 4 The structure distribution view of the outer tank body, the inner tank body and the water removing assembly in the present application;
[0028] Figure 5 The structure distribution view of the outer tank body, the inner tank body, the water permeable filter and the guided stirring assembly in the present application;
[0029] Figure 6 The structure distribution view of the water permeable filter and the guided stirring assembly in the present application;
[0030] Figure 7 The structure sectional view of the water permeable filter, the stirring piece and the guided stirring assembly in the present application.
[0031] In the figure: 1, centrifugal separator; 2, heating tank body; 3, outer tank body; 31, support frame; 32, shielding tank; 33, inner heating piece; 4, inner tank body; 5, water removing assembly; 51, rotating dehydration assembly; 511, driving piece; 52, guided stirring assembly; 521, guided cone; 522, shielding table; 523, control piece; 6, water permeable filter; 61, grease permeation prevention membrane; 62, water permeable filter screen; 63, shaped mounting frame; 7, stirring piece; 71, driving motor; 72, sealing ring; 73, stirring frame; 8, wastewater leading-out pipeline. DETAILED DESCRIPTION
[0032] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments of the present application. Based on the embodiments in the present application, all the other embodiments obtained by those skilled in the art without creative work fall within the scope of protection of the present application.
[0033] With reference to Figure 1 , Figure 4 , Figure 6 and Figure 7 , the present application provides a grease recovery mechanism based on carbonized wool wastewater treatment. In order to absorb the water in the scouring wastewater after completing the sedimentation step, thereby increasing the grease concentration of the wastewater and increasing the subsequent lanolin centrifugal recovery rate, and avoiding multiple separation and recovery, a heating tank body 2 connected to the feed inlet of a centrifugal separator 1 is arranged, and a wastewater removing mechanism connected to the feed inlet of the heating tank body 2 is further arranged. The wastewater removing mechanism comprises an outer tank body 3, an inner tank body 4 and a water removing assembly 5.
[0034] As Figure 3 shown, the outer tank body 3 includes a support frame 31, a shielding tank 32 and an inner heating element 33, the shielding tank 32 is a metal tank, the inner heating element 33 is arranged on the inner wall of the shielding tank 32 and can provide heating function when needed, and the support frame 31 is arranged at the bottom end of the shielding tank 32.
[0035] The inner tank body 4 is arranged inside the shielding tank 32, and the end of the shielding tank 32 is provided with a connecting pipeline connecting the sedimentation part, and the connecting pipeline connects the inlet at the top wall center of the shielding tank 32 and the inner tank body 4.
[0036] As Figure 4 shown, the water removal assembly 5 includes a rotary dewatering assembly 51 and a guide stirring assembly 52, the rotary dewatering assembly 51 is arranged inside the inner tank body 4, the rotary dewatering assembly 51 includes a driving element 511 and a water-permeable filter element 6, the water-permeable filter element 6 includes a grease-proof permeable membrane 61, a water-permeable filter screen 62 and a shaped mounting frame 63, the shaped mounting frame 63 is mounted at the center inside the inner tank body 4, and a waste water guide pipeline 8 is arranged at the connection between the bottom end of the shaped mounting frame 63 and the inner tank body 4, the waste water guide pipeline 8 connects the inlet of the heating tank body 2, the driving element 511 is arranged at the end of the shielding tank 32, and the output end of the driving element 511 penetrates through the top wall of the shielding tank 32 and the inner tank body 4 and acts on the shaped mounting frame 63, the grease-proof permeable membrane 61 and the water-permeable filter screen 62 are both arranged around the shaped mounting frame 63, so that the wool washing waste water falling from the center of the top wall of the inner tank body 4 can fall into the water-permeable filter element 6, and then part of the water body can permeate through the grease-proof permeable membrane 61 and the water-permeable filter screen 62 after the action of the grease-proof permeable membrane 61 and the water-permeable filter screen 62, so as to reduce the water content in the wool washing waste liquid, thereby increasing the grease content, after water removal, the waste water is guided into the heating tank body 2 through the waste water guide pipeline 8, heated and then enters the centrifugal separator 1 for separation, so that the wool washing waste water can enter the subsequent process in a state of high grease content, thereby increasing the centrifugal recovery rate of lanolin.
[0037] As Figure 5As shown, the shaped mounting frame 63 is an annular frame body, and the shaped mounting frame 63 is divided into upper and lower two parts, wherein the upper half of the shaped mounting frame 63 is provided with a rubber ring at the edge, and the lower half is a concave metal bottom ring, and the lower half of the shaped mounting frame 63 is connected with the wastewater discharge pipeline 8, the grease-proof permeable membrane 61 and the water-permeable filter screen 62 are arranged around the upper half of the shaped mounting frame 63, and the grease-proof permeable membrane 61 is located on the inner side, and the water-permeable filter screen 62 is located on the outer side, the driving part 511 is a motor, and the motor output end is provided with a driving rotating piece, and the driving rotating piece closely fits the rubber ring of the upper half of the shaped mounting frame 63, so that the driving part 511 can drive the upper half of the shaped mounting frame 63 to rotate inside the inner layer tank body 4, so that the grease-proof permeable membrane 61 and the water-permeable filter screen 62 rotate synchronously, and the water body is permeated during rotation. In addition, the grease-proof permeable membrane 61 in motion state can avoid lanolin sticking.
[0038] The water-permeable filter screen 62 is an annular filter screen, and the screen body is provided with wrinkles, which can increase the water permeation area, help the water to quickly pass through the water-permeable filter screen 62 and flow out, and the water-permeable filter screen 62 can play a protective and shaping role outside the grease-proof permeable membrane 61, preventing the grease-proof permeable membrane 61 from deforming when the water pressure is too large.
[0039] The inner layer tank body 4 is provided with a water outlet corresponding to the water-permeable filter screen 62 at the bottom, for discharging the water permeated into the inner layer tank body 4.
[0040] The guide stirring assembly 52 is arranged inside the inner layer tank body 4, and the guide stirring assembly 52 acts on the middle of the water-permeable filter element 6.
[0041] As shown in the figure, Figure 6 The guide stirring assembly 52 includes a guide cone 521, a shielding table 522, a control part 523 and a stirring part 7, the shielding table 522 is arranged above the connection between the wastewater discharge pipeline 8 and the shaped mounting frame 63, and plays a role of shielding the wastewater discharge pipeline 8, so that the wastewater inside the inner layer tank body 4 cannot be discharged through the wastewater discharge pipeline 8, the control part 523 is arranged at the bottom end of the inner layer tank body 4, and the control end of the control part 523 is connected with the shielding table 522, so that the shielding table 522 can be controlled to shield the wastewater discharge pipeline 8, the stirring part 7 is arranged at the end of the shielding table 522, the guide cone 521 is arranged at the top end of the stirring part 7, the guide cone 521 is located below the top wall inlet of the inner layer tank body 4, and the edge of the guide cone 521 is close to the grease-proof permeable membrane 61, so that the wool washing wastewater falling into the inner layer tank body 4 can be guided by the guide cone 521 to flow down close to the grease-proof permeable membrane 61, so that the wastewater produces water body exosmosis during falling.
[0042] The control member 523 comprises a driving cylinder and a control support connected with the shielding table 522, the control support is slidingly installed through the bottom wall of the inner tank 4, the driving cylinder is arranged below the inner tank 4, and the driving end of the driving cylinder is connected with the control support, so that the control support and the shielding table 522 can be driven upward by the driving cylinder, the shielding of the shielding table 522 on the wastewater outlet pipeline 8 is released, the wastewater can stay in the inner tank 4 and the water-permeable filter 6, and after the water body is infiltrated under the action of water pressure, the shielding table 522 is controlled to move upward, and the wastewater after part of water is removed is led out of the wastewater outlet pipeline 8 to the subsequent process.
[0043] The top surface of the shielding table 522 is a conical surface, and the lower half of the shielding table 522 is a cylindrical body, and the edge of the cylindrical body is attached to the grease-proof permeable membrane 61.
[0044] As shown in Figure 7 When the wastewater stays in the inner tank 4, the wastewater stays on the inside of the grease-proof permeable membrane 61, at this time, the water body is pressed out of the grease-proof permeable membrane 61 under the action of water pressure, and the grease-proof permeable membrane 61 can prevent lanolin from infiltrating, and the position of the final wastewater outlet is at the wastewater outlet pipeline 8 below the shielding table 522, when the shielding table 522 moves upward, the wastewater will pass between the edge of the shielding table 522 and the grease-proof permeable membrane 61, at this time, the wastewater slowly flows between the shielding table 522 and the grease-proof permeable membrane 61, and in the process, the pressure increases, and the infiltration of the water body is further completed.
[0045] As shown in Figure 7 The stirring member 7 comprises a driving motor 71, a sealing ring 72 and a stirring support 73, the shielding table 522 is hollow, the driving motor 71 is arranged on the inside of the shielding table 522, the stirring support 73 is vertically rotatably installed at the end of the shielding table 522, the stirring support 73 is connected with the output end of the driving motor 71, the sealing ring 72 is arranged at the connection between the stirring support 73 and the shielding table 522, and the guide cone 521 is arranged at the top end of the stirring support 73, so that the guide cone 521 can guide and throw off the wastewater to flow down the grease-proof permeable membrane 61 in a rotating state.
[0046] The stirring support 73 comprises a rotating shaft connected with the output end of the driving motor 71 and a stirring inclined rod arranged on the opposite side of the rotating shaft, and the stirring inclined rod is located between the shielding table 522 and the guide cone 521, so as to stir the wastewater staying on the inside of the water-permeable filter 6 and prevent the lanolin from sticking.
[0047] It should be noted that the rotating directions of the guide cone 521 and the water-permeable filter 6 are opposite, so that the wastewater guided by the guide cone 521 falls on the grease-proof permeable membrane 61 at a faster speed, and the infiltration speed of the wastewater at the connection between the guide cone 521 and the grease-proof permeable membrane 61 is increased by combining the rotating centrifugal force and the dynamic water pressure.
[0048] Working principle: first let the waste water through the communication pipeline into the shielding tank 32 and the inner layer tank body 4 top wall central inlet, at this time the waste water by top into the water filter 6, start the drive motor 71 drive stirring frame 73 and guide cone 521 rotation, at the same time start the driving part 511, drive the shaping mounting frame 63 rotation, make the greaseproof permeable membrane 61 and water filter screen 62 synchronous rotation, the falling into the scouring waste water can be guided by the rotation of guide cone 521, adhere to the greaseproof permeable membrane 61 and flow down, let the waste water produce water body osmosis in the falling process, when the waste water fills the entire inside space of greaseproof permeable membrane 61, under the action of water pressure, water body osmosis in large quantities, and through the water filter screen 62 and fall into the inside bottom end of inner layer tank body 4, when the water pressure is not enough to let water body continue to osmosis, start the control part 523, control the shielding platform 522 and remove the shielding of waste water guide pipeline 8, at this time the waste water in the inside of greaseproof permeable membrane 61 will slowly flow down through the edge of shielding platform 522 and between greaseproof permeable membrane 61, in the process, due to the smaller space, the water pressure will increase, at this time the water body will further osmosis through the greaseproof permeable membrane 61, finally the scouring waste water that part of water body is removed will enter the heating tank body 2 through the waste water guide pipeline 8 and complete heating and finally enter the centrifugal separator 1 and complete centrifugal separation.
[0049] The above shows and describes the basic principle, main features and advantages of the present application. Those skilled in the art should understand that the present application is not limited to the above examples, and the above examples and descriptions in the specification are only preferred examples of the present application and are not intended to limit the present application. Without departing from the spirit and scope of the present application, various changes and improvements can be made to the present application, and these changes and improvements all fall within the scope of the claimed present application. The scope of protection of the present application is defined by the appended claims and their equivalents.
Claims
1. A grease recovery mechanism based on carbonized wool wastewater treatment, comprising a centrifuge (1) and a heating tank (2) connected to the inlet of the centrifuge (1), characterized in that, Also includes: The wastewater removal mechanism is connected to the feed inlet of the heating tank (2). The wastewater removal mechanism includes an inner tank (4) for introducing wastewater and a water removal component (5). The dewatering component (5) includes a rotary dewatering component (51) and a guiding stirring component (52); The rotary dehydration assembly (51) includes a water-permeable filter element (6) arranged along the central axis of the inner tank (4) and a drive element (511) for driving the water-permeable filter element (6) to rotate. The water-permeable filter element (6) includes an anti-grease permeation membrane (61) and a water-permeable filter screen (62) arranged around it, forming an annular water seepage area inside the inner tank (4). The guiding and stirring component (52) is located below the inner tank (4) and acts on the water seepage area of the anti-grease seepage membrane (61) to form multiple guiding seepage and static stirring of wastewater. The water-permeable filter element (6) also includes a shaped mounting bracket (63), which is installed in the center of the inner side of the inner tank (4), and a wastewater outlet pipe (8) is provided at the connection between the bottom end of the shaped mounting bracket (63) and the inner tank (4), which is connected to the inlet of the heating tank (2). The guiding stirring assembly (52) includes a guiding cone (521), a shielding platform (522), a control component (523), and a stirring component (7); The shielding platform (522) is located above the connection between the wastewater outlet pipe (8) and the fixed installation frame (63). The control component (523) is located at the bottom of the inner tank (4), and the control end of the control component (523) is connected to the shielding platform (522), which can control the shielding platform (522) to rise and fall to open and close the wastewater outlet pipe (8). The stirring component (7) is installed on the top of the shielding platform (522), and the guide cone (521) is fixed to the top of the stirring component (7) with its edge close to the inner wall of the grease-proof membrane (61); The stirring component (7) includes a drive motor (71), a sealing ring (72), and a stirring frame (73). The drive motor (71) is located inside the hollow shielding platform (522). The stirring frame (73) is vertically rotatably mounted on the top of the shielding platform (522) and driven by the drive motor (71). The sealing ring (72) is located at the connection between the stirring frame (73) and the shielding platform (522). The guide cone (521) is fixedly installed at the end of the stirring frame (73). The stirring rack (73) includes a rotating shaft connected to a drive motor (71) and a stirring slant bar located outside the rotating shaft. The stirring slant bar is located between the shielding platform (522) and the guide cone (521).
2. The grease recovery mechanism based on carbonized wool wastewater treatment according to claim 1, characterized in that, The fixed mounting frame (63) is a ring frame and is divided into upper and lower parts. The grease-proof membrane (61) and the water-permeable filter (62) are arranged around the outer side of the upper part of the fixed mounting frame (63). The water-permeable filter (62) is an annular pleated filter, and the inner pleats are attached to the anti-grease penetration membrane (61), and the wastewater inlet on the top wall of the inner tank (4) is located at the center of the anti-grease penetration membrane (61).
3. The grease recovery mechanism based on carbonized wool wastewater treatment according to claim 1, characterized in that, The wastewater removal mechanism also includes an outer tank (3), which includes a support frame (31), a metal shielding tank (32), and an internal heating element (33) fitted to the inner wall of the shielding tank (32). The inner tank (4) is located inside the shielding tank (32).
4. The grease recovery mechanism based on carbonized wool wastewater treatment according to claim 3, characterized in that, The drive unit (511) is located at the end of the shielding tank (32). The output end of the drive unit (511) passes through the shielding tank (32) and the top wall of the inner tank (4) and is provided with a drive vane. The upper half of the shaping mounting frame (63) is provided with a rubber ring. The drive vane is tightly fitted with the rubber ring of the upper half of the shaping mounting frame (63) to transmit rotational power, so that the upper half of the shaping mounting frame (63) can carry the anti-grease penetration membrane (61) and the water-permeable filter screen (62) in a rotating state, while the lower half of the shaping mounting frame (63) is connected to the wastewater outlet pipe (8) for fixation.
5. The grease recovery mechanism based on carbonized wool wastewater treatment according to claim 1, characterized in that, The top surface of the shielding platform (522) is conical, and the lower half is cylindrical, with the edge of the cylindrical part attached to the inner wall of the grease-proof membrane (61).
6. The grease recovery mechanism based on carbonized wool wastewater treatment according to claim 1, characterized in that, The bottom of the inner tank (4) is provided with a drain outlet corresponding to the water-permeable filter screen (62).
Citation Information
Patent Citations
Wool washing wastewater treatment method
CN103979713A
Device for extracting grease in wool washing wastewater
CN216336929U