CN217265348U - Cold rolling fatlute of steel mill purifies decrement system - Google Patents
Cold rolling fatlute of steel mill purifies decrement system Download PDFInfo
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- CN217265348U CN217265348U CN202220768185.0U CN202220768185U CN217265348U CN 217265348 U CN217265348 U CN 217265348U CN 202220768185 U CN202220768185 U CN 202220768185U CN 217265348 U CN217265348 U CN 217265348U
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Abstract
The utility model discloses a cold rolling fatlute of steel mill purifies decrement system, including automatic row's sediment rotor purification machine, the emulsion case, purifying box and collecting box, the liquid outlet of automatic row's sediment rotor purification machine passes through connecting tube one and is connected with the purifying box, be provided with connecting tube two between emulsion case and the purifying box and be connected, connect through connecting tube five between collecting box and the purifying box, the lower extreme row's of sediment rotor purification machine department of arranging automatically is provided with the collection sediment car, the one end of automatic row's sediment rotor purification machine is provided with the master control cabinet, inside one side of emulsion case is provided with magnetic separator, magnetic separator is connected with connecting tube three, upper end one side of collecting box is provided with the funnel of being connected with connecting tube three, the middle part of purifying box and collecting box all is provided with the stirring and scrapes the sediment ware. Has the advantages that: the purification decrement system runs fully automatically, automatically collects, mixes, purifies, shuts down, clean fluid returns, has very high practicality.
Description
Technical Field
The utility model relates to a steel mill purification treatment technical field particularly, relates to a cold rolling fatlute of steel mill purifies decrement system.
Background
The cold rolling fatlute of steel mill belongs to the solid-liquid mixture, the unable processing of enterprise's own sewage treatment plant, generally handle through entrusting the outside, and adopt and entrust the external treatment cost higher, and contain the rolling oil more than 50% in the fatlute, lead to every line to need supplying nearly a bucket new oil every day, and the purchasing cost of every bucket of oil teaches highly, cause the cost to increase, fatlute leaves mill and accounts for the place simultaneously, it can foul not cover the bung, it can ferment and produce gas and cause the staving explosion to cover the bung, there is the potential safety hazard, and magnetic separator opens for a long time and can cause the rolling oil loss, the time overlength of stopping can cause the iron powder content in the emulsion to rise, influence product quality.
An effective solution to the problems in the related art has not been proposed yet.
SUMMERY OF THE UTILITY MODEL
To the problem in the correlation technique, the utility model provides a cold rolling fatlute of steel mill purifies decrement system to overcome the above-mentioned technical problem that current correlation technique exists.
Therefore, the utility model discloses a specific technical scheme as follows:
a steel mill cold rolling oil sludge purification decrement system comprises an automatic slag discharging rotor purifier, an emulsion box, a purifying box and a collecting box, wherein a liquid outlet of the automatic slag discharging rotor purifier is connected with the purifying box through a first connecting pipeline, a second connecting pipeline is arranged between the emulsion box and the purifying box and is connected with the purifying box, a middle branch pipe of the second connecting pipeline is connected with a liquid inlet of the automatic slag discharging rotor purifier, the emulsion box is connected with the collecting box through a third connecting pipeline and a fourth connecting pipeline, the collecting box is connected with the purifying box through a fifth connecting pipeline, a slag collecting vehicle is arranged at a slag discharging port at the lower end of the automatic slag discharging rotor purifier, a main control cabinet is arranged at one end of the automatic slag discharging rotor purifier, a magnetic separator is arranged on one side inside the emulsion box and is connected with the third connecting pipeline, and a funnel connected with the third connecting pipeline is arranged on one side of the upper end of the collecting box, and stirring slag scrapers are arranged in the middle of the purifying box and the collecting box.
Furthermore, the upper ends of one side of the purifying box and one side of the collecting box are both provided with electric control boxes, the electric control boxes are connected with the main control cabinet, and the upper ends of one side of the purifying box and one side of the collecting box are both provided with liquid level meters.
Furthermore, the middle part of the connecting pipeline IV is sequentially provided with a first filter, a first diaphragm pump, a first manual valve and a first electromagnetic valve, and the first filter, the first diaphragm pump, the first manual valve and the first electromagnetic valve are sequentially arranged from top to bottom.
Furthermore, a second filter, a first liquid flow meter, a second manual valve, a second electromagnetic valve and a second diaphragm pump are sequentially arranged in the middle of the fifth connecting pipeline, and the second filter, the first liquid flow meter, the second manual valve, the second electromagnetic valve and the second diaphragm pump are sequentially arranged from the collecting box to the direction of the purifying box.
Furthermore, a third filter, a second liquid flow meter, a third manual valve, a third electromagnetic valve and a third diaphragm pump are sequentially arranged at the lower end of one side of the purification box on the second connecting pipeline from left to right, the third filter, the second liquid flow meter, the third manual valve, the third electromagnetic valve and the third diaphragm pump are arranged on the second connecting pipeline, a fourth electromagnetic valve is arranged on a branch pipe of the second connecting pipeline, and a fifth electromagnetic valve is arranged on one side of the second connecting pipeline, which is located on the fourth electromagnetic valve.
Further, the automatic slag discharging rotor purifier comprises a vibration-proof pad, a spindle motor, a bottom frame, a base, a scraper shaft, a lower cylinder, a scraper, a rotary drum cover, a lower bearing, an upper cylinder, an upper bearing, a spindle, a belt pulley, a housing, a clutch and a slag scraping motor.
Further, the upper end of the base is provided with the lower cylinder, one side of the upper end of the upper cylinder is provided with a slag scraping motor, a housing is arranged on one side of the upper cylinder body, a spindle motor is arranged at the lower end of one side of the housing, a belt pulley is arranged on the output shaft at the upper end of the spindle motor and positioned inside the housing, a clutch connected with the slag scraping motor is arranged inside the upper cylinder body, the lower end of the clutch is provided with a main shaft, the two ends of the main shaft are respectively provided with an upper bearing and a lower bearing, the lower end of the upper cylinder body is provided with a lower cylinder body, the interior of the lower cylinder body is provided with a rotary drum, the upper end of the rotary drum is provided with a rotary drum cover, the middle part of rotary drum is provided with the scraper, one side of barrel is provided with the scraper axle down, the lower extreme of base is provided with the chassis, the chassis with be provided with the antivrbration pad between the base.
The utility model provides a cold rolling fatlute of steel mill purifies decrement system, beneficial effect as follows: the utility model discloses a let the fatlute that magnetic separator separated on the rolling mill carry out certain decrement, the sediment of coming out is semi-solid, reduces its treatment cost, falls emulsion and rolling oil after the fatlute through the separation and can return emulsion pond well recycle, practices thrift the use cost of rolling oil, the utility model discloses a purify the full automatic operation of decrement system, automatic collection, thoughtlessly join in marriage, purify, shut down, clean fluid returns, has very high practicality.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural diagram of a cold rolling sludge purification and reduction system in a steel mill according to an embodiment of the invention;
fig. 2 is a schematic view of an automatic slag discharge rotor purifier of a cold rolling sludge purification and reduction system in a steel mill according to an embodiment of the present invention.
In the figure:
1. an automatic slag discharge rotor purifier; 2. an emulsion tank; 3. a purification box; 4. a collection box; 5. connecting a first pipeline; 6. a second connecting pipeline; 7. a third connecting pipeline; 8. a fourth connecting pipeline; 9. connecting a pipeline five; 10. A slag collection vehicle; 11. a master control cabinet; 12. a magnetic separator; 13. a funnel; 14. stirring a slag scraper; 15. an electric cabinet; 16. a liquid level meter; 17. a first filter; 18. a first diaphragm pump; 19. a first manual valve; 20. a first electromagnetic valve; 21. a second filter; 22. a first liquid flow meter; 23. a second manual valve; 24. a second electromagnetic valve; 25. A second diaphragm pump; 26. a second filter; 27. a second liquid flow meter; 28. a manual valve III; 29. a third electromagnetic valve; 30. a diaphragm pump III; 31. a fourth electromagnetic valve; 32. a fifth electromagnetic valve; 33. a crash pad; 34. a spindle motor; 35. a chassis; 36. a base; 37. a scraper shaft; 38. a lower cylinder body; 39. a scraper; 40. a drum; 41. Rotating the drum cover; 42. a lower bearing; 43. an upper cylinder body; 44. an upper bearing; 45. a main shaft; 46. a pulley; 47. A housing; 48. a clutch; 49. a slag scraping motor.
Detailed Description
For further explanation of the embodiments, the drawings are provided as part of the disclosure and serve primarily to illustrate the embodiments and, together with the description, to explain the principles of operation of the embodiments, and to provide further explanation of the invention and advantages thereof, it will be understood by those skilled in the art that various other embodiments and advantages of the invention are possible, and that elements in the drawings are not to scale and that like reference numerals are generally used to designate like elements.
According to the utility model discloses an embodiment provides a cold rolling fatlute of steel mill purifies decrement system.
The first embodiment is as follows:
as shown in fig. 1-2, the steel mill cold rolling sludge purification and reduction system according to the embodiment of the present invention comprises an automatic slag discharging rotor purifier 1, an emulsion tank 2, a purification tank 3 and a collection tank 4, wherein a liquid outlet of the automatic slag discharging rotor purifier 1 is connected with the purification tank 3 through a first connection pipe 5, the emulsion tank 2 is connected with the purification tank 3 through a second connection pipe 6, a middle branch pipe of the second connection pipe 6 is connected with a liquid inlet of the automatic slag discharging rotor purifier 1, the emulsion tank 2 is connected with the collection tank 4 through a third connection pipe 7 and a fourth connection pipe 8, the collection tank 4 is connected with the purification tank 3 through a fifth connection pipe 9, a slag collecting vehicle 10 is disposed at a lower slag discharging port of the automatic slag discharging rotor purifier 1, a main control cabinet 11 is disposed at one end of the automatic slag discharging rotor purifier 1, a magnetic separator 12 is arranged on one side inside the emulsion box 2, the magnetic separator 12 is connected with the third connecting pipeline 7, a funnel 13 connected with the third connecting pipeline 7 is arranged on one side of the upper end of the collection box 4, and stirring and slag scraping devices 14 are arranged in the middles of the purification box 3 and the collection box 4.
Example two:
as shown in fig. 1-2, the upper ends of one side of the purification box 3 and the collection box 4 are respectively provided with an electric cabinet 15, the electric cabinet 15 is connected with the main control cabinet 11, and the upper ends of one side of the purification box 3 and the collection box 4 are respectively provided with a liquid level meter 16. The middle part of the connecting pipeline IV 8 is sequentially provided with a filter I17, a diaphragm pump I18, a manual valve I19 and an electromagnetic valve I20, and the filter I17, the diaphragm pump I18, the manual valve I19 and the electromagnetic valve I20 are sequentially arranged from top to bottom. The middle part of the connecting pipeline five 9 is sequentially provided with a second filter 21, a first liquid flow meter 22, a second manual valve 23, a second electromagnetic valve 24 and a second diaphragm pump 25, and the second filter 21, the first liquid flow meter 22, the second manual valve 23, the second electromagnetic valve 24 and the second diaphragm pump 25 are sequentially arranged from the collecting box 4 to the direction of the purifying box 3. The second connecting pipeline 6 is located at the lower end of one side of the purifying box 3 and is sequentially provided with a third filter 26, a second liquid flow meter 27, a third manual valve 28, a third electromagnetic valve 29 and a third diaphragm pump 30 from left to right, the third filter 26, the second liquid flow meter 27, the third manual valve 28, the third electromagnetic valve 29 and the third diaphragm pump 30 are arranged on the lower end of the purifying box, a fourth electromagnetic valve 31 is arranged on a branch pipe of the second connecting pipeline 6, and a fifth electromagnetic valve 32 is arranged on one side, located on the fourth electromagnetic valve 31, of the second connecting pipeline 6.
As shown in fig. 1-2, the automatic slag discharging rotor cleaner 1 includes a vibration-proof pad 33, a spindle motor 34, a base frame 35, a base 36, a scraper shaft 37, a lower cylinder 38, a scraper 39, a rotary drum 40, a rotary drum cover 41, a lower bearing 42, an upper cylinder 43, an upper bearing 44, a spindle 45, a belt pulley 46, a housing 47, a clutch 48, and a slag-scraping motor 49. The upper end of the base 36 is provided with the lower cylinder 38, one side of the upper end of the upper cylinder 43 is provided with a slag scraping motor 49, one side of the upper cylinder 43 is provided with a housing 47, the lower end of one side of the housing 47 is provided with a spindle motor 34, an upper end output shaft of the spindle motor 34 is arranged in the housing 47 and is provided with a belt pulley 46, the interior of the upper cylinder 43 is provided with a clutch 48 connected with the slag scraping motor, the lower end of the clutch 48 is provided with a spindle 45, two ends of the spindle 45 are respectively provided with an upper bearing 44 and a lower bearing 42, the lower end of the upper cylinder 43 is provided with the lower cylinder 38, the interior of the lower cylinder 38 is provided with a rotating drum 40, the upper end of the rotating drum 40 is provided with a rotating drum cover 41, the middle part of the rotating drum 40 is provided with a scraper 39, one side of the lower cylinder 38 is provided with a scraper shaft 37, and the lower end of the base 36 is provided with a bottom frame 35, a shock pad 33 is arranged between the bottom frame 35 and the base 36.
For the convenience of understanding the technical solution of the present invention, the following detailed description is made on the working principle or the operation mode of the present invention in the practical process.
During practical application, through making two independent 380L volumetric circular water tanks, divide into fatlute collecting box 4 (foul solution case) and purifying box 3, two liquid tanks all have heating and thermostatic control function. The two liquid tanks have stirring function, and the stirring rod is provided with two upward spiral impellers and a mouth-shaped stirring scraper below the stirring rod according to pictures. The two liquid tanks are provided with three-point level gauges 16, and the outlets of the two liquid tanks are respectively provided with a flow switch, a pump and an electromagnetic valve;
the oil sludge (oil/liquid/impurity mixture) separated by the rolling mill magnetic separator 12 overflows into the oil sludge collection box 4 through high-low head, the heating device is always started to work, and the temperature of the mixed liquid is kept between 50 and 60 ℃;
when the liquid in the dirty liquid tank reaches a low liquid level (200L is adjustable), the liquid level switch gives a signal to start the first diaphragm pump 18, the emulsified liquid in the water tank of the emulsified liquid rolling mill is supplemented into the dirty liquid collecting tank 4, and when the liquid level reaches 300L, the liquid level sensor closes the first electromagnetic valve 20 (the electromagnetic valve is a normally closed electromagnetic valve) and the first diaphragm pump 18 air inlet electromagnetic valve (the electromagnetic valve is a normally closed electromagnetic valve). Remarking: the high liquid level of the dirty liquid tank is 350L of alarm liquid level, when the high liquid level reaches the alarm liquid level, the system gives an audible and visual alarm and closes the electromagnetic valve of the emulsion inlet pipeline and the electromagnetic valve of the diaphragm pump air inlet at the same time, so that the liquid leakage accident caused by the failure of the high liquid level is avoided;
when the dirty liquid collecting box 4 reaches 300 liters of medium liquid level, the system starts a stirrer to work for 5-10 minutes, after the two liquids are fully stirred, a second diaphragm pump 25 arranged at an outlet at the bottom of the dirty liquid collecting box is started to pump all the 300 liters of liquid into the purifying box 3, a pulse flowmeter is arranged outside a pipeline of the second diaphragm pump 25, after the 300L of liquid is exhausted, the flowmeter gives a signal to the system, the system delays for one minute to close the second diaphragm pump 25, and the liquid is ensured not to be stored in the pipeline as far as possible. Remarking: the pipeline is proposed to be vertically lifted after coming out from an outlet at the bottom of the dirty liquid tank, and then overflows to the purification tank 3 after reaching the height higher than the top of the purification tank 3, so that the position of the pipeline possibly blocked by oil cooling is only a vertical part, whether the pipeline needs to be provided with a pipeline heating function or not is determined according to the situation, and the possibility of blockage is small due to the gradient and the pressure of the pump in the overflow part;
when the liquid in the dirty liquid tank is pumped to the low liquid level (200L) of the purification tank 3, the low liquid level gives a signal to start the centrifugal machine to work simultaneously with the heating function and the stirring function, the centrifugal machine pumps the liquid from the bottom of the purification tank 3, the liquid returns from the top, and the circulation purification is started in the purification tank 3 for 24 hours. The liquid level and the high liquid level in the purifying box 3 are both protective liquid levels, the set heights are 320/350L respectively, and when the liquid level reaches 320/350L due to the fact that the purifying box 3 cannot be emptied in time if the third diaphragm pump 30 is damaged or the dirty liquid box is filled with 200L more than the centrifugal emptying time of the purifying box 3, the system can shut down the second diaphragm pump 25 of the dirty liquid box and give an alarm, and liquid leakage accidents are avoided;
when the circulation purification is finished for 24 hours (the time can be adjusted according to the dirty liquid cleaning), the automatic deslagging rotor purifier 1 stops running, a diaphragm pump III 30 arranged at the bottom of the purification box 3 is started up, and all liquid in the purification box 3 is pumped into a large liquid box of an emulsion rolling mill for use. The liquid pumping pipeline is also provided with a pulse flowmeter, and when the pump is evacuated, the electromagnetic valve of the gas circuit of the diaphragm pump is closed, and the whole cycle is ended.
The principle of centrifugation adopted by the automatic slag removal rotor purifier 1 is that centrifugation is a method for separating, concentrating and purifying a dirty liquid by utilizing centrifugal force of rotary motion and difference of sedimentation coefficient or suspension density of substances. The rotor rotates at a high speed to generate strong centrifugal force, so that liquid in the dirty liquid is separated from solid particles, the solid particles are remained on the inner wall of the rotary drum 40, and the liquid is discharged from the liquid outlet;
automatic arrange sediment rotor clearing machine 1 and get into centrifuge drum 40 from the inlet through the auxiliary pump with pending liquid, impurity in the dirty liquid is by high-speed separation, adhere to around the drum 40 inner wall, liquid after the processing is arranged back to the circulation groove again, after equipment operation certain time, equipment starts automatic slag removal function row cinder notch and opens, equipment automatic disconnection and main shaft motor 34 transmission, connect simultaneously and scrape sediment motor 49 and operate, built-in scraper 39 begins to move and advances the slagging-off, the impurity of cleaing off falls into the impurity collecting vat of equipment below from the cinder notch, accomplish the effect of automatic sediment of arranging.
To sum up, with the help of the utility model discloses an above-mentioned technical scheme, carry out certain decrement through letting the fatlute that magnetic separator 12 separated on the rolling mill, the sediment of coming out is semi-solid, reduces its treatment cost, and the emulsion after falling fatlute through the separation can return emulsion pond mesocycle use with rolling oil, practices thrift the use cost of rolling oil, the utility model discloses a purify the full automatic operation of decrement system, automatic collection, thoughtlessly join in marriage, purify, shut down, clean fluid returns, has very high practicality.
The above description is only for the preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (7)
1. A steel mill cold rolling oil sludge purification decrement system is characterized by comprising an automatic slag discharging rotor purifier (1), an emulsion tank (2), a purification tank (3) and a collection tank (4), wherein a liquid outlet of the automatic slag discharging rotor purifier (1) is connected with the purification tank (3) through a first connecting pipeline (5), the emulsion tank (2) is connected with the purification tank (3) through a second connecting pipeline (6), a middle branch pipe of the second connecting pipeline (6) is connected with a liquid inlet of the automatic slag discharging rotor purifier (1), the emulsion tank (2) is connected with the collection tank (4) through a third connecting pipeline (7) and a fourth connecting pipeline (8), the collection tank (4) is connected with the purification tank (3) through a fifth connecting pipeline (9), and a slag collection vehicle (10) is arranged at the lower port of the automatic slag discharging rotor purifier (1), one end of the automatic slag discharging rotor purifier (1) is provided with a main control cabinet (11), one side of the interior of the emulsion tank (2) is provided with a magnetic separator (12), the magnetic separator (12) is connected with the connecting pipeline III (7), one side of the upper end of the collecting tank (4) is provided with a funnel (13) connected with the connecting pipeline III (7), and the middles of the purifying tank (3) and the collecting tank (4) are both provided with stirring and slag scraping devices (14).
2. The steel mill cold rolling oil sludge purification and reduction system according to claim 1, wherein an electric cabinet (15) is arranged at the upper end of one side of each of the purification box (3) and the collection box (4), the electric cabinet (15) is connected with the master control cabinet (11), and a liquid level meter (16) is arranged at the upper end of one side of each of the purification box (3) and the collection box (4).
3. The steel mill cold rolling sludge purification and reduction system according to claim 1, wherein a first filter (17), a first diaphragm pump (18), a first manual valve (19) and a first electromagnetic valve (20) are sequentially arranged in the middle of the fourth connecting pipe (8), and the first filter (17), the first diaphragm pump (18), the first manual valve (19) and the first electromagnetic valve (20) are sequentially arranged from top to bottom.
4. The steel mill cold rolling oil sludge purification and reduction system according to claim 1, wherein a second filter (21), a first liquid flow meter (22), a second manual valve (23), a second electromagnetic valve (24) and a second diaphragm pump (25) are sequentially arranged in the middle of the fifth connecting pipe (9), and the second filter (21), the first liquid flow meter (22), the second manual valve (23), the second electromagnetic valve (24) and the second diaphragm pump (25) are sequentially arranged from the collection box (4) to the direction of the purification box (3).
5. The steel mill cold rolling oil sludge purification and reduction system according to claim 1, wherein a third filter (26), a second liquid flow meter (27), a third manual valve (28), a third electromagnetic valve (29) and a third diaphragm pump (30) are sequentially arranged at the lower end of one side of the purification box (3) in the second connecting pipeline (6) from left to right, the third filter (26), the second liquid flow meter (27), the third manual valve (28), the third electromagnetic valve (29) and the third diaphragm pump (30) are arranged, a fourth electromagnetic valve (31) is arranged on a branch pipe of the second connecting pipeline (6), and a fifth electromagnetic valve (32) is arranged at one side of the fourth electromagnetic valve (31) of the second connecting pipeline (6).
6. The steel mill cold rolling oil sludge purification and reduction system according to claim 1, wherein the automatic slag discharging rotor purifier (1) comprises a vibration-proof pad (33), a spindle motor (34), a chassis (35), a base (36), a scraper shaft (37), a lower cylinder (38), a scraper (39), a rotary drum (40), a rotary drum cover (41), a lower bearing (42), an upper cylinder (43), an upper bearing (44), a spindle (45), a belt pulley (46), a housing (47), a clutch (48) and a slag scraping motor (49).
7. The steel mill cold rolling oil sludge purification and reduction system according to claim 6, wherein the lower cylinder (38) is arranged at the upper end of the base (36), a slag scraping motor (49) is arranged at one side of the upper end of the upper cylinder (43), a housing (47) is arranged at one side of the upper cylinder (43), a spindle motor (34) is arranged at the lower end of one side of the housing (47), a belt pulley (46) is arranged at an upper end output shaft of the spindle motor (34) and inside the housing (47), a clutch (48) connected with the slag scraping motor (49) is arranged inside the upper cylinder (43), a spindle (45) is arranged at the lower end of the clutch (48), an upper bearing (44) and a lower bearing (42) are respectively arranged at two ends of the spindle (45), and the lower cylinder (38) is arranged at the lower end of the upper cylinder (43), the inside of barrel (38) is provided with rotary drum (40) down, the upper end of rotary drum (40) is provided with changes drum cover (41), the middle part of rotary drum (40) is provided with scraper (39), one side of barrel (38) is provided with scraper axle (37) down, the lower extreme of base (36) is provided with chassis (35), chassis (35) with be provided with antivrbration pad (33) between base (36).
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114716121A (en) * | 2022-05-01 | 2022-07-08 | 江苏沙钢集团有限公司 | Oil-sludge separation device of rolling mill and working method thereof |
CN115837314A (en) * | 2022-11-17 | 2023-03-24 | 冠县鸿舜复合材料有限公司 | System and method for reducing weight of iron powder after emulsion filtration |
-
2022
- 2022-04-06 CN CN202220768185.0U patent/CN217265348U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114716121A (en) * | 2022-05-01 | 2022-07-08 | 江苏沙钢集团有限公司 | Oil-sludge separation device of rolling mill and working method thereof |
CN115837314A (en) * | 2022-11-17 | 2023-03-24 | 冠县鸿舜复合材料有限公司 | System and method for reducing weight of iron powder after emulsion filtration |
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