JP2006326445A - Separation recovery device and method of contained material in waste liquid such as recovery coolant - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To enable a separation recovery of three different materials, that is, water, oil, and sludge, contained in a waste liquid such as recovery coolant, simultaneously and further, continuously in a simple device. <P>SOLUTION: A device treats the waste liquid such as recovery coolant containing at least the oil, water, and sludge in the simple device simultaneously and continuously to separate into the oil, water, and sludge to recover. The separation recovery device of the waste liquid containing component such as recovery coolant has a degassing mechanism by a cyclone, a separation recovery mechanism of the oil, water, and sludge by the gravity using a separation tank, and a dewatering and recovery mechanism of water-containing sludge settled down in the bottom of the separation tank. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a recovered coolant used for separating and recovering sludge containing oil, moisture, metal powder, grindstone particles, etc. contained in a coolant recovered after being used for cooling various apparatuses and devices. The present invention relates to an apparatus and method for separating waste liquid-containing components.

  The apparatus according to the present invention is not limited to the above-described recovery coolant, and is used for separating and recovering oil, moisture and sludge from various waste liquids containing at least oil, moisture and sludge. .

  Furthermore, the apparatus and method according to the present invention do not separate and collect sludge such as oil, moisture, metal powder, and grindstone particles with separate devices, but a single device for three types of oil, moisture, and sludge. It is characterized by the fact that it can be separated and recovered simultaneously and continuously, but excludes the configuration with a process (apparatus / equipment) for separating and collecting (coarse) cutting waste such as iron, aluminum and copper. is not.

  Coolant recovered after being used to cool machinery (Cooolant = coolant) contained sludge (Sludge = sludge) composed of fine particles such as iron powder, aluminum powder and grinding stone particles in addition to oil and moisture. Although it is a slurry (Slurry = suspension), these components are separated and recovered and the coolant is reused.

  Various proposals have been made as a device for separating and recovering a coolant-containing component, and examples thereof include Patent Literature 1, Patent Literature 2, Patent Literature 3, Patent Literature 4, Patent Literature 5, Patent Literature 6, and the like. .

  A configuration using a cyclone device for introducing the recovered coolant into the separation device and a configuration including a device for separating the magnetic material prior to the separation and recovery process are disclosed in Patent Document 2, Patent Document 6, and the like.

The structure which removes the surface floating thing of an oil-water separation tank by scraping off with a scraper is disclosed by patent document 7 grade | etc.,.
Japanese Utility Model Publication No. 6-57994 JP 2003-275938 A JP 2004-249178 A JP 2004-249382 A JP 2004-250134 A JP 2005-28353 A Japanese Patent Laid-Open No. 10-5756

  In general, waste oil and coolant waste liquid (floating oil) always contain a large amount of impurities in the oil. By the way, when looking at the actual situation of concentrated coolant treatment at a certain manufacturer, more than 10% of machine-cut aluminum and grinding stone particles were mixed in oil that easily foamed, and it was sinking in the tank during oil-water separation. .

  In the conventional separation method, it is common to first filter the slurry contained in the oil with a non-woven fabric or a cartridge filter, and then separate the oil. The maintenance load was high because it was high.

  Iron powder in the waste liquid is attracted and separated by the magnet magnet, so the oil and water separation is easy afterwards, and there are many practical machines, but aluminum powder, whetstone particles, etc. with a small specific gravity and a large surface area are particularly oily. If these are collected together and flowed into the separator, these particulate components settle and accumulate at the bottom of the separation tank, clogging the piping and drain valve, and cannot be discharged as a drain. Disassembly cleaning was necessary.

  The coolant waste liquid recovered after being used to cool machinery is a slurry containing sludge composed of fine particles such as iron powder, aluminum powder, and grinding stone particles in addition to oil and moisture. Without separation and recovery, the coolant cannot be reused or discarded.

If oil and water are separated, they can be separated relatively easily by various separators using specific gravity differences, and iron fine particles can also be separated by using magnetic force.
However, coolant waste fluids containing fine particles (sludge) such as aluminum and grindstones have the problem of clogging the treatment tank and piping due to the sinking and solidification of the sludge. The equipment had to be disassembled and cleaned, and the maintenance load was high.

  In particular, if the separation and collection of sludge is performed with a single device at the same time as the separation and collection of oil and moisture, the sludge easily sinks to the bottom of the device due to the specific gravity and solidifies, making the device inoperable. In many cases, smooth operation required very complicated maintenance.

  The apparatus and method for separating waste liquid-containing components such as recovered coolant to be clarified by the present invention simultaneously separates and recovers three different substances such as moisture, oil, and sludge contained in the waste liquid such as recovered coolant. Moreover, it is possible to carry out continuously with a single device.

The present invention for solving the above problems has the following configuration.
1. It is a device that separates and recovers waste liquid such as recovered coolant containing at least oil, moisture and sludge into oil, moisture and sludge by simultaneous and continuous processing with a single device. Separation and recovery device for waste liquid components such as recovery coolant, which has a mechanism for separation and recovery of oil, moisture and sludge by gravity using a tank, and a dewatering and recovery mechanism for hydrous sludge settled at the bottom of the separation tank .

2. 2. A waste liquid-containing component such as a recovery coolant as described in 1 above, wherein the separation and recovery mechanism for oil, moisture and sludge by gravity using a separation tank is equipped with a moisture filtration mechanism using whiskernet and a filter. Separation and recovery equipment.

3. In the above 1 or 2, wherein the separation / recovery mechanism for oil / water / sludge components by gravity using a separation tank includes a scraper mechanism for scraping the settled sludge component adhering to the inner wall surface of the separation tank. Separation and recovery equipment for waste liquid-containing components such as the recovery coolant described.

4). Separation and recovery of waste liquid-containing components such as the recovery coolant according to any one of the above 1 to 3, characterized in that, as a mechanism for recovering water separated in the separation tank, a water level adjusting means communicating with the separation tank is provided. apparatus.

5. The apparatus for separating and recovering waste liquid-containing components such as the recovery coolant according to any one of the above 1 to 4, further comprising a scraper mechanism that scrapes and discharges suspended matter at an upper position in the separation tank.

6). A screw conveyor is used as a mechanism for dewatering and collecting the water-containing sludge settled in the lower part of the separation tank, the screw conveyor is disposed in an inclined state, and at least the sludge discharge part of the screw conveyor is higher than the water level of the separation tank The apparatus for separating and recovering waste liquid-containing components such as the recovery coolant according to any one of 1 to 5 above, wherein dehydration is performed in the middle of conveyance by the screw conveyor.

7). 7. A waste liquid-containing component such as a recovered coolant as described in 6 above, wherein a means for preventing co-rotation of the object to be transported is provided on the inner wall surface of a cylinder of a screw conveyor used as a dewatering and recovery mechanism for water-containing sludge. Separation and recovery equipment.
8). The number of rotations of the screw conveyor is 100 N (rpm) or less, The apparatus for separating and recovering waste liquid-containing components such as the recovery coolant according to any one of 1 to 7 above.

9. This is a device that separates and collects waste liquid such as recovered coolant containing at least oil, moisture, and sludge into oil, moisture, and sludge by simultaneously and continuously using a single device. A device that separates and collects oil, moisture, and sludge by the action of gravity using a tank and dehydrates and collects water-containing sludge settled at the bottom of the separation tank is incorporated as a single device. A screw conveyor is used as a mechanism for performing the process, the screw conveyor is disposed in an inclined state, and at least the sludge discharge portion of the screw conveyor is set to a position higher than the water level of the separation tank. These processes are always performed and the screw conveyor is operated to continuously separate and recover the waste liquid-containing components. The method of separating and recovering waste containing components, such as collection coolant and performs a manner.

  According to the present invention, when processing a waste liquid such as a coolant liquid in which oil, water, and sludge are mixed, oil, water, and sludge can be separated and recovered simultaneously by a single device. Compared with a conventional apparatus that has a heavy maintenance load such as disassembly and cleaning, the operation may be stopped due to the solidified sludge, so that continuous operation is possible and the maintenance load is significantly reduced.

The apparatus of Example 1 which concerns on this invention is demonstrated according to attached FIG. 1-3.
In the figure, reference numeral 100 denotes a cyclone, and coolant waste liquid used for machine cutting or the like is recovered by a waste liquid recovery pump (not shown) and is supplied from a waste liquid input port 110. The waste liquid recovered by the waste liquid recovery pump is not directly put into the cyclone 100, but is stored in the primary storage tank, or the removal process of coarse metal debris, the iron separation process by magnetic force, etc. It is not excluded that the embodiment goes through.

  The function of the cyclone 100 is to separate the air sucked together with the waste liquid when the waste liquid is collected by the collection pump. If the waste liquid containing air is introduced into the separator as it is, the air rises in the waste liquid stored in the separator tank and the liquid level moves vigorously, so that the liquid level cannot be made constant. If such a situation occurs, even at the liquid surface position, it results in a state where moisture and oil are mixed without being separated, and in the next process, the oil layer that has floated above the moisture layer due to the difference in specific gravity is separated and removed. This is an obstacle to adopting the oil-water separation configuration.

Since the cyclone 100 does not require special specifications, various cyclones used in a known waste liquid treatment apparatus can be incorporated.
The waste liquid deaerated by the cyclone 100 is introduced into the separation device 200 through the guide tube 120, separated into moisture, oil, and sludge, and collected separately.

  The separation tank 210 of the separation apparatus 200 has a conical lower end funnel-shaped tank part 212 formed on the lower end side and a conical upper end funnel-shaped tank part 213 formed on the upper end side with the cylindrical tank part 211 as the center. Consists of. An oil outlet 215 is provided in the top tubular body 214 that is continuous with the top of the upper funnel-shaped tank 213.

The upper end funnel-shaped tank part 213 is detachably mounted on the upper end of the cylindrical tank part 211 via a flange.
The waste liquid guide tube 120 from the cyclone 100 described above is connected to the side surface of the lower end funnel-shaped tank portion 212 of the separation tank 210.

  A cylindrical frame body 220 in which a large number of through holes are formed is arranged inside the cylindrical tank portion 211 of the separation tank 210, and the whisker net 221 and the filter 222 are connected via the cylindrical frame body 220. It is attached. Fine oil and slurry contained in the waste liquid are separated from most of the filtered water by adhering to the whisker net 221 and the filter 222.

  A scraper 230 is disposed on the inner inclined surface of the lower end funnel-shaped tank portion 212 of the separation tank 210, and on the inner inclined surface of the lower funnel-shaped tank portion 212 according to the rotation of the drive shaft 231 connected to the scraper motor 232. The sludge adhering to the inner inclined surface is removed according to sedimentation.

  A stirring rod 233 is attached to the lower end of the drive shaft 231 of the scraper 230, and sludge is prevented from stagnating and solidifying in the lowermost layer portion of the lower end funnel-shaped tank portion 212. A sludge guide tube 240 is continuous below the lower end funnel-shaped tank section 212, and a mixed liquid of moisture and sedimented sludge is guided to the base of the screw conveyor 300. At this time, When the mixed solution is stagnated in the lowermost layer, the concentrated sludge content is easily solidified and clogs the lower end release portion of the lower end funnel-shaped tank portion 212. The subsequent portion of the mixed liquid is cut off, and the sludge content is easily solidified. By rotating the stirring rod 233, it is possible to prevent the stagnation of the water / sediment sludge mixed liquid.

  The lower end of the drive shaft 231 of the scraper 230 may be extended downward from the position shown in FIG. 2 so that the stirring rod 233 exists over substantially the entire length of the sludge guide tube 240. Moreover, it can replace with the stirring rod 233 and can also be set as the structure which arrange | positions a screw conveyor.

  Further, the drive shaft 231 of the scraper 230 is configured to be interlocked with the whisker net 221 and the cylindrical frame body 220 for the filter 222 via the cam mechanism 234. That is, the lower surface of the opening end of the central portion of the cylindrical frame 220 is placed on the upper surface of the cam mechanism 234 fixed to the drive shaft 231, so that the cam mechanism 234 is horizontally moved with the rotation of the drive shaft 231. By only rotating, the cylindrical frame body 220 moves up and down along the inclination of the cam. The cam mechanism 234 can cause the cylindrical frame 220 to undergo a gentle ascending motion and a sudden falling motion by a combination of an inclined surface and a steep step.

  In particular, regarding the cam mechanism 234, it is preferable to always generate a vertical motion shock by rotating the cylindrical ring of the filter 222 to remove the adhered oil and sludge, and it is preferable to always perform this operation.

  The oil that has come off rises, the sludge sinks, and the filter is not clogged at all times. In particular, when the oil contains sludge, the filter is severely clogged, so it is generally in trouble, but this example can also solve this problem.

  Since the oil and slurry adhering to the whisker net 221 are likely to be clogged, the above-mentioned continuous shock shock removes the adhering oil and the slurry from the whisker net 221 to raise the oil and allow the slurry to settle. Therefore, the whisker net 221 can always be used continuously in a clean state, which is effective for reducing maintenance.

  Of the components contained in the waste liquid put into the separation tank 210, the oil component having a low specific gravity is concentrated while rising in the separation tank 210, gathers at the center of the upper funnel-shaped tank section 213, and the top cylindrical body 214. The portion overflowed from the middle is discharged as a concentrated oil through the oil outlet 215 and collected.

  In the case where the concentrated oil contains a large amount of metal aluminum or abrasive particles, it may clog without flowing from the top cylindrical body 214 to the discharge part leading to the oil discharge outlet 215. In the case of foam oil, In such a case, a coil screw or the like is disposed inside the top cylindrical body 214 so that it can be scraped off. Is preferred.

  Most of the moisture contained in the waste liquid is the amount that has passed through the whisker net 221 and the filter 222, and this moisture passes through the drainage communication pipe 250 connected to the side surface of the cylindrical tank portion 211 of the separation tank 210. The amount that is guided to the water level adjusting cylinder 251 and overflows from the upper end of the water level adjusting cylinder 251 is discharged from the moisture outlet 252 and collected.

  The water level adjustment cylinder 251 is arranged on the outlet side of the drainage communication pipe 250 and is configured to be movable up and down. Therefore, by moving the water level adjustment cylinder 251 up and down, the overflow position can be adjusted up and down, and accordingly, the water level in the separation tank 210 communicating with the water level adjustment cylinder 252 by the drainage communication pipe 250 is adjusted. Can be varied up and down.

  Sludge settled through the sludge guide tube 240 is separated from the oil, but the water level in the separation tank 210 is at the position of the upper end funnel-shaped tank portion 213, so it still exists as a slurry containing moisture. To do. However, although the water in this slurry works as a solvent for dissolving the sludge, it is not homogeneous throughout the slurry, and one part of the sludge is solidified and becomes highly viscous. It can also be expressed that the moisture content of the sludge is not uniform. For this reason, in the conventional apparatus, a solidified or easily solidified sludge component having a low water content is easily accumulated in a portion from the lower layer of the separation tank 210 to the sludge guide tube 240, and there is a problem of solidification. It had to be difficult to separate and collect.

  In a concentrated coolant treatment at a certain factory, floating oil that contains machine-cut aluminum and grindstone particles is mixed, but more than 10% of fine particles are mixed in oil that easily foams. It was sinking in the tank inside, and it was a tough site for the separation and recovery of moisture, oil and sludge. That is, the conventional separator is mainly intended for separation of oil that does not contain fine particles. Therefore, when trying to treat waste liquid in which fine particles are mixed in an oil that easily foams, the separation tank is The current situation is that it becomes clogged and becomes inoperable within a short period of time.

  The adoption of a screw conveyor was considered as a measure to solve the above, but when it was actually installed and the experiment was attempted, it was good when the separated oil was continuously collected from the upper part of the separation tank, but weekends and holidays continued. It was found that sludge accumulated in the lower part of the discharge pipe, deposits grew on the inner wall surface of the discharge pipe, and finally the discharge pipe was closed.

The above problem can be solved by keeping the screw conveyor always in operation and discharging the sludge before the sludge solidifies in the separation tank and the discharge pipe.
However, in the case where the fine grindstone particles are contained in the sludge, it has been found that when the screw conveyor is always in an operating state, the screw bearings are easily worn by the mixed fine grindstone particles, and the operation often stops.

  The problem with the wear of the screw conveyor bearing is that the screw rotation speed is 100 N (rpm) or less, preferably 50 N (rpm) or less, more preferably 15 N (rpm) or less, and continuous operation at a very low speed. As a result, the wear rate can be reduced, and the parts worn by the slurry can be provided in an inexpensive unit, which can be provided at a low cost, and can be solved by reducing the maintenance load of parts replacement.

Next, how the present invention solves the above-described problem, that is, how to separate and collect the moisture-containing sludge will be described focusing on the configuration of the screw conveyor 300.
The screw conveyor 300 is arranged not in a vertical arrangement but in an inclined state. In the vertical arrangement, all of the weight of the moisture-containing sludge that is the object to be conveyed is applied to the upper surface of the spiral screw, but in the inclined arrangement, the inner wall surface of the outer cylinder surrounding the screw is also the weight of the moisture-containing sludge. The structure of the screw part can be reduced in weight, which is beneficial for reducing the manufacturing cost.

  Further, the screw conveyor 300 is configured such that a part on the upper end side in the entire length is located above the water level in the separation tank 210, and in the screw conveyance part at a position above the water level, moisture is The draining action from the contained sludge will be performed.

  Of course, if the purpose is only the draining function, the screw conveyor 300 is arranged vertically, and only one part on the upper end side is positioned above the water level of the separation tank 210, so that the necessary and sufficient conditions are satisfied. However, in addition to solving the above-described problem of weight support for the moisture-containing sludge, the inclined arrangement is more effective in consideration of the problem of transporting the separated sludge, for example, transportation by a truck or the like.

  Incidentally, in the vertical arrangement method, an intermediate transfer means such as a belt conveyor is required to transfer the separated sludge discharged from the screw conveyor to the next transfer means, but in the inclined arrangement, from the terminal end side of the screw conveyor. It is only necessary to drop the object to be transported, which is simple in structure and beneficial for reducing the manufacturing cost.

  The sludge content is easy to harden if left unattended, but the scraper 230 is operated in the separation tank 200 and the screw conveyor 300 is always operated in the sludge guide tube 240 on the lower surface of the separation tank. The state where it is easy to collect is maintained.

  The water level in the screw conveyor 300 and the water level in the separation tank 210 are equalized by the principle of the communication pipe. Accordingly, the upper end side of the screw conveyor 300 including the sludge carry-out port 310 is positioned higher than the liquid level in the separation tank 210, so that it is mixed into the sludge portion located on the upper end side of the screw conveyor 300. The moisture that is falling falls within the screw conveyor 300 and dehydrates the sludge, so that the sludge having a low moisture content can be recovered.

  By maintaining the screw conveyor 300 in a constantly operating state, the settled sludge is continuously discharged before solidifying in the lower layer of the separation tank 210 and the portion of the sludge guide tube 240, thereby solidifying the sludge. Although the accompanying problems can be solved, as described above, there are problems of wear of screw bearings and a problem of electric power burden due to constant operation.

  Regarding the problem of screw bearing wear, measures are taken to reduce the wear rate by operating the screw conveyor 300 at a low speed, and measures to reduce maintenance load such as easy unitization and replacement of wear parts are adopted.

  More specifically, the low speed operation of the screw conveyor 300 is a continuous operation at a very low speed such as about 10 rpm. Note that this numerical value is illustrative rather than limiting.

  The concept of continuous operation includes intermittent operation, and in addition to intermittent operation at regular intervals such as 1 minute operation and 1 minute pause, it is operated like 5 minutes operation and 10 minutes pause. In this way, the operation time and the stop time are set differently, and the rotation speed is lowered when the operation time is set for a relatively long time, and the rotation speed is increased when the operation time is set for a short time. can do.

  The rotation speed and operation stop time described above are set based on data detected by various sensors such as the amount of waste liquid to be processed introduced into the apparatus and the amount of sludge accumulated in the sludge guide tube 240.

Next, measures for reducing maintenance load, such as easy unitization and replacement of wear parts, are performed as follows.
The screw conveyor 300 is composed of a cylindrical body 320 and a spiral screw portion 331 disposed on the outer peripheral surface of the shaft body 330, and is driven to rotate by a motor 340 so that an object to be conveyed is the screw portion 331. By moving while sliding on the upper surface, it is transported (ascending, horizontal, oblique). In the configuration in which the screw conveyor 300 is arranged vertically or obliquely, the screw shaft body 330 is supported by the bearing 332 provided in the lower base 321 of the screw conveyor, so that the screw shaft body 330, the screw portion 331, The entire weight of the object to be conveyed is applied to the bearing 332, and in the oblique arrangement, a part of the weight is supported by the inner wall surface of the cylindrical body 320 of the screw conveyor.

  As described above, in the case where the sludge is a slurry containing moisture and fine grindstone particles, the fine grindstone particles and the like easily enter the bearing 332 portion. In particular, the lower end of the screw shaft body 330 and the bearing 332 are worn significantly. In addition, as the wear progresses, the amount of fine particles entering increases, resulting in a hindrance to the smooth rotation of the screw.

  Therefore, in the present invention, as shown in FIG. 7, an end member that can be attached to the lower end of the screw shaft 330 is prepared as a single unit so that it can be easily replaced as the wear progresses. It is unitized by configuring. This unit is configured to be easily replaced by removing the lower base 321 of the screw conveyor.

  Next, the problem with the conveyance of the water-containing sludge by the screw conveyor 300 is that the contained sludge that is the object to be conveyed is not conveyed upward along the upper surface of the screw portion 331 and is so-called co-rotated at the same place. It is a phenomenon that ends up. This phenomenon is unlikely to occur when the moisture content of the sludge is high and the viscosity is low, but this phenomenon is likely to occur when the sludge is solidified and becomes highly viscous.

In the present invention, in order to prevent this phenomenon, as shown in FIG. 7, a plurality of vertical grooves 323 are provided on the inner wall surface 322 of the cylinder 320 of the conveyor that covers the screw portion 331.
What is necessary is just to determine the specific structure of the vertical groove 323 according to the component of waste liquids (to-be-processed object), such as collection | recovery coolant.

  It should be noted that a known technique may be employed in place of the above-described configuration in which the vertical groove 323 prevents the conveyed object from co-rotating, or in addition to the above-described configuration of the vertical groove 323. The structure of a spiral groove described in JP-A-72524, the structure in which a plurality of protrusions are provided on the inner surface of a cylinder described in Japanese Utility Model Laid-Open No. 6-57994, in the circumferential direction of the cylinder. A configuration in which a protrusion for increasing the frictional force between the cylinder body and the article to be conveyed is formed on the inner peripheral surface of the cylinder body described in JP-A No. 129827, and a cylindrical wall surface described in JP-A-2004-224666 The structure etc. which stick a protrusion can be utilized.

The apparatus of Example 2 which concerns on this invention is demonstrated according to FIGS.
The configuration of the second embodiment is common in the basic part to the configuration of the first embodiment described above, but a different configuration is that a floating material scraper mechanism 260 is introduced into the separation tank 210. That is, in this second embodiment, instead of the configuration of the upper end funnel-shaped tank portion 213, the top cylindrical body 214, and the oil discharge port 215 in the first embodiment, a floating material scraper 261 that is operated by the scraper drive shaft 231 is provided. The suspended matter floating on the upper surface of 210 is scraped and discharged to the outside through the suspended matter discharge unit 262.

The top view which shows 1st Example of the separation-recovery apparatus which concerns on this invention 1 is a front view showing a first embodiment of a separation and recovery apparatus according to the present invention. 1 is a side view showing a first embodiment of a separation and recovery apparatus according to the present invention. The top view which shows 2nd Example of the separation-and-recovery apparatus which concerns on this invention Front view showing a second embodiment of the separation and recovery apparatus according to the present invention. Side view showing a second embodiment of the separation and recovery apparatus according to the present invention. Partial cutaway view of the lower end of the screw conveyor

Explanation of symbols

DESCRIPTION OF SYMBOLS 100- Cyclone 110- Waste liquid inlet 120- Guide pipe 200- Separation apparatus 210- Separation tank 211- Cylindrical tank part 212- Lower end funnel-shaped tank part 213- Upper end funnel-shaped tank part 214- Top cylinder 215- Oil content outlet 220-cylindrical frame 221-whisker net 222-filter 230-scraper

231-Scraper drive shaft 232-Scraper motor 233-Stirring rod 234-Cam mechanism 240-Sludge guide tube 250-Drain communication tube 251-Water level adjusting tube 252-Moisture discharge port 260-Floating material scraper mechanism 261-Floating material Scraper 262-suspended matter discharge section

300-Screw conveyor 310-Sludge outlet 320-Screw conveyor cylinder 321-Lower base of screw conveyor 322-Inner wall surface of screw conveyor cylinder 323-Vertical groove 330-Screw shaft body 331-Screw part 332-Screw shaft Body bearings 340-Screw drive motor

Claims (9)

It is a device that separates and recovers waste liquid such as recovered coolant containing at least oil, moisture and sludge into oil, moisture and sludge by simultaneous and continuous processing with a single device. Separation and recovery device for waste liquid components such as recovery coolant, which has a mechanism for separation and recovery of oil, moisture and sludge by gravity using a tank, and a dewatering and recovery mechanism for hydrous sludge settled at the bottom of the separation tank . The waste liquid content such as recovered coolant according to claim 1, wherein the separation / recovery mechanism of oil, moisture, and sludge by gravity using a separation tank includes a whiskernet and a moisture filtering mechanism using a filter. Component separation and recovery equipment. 3. A separation / recovery mechanism for oil, moisture and sludge by gravity using a separation tank is provided with a scraper mechanism for scraping sediment sludge components adhering to the inner wall surface of the separation tank. An apparatus for separating and recovering waste liquid-containing components such as the recovery coolant described in 1. The separation of waste liquid-containing components such as the recovered coolant according to any one of claims 1 to 3, further comprising a water level adjusting means communicating with the separation tank as a mechanism for collecting the water separated in the separation tank. Recovery device. The apparatus for separating and collecting waste liquid-containing components such as the recovery coolant according to any one of claims 1 to 4, further comprising a scraper mechanism that scrapes and discharges suspended matter at an upper position in the separation tank. A screw conveyor is used as a mechanism for dewatering and collecting the water-containing sludge settled in the lower part of the separation tank, the screw conveyor is disposed in an inclined state, and at least the sludge discharge part of the screw conveyor is higher than the water level of the separation tank The apparatus for separating and collecting waste liquid-containing components such as a recovered coolant according to any one of claims 1 to 5, wherein dehydration is performed in the middle of conveyance by the screw conveyor. The waste liquid content such as recovered coolant according to claim 6, wherein means for preventing co-rotation of the object to be conveyed is provided on an inner wall surface of a cylinder of a screw conveyor used as a dewatering and recovery mechanism for water-containing sludge. Component separation and recovery equipment. The apparatus for separating and collecting waste liquid-containing components such as a recovered coolant according to any one of claims 1 to 7, wherein the rotational speed of the screw conveyor is 100 N (rpm) or less. This is a device that separates and collects waste liquid such as recovered coolant containing at least oil, moisture, and sludge into oil, moisture, and sludge by simultaneously and continuously using a single device. A device that separates and collects oil, moisture, and sludge by the action of gravity using a tank and dehydrates and collects water-containing sludge settled at the bottom of the separation tank is incorporated as a single device. A screw conveyor is used as a mechanism for performing the process, the screw conveyor is disposed in an inclined state, and at least the sludge discharge portion of the screw conveyor is set to a position higher than the water level of the separation tank. These processes are always performed and the screw conveyor is operated to continuously separate and recover the waste liquid-containing components. The method of separating and recovering waste containing components, such as collection coolant and performs a manner.

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