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WO2009028519A1 - Oil sludge weight reducing apparatus - Google Patents

Oil sludge weight reducing apparatus Download PDF

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Publication number
WO2009028519A1
WO2009028519A1 PCT/JP2008/065225 JP2008065225W WO2009028519A1 WO 2009028519 A1 WO2009028519 A1 WO 2009028519A1 JP 2008065225 W JP2008065225 W JP 2008065225W WO 2009028519 A1 WO2009028519 A1 WO 2009028519A1
Authority
WO
WIPO (PCT)
Prior art keywords
oil
sludge
screw
inner cylinder
cylinder
Prior art date
Application number
PCT/JP2008/065225
Other languages
French (fr)
Japanese (ja)
Inventor
Tatsuhiko Minami
Original Assignee
System Kikou Co., Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by System Kikou Co., Ltd. filed Critical System Kikou Co., Ltd.
Priority to JP2009530135A priority Critical patent/JP5302889B2/en
Publication of WO2009028519A1 publication Critical patent/WO2009028519A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/12Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
    • B30B9/14Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing operating with only one screw or worm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/06Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
    • B01D33/073Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for inward flow filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/58Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
    • B01D33/62Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying
    • B01D33/64Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by compression
    • B01D33/648Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by compression by screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D35/00Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/18Heating or cooling the filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/004Sludge detoxification
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/18Treatment of sludge; Devices therefor by thermal conditioning

Definitions

  • the present invention relates to an oil-impregnated sludge reduction device for separating and reducing oil content and harmful substances from oil-containing sludge such as crude oil sludge and crude oil drilling mud.
  • the wax content and alfalten content in the crude oil are deposited, and these are also decomposed products generated by the decomposition of microorganisms such as moisture in the crude oil, iron rust mixed in the crude oil, sand and mud.
  • microorganisms such as moisture in the crude oil, iron rust mixed in the crude oil, sand and mud.
  • sludge sludge containing oil accumulates at the bottom of the crude oil tank.
  • Such sludge is generally called crude oil sludge.
  • oil-containing sludge that resembles crude oil sludge is generated.
  • Such sludge is generally called a drilling mat.
  • the crude oil sludge and the excavation mud contain trace amounts of harmful substances such as water-soluble mercury.
  • oil-containing sludge is disposed of in the case of crude oil sludge with a large amount of oil.
  • the crude oil sludge is subjected to an intermediate treatment and centrifuged, the oil content is reduced from the crude oil sludge and then incinerated.
  • the crude oil sludge or drilling mud was centrifuged, and the oil content decreased after roughly separating the oil content from the crude oil sludge or drilling mud. Oil is removed by incineration of oil-impregnated sludge, and then the residue with reduced oil content is removed. It has been done by landfill.
  • an object of the present invention is to provide a device for reducing the amount of oil-containing sludge that can reduce the content of oil and harmful substances in the oil-containing sludge to an amount that can be disposed of in landfill in a single operation. is there. Disclosure of the invention
  • the present inventor squeezed the oil-containing sludge while supplying water vapor using a screw press type squeezing device.
  • the oil content and harmful substance content in the oil-containing sludge can be reduced satisfactorily in a single operation, and the pitch of the screw blades can be specified.
  • the present invention (1) includes: a screw shaft having a water vapor supply hole; and a screw comprising a screw blade provided in a spiral shape on the outer periphery of at least a part of the screw shaft;
  • An inner cylinder having an oil-water passage hole and surrounding the screw
  • An outer cylinder that is installed outside the casing, and that forms an oil-water discharge gap with the inner cylinder;
  • An oil-impregnated sludge supply port for supplying oil-containing sludge into the inner cylinder, an outer cylinder-side steam supply port for supplying water vapor into the outer cylinder, and a vicinity of the cylinder end on the residue discharge side of the inner cylinder
  • An oil water discharge port for discharging the oil water discharged into the oil water discharge gap to the outside of the device
  • the ratio of the length of the inner cylinder from the cylinder end on the oil-impregnated sludge supply side to the outer cylinder-side water vapor supply port with respect to the length of the inner cylinder is 0.5 or less
  • An oil impregnated sludge reduction device characterized by the above is provided.
  • the present invention (2) is characterized in that the ratio of the pitch of the screw blade to the diameter of the screw blade is 0.5 to 1.25, wherein the oil impregnation according to the present invention (1) is provided.
  • An apparatus for reducing sludge is provided.
  • the present invention (3) is characterized in that the stopper is a stopper through which the screw shaft is passed, slidably attached to the screw shaft, and a pressure adjusting member attached to the back surface.
  • the present invention provides a device for reducing the amount of oil-containing sludge described in the present invention (1). According to the present invention, the oil-containing sludge that can reduce the content of oil and harmful substances in the oil-containing sludge to an amount that can be disposed by landfill in one stage of operation.
  • FIG. 1 is a schematic cross-sectional view of the oil-impregnated sludge reduction device of the present invention when cut along a plane parallel to the direction of movement of the oil-containing sludge, and FIG. 2 shows the direction of movement of the oil-containing sludge.
  • FIG. 3 is a schematic cross-sectional view of the oil-impregnated sludge weight reducing device of the present invention when cut along a plane perpendicular to FIG. 3, and FIG. 3 is a side view of the screw in FIGS. 1 and 2.
  • Fig. 4 is a cross-sectional view showing the inner cylinder and the outer cylinder of Fig. 1, and Fig.
  • FIG. 5 shows how the oil-containing sludge is processed using the oil-containing sludge reduction device 1 1 is a schematic cross-sectional view of the oil-retaining sludge reducing device 1.
  • An oil-impregnated sludge reduction device comprises: a screw shaft having a steam supply hole; and a screw comprising a screw blade spirally provided on the outer periphery of at least a part of the screw shaft;
  • An inner cylinder having an oil-water passage hole and surrounding the screw
  • An outer cylinder that is installed outside the inner cylinder and forms an oil-water discharge gap with the inner cylinder;
  • An oil-containing sludge supply port for supplying oil-containing sludge into the inner cylinder, an outer cylinder-side water vapor supply port for supplying water vapor into the outer cylinder,
  • a stopper installed in the vicinity of the cylinder end of the inner cylinder on the residue discharge side, and forming a residue discharge gap between the inner cylinder and the cylinder end of the inner cylinder on the residue discharge side;
  • An oil water discharge port for discharging the oil water discharged into the oil water discharge gap to the outside of the device
  • the oil-impregnated sludge reducing device has a ratio of a length from a cylinder end of the inner cylinder on the oil-impregnated sludge supply side to the outer cylinder-side steam supply port to a length of the inner cylinder of 0.5 or less.
  • the oil, sludge and moisture in the oil-containing sludge, and the supplied water vapor are discharged into the oil water discharge gap by treating the oil-containing sludge.
  • Condensed water is discharged, but in the present invention, all the oil, harmful substances and moisture in the oil-containing sludge, and the water condensed from the supplied water vapor are all discharged into the oil water discharge gap. Items are described as “oil / water”.
  • FIGS. 1 and 2 are schematic cross-sectional views of the oil-impregnated sludge reduction device of the present invention
  • FIG. 1 is a cross-sectional view taken along a plane parallel to the moving direction of the oil-containing sludge.
  • Fig. 2 is a cross-sectional view of the oil-containing sludge cut along a plane perpendicular to the moving direction.
  • FIG. 3 is a side view of the screw in FIGS. 1 and 2.
  • FIG. 4 is a cross-sectional view showing the inner cylinder and the outer cylinder of FIG. In FIG. 1 and FIG.
  • the oil-impregnated sludge reducing device 1 includes a screw 4, an inner cylinder 5 surrounding the screw 4, an outer side of the inner cylinder 5, and the inner cylinder 5.
  • An outer cylinder 6 installed in such a manner that an oil-water discharge gap 2 2 is formed in the inner cylinder 5, a stopper 7 installed in the vicinity of the cylinder end 18 on the residue discharge side of the inner cylinder 5, and the inner cylinder 5
  • an oil-impregnated sludge supply side flange 8 installed on the oil-impregnated sludge supply side of the outer cylinder 6, and a residue discharge chamber 14 formed on the residue discharge side of the inner cylinder 5 and the outer cylinder 6
  • Residue discharge side flange 9 oil-impregnated sludge supply port 10 for supplying oil-impregnated sludge into the inner cylinder 5, and outer cylinder-side steam supply port for supplying water vapor into the outer cylinder 6 1 1 and the residue discharge chamber 1 4 and the residue discharge port 1 2 for dis
  • the screw 4 includes a screw shaft 2 and screw blades 3.
  • the screw blade 3 is spirally provided on the outer periphery of at least a part of the screw single shaft 2.
  • the screw shaft 2 is rotatably fixed to the oil-containing sludge supply side flange 8 and the residue discharge side flange 9.
  • the screw shaft 2 is a hollow tube, and one end 28 of the screw shaft 2 is opened to supply water vapor into the tube of the screw shaft 2, while the screw shaft 2 The other end 29 of the shaft 2 is sealed.
  • the shaft wall of the screw shaft 2 is formed with a water vapor supply hole 27 for discharging water vapor from the space inside the shaft to the outside of the shaft.
  • the water vapor supply hole 27 is a water vapor supply hole for supplying water vapor to the oil-impregnated sludge in the inner cylinder 5 from the screw shaft 2 side, that is, from the center of the inner cylinder 5 to the outside. is there.
  • the diameter of the water vapor supply hole 27 is appropriately selected depending on the size of the residue in the oil-containing sludge to be treated, but is usually 5 to 12 mm, preferably 8 to 12 mm, particularly preferably 8 to 1. Omm.
  • the range 24 in which the water vapor supply hole 27 is formed is selected as appropriate, but normally, the oil-impregnated sludge supply side is close to the oil-impregnated sludge supply-side flange 8, and normally
  • the residue discharge side is the ratio of the length of the range 24 in which the water vapor supply hole 2 7 is formed to the length of the portion 23 surrounded by the inner cylinder 5 (reference numeral 24 Z code 2 3) force S 0.5 to 0.8 6 6, preferably 0.6 6 to 0.8 6 6, particularly preferably 0.7 6 to 0.8 6 6.
  • the number of water vapor supply holes 27 is appropriately selected depending on the type of oil-containing sludge, the scale of the apparatus, and the like.
  • the screw blade 3 is formed in a spiral shape on the outer periphery of the screw shaft 2, and when the screw 4 rotates, the oil-containing sludge in the inner cylinder 5 is discharged from the oil-containing sludge supply side.
  • the shape is not particularly limited as long as it can be moved to the side.
  • the diameter 25 of the screw blade 3 may be the same length as the inner diameter of the inner cylinder 5 or may be slightly smaller than the inner diameter of the inner cylinder 5.
  • the clearance between the screw blade 3 and the inner cylinder 5 is usually 1 mm or less, preferably 0.5 mm or less, especially Preferably it is 0.1 mm or less.
  • the ratio of the pitch 26 of the screw blade 3 to the diameter 25 of the screw blade 3 (reference numeral 26 / reference numeral 25) is 0.25 to 1 ⁇ 25.
  • the ratio of the pitch 26 of the screw blade 3 to the diameter 25 of the screw (code 26 Z symbol 25) is preferably 0.5 to 1.25, particularly preferably 0.75 to: I More preferably, it is 0.9 to 1.
  • the pitch 26 of the screw blade 3 is the distance between the apexes 26 1 a and 26 1 b of the screw blade in FIG. 3, that is, the screw blade 3 is viewed from the side. This is the distance between the apexes of adjacent feathers.
  • the pitch 26 of the screw blade 3 may be the same or different over the entire range of the screw blade 3.
  • the shape of the screw 4 is as shown in FIGS.
  • the shape is not limited to the shape shown in Fig. 1.
  • Other examples include those with a larger screw shaft diameter toward the residue discharge side and those with a smaller pitch toward the residue discharge side. Can be mentioned.
  • the inner cylinder 5 has a cylindrical shape.
  • a cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder 5 is fixed to the oil-impregnated sludge supply-side flange 8, and the cylinder end 19 is closed by the oil-containing sludge supply-side flange 8.
  • the cylinder end 18 on the residue discharge side of the inner cylinder 5 is fixed to the residue discharge side flange 9, and the opening of the cylinder end 18 is connected to the residue discharge chamber 14. ing. That is, the tube end 18 is opened so that the residue is discharged out of the inner tube.
  • An oil water passage hole is formed on the cylindrical wall of the inner cylinder 5 so that the oil water separated from the oil containing sludge is discharged from the casing 5 to the oil water discharge gap 22 2 by squeezing the oil containing sludge. (Not shown) is formed.
  • the cylindrical wall of the inner cylinder 5 is not particularly limited as long as the oil water passage hole is formed.
  • Examples of the cylindrical wall of the inner cylinder 5 include holes such as a wire mesh and a punching metal. Punched plate material, screen wire mesh, etc. are listed.
  • the diameter of the oil water passage hole formed in the cylindrical wall of the inner cylinder 5 is appropriately selected depending on the size of the residue in the oil-containing sludge to be treated, but usually 0.76 to: 1. It is 96 mm, preferably 1.40 to 1.74 mm, particularly preferably 1.53 to 1.63 mm.
  • the diameter of the oil water passage hole indicates the opening length of the wire mesh, and when the cylinder wall of the inner cylinder 5 is a punching metal, The diameter of the oil / water passage hole is the diameter of the punched hole.
  • Oil-containing sludge is squeezed between the inner wall of the inner cylinder 5 and the screw blade 4 by being installed so as to surround the inner cylinder 5 and the screw 4.
  • a squeezing space 17 is formed.
  • the outer cylinder 6 has a cylindrical shape.
  • a cylinder end 20 on the oil-impregnated sludge supply side of the outer cylinder 6 is fixed to the oil-impregnated sludge supply-side flange 8, and the cylinder end 20 is closed by the oil-containing sludge supply-side flange 8.
  • the cylinder end 21 on the residue discharge side of the outer cylinder 6 is fixed to the residue discharge flange 9, and the oil water discharge gap 22 and the residue discharge chamber 14 are It is isolated by the residue discharge flange 9. That is, the oil water discharge gap 22 is blocked by the residue discharge side flange 9 so that the oil water discharged into the oil water discharge gap 22 does not flow into the residue discharge chamber 14. Yes.
  • the width of the oil water discharge gap 22 formed by the inner cylinder 5 and the outer cylinder 6, in other words, the distance between the outer side of the inner cylinder 5 and the inner side of the outer cylinder 6 is determined by the oil-containing sludge. If the oil, toxic substances and moisture separated from the oil-containing sludge by squeezing, and the water that the supplied water vapor has liquefied, that is, the oil water is discharged and can flow to the oil water discharge port 13, There are no particular restrictions.
  • FIGS. 1 and 2 show that the outer cylinder 6 has a circular cross-sectional shape when cut along a plane perpendicular to the moving direction of the oil-containing sludge.
  • the shape of the outer cylinder 6 is not limited to this, but the inner cylinder 5 can be installed on the inner side, and the oil water discharge gap for allowing the oil water to be discharged and flow to the oil water discharge port 13 is provided. Any material that can be formed may be used.
  • the shape of the outer cylinder for example, a force-pillar shape in which the upper side is flat and the lower side is rounded.
  • the cylindrical wall at the bottom of the outer cylinder 6 may be inclined toward the oil / water discharge port 13.
  • the stopper 7 is fixed to the screw shaft 2 and is installed in the vicinity of the cylinder end 18 on the residue discharge side of the inner cylinder 5.
  • the stopper 7 It functions to adjust the compressibility of oil-containing sludge by adjusting the amount of residue discharged. Specifically, by adjusting the installation position of the stopper 7, the size of the residue discharge gap 15 formed between the stopper 7 and the tube end 18 is adjusted, and the Residue discharge can be adjusted. Then, the compression ratio of the oil-containing sludge can be adjusted by adjusting the ratio of the discharge amount of the residue to the supply amount of the oil-containing sludge.
  • the installation position of the stopper 7 or the discharge gap 15 of the residue formed by the stopper 7 and the cylinder end 18 is the type of oil-containing sludge, the oil content of the oil-containing sludge, processing conditions, etc. Is appropriately selected.
  • the screw shaft is passed through, and is slidably attached to the screw shaft via a bearing or the like.
  • examples include a stopper to which a pressure adjusting member that applies pressure by hydraulic pressure, air pressure, or the like is attached.
  • the back surface of the stopper is the side opposite to the side that forms the discharge gap with the inner cylinder.
  • the size of the discharge gap and the pressure of the squeezing are adjusted according to the type and physical properties of the object to be processed. This makes it easy to select treatment conditions such as the amount of residue discharged and the compression rate.
  • the oil-containing sludge supply port 10 is a supply port for supplying oil-containing sludge into the inner cylinder 5.
  • the installation position of the oil-impregnated sludge supply port 10 in the oil-impregnated sludge moving direction 34 is on the oil-impregnated sludge supply side of the inner cylinder 5 with respect to the length 31 of the inner cylinder 5.
  • the ratio of the length 33 from the cylinder end 19 to the oil-impregnated sludge supply port 10 (reference numeral 3 3 Z sign 3 1), 0.15 or less, preferably 0.125 or less, particularly preferably It is a position where 0 .09 3 to 0.
  • Length 3 from the cylinder end 10 on the oil-impregnated sludge supply side of the inner cylinder 5 to the length 31 of the inner cylinder 5 to the oil-containing sludge supply port 10 When the ratio of 3 is within the above range, the oil content of the oil-containing sludge is reduced.
  • the length 31 of the inner cylinder 5 refers to the distance from the cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder to the cylinder end 18 on the residue discharge side of the inner cylinder.
  • the position of the oil-containing sludge supply port 10 refers to the center position of the oil-containing sludge supply port 10.
  • the installation position of the oil-impregnated sludge supply port 10 in the circumferential direction of the inner cylinder 5 and the outer cylinder 6 is usually the uppermost position as shown in FIGS. 1 and 4, It is not limited to this, and is appropriately selected depending on the position of an oil-containing sludge supply pipe (not shown).
  • the outer cylinder-side water vapor supply port 11 supplies water vapor to supply oil vapor from the inner cylinder 5 side to the oil-impregnated sludge in the inner cylinder 5, that is, from the outside of the inner cylinder 5 toward the center. Supply port.
  • the installation position of the outer cylinder-side water vapor supply port 11 in the moving direction of the oil-impregnated sludge is as follows.
  • the ratio of the length 3 2 (symbol 3 2 / symbol 3 1) from the cylinder end 19 to the outer cylinder side steam supply port 11 is not more than 0 ⁇ 5, preferably ⁇ 0.3 to 0.5, especially The position is preferably 0.14 to 0.3, and more preferably 0.18 to 0.25.
  • the ratio of the length 3 2 from the cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder 5 to the length 31 of the inner cylinder 5 to the outer cylinder side water vapor supply port 11 is within the above range.
  • the position of the outer cylinder side water vapor supply port 11 refers to the center position of the outer cylinder side water vapor supply port 11.
  • the installation position of the outer cylinder side water vapor supply port 11 in the circumferential direction of the outer cylinder 6 is the lowest position in FIGS. 1 and 4, but is limited to this. Instead, it is appropriately selected depending on the position of a water vapor supply pipe (not shown). Further, the number of the outer cylinder side water vapor supply ports 11 is not particularly limited, and may be 1 or 2 or more.
  • the oil water discharge port 13 is a discharge port for discharging the oil water discharged to the oil water discharge gap 22 to the outside of the apparatus.
  • the installation position of the oil / water discharge ports 13 and the number of the oil / water discharge ports 13 in the moving direction of the oil-containing sludge are not particularly limited and are appropriately selected. Further, the installation position of the oil / water discharge port 13 in the circumferential direction of the outer cylinder 6 is usually at the lowest position.
  • the exhaust port 16 is a gas discharge port for discharging a gas such as water vapor in the apparatus to the outside of the apparatus.
  • the installation position of the exhaust port 16 and the number of the exhaust ports 16 in the moving direction of the oil-containing sludge are not particularly limited and are appropriately selected.
  • the oil-containing sludge supply port 10, the residue discharge port 12, the oil / water discharge port 13, and the exhaust port 16 are normally open. Further, a strainer for separating fine residues mixed in the oil water may be installed at the oil water discharge port 13.
  • the oil-impregnated sludge reducing device 1 is provided with driving means (not shown) for rotating the screw 4.
  • the screw shaft 2 and the inner cylinder 5 may be horizontal, may be inclined to the oil-containing sludge supply side, and may be inclined to the residue discharge side. Or it may be vertical.
  • FIG. 5 is a schematic cross-sectional view of the oil-retaining sludge reduction device 1 showing a state in which the oil-containing sludge reduction device 1 is used to process the oil-containing sludge.
  • the oil impregnated sludge reducing device 1 the oil impregnated sludge 41 is supplied to the oil impregnated sludge supply port 1 by supplying the oil impregnated sludge 41 from the oil impregnated sludge supply port 10 and rotating the screw 4.
  • the compressed space 17 formed in a spiral around the screw shaft 2 is moved toward the cylinder end 18 on the residue discharge side of the inner cylinder, and the oil-containing sludge 41 is By pushing toward the cylinder end 18, high pressure is applied to the oil-containing sludge 41, and the oil-containing sludge 41 is squeezed.
  • steam 40 0 a is supplied from one end 28 of the screw shaft 2
  • steam 40 b is supplied from the outer cylinder side steam supply port 11 1, thereby Steam is brought into contact with the sludge 41 from both the center of the inner cylinder 5 and the outside.
  • the oil-impregnated sludge reducing device 1 In the oil-impregnated sludge reducing device 1, the oil-impregnated sludge 4 1 comes into contact with the water vapor 40 at the time of pressing, so that the oil-impregnated sludge becomes high temperature and the water content increases. This makes it easier to separate the solid and liquid components. Therefore, the oil-retaining sludge reducing device 1 can increase the effect of reducing the oil content in the oil-containing sludge 41, so that the oil content in the residue 43 can be reduced. it can.
  • the oil-containing sludge is heated by water vapor supplied into the oil-containing sludge reduction device 1, and the temperature of the water vapor supplied is preferably from 100 to 200 ° C., preferably Is from 100 to 180 ° C, particularly preferably from 110 to 150 ° C, and more preferably from 110 to 120 ° C.
  • the supplied When the temperature of the water vapor is within the above range, the effect of reducing the oil content in the oil-containing sludge 41 is enhanced. Further, the temperature in the oil-reducing sludge reducing device 1 during the pressing is a steady-state temperature of 100 to 200 ° C., preferably 100 to 180, particularly preferably.
  • the temperature in the oil-containing sludge reducing device 1 during the pressing is within the above range, the effect of reducing the oil content in the oil-containing sludge 4 1 is enhanced.
  • the temperature in the oil-retaining sludge reducing device 1 during the pressing is such that a thermocouple or the like is installed in the oil water discharge gap 22 at a position that does not directly contact the supplied steam. Obtained by measuring the temperature of oil drain gap 2 2.
  • the pressing pressure for pressing the oil-containing sludge is appropriately selected according to the type of oil-containing sludge.
  • the pressing time of the oil-containing sludge 41 during the pressing that is, the oil-containing sludge 41 is supplied from the oil-containing sludge supply port 10, and the residue 4 3 is discharged from the residue discharge gap 15.
  • the time until it is discharged as 1 to 3 hours, preferably 1.5 to 3 hours, particularly preferably 2 to 2.5 hours.
  • the pressing time of the oil-containing sludge 41 during the pressing is within the above range, the effect of reducing the oil content in the oil-containing sludge 41 is enhanced.
  • the rotational speed of the screw 4 the supply amount of the oil impregnated sludge 41 from the oil impregnated sludge supply port 10, and the residue from the discharge gap 15 of the residue
  • the squeezing time of the oil-containing sludge 41 during the squeezing can be adjusted.
  • the amount of the residue 4 3 discharged from the residue discharge gap 15 is adjusted by adjusting the size of the residue discharge gap 15. be able to.
  • the oil-impregnated sludge reduction device of the present invention comprises the inner cylinder relative to the length of the inner cylinder.
  • the ratio of the length from the cylinder end on the oil-impregnated sludge supply side to the steam supply port on the outer cylinder side is 0.5 or less, so that at the initial stage of the oil-containing sludge pressing step, that is, the oil-containing sludge supply Since water vapor can be brought into contact with the oil-containing sludge closer to the mouth, the oil-containing sludge's oil content and harmful substances are reduced more effectively, and a residue with a low content of oil and harmful substances is obtained. It is done.
  • the oil-impregnated sludge reduction device of the present invention further increases the ratio of the pitch of the screw blade to the diameter of the screw blade, that is, by relatively increasing the pitch of the screw blade.
  • the oil-containing sludge is compressed and heated for a long time so that the oil-containing sludge is slowly compressed. Further, by increasing the pressing time and heating time of the oil-containing sludge, the effect of reducing the oil content and harmful substances of the oil-containing sludge is further enhanced.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Treatment Of Sludge (AREA)

Abstract

An oil sludge weight reducing apparatus characterized by including a screw composed of a screw axle with a steam supply hole and a screw vane helically provided around the outer circumference of at least a portion of the screw axle; an inner tube with oil water passage hole provided so as to surround the screw; an outer tube disposed outside the inner tube so as to provide an oil water discharge interstice between the same and the inner tube; an oil sludge supply port for supply of oil sludge in the inner tube; an outer-tube-side steam supply port for supply of steam in the outer tube; a stopper disposed in the vicinity of the edge of the inner tube on a residue discharge side so as to provide a residue discharge interstice between the same and the edge of the inner tube on a residue discharge side; an oil water discharge port for discharge, outside the apparatus, of the oil water having been discharged in the oil water discharge interstice; and driving means for rotary drive of the screw, wherein the ratio of the length from the edge of the inner tube on an oil sludge supply side to the outer-tube-side steam supply port to the length of the inner tube is 0.5 or below. The oil sludge weight reducing apparatus would attain reduction of the amount of oil and hazardous substances contained in oil sludge to the level allowing landfill disposal by a one-step operation.

Description

2008/065225 明細書 含油スラッジの減量化装置 技術分野  2008/065225 Description Oil-impregnated sludge reduction equipment Technical Field
本発明は、 原油スラッジ、 原油掘削マッド等の含油スラッジから、 油 分及び有害物質を分離し、 減量化するための含油スラッジの減量化装置 に関する。 背景技術  The present invention relates to an oil-impregnated sludge reduction device for separating and reducing oil content and harmful substances from oil-containing sludge such as crude oil sludge and crude oil drilling mud. Background art
原油をタンク中で貯蔵すると、 原油中のワックス分やアルファルテン 分が析出し、そして、 これらと、原油中の水分、原油に混入した鉄さび、 砂、 泥等、 微生物の分解により生成した分解物とが混ざり合ったものが 汚泥となって沈降するので、 原油タンクの底部には、 油分を含有する汚 泥が堆積する。 このような汚泥は、 一般に、 原油スラッジと呼ばれてい る。 また、 原油を掘削した際にも、 原油スラッジによく似た含油汚泥が 生じる。 このような汚泥は、一般に、掘削マツドと呼ばれている。 また、 該原油スラッジゃ該掘削マッドには、 水溶性の水銀等の微量の有害物質 が含まれている。  When crude oil is stored in a tank, the wax content and alfalten content in the crude oil are deposited, and these are also decomposed products generated by the decomposition of microorganisms such as moisture in the crude oil, iron rust mixed in the crude oil, sand and mud. As the sludge is mixed with sludge and settles, sludge containing oil accumulates at the bottom of the crude oil tank. Such sludge is generally called crude oil sludge. In addition, when oil is excavated, oil-containing sludge that resembles crude oil sludge is generated. Such sludge is generally called a drilling mat. Further, the crude oil sludge and the excavation mud contain trace amounts of harmful substances such as water-soluble mercury.
従来、 このような含油スラッジの処分は、 油分が多い原油スラッジの 場合、 原油スラッジを中間処理後遠心分離して、 原油スラッジから概ね の油分を分離した後、 油分量が減少した含油スラッジを焼却することに より、 また、 油分が少ない原油スラッジゃ掘削マッドの場合、 原油スラ ッジ又は掘削マッドを遠心分離して、 原油スラッジ又は掘削マッドから 概ねの油分を分離した後、 油分量が減少した含油スラッジを焼却するこ とにより、 油分を除去し、 次いで、 油分の含有量が減少した残渣物を、 埋立処分することにより行われてきた。 Conventionally, such oil-containing sludge is disposed of in the case of crude oil sludge with a large amount of oil. After the crude oil sludge is subjected to an intermediate treatment and centrifuged, the oil content is reduced from the crude oil sludge and then incinerated. In addition, in the case of crude oil sludge drilling mud with low oil content, the crude oil sludge or drilling mud was centrifuged, and the oil content decreased after roughly separating the oil content from the crude oil sludge or drilling mud. Oil is removed by incineration of oil-impregnated sludge, and then the residue with reduced oil content is removed. It has been done by landfill.
環境への負荷という観点から、 残渣物を埋立処分するためには、 残渣 物中の油分及び有害物質の含有量は、 埋立処分に係る判定基準以下でな ければならない。 ところが、 中間処理及び遠心分離だけでは、 残渣物中 の油分及び有害物質の含有量を、 埋立処分に係る判定基準以下にするこ とはできないため、 従来の含油スラッジの処分方法では、 遠心分離の後 に、 含油スラッジの焼却操作が必須であった。  From the viewpoint of environmental impact, in order to dispose of residue in landfills, the content of oil and harmful substances in the residue must be below the criteria for landfill disposal. However, only intermediate treatment and centrifugation cannot reduce the content of oil and hazardous substances in the residue below the criteria for landfill disposal. Later, incineration of oil-containing sludge was essential.
そのため、 従来の含油スラッジの処分方法では、 遠心分離及ぴ焼却、 又は中間処理、 遠心分離及び焼却という 2〜3段の操作を行うため、 処 理コストが高くなるという問題及び装置スペースが広くなってしまうと いう問題があった。よって、 1段の操作で、含油スラッジ中の油分量を、 埋立処分可能な量まで減少させることができる装置の開発が望まれてい る。  For this reason, conventional oil-containing sludge disposal methods perform two- and three-stage operations such as centrifugation and incineration, or intermediate treatment, centrifugation and incineration, resulting in increased processing costs and equipment space. The problem was that Therefore, it is desired to develop a device that can reduce the amount of oil in the oil-containing sludge to a level that can be disposed of by landfill in a single operation.
従って、 本発明の課題は、 1段の操作で、 含油スラッジ中の油分及び 有害物質の含有量を、 埋立処分可能な量まで減少させることができる含 油スラッジの減量化装置を提供することにある。 発明の開示  Accordingly, an object of the present invention is to provide a device for reducing the amount of oil-containing sludge that can reduce the content of oil and harmful substances in the oil-containing sludge to an amount that can be disposed of in landfill in a single operation. is there. Disclosure of the invention
本発明者は、 上記従来技術における課題を解決すべく、 鋭意研究を重 ねた結果、 スク リ ュープレス型の圧搾装置を用い、 水蒸気を供給しなが ら含油スラッジを圧搾し、 その圧搾の際に、 水蒸気の供給位置を特定の 範囲とすることにより、 1段の操作で、 含油スラッジ中の油分及び有害 物質の含有量を良好に減量化することができること、 更に、 スクリュー 羽根のピッチを特定の範囲とすることにより、 長時間を掛けて圧搾する のに適するので、 更に、 減量化効果が高まることを見出し、 本発明を完 成させるに至った。 すなわち、 本発明 (1 ) は、 水蒸気の供給孔を有するスクリュー軸、 及び該スクリユー軸の少なく とも一部の外周に螺旋状に設けられるスク リユー羽根からなるスクリューと、 As a result of diligent research to solve the above-described problems in the prior art, the present inventor squeezed the oil-containing sludge while supplying water vapor using a screw press type squeezing device. In addition, by setting the supply position of the water vapor within a specific range, the oil content and harmful substance content in the oil-containing sludge can be reduced satisfactorily in a single operation, and the pitch of the screw blades can be specified. By making it within the range, it is suitable for squeezing for a long time, and further, it has been found that the effect of reducing the weight is enhanced, and the present invention has been completed. That is, the present invention (1) includes: a screw shaft having a water vapor supply hole; and a screw comprising a screw blade provided in a spiral shape on the outer periphery of at least a part of the screw shaft;
油水の通過孔を有し、 該スクリューを囲む内筒と、  An inner cylinder having an oil-water passage hole and surrounding the screw;
該內筒の外側に設置され、 該内筒との間に油水の排出隙間を形成する 外筒と、  An outer cylinder that is installed outside the casing, and that forms an oil-water discharge gap with the inner cylinder;
該内筒内に、 含油スラッジを供給するための含油スラッジ供給口と、 該外筒内に水蒸気を供給するための外筒側水蒸気供給口と、 該内筒の残渣物排出側の筒端近傍に設置され、 該内筒の残渣物排出側 の筒端との間に残渣物の排出隙間を形成するストッパーと、  An oil-impregnated sludge supply port for supplying oil-containing sludge into the inner cylinder, an outer cylinder-side steam supply port for supplying water vapor into the outer cylinder, and a vicinity of the cylinder end on the residue discharge side of the inner cylinder A stopper that forms a residue discharge gap between the inner cylinder and the cylinder end on the residue discharge side of the inner cylinder;
該油水の排出隙間に排出された油水を、 装置外に排出するための油水 排出口と、  An oil water discharge port for discharging the oil water discharged into the oil water discharge gap to the outside of the device;
該スクリユーを回転駆動させる駆動手段と、  Drive means for rotationally driving the screw;
を有し、 Have
該内筒の長さに対する該内筒の含油スラッジ供給側の筒端から該外筒 側水蒸気供給口までの長さの比が、 0 . 5以下であること、  The ratio of the length of the inner cylinder from the cylinder end on the oil-impregnated sludge supply side to the outer cylinder-side water vapor supply port with respect to the length of the inner cylinder is 0.5 or less,
を特徴とする含油スラッジの減量化装置を提供するものである。 An oil impregnated sludge reduction device characterized by the above is provided.
また、 本発明 (2 ) は、 前記スクリュー羽根の径に対する前記スクリ ユー羽根のピッチの比が、 0 . 5 〜 1 . 2 5であることを特徴とする前 記本発明( 1 )記載の含油スラッジの減量化装置を提供するものである。 また、 本発明 (3 ) は、 前記ストッパーが、 前記スクリュー軸が揷通 され、 前記スクリュー軸に摺動可能に取り付けられ、 且つ、 背面に調圧 部材が取り付けられているストッパーであることを特徴とする前記本発 明 (1 ) 記載の含油スラッジの減量化装置を提供するものである。 本発明によれば、 1段の操作で、 含油スラッジ中の油分及び有害物質 の含有量を、 埋立処分可能な量まで減少させることができる含油スラッ ジの減量化装置を提供することができる 図面の簡単な説明 Further, the present invention (2) is characterized in that the ratio of the pitch of the screw blade to the diameter of the screw blade is 0.5 to 1.25, wherein the oil impregnation according to the present invention (1) is provided. An apparatus for reducing sludge is provided. Further, the present invention (3) is characterized in that the stopper is a stopper through which the screw shaft is passed, slidably attached to the screw shaft, and a pressure adjusting member attached to the back surface. The present invention provides a device for reducing the amount of oil-containing sludge described in the present invention (1). According to the present invention, the oil-containing sludge that can reduce the content of oil and harmful substances in the oil-containing sludge to an amount that can be disposed by landfill in one stage of operation. Brief Description of the Drawings
第 1図は、含油スラッジの移動方向に対して平行な面で切ったときの、 本発明の含油スラッジの減量化装置の模式的な断面図であり、第 2図は、 含油スラッジの移動方向に対して垂直な面で切ったときの、 本発明の含 油スラッジの減量化装置の模式的な断面図であり、 第 3図は、 第 1図及 び第 2図中のスクリューの側面図であり、 第 4図は、 第 1図の内筒及び 外筒を記載した断面図であり、 第 5図は、 含油スラッジの減量化装置 1 を用いて含油スラッジを処理している様子を示す、 該含油スラッジの減 量化装置 1の模式的な断面図である。 発明を実施するための最良の形態  FIG. 1 is a schematic cross-sectional view of the oil-impregnated sludge reduction device of the present invention when cut along a plane parallel to the direction of movement of the oil-containing sludge, and FIG. 2 shows the direction of movement of the oil-containing sludge. FIG. 3 is a schematic cross-sectional view of the oil-impregnated sludge weight reducing device of the present invention when cut along a plane perpendicular to FIG. 3, and FIG. 3 is a side view of the screw in FIGS. 1 and 2. Fig. 4 is a cross-sectional view showing the inner cylinder and the outer cylinder of Fig. 1, and Fig. 5 shows how the oil-containing sludge is processed using the oil-containing sludge reduction device 1 1 is a schematic cross-sectional view of the oil-retaining sludge reducing device 1. FIG. BEST MODE FOR CARRYING OUT THE INVENTION
本発明の含油スラッジの減量化装置は、 水蒸気の供給孔を有するスク リュー軸、 及び該スクリュー軸の少なくとも一部の外周に螺旋状に設け られるスクリユー羽根からなるスクリューと、  An oil-impregnated sludge reduction device according to the present invention comprises: a screw shaft having a steam supply hole; and a screw comprising a screw blade spirally provided on the outer periphery of at least a part of the screw shaft;
油水の通過孔を有し、 該スクリューを囲む内筒と、  An inner cylinder having an oil-water passage hole and surrounding the screw;
該内筒の外側に設置され、 該内筒との間に油水の排出隙間を形成する 外筒と、  An outer cylinder that is installed outside the inner cylinder and forms an oil-water discharge gap with the inner cylinder;
該内筒内に、 含油スラッジを供給するための含油スラッジ供給口と、 該外筒内に水蒸気を供給するための外筒側水蒸気供給口と、  An oil-containing sludge supply port for supplying oil-containing sludge into the inner cylinder, an outer cylinder-side water vapor supply port for supplying water vapor into the outer cylinder,
該内筒の残渣物排出側の筒端近傍に設置され、 該内筒の残渣物排出側 の筒端との間に残渣物の排出隙間を形成するストッパーと、  A stopper installed in the vicinity of the cylinder end of the inner cylinder on the residue discharge side, and forming a residue discharge gap between the inner cylinder and the cylinder end of the inner cylinder on the residue discharge side;
該油水の排出隙間に排出された油水を、 装置外に排出するための油水 排出口と、  An oil water discharge port for discharging the oil water discharged into the oil water discharge gap to the outside of the device;
該スクリユーを回転駆動させる駆動手段と、 を有し、 Drive means for rotationally driving the screw; Have
該内筒の長さに対する該内筒の含油スラッジ供給側の筒端から該外筒 側水蒸気供給口までの長さの比が、 0 . 5以下である含油スラッジの減 量化装置である。 なお、 本発明の含油スラッジの減量化装置では、 該含 油スラッジを処理することにより、 該油水の排出隙間には、 該含油スラ ッジ中の油分、 有害物質及び水分、 並びに供給した水蒸気が凝縮した水 分が排出されるが、 本発明では、 該含油スラッジ中の油分、 有害物質及 ぴ水分、 並びに供給した水蒸気が凝縮した水分を全て含めて、 該油水の 排出隙間に排出される排出物を、 「油水」 と記載する。  The oil-impregnated sludge reducing device has a ratio of a length from a cylinder end of the inner cylinder on the oil-impregnated sludge supply side to the outer cylinder-side steam supply port to a length of the inner cylinder of 0.5 or less. In the oil-impregnated sludge reduction device of the present invention, the oil, sludge and moisture in the oil-containing sludge, and the supplied water vapor are discharged into the oil water discharge gap by treating the oil-containing sludge. Condensed water is discharged, but in the present invention, all the oil, harmful substances and moisture in the oil-containing sludge, and the water condensed from the supplied water vapor are all discharged into the oil water discharge gap. Items are described as “oil / water”.
本発明の含油スラッジの減量化装置について、 第 1図〜第 4図を参照 して説明する。 第 1図及び第 2図は、 本発明の含油スラッジの減量化装 置の模式的な断面図であり、 第 1図は、 含油スラッジの移動方向に対し て平行な面で切ったときの断面図であり、 第 2図は、 含油スラッジの移 動方向に対して垂直な面で切ったときの断面図である。また、第 3図は、 第 1図及び第 2図中のスク リ ューの側面図である。 また、 第 4図は、 第 1図の内筒及び外筒を記載した断面図である。 第 1図及び第 2図中、 含 油スラッジの減量化装置 1は、 スク リ ュー 4と、 該スクリュー 4を囲む 内筒 5と、 該内筒 5の外側に、 該内筒 5との間に油水の排出隙間 2 2が 形成されるようにして設置される外筒 6と、 該内筒 5の残渣物排出側の 筒端 1 8の近傍に設置されるストッパー 7と、 該内筒 5及び該外筒 6の 含油スラッジ供給側に設置される含油スラッジ供給側フランジ 8と、 該 内筒 5及び該外筒 6の残渣物排出側に残渣物排出室 1 4を形成するよう にして設置される残渣物排出側フランジ 9と、 該内筒 5内に含油スラッ ジを供給するための含油スラッジ供給口 1 0と、 該外筒 6内に水蒸気を 供給するための外筒側水蒸気供給口 1 1と、 該残渣物排出室 1 4から残 渣物を装置外へ排出するための残渣物排出口 1 2と、 該油水の排出隙間  The oil-impregnated sludge reduction device of the present invention will be described with reference to FIGS. 1 and 2 are schematic cross-sectional views of the oil-impregnated sludge reduction device of the present invention, and FIG. 1 is a cross-sectional view taken along a plane parallel to the moving direction of the oil-containing sludge. Fig. 2 is a cross-sectional view of the oil-containing sludge cut along a plane perpendicular to the moving direction. FIG. 3 is a side view of the screw in FIGS. 1 and 2. FIG. 4 is a cross-sectional view showing the inner cylinder and the outer cylinder of FIG. In FIG. 1 and FIG. 2, the oil-impregnated sludge reducing device 1 includes a screw 4, an inner cylinder 5 surrounding the screw 4, an outer side of the inner cylinder 5, and the inner cylinder 5. An outer cylinder 6 installed in such a manner that an oil-water discharge gap 2 2 is formed in the inner cylinder 5, a stopper 7 installed in the vicinity of the cylinder end 18 on the residue discharge side of the inner cylinder 5, and the inner cylinder 5 And an oil-impregnated sludge supply side flange 8 installed on the oil-impregnated sludge supply side of the outer cylinder 6, and a residue discharge chamber 14 formed on the residue discharge side of the inner cylinder 5 and the outer cylinder 6 Residue discharge side flange 9, oil-impregnated sludge supply port 10 for supplying oil-impregnated sludge into the inner cylinder 5, and outer cylinder-side steam supply port for supplying water vapor into the outer cylinder 6 1 1 and the residue discharge chamber 1 4 and the residue discharge port 1 2 for discharging the residue from the apparatus to the outside of the apparatus, and the oil water discharge gap
5 22に排出された油水を、 装置外へ排出するための油水排出口 1 3と、 該外筒 6内のガスを、装置外へ排出するための排気口 1 6と、を有する。 第 3図に示すように、 該スク リ ュー 4は、 スク リュー軸 2と、 スク リ ユー羽根 3と、 からなる。 そして、 該スク リ ュー羽根 3は、 該スクリュ 一軸 2の少なくとも一部の外周に螺旋状に設けられている。 該スクリュ 一軸 2は、 該含油スラッジ供給側フランジ 8と該残渣物排出側フランジ 9に、 回転可能に固定される。 Five An oil / water discharge port 13 for discharging the oil / water discharged to the outside of the apparatus 13 and an exhaust port 16 for discharging the gas in the outer cylinder 6 to the outside of the apparatus are provided. As shown in FIG. 3, the screw 4 includes a screw shaft 2 and screw blades 3. The screw blade 3 is spirally provided on the outer periphery of at least a part of the screw single shaft 2. The screw shaft 2 is rotatably fixed to the oil-containing sludge supply side flange 8 and the residue discharge side flange 9.
該スク リ ュー軸 2は、 中空の管であり、 該スク リュー軸 2の一端 2 8 は、 該スクリユー軸 2の管内に水蒸気を供給するために開口になってお り、 一方、 該スク リュー軸 2の他端 2 9は、 封止されている。 そして、 該スクリユー軸 2の軸壁には、 軸内の空間から軸外へ水蒸気を放出する ための、 水蒸気供給孔 2 7が形成されている。 該水蒸気供給孔 2 7は、 該内筒 5内の含油スラッジに対しスク リ ュー軸 2側から、 すなわち、 該 内筒 5の中心から外に向けて水蒸気を供給するための水蒸気の供給孔で ある。  The screw shaft 2 is a hollow tube, and one end 28 of the screw shaft 2 is opened to supply water vapor into the tube of the screw shaft 2, while the screw shaft 2 The other end 29 of the shaft 2 is sealed. The shaft wall of the screw shaft 2 is formed with a water vapor supply hole 27 for discharging water vapor from the space inside the shaft to the outside of the shaft. The water vapor supply hole 27 is a water vapor supply hole for supplying water vapor to the oil-impregnated sludge in the inner cylinder 5 from the screw shaft 2 side, that is, from the center of the inner cylinder 5 to the outside. is there.
該水蒸気供給孔 2 7の孔径は、 処理される含油スラッジ中の残渣物の 大きさにより、 適宜選択されるが、 通常、 5〜 1 2mm、 好ましくは 8 〜 1 2mm、 特に好ましくは 8〜 1 Ommである。 第 3図中、 該水蒸気 供給孔 2 7が形成される範囲 24は、 適宜選択されるが、 通常、 含油ス ラッジ供給側は、 該含油スラッジ供給側フランジ 8の近傍まであり、 ま た、 通常、 残渣物排出側は、 該内筒 5により囲まれている部分 2 3の長 さに対する該水蒸気供給孔 2 7が形成される範囲 24の長さの比 (符号 24 Z符号 2 3) 力 S、 0. 5〜0. 8 6 6、 好ましくは 0. 6 6〜0. 8 6 6、 特に好ましくは 0. 7 6〜0. 8 6 6となる位置までである。 該内筒 5により囲まれている部分 2 3の長さに対する該水蒸気供給孔 2 7が形成される範囲 24の長さの比 (符号 24/符号 2 3) 1S 上記範 囲を超えると、 残渣物中の水分量が多くなり易い。 該水蒸気供給孔 2 7 の数は、 含油スラッジの種類、 装置のスケール等により、 適宜選択され る。 The diameter of the water vapor supply hole 27 is appropriately selected depending on the size of the residue in the oil-containing sludge to be treated, but is usually 5 to 12 mm, preferably 8 to 12 mm, particularly preferably 8 to 1. Omm. In FIG. 3, the range 24 in which the water vapor supply hole 27 is formed is selected as appropriate, but normally, the oil-impregnated sludge supply side is close to the oil-impregnated sludge supply-side flange 8, and normally The residue discharge side is the ratio of the length of the range 24 in which the water vapor supply hole 2 7 is formed to the length of the portion 23 surrounded by the inner cylinder 5 (reference numeral 24 Z code 2 3) force S 0.5 to 0.8 6 6, preferably 0.6 6 to 0.8 6 6, particularly preferably 0.7 6 to 0.8 6 6. Ratio of the length of the range 24 in which the water vapor supply hole 27 is formed to the length of the portion 23 surrounded by the inner cylinder 5 (reference numeral 24 / reference numeral 23) 1S Beyond the range, the amount of water in the residue tends to increase. The number of water vapor supply holes 27 is appropriately selected depending on the type of oil-containing sludge, the scale of the apparatus, and the like.
該スクリユー羽根 3は、 該スクリユー軸 2の外周に螺旋状に形成され ており、 該スクリュー 4が回転することにより、 該内筒 5内の含油スラ ッジを、 含油スラッジ供給側から残渣物排出側へと移動させることがで きる形状であれば、 特に制限されない。  The screw blade 3 is formed in a spiral shape on the outer periphery of the screw shaft 2, and when the screw 4 rotates, the oil-containing sludge in the inner cylinder 5 is discharged from the oil-containing sludge supply side. The shape is not particularly limited as long as it can be moved to the side.
該スクリユー羽根 3の径 2 5は、 該内筒 5の内径と同じ長さであって もよく、 あるいは、 該内筒 5の内径より若干小さくてもよい。 該スタリ ユー羽根 3の径 2 5が、 該内筒 5の内径より小さい場合、 該スクリュー 羽根 3と該内筒 5との隙間は、 通常、 1 m m以下、 好ましくは 0 . 5 m m以下、 特に好ましくは 0 . 1 m m以下である。  The diameter 25 of the screw blade 3 may be the same length as the inner diameter of the inner cylinder 5 or may be slightly smaller than the inner diameter of the inner cylinder 5. When the diameter 25 of the stationary blade 3 is smaller than the inner diameter of the inner cylinder 5, the clearance between the screw blade 3 and the inner cylinder 5 is usually 1 mm or less, preferably 0.5 mm or less, especially Preferably it is 0.1 mm or less.
該スクリユー羽根 3の径 2 5に対する該スクリユー羽根 3のピッチ 2 6の比 (符号 2 6 /符号 2 5 ) は、 0 . 2 5 〜 1 · 2 5である。 そして、 含油スラッジの移動速度を遅く し易くなるので、 言い換えると、 該含油 スラッジの圧搾時間を長く し易くなるので、 含油スラッジ中の油分を減 量化する効果が高くなる点で、 該スクリユー羽根 3の径 2 5に対する該 スクリュ一羽根 3のピッチ 2 6の比 (符号 2 6 Z符号 2 5 ) は、 好まし くは 0 . 5 〜 1 . 2 5、 特に好ましくは 0 . 7 5〜: I、 更に好ましくは 0 . 9 〜 1である。 なお、 本発明において、 該スクリュー羽根 3のピッ チ 2 6とは、 第 3図中のスクリユー羽根の頂点 2 6 1 a と 2 6 1 b間の 距離、 すなわち、 該スクリュー羽根 3を側面視したときの、 隣り合う羽 根の頂点間の距離を指す。  The ratio of the pitch 26 of the screw blade 3 to the diameter 25 of the screw blade 3 (reference numeral 26 / reference numeral 25) is 0.25 to 1 · 25. In addition, since it becomes easy to slow down the moving speed of the oil-containing sludge, in other words, it is easy to lengthen the pressing time of the oil-containing sludge, so that the effect of reducing the oil content in the oil-containing sludge is increased. The ratio of the pitch 26 of the screw blade 3 to the diameter 25 of the screw (code 26 Z symbol 25) is preferably 0.5 to 1.25, particularly preferably 0.75 to: I More preferably, it is 0.9 to 1. In the present invention, the pitch 26 of the screw blade 3 is the distance between the apexes 26 1 a and 26 1 b of the screw blade in FIG. 3, that is, the screw blade 3 is viewed from the side. This is the distance between the apexes of adjacent feathers.
該スクリユー羽根 3のピッチ 2 6は、 該スクリユー羽根 3の全範囲に 亘つて同じであっても、 異なっていてもよい。  The pitch 26 of the screw blade 3 may be the same or different over the entire range of the screw blade 3.
なお、 本発明において、 該スクリュー 4の形状は、 第 1図及び第 3図 に示す形状に限定されるものではなく、 他に例えば、 残渣物排出側に向 かってスクリユー軸の径が大きくなっているものや、 残渣物排出側に向 かってピッチが小さくなっているもの等が挙げられる。 In the present invention, the shape of the screw 4 is as shown in FIGS. The shape is not limited to the shape shown in Fig. 1. Other examples include those with a larger screw shaft diameter toward the residue discharge side and those with a smaller pitch toward the residue discharge side. Can be mentioned.
該内筒 5は、 円筒形状である。 該内筒 5の含油スラッジ供給側の筒端 1 9は、 該含油スラッジ供給側フランジ 8に固定されており、 該筒端 1 9は該含油スラッジ供給側フランジ 8により塞がれている。 一方、 該内 筒 5の残渣物排出側の筒端 1 8は、 該残渣物排出側フランジ 9に固定さ れており、 該筒端 1 8の開口は、 該残渣物排出室 1 4に繋がっている。 つまり、 該筒端 1 8は、 残渣物が該内筒の外へ排出されるように、 開放 されている。  The inner cylinder 5 has a cylindrical shape. A cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder 5 is fixed to the oil-impregnated sludge supply-side flange 8, and the cylinder end 19 is closed by the oil-containing sludge supply-side flange 8. On the other hand, the cylinder end 18 on the residue discharge side of the inner cylinder 5 is fixed to the residue discharge side flange 9, and the opening of the cylinder end 18 is connected to the residue discharge chamber 14. ing. That is, the tube end 18 is opened so that the residue is discharged out of the inner tube.
該内筒 5の筒壁には、 含油スラッジを圧搾することにより、 該含油ス ラッジから分離する油水が、 該內筒 5から該油水排出隙間 2 2に排出さ れるように、 油水の通過孔 (図示しない。 ) が形成されている。  An oil water passage hole is formed on the cylindrical wall of the inner cylinder 5 so that the oil water separated from the oil containing sludge is discharged from the casing 5 to the oil water discharge gap 22 2 by squeezing the oil containing sludge. (Not shown) is formed.
該内筒 5の筒壁は、 該油水の通過孔が形成されているものであれば、 特に制限されず、 該内筒 5の筒壁としては、 例えば、 金網、 パンチング メタルのような孔が打ち抜かれた板材、 スクリーン用金網等が挙げられ る。  The cylindrical wall of the inner cylinder 5 is not particularly limited as long as the oil water passage hole is formed. Examples of the cylindrical wall of the inner cylinder 5 include holes such as a wire mesh and a punching metal. Punched plate material, screen wire mesh, etc. are listed.
該内筒 5の筒壁に形成される該油水の通過孔の径は、 処理される含油 スラッジ中の残渣物の大きさにより、 適宜選択されるが、 通常、 0 . 7 6〜: 1 . 9 6 m m、 好ましくは 1 . 4 0 〜 1 . 7 4 m m、 特に好ましく は 1 . 5 3 〜 1 . 6 3 m mである。 なお、該内筒 5の筒壁が金網の場合、 該油水の通過孔の径は、 該金網の目開きの長さを指し、 また、 該内筒 5 の筒壁がパンチングメタルの場合、 該油水の通過孔の径は、 打ち抜かれ た孔の径を指す。  The diameter of the oil water passage hole formed in the cylindrical wall of the inner cylinder 5 is appropriately selected depending on the size of the residue in the oil-containing sludge to be treated, but usually 0.76 to: 1. It is 96 mm, preferably 1.40 to 1.74 mm, particularly preferably 1.53 to 1.63 mm. When the cylinder wall of the inner cylinder 5 is a wire mesh, the diameter of the oil water passage hole indicates the opening length of the wire mesh, and when the cylinder wall of the inner cylinder 5 is a punching metal, The diameter of the oil / water passage hole is the diameter of the punched hole.
該内筒 5カ、該スクリュー 4を囲むようにして設置されることにより、 該内筒 5の内壁及ぴ該スクリユー羽根 4との間に、 含油スラッジを圧搾 するための圧搾空間 1 7が形成される。 Oil-containing sludge is squeezed between the inner wall of the inner cylinder 5 and the screw blade 4 by being installed so as to surround the inner cylinder 5 and the screw 4. A squeezing space 17 is formed.
該外筒 6は、 円筒形状である。 該外筒 6の含油スラッジ供給側の筒端 2 0は、 該含油スラッジ供給側フランジ 8に固定されており、 該筒端 2 0は該含油スラッジ供給側フランジ 8により塞がれている。 一方、 該外 筒 6の残渣物排出側の筒端 2 1は、 該残渣物排出側フランジ 9に固定さ れており、 該油水の排出隙間 2 2と該残渣物排出室 1 4とは、 該残渣物 排出側フランジ 9により隔離されている。 つまり、 該油水の排出隙間 2 2に排出された油水が、 該残渣物排出室 1 4に流れ込まないように、 該 油水の排出隙間 2 2は、該残渣物排出側フランジ 9により塞がれている。 該内筒 5と該外筒 6とにより形成される該油水の排出隙間 2 2の幅、 言い換えると、 該内筒 5の外側と該外筒 6の内側との距離は、 含油スラ ッジを圧搾することにより、 該含油スラッジから分離する油分、 有害物 質及び水分並びに供給した水蒸気が液化した水分、 すなわち、 該油水が 排出されて、 該油水排出口 1 3へ流動できる程度であれば、 特に制限さ れない。  The outer cylinder 6 has a cylindrical shape. A cylinder end 20 on the oil-impregnated sludge supply side of the outer cylinder 6 is fixed to the oil-impregnated sludge supply-side flange 8, and the cylinder end 20 is closed by the oil-containing sludge supply-side flange 8. On the other hand, the cylinder end 21 on the residue discharge side of the outer cylinder 6 is fixed to the residue discharge flange 9, and the oil water discharge gap 22 and the residue discharge chamber 14 are It is isolated by the residue discharge flange 9. That is, the oil water discharge gap 22 is blocked by the residue discharge side flange 9 so that the oil water discharged into the oil water discharge gap 22 does not flow into the residue discharge chamber 14. Yes. The width of the oil water discharge gap 22 formed by the inner cylinder 5 and the outer cylinder 6, in other words, the distance between the outer side of the inner cylinder 5 and the inner side of the outer cylinder 6 is determined by the oil-containing sludge. If the oil, toxic substances and moisture separated from the oil-containing sludge by squeezing, and the water that the supplied water vapor has liquefied, that is, the oil water is discharged and can flow to the oil water discharge port 13, There are no particular restrictions.
なお、 第 1図及ぴ第 2図では、 該外筒 6の形状が、 含油スラッジの移 動方向に対して垂直な面で切ったときの断面形状が円形であるものを示 しているが、 該外筒 6の形状は、 これに限定されるものではなく、 内側 に該内筒 5を設置でき且つ油水が排出されて、 該油水排出口 1 3へ流動 するための油水の排出隙間を形成できるものであればよい。 他に、 該外 筒の形状としては、 例えば、 上側が平坦で下側に丸み帯びた力マボコ状 のものが挙げられる。 また、 該外筒 6の底部の筒壁は、 該油水排出口 1 3に向かって傾斜していてもよい。  FIGS. 1 and 2 show that the outer cylinder 6 has a circular cross-sectional shape when cut along a plane perpendicular to the moving direction of the oil-containing sludge. The shape of the outer cylinder 6 is not limited to this, but the inner cylinder 5 can be installed on the inner side, and the oil water discharge gap for allowing the oil water to be discharged and flow to the oil water discharge port 13 is provided. Any material that can be formed may be used. In addition, as the shape of the outer cylinder, for example, a force-pillar shape in which the upper side is flat and the lower side is rounded. Further, the cylindrical wall at the bottom of the outer cylinder 6 may be inclined toward the oil / water discharge port 13.
該ストッパー 7は、 該スクリュー軸 2に固定されており、 該内筒 5の 残渣物排出側の筒端 1 8の近傍に設置されている。 該ストッパー 7は、 残渣物が、 該筒端 1 8から該残渣物排出室 1 4へ排出される際に、 該残 渣物の排出量を調節することにより、 含油スラッジの圧縮率を調節する 機能を果たす。 具体的には、 該ス トッパー 7の設置位置を調節すること により、 該ストッパー 7と該筒端 1 8との間に形成される残渣物の排出 隙間 1 5の大きさを調節して、 該残渣物の排出量を調節することができ る。 そして、 該含油スラッジの供給量に対する該残渣物の排出量の比を 調節することにより、該含油スラッジの圧縮率を調節することができる。 なお、 該ス トッパー 7の設置位置、 あるいは、 該ス トッパー 7と該筒端 1 8により形成される該残渣物の排出隙間 1 5は、含油スラッジの種類、 含油スラッジの含油量、 処理条件等により適宜選択される。 The stopper 7 is fixed to the screw shaft 2 and is installed in the vicinity of the cylinder end 18 on the residue discharge side of the inner cylinder 5. When the stopper 7 is discharged from the cylinder end 18 to the residue discharge chamber 14, the stopper 7 It functions to adjust the compressibility of oil-containing sludge by adjusting the amount of residue discharged. Specifically, by adjusting the installation position of the stopper 7, the size of the residue discharge gap 15 formed between the stopper 7 and the tube end 18 is adjusted, and the Residue discharge can be adjusted. Then, the compression ratio of the oil-containing sludge can be adjusted by adjusting the ratio of the discharge amount of the residue to the supply amount of the oil-containing sludge. The installation position of the stopper 7 or the discharge gap 15 of the residue formed by the stopper 7 and the cylinder end 18 is the type of oil-containing sludge, the oil content of the oil-containing sludge, processing conditions, etc. Is appropriately selected.
また、 該ス トッパーとしては、 第 1図に示すもの以外に、 例えば、 該 スクリユー軸が揷通され、 ベアリング等を介して該スクリユー軸に摺動 可能に取り付けられ、 且つ、 背面に弾性体、 油圧、 空気圧等により圧力 をかける調圧部材が取り付けられているストッパーが挙げられる。なお、 該ス トッパーの背面とは、 該内筒との間で該排出隙間を形成する側とは 反対側のことである。 この調圧部材が取り付けられているス トッパーを 有する形態例では、 該調圧部材で圧力調節することにより、 被処理物の 種類や物性等に応じて、 排出隙間の大きさや圧搾の圧力の調節ができる ので、 残渣物の排出量、 圧縮率等の処理条件の選択が容易になる。  In addition to the stopper shown in FIG. 1, for example, the screw shaft is passed through, and is slidably attached to the screw shaft via a bearing or the like. Examples include a stopper to which a pressure adjusting member that applies pressure by hydraulic pressure, air pressure, or the like is attached. The back surface of the stopper is the side opposite to the side that forms the discharge gap with the inner cylinder. In the embodiment having the stopper to which the pressure adjusting member is attached, by adjusting the pressure with the pressure adjusting member, the size of the discharge gap and the pressure of the squeezing are adjusted according to the type and physical properties of the object to be processed. This makes it easy to select treatment conditions such as the amount of residue discharged and the compression rate.
該含油スラッジ供給口 1 0は、 該内筒 5内へ含油スラッジを供給する ための供給口である。 含油スラッジの移動方向 3 4における、 該含油ス ラッジ供給口 1 0の設置位置は、 第 4図に示すように、 該内筒 5の長さ 3 1に対する該内筒 5の含油スラッジ供給側の筒端 1 9から該含油スラ ッジ供給口 1 0までの長さ 3 3の比 (符号 3 3 Z符号 3 1 ) 、 0 . 1 5以下、 好ましくは 0 . 1 2 5以下、 特に好ましくは 0 . 0 9 3 〜 0 . 1 2 5となる位置である。 該内筒 5の長さ 3 1に対する該内筒 5の含油 スラッジ供給側の筒端 1 0から該含油スラッジ供給口 1 0までの長さ 3 3の比が上記範囲内にあることにより、 含油スラッジの油分の減量化効 果が高くなる。 なお、 本発明において、 該内筒 5の長さ 3 1とは、 該内 筒の含油スラッジ供給側の筒端 1 9から該内筒の残渣物排出側の筒端 1 8までの距離を指し、 また、 該含油スラッジ供給口 1 0の位置とは、 該 含油スラッジ供給口 1 0の中央の位置を指す。 また、 該内筒 5及ぴ該外 筒 6の周方向における、該含油スラッジ供給口 1 0の設置位置は、通常、 第 1図及ぴ第 4図に示すように、 最上方であるが、 これに制限されるも のではなく、 図示しない含油スラッジ供給管の位置等により適宜選択さ れる。 The oil-containing sludge supply port 10 is a supply port for supplying oil-containing sludge into the inner cylinder 5. As shown in FIG. 4, the installation position of the oil-impregnated sludge supply port 10 in the oil-impregnated sludge moving direction 34 is on the oil-impregnated sludge supply side of the inner cylinder 5 with respect to the length 31 of the inner cylinder 5. The ratio of the length 33 from the cylinder end 19 to the oil-impregnated sludge supply port 10 (reference numeral 3 3 Z sign 3 1), 0.15 or less, preferably 0.125 or less, particularly preferably It is a position where 0 .09 3 to 0. Length 3 from the cylinder end 10 on the oil-impregnated sludge supply side of the inner cylinder 5 to the length 31 of the inner cylinder 5 to the oil-containing sludge supply port 10 When the ratio of 3 is within the above range, the oil content of the oil-containing sludge is reduced. In the present invention, the length 31 of the inner cylinder 5 refers to the distance from the cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder to the cylinder end 18 on the residue discharge side of the inner cylinder. Further, the position of the oil-containing sludge supply port 10 refers to the center position of the oil-containing sludge supply port 10. Further, the installation position of the oil-impregnated sludge supply port 10 in the circumferential direction of the inner cylinder 5 and the outer cylinder 6 is usually the uppermost position as shown in FIGS. 1 and 4, It is not limited to this, and is appropriately selected depending on the position of an oil-containing sludge supply pipe (not shown).
該外筒側水蒸気供給口 1 1は、 該内筒 5内の含油スラッジに対して該 内筒 5側から、 すなわち、 該内筒 5の外から中心に向けて水蒸気を供給 するための水蒸気の供給口である。該含油スラッジの移動方向における、 該外筒側水蒸気供給口 1 1の設置位置は、 第 4図に示すように、 該内筒 5の長さ 3 1に対する該内筒 5の含油スラッジ供給側の筒端 1 9から該 外筒側水蒸気供給口 1 1までの長さ 3 2の比(符号 3 2 /符号 3 1 )が、 〇· 5以下、 好ましくは◦. 0 3〜0 . 5、 特に好ましくは 0 . 1 4〜 0 . 3、 更に好ましくは 0 . 1 8〜0 . 2 5となる位置である。 該内筒 5の長さ 3 1に対する該内筒 5の含油スラッジ供給側の筒端 1 9から該 外筒側水蒸気供給口 1 1までの長さ 3 2の比が、 上記範囲内にあること により、 該内筒 5内で該含油スラッジが圧搾される際の初期の段階で、 多くの水蒸気を該含油スラッジに接触させることができるので、 含油ス ラッジの油分の減量化効果が高くなる。 なお、 本発明において、 該外筒 側水蒸気供給口 1 1の位置とは、 該外筒側水蒸気供給口 1 1の中央の位 置を指す。  The outer cylinder-side water vapor supply port 11 supplies water vapor to supply oil vapor from the inner cylinder 5 side to the oil-impregnated sludge in the inner cylinder 5, that is, from the outside of the inner cylinder 5 toward the center. Supply port. As shown in FIG. 4, the installation position of the outer cylinder-side water vapor supply port 11 in the moving direction of the oil-impregnated sludge is as follows. The ratio of the length 3 2 (symbol 3 2 / symbol 3 1) from the cylinder end 19 to the outer cylinder side steam supply port 11 is not more than 0 · 5, preferably ◦0.3 to 0.5, especially The position is preferably 0.14 to 0.3, and more preferably 0.18 to 0.25. The ratio of the length 3 2 from the cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder 5 to the length 31 of the inner cylinder 5 to the outer cylinder side water vapor supply port 11 is within the above range. Thus, since a large amount of water vapor can be brought into contact with the oil-containing sludge at the initial stage when the oil-containing sludge is compressed in the inner cylinder 5, the effect of reducing the oil content of the oil-containing sludge is enhanced. In the present invention, the position of the outer cylinder side water vapor supply port 11 refers to the center position of the outer cylinder side water vapor supply port 11.
また、 該外筒 6の周方向における、 該外筒側水蒸気供給口 1 1の設置 位置は、 第 1図及び第 4図では、 最下方であるが、 これに制限されるも のではなく、 図示しない水蒸気供給管の位置等により適宜選択される。 また、 該外筒側水蒸気供給口 1 1の数は、 特に制限されず、 1であって も、 2以上であってもよレヽ。 Further, the installation position of the outer cylinder side water vapor supply port 11 in the circumferential direction of the outer cylinder 6 is the lowest position in FIGS. 1 and 4, but is limited to this. Instead, it is appropriately selected depending on the position of a water vapor supply pipe (not shown). Further, the number of the outer cylinder side water vapor supply ports 11 is not particularly limited, and may be 1 or 2 or more.
該油水排出口 1 3は、 該油水の排出隙間 2 2に排出される油水を、 装 置外へ排出するための排出口である。含油スラッジの移動方向における、 該油水排出口 1 3の設置位置及び該油水排出口 1 3の設置数は、 特に制 限されず、 適宜選択される。 また、 該外筒 6の周方向における、 該油水 排出口 1 3の設置位置は、 通常、 最下方である。  The oil water discharge port 13 is a discharge port for discharging the oil water discharged to the oil water discharge gap 22 to the outside of the apparatus. The installation position of the oil / water discharge ports 13 and the number of the oil / water discharge ports 13 in the moving direction of the oil-containing sludge are not particularly limited and are appropriately selected. Further, the installation position of the oil / water discharge port 13 in the circumferential direction of the outer cylinder 6 is usually at the lowest position.
該排気口 1 6は、 装置内の水蒸気等のガスを装置外に排出するための ガスの排出口である。 含油スラッジの移動方向における、 該排気口 1 6 の設置位置及び該排気口 1 6の設置数は、 特に制限されず、 適宜選択さ れる。  The exhaust port 16 is a gas discharge port for discharging a gas such as water vapor in the apparatus to the outside of the apparatus. The installation position of the exhaust port 16 and the number of the exhaust ports 16 in the moving direction of the oil-containing sludge are not particularly limited and are appropriately selected.
該含油スラッジ供給口 1 0、 該残渣物排出口 1 2、 該油水排出口 1 3 及び該排気口 1 6は、 通常、 開放状態である。 また、 該油水排出口 1 3 には、 該油水に混入した細かい残渣物を分離するためのス ト レーナ一が 設置されていてもよい。  The oil-containing sludge supply port 10, the residue discharge port 12, the oil / water discharge port 13, and the exhaust port 16 are normally open. Further, a strainer for separating fine residues mixed in the oil water may be installed at the oil water discharge port 13.
該含油スラッジの減量化装置 1には、 該スクリユー 4を回転駆動させ るための駆動手段 (図示しない。 ) が設置されている。  The oil-impregnated sludge reducing device 1 is provided with driving means (not shown) for rotating the screw 4.
該含油スラッジの減量化装置 1においては、 該スクリユー軸 2及ぴ該 内筒 5は水平であってもよく、 含油スラッジの供給側に傾斜していても よく、 残渣物の排出側に傾斜していてもよく、 あるいは、 垂直であって もよい。  In the oil-impregnated sludge reduction device 1, the screw shaft 2 and the inner cylinder 5 may be horizontal, may be inclined to the oil-containing sludge supply side, and may be inclined to the residue discharge side. Or it may be vertical.
次に、 本発明の含油スラッジの減量化装置の運転方法について、 第 5 図を参照して説明する。 第 5図は、 該含油スラッジの減量化装置 1を用 いて含油スラッジを処理している様子を示す、 該含油スラッジの減量化 装置 1の模式的な断面図である。 該含油スラッジの減量化装置 1では、該含油スラッジ供給口 1 0から、 含油スラッジ 4 1を供給して、該スクリユー 4を回転させることにより、 該含油スラッジ 4 1を、 該含油スラッジ供給口 1 0から、 該内筒の残渣 物排出側の筒端 1 8に向かって、 該スクリュー軸 2の周りに螺旋状に形 成される該圧搾空間 1 7を移動させて、 該含油スラッジ 4 1を該筒端 1 8に向かって押し込むことにより、該含油スラッジ 4 1に高圧を与えて、 該含油スラッジ 4 1を圧搾する。 この圧搾の際、 該スクリュー 4を回転 させながら、 該スクリユー軸 2の一端 2 8から水蒸気 4 0 aを、 該外筒 側水蒸気供給口 1 1から水蒸気 4 0 bを供給することにより、 該含油ス ラッジ 4 1に対し水蒸気を、 該内筒 5の中心から及び外側からの両方向 から接触させる。 Next, the operation method of the oil-impregnated sludge reduction device of the present invention will be described with reference to FIG. FIG. 5 is a schematic cross-sectional view of the oil-retaining sludge reduction device 1 showing a state in which the oil-containing sludge reduction device 1 is used to process the oil-containing sludge. In the oil impregnated sludge reducing device 1, the oil impregnated sludge 41 is supplied to the oil impregnated sludge supply port 1 by supplying the oil impregnated sludge 41 from the oil impregnated sludge supply port 10 and rotating the screw 4. From 0, the compressed space 17 formed in a spiral around the screw shaft 2 is moved toward the cylinder end 18 on the residue discharge side of the inner cylinder, and the oil-containing sludge 41 is By pushing toward the cylinder end 18, high pressure is applied to the oil-containing sludge 41, and the oil-containing sludge 41 is squeezed. During this compression, while the screw 4 is rotated, steam 40 0 a is supplied from one end 28 of the screw shaft 2, and steam 40 b is supplied from the outer cylinder side steam supply port 11 1, thereby Steam is brought into contact with the sludge 41 from both the center of the inner cylinder 5 and the outside.
そして、 該スクリュー 4を回転させながら、 該水蒸気 4 0 a及ぴ 4 0 bを供給しながら、 該含油スラッジ 4 1を連続的に供給しつつ、 該残渣 物 4 3を排出させることにより、 連続的に、 該含油スラッジ 4 1の油分 の減量化を行うことができる。 その際、 適宜、 油水 4 2を該油水排出口 1 3から排出し、 排気ガス 4 5を該排気口 1 6から排出する。  And while rotating the screw 4, supplying the steam 40 a and 40 b, continuously supplying the oil-containing sludge 41, and discharging the residue 43, continuously. In particular, the oil content of the oil-containing sludge 41 can be reduced. At that time, the oil water 4 2 is discharged from the oil water discharge port 13 and the exhaust gas 45 is discharged from the exhaust port 16 as appropriate.
該含油スラッジの減量化装置 1では、 この圧搾の際に該含油スラッジ 4 1が水蒸気 4 0と接触することより、 該含油スラッジは高温となり且 つ水分量が増えるので、 該含油スラッジ 4 1中の固形分と液体分とが分 離し易くなる。 そのため、 該含油スラッジの減量化装置 1は、 該含油ス ラッジ 4 1中の油分を減量化する効果を高くすることができるので、 残 渣物 4 3中の油分の含有量を少なくすることができる。  In the oil-impregnated sludge reducing device 1, the oil-impregnated sludge 4 1 comes into contact with the water vapor 40 at the time of pressing, so that the oil-impregnated sludge becomes high temperature and the water content increases. This makes it easier to separate the solid and liquid components. Therefore, the oil-retaining sludge reducing device 1 can increase the effect of reducing the oil content in the oil-containing sludge 41, so that the oil content in the residue 43 can be reduced. it can.
該圧搾の際、 該含油スラッジは、 該含油スラッジの減量化装置 1内に 供給される水蒸気により加熱されるが、 供給される該水蒸気の温度は、 1 0 0 〜 2 0 0 °C、 好ましくは 1 0 0 〜 1 8 0 °C、 特に好ましくは 1 1 0 〜 1 5 0 °C、 更に好ましくは 1 1 0 〜 1 2 0 °Cである。 供給される該 水蒸気の温度が上記範囲内にあることにより、 該含油スラッジ 4 1中の 油分を減量化する効果が高くなる。 また、 該圧搾の際の該含油スラッジ の減量化装置 1内の温度は、 定常状態の温度で、 1 0 0〜 2 0 0 °C、 好 ましくは1 0 0〜 1 8 0 、 特に好ましくは 1 1 0〜 1 5 0 °C、 更に好 ましくは 1 1 0〜 1 2 0 °Cである。 該圧搾の際の該含油スラッジの減量 化装置 1内の温度が上記範囲内にあることにより、 該含油スラッジ 4 1 中の油分を減量化する効果が高くなる。 なお、 該圧搾の際の該含油スラ ッジの減量化装置 1内の温度は、 該油水の排出隙間 2 2のうち、 供給さ れる水蒸気に直接接触しない位置に熱電対等を設置して、 該油水の排出 隙間 2 2の温度を測定して得られる。 During the pressing, the oil-containing sludge is heated by water vapor supplied into the oil-containing sludge reduction device 1, and the temperature of the water vapor supplied is preferably from 100 to 200 ° C., preferably Is from 100 to 180 ° C, particularly preferably from 110 to 150 ° C, and more preferably from 110 to 120 ° C. The supplied When the temperature of the water vapor is within the above range, the effect of reducing the oil content in the oil-containing sludge 41 is enhanced. Further, the temperature in the oil-reducing sludge reducing device 1 during the pressing is a steady-state temperature of 100 to 200 ° C., preferably 100 to 180, particularly preferably. Is 1 1 0 to 1 5 0 ° C, more preferably 1 1 0 to 1 2 0 ° C. When the temperature in the oil-containing sludge reducing device 1 during the pressing is within the above range, the effect of reducing the oil content in the oil-containing sludge 4 1 is enhanced. Note that the temperature in the oil-retaining sludge reducing device 1 during the pressing is such that a thermocouple or the like is installed in the oil water discharge gap 22 at a position that does not directly contact the supplied steam. Obtained by measuring the temperature of oil drain gap 2 2.
該圧搾の際、 該含油スラッジを圧搾する圧搾圧力は、 含油スラッジの 種類により適宜選択される。  In the pressing, the pressing pressure for pressing the oil-containing sludge is appropriately selected according to the type of oil-containing sludge.
該圧搾の際の該含油スラッジ 4 1の圧搾時間、 すなわち、 該含油スラ ッジ 4 1が該含油スラッジ供給口 1 0から供給されて、 該残渣物の排出 隙間 1 5から該残渣物 4 3として排出されるまでの時間は、 1〜3時間、 好ましくは 1 . 5〜 3時間、 特に好ましくは 2〜 2 . 5時間である。 該 圧搾の際の該含油スラッジ 4 1の圧搾時間が上記範囲内にあることによ り、 該含油スラッジ 4 1中の油分を減量化する効果が高くなる。 なお、 該含油スラッジの減量化装置 1では、 該スクリュー 4の回転速度、 該含 油スラッジ供給口 1 0からの該含油スラッジ 4 1の供給量、 及び該残渣 物の排出隙間 1 5からの該残渣物 4 3の排出量を、 適宜選択することに より、 該圧搾の際の該含油スラッジ 4 1の圧搾時間を調節することがで きる。 なお、 該含油スラッジの減量化装置 1では、 該残渣物の排出隙間 1 5の大きさを調節することにより、 該残渣物の排出隙間 1 5からの該 残渣物 4 3の排出量を調節することができる。  The pressing time of the oil-containing sludge 41 during the pressing, that is, the oil-containing sludge 41 is supplied from the oil-containing sludge supply port 10, and the residue 4 3 is discharged from the residue discharge gap 15. The time until it is discharged as 1 to 3 hours, preferably 1.5 to 3 hours, particularly preferably 2 to 2.5 hours. When the pressing time of the oil-containing sludge 41 during the pressing is within the above range, the effect of reducing the oil content in the oil-containing sludge 41 is enhanced. In the oil impregnated sludge reducing device 1, the rotational speed of the screw 4, the supply amount of the oil impregnated sludge 41 from the oil impregnated sludge supply port 10, and the residue from the discharge gap 15 of the residue By appropriately selecting the discharge amount of the residue 43, the squeezing time of the oil-containing sludge 41 during the squeezing can be adjusted. In the oil-impregnated sludge reduction device 1, the amount of the residue 4 3 discharged from the residue discharge gap 15 is adjusted by adjusting the size of the residue discharge gap 15. be able to.
本発明の含油スラッジの減量化装置は、 該内筒の長さに対する該内筒 の含油スラッジ供給側の筒端から該外筒側水蒸気供給口までの長さの比 力 0 . 5以下であることにより、 該含油スラッジの圧搾工程の初期の 段階で、 すなわち、 該含油スラッジ供給口に近い方で、 該含油スラッジ に水蒸気を接触させることができるので、 該含油スラッジの油分及び有 害物質の減量化効果が高くなり、 油分及び有害物質の含有量が少ない残 渣物が得られる。 The oil-impregnated sludge reduction device of the present invention comprises the inner cylinder relative to the length of the inner cylinder. The ratio of the length from the cylinder end on the oil-impregnated sludge supply side to the steam supply port on the outer cylinder side is 0.5 or less, so that at the initial stage of the oil-containing sludge pressing step, that is, the oil-containing sludge supply Since water vapor can be brought into contact with the oil-containing sludge closer to the mouth, the oil-containing sludge's oil content and harmful substances are reduced more effectively, and a residue with a low content of oil and harmful substances is obtained. It is done.
また、 本発明の含油スラッジの減量化装置は、 更に、 該スクリュー羽 根の径に対する該スクリユー羽根のピッチの比を大きくすること、 つま り、 該スク リュー羽根のピッチを比較的大きくすることにより、 含油ス ラッジの圧搾時間及び加熱時間を長く して、 ゆっく り と該含油スラッジ を圧搾するのに適した構造となる。 そして、 該含油スラッジの圧搾時間 及ぴ加熱時間を長くすることにより、 該含油スラッジの油分及び有害物 質の減量化効果が更に高まる。 符号の説明  The oil-impregnated sludge reduction device of the present invention further increases the ratio of the pitch of the screw blade to the diameter of the screw blade, that is, by relatively increasing the pitch of the screw blade. The oil-containing sludge is compressed and heated for a long time so that the oil-containing sludge is slowly compressed. Further, by increasing the pressing time and heating time of the oil-containing sludge, the effect of reducing the oil content and harmful substances of the oil-containing sludge is further enhanced. Explanation of symbols
1 含油スラッジの減量化装置  1 Oil-retaining sludge reduction device
スク リユー軸  Screw shaft
スク リユー羽根  Screw feather
スク リュー  Screw
内筒  Inner cylinder
外筒  Outer cylinder
ス トッノ 一  Stock
含油スラッジ供給側フランジ  Oil-impregnated sludge supply side flange
残渣物排出側フランジ  Residue discharge flange
含油スラッジ供給口  Oil-impregnated sludge supply port
外筒側水蒸気供給口 1 2 残渣物排出口 Outer cylinder side steam supply port 1 2 Residue outlet
1 3 油水排出口  1 3 Oil / water outlet
1 4 残渣物排出室  1 4 Waste discharge chamber
1 5 残渣物の排出隙間  1 5 Residue discharge gap
1 6 排気口  1 6 Exhaust port
1 7 圧搾空間  1 7 Compressed space
1 8 内筒の残渣物排出側の筒端  1 8 Tube end on the waste discharge side of the inner tube
1 9 內筒の含油スラッジ供給側の筒端  1 9 Tube end on the oil-impregnated sludge supply side
2 0 外筒の含油スラッジ供給側の筒端  2 0 Outer cylinder end of oil-impregnated sludge supply side
2 1 外筒の残渣物排出側の筒端  2 1 Tube end on the waste discharge side of the outer tube
2 2 油水の排出隙間  2 2 Oil water discharge gap
2 3 内筒 5により囲まれている部分  2 3 Part surrounded by inner cylinder 5
2 4 水蒸気供給孔 2 7が形成される範囲  2 4 Range where water vapor supply holes 2 7 are formed
2 5 スクリユー羽根 3の径  2 5 Diameter of screw blade 3
2 6 スクリユー羽根 3のピッチ  2 6 Skew feather 3 pitch
2 7 水蒸気供給孔  2 7 Water vapor supply hole
2 8 スクリユー軸 2の一端  2 8 One end of screw shaft 2
2 9 スクリユー軸 2の他端  2 9 The other end of screw shaft 2
3 1 内筒 5の長さ  3 1 Length of inner cylinder 5
3 2 内筒 5の含油スラッジ供給側の筒端 1 9から外筒側水蒸 気供給口 1 1までの長さ  3 2 Length from the cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder 5 to the steam supply port 1 1 on the outer cylinder side
3 3 内筒 5の含油スラッジ供給側の筒端 1 9から含油スラッ ジ供給口 1 0までの長さ  3 3 Length from the cylinder end 19 on the oil-impregnated sludge supply side of the inner cylinder 5 to the oil-impregnated sludge supply port 10
3 4 含油スラッジの移動方向  3 4 Movement direction of oil-impregnated sludge
4 0 a 、 4 0 b 水蒸気  4 0 a, 4 0 b Water vapor
4 1 含油スラッジ 4 2 油水 4 1 Oil-impregnated sludge 4 2 Oil and water
4 3 残渣物  4 3 Residue
4 5 排気ガス 4 5 Exhaust gas
2 6 1 a、 2 6 1 b スクリユー羽根の頂点  2 6 1 a, 2 6 1 b
産業上の利用可能性 Industrial applicability
本発明によれば、 含油スラッジの減量化を容易に行うことができる。  According to the present invention, it is possible to easily reduce the amount of oil-containing sludge.

Claims

請求の範囲 The scope of the claims
1 . 水蒸気の供給孔を有するスク リュー軸、 及び該スク リ ュー軸の少な く とも一部の外周に螺旋状に設けられるスクリユー羽根からなるスクリ ユーと、 1. a screw shaft having a steam supply hole, and a screw comprising a screw blade spirally provided on the outer periphery of at least a part of the screw shaft;
油水の通過孔を有し、 該スク リューを囲む内筒と、  An inner cylinder having an oil-water passage hole and surrounding the screw;
該内筒の外側に設置され、 該内筒との間に油水の排出隙間を形成する 外筒と、  An outer cylinder that is installed outside the inner cylinder and forms an oil-water discharge gap with the inner cylinder;
該内筒内に、 含油スラッジを供給するための含油スラッジ供給口と、 該外筒内に水蒸気を供給するための外筒側水蒸気供給口と、 該内筒の残渣物排出側の筒端近傍に設置され、 該内筒の残渣物排出側 の筒端との間に残渣物の排出隙間を形成するストッパーと、  An oil-impregnated sludge supply port for supplying oil-containing sludge into the inner cylinder, an outer cylinder-side steam supply port for supplying water vapor into the outer cylinder, and a vicinity of the cylinder end on the residue discharge side of the inner cylinder A stopper that forms a residue discharge gap between the inner cylinder and the cylinder end on the residue discharge side of the inner cylinder;
該油水の排出隙間に排出された油水を、 装置外に排出するための油水 排出口と、  An oil water discharge port for discharging the oil water discharged into the oil water discharge gap to the outside of the device;
該スク リ ューを回転駆動させる駆動手段と、  Driving means for rotationally driving the screw;
を有し、 Have
該内筒の長さに対する該内筒の含油スラッジ供給側の筒端から該外筒 側水蒸気供給口までの長さの比が、 0 . 5以下であること、  The ratio of the length of the inner cylinder from the cylinder end on the oil-impregnated sludge supply side to the outer cylinder-side water vapor supply port with respect to the length of the inner cylinder is 0.5 or less,
を特徴とする含油スラッジの減量化装置。 A device for reducing oil content sludge.
2 . 前記スク リュー羽根の径に対する前記スク リ ュー羽根のピッチの比 力 0 . 5〜 1 . 2 5であることを特徴とする請求項 1記載の含油スラ ッジの減量化装置。 2. The oil-impregnated sludge reduction device according to claim 1, wherein a specific force of the pitch of the screw blades to the diameter of the screw blades is 0.5 to 1.25.
3 . 前記ス トッパーが、 前記スク リュー軸が挿通され、 前記スク リ ュー 軸に摺動可能に取り付けられ、 且つ、 背面に調圧部材が取り付けられて いるストッパーであることを特徴とする請求項 1記載の含油スラッジの 減量化装置。  3. The stopper is a stopper in which the screw shaft is inserted, is slidably attached to the screw shaft, and a pressure adjusting member is attached to the back surface. The oil-retaining sludge reduction device according to 1.
PCT/JP2008/065225 2007-08-24 2008-08-20 Oil sludge weight reducing apparatus WO2009028519A1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104623966A (en) * 2015-01-08 2015-05-20 天津鼎天斯凯特机械有限公司 Used engine oil recycling equipment
WO2015149519A1 (en) * 2014-04-03 2015-10-08 西安交通大学 Radial-flow-type hydrothermal reactor for sludge pyrohydrolysis treatment
CN105150580A (en) * 2015-09-01 2015-12-16 太仓市伦凯自动化设备有限公司 Oil expeller

Citations (3)

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Publication number Priority date Publication date Assignee Title
JPS5893788A (en) * 1981-11-30 1983-06-03 Toho Kogyo Kk Disposal of oil-containing sludge
JPS61289996A (en) * 1985-06-14 1986-12-19 Nikko Sogyo Kk Treatment device for dehydrating and drying sludge or the like
JP2000015015A (en) * 1998-07-07 2000-01-18 Teera Bunri:Kk Shaft heating type multi-plate screw press filter

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Publication number Priority date Publication date Assignee Title
JPH05317900A (en) * 1992-05-14 1993-12-03 Hirofumi Yamada Continuous recovery method for fine silica sand or the like contained in slurry and device therefor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5893788A (en) * 1981-11-30 1983-06-03 Toho Kogyo Kk Disposal of oil-containing sludge
JPS61289996A (en) * 1985-06-14 1986-12-19 Nikko Sogyo Kk Treatment device for dehydrating and drying sludge or the like
JP2000015015A (en) * 1998-07-07 2000-01-18 Teera Bunri:Kk Shaft heating type multi-plate screw press filter

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015149519A1 (en) * 2014-04-03 2015-10-08 西安交通大学 Radial-flow-type hydrothermal reactor for sludge pyrohydrolysis treatment
US9994473B2 (en) 2014-04-03 2018-06-12 Xi'an Jiaotong University Radial flow hydrothermal reactor for sludge thermal hydrolysis treatment
CN104623966A (en) * 2015-01-08 2015-05-20 天津鼎天斯凯特机械有限公司 Used engine oil recycling equipment
CN105150580A (en) * 2015-09-01 2015-12-16 太仓市伦凯自动化设备有限公司 Oil expeller

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