CN106238444B - The system of industrial treatment mud dregs - Google Patents
The system of industrial treatment mud dregs Download PDFInfo
- Publication number
- CN106238444B CN106238444B CN201610879350.9A CN201610879350A CN106238444B CN 106238444 B CN106238444 B CN 106238444B CN 201610879350 A CN201610879350 A CN 201610879350A CN 106238444 B CN106238444 B CN 106238444B
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- China
- Prior art keywords
- mud
- sand
- silt particle
- separator
- fine
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B7/00—Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
- B03B9/061—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
- B03B9/063—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial the refuse being concrete slurry
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
- B03B9/061—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
- B03B9/065—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial the refuse being building rubble
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/13—Compounding ingredients
- C04B33/132—Waste materials; Refuse; Residues
- C04B33/1321—Waste slurries, e.g. harbour sludge, industrial muds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
Abstract
A kind of system of industrial treatment mud dregs, be primarily suitable for for process excavated in urban construction silt particle soil, including:One drum-type silt particle separator, row preliminary treatment during by processed silt particle;Silt particle separator, separates the coarse sand in mud and carefully;Mud conditioning part, is dehydrated that to obtain dry mud standby after the further fine processing of mud after desanding.Processed silt particle is processed into sposh sand and aniseed mixture by the present invention as a result of drum-type silt particle separator, so, from building site with soil car draw come useless soil directly can pour into separator, be quickly processed into sposh sand and aniseed mixture, do not result in accumulation;In addition, processed soil out, the difference according to soil composition can be made fictile or ceramic products, be truly realized all wastes and be fully utilized, and realizing turns waste into wealth, and is a project for green exhausted sustainable development.
Description
Technical field
The present invention relates to a kind of processing system for processing the mud dregs produced in Process of Urban Development, especially exist
The soil dug out in urban construction, such as subway work, building construction dig the processing system of the dregs of ground generation.
Technical background
Subway construction and high-rise building building are the marks that a city develops rapidly.Built in subway construction and high-rise building
In building, the substantial amounts of soil for being mined out will necessarily be produced.The method for processing this kind of soil now only has a kind of mode, is exactly
In the perimeter strip in city, some soil are set up by Na Chang in the place for being adapted to mound.The soil produced in Process of Urban Development
Directly these be sent to by soil car filled by Na Chang, this processing method its be substantially exactly the local excavation for needing to build
Soil out has been transported to the place that need not temporarily carry out urban construction.But, conduct is adapted in surrounding city
Received place side, it is also fewer and feweri, have no alternative but, an overload operation can only be received by existing, form artificial massif, this people
For massif soil property it is of a relatively loose, once by geographical environment change and weather conditions influenceed, such as earthquake or for a long time rain,
It is easy to cause artificial landslide, causes immeasurable artificial loss.Such as this summer, City in South China it is this by Na Chang
Artificial landslide, just almost several industrial areas on massif periphery are all ruined and are buried, cause huge casualties and wealth
Produce loss.
Therefore, how soil of the quick industrial treatment as produced by urban construction, make its turn waste into wealth be pendulum in people
In face of a problem demanding prompt solution.
The content of the invention
In order to solve the deficiencies in the prior art, the present invention is provided to society and a kind of will can produced in Process of Urban Development
Soil, carries out rapid industrial treatment, so that it becomes the system of the industrial treatment mud dregs of construction material and industrial soil.
The technical scheme is that:A kind of system of industrial treatment mud dregs is provided, is primarily suitable for for locating
The silt particle soil excavated in reason urban construction, including:
One drum-type silt particle separator, the drum-type silt particle separator at least includes abrasive segments and silt particle point
From part;The processed silt particle that abrasive member on the cylinder inner wall of the abrasive segments will enter in abrasive segments tentatively breaks
It is broken, and silt particle separate section is sent to, high pressure dilution (operating) water nozzle is provided with the outside of silt particle separate section, will go into the thing
Expect that the silt particle of separate section is diluted to sposh sand, the silt particle separate section allows particle diameter less than the sposh sand of aniseed predetermined particle diameter
Mixture passes through;And particle diameter is then discharged more than or equal to the aniseed mixture of aniseed predetermined particle diameter from discharge gate;
Silt particle separator, the silt particle separator includes coarse sand separator and fine sand separator;The coarse sand
Separator includes coarse sand separating tank and the coarse sand impeller sets by motor-driven slow rotation being arranged on coarse sand separating tank
Part, the coarse sand impeller assembly at least including a pair of parallel setting interval preset space length impeller blade, the impeller blade it
Between be tangentially provided with some scalping pieces, the aperture of the scalping piece is equal to coarse sand predetermined particle diameter;During coarse sand wheel rotation, it is deposited on thick
The silt particle of sand separation trench bottom is drawn onto scalping piece, and coarse sand separating tank is discharged by clean coarse sand;Overflow from coarse sand separating tank
The mud of outflow enters mud conditioning part;The mud for having been filtered coarse sand enters fine sand separator;
The fine sand separator includes fine sand separating tank, and the fine sand leaf of slow rotation is provided with the fine sand separating tank
Wheel assembly, the impeller blade of interval preset space length of the fine sand impeller assembly at least including a pair of parallel setting, in the impeller
Some sifting screen tablets are tangentially provided between piece, the aperture of the sifting screen tablet is equal to fine sand predetermined particle diameter;When fine sand impeller assembly is rotated,
The silt particle for being deposited on fine sand separation trench bottom is drawn onto sifting screen tablet, and fine sand separating tank is discharged by clean fine sand;Filtered
The mixed water of fine sand by return feeding mouth 132 to the drum-type silt particle separator as dilution water use;
Mud conditioning part, the mud gone out from coarse sand separating tank overflow is dehydrated after further fine processing obtains dry mud
It is standby.
Used as improvement of the present invention, the mud conditioning part includes sposh stock tank and hydraulic cyclone sand dividing device, institute
Hydraulic cyclone sand dividing device is stated including cylinder and the bullet of the cylinder bottom is arranged on, is provided with the cylinder
Overflow pipe, mouth will be at least extended in the bullet under the overflow pipe, from sposh stock tank thin mud out by tangential high
Speed enters in the cylinder of hydraulic cyclone sand dividing device, and the mortar being separated is discharged from the lower mouth of the bullet, mortar
Fine sand separator is returned to further to process;Enter deironing apparatus from the mud of overflow pipe outflow;
Deironing apparatus, the irony material in mud is removed by means of magnet, is obtained except mud after iron;
Except organic matter device includes being provided with the sieve of the first predetermined mesh number, to except after iron mud remove organic matter, removed
Organic matter mud;
Fine mud mixing device, including the sieve of the second predetermined mesh number is provided with, wherein the second predetermined mesh number is more than first
Predetermined mesh number, to except the further fine screen of organic matter mud, obtaining fine mud;
Mud-settling pit, fine mud is admitted to sedimentation basin precipitation, and it is dilute that the clear water on sedimentation basin top is returned as high pressure
Water is released to use;The mud of sedimentation basin bottom enters dehydration equipment;
Be dehydrated for the mud of sedimentation basin bottom by dehydration equipment, obtains dry mud standby;The water deviate from is dilute as high pressure
Water is released to use.
Used as improvement of the present invention, the coarse sand predetermined particle diameter is selected between 2 millimeters -3.5 millimeters.
Used as improvement of the present invention, the fine sand predetermined particle diameter is selected between 0.5 millimeter -1.5 millimeters.
Used as improvement of the present invention, the aniseed predetermined particle diameter is selected between 20 millimeters -50 millimeters.
As improvement of the present invention, also including mud device manufacture device, after dry mud is further dried, according to dry mud into
Part, it is made into fictile or ceramic products.
Used as improvement of the present invention, the fictile is at least made into soft ceramics, and the composition of the soft ceramics is dioxy
Soil 80%-90%, soil modifying agent 10%-20% of the SiClx content more than or equal to 70%;Wherein, the soil modifying agent is by 5-8
Part cellulose, urea 1-3 parts and second it is dilute-dilute ester copolymer 6-10 parts of acetic acid second mixes.
Used as improvement of the present invention, a part for the high pressure dilution water comes from secondary water.
As improvement of the present invention, the abrasive member be made up of screw-thread steel herringbone structure, triangle contract block or
Triangle circular cone.
Used as improvement of the present invention, the diameter of the drum-type silt particle separator is selected between 1 meter -5 meters, length
Selected between 5-20 meters.
Processed silt particle is processed into sposh sand as a result of drum-type silt particle separator for the present invention and aniseed mixes
Thing, so, from building site with soil car draw come useless soil directly can pour into separator, be quickly processed into sposh sand and greatly
Material mixture, does not result in accumulation;In addition, processed soil out, the difference according to soil composition can be made fictile
Or ceramic products, it has been truly realized all wastes and has been fully utilized, realizing turns waste into wealth, and is a green exhausted sustainable development
Project.Can realize that the materials that have for rinsing in mud more than 98% are recycled using system of the invention, can be real after purification of waste water
Existing more than 90% recycles.
Brief description of the drawings
Fig. 1 is the frame structure schematic diagram of the processing system of an embodiment of the present invention.
Fig. 2 is the structural representation of the one drum-type silt particle separator in Fig. 1.
Fig. 3 is the main-vision surface structural representation of coarse sand in Fig. 1 or fine sand desanding device.
Fig. 4 is the side elevation view structural representation of Fig. 3.
Fig. 5 is the hydraulic cyclone sand dividing device structural representation in Fig. 1.
Specific embodiment
Fig. 1 to Fig. 5 is referred to, what Fig. 1 to Fig. 5 was disclosed is a kind of system of industrial treatment mud dregs, is mainly suitable for
In the silt particle soil for being excavated in processing urban construction, including:
One drum-type silt particle separator 1, during installation, the drum-type silt particle separator 1 is sideling installed, and it enters
Material mouth 132 is higher than discharge gate 122, descending under gravity with the treatment silt particle such as profit, the drum-type silt particle separator 1
At least include abrasive segments 11 and silt particle separate section 12;Abrasive member 111 on the cylinder inner wall of the abrasive segments 11 will
Tentatively crushed into the processed silt particle in abrasive segments 11, and be sent to silt particle separate section 12, in silt particle separate section 12
Outside be provided with high pressure dilution (operating) water nozzle 121, the silt particle that will go into the feed separation part 12 is diluted to sposh sand, described
Silt particle separate section allows particle diameter to pass through circular hole 123 less than the sposh sand mixture of aniseed predetermined particle diameter;And particle diameter is more than or equal to
The aniseed mixture of aniseed predetermined particle diameter is then discharged from discharge gate 122;In the present embodiment, the aniseed predetermined particle diameter is in 20 millis
Selected between -50 millimeters of rice, specific implementation is got up, can be that some a diameter of 20 millis are set on the cylinder of silt particle separate section
Circular hole 123 in -50 millimeters of rice, the silt particle after tentatively being crushed, when its diameter is less than or equal to 20 millimeters -50 millimeters, can
With the lower leakage from circular hole 123;And the aniseed with diameter greater than 20 millimeters -50 millimeters, including metal class, bamboo and wood class, Plastic, and
Bulky grain building stones and pug etc., all discharge from discharge gate 122, from the aniseed of the discharge of discharge gate 122, then are processed through aniseed described later
Operation is processed(Referring to Fig. 2);
Silt particle separator 2, the silt particle separator 2 includes coarse sand separator 21 and fine sand separator 22;Institute
State coarse sand separator 21 including coarse sand separating tank 211 and be arranged on coarse sand separating tank 211 by motor 215 drive it is slow
The coarse sand impeller assembly 212 of rotation, interval preset space length of the coarse sand impeller assembly 212 at least including a pair of parallel setting
Impeller blade 213, is tangentially provided with some scalping pieces 214 between the impeller blade 213, and the aperture of the scalping piece 214 is equal to slightly
Sand predetermined particle diameter;When coarse sand impeller 212 is rotated, the silt particle for being deposited on coarse sand separation trench bottom is drawn onto scalping piece 214, is washed
Net coarse sand is discharged coarse sand separating tank 211;The mud gone out from the overflow of coarse sand separating tank 211 enters mud conditioning part 3;By mistake
The mud for having filtered coarse sand enters fine sand separator 22;In the present embodiment, the coarse sand predetermined particle diameter 2 millimeters -3.5 millimeters it
Between select.Namely when a diameter of 2 millimeters of scalping piece 214, the diameter of sand grains can be taken as slightly if greater than 2 millimeters, then
Sand separation is out;When a diameter of 3.5 millimeters of scalping piece 214, the diameter of sand grains can then be taken as if greater than 3.5 millimeters
Coarse sand is separated(Referring to Fig. 3 and Fig. 4);
Coarse sand separator of the invention is also designed to, including coarse sand separating tank, and the coarse sand separating tank includes material
Bucket and deep-slotted chip breaker body, set desanding helical axis in the arch groove body, and particle diameter enters pan feeding less than the sposh sand of aniseed predetermined particle diameter
In bucket, the coarse sand being deposited in hopper is brought into deep-slotted chip breaker body under helical axis effect, is separated from sand export;From hopper
The mud that overflow goes out enters 3 mud conditioning devices;The mud for having been filtered coarse sand enters 22 fine sand separators(Do not draw);
The structure of the fine sand separator 22 is identical with the structure of coarse sand separator 21, and the sieve in sieve is not both
Less than the sieve diameter of coarse sand separator, it includes fine sand separating tank 221, is set on the fine sand separating tank 221 bore dia
There is the fine sand impeller assembly 222 of slow rotation, the fine sand impeller assembly 222 at least interval including a pair of parallel setting makes a reservation for
The impeller blade 223 of spacing, is tangentially provided with some sifting screen tablets 224, the aperture of the sifting screen tablet 224 between the impeller blade 223
Equal to fine sand predetermined particle diameter;When fine sand impeller assembly 222 is rotated, the silt particle for being deposited on fine sand separation trench bottom is drawn to sifting screen tablet
On 224, by clean fine sand discharge fine sand separating tank 221;The mixed water for having been filtered fine sand is returned to the drum-type silt particle point
From device 1 feeding mouth 132 as dilution water use;In the present embodiment, the fine sand predetermined particle diameter is in 0.5 millimeter of -1.5 milli
Selected between rice.Namely when a diameter of 0.5 millimeter of sifting screen tablet, the diameter of sand grains can then be worked as if greater than 0.5 millimeter
Separated as fine sand;When a diameter of 1.5 millimeters of scalping piece, the diameter of sand grains can then be taken as if greater than 1.5 millimeters
Fine sand is separated(Referring to Fig. 3 and Fig. 4);
The mud that fine sand separating step of the invention is also designed to filtered coarse sand enters fine sand separating tank, described
Fine sand separating tank includes hopper and deep-slotted chip breaker body, and desanding helical axis is set in the arch groove body, and particle diameter is less than the predetermined grain of fine sand
The sposh sand in footpath enters in material bin, the coarse sand being deposited in hopper helical axis effect under be brought into deep-slotted chip breaker body, by from
Sand export is separated;The mixed water for having been filtered fine sand is used as the dilution water of feeding mouth 132(Do not draw);
Mud conditioning part 3, the mud gone out from the overflow of coarse sand separating tank 211 is dehydrated after further fine processing to be obtained
Dry mud 37 is standby.
Preferably, the mud conditioning part 3 includes sposh stock tank 38 and hydraulic cyclone sand dividing device 31, the waterpower rotation
Stream sand dividing device 31 includes cylinder 311 and is arranged on the bullet 312 of the bottom of the cylinder 311, in the cylinder 311
Overflow pipe 313 is inside provided with, 313 times mouths of the overflow pipe will be at least extended in the bullet 312, dilute in sposh stock tank 38
Mud by the tangential cylinder 311 for entering hydraulic cyclone sand dividing device 31 at a high speed of high-pressure pump 314, the mortar being separated from
The lower mouth 315 of the bullet 312 is discharged, and mortar returns to fine sand separator 22 and further processes;Flowed from the overflow pipe 313
The mud for going out enters deironing apparatus 32;
Deironing apparatus 32, the irony material in mud is removed by means of magnet, is obtained except mud after iron;
Except organic matter device 33 includes being provided with the sieve of the first predetermined mesh number, to except after iron mud remove organic matter, obtain
Except organic matter mud;
Fine mud mixing device 34, including be provided with the sieve of the second predetermined mesh number, wherein the second predetermined mesh number is more than the
One predetermined mesh number, to except the further fine screen of organic matter mud, obtaining fine mud;
Mud-settling pit 35, fine mud is admitted to sedimentation basin precipitation, and the clear water on sedimentation basin top is returned as high pressure
Dilution water 39 is used;The mud of sedimentation basin bottom enters dehydration equipment 36;
Be dehydrated for the mud of sedimentation basin bottom by dehydration equipment 36, obtains dry mud standby;The water deviate from is used as high pressure
Dilution water 39 is used.
Preferably, present invention additionally comprises mud device manufacture device 4, after dry mud is further dried, according to the composition of dry mud, quilt
Make fictile or ceramic products.Mud device manufacture device 4 can be existing according to the difference of product, from different device and technique
There is technology, repeat no more here.
In the present invention, dry mud is further dried water content less than 20% or dry mud is dried to moisture content less than 10%,
Then need to re-grind, after grinding, according to the composition of dry mud, be made into fictile 41 or ceramic products 42;If the composition of soil
The content of middle silica is more than or equal to 70%, then be potter's clay, can be as the raw material of fictile, if three in the composition of soil
The composition of Al 2 O is more than 30%, then be china clay, can be as the raw material of ceramic products.
The fictile 41 can make building pottery part 411, daily pottery part 412 and soft ceramic 413 etc., and building can be each
Class pottery floor tile, potlery tile etc., daily pottery part can be with pottery pot, pottery bowls etc., and soft ceramic 413 is a kind of new ceramic material, and it can be used
The soil of various different components makes as base-material is modified, wherein, the composition of the preferred soft ceramics can be to use titanium dioxide
Soil 80%-90%, soil modifying agent 10%-20% of the silicone content more than or equal to 70%;Wherein, the soil modifying agent is by 5-8 parts
Cellulose, urea 1-3 parts and second it is dilute-dilute ester copolymer 6-10 parts of acetic acid second mixes.
Embodiment 1:Soil 80%, soil modifying agent then uses 20%, is well mixed, then in 130-150 degrees Celsius of condition
Under, further kneaded in banbury, it is molded;
Embodiment 2:Soil 85%, soil modifying agent then uses 15%, is well mixed, then in 130-150 degrees Celsius of condition
Under, further kneaded in banbury, it is molded;
Implement:3:Soil 90%, soil modifying agent then uses 10%, is well mixed, then in 130-150 degrees Celsius of condition
Under, further kneaded in banbury, it is molded;
As for soil modifying agent, can with 5-8 parts of cellulose, urea 1-3 parts and second it is dilute-the dilute ester copolymer 6-10 of acetic acid second
Part mixes;
Such as, can with 5 parts of celluloses, 1 part of urea and second it is dilute -6 parts of the dilute ester copolymer of acetic acid second mixes;Also 7 parts can be used
Cellulose, 2 parts of urea and second it is dilute -8 parts of the dilute ester copolymer of acetic acid second mixes;Can also with 8 parts of celluloses, 3 parts of urea and
Second is dilute-and 10 parts of the dilute ester copolymer of acetic acid second mixes.
Cellulose in the present invention can be hydroxyethyl cellulose, hydroxypropyl methyl cellulose or hydroxypropyl cellulose,
Can be any two or more combination in hydroxyethyl cellulose, hydroxypropyl methyl cellulose and hydroxypropyl cellulose, its ratio
Example is not limited.
By the embodiment 1 in the present invention, embodiment 2 and embodiment 3 and the soft ceramic floor of in the market purchase, elastic comprehensive
Closing two indexs of performance and anti-wear performance has carried out contrast test, and its method of testing and result are as follows:
Elastic integrated performance index method of testing, elastic index mainly tests elongation and response rate;
The assay method of the elongation of soft ceramics:
Test equipment, steel ruler(It is accurate to 0.1mm)With sign pen.
Sample clamp, jaws width is more than 50 millimeters.
Experimental condition, tested soft ceramics and control sample are made into the batten of 65 cm × 5cm wide long, perform 50cm marks
Note;Balanced 4 hours under conditions of temperature is 21 ± 1 DEG C and humidity is 65 ± 2%.
Test, is continuously slowly stretched to 30N, stops 3 seconds, stops redrawing for 3 seconds after slowly lifting, reciprocal three times, the 4th
Measurement markers size after secondary stretching.
Elongation is calculated, elongation %=(- 50 centimetres of size after stretching)/ 50 centimetres.
The assay method of the response rate of soft ceramics:
Test equipment, timer, meter ruler and tape(It is accurate to 0.1MM), static(al) extensibility tester;
Experimental condition, tested soft ceramics and control sample are made into the batten of 65 cm × 5cm wide long, are 21 in temperature
± 1 DEG C and humidity are to balance 4 hours under conditions of 65 ± 2%.
Operation, first determines elongation by the assay method of above-mentioned elongation;
By sample on the basis of original is long tensile elongation 80%, unclamped after fixed half an hour, measured after 1 hour
Its length L1.
For example, elongation is 40%, then 50+50 × 40% × 80% centimetre, i.e., 66 centimetre are stretched to.
Elastic elongation response rate=(L1-50 centimetres)/ 50 centimetres.
Anti-wear performance index determining:According to GB GB/T 12988《Inorganic earth material polishing machine experimental technique》Enter
OK.
Result of the test is as follows:
As can be seen from the above table, embodiments of the invention 1, embodiment 2 and embodiment 3 are equal in elastic performance and anti-wear performance
Better than control sample.Control sample is the soft floor tile of Foshan plant produced from market purchase.
Soft ceramic recyclable regeneration new product in the present invention, also can reduce soil essence by materialization mechanical treatment, return
Cultivate.
The ceramic products 42 can be building porcelain piece 421 such as ceramic tile, such as domestic porcelain 422, porcelain kettle, china bowl and porcelain vase
Deng may also be fabricated which industrial porcelain piece 433, such as electric power insulating porcelain piece.
Preferably, a part for the high pressure dilution water 39 comes from secondary water, and such as running water or river, river or lake is taken out
Water.
Preferably, the diameter of the drum-type silt particle separator is selected between 1 meter -5 meters, and length is in 5-20 rice
Between select.
When the diameter of drum-type silt particle separator is more than 3 meters, 10-20 tons of soil car can directly will be pending
Soil is poured into drum-type silt particle separator, and in this case, the most leading portion preferably in drum-type silt particle separator is set
One conveying section 13, to extend pending soil into the time of abrasive segments 11, and adds appropriate moisture content in this conveying section 13
Pending soil is carried out into preliminarily diluted;The first curved stock guide 1311 is provided with the cylinder inner wall of conveying section 13, if
Dry the first axially arranged curved stock guide 1311 being parallel to each other constitutes some first curved deflector chutes 131, pending silt particle
Abrasive segments 11 are admitted to along the first curved deflector chute 131.
The second curved stock guide 112, some axial directions being parallel to each other are provided with the cylinder inner wall of the abrasive segments 11
The the second curved stock guide 112 for setting constitutes some second curved deflector chutes 113, is set in the described second curved deflector chute 113
There are some abrasive members 111 and the circumferential plate washer 114 being radially arranged of pending silt particle is lifted for being rotated with cylinder, it is pending
On the one hand silt particle is carried out abrasive member 111 and is constantly smashed in abrasive segments 11, while also under the effect of circumferential plate washer 114, no
It is disconnected to be fallen again after cylinder is lifted, reach and further smash;The silt particle being crashed to pieces moves ahead along the second curved deflector chute 113, enters
Enter silt particle separate section 12.
Preferably, the abrasive member 111 is herringbone structure, triangle contract block or the triangle taper being made up of screw-thread steel
Block.In order to improve the wearability of abrasive member 111, the abrasive member 111 can be manufactured with following high-carbbon iron alloys, and it is by weight percent
The titanium 13%~16% of ratio, carbon 4-6%, silicon 2-3%, lead 1-3%, tungsten carbide 5-8%, copper 0.1-0.3%, boron 2-5%, chromium 2-
5%, balance of iron.
Embodiment 1
The abrasive member 111 can be manufactured with following high-carbbon iron alloys, its titanium 13%, carbon 4%, silicon by percentage by weight
2%th, lead 1%, tungsten carbide 5%, copper 0.1%, boron 2% and chromium 2%, balance of iron.
Embodiment 2
The abrasive member 111 can be manufactured with following high-carbbon iron alloys, its titanium 14%, carbon 5%, silicon by percentage by weight
3%th, lead 2%, tungsten carbide 6%, copper 0.2%, boron 4%, chromium 4%, balance of iron.
Embodiment 3
The abrasive member 111 can be manufactured with following high-carbbon iron alloys, its titanium 16%, carbon 6%, silicon by percentage by weight
3%th, lead 3%, tungsten carbide 8%, copper 0.3%, boron 5%, chromium 5%, balance of iron.
The difference of above-mentioned alloy exists, and common people think that copper is harmful element at for ferroalloy, it is impossible to make
With, and together with tungsten carbide be added to when in ferrotianium copper by the present invention, greatly increases the wearability of ferrotitanium conjunction
Energy.
Contrast of Wear Resistance method of testing and result that abrasive member of the invention is closed with the ferrotitanium bought on the market:
Method of testing, uses device, ML-10 type abrasive testers, 200# emery papers, a ten thousandth precision day
It is flat.Sample rotation rate is 180 revs/min, and normal load power is 750N, and the time is 4 hours.
Result of the test:
As can be seen from the above table, abrasive member of the invention is good with anti-wear performance compared with the ferrotitanium bought on the market is closed
Advantage.
Preferably, the dehydration equipment in the present invention can be realized using plate and frame filter press or high-power soil dehydration machine.
Preferably, the present invention can also include aniseed process part 5, to the aniseed discharged from discharge gate, first pass around big
Material removal of impurities 51, the debris such as the metal in aniseed, bamboo and wood, plastics is sorted and is detected, then, by aniseed breaker 52, with broken
Broken machine is crushed to major class, after crushing building stones can be used directly as construction material, in aniseed processing procedure produce
Pug out can return to the first step of the invention as new pending material, be further processed.
Claims (9)
1. a kind of system of industrial treatment mud dregs, is primarily suitable for for processing the silt particle excavated in urban construction
Soil, it is characterised in that including:
One drum-type silt particle separator(1), the drum-type silt particle separator(1)At least include abrasive segments(11)With
Silt particle separate section(12);In the abrasive segments(11)Cylinder inner wall on abrasive member(111)Will be into abrasive segments
(11)Interior processed silt particle is tentatively crushed, and is sent to silt particle separate section(12), in silt particle separate section(12)Outside
It is provided with high pressure dilution (operating) water nozzle(121), will go into the silt particle separate section(12)Silt particle be diluted to sposh sand, the mud
Sand separation part allows particle diameter to pass through less than the sposh sand mixture of aniseed predetermined particle diameter, and enters silt particle separator(2);And
Particle diameter more than or equal to aniseed predetermined particle diameter aniseed mixture then by from discharge gate(122)Discharge;
Silt particle separator(2), the silt particle separator(2)Including coarse sand separator(21)With fine sand separator
(22);The coarse sand separator(21)Including coarse sand separating tank(211)Be arranged on coarse sand separating tank(211)On by motor
The coarse sand impeller assembly of the slow rotation for driving(212), the coarse sand impeller assembly(212)At least including a pair of parallel setting
It is spaced the impeller blade of preset space length(213), in the impeller blade(213)Between be tangentially provided with some scalping pieces(214), it is described thick
Sieve(214)Aperture be equal to coarse sand predetermined particle diameter;Coarse sand impeller assembly(212)During rotation, it is deposited on coarse sand and separates trench bottom
Silt particle drawn to scalping piece(214)On, coarse sand separating tank is discharged by clean coarse sand(211);From coarse sand separating tank(211)
The mud that overflow goes out enters mud conditioning part(3);The mud for having been filtered coarse sand enters fine sand separator(22);
The fine sand separator(22)Including fine sand separating tank(221), in the fine sand separating tank(221)It is provided with slow turning
Dynamic fine sand impeller assembly(222), the fine sand impeller assembly(222)At least include the interval preset space length of a pair of parallel setting
Impeller blade(223), in the impeller blade(223)Between be tangentially provided with some sifting screen tablets(224), the sifting screen tablet(224)'s
Aperture is equal to fine sand predetermined particle diameter;Fine sand impeller assembly(222)During rotation, be deposited on fine sand separate trench bottom silt particle drawn to
Sifting screen tablet(224)On, fine sand separating tank is discharged by clean fine sand(221);The mixed water for having been filtered fine sand is returned to the rolling
Cartridge type silt particle separator(1)Feeding mouth(13)As dilution water use;
Mud conditioning part(3), from coarse sand separating tank(211)The mud that overflow goes out is dehydrated after further fine processing to be obtained
Dry mud is standby.
2. the system of industrial treatment mud dregs according to claim 1, it is characterised in that the mud conditioning part
(3)Including sposh stock tank(38)With hydraulic cyclone sand dividing device(31), the hydraulic cyclone sand dividing device(31)Including cylinder
(311)Be arranged on the cylinder(311)The bullet of bottom(312), in the cylinder(311)Inside it is provided with overflow pipe
(313), the overflow pipe(313)Lower mouth will at least extend to the bullet(312)It is interior, from sposh stock tank(38)Out dilute
Mud enters at a high speed hydraulic cyclone sand dividing device by tangential(31)Cylinder(311)Interior, the mortar being separated is from described
Bullet(312)The discharge of lower mouth, mortar returns to fine sand separator(22)Further treatment;From the overflow pipe(313)Stream
The mud for going out enters deironing apparatus(32);
Deironing apparatus(32), the irony material in mud is removed by means of magnet, obtain except mud after iron;
Except organic matter device(33)Sieve including being provided with the first predetermined mesh number, to except after iron mud remove organic matter, removed
Organic matter mud;
Fine mud mixing device(34), including the sieve of the second predetermined mesh number is provided with, wherein the second predetermined mesh number is more than first
Predetermined mesh number, to except the further fine screen of organic matter mud, obtaining fine mud;
Mud-settling pit(35), fine mud is admitted to sedimentation basin precipitation, and it is dilute that the clear water on sedimentation basin top is returned as high pressure
Release water(39)Use;The mud of sedimentation basin bottom enters dehydration equipment(36);
Dehydration equipment(36)The mud of sedimentation basin bottom is dehydrated, dry mud is obtained standby;The water deviate from is dilute as high pressure
Release water(39)Use.
3. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that the coarse sand makes a reservation for
Particle diameter is selected between 2 millimeters -3.5 millimeters.
4. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that the fine sand makes a reservation for
Particle diameter is selected between 0.5 millimeter -1.5 millimeters.
5. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that the aniseed makes a reservation for
Particle diameter is selected between 20 millimeters -50 millimeters.
6. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that also including mud device system
Make device(4), after dry mud is further dried, according to the composition of dry mud, it is made into fictile or ceramic products.
7. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that the high pressure dilution
Water(39)A part come from secondary water.
8. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that the abrasive member
(111)It is herringbone structure, triangle contract block or the triangle circular cone being made up of screw-thread steel.
9. the system of industrial treatment mud dregs according to claim 1 and 2, it is characterised in that the drum-type mud
The diameter of sand separating apparatus is selected between 1 meter -5 meters, and length is selected between 5 meters -20 meters.
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PCT/CN2017/077801 WO2018064878A1 (en) | 2016-09-26 | 2017-03-23 | System for industrializedly processing silt and muck |
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CN201610845753 | 2016-09-26 | ||
CN2016108457531 | 2016-09-26 |
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CN106311725B (en) * | 2016-09-26 | 2017-05-31 | 深圳申佳原环保科技有限公司 | The method of industrial treatment mud dregs |
CN106238180A (en) * | 2016-09-26 | 2016-12-21 | 深圳申佳原环保科技有限公司 | Integrated high-efficiency mud dregs processing means |
CN106238444B (en) * | 2016-09-26 | 2017-05-31 | 深圳申佳原环保科技有限公司 | The system of industrial treatment mud dregs |
CN106623368A (en) * | 2017-01-07 | 2017-05-10 | 长沙锦佳环保科技有限公司 | Innocent treatment method for shield tunneling residue soil |
CN108160318A (en) * | 2017-11-28 | 2018-06-15 | 深圳市万佳晟环保产业有限公司 | Building waste processing system |
CN107971129A (en) * | 2017-11-28 | 2018-05-01 | 深圳市万佳晟环保产业有限公司 | Building waste processing system |
CN108160317A (en) * | 2017-11-28 | 2018-06-15 | 深圳市万佳晟环保产业有限公司 | Building waste processing system |
CN108160316A (en) * | 2017-11-28 | 2018-06-15 | 深圳市万佳晟环保产业有限公司 | Building waste processing system |
CN108160319A (en) * | 2017-11-28 | 2018-06-15 | 深圳市万佳晟环保产业有限公司 | Building waste processing system |
CN108160315A (en) * | 2017-11-28 | 2018-06-15 | 深圳市万佳晟环保产业有限公司 | For the water circulation system of building waste processing |
CN108160314B (en) * | 2017-11-28 | 2023-06-06 | 深圳江氏恩泽实业有限公司 | Construction waste treatment system |
CN110665934A (en) * | 2019-09-19 | 2020-01-10 | 台州职业技术学院 | Construction waste's recovery processing system |
CN111347689B (en) * | 2020-03-25 | 2022-04-19 | 广州勒高汽车科技有限公司 | Coating equipment for automobile door handle |
CN113441529B (en) * | 2021-07-14 | 2021-12-31 | 武汉中科固废资源产业技术研究院有限公司 | Urban waste residue soil recycling system |
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JP3493209B2 (en) * | 1993-05-25 | 2004-02-03 | 大東株式会社 | Drilling mud treatment method |
CN101177325A (en) * | 2006-11-11 | 2008-05-14 | 宜昌黑旋风工程机械有限公司 | Plaster multi-step treatment device for underground engineering construction |
CN101585714B (en) * | 2009-06-19 | 2012-05-02 | 方远建设集团股份有限公司 | Preparing method of ceram site fully using biosolid and sludge |
CN102228866B (en) * | 2011-04-18 | 2013-11-27 | 昆明理工大学 | Compound classification method and equipment for ground ore product |
JP2013221353A (en) * | 2012-04-18 | 2013-10-28 | Gecoss Corp | Recovery method of cement slurry from surplus sludge containing cement |
CN204276137U (en) * | 2014-11-28 | 2015-04-22 | 魏根友 | Mudstone environmental protection reclaiming system |
CN204396456U (en) * | 2014-12-11 | 2015-06-17 | 北京建工环境修复股份有限公司 | A kind of Soil leaching repair system concentrating design concept based on decrement |
CN104858048B (en) * | 2015-05-07 | 2017-04-05 | 康明克斯(北京)机电设备有限公司 | The environmental friendly regenerated processing method of earth pressure balanced shield, EPBS dregs and equipment |
CN104874591B (en) * | 2015-06-11 | 2017-06-13 | 绿源环保有限公司 | The remaining sludge treatment technology of building and system |
CN204747062U (en) * | 2015-06-11 | 2015-11-11 | 揭阳市绿源环保处理有限公司 | Surplus mud processing system of building |
CN105057320A (en) * | 2015-09-18 | 2015-11-18 | 南通天蓝环保能源成套设备有限公司 | Process for disposing waste residue of engineering |
CN106238444B (en) * | 2016-09-26 | 2017-05-31 | 深圳申佳原环保科技有限公司 | The system of industrial treatment mud dregs |
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