CN109111074A - A kind of greasy filth drying particles device - Google Patents
A kind of greasy filth drying particles device Download PDFInfo
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- CN109111074A CN109111074A CN201810985119.7A CN201810985119A CN109111074A CN 109111074 A CN109111074 A CN 109111074A CN 201810985119 A CN201810985119 A CN 201810985119A CN 109111074 A CN109111074 A CN 109111074A
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- Prior art keywords
- auger
- air
- desiccation
- greasy filth
- drying particles
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- 238000001035 drying Methods 0.000 title claims abstract description 34
- 239000002245 particle Substances 0.000 title claims abstract description 31
- 238000012856 packing Methods 0.000 claims description 16
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 230000008859 change Effects 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 26
- 238000013461 design Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 26
- 238000000034 method Methods 0.000 description 17
- 239000003921 oil Substances 0.000 description 13
- 239000010802 sludge Substances 0.000 description 12
- 239000010410 layer Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000008187 granular material Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000003209 petroleum derivative Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000010779 crude oil Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000002365 multiple layer Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000011265 semifinished product Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- -1 category Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000001698 pyrogenic effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000010729 system oil Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/14—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives within horizontal containers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
- B02C18/18—Knives; Mountings thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/26—Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles
Abstract
The invention discloses a kind of greasy filth drying particles devices, it is related to drying device technical field, including desiccation auger, air-heater, muff, air-introduced machine and thermo detector, desiccation auger both ends are equipped with inlet port and outlet port, and one end is equipped with moisture pump orifice and temperature-measuring base, moisture pump orifice is connected with air-introduced machine air inlet, thermo detector is housed on temperature-measuring base, muff is cased with outside desiccation auger, is equipped with insulating layer in muff, both ends are equipped with air inlet and air outlet, and gas outlet is connected with air-heater air inlet.The moisture content of material can be effectively reduced in the present invention, reaches within the scope of design requirement；Treated that material particles degree is small by the present invention, facilitates and handles in next step.
Description
Technical field
The invention belongs to drying device technical fields, and in particular to a kind of greasy filth drying particles device.
Background technique
Oily sludge is a kind of stable gluey system containing the compositions such as the organic matters such as petroleum and water, silt, therein to have
Machine matter goes back a large amount of condensed-nuclei aromatics of oil-containing and harmful microorganism, oil-containing in addition to containing heaviness crude oil, semi-finished product residual oil and product oil
Sludge adopts along with crude oil, refines, collecting, defeated links, and can be divided mainly into source by its source is crude oil, semi-finished product oil and finished product
Tank bottom oil sludge, sewage from oil refinery processing system oil separator bed mud, biochemical sludge and air-floating apparatus are formed by during oil collection is defeated
The ground sludge three categories that dross is formed by " three mud " and is formed during oil extraction.Its enormous amount, according to incomplete
Only annual output all kinds of greasy filth in China's are up to 30,000,000 tons to statistics, due to wherein containing a large amount of unsegregated crude oil, microorganism, a huge sum of moneys
The poisonous and harmful substances such as category, benzene homologues, it is huge to human body and environmental hazard, solid hazardous waste is classified as by China
, it is necessary to through being effectively treated it is innoxious after can just discharge.The method of existing processing oily sludge domestic at present, is summed up
Have: incineration method, pyrogenic process, landfill method, till, solvent extraction, oily sludge comprehensive utilization, solidification method, chemical demulsification method
And biological treating etc..The method of disposal that traditional greasy filth uses substantially can be divided into Resource Access type and harmless transformant two major classes.
Currently, Treatment of Sludge be sludge is concentrated, is quenched, dehydration, is stablized, the minimizings, stabilization such as desiccation or burning
Change, innoxious process, oily sludge disposal technology is broadly divided into mechanical dehydration technique, sludge drying process, outward transport are burnt
Firing technique.General sludge drying device is using hot wind blade drying machine, using the hot wind that coal-fired hot-blast stove generates as baking
Dry heat source, drying efficiency is low, and the vapour content after desiccation in flue gas is very big, and moisture content and solid phase particles size are uncontrollable, deposits
In the problem that mud granule can not separate very well and cause total dustiness excessively high.
Summary of the invention
It is an object of the invention to: low for above-mentioned drying efficiency, the vapour content after desiccation in flue gas is very big, aqueous
Rate and solid phase particles size are uncontrollable, and the excessively high problem of total dustiness, the present invention provides a kind of greasy filth drying particles device, can be with
The moisture content of greasy filth is effectively reduced, adjusts the form of greasy filth.
The technical solution adopted by the invention is as follows:
A kind of greasy filth drying particles device, includes desiccation auger, desiccation auger both ends be respectively equipped with feed inlet and
Discharge port, desiccation auger one end are additionally provided with moisture pump orifice and temperature-measuring base, and the moisture pump orifice is connected with air-introduced machine,
Thermo detector is housed, the desiccation auger outer cover is equipped with muff, and the muff both ends are respectively equipped on the temperature-measuring base
Air inlet and air outlet, the air inlet are connected with heat source, and the gas outlet is connected with air-heater.
When the invention works, when needing drying particles, hot gas is admitted in muff, to desiccation auger heat, material from
Feed inlet is admitted to desiccation auger, mobile with desiccation auger, is heated simultaneously, reduces its moisture content, material is broken, Zhi Houcong
Discharge port drops out；It is set according to material water ratio and hot air temperature, the drying particles device can be applied in combination with multiple groups, thermometric
Meter real time monitoring discharge port temperature keeps it in and requires in temperature range by adjusting air inflow and auger revolving speed；Muff
The power of interior hot gas circulation and direction are provided by air-heater, and the steam and a small amount of light petroleum gas generated in desiccation auger is by air inducing
Machine is sent at heat source, and second energy utilizes, and is avoided pollution；The air-heater for the circulation of hot gas in muff provide power and
Direction；The drying particles device is set according to material water ratio and temperature, can be applied in combination using multiple groups, i.e., using more
Layer superposition uses, the size in the form of the moisture content and solid granulates for reaching required, and in being applied in combination, the moisture of every layer of device is taken out
Suction inlet connection communicates, and is sent out steam and a small amount of light petroleum gas by connection air-introduced machine；When needing drying particles, hot gas is sent
Enter in muff, desiccation auger is heated；Material is admitted to desiccation auger from feed inlet, mobile with desiccation auger, while being added
Heat reduces its moisture content, and material is broken, and drops out later from discharge port.
Further, the desiccation auger includes the packing auger blade of inner shaft and the inner shaft Spiral distribution around desiccation auger,
The packing auger blade is the sheet metal being continuously arranged.
Further, the packing auger blade is equipped with air channel and bite, and the air channel is uniform on packing auger blade
The small gap of distribution, the bite are the blade being fixedly connected in small gap adjacent with air channel on packing auger blade, ventilation
Slot not only can be used as the channel of air circulation, but also have the function of broken material；The further broken material of bite, makes its granularity
It is smaller.
Further, the inner shaft of the desiccation auger is connected to motor, and the motor is surveyed for driving desiccation auger to rotate
Temperature meter real time monitoring discharge port temperature, by adjusting motor speed, the revolving speed for adjusting desiccation auger keeps temperature when discharging
Within the temperature range of requiring.
Further, the air inlet of the moisture pump orifice and air-introduced machine connects, in the induced draft blower withdraws desiccation auger
The steam and oil gas of generation.
Further, the air outlet of the air-introduced machine is connect with heat source, the steam generated in desiccation auger and on a small quantity light
Matter oil gas is sent to heat source by the air outlet of air-introduced machine, and second energy is utilized, avoided pollution.
Further, the air inlet of the gas outlet and air-heater connects, and the air-heater is the stream of hot gas in muff
It is logical that power and direction are provided.
Further, the feed inlet and gas outlet are located at desiccation auger the same end, and the discharge port is located at air inlet
Desiccation auger the same end, greasy filth enter from feed inlet, are discharged from discharge port, and hot wind enters from air inlet, are discharged from gas outlet, because
And greasy filth flow direction and air circulation direction are incorgruous, hot wind sufficiently recycles, and desiccation effect is good.
Further, insulating layer is equipped in the muff, the insulating layer can completely cut off heat exchange, realize muff
Heat insulation effect.
Further, regulating valve is equipped between the heat source and air inlet, thermo detector monitors discharge port temperature in real time, passes through
Regulating valve adjusts air inflow, keeps it in and requires in temperature range.
In conclusion by adopting the above-described technical solution, the beneficial effects of the present invention are:
1, the present invention makes material be admitted to desiccation auger from feed inlet, mobile with desiccation auger, is heated simultaneously, Ke Yiyou
Effect reduces the moisture content of material, reaches within the scope of design requirement；
2, the further broken material of bite of the present invention keeps its granularity smaller, can effectively adjust greasy filth form, processing
Material particles degree afterwards is small, facilitates and handles in next step；
3, thermo detector of the present invention monitors discharge port temperature in real time, is set according to material water ratio and temperature, can be with multiple groups group
It closes and uses, the size in the form of the moisture content and solid granulates that reach discharging demand.
Detailed description of the invention
In order to illustrate the technical solution of the embodiments of the present invention more clearly, below will be to needed in the embodiment attached
Figure is briefly described, it should be understood that the following drawings illustrates only certain embodiments of the present invention, therefore is not construed as pair
The restriction of range for those of ordinary skill in the art without creative efforts, can also be according to this
A little attached drawings obtain other relevant attached drawings.
Fig. 1 is the structural schematic diagram of drying particles device of the present invention；
Fig. 2 is the structural schematic diagram of desiccation packing auger blade；
Fig. 3 is the structural schematic diagram that multiple groups of the present invention are applied in combination；
Marked in the figure: 1- desiccation auger, 2- feed inlet, 3- air-heater, the gas outlet 4-, 5- muff, 6- insulating layer, 7- draw
Blower, 8- thermo detector, 9- discharge port, 10- air inlet, 11- moisture pump orifice, 12- temperature-measuring base, 13- packing auger blade, 14- are logical
Air drain, 15- bite, 16- motor.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, with reference to the accompanying drawings and embodiments, right
The present invention is further elaborated.It should be appreciated that described herein, specific examples are only used to explain the present invention, not
For limiting the present invention, i.e., described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is logical
The component for the embodiment of the present invention being often described and illustrated herein in the accompanying drawings can be arranged and be designed with a variety of different configurations.
Therefore, the detailed description of the embodiment of the present invention provided in the accompanying drawings is not intended to limit below claimed
The scope of the present invention, but be merely representative of selected embodiment of the invention.Based on the embodiment of the present invention, those skilled in the art
Member's every other embodiment obtained without making creative work, shall fall within the protection scope of the present invention.
It should be noted that the relational terms of term " first " and " second " or the like be used merely to an entity or
Operation is distinguished with another entity or operation, and without necessarily requiring or implying between these entities or operation, there are any
This actual relationship or sequence.Moreover, the terms "include", "comprise" or its any other variant be intended to it is non-exclusive
Property include so that include a series of elements process, method, article or equipment not only include those elements, but also
Further include other elements that are not explicitly listed, or further include for this process, method, article or equipment it is intrinsic
Element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that including described
There is also other identical elements in the process, method, article or equipment of element.
A kind of greasy filth drying particles device includes desiccation auger 1, and 1 both ends of desiccation auger are respectively equipped with feed inlet 2
With discharge port 9, described 1 one end of desiccation auger is additionally provided with moisture pump orifice 11 and temperature-measuring base 12, and the moisture pump orifice 11 connects
It is connected to air-introduced machine 7, the air-introduced machine 7 aspirates the steam and oil gas generated in desiccation auger 1, is equipped with and surveys on the temperature-measuring base 12
Temperature meter 8, discharge port temperature can be monitored in real time in the thermo detector 8, by adjusting air inflow and auger revolving speed, keeps it in
It is required that 1 outer cover of desiccation auger is equipped with muff 5, and 5 both ends of muff are respectively equipped with air inlet 10 in temperature range
With gas outlet 4, the air inlet 10 is connected with heat source, and the gas outlet 4 is connected with air-heater 3, and the air-heater 3 is muff
The circulation of hot gas provides power and direction in 5, and the drying particles device sets according to material water ratio and temperature, can adopt
It is applied in combination, i.e., is used using multiple-layer stacked, the size in the form of the moisture content and solid granulates for reaching required with multiple groups.It needs to do
When changing granulation, hot gas is admitted in muff 5, is heated to desiccation auger 1；Material is admitted to desiccation auger 1 from feed inlet 2, with
Desiccation auger 1 is mobile, is heated simultaneously, reduces its moisture content, material is broken, and drops out later from discharge port 9.
Feature and performance of the invention are described in further detail with reference to embodiments.
Embodiment 1
Present pre-ferred embodiments provide a kind of greasy filth drying particles device, include desiccation auger 1, the desiccation auger
1 both ends are respectively equipped with feed inlet 2 and discharge port 9, and described 1 one end of desiccation auger is additionally provided with moisture pump orifice 11 and temperature-measuring base
12, the moisture pump orifice 11 is connected with air-introduced machine 7, and thermo detector 8 is housed on the temperature-measuring base 12, outside the desiccation auger 1
Portion is arranged with muff 5, and 5 both ends of muff are respectively equipped with air inlet 10 and gas outlet 4, and the air inlet 10 is connected with heat
Source, the gas outlet 4 are connected with air-heater 3.
When the present embodiment works, when needing drying particles, hot gas is admitted in muff 5, is heated to desiccation auger 1, object
Material is admitted to desiccation auger 1 from feed inlet 2, mobile with desiccation auger 1, is heated simultaneously, reduces its moisture content, material is broken
It is broken, it is dropped out later from discharge port 9；It is set according to material water ratio and hot air temperature, the drying particles device can be with multiple groups group
It closes and uses, thermo detector 8 monitors 9 temperature of discharge port in real time and keeps it in by adjusting air inflow and auger revolving speed and require temperature
In range；The power and direction that hot gas circulates in muff 5 are provided by air-heater 3, the steam that generates in desiccation auger 1 and a small amount of
Light petroleum gas heat source is sent to by air-introduced machine 7, second energy utilizes, and avoids pollution；According to operating condition needs, using multiple groups group
It closes and uses, i.e., used using multiple-layer stacked, the size in the form of the moisture content and solid granulates for reaching required, in being applied in combination,
The moisture pump orifice connection of every layer of device communicates, and is sent out steam and a small amount of light petroleum gas by connection air-introduced machine.
The moisture content of material can be effectively reduced in the present invention, reaches within the scope of design requirement；Treated by the present invention
Material particles degree is small, facilitates and handles in next step；It is set, can be applied in combination with multiple groups, to reach according to material water ratio and temperature
The moisture content and solid granulates form size of discharging demand.
Embodiment 2
On the basis of embodiment 1, the desiccation auger 1 includes inner shaft and the inner shaft Spiral distribution around desiccation auger 1
Packing auger blade 13, the packing auger blade 13 is the sheet metal being continuously arranged.
Embodiment 3
On the basis of embodiment 2, the packing auger blade 13 is equipped with air channel 14 and bite 15, the air channel 14
For equally distributed small gap on packing auger blade 13, the bite 15 is adjacent with air channel 14 on packing auger blade 13 small lacks
The blade being fixedly connected in mouthful, the air channel 14 not only can be used as the channel of air circulation, but also have the function of broken material；Institute
The further broken material of bite 15 is stated, keeps its granularity smaller.
Embodiment 4
On the basis of embodiment 2, the inner shaft of the desiccation auger 1 is connect with motor 16, and the motor 16 passes through driving
The inner shaft of desiccation auger 1 rotates, and desiccation auger 1 is driven to rotate；Thermo detector 8 monitors discharge port temperature in real time, by adjusting motor
16 revolving speeds, the revolving speed for adjusting desiccation auger 1 are maintained at temperature when discharging within the temperature range of requirement.
Embodiment 5
On the basis of embodiment 1, the moisture pump orifice 11 is connect with the air inlet of air-introduced machine 7, and the air-introduced machine 7 is logical
Excess moisture pump orifice 11 aspirates the steam and oil gas generated in drying process in desiccation auger 1.
Embodiment 6
On the basis of embodiment 5, the air outlet of the air-introduced machine 7 is connect with heat source, in desiccation auger 1 in the course of work
The steam of generation and a small amount of light petroleum gas are discharged by the air outlet of 7 quilt of air-introduced machine, are sent at heat source, and second energy utilizes, and keeps away
Exempt to pollute.
Embodiment 7
On the basis of embodiment 1, the gas outlet 4 is connect with the air inlet of air-heater 3, and the air-heater 3 is heat preservation
The circulation of hot gas provides power and direction in set 5.
Embodiment 8
On the basis of embodiment 1, the feed inlet 2 is located at 1 the same end of desiccation auger, the discharge port 9 with gas outlet 4
Be located at 1 the same end of desiccation auger with air inlet 10, when work, greasy filth enters from feed inlet 2, be discharged from discharge port 9, hot wind from into
Port 10 enters, and is discharged from gas outlet 4, thus greasy filth flow direction and air circulation direction are incorgruous, and hot wind sufficiently recycles, desiccation
Effect is good.
Embodiment 9
On the basis of embodiment 1, insulating layer 6, covering and heat insulating layer 6, energy on muff 5 are equipped in the muff 5
Sufficiently isolation muff 5 is exchanged with extraneous heat, realizes the heat insulation effect of muff 5.
Embodiment 10
On the basis of embodiment 1, regulating valve (not shown) is equipped between the heat source and air inlet 10, thermo detector 8 is real
When monitor discharge port temperature, air inflow is adjusted by regulating valve, drop temperature is maintained at and requires in temperature range.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention
Made any modifications, equivalent replacements, and improvements etc., should all be included in the protection scope of the present invention within mind and principle.
Claims (10)
1. a kind of greasy filth drying particles device, it is characterised in that: it include desiccation auger (1), desiccation auger (1) both ends point
Not She You feed inlet (2) and discharge port (9), described desiccation auger (1) one end is additionally provided with moisture pump orifice (11) and temperature-measuring base
(12), the moisture pump orifice (11) is connected with air-introduced machine (7), and thermo detector (8) are housed on the temperature-measuring base (12), described dry
To change auger (1) outer cover and is equipped with muff (5), muff (5) both ends are respectively equipped with air inlet (10) and gas outlet (4),
The air inlet (10) is connected with heat source, and the gas outlet (4) is connected with air-heater (3).
2. a kind of greasy filth drying particles device according to claim 1, it is characterised in that: the desiccation auger (1) includes
The packing auger blade (13) of inner shaft and the inner shaft Spiral distribution around desiccation auger (1).
3. a kind of greasy filth drying particles device according to claim 2, it is characterised in that: set on the packing auger blade (13)
There are air channel (14) and bite (15), the air channel (14) is equally distributed small gap on packing auger blade (13), described
Bite (15) is the blade being fixedly connected in small gap adjacent with air channel (14) on packing auger blade (13).
4. a kind of greasy filth drying particles device according to claim 2, it is characterised in that: the desiccation auger (1) it is interior
Axis is connect with motor (16).
5. a kind of greasy filth drying particles device according to claim 1, it is characterised in that: the moisture pump orifice (11) with
The air inlet of air-introduced machine (7) connects.
6. a kind of greasy filth drying particles device according to claim 5, it is characterised in that: the outlet air of the air-introduced machine (7)
Mouth is connect with heat source.
7. a kind of greasy filth drying particles device according to claim 1, it is characterised in that: the gas outlet (4) and hot wind
The air inlet of machine (3) connects.
8. a kind of greasy filth drying particles device according to claim 1, it is characterised in that: the feed inlet (2) and outlet
Mouth (4) is located at desiccation auger (1) the same end, and the discharge port (9) and air inlet (10) are located at desiccation auger (1) the same end.
9. a kind of greasy filth drying particles device according to claim 1, it is characterised in that: be equipped in the muff (5)
Insulating layer (6).
10. a kind of greasy filth drying particles device according to claim 1, it is characterised in that: the heat source and air inlet
(10) regulating valve is equipped between.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810985119.7A CN109111074A (en) | 2018-08-28 | 2018-08-28 | A kind of greasy filth drying particles device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810985119.7A CN109111074A (en) | 2018-08-28 | 2018-08-28 | A kind of greasy filth drying particles device |
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| Publication Number | Publication Date |
|---|---|
| CN109111074A true CN109111074A (en) | 2019-01-01 |
Family
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| CN201810985119.7A Pending CN109111074A (en) | 2018-08-28 | 2018-08-28 | A kind of greasy filth drying particles device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116874154A (en) * | 2023-06-05 | 2023-10-13 | 合肥吴山新型建材有限公司 | Utilize device of tunnel cave pyrolysis deodorization mud |
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| CN103964661A (en) * | 2013-02-06 | 2014-08-06 | 同济大学 | System and method for gradient dewatering drying of sludge |
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