CN106336098A - Device and method for emulsifying combustion treatment of oily sludge - Google Patents
Device and method for emulsifying combustion treatment of oily sludge Download PDFInfo
- Publication number
- CN106336098A CN106336098A CN201610885387.2A CN201610885387A CN106336098A CN 106336098 A CN106336098 A CN 106336098A CN 201610885387 A CN201610885387 A CN 201610885387A CN 106336098 A CN106336098 A CN 106336098A
- Authority
- CN
- China
- Prior art keywords
- oily sludge
- combustion
- tower
- boiler
- mud
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 26
- 239000010802 sludge Substances 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 18
- 230000001804 emulsifying effect Effects 0.000 title claims abstract description 10
- 239000004576 sand Substances 0.000 claims description 15
- 238000004945 emulsification Methods 0.000 claims description 14
- 239000002699 waste material Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 238000010298 pulverizing process Methods 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000000084 colloidal system Substances 0.000 claims description 3
- 239000006185 dispersion Substances 0.000 claims description 3
- 239000000839 emulsion Substances 0.000 claims description 3
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000009833 condensation Methods 0.000 abstract 2
- 230000005494 condensation Effects 0.000 abstract 2
- 238000007790 scraping Methods 0.000 abstract 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000126 substance Substances 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
-
- 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
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
- F23C5/08—Disposition of burners
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Treatment Of Sludge (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses a device for emulsifying combustion treatment of oily sludge. The device comprises a combustion boiler, a separating tower and a condensation tower. A boiler tube is arranged in the combustion boiler, the input end of the boiler tube extends out of the combustion boiler, the output end of the boiler tube extends out of the combustion boiler to be connected with the separating tower, and the separating tower is further connected with the condensation tower through a pipeline. The bottom of the combustion boiler is provided with a burner, the top of the combustion boiler is provided with a chimney, the lower end of the separating tower is provided with a speed reduction motor, the output end of the speed reduction motor is connected with a rotating shaft, and the rotating shaft is inserted in the separating tower and provided with a plurality of scraping plates. The invention further discloses a method for emulsifying combustion treatment of oily sludge. The device for emulsifying combustion treatment of oily sludge is simple and reliable in structure, low in cost and high in safety and can effectively perform oil, mud and water separation on the oily sludge, and the process has fewer steps and is convenient to operate.
Description
Technical field
The present invention relates to chemical industry hydro carbons processing meanss and method, more particularly, to a kind of dress of emulsification, combustion disposal oily sludge
Put and method of disposal.
Background technology
With industrial fast development, various petroleum hydrocarbon class pollutants are increasing, but the mud in waste petroleum
The dustiness of (mud, sand) is very high, if being directly entered air, soil, after water system, animals and plants and human body being produced with serious danger
Evil.Although the processing method at present oil-containing discarded, all make substantial amounts of research both at home and abroad, traditional physics, physico
Learn, chemistry, electrochemical method all can not reach and the mud in waste petroleum is processed.
Oily sludge incineration device in the market is a lot, but all exists and burn insufficient, and organic matter removal is not thorough, especially
The efficiency that it is processed is very low, and production cost is high, and equipment investment is larger.
Content of the invention
The present invention is for avoiding the weak point existing for above-mentioned prior art, providing a kind of emulsification, combustion to dispose and contain greasy dirt
The device of mud and method of disposal.
The present invention solves technical problem and be the technical scheme is that
A kind of emulsification, combustion disposes the device of oily sludge, and it includes burning boiler, knockout tower and condensing tower, described burning
Be provided with boiler tube in boiler, described boiler tube input stretches out outside burning boiler, its outfan stretch out burning boiler outer with knockout tower phase
Even, described knockout tower is also connected with described condensing tower by pipeline；
Described burning boiler bottom is provided with burner, and its top is provided with chimney；
Described knockout tower lower end is provided with reducing motor, and the outfan of this reducing motor is connected with rotary shaft, this rotary shaft
In the described knockout tower of insertion, and several piece scraper plate is provided with described rotary shaft.
Further, the boiler tube spiral setting in described burning boiler.
Further, described knockout tower lower portion is tapered, and cone angle is at 60-80 DEG C.
Further, it is additionally provided with waste outlet below described knockout tower.
Further, described inclination is arranged on the rotary shaft.
Further, described condensing tower one end is provided with vacuum interface, and the other end is provided with outlet；Described condensing tower is provided with to be washed
Wash section.
The invention also discloses a kind of method that emulsification, combustion disposes oily sludge, specifically comprise the following steps that
Step 1, greasy filth and sump oil uniform stirring are mixed after deliver in colloid mill, and add emulsion, make thing
Material, by emulsifying effectively, dispersion, homogenizing and pulverizing, reaches the effect of material fining pulverizing and emulsifying, is then fed into the pot that burns
In stove；
Step 2, the high-pressure pump starting the external world and burner, make the flame that burner sprays carry out high-temperature heating to boiler tube,
Also the oily sludge in boiler tube is heated simultaneously；
Step 3, heated after oily sludge in moisture content evaporated, and oil, mud, sand then enter and carry out in knockout tower point
From, and mud and sand are discharged from waste outlet in the presence of scraper plate；
Step 4, some mud, sand, oil then can enter in condensing tower by pipeline, and the residual liquid of oil-containing passes through to discharge
Mouth is discharged, and waits the later stage to process；
Step 5, remaining mud, husky surface also can be coated with one layer of oil, now by washing section cleaning showers, by mud, sand
After surface coated oil has cleaned, residual liquid is discharged by outlet, and mud, sand then pass through vacuum interface and by extraneous vacuum
Pump or miscellaneous equipment are discharged, and wait the later stage to process.
Further, the furnace tube temperature in described burning boiler is at 400-450 DEG C.
Further, the temperature in described condensing tower is < 100 DEG C.
Compared with the prior art, beneficial effects of the present invention are embodied in:
Present configuration is simple and reliable, low cost, safe, effectively oily sludge can be carried out oil, mud, water separation,
And this processing step is few, easy to operate, it is easy to accomplish Automated condtrol.
Brief description
Fig. 1 is present configuration schematic diagram.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the present invention realizes are easy to understand, tie below
Conjunction is specifically illustrating, and the present invention is expanded on further.
As shown in figure 1, a kind of emulsification, combustion disposes the device of oily sludge, it includes burning boiler 1, knockout tower 2 and cold
Solidifying tower 3, is provided with boiler tube 4, described boiler tube 4 input stretches out outside burning boiler 1, and its outfan stretches out combustion in described burning boiler 1
Burning boiler 1 is outer to be connected with knockout tower 2, and described knockout tower 2 is also connected with described condensing tower 3 by pipeline 5；
Described burning boiler 1 bottom is provided with burner 6, and its top is provided with chimney 7；
Described knockout tower 2 lower end is provided with reducing motor 8, and the outfan of this reducing motor 8 is connected with rotary shaft 9, this rotation
In the knockout tower 2 described in insertion of axle 9, and it is provided with several piece scraper plate 10 in described rotary shaft 9.
Boiler tube 4 spiral setting in described burning boiler 1.
Described knockout tower 2 lower portion is tapered, and cone angle is at 60-80 DEG C.
It is additionally provided with waste outlet 11 below described knockout tower 2.
Described scraper plate 10 is inclined in rotary shaft 9.
Described condensing tower 3 one end is provided with vacuum interface 12, and the other end is provided with outlet 13；Described condensing tower 3 is provided with to be washed
Wash section 14.
A kind of method that emulsification, combustion disposes oily sludge, specifically comprises the following steps that
Step 1, greasy filth and sump oil uniform stirring are mixed after deliver in colloid mill, and add emulsion, make thing
Material, by emulsifying effectively, dispersion, homogenizing and pulverizing, reaches the effect of material fining pulverizing and emulsifying, is then fed into the pot that burns
In stove 1；
Step 2, the high-pressure pump starting the external world and burner 6, make the flame that burner 6 sprays carry out high temperature to boiler tube 4 and add
Heat, also heats to the oily sludge in boiler tube 4 simultaneously；
Step 3, heated after oily sludge in moisture content evaporated, and oil, mud, sand then enter in knockout tower 3 and carry out
Separate, and mud and sand are discharged from waste outlet 11 in the presence of scraper plate 10；
Step 4, some mud, sand, oil then can enter in condensing tower 3 by pipeline 5, and the residual liquid of oil-containing passes through row
Outlet 13 discharge, waits the later stage to process；
Step 5, remaining mud, husky surface also can be coated with one layer of oil, now by washing section 14 cleaning showers, by mud,
After husky surface coated oil has cleaned, residual liquid is discharged by outlet 13, and mud, sand then pass through vacuum interface 12 and by the external world
Vacuum pump or miscellaneous equipment discharge, wait the later stage process.
Further, the furnace tube temperature in described burning boiler is at 400-450 DEG C.
Further, the temperature in described condensing tower is < 100 DEG C.
In the present invention, the combustion medium of burner injection is natural gas or oil.
The basic principles, principal features and advantages of the present invention have been shown and described above.The technical staff of the industry should
Understand, the present invention is not restricted to the described embodiments, the simply explanation present invention's described in above-described embodiment and description is former
Reason, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, these changes and improvements
Both fall within scope of the claimed invention.Claimed scope is by appending claims and its equivalent circle.
Fixed.
Claims (9)
1. a kind of emulsification, combustion disposes the device of oily sludge, and it includes burning boiler (1), knockout tower (2) and condensing tower (3),
It is characterized in that: it is provided with boiler tube (4) in described burning boiler (1), described boiler tube (4) input stretches out burning boiler (1) outward, its
Outfan is stretched out burning boiler (1) and is connected with knockout tower (2) outward, and it is also cold with described that described knockout tower (2) passes through pipeline (5)
Solidifying tower (3) is connected；
Described burning boiler (1) bottom is provided with burner (6), and its top is provided with chimney (7)；
Described knockout tower (2) lower end is provided with reducing motor (8), and the outfan of this reducing motor (8) is connected with rotary shaft (9), should
The knockout tower (2) that the insertion of rotary shaft (9) is described is interior, and is provided with several piece scraper plate (10) in described rotary shaft (9).
2. according to claim 1 a kind of emulsification, combustion dispose oily sludge device it is characterised in that: positioned at described burning
Boiler tube (4) spiral setting in boiler (1).
3. according to claim 1 a kind of emulsification, combustion dispose oily sludge device it is characterised in that: described knockout tower
(2) lower portion is tapered, and cone angle is at 60-80 DEG C.
4. according to claim 1 a kind of emulsification, combustion dispose oily sludge device it is characterised in that: described knockout tower
(2) it is additionally provided with waste outlet (11) below.
5. according to claim 1 a kind of emulsification, combustion dispose oily sludge device it is characterised in that: described scraper plate
(10) it is inclined in rotary shaft (9).
6. according to claim 1 a kind of emulsification, combustion dispose oily sludge device it is characterised in that: described condensing tower
(3) one end is provided with vacuum interface (12), and the other end is provided with outlet (13)；Described condensing tower (3) is provided with washing section (14).
7. a kind of dispose the method for oily sludge using a kind of emulsification, combustion as described in claim 1-6 it is characterised in that concrete
Step is as follows:
Step 1, greasy filth and sump oil uniform stirring are mixed after deliver in colloid mill, and add emulsion, make material quilt
Emulsifying, dispersion, homogenizing and pulverizing effectively, reaches the effect of material fining pulverizing and emulsifying, is then fed into burning boiler (1)
In；
Step 2, the high-pressure pump starting the external world and burner (6), make the flame that burner (6) sprays carry out high temperature to boiler tube (4)
Heating, also heats to the oily sludge in boiler tube (4) simultaneously；
Step 3, heated after oily sludge in moisture content evaporated, and oil, mud, sand then enter and carry out in knockout tower (2) point
From, and mud and sand are discharged from waste outlet (11) in the presence of scraper plate (10)；
Step 4, some mud, sand, oil then can enter in condensing tower (3) by pipeline (5), and the residual liquid of oil-containing passes through row
Outlet (13) is discharged, and waits the later stage to process；
Step 5, remaining mud, husky surface also can be coated with one layer of oil, now by washing section (14) cleaning showers, by mud, sand
After surface coated oil has cleaned, residual liquid passes through outlet (13) and discharges, and mud, sand then pass through vacuum interface (12) and by outer
The vacuum pump on boundary or miscellaneous equipment are discharged, and wait the later stage to process.
8. method according to claim 7 it is characterised in that: boiler tube (4) temperature in described burning boiler (1) is in 400-
450℃.
9. method according to claim 7 it is characterised in that: the temperature in described condensing tower (3) be < 100 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610885387.2A CN106336098B (en) | 2016-10-11 | 2016-10-11 | Device and method for treating oily sludge through emulsification combustion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610885387.2A CN106336098B (en) | 2016-10-11 | 2016-10-11 | Device and method for treating oily sludge through emulsification combustion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106336098A true CN106336098A (en) | 2017-01-18 |
| CN106336098B CN106336098B (en) | 2023-04-18 |
Family
ID=57838759
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610885387.2A Active CN106336098B (en) | 2016-10-11 | 2016-10-11 | Device and method for treating oily sludge through emulsification combustion |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106336098B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2225007Y (en) * | 1994-08-21 | 1996-04-17 | 广东省环境工程装备总公司茂名分公司 | Wet dust collector of vertical kiln with automatic separation of mud and water |
| JP2005114327A (en) * | 2003-10-03 | 2005-04-28 | Kurieteikku Corp | Drying method and drying equipment |
| CN203700132U (en) * | 2014-02-24 | 2014-07-09 | 盘锦宁泰能源科技有限公司 | Multistage continuous oil sludge treatment equipment |
| CN105018159A (en) * | 2015-06-19 | 2015-11-04 | 四川华益隆环保科技有限公司 | Oil gas engineering oil-containing solid waste resource modification treatment method |
| CN206188604U (en) * | 2016-10-11 | 2017-05-24 | 安徽国孚润滑油工业有限公司 | Device that contains oil sludge is dealt with in emulsification burning |
-
2016
- 2016-10-11 CN CN201610885387.2A patent/CN106336098B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2225007Y (en) * | 1994-08-21 | 1996-04-17 | 广东省环境工程装备总公司茂名分公司 | Wet dust collector of vertical kiln with automatic separation of mud and water |
| JP2005114327A (en) * | 2003-10-03 | 2005-04-28 | Kurieteikku Corp | Drying method and drying equipment |
| CN203700132U (en) * | 2014-02-24 | 2014-07-09 | 盘锦宁泰能源科技有限公司 | Multistage continuous oil sludge treatment equipment |
| CN105018159A (en) * | 2015-06-19 | 2015-11-04 | 四川华益隆环保科技有限公司 | Oil gas engineering oil-containing solid waste resource modification treatment method |
| CN206188604U (en) * | 2016-10-11 | 2017-05-24 | 安徽国孚润滑油工业有限公司 | Device that contains oil sludge is dealt with in emulsification burning |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106336098B (en) | 2023-04-18 |
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Address after: 246000 Xizhuang Group, Nongzhuang Village, Yangqiao Town, Yixiu District, Anqing City, Anhui Province Patentee after: Anhui Guofu Environmental Technology Co.,Ltd. Address before: 246000 Xizhuang Group, Nongzhuang Village, Yangqiao Town, Yixiu District, Anqing City, Anhui Province Patentee before: ANHUI GUOFU LUBRICANT INDUSTRY Co.,Ltd. |
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