CN206188604U - Device that contains oil sludge is dealt with in emulsification burning - Google Patents
Device that contains oil sludge is dealt with in emulsification burning Download PDFInfo
- Publication number
- CN206188604U CN206188604U CN201621111355.9U CN201621111355U CN206188604U CN 206188604 U CN206188604 U CN 206188604U CN 201621111355 U CN201621111355 U CN 201621111355U CN 206188604 U CN206188604 U CN 206188604U
- Authority
- CN
- China
- Prior art keywords
- knockout tower
- tower
- emulsification
- combustion
- oily sludge
- 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.)
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- 239000010802 sludge Substances 0.000 title claims abstract description 21
- 238000004945 emulsification Methods 0.000 title claims abstract description 15
- 238000002485 combustion reaction Methods 0.000 claims description 13
- 239000002699 waste material Substances 0.000 claims description 7
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- 235000013547 stew Nutrition 0.000 abstract 5
- 238000010304 firing Methods 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000004576 sand Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 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
- 238000005507 spraying Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000002848 electrochemical method 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
- 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
Abstract
The utility model discloses a device that contains oil sludge is dealt with in emulsification burning, it includes fires stew pot stove, knockout tower and condensing tower, it is equipped with the boiler tube in the stew pot stove to fire, outside the boiler tube input stretched out and fires the stew pot stove, its output stretched out and fires that the stew pot stove is outer to link to each other with the knockout tower, the knockout tower pass through the pipeline still with the condensing tower link to each other, firing stew pot stove bottom portion and being equipped with the combustor, its top is equipped with the chimney, the knockout tower lower extreme is equipped with gear motor, and this gear motor's output is connected with the rotation axis, the inserting of this rotation axis the knockout tower in, and the rotation axis on be equipped with several scraper blades. The utility model discloses simple structure is reliable, and is with low costs, and the security is high, can effectively carry out oil, mud, separation of water with containing oil sludge, and this technology step is few, convenient operation.
Description
Technical field
The utility model is related to chemical industry hydro carbons processing unit, more particularly to a kind of emulsification, combustion to dispose the dress of oily sludge
Put.
Background technology
With the fast development of industry, various petroleum hydrocarbon class pollutants are increasing, but the sludge in waste petroleum
The dustiness of (mud, sand) is very high, if after being directly entered air, soil, water system, serious danger will be produced to animals and plants and human body
Evil.It is traditional physics, physico although the processing method discarded to oil-containing at present, has all made substantial amounts of research both at home and abroad
Learn, chemistry, electrochemical method can not all reach and the sludge in waste petroleum is processed.
Oily sludge incineration device in the market is a lot, but all insufficient in the presence of burning, and organic matter removal is not thorough, especially
The efficiency of its treatment is very low, and production cost is high, and equipment investment is larger.
Utility model content
The utility model is to avoid the weak point existing for above-mentioned prior art, there is provided a kind of emulsification, combustion disposal contains
The device of greasy dirt.
The utility model solves the technical scheme that is used of technical problem：
A kind of emulsification, combustion disposes the device of oily sludge, and it includes burning boiler, knockout tower and condensing tower, the burning
Boiler tube is provided with boiler, the boiler tube input is stretched out outside burning boiler, it is outer with knockout tower phase that its output end stretches out burning boiler
Even, described knockout tower is also connected by pipeline with described condensing tower；
The burning boiler bottom is provided with burner, and its top is provided with chimney；
The knockout tower lower end is provided with reducing motor, and the output end of the reducing motor is connected with rotary shaft, the 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 in the burning boiler is set.
Further, the knockout tower lower portion is tapered, and cone angle is at 60-80 DEG C.
Further, described knockout tower lower section is additionally provided with waste outlet.
Further, described inclination is set on the rotary shaft.
Further, described condensing tower one end is provided with vacuum interface, and the other end is provided with outlet；The condensing tower is provided with to be washed
Wash section.
Utility model works step is as follows：
Step 1, greasy filth and sump oil uniform stirring are mixed after be sent in colloid mill, and add emulsion, make thing
Material reaches the effect that material fining is crushed and emulsified by effectively emulsification, dispersion, homogeneous and crushing, is then fed into the pot that burns
In stove；
Step 2, the high-pressure pump and burner that start the external world, the flame for spraying burner carry out high-temperature heating to boiler tube,
Simultaneously also to the oily sludge heating in boiler tube；
Step 3, be heated after oily sludge in moisture content evaporated, and oil, mud, sand are then into being divided in knockout tower
From, and mud and sand are discharged from waste outlet in the presence of scraper plate；
Step 4, some mud, sand, oil can be then entered into condensing tower by pipeline, and the raffinate of oil-containing is by discharge
Mouth discharge, waits later stage treatment；
Step 5, remaining mud, husky surface can also be coated with one layer of oil, now by washing section cleaning showers, by mud, sand
After surface coated oil has been cleaned, raffinate is discharged by outlet, and mud, sand are then by vacuum interface and by extraneous vacuum
Pump or miscellaneous equipment are discharged, and wait later stage treatment.
Further, the furnace tube temperature in the burning boiler is at 400-450 DEG C.
Further, the temperature in the condensing tower is<100℃.
Compared with the prior art, the beneficial effects of the utility model are embodied in：
The utility model is simple and reliable for structure, low cost, safe, oily sludge effectively can be carried out into oil, mud, moisture
From, and the processing step is few, it is easy to operate, it is easy to accomplish Automated condtrol.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and the utility model 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, boiler tube 4 is provided with the burning boiler 1, and the input of the boiler tube 4 is stretched out outside burning boiler 1, and its output end stretches out combustion
Burning boiler 1 is outer to be connected with knockout tower 2, and described knockout tower 2 is also connected by pipeline 5 with described condensing tower 3；
The bottom of the burning boiler 1 is provided with burner 6, and its top is provided with chimney 7；
The lower end of the knockout tower 2 is provided with reducing motor 8, and the output end of the reducing motor 8 is connected with rotary shaft 9, the rotation
In knockout tower 2 described in the insertion of axle 9, and several piece scraper plate 10 is provided with described rotary shaft 9.
The spiral of boiler tube 4 in the burning boiler 1 is set.
The lower portion of the knockout tower 2 is tapered, and cone angle is at 60-80 DEG C.
The described lower section of knockout tower 2 is additionally provided with waste outlet 11.
Described scraper plate 10 is inclined in rotary shaft 9.
Described one end of condensing tower 3 is provided with vacuum interface 12, and the other end is provided with outlet 13；The condensing tower 3 is provided with to be washed
Wash section 14.
Utility model works step is as follows：
Step 1, greasy filth and sump oil uniform stirring are mixed after be sent in colloid mill, and add emulsion, make thing
Material reaches the effect that material fining is crushed and emulsified by effectively emulsification, dispersion, homogeneous and crushing, is then fed into the pot that burns
In stove 1；
Step 2, the high-pressure pump and burner 6 that start the external world, the flame for spraying burner 6 carry out high temperature and add to boiler tube 4
Heat, while also being heated to the oily sludge in boiler tube 4；
Step 3, be heated after oily sludge in moisture content evaporated, and oil, mud, sand are then into carrying out in knockout tower 3
Separate, and mud and sand are discharged from waste outlet 11 in the presence of scraper plate 10；
Step 4, some mud, sand, oil can be then entered into condensing tower 3 by pipeline 5, and the raffinate of oil-containing is by row
Outlet 13 is discharged, and waits later stage treatment；
Step 5, remaining mud, husky surface can also be coated with one layer of oil, now by the cleaning showers of washing section 14, by mud,
After husky surface coated oil has been cleaned, raffinate is discharged by outlet 13, and mud, sand are then by vacuum interface 12 and by the external world
Vavuum pump or miscellaneous equipment discharge, wait the later stage treatment.
Further, the furnace tube temperature in the burning boiler is at 400-450 DEG C.
Further, the temperature in the condensing tower is<100℃.
In the utility model, the combustion medium of burner injection is natural gas or oil.
General principle of the present utility model, principal character and advantage has been shown and described above.The technical staff of the industry
It should be appreciated that the utility model is not restricted to the described embodiments, the simply explanation described in above-described embodiment and specification is originally
The principle of utility model, on the premise of the utility model spirit and scope are not departed from, the utility model also has various change
And improvement, these changes and improvements are both fallen within the range of claimed the utility model.The utility model claims scope
By appending claims and its equivalent thereof.
Claims (6)
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：Boiler tube (4) is provided with the burning boiler (1), boiler tube (4) input stretches out burning boiler (1) outward, its
Output end is stretched out burning boiler (1) and is connected with knockout tower (2) outward, and described knockout tower (2) is cold also with described by pipeline (5)
Solidifying tower (3) is connected；
Burning boiler (1) bottom is provided with burner (6), and its top is provided with chimney (7)；
Knockout tower (2) lower end is provided with reducing motor (8), and the output end of the reducing motor (8) is connected with rotary shaft (9), should
In knockout tower (2) described in the insertion of rotary shaft (9), and several piece scraper plate (10) is provided with described rotary shaft (9).
2. a kind of emulsification, combustion disposes the device of oily sludge according to claim 1, it is characterised in that：Positioned at the burning
Boiler tube (4) spiral in boiler (1) is set.
3. a kind of emulsification, combustion disposes the device of oily sludge according to claim 1, it is characterised in that：The knockout tower
(2) lower portion is tapered, and cone angle is at 60-80 DEG C.
4. a kind of emulsification, combustion disposes the device of oily sludge according to claim 1, it is characterised in that：Described knockout tower
(2) lower section is additionally provided with waste outlet (11).
5. a kind of emulsification, combustion disposes the device of oily sludge according to claim 1, it is characterised in that：Described scraper plate
(10) it is inclined in rotary shaft (9).
6. a kind of emulsification, combustion disposes the device of oily sludge according to claim 1, 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)；The condensing tower (3) is provided with washing section (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621111355.9U CN206188604U (en) | 2016-10-11 | 2016-10-11 | Device that contains oil sludge is dealt with in emulsification burning |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621111355.9U CN206188604U (en) | 2016-10-11 | 2016-10-11 | Device that contains oil sludge is dealt with in emulsification burning |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206188604U true CN206188604U (en) | 2017-05-24 |
Family
ID=58730715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621111355.9U Active CN206188604U (en) | 2016-10-11 | 2016-10-11 | Device that contains oil sludge is dealt with in emulsification burning |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206188604U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106336098A (en) * | 2016-10-11 | 2017-01-18 | 安徽国孚润滑油工业有限公司 | Device and method for emulsifying combustion treatment of oily sludge |
-
2016
- 2016-10-11 CN CN201621111355.9U patent/CN206188604U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106336098A (en) * | 2016-10-11 | 2017-01-18 | 安徽国孚润滑油工业有限公司 | Device and method for emulsifying combustion treatment of oily sludge |
| CN106336098B (en) * | 2016-10-11 | 2023-04-18 | 安徽国孚润滑油工业有限公司 | Device and method for treating oily sludge through emulsification combustion |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Tianjin Guofu Environmental Protection Technology Co.,Ltd. Assignor: ANHUI GUOFU LUBRICANT INDUSTRY Co.,Ltd. Contract record no.: X2020340000009 Denomination of utility model: A device for treating oily sludge by emulsion combustion Granted publication date: 20170524 License type: Common License Record date: 20201223 |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
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. |