CN104801115B - Dust pelletizing system containing oil fume - Google Patents
Dust pelletizing system containing oil fume Download PDFInfo
- Publication number
- CN104801115B CN104801115B CN201510154072.6A CN201510154072A CN104801115B CN 104801115 B CN104801115 B CN 104801115B CN 201510154072 A CN201510154072 A CN 201510154072A CN 104801115 B CN104801115 B CN 104801115B
- Authority
- CN
- China
- Prior art keywords
- bucket
- settling vat
- dust
- oil fume
- containing oil
- 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.)
- Expired - Fee Related
Links
- 239000000428 dust Substances 0.000 title claims abstract description 52
- 239000003517 fume Substances 0.000 title claims abstract description 30
- 238000005453 pelletization Methods 0.000 title claims abstract description 29
- 238000009413 insulation Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 description 13
- 230000001174 ascending effect Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000008187 granular material Substances 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000010410 dusting Methods 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
Abstract
A kind of dust pelletizing system containing oil fume, including housing, settling vat, housing includes boring bucket and being positioned at the post bucket at cone bucket top, is surrounded by heat-insulation layer outside cone bucket and post bucket, settling vat bottom opening, top have air outlet, cone bottom of the barrel has dust-exhausting port, and described settling vat is fixed in post bucket, leaves spacing between settling vat and post bucket inwall, this spacing forms circular passage, post bucket sidewall is provided with blast pipe, and blast pipe connects with circular passage, and the inwall of blast pipe is tangent with the inwall of circular passage.The present invention dust pelletizing system containing oil fume, efficiency of dust collection is higher.
Description
Technical field
The present invention relates to a kind of dust pelletizing system, in particular relate to a kind of dust pelletizing system containing oil fume.
Background technology
Oil gas can be present in nature with three kinds of different states of solid, liquid, gas at different temperature.Dust-laden high-temperature gas exists
When during Pipeline transport, temperature reduces, part oil gas can be converted into liquid, and the biggest oil gas of temperature drop is converted into the ratio of liquid
The biggest.If under such condition containing dust in dust-laden high-temperature gas, dust will mix with liquid oil to be bonded to carry manages
On wall, As time goes on the adhesive on tube wall progressively increases, and finally results in that pipeline all blocks and system can not be normal
Work.For avoiding the generation of above-mentioned situation, generally use cyclone dust collector to containing oil fume dedusting, but existing whirlwind
Formula cleaner unit, efficiency of dust collection is relatively low.
Summary of the invention
It is an object of the invention to provide a kind of dust pelletizing system containing oil fume, its efficiency of dust collection is higher.
To achieve these goals, the technical solution of the present invention is: a kind of dust pelletizing system containing oil fume, including housing,
Settling vat, housing includes boring bucket and being positioned at the post bucket at cone bucket top, bores and be surrounded by heat-insulation layer outside bucket and post bucket, settling vat bottom opening,
Top has air outlet, and cone bottom of the barrel has dust-exhausting port, and described settling vat is fixed in post bucket, between settling vat and post bucket inwall
Leaving spacing, this spacing forms circular passage, and post bucket sidewall is provided with blast pipe, and blast pipe connects with circular passage, and enters
The inwall of airduct is tangent with the inwall of circular passage.
This utility model dust pelletizing system containing oil fume, wherein, is provided with deflector bottom described settling vat and between post bottom of the barrel,
Described settling vat bottom interior wall is provided with deflector.
This utility model dust pelletizing system containing oil fume, wherein, also includes temperature control system, and temperature control system includes heating
Device, temperature sensor and temperature-controlled cabinet, heater, temperature sensor be mounted in housing, and temperature-controlled cabinet is installed on shell
External, heater, temperature sensor are all connected with temperature-controlled cabinet.
This utility model dust pelletizing system containing oil fume, wherein, is provided with discharge pipe at described air outlet, the internal diameter of discharge pipe is
D1, discharge pipe end portion is positioned at inside described settling vat, and discharge pipe is positioned at part within settling vat and is positioned at outside settling vat
Partial-length be D1/2.
This utility model dust pelletizing system containing oil fume, wherein, the width of described circular passage is a, the internal diameter of described settling vat
For D2, the diameter D3=D2+2a of described post bucket.
This utility model dust pelletizing system containing oil fume, wherein, a diameter of D4 of described blast pipe, described post bucket height h1=5D4.
This utility model dust pelletizing system containing oil fume, wherein, described settling vat height h2=h1+2a, and described settling vat top
Portion exceeds described post bucket, concordant with described post bucket bottom described settling vat.
This utility model dust pelletizing system containing oil fume, wherein, described cone bucket height h3=2D3.
This utility model dust pelletizing system containing oil fume, wherein, the diameter D4 of described blast pipe and the width a of described circular passage
Ratio be 2.
This utility model dust pelletizing system containing oil fume, wherein, the internal diameter of described discharge pipe is equal with the internal diameter of dust-exhausting port.
After using such scheme, compared with prior art, it is provided with sedimentation in the housing of the dust pelletizing system containing oil fume due to the present invention
Bucket, settling vat is fixed in post bucket, leaves spacing between settling vat and post bucket inwall, and this spacing forms circular passage, therefore may be used
First make dust-contained airflow enter circular passage, and in circular passage, do top-down rotary motion, the dust in dust-contained airflow
Grain falls along cone bucket wall under centrifugal force and action of gravity and discharges from dust-exhausting port, and then the air-flow through rough dusting draws at air-flow
Under the drive of wind, moving to air outlet from bottom to top, a small amount of dust is followed ascending air and is moved upward entrance settling vat, settling vat
Interior wind speed is the lowest, and dust falls under gravity into lower cone bucket and discharges, and separately has the dust that partial particulate is less to continue with rising gas
Stream moves upward, and ascending air still rotates under the effect of deflector, and dust granule is under the influence of centrifugal force to heavy
Fall bucket inwall attachment, is stacked into a certain degree, naturally comes off, and the air-flow containing flue dust is greatly improved through twice dedusting, efficiency of dust collection.
Accompanying drawing explanation
Fig. 1 is the main TV structure schematic diagram that the present invention contains the dust pelletizing system of oil fume；
Fig. 2 is the plan structure schematic diagram that the present invention contains the dust pelletizing system of oil fume.
Detailed description of the invention
As it is shown in figure 1, the dust pelletizing system that the present invention is containing oil fume includes housing 11, settling vat 12, housing 11 includes boring bucket 111
Be positioned at the post bucket 112 at cone bucket 111 top, cone bucket 111 and the outer heat-insulation layer 13 that is all surrounded by of post bucket 112, open bottom cone bucket 111
Having dust-exhausting port 113, settling vat 12 to be arranged in post bucket 112, settling vat 12 top and post bucket 112 fix, bottom is passed through
Six deflectors 17 fix with post bucket 112, and deflector 17 may also be configured to more than six or less than six, settling vat 12 He
Leaving spacing between post bucket 112 inwall, this spacing forms circular passage 14, and settling vat 12 bottom opening, top have air-out
Mouthful, distinguished and admirable rotate according to the mode set for make in entrance housing 11 and settling vat 12, be provided with bottom settling vat 12 inwall
Multiple deflectors, as in figure 2 it is shown, post bucket 112 sidewall is provided with blast pipe 15, blast pipe 15 connects with circular passage 14,
And the inwall of blast pipe 15 is tangent with the inwall of circular passage 14.
During dedusting, first make dust-contained airflow enter circular passage 14 through blast pipe 15, and do top-down in circular passage 14
Rotary motion, the outer wall under the influence of centrifugal force of the dust granules in dust-contained airflow moves, and arrives the dust of outer wall at backspin gas
The common effect of stream and gravity is lower falls along cone bucket 111 wall and discharges from dust-exhausting port 113, and then the air-flow through rough dusting exists
Under the drive of air-flow air inducing, moving to air outlet from bottom to top, a small amount of dust in air-flow is followed ascending air and is moved upward entrance
Settling vat 12, in settling vat 12, wind speed is the lowest, and dust falls under gravity into cone bucket 111 and discharges, and separately has partial particulate relatively
Little dust continues to move upward with ascending air, and ascending air still rotates under the effect of deflector, dust granule
Adhere to settling vat 12 inwall under the influence of centrifugal force, be stacked into a certain degree, naturally come off.
The present invention dust pelletizing system containing oil fume also includes temperature control system, and temperature control system includes heater, temperature sensing
Device and temperature-controlled cabinet, heater, temperature sensor be mounted in housing 11, and temperature-controlled cabinet is installed on outside housing 11,
Owing to containing containing the materials such as oil gas, steam and fuel gas in oil fume, if temperature is too low, some material can turn from gas phase
For liquid phase, cause mobility to decline, and liquid phase substance be combined with dust and can cause dust accumulation, block gas channel, it is impossible to
Normally produce, after adding temperature control system, the material in air-flow can be avoided to liquid-phase conversion from gas phase.Temperature controls
The temperature of system can be set according to flow constituents, and in temperature sensor measurement cleaner unit, actual temperature is transferred to temperature control
Case, temperature-controlled cabinet send the electric power whether heated to heater.
Also being welded with discharge pipe 16 at air outlet, the internal diameter of discharge pipe 16 is D1, and discharge pipe 16 end portion is positioned at settling vat
12 is internal, and the part that discharge pipe 16 is positioned within settling vat 12 is D1/2 with the partial-length being positioned at outside settling vat 12.
The width of circular passage 14 is a, and the internal diameter of settling vat 12 is D2, the diameter D3=D2+2a of post bucket 112, it is ensured that contain
The distinguished and admirable flow velocity in circular passage of dirt, making flow rate set is 15 meter per seconds, and flow velocity is very fast, dust rotation point good dedusting effect, but
Crossing conference and produce turbulent flow, flow velocity size answers column bucket diameter to adjust accordingly.
A diameter of D4 of blast pipe 15, post bucket 112 height h1=5D4, make dust-laden distinguished and admirable between post bucket 112 and settling vat 12
Circular passage rotate four circle, make distinguished and admirable in flue dust fully settle.
Cone bucket 111 height h3=2D3, can prevent the dust settled from being rolled by distinguished and admirable.
It addition, the ratio of the diameter D4 of the blast pipe 15 and width a of circular passage 14 is 2, settling vat 12 height h2=h1+2a,
And settling vat 12 top exceeds post bucket 112, concordant with post bucket 112 bottom settling vat 12, the internal diameter of discharge pipe 16 and dust discharge
The internal diameter of mouthfuls 113 is equal, and in/out air tube diameter press economic velocity and designed, and concordant with post bucket 112 bottom settling vat 12 ensures gas
Stream rotating cycle in circular passage is enough.
Embodiment described above is only to be described the preferred embodiment of the present invention, not limits the scope of the present invention
Fixed, on the premise of designing spirit without departing from the present invention, technical scheme is made by this area ordinary skill technical staff
Various deformation and improvement, all should fall in the protection domain that claims of the present invention determines.
Claims (7)
1. the dust pelletizing system containing oil fume, it is characterised in that: include housing (11), settling vat (12), housing (11)
Including boring bucket (111) and being positioned at the post bucket (112) at cone bucket (111) top, cone bucket (111) and post bucket (112)
Being surrounded by outward heat-insulation layer (13), settling vat (12) bottom opening, top have air outlet, cone bucket (111) bottom
Having dust-exhausting port (113), described settling vat (12) is fixed in post bucket (112), settling vat (12) and post bucket
(112) leave spacing between inwall, this spacing formed circular passage (14), post bucket (112) sidewall be provided with into
Airduct (15), blast pipe (15) connects with circular passage (14), and the inwall of blast pipe (15) is with annular
The inwall of passage (14) is tangent, and the width of described circular passage (14) is a, the internal diameter of described settling vat (12)
For D2, the diameter D3=D2+2a of described post bucket (112), a diameter of D4 of described blast pipe (15), described post
Bucket (112) highly h1=5D4, described settling vat (12) highly h2=h1+2a, and described settling vat (12) top
Portion exceeds described post bucket (112), and described settling vat (12) bottom is concordant with described post bucket (112).
2. the dust pelletizing system containing oil fume as claimed in claim 1, it is characterised in that: described settling vat (12) bottom and post
Bucket (112) is provided with deflector (17) between bottom, and described settling vat (12) bottom interior wall is provided with deflector.
3. the dust pelletizing system containing oil fume as claimed in claim 2, it is characterised in that: also include temperature control system, temperature
Control system includes that heater, temperature sensor and temperature-controlled cabinet, heater, temperature sensor are mounted on housing
(11) in, temperature-controlled cabinet is installed on housing (11) outward, heater, temperature sensor all with temperature-controlled cabinet phase
Connect.
4. the dust pelletizing system containing oil fume as claimed in claim 3, it is characterised in that: at described air outlet, discharge pipe is installed
(16), the internal diameter of discharge pipe (16) is D1, and discharge pipe (16) end portion is positioned at described settling vat (12)
Inside, the part that discharge pipe (16) is positioned at the internal part of settling vat (12) outside with being positioned at settling vat (12) is long
Degree is D1/2.
5. the dust pelletizing system containing oil fume as claimed in claim 4, it is characterised in that: described cone bucket (111) highly h3=2D3.
6. the dust pelletizing system containing oil fume as claimed in claim 5, it is characterised in that: the diameter of described blast pipe (15)
D4 is 2 with the ratio of the width a of described circular passage (14).
7. the dust pelletizing system containing oil fume as claimed in claim 6, it is characterised in that: the internal diameter of described discharge pipe (16) with
The internal diameter of dust-exhausting port (113) is equal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510154072.6A CN104801115B (en) | 2015-04-02 | 2015-04-02 | Dust pelletizing system containing oil fume |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510154072.6A CN104801115B (en) | 2015-04-02 | 2015-04-02 | Dust pelletizing system containing oil fume |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104801115A CN104801115A (en) | 2015-07-29 |
| CN104801115B true CN104801115B (en) | 2016-09-28 |
Family
ID=53686571
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510154072.6A Expired - Fee Related CN104801115B (en) | 2015-04-02 | 2015-04-02 | Dust pelletizing system containing oil fume |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104801115B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111804521B (en) * | 2020-07-28 | 2021-05-14 | 苏州绿萃筑信息科技有限公司 | Insulating paper processing is with gluing stick |
| CN112121540A (en) * | 2020-09-22 | 2020-12-25 | 邵阳县坪峰生态油茶专业合作社 | Multi-functional ecological oil cyclone |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102407058A (en) * | 2010-09-20 | 2012-04-11 | 何润岚 | High-efficiency spiral deduster |
| CN203235344U (en) * | 2013-04-02 | 2013-10-16 | 嘉兴逸镁节能科技有限公司 | Cyclone dust removal device |
| CN103977638A (en) * | 2014-03-06 | 2014-08-13 | 安徽博瑞特热能设备股份有限公司 | Self-dedusting economizer |
| CN204017542U (en) * | 2014-08-11 | 2014-12-17 | 扬州金圆化工设备有限公司 | A kind of cyclone dust collectors |
| CN204709954U (en) * | 2015-04-02 | 2015-10-21 | 龙口市中晟新能源科技开发有限公司 | Containing the dust pelletizing system of oil fume |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1279869C (en) * | 2002-04-28 | 2006-10-18 | 苏州金莱克清洁器具有限公司 | Speed reducing centrifugal duster for cleaner |
-
2015
- 2015-04-02 CN CN201510154072.6A patent/CN104801115B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102407058A (en) * | 2010-09-20 | 2012-04-11 | 何润岚 | High-efficiency spiral deduster |
| CN203235344U (en) * | 2013-04-02 | 2013-10-16 | 嘉兴逸镁节能科技有限公司 | Cyclone dust removal device |
| CN103977638A (en) * | 2014-03-06 | 2014-08-13 | 安徽博瑞特热能设备股份有限公司 | Self-dedusting economizer |
| CN204017542U (en) * | 2014-08-11 | 2014-12-17 | 扬州金圆化工设备有限公司 | A kind of cyclone dust collectors |
| CN204709954U (en) * | 2015-04-02 | 2015-10-21 | 龙口市中晟新能源科技开发有限公司 | Containing the dust pelletizing system of oil fume |
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| Publication number | Publication date |
|---|---|
| CN104801115A (en) | 2015-07-29 |
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| EXSB | Decision made by sipo to initiate substantive examination | ||
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| C14 | Grant of patent or utility model | ||
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| TR01 | Transfer of patent right |
Effective date of registration: 20180528 Address after: 265700 No. 369 Zhenxing South Road, Longkou City, Yantai, Shandong Patentee after: Zhang Chuanguo Address before: 265700 Meng Jia village, Longkou City Longgang street, Yantai, Shandong Patentee before: Longkou City Zhong Sheng new forms of energy Science and Technology Development Co., Ltd. |
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| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160928 Termination date: 20180402 |
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| CF01 | Termination of patent right due to non-payment of annual fee |