CN206063973U - A kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus - Google Patents
A kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus Download PDFInfo
- Publication number
- CN206063973U CN206063973U CN201621071862.4U CN201621071862U CN206063973U CN 206063973 U CN206063973 U CN 206063973U CN 201621071862 U CN201621071862 U CN 201621071862U CN 206063973 U CN206063973 U CN 206063973U
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- Prior art keywords
- waste gas
- outlet
- pipeline
- heat exchanger
- activity charcoal
- 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
- 239000010802 sludge Substances 0.000 title claims abstract description 20
- 230000004913 activation Effects 0.000 title claims abstract description 17
- 239000003292 glue Substances 0.000 title claims abstract description 13
- 238000002360 preparation method Methods 0.000 title claims abstract description 13
- 230000008929 regeneration Effects 0.000 title claims abstract description 13
- 238000011069 regeneration method Methods 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000002912 waste gas Substances 0.000 claims abstract description 52
- 239000007789 gas Substances 0.000 claims abstract description 35
- 238000001816 cooling Methods 0.000 claims abstract description 33
- 239000007921 spray Substances 0.000 claims abstract description 33
- 239000003610 charcoal Substances 0.000 claims abstract description 32
- 230000000694 effects Effects 0.000 claims abstract description 32
- 238000001179 sorption measurement Methods 0.000 claims abstract description 31
- 230000005484 gravity Effects 0.000 claims abstract description 20
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 20
- 230000003647 oxidation Effects 0.000 claims abstract description 18
- 230000003197 catalytic effect Effects 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000002699 waste material Substances 0.000 claims abstract description 15
- 239000012530 fluid Substances 0.000 claims abstract description 9
- 239000013589 supplement Substances 0.000 claims abstract description 4
- 239000000428 dust Substances 0.000 claims description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims 1
- 238000001994 activation Methods 0.000 abstract description 14
- 238000004064 recycling Methods 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract 1
- 229920001971 elastomer Polymers 0.000 description 8
- 239000005060 rubber Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000004332 deodorization Methods 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 229920002209 Crumb rubber Polymers 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Treating Waste Gases (AREA)
Abstract
A kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus, it is characterized in, gravity settling chamber (1), cooling heat exchanger (2), Water spray tower (3), two-stage water filter (4), photochemical catalytic oxidation deodoriser (5), primary activity charcoal adsorption tower (6), second order activity charcoal adsorption tower (7), chimney (8) are sequentially connected by pipeline；Cooling heat exchanger (2) arranges coil pipe and steam-water separator, and coil inlet is connected with gravity settling chamber (1) waste gas outlet, and hot water outlet is connected with boiler (9) water supplement port, and waste liquid outlet is connected with fluid reservoir (10)；The outlet of Water spray tower (3) bottom waste stream is connected with two-stage water filter (4)；Second order activity charcoal adsorption tower (7) outlet is connected with chimney.The high-temperature odor waste gas produced in oily sludge preparation, regeneration glue activation process are carried out energy recovery recycling by the device, and the harmful substance in waste gas is carried out decomposing, adsorbed, energy-saving and emission-reduction, reduce the pollution to surrounding air.
Description
Technical field
This utility model is related to contained Mud Treatment Technology field, and in particular to a kind of oily sludge prepares reclaimed rubber activation
Exhaust-gas treatment simultaneously carries out the device of recycling to its heat energy.
Background technology
Oily sludge is produced in oil development, transport, refining and sewage disposal process, and oily sludge composition is multiple
It is miscellaneous, containing a large amount of aged crude oils, waxiness, asphalitine, colloid, solid suspension, antibacterial, salt, sour gas, corrosion product
Deng greasy filth has been put into National Hazard garbage register.The application of greasy filth and processing method are globe petroleum industry environmental conservation
During relatively scabrous problem, air storage can take a large amount of soils, and the harmful substance which contains can severe contamination water, soil
Earth and air, deteriorate ecological environment.
Oily sludge prepare reclaimed rubber technology be oily sludge is cleaned after, with junked tire powder, sebific duct powder, rubber overshoes powder etc.
Activation desulfurization is carried out in being mixed to join crumb rubber activation tank according to a certain percentage, the activated rubber powder of different quality, Jing refinings is formed
Into the reclaimed rubber film of different-thickness.Further kneaded and vulcanized and can also be made the rubbers such as highway deceleration strip, it is real
The recycling of existing waste.But, substantial amounts of high temperature stench harmful gass can be produced in activation sweetening process, it is directly outer to arrange
A large amount of heat energy can be wasted and secondary pollution is caused to atmospheric environment.
The content of the invention
The technical problems to be solved in the utility model is generation in existing oily sludge preparation, regeneration glue activation sweetening process
A large amount of high temperature stench harmful gass, direct outer row can waste a large amount of heat energy and serious secondary pollution is caused to air.
For above-mentioned technical problem, the technical scheme adopted by this utility model for：
A kind of oily sludge preparation, regeneration glue activates exhaust-gas treatment and heat-energy recovering apparatus, including gravity settling chamber, cooling are changed
Hot device, Water spray tower, two-stage water filter, photochemical catalytic oxidation deodoriser, primary activity charcoal adsorption tower, the absorption of second order activity charcoal
Tower, chimney, boiler, fluid reservoir.Exhaust gas entrance is wherein set on the left of gravity settling chamber, and right side arranges waste gas outlet, and bottom is arranged
Dust outlet, gravity settling chamber waste gas outlet are connected with cooling heat exchanger coil pipe exhaust gas entrance by pipeline；Cooling heat exchanger sets
Coil pipe is put, cooling heat exchanger waste gas outlet is connected with Water spray tower exhaust gas entrance by pipeline；Water spray tower is provided with top
Waste gas outlet, Water spray tower waste gas outlet are connected with photochemical catalytic oxidation deodoriser exhaust gas entrance by pipeline；Photocatalytic-oxidation is eliminated
Waste gas outlet is provided with the left of smelly device, photochemical catalytic oxidation deodoriser waste gas outlet is by pipeline and primary activity charcoal adsorption tower waste gas
Entrance connects；Primary activity charcoal adsorption tower arranges waste gas outlet at top, and primary activity charcoal adsorption tower waste gas outlet passes through pipeline
It is connected with second order activity charcoal adsorption tower exhaust gas entrance；Second order activity charcoal adsorption tower arranges waste gas outlet, second order activity charcoal at top
Adsorption tower waste gas enters air by chimney.
Cooling heat exchanger bottom arranges cold water inlet, and top arranges hot water outlet, and cooling heat exchanger hot water outlet is by pipe
Road is connected with boiler replenishing water mouth；Cooling heat exchanger arranges steam-water separator, and cooling heat exchanger waste liquid outlet passes through pipeline and liquid storage
Tank connects.
Water spray tower is provided with waste liquid outlet in bottom left, and Water spray tower waste liquid outlet is by pipeline and two-stage water filtration
Device entrance connects；Two-stage water filter liquid outlet is connected with Water spray tower spray equipment by pipeline.
When processing waste gas, activation high-temp waste gas initially enter gravity settling chamber, and big dust particle is carried out by action of gravity
Sedimentation, by arranging outside gravity settling chamber outlet at bottom, the waste gas after separation enters cooling heat exchanger to dust.Waste gas is changed into cooling
Fully exchange heat with cooling water after hot device, the hot water after heat exchange carries out moisturizing to boiler into boiler replenishing water mouth, it is useless after heat exchange
The steam-water separator that gas is entered in cooling heat exchanger, the waste liquid after separation are stored and are carried out at next step sewage into fluid reservoir
Reason, the waste gas after separation enter Water spray tower.Waste gas is further purified after entering Water spray tower, and the waste water after use enters two-stage
Water filter, water after filtering reuse spray, and the waste gas after further purifying enters photochemical catalytic oxidation deodoriser；Into
The gas of photochemical catalytic oxidation deodoriser fully decomposes, deodorization, purified gas sequentially enter primary activity charcoal adsorption tower, two grades
Activated carbon adsorber；Pass through to arrange outside chimney through the purification gas of two-stage activated carbon adsorber.
Oily sludge preparation, regeneration glue activation exhaust-gas treatment of the present utility model and heat-energy recovering apparatus, by oily sludge system again
The high temperature stench harmful exhaust produced in rubber activation sweetening process carries out photochemical catalytic oxidation decomposition, absorption so as to reach country
With industry emission request, and recycling is carried out to heat energy, energy-saving and emission-reduction reduce secondary pollution.
Description of the drawings
Fig. 1 is the schematic diagram that this utility model oily sludge preparation, regeneration glue activates exhaust-gas treatment and heat-energy recovering apparatus.
In figure, 1 --- gravity settling chamber；2 --- cooling heat exchanger；3 --- Water spray tower；4 --- two-stage water filter；
5 --- photochemical catalytic oxidation deodoriser；6 --- primary activity charcoal adsorption tower；7 --- second order activity charcoal adsorption tower；8 --- chimney；
9 --- boiler；10 --- fluid reservoir.
Specific embodiment
With reference to the accompanying drawings and examples this utility model is illustrated, but this utility model is not by following embodiments
Limit.
A kind of oily sludge preparation, regeneration glue activates exhaust-gas treatment and heat-energy recovering apparatus, including gravity settling chamber 1, cooling are changed
Hot device 2, Water spray tower 3, two-stage water filter 4, photochemical catalytic oxidation deodoriser 5, primary activity charcoal adsorption tower 6, second order activity charcoal
Adsorption tower 7, chimney 8, boiler 9, fluid reservoir 10.Exhaust gas entrance is wherein set on the left of gravity settling chamber 1, and right side arranges waste gas and goes out
Mouthful, bottom arranges dust outlet, and 1 waste gas outlet of gravity settling chamber is connected with 2 coil pipe exhaust gas entrance of cooling heat exchanger by pipeline；
Cooling heat exchanger 2 arranges coil pipe, and 2 waste gas outlet of cooling heat exchanger is connected with 3 exhaust gas entrance of Water spray tower by pipeline；Water spray
Tower 3 is provided with waste gas outlet at top, and 3 waste gas outlet of Water spray tower is by pipeline and 5 exhaust gas entrance of photochemical catalytic oxidation deodoriser
Connection；Be provided with waste gas outlet on the left of photochemical catalytic oxidation deodoriser 5,5 waste gas outlet of photochemical catalytic oxidation deodoriser by pipeline with
6 exhaust gas entrance of primary activity charcoal adsorption tower connects；Primary activity charcoal adsorption tower 6 arranges waste gas outlet, primary activity charcoal at top
6 waste gas outlet of adsorption tower is connected with 7 exhaust gas entrance of second order activity charcoal adsorption tower by pipeline；Second order activity charcoal adsorption tower 7 is on top
Portion arranges waste gas outlet, and 7 waste gas of second order activity charcoal adsorption tower enters air by chimney 8.
2 bottom of cooling heat exchanger arranges cold water inlet, and top arranges hot water outlet, and 2 hot water outlet of cooling heat exchanger passes through
Pipeline is connected with 9 water supplement port of boiler；Cooling heat exchanger 2 arrange steam-water separator, 2 waste liquid outlet of cooling heat exchanger by pipeline with
Fluid reservoir 10 connects.
Water spray tower 3 is provided with waste liquid outlet in bottom left, and 3 waste liquid outlet of Water spray tower is by pipeline and two-stage water mistake
4 entrance of filter connects；4 liquid outlet of two-stage water filter is connected with 3 spray equipment of Water spray tower by pipeline.
When processing waste gas, activation high-temp waste gas initially enter gravity settling chamber 1, and big dust particle is carried out by action of gravity
Sedimentation, by arranging outside 1 outlet at bottom of gravity settling chamber, the waste gas after separation enters cooling heat exchanger 2 to dust.Waste gas enters cooling
Fully exchange heat with cooling water after heat exchanger 2, the hot water after heat exchange carries out moisturizing to boiler into 9 water supplement port of boiler, after heat exchange
The steam-water separator that enters in cooling heat exchanger 2 of waste gas, the waste liquid after separation stores into fluid reservoir 10 and carries out next step
Sewage disposal, the waste gas after separation enter Water spray tower 3.Waste gas is further purified after entering Water spray tower 3, the waste water after use
Into two-stage water filter 4, water after filtering reuses spray, and the waste gas after further purifying is eliminated into photocatalytic-oxidation
Smelly device 5；Into photochemical catalytic oxidation deodoriser 5 gas fully decompose, deodorization, purified gas sequentially enters primary activity charcoal
Adsorption tower 6, second order activity charcoal adsorption tower 7；Arrange by chimney 8 is outer through the purification gas of two-stage activated carbon adsorber.
Oily sludge preparation, regeneration glue activation exhaust-gas treatment of the present utility model and heat-energy recovering apparatus, by oily sludge system again
The high temperature stench harmful exhaust produced in rubber activation sweetening process carries out photochemical catalytic oxidation decomposition, absorption so as to reach country
With industry emission request, and recycling is carried out to heat energy, energy-saving and emission-reduction reduce secondary pollution.
Claims (3)
1. a kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus, including gravity settling chamber (1), cooling are changed
Hot device (2), Water spray tower (3), two-stage water filter (4), photochemical catalytic oxidation deodoriser (5), primary activity charcoal adsorption tower (6),
Second order activity charcoal adsorption tower (7), chimney (8), boiler (9), fluid reservoir (10), it is characterised in that：
Exhaust gas entrance is set on the left of the gravity settling chamber (1), waste gas outlet is set on the right side of the gravity settling chamber (1), it is described
Gravity settling chamber (1) bottom arranges dust outlet, and gravity settling chamber (1) waste gas outlet passes through pipeline and cooling heat exchanger
(2) coil pipe exhaust gas entrance connection；
The cooling heat exchanger (2) arranges coil pipe, and cooling heat exchanger (2) waste gas outlet passes through pipeline and the Water spray tower (3)
Exhaust gas entrance connects；
The Water spray tower (3) is provided with waste gas outlet at top, and Water spray tower (3) waste gas outlet is urged with the light by pipeline
Change oxidation deodoriser (5) exhaust gas entrance connection；
Waste gas outlet is provided with the left of the photochemical catalytic oxidation deodoriser (5), photochemical catalytic oxidation deodoriser (5) waste gas outlet passes through
Pipeline is connected with primary activity charcoal adsorption tower (6) exhaust gas entrance；
The primary activity charcoal adsorption tower (6) arranges waste gas outlet at top, and primary activity charcoal adsorption tower (6) waste gas outlet passes through
Pipeline is connected with second order activity charcoal adsorption tower (7) exhaust gas entrance；
The second order activity charcoal adsorption tower (7) arranges waste gas outlet at top, and second order activity charcoal adsorption tower (7) waste gas outlet passes through
Pipeline is connected with the chimney (8) entrance.
2. according to oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus described in claim 1, it is characterised in that：
Cooling heat exchanger (2) bottom arranges cold water inlet, arranges hot water outlet at the top of the cooling heat exchanger (2), cools down
Heat exchanger (2) hot water outlet is connected with the boiler (9) water supplement port by pipeline；The cooling heat exchanger (2) arranges soda pop point
From device, cooling heat exchanger (2) waste liquid outlet is connected with the fluid reservoir (10) by pipeline.
3. according to oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus described in claim 1, it is characterised in that：
The Water spray tower (3) is provided with waste liquid outlet in bottom left, Water spray tower (3) waste liquid outlet by pipeline with it is described
Two-stage water filter (4) entrance connects；Two-stage water filter (4) liquid outlet passes through pipeline and the Water spray tower (3)
Spray equipment connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621071862.4U CN206063973U (en) | 2016-09-22 | 2016-09-22 | A kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621071862.4U CN206063973U (en) | 2016-09-22 | 2016-09-22 | A kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206063973U true CN206063973U (en) | 2017-04-05 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621071862.4U Expired - Fee Related CN206063973U (en) | 2016-09-22 | 2016-09-22 | A kind of oily sludge preparation, regeneration glue activation exhaust-gas treatment and heat-energy recovering apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206063973U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107376576A (en) * | 2017-08-25 | 2017-11-24 | 武汉坤久环保科技有限公司 | A kind of waste gas purification apparatus for amino acid fermentation workshop |
| CN107485996A (en) * | 2017-08-25 | 2017-12-19 | 武汉坤久环保科技有限公司 | A kind of multiplex roles waste gas purification apparatus |
| CN108532200A (en) * | 2018-06-22 | 2018-09-14 | 海盐鸳鸯丝绸印染有限公司 | A kind of environment-friendly type printing and dyeing fabrics shaping equipment |
| CN110201482A (en) * | 2019-06-30 | 2019-09-06 | 河南查瑞特种设备有限公司 | A kind of energy-saving and environment-friendly boiler exhaust gas processing system |
| CN111495086A (en) * | 2020-04-23 | 2020-08-07 | 魏庆 | Steel mill exhaust emission environmental protection processing system |
| CN113521927A (en) * | 2021-08-12 | 2021-10-22 | 南京同诚节能环保装备研究院有限公司 | Method for treating xylene waste gas |
-
2016
- 2016-09-22 CN CN201621071862.4U patent/CN206063973U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107376576A (en) * | 2017-08-25 | 2017-11-24 | 武汉坤久环保科技有限公司 | A kind of waste gas purification apparatus for amino acid fermentation workshop |
| CN107485996A (en) * | 2017-08-25 | 2017-12-19 | 武汉坤久环保科技有限公司 | A kind of multiplex roles waste gas purification apparatus |
| CN107485996B (en) * | 2017-08-25 | 2020-11-13 | 武汉坤久环保科技有限公司 | Multi-interface waste gas purification device |
| CN108532200A (en) * | 2018-06-22 | 2018-09-14 | 海盐鸳鸯丝绸印染有限公司 | A kind of environment-friendly type printing and dyeing fabrics shaping equipment |
| CN110201482A (en) * | 2019-06-30 | 2019-09-06 | 河南查瑞特种设备有限公司 | A kind of energy-saving and environment-friendly boiler exhaust gas processing system |
| CN111495086A (en) * | 2020-04-23 | 2020-08-07 | 魏庆 | Steel mill exhaust emission environmental protection processing system |
| CN113521927A (en) * | 2021-08-12 | 2021-10-22 | 南京同诚节能环保装备研究院有限公司 | Method for treating xylene waste gas |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170405 Termination date: 20180922 |
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| CF01 | Termination of patent right due to non-payment of annual fee |