CN106524182A - Treatment device and method for high-content petroleum hydrocarbon sewage - Google Patents
Treatment device and method for high-content petroleum hydrocarbon sewage Download PDFInfo
- Publication number
- CN106524182A CN106524182A CN201610885379.8A CN201610885379A CN106524182A CN 106524182 A CN106524182 A CN 106524182A CN 201610885379 A CN201610885379 A CN 201610885379A CN 106524182 A CN106524182 A CN 106524182A
- Authority
- CN
- China
- Prior art keywords
- heat pipe
- petroleum hydrocarbon
- sewage
- combustion furnace
- gas
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 38
- 239000003209 petroleum derivative Substances 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 9
- 238000002485 combustion reaction Methods 0.000 claims abstract description 44
- 230000000694 effects Effects 0.000 claims abstract description 4
- 230000008020 evaporation Effects 0.000 claims abstract description 4
- 238000001704 evaporation Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 27
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 18
- 238000012545 processing Methods 0.000 claims description 11
- 239000003345 natural gas Substances 0.000 claims description 9
- 238000003672 processing method Methods 0.000 claims description 7
- 238000005507 spraying Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000007667 floating Methods 0.000 claims description 3
- 230000002706 hydrostatic effect Effects 0.000 claims description 3
- 238000003973 irrigation Methods 0.000 claims description 3
- 230000002262 irrigation Effects 0.000 claims description 3
- 239000003921 oil Substances 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 239000003570 air Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009471 action Effects 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
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/008—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for liquid waste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/05—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste oils
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/60—Separating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2204/00—Supplementary heating arrangements
- F23G2204/10—Supplementary heating arrangements using auxiliary fuel
- F23G2204/103—Supplementary heating arrangements using auxiliary fuel gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/10—Liquid waste
Abstract
The invention discloses a treatment device for high-content petroleum hydrocarbon sewage. The treatment device for high-content petroleum hydrocarbon sewage comprises a combustion furnace, a heat pipe and a heat pipe boiler, wherein the output end of the combustion furnace is connected with the evaporation heat-absorbing end of the heat pipe, the heat pipe boiler is arranged over the heat pipe, and a steam pocket is arranged above the heat pipe boiler. The invention further discloses a treatment method for high-content petroleum hydrocarbon sewage. According to the treatment device and method for high-content petroleum hydrocarbon sewage, the structure is simple and reliable, the cost is low, and the safety is high; and oil and gas are utilized during double return strokes, so that the energy utilization rate is greatly increased, and the energy-saving effect is achieved accordingly.
Description
Technical field
A kind of the present invention relates to chemical industry hydro carbons processing meanss and method, more particularly to process of high-load petroleum hydrocarbon sewage
Device and its processing method.
Background technology
As oil exploitation and the fast development of petrochemical processing industry, various petroleum hydrocarbon class pollutants are increasing, these contain
There is the dustiness of the waste water of petroleum hydrocarbon, sludge very high, if after being directly entered air, soil, water system, will produce to environment tight
Endanger again.Although the processing method at present to oily waste, all make substantial amounts of research both at home and abroad, traditional physics,
Physical chemistry, chemistry, electrochemical method can not all reach to the sewage and sludge in waste petroleum efficiently, it is complete, without secondary dirt
The process of dye.
The content of the invention
The present invention is for avoiding the weak point existing for above-mentioned prior art, there is provided a kind of high-load petroleum hydrocarbon sewage
Processing meanss and its processing method.
The technical proposal for solving the technical problem of the invention is：
A kind of processing meanss of high-load petroleum hydrocarbon sewage, it includes combustion furnace, heat pipe and heat pipe boiler, described combustion
Burn stove output end to connect with the evaporation endothermic end of heat pipe, described heat pipe boiler is arranged on above heat pipe, on the heat pipe boiler
Side is provided with drum；
Described drum is provided with the first pipeline, second pipe and the 3rd pipeline, first pipeline and second pipe point
It is not connected with described heat pipe boiler, is connected with combustion furnace in the 3rd described pipeline；
The 4th pipeline is provided with above the heat pipe boiler side, and the other end of the 4th pipeline is connected with combustion furnace,
Sewage inlet is additionally provided with described heat pipe boiler；
The heat pipe is provided with gas discharge outlet.
Further, toroidal combustion chamber is provided with described combustion furnace.
Further, gas spraying loophole is additionally provided with described combustion furnace.
Further, first pipeline is located at the lower section of drum, and inserts in heat pipe boiler, and the lower end of the first pipeline is leaned on
The inner bottom part of near-thermal pipe boiler.
Further, fin is respectively equipped with described heat pipe and heat pipe boiler.
Further, storage bin and high-pressure pump are additionally provided with the 4th pipeline.
The invention also discloses a kind of processing method of high-load petroleum hydrocarbon sewage, which comprises the following steps that：
Step 1, the sewage inlet by high-load petroleum hydrocarbon sewage from heat pipe boiler are transported in heat pipe boiler；
Step 2, by gas spraying loophole to burning furnace injection natural gas, make natural gas in combustion furnace annular combustion
Burn interior to be burnt；
Step 3, the burning gases with heat are transported in heat pipe from combustion furnace, and the high-load stone in opposite heat tube boiler
Petroleum hydrocarbon class sewage is heated；
Step 4, high-load petroleum hydrocarbon sewage seethe with excitement when, many micro-bubbles can be formed, under bubble constitute water,
Gas, oil droplet three-phase heterodisperse system, form gas-oil droplet knot in the presence of interfacial tension, bubble floating power and hydrostatic pressure difference
It is fit to float, and flowed in storage bin, under high pressure pumping action by the 4th pipeline, gas-oil droplet combination is sprayed into into combustion furnace
Inside burnt；
Gas pearl in step 5, step 4 then can be led in drum by second pipe, now can produce in drum gas and
The globule, wherein gas are led in combustion furnace by the 3rd pipeline and natural gas mixed combustion, and the globule is then led to by the first pipeline
Heated in heat pipe boiler again；
Step 6, complete step 4 and the sewage after step 5 can be directly used for field irrigation.
Further, the temperature control in described combustion furnace is at 700 DEG C -900 DEG C.
Further, the air pressure in the drum is in 0.2-1.2MPa.
Further, the temperature in the heat pipe boiler is at 120 DEG C -150 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, using double back journey (all the way by oil recycling, Ling Yilu
By Gas recovery) by the utilization of oil and gas, so as to substantially increase the utilization of the energy, so as to realize energy-saving effect.
Description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is gas and water of the present invention, oil moves towards schematic diagram.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the present invention is realized are easy to understand, tie below
Conjunction is specifically illustrating, and the present invention is expanded on further.
As shown in Figure 1-2, a kind of processing meanss of high-load petroleum hydrocarbon sewage, it includes combustion furnace 1, heat pipe 2 and heat
Pipe boiler 3, described 1 output end of combustion furnace are connected with the evaporation endothermic end of heat pipe 2, and described heat pipe boiler 3 is arranged on heat pipe 2
Top, is provided with drum 4 above the heat pipe boiler 3；
Described drum 4 is provided with the first pipeline 40, second pipe 41 and the 3rd pipeline 42, first pipeline 40 and
Two pipelines 41 are connected with described heat pipe boiler 3 respectively, are connected with combustion furnace 1 in the 3rd described pipeline 42；
The 4th pipeline 30 is provided with above 3 side of the heat pipe boiler, and the other end of the 4th pipeline 30 is connected with combustion furnace 1
Connect, sewage inlet 31 is additionally provided with described heat pipe boiler 3；
The heat pipe 2 is provided with gas discharge outlet 20.
Toroidal combustion chamber 100 is provided with described combustion furnace 1.
Gas spraying loophole 101 is additionally provided with described combustion furnace 1.
First pipeline 40 is located at the lower section of drum 4, and inserts in heat pipe boiler 3, and the lower end of the first pipeline 40 is leaned on
The inner bottom part of near-thermal pipe boiler 3.
Fin 5 is respectively equipped with described heat pipe 2 and heat pipe boiler 3.
Storage bin 6 and high-pressure pump 7 are additionally provided with 4th pipeline 30.
A kind of processing method of high-load petroleum hydrocarbon sewage, which comprises the following steps that：
Step 1, the sewage inlet 31 by high-load petroleum hydrocarbon sewage from heat pipe boiler 3 are transported in heat pipe boiler 3；
Step 2, natural gas is sprayed by gas spraying loophole 101 into combustion furnace 1, make natural gas in combustion furnace 1
Burnt in toroidal combustion chamber 100；
Step 3, the burning gases with heat are transported in heat pipe 2 from combustion furnace 1, and the height in opposite heat tube boiler 3 contains
Amount petroleum hydrocarbon sewage is heated；
Step 4, high-load petroleum hydrocarbon sewage seethe with excitement when, many micro-bubbles can be formed, under bubble constitute water,
Gas, oil droplet three-phase heterodisperse system, form gas-oil droplet knot in the presence of interfacial tension, bubble floating power and hydrostatic pressure difference
It is fit to float, and flowed in storage bin 6 by the 4th pipeline 30, in the case where high-pressure pump 7 is acted on, gas-oil droplet combination is sprayed into into combustion
Burn in stove 1 and burnt；
Gas pearl in step 5, step 4 then can be led in drum 4 by second pipe 41, now can produce gas in drum 4
Body and the globule, wherein gas are led in combustion furnace 1 by 42 road of the 3rd pipe and natural gas mixed combustion, and the globule then passes through first pipe
Road 40 leads in heat pipe boiler 3 and heats again；
Step 6, complete step 4 and the sewage after step 5 can be directly used for field irrigation.
Temperature control in described combustion furnace 1 is at 700 DEG C -900 DEG C.Air pressure in the drum 4 is in 0.2-1.2MPa.
Temperature in the heat pipe boiler 3 is at 120 DEG C -150 DEG C.
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 original for simply illustrating the present invention described in above-described embodiment and specification
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.The claimed scope of the invention is by appending claims and its equivalent circle.
It is fixed.
Claims (10)
1. a kind of processing meanss of high-load petroleum hydrocarbon sewage, it includes combustion furnace (1), heat pipe (2) and heat pipe boiler (3),
It is characterized in that：Described combustion furnace (1) output end is connected with the evaporation endothermic end of heat pipe (2), and described heat pipe boiler (3) sets
Put above heat pipe (2), above heat pipe boiler (3), be provided with drum (4)；
Described drum (4) is provided with the first pipeline (40), second pipe (41) and the 3rd pipeline (42), first pipeline
(40) it is connected with described heat pipe boiler (3) with second pipe (41) respectively, in the 3rd described pipeline (42) and combustion furnace
(1) it is connected；
The 4th pipeline (30), the other end and the combustion furnace (1) of the 4th pipeline (30) is provided with above heat pipe boiler (3) side
Be connected, sewage inlet (31) is additionally provided with described heat pipe boiler (3)；
Heat pipe (2) are provided with gas discharge outlet (20).
2. a kind of disposal plant of high-load petroleum hydrocarbon sewage according to claim 1, it is characterised in that：Described burning
Toroidal combustion chamber (100) is provided with stove (1).
3. a kind of processing meanss of high-load petroleum hydrocarbon sewage according to claim 1, it is characterised in that：Described burning
Gas spraying loophole (101) is additionally provided with stove (1).
4. a kind of processing meanss of high-load petroleum hydrocarbon sewage according to claim 1, it is characterised in that：The first pipe
Road (40) is located at the lower section of drum (4), and inserts in heat pipe boiler (3), and the lower end of the first pipeline (40) is near heat pipe boiler
(3) inner bottom part.
5. processing meanss of a kind of high-load petroleum hydrocarbon sewage and sludge according to claim 1, it is characterised in that：It is described
Heat pipe (2) and heat pipe boiler (3) on be respectively equipped with fin (5).
6. a kind of processing meanss of high-load petroleum hydrocarbon sewage according to claim 1, it is characterised in that：4th pipe
Storage bin (6) and high-pressure pump (7) is additionally provided with road (30).
7. a kind of using a kind of processing method of high-load petroleum hydrocarbon sewage as described in claim 1-6, it is characterised in that its
Comprise the following steps that：
Step 1, the sewage inlet (31) by high-load petroleum hydrocarbon sewage from heat pipe boiler (3) are transported to heat pipe boiler (3)
It is interior；
Step 2, by gas spraying loophole (101) to injection natural gas in combustion furnace (1), make natural gas in combustion furnace (1)
Toroidal combustion chamber (100) in burnt；
Step 3, the burning gases with heat are transported in heat pipe (2) from combustion furnace (1), and the height in opposite heat tube boiler (3)
Content petroleum hydrocarbon sewage is heated；
Step 4, high-load petroleum hydrocarbon sewage seethe with excitement when, many micro-bubbles can be formed, under bubble constitute water, gas,
Oil droplet three-phase heterodisperse system, forms gas-oil droplet combination in the presence of interfacial tension, bubble floating power and hydrostatic pressure difference
Float, and flowed in storage bin (6) by the 4th pipeline (30), under high-pressure pump (7) effect, gas-oil droplet combination is sprayed into
Burnt in combustion furnace (1)；
Gas pearl in step 5, step 4 then can be led in drum (4) by second pipe (41), now can produce in drum (4)
Gas and the globule, wherein gas are led in combustion furnace (1) and natural gas mixed combustion by the 3rd pipe (42) road, and the globule then passes through
First pipeline (40) leads to；
Step 6, complete step 4 and the sewage after step 5 can be directly used for field irrigation.
8. method according to claim 7, it is characterised in that：Temperature control in described combustion furnace (1) 700 DEG C-
900℃。
9. method according to claim 7, it is characterised in that：Air pressure in drum (4) is in 0.2-1.2MPa.
10. method according to claim 7, it is characterised in that：Temperature in heat pipe boiler (3) is at 120 DEG C -150
℃。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610885379.8A CN106524182B (en) | 2016-10-11 | 2016-10-11 | A kind of processing unit and its processing method of high-content petroleum hydrocarbon sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610885379.8A CN106524182B (en) | 2016-10-11 | 2016-10-11 | A kind of processing unit and its processing method of high-content petroleum hydrocarbon sewage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106524182A true CN106524182A (en) | 2017-03-22 |
| CN106524182B CN106524182B (en) | 2019-04-02 |
Family
ID=58331192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610885379.8A Active CN106524182B (en) | 2016-10-11 | 2016-10-11 | A kind of processing unit and its processing method of high-content petroleum hydrocarbon sewage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106524182B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6470180A (en) * | 1987-09-10 | 1989-03-15 | Mitsubishi Heavy Ind Ltd | Waste water treatment |
| JPH02118311A (en) * | 1988-10-27 | 1990-05-02 | Ishikawajima Harima Heavy Ind Co Ltd | Waste oil combustion furnace |
| CN1045962A (en) * | 1989-03-02 | 1990-10-10 | 格哈特·施米特 | Device for dehydration of sewage sludge |
| JP2001104939A (en) * | 1999-10-07 | 2001-04-17 | Nichibaku:Kk | Method for cleaning wastewater |
| CN1367344A (en) * | 2002-02-05 | 2002-09-04 | 广西绿洲热能设备有限公司 | Hot-pipe type organic waste liquor treatment system |
| CN101290121A (en) * | 2007-04-18 | 2008-10-22 | 深圳市环源科技发展有限公司 | Wet sludge anhydration burning processing system and process |
| CN204939165U (en) * | 2015-07-30 | 2016-01-06 | 天津霍普环保科技有限公司 | A kind of purifying processing device of high salt organic waste water |
| CN206191605U (en) * | 2016-10-11 | 2017-05-24 | 安徽国孚润滑油工业有限公司 | Processing apparatus of high -load oil hydro carbons sewage |
-
2016
- 2016-10-11 CN CN201610885379.8A patent/CN106524182B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6470180A (en) * | 1987-09-10 | 1989-03-15 | Mitsubishi Heavy Ind Ltd | Waste water treatment |
| JPH02118311A (en) * | 1988-10-27 | 1990-05-02 | Ishikawajima Harima Heavy Ind Co Ltd | Waste oil combustion furnace |
| CN1045962A (en) * | 1989-03-02 | 1990-10-10 | 格哈特·施米特 | Device for dehydration of sewage sludge |
| JP2001104939A (en) * | 1999-10-07 | 2001-04-17 | Nichibaku:Kk | Method for cleaning wastewater |
| CN1367344A (en) * | 2002-02-05 | 2002-09-04 | 广西绿洲热能设备有限公司 | Hot-pipe type organic waste liquor treatment system |
| CN101290121A (en) * | 2007-04-18 | 2008-10-22 | 深圳市环源科技发展有限公司 | Wet sludge anhydration burning processing system and process |
| CN204939165U (en) * | 2015-07-30 | 2016-01-06 | 天津霍普环保科技有限公司 | A kind of purifying processing device of high salt organic waste water |
| CN206191605U (en) * | 2016-10-11 | 2017-05-24 | 安徽国孚润滑油工业有限公司 | Processing apparatus of high -load oil hydro carbons sewage |
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| Publication number | Publication date |
|---|---|
| CN106524182B (en) | 2019-04-02 |
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Application publication date: 20170322 Assignee: Tianjin Guofu Environmental Protection Technology Co.,Ltd. Assignor: ANHUI GUOFU LUBRICANT INDUSTRY Co.,Ltd. Contract record no.: X2020340000009 Denomination of invention: A device for treating wastewater containing high content of petroleum hydrocarbon and its treatment method Granted publication date: 20190402 License type: Common License Record date: 20201223 |
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Application publication date: 20170322 Assignee: Suzhou zeneng Environmental Protection Technology Co.,Ltd. Assignor: ANHUI GUOFU LUBRICANT INDUSTRY Co.,Ltd. Contract record no.: X2020340000010 Denomination of invention: A device for treating wastewater containing high content of petroleum hydrocarbon and its treatment method Granted publication date: 20190402 License type: Common License Record date: 20201230 |
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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. |