CN204661482U - Water-gas refining plant - Google Patents
Water-gas refining plant Download PDFInfo
- Publication number
- CN204661482U CN204661482U CN201520148861.4U CN201520148861U CN204661482U CN 204661482 U CN204661482 U CN 204661482U CN 201520148861 U CN201520148861 U CN 201520148861U CN 204661482 U CN204661482 U CN 204661482U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- phenol
- phenol water
- gas
- settling tank
- 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
Landscapes
- Industrial Gases (AREA)
Abstract
The utility model belongs to water-gas processing technology field, is specifically related to a kind of water-gas refining plant.Comprise phenol pond, settling tank, phenol water heater and gas furnace, settling tank top arranges tar light oil overflow port, settling tank bottom arranges tar heavy oil outlet, settling tank middle wall is arranged phenol water out, phenol pond is connected with settling tank by pipeline, phenol water out is connected with phenol water heater by pipeline, phenol water heater connects drum, pipeline between phenol water out and phenol water heater arranges force (forcing) pump, phenol water heater connects bottom gas furnace by pipeline, gas furnace lower part outlet connects tornado dust collector successively by pipeline, interchanger, inter cooler, electric fishing light oil device and custom system, interchanger is connected with gas blower, gas furnace top exit connects electrical tar precipitator by pipeline, electrical tar precipitator connects inter cooler by pipeline.The utility model is rational in infrastructure, can effectively disposal and utilization gas station produce poison sewage phenol water.
Description
Technical field
The utility model belongs to water-gas processing technology field, is specifically related to a kind of water-gas refining plant.
Background technology
The phenol water (phenol-containing wastewater) produced in gasification scavenging process a kind ofly environment is had to the liquid had a strong impact on, and along with more and more tighter to the requirement of environmental protection, progressively strengthens the improvement of phenol water.The phenol water produced in prior art gasification scavenging process is difficult to utilize in time and process.
Summary of the invention
For the deficiencies in the prior art, the purpose of this utility model is to provide a kind of water-gas refining plant, rational in infrastructure, can effectively disposal and utilization gas station produce poison sewage phenol water.
Water-gas refining plant described in the utility model, comprise phenol pond, settling tank, phenol water heater and gas furnace, settling tank top arranges tar light oil overflow port, settling tank bottom arranges tar heavy oil outlet, settling tank middle wall is arranged phenol water out, phenol pond is connected with settling tank by pipeline, phenol water out is connected with phenol water heater by pipeline, phenol water heater connects drum, pipeline between phenol water out and phenol water heater arranges force (forcing) pump, phenol water heater connects bottom gas furnace by pipeline, gas furnace centre exit connects tornado dust collector successively by pipeline, interchanger, inter cooler, electric fishing light oil device and custom system, interchanger is connected with gas blower, gas furnace top exit connects electrical tar precipitator by pipeline, electrical tar precipitator connects inter cooler by pipeline.
Pipeline between phenol water out and force (forcing) pump arranges filtering net.
Interchanger is connected by pipeline with bottom gas furnace.
This technique main purpose is the poison sewage phenol water that disposal and utilization gas station produces.
During use, phenol water in phenol pond enters settling tank precipitation, tar heavy oil is deposited to bottom settling tank, exported by tar heavy oil and discharge, tar light oil floats on surface, discharged by tar light oil overflow port, phenol water after purification is discharged by phenol water out and is passed through filter screen filtration, then phenol water heater is entered after being pressurizeed by force (forcing) pump, in drum, steam enters phenol water heater, steam heating phenol water, and the phenol water after pressurized, heated is admitted to the atomization of gas furnace furnace bottom, phenol water after atomization is gasified further, together enters gas furnace and uses as vaporized chemical.The gas in upper segment of being discharged by gas furnace enters in electrical tar precipitator, gas in upper segment gas, separating of oil in electrical tar precipitator, and after electrical tar precipitator catches tar heavy oil, remaining gas in upper segment enters inter cooler cooling; The hypomere coal gas that gas furnace is discharged enters tornado dust collector dedusting, enter interchanger heat exchange again, hypomere gas temperature declines, and air themperature raises, and interchanger is preferably connected by pipeline with bottom gas furnace, by entering gas furnace bottom gas furnace after air is heated, the air entering gas furnace is warm air, and the hypomere coal gas after heat exchange enters inter cooler and gas in upper segment is mixed into a step-down temperature, then enters electric fishing light oil device together, catch after tar light oil through electric fishing light oil device, enter custom system.The treating processes that utilizes of the utility model phenol water is: purification-pressure-heat-atomization-vaporization, atomization and vaporization under hot blast effect.
In sum, the utility model has the following advantages:
(1) water-gas refining plant described in the utility model, rational in infrastructure, can effectively disposal and utilization gas station produce poison sewage phenol water.
(2) the utility model is at the phenol water that gasification purification utilizes in time and process produces simultaneously, realizes gas station sewage zero-discharge.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment;
In figure: 1-phenol pond, 2-tar light oil overflow port, 3-settling tank, 4-tar heavy oil exports, 5-phenol water out, 6-filtering net, 7-force (forcing) pump, 8-phenol water heater, 9-drum, 10-gas furnace, 11-tornado dust collector, 12-gas blower, 13-electrical tar precipitator, 14-interchanger, 15-inter cooler, 16-electric fishing light oil device, 17-custom system.
Embodiment
Below in conjunction with embodiment, the utility model is described further.
Embodiment
A kind of water-gas refining plant, comprise phenol pond 1, settling tank 3, phenol water heater 8 and gas furnace 10, settling tank 3 top arranges tar light oil overflow port 2, settling tank 3 bottom arranges tar heavy oil outlet 4, settling tank 3 middle wall arranges phenol water out 5, phenol pond 1 is connected with settling tank 3 by pipeline, phenol water out 5 is connected with phenol water heater 8 by pipeline, phenol water heater 8 connects drum 9, pipeline between phenol water out 5 and phenol water heater 8 is arranged force (forcing) pump 7, phenol water heater 8 connects bottom gas furnace 10 by pipeline, gas furnace 10 centre exit connects tornado dust collector 11 successively by pipeline, interchanger 14, inter cooler 15, electric fishing light oil device 16 and custom system 17, interchanger 14 is connected with gas blower 12, gas furnace 10 top exit connects electrical tar precipitator 13 by pipeline, electrical tar precipitator 13 connects inter cooler 15 by pipeline.Pipeline between phenol water out 5 and force (forcing) pump 7 is arranged filtering net 6.Interchanger 14 is connected by pipeline with bottom gas furnace 10.
During use, phenol water in phenol pond 1 enters settling tank 3 and precipitates, tar heavy oil is deposited to bottom settling tank 3, export 4 by tar heavy oil to discharge, tar light oil floats on surface, discharged by tar light oil overflow port 2, phenol water after purification is discharged by phenol water out 5 and is filtered by filtering net 6, then phenol water heater 8 is entered after being pressurizeed by force (forcing) pump 7, in drum 9, steam enters phenol water heater 8, steam heating phenol water, and the phenol water after pressurized, heated is admitted to the atomization of gas furnace 10 furnace bottom, phenol water after atomization is gasified further, together enters gas furnace 10 and uses as vaporized chemical.The gas in upper segment of being discharged by gas furnace 10 enters in electrical tar precipitator 13, gas in upper segment gas, separating of oil in electrical tar precipitator 13, and after electrical tar precipitator 13 catches tar heavy oil, remaining gas in upper segment enters inter cooler 15 and cools; The hypomere coal gas that gas furnace 10 is discharged enters tornado dust collector 11 dedusting, enter interchanger 14 heat exchange again, hypomere gas temperature declines, air themperature raises, and interchanger 14 is connected by pipeline with bottom gas furnace 10, by entering gas furnace 10 bottom gas furnace 10 after air is heated, hypomere coal gas after heat exchange enters inter cooler 15 and is mixed into a step-down temperature with gas in upper segment, then enter electric fishing light oil device 16 together, after electric fishing light oil device 16 catches tar light oil, enter custom system 17.
Claims (3)
1. a water-gas refining plant, it is characterized in that: comprise phenol pond (1), settling tank (3), phenol water heater (8) and gas furnace (10), settling tank (3) top arranges tar light oil overflow port (2), settling tank (3) bottom arranges tar heavy oil outlet (4), settling tank (3) middle wall is arranged phenol water out (5), phenol pond (1) is connected with settling tank (3) by pipeline, phenol water out (5) is connected with phenol water heater (8) by pipeline, phenol water heater (8) connects drum (9), pipeline between phenol water out (5) and phenol water heater (8) is arranged force (forcing) pump (7), phenol water heater (8) connects gas furnace (10) bottom by pipeline, gas furnace (10) centre exit connects tornado dust collector (11) successively by pipeline, interchanger (14), inter cooler (15), electric fishing light oil device (16) and custom system (17), interchanger (14) is connected with gas blower (12), gas furnace (10) top exit connects electrical tar precipitator (13) by pipeline, electrical tar precipitator (13) connects inter cooler (15) by pipeline.
2. water-gas refining plant according to claim 1, is characterized in that: the pipeline between phenol water out (5) and force (forcing) pump (7) is arranged filtering net (6).
3. water-gas refining plant according to claim 1, is characterized in that: interchanger (14) is connected by pipeline with gas furnace (10) bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520148861.4U CN204661482U (en) | 2015-03-16 | 2015-03-16 | Water-gas refining plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520148861.4U CN204661482U (en) | 2015-03-16 | 2015-03-16 | Water-gas refining plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204661482U true CN204661482U (en) | 2015-09-23 |
Family
ID=54131890
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520148861.4U Expired - Fee Related CN204661482U (en) | 2015-03-16 | 2015-03-16 | Water-gas refining plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204661482U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111362354A (en) * | 2020-04-19 | 2020-07-03 | 山西三强新能源科技有限公司 | Residual oil phenol-water mixture separation and recovery process and device thereof |
-
2015
- 2015-03-16 CN CN201520148861.4U patent/CN204661482U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111362354A (en) * | 2020-04-19 | 2020-07-03 | 山西三强新能源科技有限公司 | Residual oil phenol-water mixture separation and recovery process and device thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106277608B (en) | A kind of sewage-treatment plant with rainwater-collecting | |
| CN107777820A (en) | The technique that Air-Cooling Island exhaust steam residual heat is used for Waste Water From Fire Power Plant zero discharge treatment | |
| CN105057101A (en) | Cylindrical vertical wet-type explosion-proof and voltage-resistant electric precipitator | |
| CN105238451B (en) | A kind of efficient combined-type biomass gasification burning cooling and purifying system | |
| CN105327604A (en) | Smoke processing system and method thereof | |
| CN102515407A (en) | Gas station phenol water processing process | |
| CN204661482U (en) | Water-gas refining plant | |
| CN102586523B (en) | Blast furnace gas purification plant | |
| CN206715571U (en) | A kind of wood-based plate cyclone separator exhaust gas processing device | |
| CN103203155B (en) | A kind of electric furnace secondary aluminium melting exhaust-gas treatment production line | |
| CN203683571U (en) | Dry dedusting and energy-saving system | |
| CN102492796A (en) | After heat heating system and method for filtering blast furnace slag flushing water by using bottom filter tank | |
| CN205556588U (en) | Device that circulating oil washing high temperature coal gas removed dust | |
| CN110963462A (en) | Methanol hydrogen production system | |
| CN102886185A (en) | Waste gas filtering equipment | |
| CN202465758U (en) | Converter gas purifying and recycling system | |
| CN204485544U (en) | Water deposition type smoke and dust purifier | |
| CN203419893U (en) | Nitrogen backblowing circulating system for purification of TSA coke oven gas | |
| CN201695076U (en) | Fume recovering and dedusting device of drainage type zinc pot | |
| CN201322306Y (en) | Vaporization saturation dephenolizing process equipment system of gas producing furnace | |
| CN204073639U (en) | Binary channels electrolysis infiltration Auto-drainage cleaning system | |
| CN208449024U (en) | A kind of Handling Blast Furnace Granulated Slag circulatory system | |
| CN208406113U (en) | A kind of calcination rotary kiln tail gas pre-concentration spent acid device | |
| CN107090901B (en) | A kind of student life water cycle utilization device | |
| CN104289094A (en) | Waste gas filtering and purifying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150923 Termination date: 20190316 |