CN204084405U - Combustion evaporator under gas-water - Google Patents
Combustion evaporator under gas-water Download PDFInfo
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- CN204084405U CN204084405U CN201420432322.9U CN201420432322U CN204084405U CN 204084405 U CN204084405 U CN 204084405U CN 201420432322 U CN201420432322 U CN 201420432322U CN 204084405 U CN204084405 U CN 204084405U
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- combustion chamber
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Abstract
The utility model is a kind of for the treatment of combustion evaporator under the gas-water of trade effluent, primarily of compositions such as main body, gas burner system, auger, filter, motor, liquid level gauges, main body is provided with two combustion chambers, first combustion chamber is for the evaporation sewage that burns, second combustion chamber is for the evaporation mud that burns, two bottom of combustion chamber are all provided with auger, are provided with flame distributor above auger; Two top of combustion chamber are all provided with steam (vapor) outlet, and steam (vapor) outlet is all provided with vapour compression machine; Two side, combustion chambers are all provided with liquid level gauge; Gas burner system connects the flame import of flame distributor.Under the utility model gas-water, combustion evaporator process trade effluent does not need to add any inorganic agent, and do not have selective restriction, the thermal efficiency is high, and non-secondary pollution.
Description
Technical field
The utility model relates to a kind of plant equipment, is specially combustion evaporator under a kind of gas-water.
Background technology
Along with rapid development of economy, the sewage environmental pollution aggravation of the enterprise production process relevant to chemical industry, also more prevalent and serious to the harm of human health, in the sewage of wherein particularly discharging in fine chemical product (as pharmacy, dyestuff, daily use chemicals etc.) production process, be difficult to the material of degrading containing complex structure, poisonous and harmful and biology, these wastewater treatment difficulty are very large.
Current, in sewage water treatment method, the technology and equipment adopting combustion method to dispose of sewage has following two kinds: 1, spray combustion medium incinerator, spray combustion medium incinerator is by flammable sewage, special spray gun is utilized to spray in Burning Room, adopt the medium ignition such as fuel oil, when can form continuous burning state to combustible sewage, stop adding fuel oil, form stable fired state, Burning Room through special insulation, after-flame organic matter, reclaim or discharge non-flammable salt, waste gas discharges after residual heat boiler for exchanging heat.This incineration technology is typically applied in the process of black liquid.There are three problems in this treatment facility, one is the selective of sewage, must be flammable; Two be burning after energy sub-fraction by residual heat boiler for exchanging heat, other then emit, and equipment is in hot operation state, and energy consumption is high; Three is the work that must continue, start-stop car and ignition operation complexity.2, pressurized gasification sewage incinerator, for non-flammable sewage, through pressurized gasification, must be mixed together the sewage of atomization and combustion-supporting medium, ignition in incinerator, the water vapour produced after burning, CO, CO
2deng discharge or discharge after residual heat boiler for exchanging heat.The combustible materials such as the combustion gas of this equipment incendivity, fuel oil, waste oil, solvent slop, fire coal, material source is wide, weak point is, hot operation room is formed in burner, specially treated will be carried out to the adiabatic problem of equipment, heat waste is large, and combustion medium may cause secondary pollution, and the service life of operating temperature height equipment is low.
Summary of the invention
The purpose of this utility model be for the high concentration produced in current chemical industry, medicine and other fields production process, high salt, difficult decompose containing organic, inorganic matter sewage, a kind of sewage-treatment plant is provided, processing procedure does not need to add any inorganic agent, there is no selective restriction, energy consumption is low, non-secondary pollution.
For achieving the above object, the utility model have employed following scheme: combustion evaporator under gas-water, primarily of main body, gas burner system A, gas burner system B, auger A, auger B, filter A, filter B, motor A, motor B, liquid level gauge A, liquid level gauge B forms, main body is provided with two combustion chambers, first combustion chamber is for the evaporation sewage that burns, second combustion chamber is for the evaporation mud that burns, first bottom of combustion chamber is provided with auger A, flame distributor A is provided with above auger A, first top, combustion chamber is provided with filter A, top is provided with steam (vapor) outlet A, steam (vapor) outlet A connects vapour compression machine A, first combustion chamber lateral surface is provided with liquid level gauge A, second bottom of combustion chamber is provided with auger B, is provided with flame distributor B above auger B, and the second top, combustion chamber is provided with filter B, and top is provided with steam (vapor) outlet B, and steam (vapor) outlet B connects vapour compression machine B, and the second combustion chamber lateral surface is provided with liquid level gauge B, first combustion chamber mud mouth connects dredging tube, dredging tube outlet connects the second bottom, combustion chamber, defeated slurry valve door is provided with in the middle part of dredging tube, second combustion chamber slag notch is provided with valve of slagging tap, first top, combustion chamber is provided with water inlet, and gas burner system A connects the upper end of flame distributor A, and gas burner system B connects the upper end of flame distributor B, auger A is driven by motor A, and auger B is driven by motor B.
During work, to the first combustion chamber input sewage, when reaching design liquid level, start gas burner system, start vapour compression machine simultaneously, gas burner system flame is by flame distributor at dirty submerged combustion, and flame directly contacts with sewage, passes through high-temperature chemical reaction, destroy the molecular structure of various harmful substance in sewage, the sewage of secondary high-temperature area, becomes steam, and steam delivers to sewage disposal system other parts by vapour compression machine; Mud after concentrated is under the effect of auger, the second combustion chamber is entered by dredging tube, when reaching design liquid level, start gas burner system, start vapour compression machine, gas burner system flame is burnt in mud by flame distributor simultaneously, flame directly contacts with mud, concentrated sewage obtains second-time burning evaporation, decomposes remaining pollutant and transpiring moisture further, and the residue finally after process is discharged to outside the second combustion chamber by auger.
Owing to have employed technique scheme, the progress that the utility model obtains is: process trade effluent does not need to add any inorganic agent, and do not have selective restriction, the thermal efficiency is high, and non-secondary pollution.
Accompanying drawing explanation
Fig. 1 is the utility model structure chart,
Fig. 2 is Figure 1A-A sectional view,
Fig. 3 is Figure 1B-B sectional view,
Fig. 4 is Fig. 1 rearview.
In figure: 1, defeated slurry valve door, 2, dredging tube, 3, auger A, 4, flame distributor A, 5, liquid level gauge A, 6, water inlet, 7, first combustion chamber, 8, filter A, 9, main body, 10, steam (vapor) outlet A, 11, vapour compression machine A, 12, vapour compression machine B, 13, steam (vapor) outlet B, 14, filter B, 15, second combustion chamber, 16, liquid level gauge B, 17, flame distributor B, 18, auger B, 19, mud mouth, 20, gas burner system A, 21, motor A, 22, slag notch, 23, to slag tap valve, 24, mud inlet, 25, gas burner system B, 26, motor B.
detailed description of the invention
Below with embodiment by reference to the accompanying drawings, the utility model is described in further detail.
For 3 tons of/hour process trade effluent abilities, main body uses the thick 310S steel plate of 10mm to make, auger A and auger B uses the thick 310S steel plate of 8mm to make, level is arranged on the first combustion chamber and the second bottom of combustion chamber respectively, driven by motor A and motor B respectively, motor A and motor B uses 4kw motor, flame distributor A and flame distributor B uses the thick 310S steel plate of 8mm to make, be arranged on above auger A and auger B respectively, liquid level gauge A and liquid level gauge B uses UFZ-52 type magnetic flap level gauge, be arranged on the first combustion chamber and the second combustion chamber lateral surface respectively, filter A and filter B all use stainless (steel) wire to make, be arranged on the first combustion chamber and the second top, combustion chamber respectively, vapour compression machine A and vapour compression machine B uses SR150 steam compressor, is arranged on above steam (vapor) outlet A and steam (vapor) outlet B respectively, gas burner system A and gas burner system B uses BT17GF gas burner system, is arranged on flame distributor A and flame distributor B upper end respectively, dredging tube uses Φ 159 310S steel pipe manufacturing, a termination first combustion chamber mud mouth, another termination second combustion chamber mud inlet, and defeated slurry valve door uses stainless steel butterfly valve, is arranged in the middle part of dredging tube, valve of slagging tap uses stainless steel butterfly valve, is arranged on the second slag notch place, combustion chamber.
Claims (1)
1. combustion evaporator under gas-water, primarily of main body (9), gas burner system A(20), gas burner system B(25), auger A(3), auger B(18), filter A(8), filter B (14), motor A(21), motor B(26), liquid level gauge A(5), liquid level gauge B(16) composition, it is characterized in that: main body (9) is provided with two combustion chambers, first combustion chamber (7) and the second combustion chamber (15), bottom, first combustion chamber (7) is provided with auger A(3), auger A(3) be provided with flame distributor A(4 above), first combustion chamber (7) top is provided with filter A(8), top is provided with steam (vapor) outlet A(10), steam (vapor) outlet A(10) connect vapour compression machine A(11), first combustion chamber (7) lateral surface is provided with liquid level gauge A(5), bottom, second combustion chamber (15) is provided with auger B(18), auger B(18) be provided with flame distributor B(17 above), second combustion chamber (15) top is provided with filter B (14), top is provided with steam (vapor) outlet B(13), steam (vapor) outlet B(13) connect vapour compression machine B(12), second combustion chamber (15) lateral surface is provided with liquid level gauge B(16), first combustion chamber (7) mud mouth (19) connects dredging tube (2), dredging tube (2) outlet connects the second combustion chamber (15) bottom, dredging tube (2) middle part is provided with defeated slurry valve door (1), second combustion chamber (15) slag notch (22) is provided with valve of slagging tap (23), first combustion chamber (7) top is provided with water inlet (6), gas burner system A(20) meet flame distributor A(4) upper end, gas burner system B(25) meet flame distributor B(17) upper end, auger A(3) by motor A(21) drive, auger B(18) by motor B(26) drive.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420432322.9U CN204084405U (en) | 2014-08-03 | 2014-08-03 | Combustion evaporator under gas-water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420432322.9U CN204084405U (en) | 2014-08-03 | 2014-08-03 | Combustion evaporator under gas-water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204084405U true CN204084405U (en) | 2015-01-07 |
Family
ID=52177116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420432322.9U Expired - Fee Related CN204084405U (en) | 2014-08-03 | 2014-08-03 | Combustion evaporator under gas-water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204084405U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100981A (en) * | 2014-08-03 | 2014-10-15 | 平原中德泰兴工贸有限公司 | Underwater gas combustion evaporator |
-
2014
- 2014-08-03 CN CN201420432322.9U patent/CN204084405U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100981A (en) * | 2014-08-03 | 2014-10-15 | 平原中德泰兴工贸有限公司 | Underwater gas combustion evaporator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 253100 Branson, Xingping Road, Eastern District of Plain County Economic Development Zone, Dezhou City, Shandong Province Patentee after: PINGYUAN ZHONGDE TAIXING ENVIRONMENTAL PROTECTION TECHNOLOGY & EQUIPMENT CO.,LTD. Address before: 253100 Branson, Xingping Road, Eastern District of Plain County Economic Development Zone, Dezhou City, Shandong Province Patentee before: PINGYUAN ZHONGDE TAIXING INDUSTRY & TRADE CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 253100 Branson, Xingping Road, Eastern District of Plain County Economic Development Zone, Dezhou City, Shandong Province Patentee after: Pingyuan Xinrui Environmental Protection Technology Co.,Ltd. Address before: 253100 Branson, Xingping Road, Eastern District of Plain County Economic Development Zone, Dezhou City, Shandong Province Patentee before: PINGYUAN ZHONGDE TAIXING ENVIRONMENTAL PROTECTION TECHNOLOGY & EQUIPMENT Co.,Ltd. |
|
| 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: 20150107 Termination date: 20210803 |