CN104327884A - Coal gas dust removal system for low-moisture coal coking - Google Patents
Coal gas dust removal system for low-moisture coal coking Download PDFInfo
- Publication number
- CN104327884A CN104327884A CN201410647708.6A CN201410647708A CN104327884A CN 104327884 A CN104327884 A CN 104327884A CN 201410647708 A CN201410647708 A CN 201410647708A CN 104327884 A CN104327884 A CN 104327884A
- Authority
- CN
- China
- Prior art keywords
- gas
- dust removal
- removal system
- shower nozzle
- wash tower
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/02—Dust removal
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention discloses a coal gas dust removal system for low-moisture coal coking, which comprises a coal gas washing tower connected with a primary cooler, and the coal gas washing tower is provided with a first nozzle for spraying a washing liquid to coal gas fed into the dust removal system. The coal gas dust removal system for low-moisture coal coking disclosed by the invention reduces the amount of dust entrained in coal gas by way of circulating washing, thereby reducing the influence on a subsequent coal gas purification system as far as possible.
Description
Technical field
The invention belongs to technical field of coal chemical industry, specifically, the present invention relates to a kind of gas dust removal system of low moisture coal coking.
Background technology
Conventional gas cleaning system can normally be run when the moisture of coke oven as-fired coal is about 10%, but after coal damping project comes into operation, when the moisture of coke oven as-fired coal drops to below 8%, after running for some time, gas cleaning system reflects that in system, coal dust carries obvious increase secretly.Gassy system shows that primary cooler resistance increases cleaning increased frequency, and after primary cooler, gas line coal dust etc. increase, and thionizer and Ammonic washing tower resistance increase, the phenomenons such as gas quality index variation.The problems referred to above worsen further with the lower general who has surrendered of as-fired coal moisture.
Summary of the invention
The invention provides a kind of gas dust removal system of low moisture coal coking, object reduces the entrainment of dust in coal gas, reduces the impact on follow-up gas cleaning system.
To achieve these goals, the technical scheme that the present invention takes is: a kind of gas dust removal system of low moisture coal coking, comprises the gas wash tower be connected with primary cooler, and gas wash tower is provided with the first shower nozzle for spraying washings to the coal gas entering inside.
Described gas wash tower is empty spray tower or packing tower.
Described gas wash tower has the inlet mouth be connected with gas-liquid separator and the air outlet be connected with described primary cooler, and air outlet is positioned at above inlet mouth.
Described first shower nozzle is positioned at the below of the air outlet of described gas wash tower.
Described gas wash tower has water outlet, and water outlet is positioned at below described first shower nozzle, and is connected with cleaning circulation pump and strainer between water outlet and the first shower nozzle.
The water outlet of described gas wash tower is positioned at the below of inlet mouth, the water-in of described cleaning circulation pump is connected with the water outlet of gas wash tower, the water outlet of cleaning circulation pump is connected with the water-in of described strainer, and the water outlet of strainer is connected with described first shower nozzle.
The sewage draining exit of described strainer is connected with mechanize tar ammonia clarifying tank.
The water outlet of described cleaning circulation pump is connected with suction gas line by pipeline.
Be provided with the second shower nozzle in described gas wash tower, the second shower nozzle is between described first shower nozzle and described inlet mouth.
The gas dust removal system of low moisture coal coking of the present invention, by by the mode of circulation cleaning to reduce the entrainment of dust in coal gas, reduce the impact on follow-up gas cleaning system as much as possible.
Accompanying drawing explanation
This specification sheets comprises the following drawings, shown content respectively:
Fig. 1 is the structural representation of the gas dust removal system of low moisture coal coking of the present invention;
Be labeled as in figure:
1, gas wash tower; 11, inlet mouth; 12, air outlet; 2, cleaning circulation pump; 3, strainer; 4, the first shower nozzle; 5, the second shower nozzle; 6, mechanize tar ammonia clarifying tank.
Embodiment
Contrast accompanying drawing below, by the description to embodiment, be described in further detail the specific embodiment of the present invention, object helps those skilled in the art to have more complete, accurate and deep understanding to inventive concept of the present invention, technical scheme, and contribute to its enforcement.
As shown in Figure 1, the gas dust removal system of a kind of low moisture coal coking of the present invention, comprises gas wash tower 1, and gas wash tower 1 arranges before primary cooler, the inside of gas wash tower 1 is provided with the first shower nozzle 4 for spraying washings to the coal gas entering inside, and washings is ammoniacal liquor.
Specifically, gas wash tower 1 can be empty spray tower, or packing tower.Gas wash tower 1 has the inlet mouth 11 be connected with gas-liquid separator and the air outlet 12 be connected with primary cooler, and air outlet 12 is positioned at above inlet mouth 11.As shown in Figure 1, inlet mouth 11 is the tops being positioned at gas wash tower 1, inlet mouth 11 is the bottom position places being positioned at gas wash tower 1, and coal gas enters in gas wash tower 1 from the bottom of gas wash tower 1, then gas line before escaping into primary cooler from the air outlet 12 of top of tower.
As shown in Figure 1, the first shower nozzle 4 is the belows of the air outlet 12 being positioned at gas wash tower 1, and the first shower nozzle 4 can spray washings, to remove the part dust in coal gas, meets the requirement of gas cleaning system.
For ensureing the washing effect of washings, continuous supplementation component loops ammoniacal liquor, the bottom of gas wash tower 1 has water outlet, and is connected with cleaning circulation pump 2 and strainer 3 between water outlet and the first shower nozzle 4.Cleaning circulation pump 2 and strainer 3 are positioned at the outside of gas wash tower 1, and the outlet pipe of cleaning circulation pump 2 connects strainer 3, and strainer 3 filters the dust removed in circulating cleaning solution.
As shown in Figure 1, the water outlet of gas wash tower 1 is positioned at the below of inlet mouth 11, the water-in of cleaning circulation pump 2 is connected with the water outlet of gas wash tower 1, and the water outlet of cleaning circulation pump 2 is connected with the water-in of strainer 3, and the water outlet of strainer 3 is connected with the first shower nozzle 4.The sewage draining exit of strainer 3 is connected with mechanize tar ammonia clarifying tank 6, and blowdown liquid is to mechanize tar ammonia clarifying tank 6.
As shown in Figure 1, the second shower nozzle 5, second shower nozzle 5 is also provided with in gas wash tower 1 between the first shower nozzle 4 and inlet mouth 11.Second shower nozzle 5 is connected with the liquid supply equipment of peripheral hardware, provides washings by liquid supply equipment to the second shower nozzle 5, and the second shower nozzle 5 sprays washings to entering in gas wash tower 1, and the dust further in removing coal gas, improves dust removing effects.
As preferably, as shown in Figure 1, the unnecessary washings in washing tower drains into suction gas line by the liquid level regulation system at the bottom of tower automatically by cleaning circulation pump 2, and the water outlet of cleaning circulation pump 2 is connected with suction gas line by pipeline.
Below by reference to the accompanying drawings to invention has been exemplary description.Obviously, specific implementation of the present invention is not subject to the restrictions described above.As long as have employed the improvement of the various unsubstantialities that method of the present invention is conceived and technical scheme is carried out; Or without improvement, above-mentioned design of the present invention and technical scheme directly applied to other occasion, all within protection scope of the present invention.
Claims (9)
1. a gas dust removal system for low moisture coal coking, is characterized in that: comprise the gas wash tower be connected with primary cooler, and gas wash tower is provided with the first shower nozzle for spraying washings to the coal gas entering inside.
2. the gas dust removal system of low moisture coal coking according to claim 1, is characterized in that: described gas wash tower is empty spray tower or packing tower.
3. the gas dust removal system of low moisture coal coking according to claim 1 and 2, is characterized in that: described gas wash tower has the inlet mouth be connected with gas-liquid separator and the air outlet be connected with described primary cooler, and air outlet is positioned at above inlet mouth.
4. the gas dust removal system of low moisture coal coking according to claim 3, is characterized in that: described first shower nozzle is positioned at the below of the air outlet of described gas wash tower.
5. the gas dust removal system of low moisture coal coking according to claim 4, it is characterized in that: described gas wash tower has water outlet, water outlet is positioned at below described first shower nozzle, and is connected with cleaning circulation pump and strainer between water outlet and the first shower nozzle.
6. the gas dust removal system of low moisture coal coking according to claim 5, it is characterized in that: the water outlet of described gas wash tower is positioned at the below of inlet mouth, the water-in of described cleaning circulation pump is connected with the water outlet of gas wash tower, the water outlet of cleaning circulation pump is connected with the water-in of described strainer, and the water outlet of strainer is connected with described first shower nozzle.
7. the gas dust removal system of low moisture coal coking according to claim 6, is characterized in that: the sewage draining exit of described strainer is connected with mechanize tar ammonia clarifying tank.
8. the gas dust removal system of low moisture coal coking according to claim 7, is characterized in that: the water outlet of described cleaning circulation pump is connected with suction gas line by pipeline.
9. the gas dust removal system of low moisture coal coking according to claim 8, is characterized in that: be provided with the second shower nozzle in described gas wash tower, the second shower nozzle is between described first shower nozzle and described inlet mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410647708.6A CN104327884A (en) | 2014-11-15 | 2014-11-15 | Coal gas dust removal system for low-moisture coal coking |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410647708.6A CN104327884A (en) | 2014-11-15 | 2014-11-15 | Coal gas dust removal system for low-moisture coal coking |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104327884A true CN104327884A (en) | 2015-02-04 |
Family
ID=52402697
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410647708.6A Pending CN104327884A (en) | 2014-11-15 | 2014-11-15 | Coal gas dust removal system for low-moisture coal coking |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104327884A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689631A (en) * | 2015-03-27 | 2015-06-10 | 山东钢铁股份有限公司 | Cycling ammonia water filtering device and method |
| CN110437888A (en) * | 2019-08-21 | 2019-11-12 | 中冶焦耐(大连)工程技术有限公司 | A kind of exhaust gas cooler |
| CN112538390A (en) * | 2020-11-13 | 2021-03-23 | 鹤岗市征楠煤化工有限公司 | Coal gas primary cooler |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101608137A (en) * | 2008-06-20 | 2009-12-23 | 上海宝钢化工有限公司 | Primary cooling process for coal gas |
| CN201439517U (en) * | 2009-05-10 | 2010-04-21 | 山西太钢不锈钢股份有限公司 | Device for removing impurities in gas of pipeline |
| CN103031159A (en) * | 2013-01-07 | 2013-04-10 | 唐山中润煤化工有限公司 | Coal gas purifying and cooling technology and system |
| CN103484169A (en) * | 2013-10-30 | 2014-01-01 | 北京中亿孚佑科技有限公司 | New method for performing preliminary condensation refrigeration on coking raw gas |
-
2014
- 2014-11-15 CN CN201410647708.6A patent/CN104327884A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101608137A (en) * | 2008-06-20 | 2009-12-23 | 上海宝钢化工有限公司 | Primary cooling process for coal gas |
| CN201439517U (en) * | 2009-05-10 | 2010-04-21 | 山西太钢不锈钢股份有限公司 | Device for removing impurities in gas of pipeline |
| CN103031159A (en) * | 2013-01-07 | 2013-04-10 | 唐山中润煤化工有限公司 | Coal gas purifying and cooling technology and system |
| CN103484169A (en) * | 2013-10-30 | 2014-01-01 | 北京中亿孚佑科技有限公司 | New method for performing preliminary condensation refrigeration on coking raw gas |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104689631A (en) * | 2015-03-27 | 2015-06-10 | 山东钢铁股份有限公司 | Cycling ammonia water filtering device and method |
| CN104689631B (en) * | 2015-03-27 | 2016-09-07 | 山东钢铁股份有限公司 | A kind of cyclic ammonia water filter and method |
| CN110437888A (en) * | 2019-08-21 | 2019-11-12 | 中冶焦耐(大连)工程技术有限公司 | A kind of exhaust gas cooler |
| CN112538390A (en) * | 2020-11-13 | 2021-03-23 | 鹤岗市征楠煤化工有限公司 | Coal gas primary cooler |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204170594U (en) | Rubber powder modified asphalt produces spray washing tower | |
| CN104327884A (en) | Coal gas dust removal system for low-moisture coal coking | |
| CN104099627B (en) | A kind of descaling bath with acid recovery function | |
| CN107998789A (en) | A kind of combustion tail gas fuel gas and dust processing equipment | |
| CN204051315U (en) | A kind of water spray cleaner | |
| CN107875796B (en) | Device and method for removing impurities of coke oven gas on coke oven gas pipeline | |
| CN204544853U (en) | A kind of cage guide automatic cleaning system | |
| CN104315576B (en) | Vacuum water elution range hood | |
| CN204522602U (en) | A kind of industrial dust washing device | |
| CN208340475U (en) | Purification of water quality workshop section waste gas treatment device | |
| CN207042226U (en) | A kind of cold rolling acid mist absorbs automatic circulating system | |
| CN107892955A (en) | A kind of mass transfer separator | |
| CN212068177U (en) | Industrial waste gas purifying tower | |
| CN207734777U (en) | Device on coke oven gas pipe for removing coke-stove gas impurity | |
| CN103435209B (en) | Processing method for acidic ash water | |
| RU2567309C1 (en) | Surge-vessel - separator | |
| CN208398164U (en) | A kind of double water fenders fortune water smoke purifiers of inside insertion hanging type | |
| CN203128516U (en) | Combined washing apparatus | |
| CN207287099U (en) | A kind of Waster water reuse apparatus in catalytic cracking unit | |
| CN204275752U (en) | A kind of water scrubber with washing at a high speed centrifugal pump | |
| CN207362161U (en) | A kind of synthesis gas fine purifiation device | |
| CN205913976U (en) | Wet desulfurization dust removal static integrated device | |
| CN205990259U (en) | A kind of degasser for acid waste liquid | |
| CN204275746U (en) | A kind of cyclone dust collectors had except sulfur functional | |
| CN204319999U (en) | The washing type smoke duster that dust removal efficiency is higher |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150204 |
|
| RJ01 | Rejection of invention patent application after publication |