CN201488631U - Horizontal tubular primary cooler scale removal device - Google Patents
Horizontal tubular primary cooler scale removal device Download PDFInfo
- Publication number
- CN201488631U CN201488631U CN2009202033038U CN200920203303U CN201488631U CN 201488631 U CN201488631 U CN 201488631U CN 2009202033038 U CN2009202033038 U CN 2009202033038U CN 200920203303 U CN200920203303 U CN 200920203303U CN 201488631 U CN201488631 U CN 201488631U
- Authority
- CN
- China
- Prior art keywords
- primary cooler
- high pressure
- aqua ammonia
- pressure aqua
- removal device
- 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
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- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000007921 spray Substances 0.000 claims abstract description 14
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 25
- 239000010802 sludge Substances 0.000 claims description 7
- 125000004122 cyclic group Chemical group 0.000 claims description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 5
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 239000003034 coal gas Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000005494 condensation Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002790 naphthalenes Chemical class 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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Abstract
The utility model relates to a horizontal tubular primary cooler scale removal device, including high-pressure aqueous ammonia spray set and adjusting valve, high-pressure aqueous ammonia spray set and adjusting valve install respectively at the circulation aqueous ammonia shower entrance of primary cooler. The device simple structure, convenient operation, the effectual phenomenon that prevents the primary cooler scale deposit has prolonged the life of primary cooler.
Description
Technical field
The utility model relates to a kind of cleaning device, particularly relates to a kind of transverse tube type primary cooler apparatus for eliminating sludge.
Background technology
Primary cooler is the visual plant of coal chemical enterprise coal-gas recovering cleaning procedure, and it mainly is responsible for the cooling of coke-stove gas, is beneficial to carry with air blast.Transverse pipe initial cooler is a kind of high-effective gas cooling device newly developed, and it is compared with original commonly used vertical tube primary cooler, and to have a film-cooled heat big, the heat exchange efficiency advantages of higher.In the actual production running, the phenomenon that primary cooler exists resistance to increase after operation a period of time has influenced the normal operation of producing, and can cause coke-stove gas to diffuse when serious, has not only wasted valuable resource, and has polluted environment.
Summary of the invention
The utility model has overcome deficiency of the prior art, and a kind of simple in structure, easy to operate a kind of transverse tube type primary cooler apparatus for eliminating sludge is provided.
In order to address the above problem, the utility model by the following technical solutions:
A kind of transverse tube type primary cooler apparatus for eliminating sludge comprises high pressure aqua ammonia spray equipment and control valve, and high pressure aqua ammonia spray equipment and control valve are installed in the cyclic ammonia water shower porch of primary cooler respectively.
Described high pressure aqua ammonia spray equipment is made up of high pressure aqua ammonia pipeline and shower nozzle, and shower nozzle is installed in high pressure aqua ammonia pipeline front end.
Compared with prior art, the beneficial effects of the utility model are:
The utility model apparatus structure is simple, and easy operating and maintenance purge the separate unit primary cooler by adopting high pressure aqua ammonia, have effectively prevented the phenomenon of primary cooler fouling, have solved the problem that the primary cooler resistance increases.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
The groundwork principle of transverse pipe initial cooler is as follows: coal gas enters from transverse pipe initial cooler top, divides three sections coolings.Epimere cools off coal gas with remaining hot water winter, and all the other times, with 32 ℃ of recirculated waters, hypomere was cooled to 21~22 ℃ with 16 ℃ of chilled water with coal gas with the stage casing.For the cooling that guarantees primary cooler removes the naphthalene effect, spray tar, ammonia water mixture continuously at upper and lower section, spray with hot ammoniacal liquor circulation at its top, with impurity such as the tar on the removing tube wall, naphthalenes.On the primary cooler, the stage casing condensate liquid of discharging flows into epimere condensation liquid bath through water sealed tank, with pump it sent into the circulation of primary cooler epimere middle part and sprays, unnecessary part is delivered to mechanical settling tank.The condensate liquid that the primary cooler hypomere is discharged flows into hypomere condensation liquid bath through water sealed tank, with pump it is sent into the circulation of primary cooler hypomere top and sprays, and redundance flows into epimere condensation liquid bath.
A kind of transverse tube type primary cooler apparatus for eliminating sludge as shown in Figure 1, comprises high pressure aqua ammonia spray equipment 1 and control valve 2, and high pressure aqua ammonia spray equipment 1 is made up of high pressure aqua ammonia pipeline and shower nozzle, and shower nozzle is installed in high pressure aqua ammonia pipeline front end.High pressure aqua ammonia pipeline and control valve 2 are installed in the cyclic ammonia water shower porch of primary cooler respectively.Handover operation when control valve 2 is used to clean primary cooler.
Operating process of the present utility model is:
1) in many transverse pipe initial cooler uses of using in parallel, the separate unit primary cooler is cleaned with hot ammoniacal liquor.
2) cyclic ammonia water porch valve is closed in cleaning, opens high pressure aqua ammonia inlet control valve 2.
3) in the cleaning process, control the gas outlet temperature of transverse pipe initial cooler to be cleaned, make it be not more than 35 ℃.
4) the cleaning time was controlled at 30~40 minutes.
5) control valve 2 that after cleaning finishes high pressure aqua ammonia entered the mouth is closed ON cycle ammonia inlet valve.
Claims (2)
1. a transverse tube type primary cooler apparatus for eliminating sludge is characterized in that, comprises high pressure aqua ammonia spray equipment and control valve, and high pressure aqua ammonia spray equipment and control valve are installed in the cyclic ammonia water shower porch of primary cooler respectively.
2. a kind of transverse tube type primary cooler apparatus for eliminating sludge according to claim 1 is characterized in that described high pressure aqua ammonia spray equipment is made up of high pressure aqua ammonia pipeline and shower nozzle, and shower nozzle is installed in high pressure aqua ammonia pipeline front end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202033038U CN201488631U (en) | 2009-09-15 | 2009-09-15 | Horizontal tubular primary cooler scale removal device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202033038U CN201488631U (en) | 2009-09-15 | 2009-09-15 | Horizontal tubular primary cooler scale removal device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201488631U true CN201488631U (en) | 2010-05-26 |
Family
ID=42427506
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2009202033038U Expired - Fee Related CN201488631U (en) | 2009-09-15 | 2009-09-15 | Horizontal tubular primary cooler scale removal device |
Country Status (1)
Country | Link |
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CN (1) | CN201488631U (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104479915A (en) * | 2014-11-25 | 2015-04-01 | 攀钢集团攀枝花钢钒有限公司 | Naphthalene washing solution and production method thereof |
CN106753594A (en) * | 2017-02-17 | 2017-05-31 | 马鞍山钢铁股份有限公司 | A kind of primary cooler washes naphthalene device |
CN106871707A (en) * | 2017-02-07 | 2017-06-20 | 山西太钢不锈钢股份有限公司 | 7.63m coke oven transverse pipe initial cooler purging systems and cleaning method |
CN109971514A (en) * | 2019-04-09 | 2019-07-05 | 鞍钢化学科技有限公司 | One kind being used for transverse tube type coal gas primary cooler outer circulation cleaning method and device |
CN111220001A (en) * | 2020-01-13 | 2020-06-02 | 国家能源集团煤焦化有限责任公司 | Cooler and coal coking system |
CN112029516A (en) * | 2020-08-25 | 2020-12-04 | 中冶焦耐(大连)工程技术有限公司 | Spraying device of primary cooler |
CN112683103A (en) * | 2020-12-30 | 2021-04-20 | 国家能源集团煤焦化有限责任公司 | Cleaning device for primary cooler cooling pipe, coke oven gas cooling device and coke oven assembly |
-
2009
- 2009-09-15 CN CN2009202033038U patent/CN201488631U/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104479915A (en) * | 2014-11-25 | 2015-04-01 | 攀钢集团攀枝花钢钒有限公司 | Naphthalene washing solution and production method thereof |
CN106871707A (en) * | 2017-02-07 | 2017-06-20 | 山西太钢不锈钢股份有限公司 | 7.63m coke oven transverse pipe initial cooler purging systems and cleaning method |
CN106871707B (en) * | 2017-02-07 | 2018-12-28 | 山西太钢不锈钢股份有限公司 | 7.63m coke oven transverse pipe initial cooler cleaning method |
CN106753594A (en) * | 2017-02-17 | 2017-05-31 | 马鞍山钢铁股份有限公司 | A kind of primary cooler washes naphthalene device |
CN106753594B (en) * | 2017-02-17 | 2020-06-02 | 马鞍山钢铁股份有限公司 | Naphthalene washing device for primary cooler |
CN109971514A (en) * | 2019-04-09 | 2019-07-05 | 鞍钢化学科技有限公司 | One kind being used for transverse tube type coal gas primary cooler outer circulation cleaning method and device |
CN111220001A (en) * | 2020-01-13 | 2020-06-02 | 国家能源集团煤焦化有限责任公司 | Cooler and coal coking system |
CN112029516A (en) * | 2020-08-25 | 2020-12-04 | 中冶焦耐(大连)工程技术有限公司 | Spraying device of primary cooler |
CN112683103A (en) * | 2020-12-30 | 2021-04-20 | 国家能源集团煤焦化有限责任公司 | Cleaning device for primary cooler cooling pipe, coke oven gas cooling device and coke oven assembly |
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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 |
Granted publication date: 20100526 Termination date: 20150915 |
|
EXPY | Termination of patent right or utility model |