CN105001919A - Coke tar removal condenser - Google Patents
Coke tar removal condenser Download PDFInfo
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- CN105001919A CN105001919A CN201510462259.2A CN201510462259A CN105001919A CN 105001919 A CN105001919 A CN 105001919A CN 201510462259 A CN201510462259 A CN 201510462259A CN 105001919 A CN105001919 A CN 105001919A
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- discharge chamber
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- inlet plenum
- tar
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Abstract
The invention discloses a coke tar removal condenser. The coke tar removal condenser is characterized in that the coke tar removal condenser comprises a box body, cooling pipes, an air inlet chamber and an air outlet chamber; the cooling pipes are arranged in the box body, cooling water is arranged in the box body, the cooling pipes are soaked in the cooling water, one end of each cooling pipe is communicated with the air inlet chamber, and the other end of each cooling pipe is communicated with the air outlet chamber; the coke tar removal condenser comprises a water collection tank, and the air outlet chamber is communicated with the water collection tank; the lower end of the air outlet chamber is communicated with the water collection tank through a tee, an outlet of the tee is a coke tar discharge opening and provided with a coke tar discharge switch, and the upper portion of the water collection tank is provided with a liquefied water discharge opening. By means of the coke tar removal condenser, water vapor in gas generated by a gasifier can be removed automatically, the coke tar can be discharged into a collection container at intervals, and the water vapor and the coke tar are removed effectively and thoroughly.
Description
Technical field
The present invention relates in combustion-gas jet test process the device removing tar and the steam contained in combustion gas, specifically a kind of tar removing cryophorus.
Background technology
At present, when carrying out tar removing and vapor-removing to the output gas of vapourizing furnace, not also being used for the equipment of tar removing and vapor-removing on the market specially, making in output gas, containing relatively large tar and steam, to reduce the quality of output gas.
Summary of the invention
The object of the invention is for the deficiencies in the prior art, and a kind of tar removing cryophorus is provided.This tar removing cryophorus not only can get rid of the steam in vapourizing furnace output gas automatically, and can with gap tar emission in collection container, remove steam and tar effectively, thoroughly.
The technical scheme realizing the object of the invention is:
A kind of tar removing cryophorus, comprise casing, cooling tube, inlet plenum and discharge chamber, described cooling tube is arranged in casing, is provided with water coolant in casing, and cooling tube is immersed in water coolant, and one end of cooling tube is communicated with inlet plenum, and the other end is communicated with discharge chamber.
Comprise header tank, described discharge chamber is communicated with header tank.
The lower end of described discharge chamber is communicated with header tank by threeway, and the outlet of threeway is tar relief outlet, and outlet is provided with tar exhausting switch, and the top of header tank is provided with liquefaction water relief outlet.
Described casing is provided with cooling water inlet pipe and water shoot, and water inlet pipe and water shoot are respectively equipped with water inlet switch and drainage switch, and water inlet pipe is arranged on the bottom of casing, and water shoot is arranged on the top of casing.
Described tar relief outlet is communicated with collection container.
The first dividing plate and second partition is respectively equipped with in inlet plenum and discharge chamber, inlet plenum is divided into the first inlet plenum and the second inlet plenum by the first dividing plate, discharge chamber is divided into the first discharge chamber and the second discharge chamber by second partition, first inlet plenum is communicated with the first discharge chamber by cooling tube, second inlet plenum is communicated with the second discharge chamber by cooling tube, first inlet plenum and the first discharge chamber are one group, and the second inlet plenum and the second discharge chamber are another group, and the cooling tube between two groups is not connected.
During use, inlet plenum is communicated with the escape pipe of vapourizing furnace, output gas containing tar and moisture is by the condensation of cooling tube, tar and hydrogenesis are in prolong, and flow to discharge chamber by thrust when producing exhalation flow, water of condensation is discharged from the liquefaction water relief outlet of the header tank communicated with discharge chamber, and tar is discharged from the tar relief outlet of threeway, is from discharge chamber gas out the combustion gas eliminating tar and steam.
This tar removing cryophorus not only can get rid of steam automatically, and can with gap tar emission in collection container, remove steam and tar effectively, thoroughly.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention;
Fig. 2 is the plan structure schematic diagram being provided with two groups of inlet plenums and discharge chamber in embodiment;
Fig. 3 is the right TV structure schematic diagram being provided with two groups of inlet plenums and discharge chamber in embodiment.
In figure, 1. casing 2. cooling tube 3. inlet plenum 3-1. first inlet plenum 3-2. second inlet plenum 4. discharge chamber 4-1. first discharge chamber 4-2. second discharge chamber 5. header tank 6. threeway 7. tar exhausting switch 8. liquefies water relief outlet 9. water inlet pipe 10. water shoot 11. first dividing plate 12. second partition.
Embodiment
Below in conjunction with drawings and Examples, content of the present invention is further elaborated, but is not limitation of the invention.
Embodiment:
With reference to Fig. 1, a kind of tar removing cryophorus, comprises casing 1, cooling tube 2, inlet plenum 3 and discharge chamber 4, described cooling tube 2 is arranged in casing 1, is provided with water coolant in casing 1, and cooling tube 2 is immersed in water coolant, one end of cooling tube 2 is communicated with inlet plenum 3, and the other end is communicated with discharge chamber 4.
Comprise header tank 5, described discharge chamber 4 is communicated with header tank 5.
The lower end of described discharge chamber 4 is communicated with header tank 5 by threeway 6, and the outlet of threeway 6 is tar relief outlet, and outlet is provided with tar exhausting switch 7, and the top of header tank 5 is provided with liquefaction water relief outlet 8.
Described casing 1 is provided with cooling water inlet pipe 9 and water shoot 10, and water inlet pipe 9 and water shoot 10 are respectively equipped with water inlet switch and drainage switch, and water inlet pipe 9 is arranged on the bottom of casing 1, and water shoot 10 is arranged on the top of casing 1.
Described tar relief outlet is communicated with collection container.
Discharge chamber 4 is provided with clean-up port, and clean-up port is provided with sealing cover.
With reference to Fig. 2 Fig. 3, the first dividing plate 11 and second partition 12 is respectively equipped with in inlet plenum 3 and discharge chamber 4, inlet plenum 3 is divided into the first inlet plenum 3-1 and the second inlet plenum 3-2 by the first dividing plate 11, discharge chamber 4 is divided into the first discharge chamber 4-1 and the second discharge chamber 4-2 by second partition 12, first inlet plenum 3-1 is communicated with the first discharge chamber 4-1 by cooling tube 2, second inlet plenum 3-2 is communicated with the second discharge chamber 4-2 by cooling tube 2, first inlet plenum 3-1 and the first discharge chamber 4-1 is one group, second inlet plenum 3-2 and the second discharge chamber 4-2 is another group, cooling tube between two groups is not connected.
During use, open water coolant water inlet switch and effluent switch, cooling tube 2 is allowed to be immersed in the water coolant of flowing, inlet plenum 3 is communicated with the extraction pipe of vapourizing furnace, output gas containing tar and moisture is by the condensation of cooling tube 2, tar and hydrogenesis are in cooling tube 2, and flow to discharge chamber 4 by thrust when producing exhalation flow, water of condensation is discharged from the header tank 5 communicated with discharge chamber 4, tar is discharged from the tar relief outlet of threeway 6, and tar is released in collection container collects by opening tar exhausting switch 7 discontinuously.The combustion gas eliminating tar and steam is from discharge chamber 4 output gas out.
Arrange the first inlet plenum 3-1, the second inlet plenum 3-2 and enter the first discharge chamber 4-1, the second discharge chamber 4-2 by many cooling tubes, make the condensation of output gas better, tar and steam are got rid of cleaner, effectively improve the quality of combustion gas.
Claims (3)
1. a tar removing cryophorus, is characterized in that, comprises casing, cooling tube, inlet plenum and discharge chamber, described cooling tube is arranged in casing, is provided with water coolant in casing, and cooling tube is immersed in water coolant, one end of cooling tube is communicated with inlet plenum, and the other end is communicated with discharge chamber;
Comprise header tank, described discharge chamber is communicated with header tank;
The lower end of described discharge chamber is communicated with header tank by threeway, and the outlet of threeway is tar relief outlet, and outlet is provided with tar exhausting switch, and the top of header tank is provided with liquefaction water relief outlet.
2. tar removing cryophorus according to claim 1, it is characterized in that, described casing is provided with cooling water inlet pipe and water shoot, and water inlet pipe and water shoot are respectively equipped with water inlet switch and drainage switch, water inlet pipe is arranged on the bottom of casing, and water shoot is arranged on the top of casing.
3. tar removing cryophorus according to claim 1, it is characterized in that, the first dividing plate and second partition is respectively equipped with in inlet plenum and discharge chamber, inlet plenum is divided into the first inlet plenum and the second inlet plenum by the first dividing plate, discharge chamber is divided into the first discharge chamber and the second discharge chamber by second partition, first inlet plenum is communicated with the first discharge chamber by cooling tube, second inlet plenum is communicated with the second discharge chamber by cooling tube, first inlet plenum and the first discharge chamber are one group, second inlet plenum and the second discharge chamber are another group, and the cooling tube between two groups is not connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510462259.2A CN105001919B (en) | 2015-07-31 | 2015-07-31 | A kind of application method of tar removing cryophorus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510462259.2A CN105001919B (en) | 2015-07-31 | 2015-07-31 | A kind of application method of tar removing cryophorus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105001919A true CN105001919A (en) | 2015-10-28 |
| CN105001919B CN105001919B (en) | 2018-04-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510462259.2A Active CN105001919B (en) | 2015-07-31 | 2015-07-31 | A kind of application method of tar removing cryophorus |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107304692A (en) * | 2016-04-21 | 2017-10-31 | 柳洋 | The engine oil port cover of moisture can be separated |
| CN110652784A (en) * | 2019-11-04 | 2020-01-07 | 河北省农林科学院农业资源环境研究所 | Biochar preparation system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201073562Y (en) * | 2007-08-09 | 2008-06-18 | 张树刚 | Gasifying stove tar moisture filtering purifier |
| CN201317766Y (en) * | 2008-12-24 | 2009-09-30 | 张建超 | Biomass gas composite filtering device |
| CN202936391U (en) * | 2012-06-15 | 2013-05-15 | 罗江平 | Biomass gasified fuel gas condenser |
| CN205011718U (en) * | 2015-07-31 | 2016-02-03 | 秦家运 | Remove tar water condenser |
-
2015
- 2015-07-31 CN CN201510462259.2A patent/CN105001919B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201073562Y (en) * | 2007-08-09 | 2008-06-18 | 张树刚 | Gasifying stove tar moisture filtering purifier |
| CN201317766Y (en) * | 2008-12-24 | 2009-09-30 | 张建超 | Biomass gas composite filtering device |
| CN202936391U (en) * | 2012-06-15 | 2013-05-15 | 罗江平 | Biomass gasified fuel gas condenser |
| CN205011718U (en) * | 2015-07-31 | 2016-02-03 | 秦家运 | Remove tar water condenser |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107304692A (en) * | 2016-04-21 | 2017-10-31 | 柳洋 | The engine oil port cover of moisture can be separated |
| CN110652784A (en) * | 2019-11-04 | 2020-01-07 | 河北省农林科学院农业资源环境研究所 | Biochar preparation system |
| CN110652784B (en) * | 2019-11-04 | 2024-03-22 | 河北省农林科学院农业资源环境研究所 | Biochar preparation system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105001919B (en) | 2018-04-03 |
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Effective date of registration: 20191021 Address after: 214500 Jiangsu city of Taizhou province Jiang Road, Xingang Economic Development Zone in Jingjiang No. 43 Patentee after: Jingjiang Jinzhou Ship Equipment Co.,Ltd. Address before: 541902, Guilin, the Guangxi Zhuang Autonomous Region, Yangshuo County Campbell Township on the River Village No. 50 Patentee before: Qin Jia Yun |