CN201634627U - Asphalt and tar melter - Google Patents
Asphalt and tar melter Download PDFInfo
- Publication number
- CN201634627U CN201634627U CN2010201140533U CN201020114053U CN201634627U CN 201634627 U CN201634627 U CN 201634627U CN 2010201140533 U CN2010201140533 U CN 2010201140533U CN 201020114053 U CN201020114053 U CN 201020114053U CN 201634627 U CN201634627 U CN 201634627U
- Authority
- CN
- China
- Prior art keywords
- tar
- asphalt
- tank body
- pipeline
- melter
- 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 - Lifetime
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- Working-Up Tar And Pitch (AREA)
Abstract
The utility model relates to an asphalt and tar melting device, in particular to an asphalt and tar melter. The melter comprises a tank body; a feed opening is formed at the top of the tank body; a heating chamber is arranged at the bottom of the tank body; a chimney is arranged on and communicated with the heating chamber; a discharge opening is formed on one side at the bottom of the tank body, and is connected with a discharge pipeline; a discharge valve is arranged on the discharge pipeline; a steam coil is arranged inside the tank body; and the air inlet end and the air outlet end of the steam coil are communicated with a steam boiler arranged outside the tank body. The asphalt and tar melter provided by the utility model can better keep balance of asphalt and tar melting temperature, thereby improving the usage quality of asphalt and tar melt.
Description
Technical field
The utility model relates to a kind of asphalt tar melting appartus, relates in particular to a kind of asphalt tar melting tank.
Background technology
As everyone knows, in the process of producing gac, it is bonding with coal to need pitch and tar to make tamanori, back output gac, this process can increase the gac productive rate, pitch and tar also can be done the raw material of gac, so the quality of the fusions of pitch and tar will directly influence the Activated Carbon Production rate, existing device with pitch and tar thawing is only to heat with naked light, its shortcoming is that the local temperature of the asphalt tar that is melted is too high, make the asphalt tar coking, cause the asphalt tar degrees of fusion to reduce, influence the functional quality of asphalt tar.
The utility model content
For addressing the above problem, the utility model provides a kind of can keep the equilibrium of asphalt tar temperature of fusion preferably, thereby improves the asphalt tar melter that asphalt tar melts the functional quality of thing.
Asphalt tar melter of the present utility model, wherein, comprise tank body, the top of described tank body is provided with opening for feed, and the bottom of described tank body is provided with heating chamber, be communicated with on the described heating chamber and be provided with chimney, one side of described tank base is provided with discharge port, and described discharge port connects the discharging pipeline, and described discharging pipeline is provided with the discharging valve, it is characterized in that: be provided with steam coils in the described tank body, the inlet end of described steam coils all communicates with the steam oven that is located at described tank body outside with the outlet side.
Asphalt tar melter of the present utility model wherein, also comprises mesh screen, and described mesh screen is arranged on the top of steam coils in the described tank body, and described tank body is divided into upper and lower two chambers, and wherein, upper chamber is the blanking chamber, and lower chambers is a heating chamber.
Asphalt tar melter of the present utility model wherein, also comprises the tar test tank, and described tar test tank is communicated with described blanking chamber by the tar pipe.
Asphalt tar melter of the present utility model, wherein, described tar pipe stretches into described blanking chamber by described opening for feed.
Asphalt tar melter of the present utility model, wherein, the other end of described discharging pipeline is communicated with stirrer.
Asphalt tar melter of the present utility model, wherein, be equipped with successively from left to right on the described discharging pipeline and be provided with discharging valve, second threeway, tar pump, first threeway and the 3rd valve, the side pipe of described first threeway is communicated with described blanking chamber by first pipeline, and described first pipeline is provided with first valve.
Asphalt tar melter of the present utility model, wherein, the side pipe of described second threeway is communicated with overflow tar holding tank by second pipeline, and described overflow tar holding tank is communicated with described blanking chamber by described the 3rd pipeline.
Asphalt tar melter of the present utility model, wherein, described second pipeline is provided with second valve.
Asphalt tar melter of the present utility model, wherein, described steam coils is a weldless steel tube.
The beneficial effect of the utility model asphalt tar melter is: in tank body, is provided with steam coils, can heats faster, and homogeneous heating, thereby more help improving the functional quality that asphalt tar melts thing.
In tank body, be provided with mesh screen, block pitch can be filtered on screen cloth, thereby guaranteed the quality that asphalt tar melts thing in the heating chamber.
Adopt the tar test tank to add tar, can better grasp tar and bituminous is put into ratio, thereby require to regulate the quality that asphalt tar melts thing according to difference.
The discharging pipeline the other end is connected with stirrer, can strengthens tar and bituminous thaw process with stirrer.
Adopt first pipeline that discharging pipeline and blanking chamber are communicated with, undesirable thawing thing can be refilled the heating that circulates in the tank body.
Adopt second pipeline that discharging pipeline and overflow tar holding tank are communicated with, the 3rd pipeline is communicated with overflow tar holding tank and blanking chamber, a large amount of foams that can effectively pitch be produced in melting process and the tar that overflows reclaims injection blanking chamber, back again.
Description of drawings
Fig. 1 is the structure sectional view of the utility model asphalt tar melting tank.
Embodiment
Below in conjunction with Figure of description the utility model asphalt tar melting tank is described further.
Referring to Fig. 1, asphalt tar melting tank of the present utility model, comprise tank body 1, horizontal welding is connected to mesh screen 12 in the tank body 1, tank body 1 is divided into blanking chamber 13 and heating chamber 14, heating chamber 14 is positioned at the below in blanking chamber 13, the top of tank body 1 is provided with opening for feed 2, tar test tank 15 is communicated with blanking chamber 13 by tar pipe 16, tar test tank 15 and metope be (not shown) fixedly, tar pipe 16 stretches into blanking chamber 13 from opening for feed 2, tank body 1 bottom is provided with the heating chamber 3 that links into an integrated entity with tank body 1, the trailing flank connection of heating chamber 3 is welded with chimney 4, be provided with the steam coils 8 that weldless steel tube is made in the heating chamber 14, the inlet end 9 of steam coils 8 all communicates with the steam oven 11 that is located at tank body 1 outside with outlet side 10, the right side of tank body 1 bottom is provided with discharge port 5, discharge port 5 connects discharging pipeline 6, the other end of discharging pipeline 6 is communicated with stirrer 17, discharging valve 7 is installed on the discharging pipeline 6 successively, second threeway 23, tar pump 18, first threeway 19 and the 3rd valve 22, wherein, the side pipe of first threeway 19 is communicated with blanking chamber 13 by first pipeline 20, and first valve 21 is installed on first pipeline 20, the side pipe of second threeway 23 is communicated with overflow tar holding tank 25 by second pipeline 24, and second valve 26 is installed on second pipeline 24, and overflow tar holding tank 25 is communicated with blanking chamber 13 by the 3rd pipeline 27.
The working process of the utility model asphalt tar melting tank is as follows: the pitch of earlier needs being allocated into claims jin, inject in the tank body 1 from tar test tank 15 at the tar that needs are allocated into then, pitch is put into tank body 1 from opening for feed 2, owing to be provided with mesh screen 12 in the tank body 1, the pitch of bulk by mesh screen 12 every in the blanking chamber 13, at the bottom of having avoided bulk pitch directly to sink to jar, the pitch of fritter falls into heating chamber 14 and melts, being located at steam coils 8 in the heating chamber 14 and the heating chamber 3 that is positioned at tank body 1 bottom heat the pitch thawing that makes tank body 1 simultaneously and admixes with tar and be in the same place, when the tar overflow occurring, tar can flow in the overflow tar holding tank 25, open second valve 26 and first valve 21, with tar pump 18 tar in the overflow tar holding tank 25 is drawn back to blanking chamber 13 and to be heated once more, circulation always, when the thawing of the tar-bitumen in the heating chamber 14 does not reach requirement, open the discharging valve 7 and first valve 21, it is drawn back to blanking chamber 13 heat once more, circulation always, tar-bitumen thawing in heating chamber 14 reaches requirement, open discharging valve 7 and the 3rd valve 22, be injected in the stirrer 17 and stir at last, extract tar-bitumen and melt liquid.
Above embodiment is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; under the prerequisite that does not break away from the utility model design spirit; various distortion and improvement that the common engineering technical personnel in this area make the technical solution of the utility model all should fall in the definite protection domain of claims of the present utility model.
Claims (9)
1. asphalt tar melter, comprise tank body, the top of described tank body is provided with opening for feed, the bottom of described tank body is provided with heating chamber, is communicated with on the described heating chamber to be provided with chimney, and a side of described tank base is provided with discharge port, described discharge port connects the discharging pipeline, described discharging pipeline is provided with the discharging valve, it is characterized in that: be provided with steam coils in the described tank body, the inlet end of described steam coils all communicates with the steam oven that is located at described tank body outside with the outlet side.
2. asphalt tar melter according to claim 1 is characterized in that: also comprise mesh screen, described mesh screen is arranged on the top of steam coils in the described tank body, and described tank body is divided into upper and lower two chambers, wherein, upper chamber is the blanking chamber, and lower chambers is a heating chamber.
3. asphalt tar melter according to claim 2 is characterized in that: also comprise the tar test tank, described tar test tank is communicated with described blanking chamber by the tar pipe.
4. asphalt tar melter according to claim 3 is characterized in that: described tar pipe stretches into described blanking chamber by described opening for feed.
5. asphalt tar melter according to claim 4 is characterized in that: the other end of described discharging pipeline is communicated with stirrer.
6. asphalt tar melter according to claim 5, it is characterized in that: be equipped with successively from left to right on the described discharging pipeline and be provided with discharging valve, second threeway, tar pump, first threeway and the 3rd valve, the side pipe of described first threeway is communicated with described blanking chamber by first pipeline, and described first pipeline is provided with first valve.
7. asphalt tar melter according to claim 6 is characterized in that: the side pipe of described second threeway is communicated with overflow tar holding tank by second pipeline, and described overflow tar holding tank is communicated with described blanking chamber by described the 3rd pipeline.
8. asphalt tar melter according to claim 7 is characterized in that: described second pipeline is provided with second valve.
9. according to the described asphalt tar melter of each claim of 1-8, it is characterized in that: described steam coils is a weldless steel tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201140533U CN201634627U (en) | 2010-02-09 | 2010-02-09 | Asphalt and tar melter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201140533U CN201634627U (en) | 2010-02-09 | 2010-02-09 | Asphalt and tar melter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201634627U true CN201634627U (en) | 2010-11-17 |
Family
ID=43079116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201140533U Expired - Lifetime CN201634627U (en) | 2010-02-09 | 2010-02-09 | Asphalt and tar melter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201634627U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102732281A (en) * | 2012-07-16 | 2012-10-17 | 冀州信诚化工设备科技有限公司 | Lake asphalt melting and stirring system |
-
2010
- 2010-02-09 CN CN2010201140533U patent/CN201634627U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102732281A (en) * | 2012-07-16 | 2012-10-17 | 冀州信诚化工设备科技有限公司 | Lake asphalt melting and stirring system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170713 Address after: 102200, room 21, 420 torch street, Changping District science and Technology Park, Beijing Patentee after: Beijing Nuomansibai Environmental Protection Technology Co., Ltd. Address before: 100101 Beijing City, Chaoyang District Road No. 19 Xiao Ying Yu building 311 room Co-patentee before: Li Shengke Patentee before: Zou Yan Co-patentee before: Han Donghai Co-patentee before: Lang Jurong |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171012 Address after: 030006 B1 zone 3, block B, 402 South Central Street, Taiyuan hi tech Zone, Shanxi Patentee after: SHANXI QINGHUAN NENGCHUANG ENVIRONMENTAL TECHNOLOGY CO., LTD. Address before: 102200, room 21, 420 torch street, Changping District science and Technology Park, Beijing Patentee before: Beijing Nuomansibai Environmental Protection Technology Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20101117 |
|
| CX01 | Expiry of patent term |