CN204848787U - Condensation decoking device - Google Patents
Condensation decoking device Download PDFInfo
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- CN204848787U CN204848787U CN201520342314.XU CN201520342314U CN204848787U CN 204848787 U CN204848787 U CN 204848787U CN 201520342314 U CN201520342314 U CN 201520342314U CN 204848787 U CN204848787 U CN 204848787U
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- condensation
- water
- tank body
- cooling water
- removing appts
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Abstract
The utility model discloses a condensation decoking device, its characterized in that: condensation decoking device is including condensation decoking ware, this condensation decoking ware is including a jar body, be provided with the intake pipe on the jar body, the outlet duct, cooling water water inlet and cooling water outlet, at the internal pipeline that is equipped with of jar, trachea and the outlet duct communicates with each other or continuous with cooling water outlet with the cooling water water inlet respectively follows respectively for the both ends of this pipeline, be equipped with the burnt oil trap of water in the bottom of this jar of body, be equipped with the intake pipe of calming the anger on this water burnt oil trap upper portion, be equipped with row burnt pipe in the burnt oil trap's of this water bottom. In this condensation process, can additionally not produce waste water, the production of the waste water that has significantly reduced, simultaneously, and through lead to highly -compressed air to the intake pipe of calming the anger, the problem with regard to having solved pipe blockage like this, we are basic need not the processing like this, the equipment of running without interruption for a long time, and need not anxious pipe blockage problem, avoid often tearing open the pipeline and safeguarded the trouble of bringing.
Description
Technical field
The utility model relates to a kind of coke removing appts., particularly relates to a kind of condensation coke removing appts..
Background technology
The energy is one of three large problems of facing mankind, present human being's production.The required energy of life is mainly from non-renewable " fossil energy "---coal, oil; But coal and petroleum resources irreversibly reduce; there is exhausted one day eventually; and coal, oil produce the concern that more and more serious environmental problem and potential energy dilemma have obtained the whole society; therefore utilize refuse (comprising the organism etc. in discarded plant and domestic refuse) to carry out the production that renewable energy resources exploitation replaces current coal and oil for material, it more and more receives the concern of people.
Along with progress and the development of society, the refuse such as rubbish or plant is carried out cracking by people, thus generation inflammable gas, usually this cracking process completes in pyrolyzer, and from pyrolyzer high-temperature gas mixture out because temperature is too high, can not meet need of production, in addition, containing a large amount of tar in gas mixture, in high-temperature gas mixture temperature-fall period, the water tar of formation very easily causes the blocking in mixed gas pipeline road.
In addition, adopt the burnt method of pure water eccysis in prior art, gas mixture directly collides with water, mixes, although can lower the temperature rapidly, the particulate state tar produced in gas mixture directly enters in water, causes water pollution, adds the pressure of wastewater treatment.
Utility model content
The technical problems to be solved in the utility model is the present situation for prior art, provides one can reduce mixture temperature fast, and should not produce waste water, thus greatly alleviate wastewater treatment pressure, meanwhile, avoids water tar to block the condensation coke removing appts. of pipeline.
The utility model solves the problems of the technologies described above adopted technical scheme: a kind of condensation coke removing appts., it is characterized in that: described condensation coke removing appts. includes condensation decoking device, this condensation decoking device comprises tank body, tank body is provided with inlet pipe, escape pipe, cooling water intake and cooling water outlet, pipeline is provided with in tank body, the two ends of this pipeline tracheae that follows up respectively communicates with escape pipe or is connected with cooling water outlet with cooling water intake respectively, water tar well is provided with in the bottom of this tank body, inlet pipe of calming the anger is provided with on this water tar well top, coke discharging tube is provided with in the bottom of this water tar well.
Wherein, pipeline for gas mixture and water coolant isolation has two kinds of mode of connection, one of them is, described pipeline is prolong, this prolong has many, and inlet pipe is arranged on the upper end of tank body, and escape pipe is arranged on the lower end of tank body, follow up respectively tracheae and escape pipe of the two ends of this prolong communicates, and water tar well top communicates with escape pipe.In order to improve heat diffusion, described prolong is provided with radiator element.
Another kind of mode is that described pipeline is circulating line, and cooling water intake is arranged on the lower end of tank body, and cooling water outlet is arranged on the upper end of tank body, and the two ends of this circulating line are connected with cooling water outlet with cooling water intake respectively.
Wherein, circulating line can have multiple set-up mode, and wherein one is, the two ends of described circulating line, for gathering pipe, are gathered to be connected with between pipe at two and axially arranged multiple return line along tank body, and described return line is covered with tank interior space.
Another kind of mode is, described circulating line is along inner tank wall circumference annular spread, and circulating line is covered with tank interior space.
For the ease of cooling the collection of rear water tar, the connection section of described tank body lower end and water tar well is tapered.
For the ease of maintenance, described inlet pipe and escape pipe place are respectively equipped with access hole.
In order to control the opening and closing of water tar well, the upper end of described water tar well is provided with water tar and enters valve, is provided with water tar outlet valve in the lower end of water tar well.
In order to realize classification cooling, described condensation coke removing appts. has multiple condensation decoking device, and each condensation decoking device is connected together mutually.
Compared with prior art, owing to the utility model has the advantage of: the high-temperature gas mixture produced from pyrolyzer enters in inlet pipe, in escape pipe process out, water coolant enters in tank body from outside, high-temperature gas mixture temperature is reduced rapidly, because the pipeline in tank body is by water coolant and gas mixture isolation, water coolant does not directly contact with gas mixture, and water coolant can recycle, thus while reduction mixture temperature, avoid the generation of waste water, greatly alleviate the pressure of wastewater treatment; In addition, tar in high-temperature gas mixture and water-cooled congeal into water tar along inner tank wall following current to water tar well, when being collected into a certain amount of to water tar well, by passing into high-pressure air to inlet pipe of calming the anger, water tar is discharged, thus avoid these water tar and follow gas mixture and directly enter in transport pipe, cause the blocking of pipeline.
Accompanying drawing explanation
Fig. 1 is the structural representation (pipeline is circulating line) of condensation decoking device in the utility model;
Fig. 2 is the structural representation (pipeline is prolong) of condensation decoking device in the utility model;
Fig. 3 is the diagrammatic cross-sectional view at A-A place in Fig. 2.
Embodiment
Below in conjunction with accompanying drawing embodiment, the utility model is described in further detail.
As shown in Figures 1 to 3, the utility model discloses a kind of condensation coke removing appts., described condensation coke removing appts. includes condensation decoking device 1, and this condensation decoking device 1 quantity can arrange multiple.Each condensation decoking device 1 comprises tank body 11, tank body 11 is provided with inlet pipe 14, escape pipe 15, cooling water intake 111 and cooling water outlet 110, for the ease of observing, overhauling, inlet pipe 14 and escape pipe 15 place are respectively equipped with access hole 13, in addition, water tar well 16 is provided with in the bottom of this tank body 11, for the ease of cooling the collection of rear water tar, the connection section of described tank body 11 lower end and water tar well 16 is tapered, be provided with on this water tar well 16 top inlet pipe 17 of calming the anger, be provided with coke discharging tube 19 in the bottom of this water tar well 16.In addition, in order to control the opening and closing of water tar well 16, the upper end of described water tar well 16 is provided with water tar and enters valve 181, is provided with water tar outlet valve 182 in the lower end of water tar well 16.
The utility model in order to realize by gas mixture and water coolant isolated, pipeline is provided with in tank body 11, this pipeline has two kinds of mode of connection, and one of them is that described pipeline is prolong 120, this prolong 120 has many, inlet pipe 14 is arranged on the upper end of tank body 11, and escape pipe 15 is arranged on the lower end of tank body 11, and follow up respectively tracheae 14 and escape pipe 15 of the two ends of this prolong 120 communicates, water tar well 16 top communicates with escape pipe 15, as shown in Figure 2,3.In addition, in order to improve heat diffusion, described prolong 120 is provided with radiator element 121, this radiator element 121 adopts the mode of splicing to be connected on prolong 120, thus improves multiple radiator element 121 and pacify the convenience of tearing open.
Another kind of mode is that described pipeline is circulating line 12, and the two ends of this circulating line 12 are connected with cooling water outlet 110 with cooling water intake 111 respectively.This lower end cooling water intake 111 being arranged on tank body 11, cooling water outlet 110 is arranged on the mode of the upper end of tank body 11, is conducive to slowing down, the flow velocity of water coolant in circulating line 12, make water coolant can take away more heat, improve cooling performance.
Wherein, circulating line 12 can have multiple set-up mode, and wherein one is, the two ends of described circulating line 12, for gathering pipe, are gathered to be connected with between pipe at two and axially arranged multiple return line along tank body, and described return line is covered with tank body 11 internal space.
Another kind of mode is, described circulating line 12 is along tank body 11 inwall circumference annular spread, and circulating line 12 is covered with tank body 11 internal space.
In embodiment of the present utility model, in order to improve cooling-down effect, adopt the method for classification cooling, namely described condensation decoking device 1 is in series with multiple, preferably, in embodiment of the present utility model, three condensation decoking devices 1 of connecting, particularly, the escape pipe 15 of previous condensation decoking device 1 is made to be connected can to realize with the inlet pipe 14 of a rear adjacent condensation decoking device 1.
The utility model utilizes specific heat of water high, gasification absorbs the characteristic of heat, water coolant is connected at the cooling water intake 111 of tank body 11, finally flow out from the cooling water outlet 110 of tank body 11 upper end, simultaneously, the high-temperature gas mixture produced from pyrolyzer then enters from the inlet pipe 14 of tank body 11, and flow out from escape pipe 15, in the process, high-temperature gas mixture in tank body 11 is under the effect of water coolant, , make to reduce from condensation decoking device 1 high-temperature gas mixture temperature out, one can be made to land vertically less than 60 degrees Celsius, because the pipeline in tank body 11 is by water coolant and gas mixture isolation, water coolant does not directly contact with gas mixture, and water coolant can recycle, thus while reduction mixture temperature, avoid the generation of waste water, greatly alleviate the pressure of wastewater treatment, in addition, tar of fetching boiling water enters valve 181, tar in high-temperature gas mixture and water-cooled are congealed into water tar, water tar is collected in water tar well 16, in time collecting a certain amount of, and tar outlet valve 182 of fetching boiling water, in inlet pipe 17 of calming the anger, pass into high-pressure air simultaneously, make water tar be discharged condensation decoking device 1 by coke discharging tube 19, avoid life-time service, the water tar that condensation decoking device 1 produces blocks pipeline.
To sum up, in this condensation process, can not additional wastewater generation, with traditional with compared with Water warfare, greatly reduce the generation of waste water, alleviate wastewater treatment pressure, this process can purify the tar of more than 98% substantially, meanwhile, by leading to high-pressure air to inlet pipe 17 of calming the anger, this addresses the problem the problem of line clogging, we are basic like this need not process, can be run without interruption equipment for a long time, and without the need to worrying line clogging problem, avoid the trouble of often tearing pipeline open to safeguard and bringing.
Claims (10)
1. a condensation coke removing appts., it is characterized in that: described condensation coke removing appts. includes condensation decoking device, this condensation decoking device comprises tank body, tank body is provided with inlet pipe, escape pipe, cooling water intake and cooling water outlet, pipeline is provided with in tank body, the two ends of this pipeline tracheae that follows up respectively communicates with escape pipe or is connected with cooling water outlet with cooling water intake respectively, water tar well is provided with in the bottom of this tank body, be provided with on this water tar well top inlet pipe of calming the anger, be provided with coke discharging tube in the bottom of this water tar well.
2. condensation coke removing appts. according to claim 1, it is characterized in that: described pipeline is prolong, this prolong has many, inlet pipe is arranged on the upper end of tank body, escape pipe is arranged on the lower end of tank body, follow up respectively tracheae and escape pipe of the two ends of this prolong communicates, and water tar well top communicates with escape pipe.
3. condensation coke removing appts. according to claim 2, is characterized in that: described prolong is provided with radiator element.
4. condensation coke removing appts. according to claim 1, it is characterized in that: described pipeline is circulating line, cooling water intake is arranged on the lower end of tank body, and cooling water outlet is arranged on the upper end of tank body, and the two ends of this circulating line are connected with cooling water outlet with cooling water intake respectively.
5. condensation coke removing appts. according to claim 4, is characterized in that: the two ends of described circulating line, for gathering pipe, are gathered to be connected with between pipe at two and axially arranged multiple return line along tank body, and described return line is covered with tank interior space.
6. condensation coke removing appts. according to claim 4, is characterized in that: described circulating line is along inner tank wall circumference annular spread, and circulating line is covered with tank interior space.
7. condensation coke removing appts. according to claim 1, is characterized in that: the connection section of described tank body lower end and water tar well is tapered.
8. condensation coke removing appts. according to claim 1, is characterized in that: described inlet pipe and escape pipe place are respectively equipped with access hole.
9. condensation coke removing appts. according to claim 1, is characterized in that: the upper end of described water tar well is provided with water tar and enters valve, is provided with water tar outlet valve in the lower end of water tar well.
10. the condensation coke removing appts. according to any one of claim 1 to 9, is characterized in that: described condensation coke removing appts. has multiple condensation decoking device, and each condensation decoking device is connected together mutually.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520342314.XU CN204848787U (en) | 2015-05-26 | 2015-05-26 | Condensation decoking device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520342314.XU CN204848787U (en) | 2015-05-26 | 2015-05-26 | Condensation decoking device |
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| Publication Number | Publication Date |
|---|---|
| CN204848787U true CN204848787U (en) | 2015-12-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520342314.XU Active CN204848787U (en) | 2015-05-26 | 2015-05-26 | Condensation decoking device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104927927A (en) * | 2015-05-26 | 2015-09-23 | 张文虎 | Condensation decoking device |
| CN111359250A (en) * | 2020-03-30 | 2020-07-03 | 常州翊翔炭材科技有限公司 | Carbon/carbon composite material chemical vapor deposition high-temperature tail gas condensation filtering structure |
| CN117732195A (en) * | 2024-02-20 | 2024-03-22 | 太原理工大学 | Tar and nitrogenous substance collection device of coal pyrolysis |
-
2015
- 2015-05-26 CN CN201520342314.XU patent/CN204848787U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104927927A (en) * | 2015-05-26 | 2015-09-23 | 张文虎 | Condensation decoking device |
| CN111359250A (en) * | 2020-03-30 | 2020-07-03 | 常州翊翔炭材科技有限公司 | Carbon/carbon composite material chemical vapor deposition high-temperature tail gas condensation filtering structure |
| CN117732195A (en) * | 2024-02-20 | 2024-03-22 | 太原理工大学 | Tar and nitrogenous substance collection device of coal pyrolysis |
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Effective date of registration: 20180528 Granted publication date: 20151209 |
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Date of cancellation: 20210528 Granted publication date: 20151209 |
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