CN204514127U - A kind of building brick high temperature sintering flue gas heat-exchange unit - Google Patents
A kind of building brick high temperature sintering flue gas heat-exchange unit Download PDFInfo
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- CN204514127U CN204514127U CN201520174060.5U CN201520174060U CN204514127U CN 204514127 U CN204514127 U CN 204514127U CN 201520174060 U CN201520174060 U CN 201520174060U CN 204514127 U CN204514127 U CN 204514127U
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- Prior art keywords
- jet pipe
- flue gas
- high temperature
- building brick
- temperature sintering
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Abstract
The utility model discloses a kind of building brick high temperature sintering flue gas heat-exchange unit, comprise air-introduced machine and heat exchange tank body, the vertical setting of described heat exchange tank body is also cylindrical, is provided with that " " type heat exchanger tube, is provided with a spiral board to S inside the below of described heat exchange tank body in described heat exchange tank body; Some air jet pipe A and air jet pipe B are provided with in the gap of described " S " type heat exchanger tube, some pores are had on the surface of described air jet pipe A and air jet pipe B, described some air jet pipe A are connected with same air inlet pipe A, and described some air jet pipe B are connected with same air inlet pipe B.The utility model provides a kind of building brick high temperature sintering flue gas heat-exchange unit, regularly can carry out deashing process in heat exchanger inside, keeps heat exchanger inside unimpeded, reduces running resistance.
Description
Technical field
The utility model relates to heat exchanger, particularly relates to a kind of building brick high temperature sintering flue gas heat-exchange unit.
Background technology
Building brick generally adopts tunnel cave high temperature sintering to form, and the flue gas of release also has very high temperature under normal circumstances.Direct discharge can cause heat waste.Enterprise can utilize heat exchanger to re-use fume afterheat to reduce energy consumption under normal circumstances, also utilizes the protection of environment simultaneously.But in sintering process, in flue gas, a large amount of dust can be carried.Due to the accumulated plugging of dust after heat exchanger uses for a long time, very easily assembly heat exchanger heat transfer effect reduces, even because blocking causes the excessive accident causing blast of heat exchanger internal pressure.
Utility model content
Object of the present utility model is the defect overcoming prior art, provides a kind of building brick high temperature sintering flue gas heat-exchange unit, regularly can carry out deashing process in heat exchanger inside, keeps heat exchanger inside unimpeded, reduces running resistance.
The technical solution adopted in the utility model is:
A kind of building brick high temperature sintering flue gas heat-exchange unit, comprise air-introduced machine and heat exchange tank body, the vertical setting of described heat exchange tank body is also cylindrical, is provided with that " " type heat exchanger tube, is provided with a spiral board to S inside the below of described heat exchange tank body in described heat exchange tank body; Some air jet pipe A and air jet pipe B are provided with in the gap of described " S " type heat exchanger tube, some pores are had on the surface of described air jet pipe A and air jet pipe B, described some air jet pipe A are connected with same air inlet pipe A, and described some air jet pipe B are connected with same air inlet pipe B.
Further, described air inlet pipe A is connected with compressed air generator or steam raising plant with air inlet pipe B.
Further, described air inlet pipe A and air inlet pipe B are also connected with motor-driven valve and booster pump respectively.
Further, the motor-driven valve on described air inlet pipe A and the motor-driven valve of air inlet pipe B work or alternation simultaneously.
Further, some fins are provided with on the surface of described " S " type heat exchanger tube.
Further, below described air-introduced machine and heat exchange tank body, be provided with " U " type tube connector.
Further, be provided with a ring jet pipe in the below of described spiral board, described ring jet pipe is connected with compressed air generator and side towards described spiral board has some pores on the surface.
Further, the connecting line between described ring jet pipe and compressed air generator is provided with gas flow valve.
The beneficial effects of the utility model are:
The utility model structure is simple, spiral board is provided with in the bottom of heat exchange tank body, high-temperature flue gas enters in heat exchange tank body through the mode that spiral board effect is High Rotation Speed, and carry out heat with " S " type heat exchanger tube and hand over, high-temperature flue gas can be avoided directly to rush at " S " type heat exchanger tube and pile up in impact place, and the high-temperature flue gas rotated can also force the dust be partly adhered on " S " type heat exchanger tube to discharge heat exchanger with flue gas.On the other hand; some air jet pipe A and air jet pipe B are provided with in the gap of " S " type heat exchanger tube; simultaneously or alternately utilize compressed air or high steam to purge " S " type heat exchanger tube; prevent the accumulated plugging of dust; the not good and internal pressure of heat transfer effect is caused to increase; safe and reliable, the service life of " S " type heat exchanger tube can be extended, the number of times of power generating ratio maintenance.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
In order to make the advantage of the purpose of this utility model and technical scheme clearly understand, below in conjunction with accompanying drawing and example, the utility model is further elaborated.
As shown in Figure 1, a kind of building brick high temperature sintering flue gas heat-exchange unit, comprises air-introduced machine 1 and heat exchange tank body 2.The vertical setting of described heat exchange tank body 2 is also cylindrical, is provided with " S " type heat exchanger tube 3 in described heat exchange tank body 2.A spiral board 4 is provided with inside the below of described heat exchange tank body 2.In the gap of described " S " type heat exchanger tube 3, be provided with some air jet pipe A5 and air jet pipe B6, have some pores on the surface of described air jet pipe A5 and air jet pipe B6.Described some air jet pipe A5 are connected with same air inlet pipe A7, and described some air jet pipe B6 are connected with same air inlet pipe B8.
Further, described air inlet pipe A7 is connected with compressed air generator or steam raising plant with air inlet pipe B8, or the dust of compressed air vapours to " S " type heat exchanger tube 3 surface adhesion can be utilized to purge.When utilizing vapours to purge, because heat that steam is self-contained can reduce, the heat transfer effect of " S " type heat exchanger tube 3 with high-temperature flue gas is affected.
Further, described air inlet pipe A7 and air inlet pipe B8 are also connected with motor-driven valve 9 and booster pump 10 respectively, control the opening and closing of air jet pipe A5 and air jet pipe B6 and increase the pressure and jet velocity that purge.
Further, the motor-driven valve 9 on described air inlet pipe A7 and the motor-driven valve 9 of air inlet pipe B8 work or alternation simultaneously.Whole " S " type heat exchanger tube 3 is purged simultaneously, the dust of adhesion can be removed fast, but heat exchanging impact is larger.During alternation, air jet pipe A5 and air jet pipe B6 also alternation, can reduce the impact of heat exchanging while purging dust.
Further, be provided with some fins (not shown in FIG.) on the surface of described " S " type heat exchanger tube 3, increase heat exchange area.
Further, " U " type tube connector 11 is provided with below described air-introduced machine 1 and heat exchange tank body 2, enter in heat exchange tank body 2 after high-temperature flue gas baffling, in baffling process, the dust granules that in high-temperature flue gas, weight is larger sedimentation in " U " type tube connector 11 does not enter in heat exchange tank body 2.
Further, a ring jet pipe 12 is provided with in the below of described spiral board 4, described ring jet pipe 12 is connected with compressed air generator and side towards described spiral board 4 has some pores on the surface, can purge being attached to dust on spiral board 4.
Further, the connecting line between described ring jet pipe 12 and compressed air generator is provided with gas flow valve 13, the adjustable air mass flow purged spiral board 4.
Working method of the present utility model is:
High-temperature flue gas acts on through air-introduced machine 1, enters in heat exchange tank body 1 along " U " type tube connector 11.In the process, the dust granules that in high-temperature flue gas, weight is larger sedimentation in " U " type tube connector 11.High-temperature flue gas, when spiral board 4, forms eddy flow and carries out heat exchange with " S " type heat exchanger tube 3.When after work a period of time, air jet pipe A5 and air jet pipe B6 works, and utilizes compressed air or high steam to purge " S " type heat exchanger tube 3.Ring jet pipe 12 pairs of spiral boards 4 purge simultaneously.The dust departed from discharges heat exchange tank body 2 with high-temperature flue gas.After having cleaned, stop purging.In purge, heat exchange does not stop.
The utility model structure is simple, spiral board is provided with in the bottom of heat exchange tank body, high-temperature flue gas enters in heat exchange tank body through the mode that spiral board effect is High Rotation Speed, and carry out heat with " S " type heat exchanger tube and hand over, high-temperature flue gas can be avoided directly to rush at " S " type heat exchanger tube and pile up in impact place, and the high-temperature flue gas rotated can also force the dust be partly adhered on " S " type heat exchanger tube to discharge heat exchanger with flue gas.On the other hand; some air jet pipe A and air jet pipe B are provided with in the gap of " S " type heat exchanger tube; simultaneously or alternately utilize compressed air or high steam to purge " S " type heat exchanger tube; prevent the accumulated plugging of dust; the not good and internal pressure of heat transfer effect is caused to increase; safe and reliable, the service life of " S " type heat exchanger tube can be extended, the number of times of power generating ratio maintenance.
Claims (8)
1. a building brick high temperature sintering flue gas heat-exchange unit, comprise air-introduced machine (1) and heat exchange tank body (2), the vertical setting of described heat exchange tank body (2) is also cylindrical, in described heat exchange tank body (2), be provided with that " " type heat exchanger tube (3), is characterized in that S: inside the below of described heat exchange tank body (2), be provided with a spiral board (4); Some air jet pipe A(5 are provided with in the gap of described " S " type heat exchanger tube (3)) and air jet pipe B(6), at described air jet pipe A(5) and air jet pipe B(6) surface have some pores, described some air jet pipe A(5) with same air inlet pipe A(7) be connected, described some air jet pipe B(6) and with same air inlet pipe B(8) be connected.
2. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claim 1, is characterized in that: described air inlet pipe A(7) with air inlet pipe B(8) be connected with compressed air generator or steam raising plant.
3. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claims 1 or 2, is characterized in that: described air inlet pipe A(7) with air inlet pipe B(8) be also connected with motor-driven valve (9) and booster pump (10) respectively.
4. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claim 3, is characterized in that: described air inlet pipe A(7) on motor-driven valve (9) and air inlet pipe B(8) motor-driven valve (9) work or alternation simultaneously.
5. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claim 1,2 or 4, is characterized in that: be provided with some fins on the surface of described " S " type heat exchanger tube (3).
6. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claims 1 or 2, is characterized in that: be provided with " U " type tube connector (11) at described air-introduced machine (1) and heat exchange tank body (2) below.
7. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claim 1,2 or 4, it is characterized in that: be provided with a ring jet pipe (12) in the below of described spiral board (4), described ring jet pipe (12) is connected with compressed air generator and side towards described spiral board (4) has some pores on the surface.
8. a kind of building brick high temperature sintering flue gas heat-exchange unit according to claim 7, is characterized in that: the connecting line between described ring jet pipe (12) and compressed air generator is provided with gas flow valve (13).
Priority Applications (1)
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CN201520174060.5U CN204514127U (en) | 2015-03-26 | 2015-03-26 | A kind of building brick high temperature sintering flue gas heat-exchange unit |
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CN201520174060.5U CN204514127U (en) | 2015-03-26 | 2015-03-26 | A kind of building brick high temperature sintering flue gas heat-exchange unit |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107062281A (en) * | 2017-06-12 | 2017-08-18 | 扬州澄露环境工程有限公司 | The online clearing apparatus of round trip chilling |
CN110360830A (en) * | 2019-08-13 | 2019-10-22 | 瀚能(苏州)节能科技有限公司 | A kind of totally-enclosed powder flow heat pump drier |
-
2015
- 2015-03-26 CN CN201520174060.5U patent/CN204514127U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107062281A (en) * | 2017-06-12 | 2017-08-18 | 扬州澄露环境工程有限公司 | The online clearing apparatus of round trip chilling |
CN110360830A (en) * | 2019-08-13 | 2019-10-22 | 瀚能(苏州)节能科技有限公司 | A kind of totally-enclosed powder flow heat pump drier |
CN110360830B (en) * | 2019-08-13 | 2024-05-17 | 瀚能(苏州)节能科技有限公司 | Totally-enclosed powder flow heat pump dryer |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150729 Termination date: 20180326 |