CN201482469U - Hot air heating device for water reducer reaction kettle - Google Patents
Hot air heating device for water reducer reaction kettle Download PDFInfo
- Publication number
- CN201482469U CN201482469U CN2009200314874U CN200920031487U CN201482469U CN 201482469 U CN201482469 U CN 201482469U CN 2009200314874 U CN2009200314874 U CN 2009200314874U CN 200920031487 U CN200920031487 U CN 200920031487U CN 201482469 U CN201482469 U CN 201482469U
- Authority
- CN
- China
- Prior art keywords
- reactor
- hot
- hot air
- reaction kettle
- furnace
- 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
Links
- 229920002456 HOTAIR Polymers 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 239000003638 reducing agent Substances 0.000 title claims abstract description 15
- 238000010438 heat treatment Methods 0.000 title claims abstract description 11
- 238000006243 chemical reaction Methods 0.000 title abstract description 8
- 238000002485 combustion reaction Methods 0.000 claims abstract description 15
- 239000007789 gas Substances 0.000 claims abstract description 13
- 238000009825 accumulation Methods 0.000 claims description 10
- 239000002826 coolant Substances 0.000 claims description 7
- 239000002737 fuel gas Substances 0.000 claims description 4
- 230000000630 rising Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000571 coke Substances 0.000 abstract description 2
- 238000005338 heat storage Methods 0.000 abstract 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N naphthalene Chemical compound 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C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 4
- 238000006482 condensation reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Abstract
The utility model discloses a hot air heating device for a water reducer reaction kettle, which comprises a reaction kettle and a heat supplying device, wherein the outer wall of the reaction kettle is provided with a jacket which is communicated with the heat supplying device through a pipe, the heat supplying device is a gas hot air furnace, a furnace body is provided with a combustion chamber, a furnace opening is arranged at the lateral lower part of the hot air furnace and is internally provided with a gas furnace head, the combustion chamber is internally provided with a heat storage block, a hot air outlet is arranged at the upper part of the furnace body and is connected with a lower opening of the jacket of the reaction kettle through a pipe, and an upper opening of the jacket of the reaction kettle is connected with an induced draft fan. The utility model mainly utilizes combustible gases, such as coke oven tail gas and the like, as energy resources for heating the reaction kettle, can improve the production efficiency, and has the advantages of low energy consumption, rapid temperature raise, simple equipment and the like.
Description
Technical field
The utility model belongs to water reducer production equipment technical field, particularly relates to the firing equipment in a kind of high efficiency water reducing agent production.
Background technology
High efficiency water reducing agent is widely used in concrete workses such as highway, electric power, water conservancy.Naphthalene water reducer is the present output maximum of China, uses the widest high efficiency water reducing agent, and it is primary raw material with the crude naphthalene, makes through sulfonating reaction, hydrolysis, condensation reaction, neutralization reaction.Steam or heat-conducting oil heating are adopted in existing high efficiency water reducing agent production more, the equipment complexity, and the energy consumption height, the thermal efficiency is low, and preheating time is long.
Summary of the invention
The technical problems to be solved in the utility model provides that a kind of equipment is simple, the thermal efficiency is high, heats high efficiency water reducing agent reactor hot air heating apparatus rapidly.
For solving the problems of the technologies described above, the utility model comprises reactor and heater, and the reactor outer wall is provided with chuck, and this chuck is connected with pipeline with heater, its design feature is that heater is a fuel gas hot-blast stove, body of heater is provided with the combustion chamber, and fire door is located at the hot-blast stove side lower part, wherein is provided with gas burner, be provided with the heat accumulation piece in the combustion chamber, hot-blast outlet is located at upper of furnace body, and it is connected by pipeline with the reacting kettle jacketing end opening, and reacting kettle jacketing is suitable for reading to join with air-introduced machine.
Be provided with the layer 2-3 diaphragm plate in the described combustion chamber, three faces of every layer of diaphragm plate and combustion chamber join, and furnace inner space is revolution rising shape hot-air channel; Diaphragm plate top is equipped with the heat accumulation piece, and heat accumulation piece cross arrangement in length and breadth becomes trellis, and the hot-blast stove side lower part is provided with 3-4 fire door.
Be provided with cooler between reactor and air-introduced machine, wherein be provided with cooling medium, induced duct passes cooling medium.
Because the utility model heater is a fuel gas hot-blast stove, high-temperature hot-air directly enters reacting kettle jacketing through pipeline and heats, and equipment is simple, and the thermal medium speed of service is fast, heats up rapidly, need not preheating, high efficiency; Medium self heat accumulation is few, and energy consumption is low.Be particularly suitable for utilizing imflammable gas such as coke oven tail gas to heat as the energy, both energy savings reduced environmental pollution again.
Description of drawings
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is further described:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model hot-blast stove.
Among the figure: 1, heater, 2, reactor, 3, cooler, 4, air-introduced machine, 5, the combustion chamber, 6, gas burner, 7, pipeline, 8, chuck, 9, the heat accumulation piece, 10, cooling medium, 11, hot-blast outlet, 12, the chuck end opening, 13, chuck is suitable for reading, and 14, gas pipeline, 15, diaphragm plate, 16, hot-air channel, 17, fire door.
The specific embodiment
With reference to accompanying drawing, this water reducer reactor hot air heating apparatus comprises reactor 2, heater 1 and cooler 3, on reactor 2 outer walls, be provided with chuck 8, this chuck 8 is connected with pipeline 7 with heater 1, cooler 3, heater 1 is a fuel gas hot-blast stove, and body of heater is provided with combustion chamber 5, is provided with layer 2-3 diaphragm plate 15 in the combustion chamber 5, every layer of diaphragm plate 15 joins with three faces of combustion chamber 5, and furnace inner space is divided into revolution rising shape hot-air channel 16.The hot-blast stove side lower part is provided with 3-4 fire door 17, is equipped with gas burner 6 in each fire door 17, and gas burner 6 is its air feed by gas pipeline 14.5 bottoms, combustion chamber and diaphragm plate 15 tops are equipped with heat accumulation piece 9, and heat accumulation piece 9 cross arrangement in length and breadth becomes trellis.Hot-blast outlet 11 is located at upper of furnace body, hot-blast outlet 11 is connected by pipeline 7 with reactor 2 chuck end openings 12, reactor 2 chucks suitable for reading 13 join by induced duct and air-introduced machine 4, be provided with cooler 3 therebetween, be provided with cooling medium 10 in the cooler 3, induced duct passes cooling medium 10, with further reduction heat medium temperature, reduces thermal losses.
Claims (4)
1. water reducer reactor hot air heating apparatus, comprise reactor (2) and heater (1), reactor (2) outer wall is provided with chuck (8), this chuck (8) is connected with pipeline (7) with heater (1), it is characterized in that heater (1) is a fuel gas hot-blast stove, body of heater is provided with combustion chamber (5), fire door (17) is located at the hot-blast stove side lower part, wherein be provided with gas burner (6), be provided with heat accumulation piece (9) in the combustion chamber (5), hot-blast outlet (11) is located at upper of furnace body, and it is connected by pipeline (7) with reactor (2) chuck end opening (12), and reactor (2) chuck (13) suitable for reading joins with air-introduced machine (4).
2. according to the described water reducer reactor of claim 1 hot air heating apparatus, it is characterized in that being provided with in the combustion chamber (5) layer 2-3 diaphragm plate (15), every layer of diaphragm plate (15) joins with three faces of combustion chamber (5), and furnace inner space is divided into revolution rising shape hot-air channel (16).
3. according to the described water reducer reactor of claim 2 hot air heating apparatus, it is characterized in that diaphragm plate (15) top is equipped with heat accumulation piece (9), heat accumulation piece (9) cross arrangement in length and breadth becomes trellis, and hot-blast stove (1) side lower part is provided with 3-4 fire door (17).
4. according to the described water reducer reactor of claim 1 hot air heating apparatus, it is characterized in that being provided with cooler (3) between reactor (2) and air-introduced machine (4), wherein be provided with cooling medium (10), induced duct passes cooling medium (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200314874U CN201482469U (en) | 2009-08-08 | 2009-08-08 | Hot air heating device for water reducer reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200314874U CN201482469U (en) | 2009-08-08 | 2009-08-08 | Hot air heating device for water reducer reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201482469U true CN201482469U (en) | 2010-05-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200314874U Expired - Lifetime CN201482469U (en) | 2009-08-08 | 2009-08-08 | Hot air heating device for water reducer reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201482469U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104014292A (en) * | 2013-03-01 | 2014-09-03 | 辽宁瑞兴化工集团有限公司 | Reaction kettle for producing phosphorus pentasulfide |
| WO2016192405A1 (en) * | 2015-05-29 | 2016-12-08 | 浙江科技学院 | Hydrothermal reaction kettle |
-
2009
- 2009-08-08 CN CN2009200314874U patent/CN201482469U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104014292A (en) * | 2013-03-01 | 2014-09-03 | 辽宁瑞兴化工集团有限公司 | Reaction kettle for producing phosphorus pentasulfide |
| WO2016192405A1 (en) * | 2015-05-29 | 2016-12-08 | 浙江科技学院 | Hydrothermal reaction kettle |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANDONG WANSHAN CHEMICAL CO., LTD. Free format text: FORMER OWNER: SHANDONG WANSHAN GROUP CO., LTD. Effective date: 20111215 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20111215 Address after: 262400 Chengdong Industrial Zone, Changle County, Shandong, Weifang Patentee after: Shandong Wanshan Chemical Co., Ltd. Address before: 262400 Chengdong Industrial Zone, Changle County, Shandong Province Patentee before: Shandong Wanshan Chemical Co., Ltd. |
|
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20190529 Granted publication date: 20100526 |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20100526 |