CN102600785A - High-efficiency energy-saving reaction kettle - Google Patents
High-efficiency energy-saving reaction kettle Download PDFInfo
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- CN102600785A CN102600785A CN2012100953446A CN201210095344A CN102600785A CN 102600785 A CN102600785 A CN 102600785A CN 2012100953446 A CN2012100953446 A CN 2012100953446A CN 201210095344 A CN201210095344 A CN 201210095344A CN 102600785 A CN102600785 A CN 102600785A
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- reaction kettle
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- boiler
- agitated reactor
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Abstract
The invention relates to a high-efficiency energy-saving reaction kettle, which comprises a reaction kettle core body and a rack. A manhole, an air extraction hole, a powder material feed inlet, a liquid feed inlet and a thermometer are arranged at the top of the reaction kettle core body. A flame guide pipe and an agitator are arranged in the reaction kettle core body. A discharge outlet is arranged at the lower part of the reaction kettle core body. One side of the reaction kettle core body is connected with a combustion chamber and the other side of the reaction kettle core body is connected with a draft fan. The high-efficiency energy-saving reaction kettle has the beneficial effects that: 1) the device is suitable for treating alkaline, neutral and weakly acidic liquid materials; 2) the equipment structure is simple, the reaction kettle is convenient to install and the functions of the existing boiler and the reaction kettle are integrated; and 3) the traditional mode of indirect heat transfer through the boiler is changed, the direct heat supply method through fuel combustion is adopted, the energy consumption of the reaction kettle is equivalent to the coal consumption of a 1 ton/hour boiler, however the reaction kettle realizes the effect which cannot be reached by 4 tons/hour traditional industrial boiler and the energy saving effect is remarkable.
Description
[technical field] the present invention relates to metallurgy and chemical mechanical equipment, specifically a kind of energy-efficient agitated reactor.
Molten the soaking with evaporation of [background technology] material belongs to hydrometallurgy and the extremely important production technology of chemical enterprise; Accomplish these technical process and need material be heated to assigned temperature; The method that present stage heats all is to launch boiler, uses a kind of intermediary material, i.e. transmission of water vapor heat energy.Water vapour contacts heated body a course of conveying is arranged from producing to, has the problem of thermal efficiency discount, and the approach that therefore conducts heat is indirect.In order to improve the service efficiency of steam; Various technical measures to steam intensification, supercharging have appearred in the boiler for producing field in recent years, multiple efficient boiler equipment occurred, but as long as still adopt steam to conduct heat; Then the burning heat production from fuel obtains heat to reaction mass; The highest thermal efficiency is no more than 1/3, is usually less than 1/5, even has only 1/10.How changing traditional heat-supplying mode, make full use of the thermal efficiency, reach remarkable purpose of energy saving, is the current eager problem that needs solution.
[summary of the invention] the present invention is directed to the drawback that above-mentioned traditional heat supply method exists, and a kind of energy-efficient agitated reactor is provided.
This energy-efficient agitated reactor comprises agitated reactor stamen body and frame, it is characterized in that, agitated reactor stamen body top is provided with manhole, aspirating hole, powder charging aperture, liquid feed mouth and thermometer; The set inside of agitated reactor stamen body is led flame tube and agitator; The bottom of agitated reactor stamen body is provided with discharge port; One side of agitated reactor stamen body is connected with the combustion chamber, and the opposite side of agitated reactor stamen body is connected with air-introduced machine.
The invention has the beneficial effects as follows: 1, this device is fit to handle alkalescence, neutrality and faintly acid liquid material; 2, device structure is simple, and is easy for installation, and the function of existing boiler and agitated reactor is united two into one; 3, changed traditional mode by the boiler indirect heat transfer; Adopt fuel combustion direct heating mode; The present invention has accomplished 4 tons of/hour out of the question things of rank traditional industry boiler with the coal consumption that is equivalent to 1 ton of/hour other boiler of level, the visible significantly energy-conservation effect that reaches.
[description of drawings]
Fig. 1 is a structural representation of the present invention
Among the figure: 1, liquid feed mouth, 2, agitated reactor stamen body, 3, air-introduced machine, 4, the combustion chamber, 5, lead flame tube, 6, thermometer, 7, the powder charging aperture, 8, agitator, 9, discharge port, 10, aspirating hole, 11, manhole.
[specific embodiment] set forth as follows enforcement of the present invention below in conjunction with accompanying drawing:
In Fig. 1, agitated reactor stamen body 2 tops are provided with manhole 11, aspirating hole 10, powder charging aperture 7, liquid feed mouth 1 and thermometer 6; The set inside of agitated reactor stamen body 2 is led flame tube 5 and agitator 8; The bottom of agitated reactor stamen body 2 is provided with discharge port 9; One side of agitated reactor stamen body 2 is connected with combustion chamber 4, and the opposite side of agitated reactor stamen body 2 is connected with air-introduced machine 3.
During work, at first from liquid feed mouth 1, with calculating good liquid material, for example: the water or the aqueous solution; Consumption is put in the agitated reactor stamen body 2 according to plan, starts air-introduced machine 3 immediately, the intensification air feed of observing response still with receive thermal exhaust normal after; Start combustion chamber 4 again, the flame that burning is produced, the outer wall of fraction reacting by heating still stamen body 2 is most ofly directly led flame tube 5 through being horizontally placed in the agitated reactor stamen body 2; Make the liquid material in the stamen body 2, obtained direct heating, treat that thermometer 6 indications reach desired temperature, can be from powder charging aperture 7; In agitated reactor stamen body 2, drop into solid-state granular material, agitator 8 makes liquid-solid material even contact in agitated reactor simultaneously, dissolves and soaks reaction; Under the assigned temperature condition, remain to the scheduled time, carry out discharging from discharge port 9 at last, dissolve and soak the operation completion.
The evaporation operation with dissolve that to soak operation roughly close, difference has 2 points: the one, liquid feed mouth 1 is in normally open, liquid in the stamen body 2 can be evaporated immediately immediately replenish.The 2nd, consistent with the action and the air-introduced machine 3 of the air exhauster of aspirating hole 10 UNICOMs, with opening with closing, to keep the completeness and the security of evaporation operation.
The heat up effect comparison of indirect method of efficient and conventional boiler steam of the present invention is as shown in the table:
Contrast listed numerical value, except that one of thermal capacitance, the present invention all is superior to the close rank boiler heat supplying of scale.
Claims (1)
1. an energy-efficient agitated reactor comprises agitated reactor stamen body and frame, it is characterized in that, agitated reactor stamen body top is provided with manhole, aspirating hole, powder charging aperture, liquid feed mouth and thermometer; The set inside of agitated reactor stamen body is led flame tube and agitator; The bottom of agitated reactor stamen body is provided with discharge port; One side of agitated reactor stamen body is connected with the combustion chamber, and the opposite side of agitated reactor stamen body is connected with air-introduced machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100953446A CN102600785A (en) | 2012-04-01 | 2012-04-01 | High-efficiency energy-saving reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100953446A CN102600785A (en) | 2012-04-01 | 2012-04-01 | High-efficiency energy-saving reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102600785A true CN102600785A (en) | 2012-07-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012100953446A Pending CN102600785A (en) | 2012-04-01 | 2012-04-01 | High-efficiency energy-saving reaction kettle |
Country Status (1)
| Country | Link |
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| CN (1) | CN102600785A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2524827Y (en) * | 2002-01-14 | 2002-12-11 | 董敏 | Industrial reaction still |
| CN202555272U (en) * | 2012-04-01 | 2012-11-28 | 湖南省中杰科技发展股份有限公司 | Efficient energy-saving reaction kettle |
-
2012
- 2012-04-01 CN CN2012100953446A patent/CN102600785A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2524827Y (en) * | 2002-01-14 | 2002-12-11 | 董敏 | Industrial reaction still |
| CN202555272U (en) * | 2012-04-01 | 2012-11-28 | 湖南省中杰科技发展股份有限公司 | Efficient energy-saving reaction kettle |
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| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20120725 |