CN103638883A - Continuous reaction tank for steam and material - Google Patents
Continuous reaction tank for steam and material Download PDFInfo
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- CN103638883A CN103638883A CN201310618480.3A CN201310618480A CN103638883A CN 103638883 A CN103638883 A CN 103638883A CN 201310618480 A CN201310618480 A CN 201310618480A CN 103638883 A CN103638883 A CN 103638883A
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Abstract
The invention provides a continuous reaction tank for steam and a material. The continuous reaction tank comprises an outer tank, an inner tank, a top cover of the outer tank, a bottom cover of the inner tank, a feed port, a discharge port, an exhaust port and a deslagging port, wherein the inner tank is arranged in the outer tank, and a layer of upper annular baffle plates are arranged between the inner side walls of the outer tank and the inner tank; the inner tank is internally provided with more than one layer of round baffle plates and annular baffle plates which are arranged in a staggered manner. The continuous reaction tank provided by the invention has the characteristics that the material reaction is full, an energy source is saved and the like, and the continuous reaction tank can be widely applied to systems heating the material by utilizing the steam.
Description
Technical field
The present invention relates to heating technique, particularly relate to the successive reaction tank of a kind of steam and material.
Background technology
The features such as the enthalpy that possesses based on steam is higher, adaptability is extensive, in industry some process need adopt steam to heating material to uniform temperature, to impel material reaction.The material of, poor fluidity large compared with high, viscosity for solid content, utilizes the full and uniform heating of the more difficult realization of steam to material; But for the high pressure steam heating system of successive reaction, realize steam and fully react with the continuous of material, significant to industrial production.Industrial system mode of heating mainly contains two kinds of modes at present.First kind of way is for adopting the mode of stirring or whirligig, and this device is subject to extraneous forced disturbance heat exchange, therefore heat transfer effect is better; But for high-pressure reaction pot, because himself pressure is very high, and also very high to carrying out the requirement of energy-dissipating device of forced flow, therefore power consumption is large, and also also very high to the designing requirement of tumbler.The second way is for adopting the mode of the conventional heat-exchanger rig of no-rotary part, and this device utilizes traditional heat exchange mode, therefore itself is without extra power consumption; But its heat transfer effect is poor, heat exchange is inhomogeneous, and cannot realize the laser heating reaction to material.
As can be seen here, in prior art, for needing the viscous material that reaction pressure is higher, there is no at present reaction relatively fully and the heating material successive reaction tank of the saving energy.
Summary of the invention
In view of this, main purpose of the present invention be to provide a kind of material reaction relatively fully, efficient energy-saving, steam and the successive reaction tank of material.
In order to achieve the above object, a kind of technical scheme that the present invention proposes is:
A successive reaction tank for steam and material, comprising: outer tank, inner canister, outer top ends of cans, inner canister bottom; Inner canister is along outer tank central shaft to being installed in outer tank inside, and by fixed head, is fixedly connected with between inner canister and outer tank, and fixed head is positioned at outside outer tank madial wall, inner canister lateral wall; Outer tank is fixedly connected with by the first flange with outer top ends of cans; Inner canister is fixedly connected with by the second flange with inner canister bottom; Wherein, between outer tank madial wall and inner canister lateral wall, be provided with outer ring deflection plate more than one deck; In inner canister, be provided with circular deflection plate more than one deck, interior ring baffle plate more than one deck, and arrangement is for alternately arranging; The outside side in outer tank bottom is provided with a charging aperture, pot bottom in charging aperture is communicated with by feed pipe; The outside opposite side in outer tank bottom is provided with a slag-drip opening, pot bottom in slag-drip opening is communicated with by scum pipe; Outer pot bottom is provided with a discharging opening.
In sum, in the successive reaction tank of steam of the present invention and material, after steam and mixing of materials, by charging aperture, enter interior pot bottom in the lump, and externally, under the promotion of feed pump, after the interior ring baffle plate arranging through inner canister successively from top to bottom from interior pot bottom and circular deflection plate, arrive interior tank top; Afterwards, material and vapour mixture overflow from inner canister top perimeter, and enter the space between inner canister and outer tank; In space between inner canister and outer tank, material and vapour mixture, from top to bottom through outer ring deflection plate, arrive outer pot bottom.In this process, material is the even also sufficient reacting of heat exchange, and material, after said process sufficient reacting, is discharged this tank body by discharge gate.The successive reaction tank of steam of the present invention and material adopts inner canister to be socketed in the structure of outer tank inside, and in inner canister, adopt the circular deflection plate with holes of multilayer and multi-layer annular deflection plate with holes, between inner canister lateral wall and outer tank madial wall, be also provided with multi-layer annular deflection plate with holes, so just can guarantee the time that material fully contacts with steam, complete sufficient heat exchange; Therefore, the successive reaction tank of steam of the present invention and material can be controlled steam pressure, heating-up temperature and reaction time preferably, thereby makes material reaction more abundant, saves the energy.
Accompanying drawing explanation
Fig. 1 is the successive reaction tank forward cutaway view of steam of the present invention and material.
Fig. 2 is the successive reaction top view of steam of the present invention and material.
The specific embodiment
For making the object, technical solutions and advantages of the present invention clearer, the present invention is described in further detail below in conjunction with the accompanying drawings and the specific embodiments.
Fig. 1 is the successive reaction tank forward cutaway view of steam of the present invention and material.As shown in Figure 1, the successive reaction tank of steam of the present invention and material, comprising: outer tank 1, inner canister 2, outer top ends of cans 3, inner canister bottom 27; Inner canister 2 is along outer tank 1 central shaft to being installed in outer tank 1 inside, and by fixed head, is fixedly connected with between inner canister 2 and outer tank 1, and fixed head is positioned at outside outer tank 1 madial wall, inner canister 2 lateral walls; Outer tank 1 is fixedly connected with by the first flange 14 with outer top ends of cans 3; Inner canister 2 is fixedly connected with by the second flange 28 with inner canister bottom 27; Wherein, between outer tank 1 madial wall and inner canister 2 lateral walls, be provided with outer ring deflection plate 11 more than one deck; In inner canister 2, be provided with circular deflection plate 21 more than one deck, interior ring baffle plate 22 more than one deck, and arrangement is for alternately arranging; The outside side in outer tank 1 bottom is provided with a charging aperture 4, and charging aperture 4 is communicated with inner canister 2 bottoms by feed pipe; The outside opposite side in outer tank 1 bottom is provided with a slag-drip opening 6, and slag-drip opening 6 is communicated with inner canister 2 bottoms by scum pipe; Outer tank 1 bottom is provided with a discharging opening 5.
Here, outer ring deflection plate 11, interior ring baffle plate 22, circular deflection plate 21 are all fixed in outer tank 1 or inner canister 2 by angle bar etc., and this partial content is prior art, repeats no more.
In a word, in the successive reaction tank of steam of the present invention and material, after steam and mixing of materials, by charging aperture, enter interior pot bottom in the lump, and externally under the promotion of feed pump, from interior pot bottom, pass through successively from top to bottom interior annular deflection plate with holes, circular deflection plate with holes, tank top in arriving; Afterwards, material and vapour mixture overflow from inner canister top perimeter, and enter the space between inner canister and outer tank; In space between inner canister and outer tank, material and vapour mixture successively by outer ring deflection plate, arrive outer pot bottom from top to bottom.The mixture of material and steam is after said process, and the material that material obtains after fully reacting with steam is discharged from discharge gate.The successive reaction tank of steam of the present invention and material adopts inner canister to be socketed in the structure of outer tank inside, and in inner canister, adopt the circular deflection plate with holes of multilayer and multi-layer annular deflection plate with holes, between inner canister lateral wall and outer tank madial wall, be also provided with multi-layer annular deflection plate with holes, so just can guarantee the time that material fully contacts with steam, complete sufficient heat exchange; Therefore, the successive reaction tank of steam of the present invention and material can be controlled steam pressure, heating-up temperature and reaction time preferably, thereby makes material reaction more abundant, saves the energy.
In practical application, owing to entering in the material of successive reaction tank of steam of the present invention and material, contain block slag charge, and the effect of outside feed pump cannot make these block slag charges carry out material reaction process, block slag charge can be deposited in interior pot bottom, and discharges by slag-drip opening.
In the present invention, on outer top ends of cans 3, be also provided with exhaust outlet 31.Practical application, exhaust outlet 31 is communicated with the preheating unit steam inlet of material continuous reaction system.Exhaust outlet 31 is delivered to the preheating can of described this retort tank outside for the residue steam that the successive reaction tank of steam of the present invention and material is produced, for the abundant circulation graded utilization of steam, save the energy.
In the present invention, on outer top ends of cans 3, be also provided with an above relief valve port 33, flushing water entrance 34, above thermometer mouth 35, an above gauge port 36.
In the present invention, in outer tank 1, be also provided with minimum level-sensing device mouth 16, high charge level meter mouth 15; In practical application, minimum level-sensing device mouth 16 can specifically be set according to practical application with high charge level meter mouth 15, but the setting of minimum level-sensing device mouth 16 must meet: externally, under the effect of pump, the material of sufficient reacting could be discharged after keeping a period of time in the successive reaction tank of steam of the present invention and material.Here, described a period of time can specifically be set according to actual needs.
Fig. 2 is the successive reaction tank top view of steam of the present invention and material.As shown in Figure 2, in outer tank 1, be also provided with a manhole 7, facilitate personnel to come in and go out when overhauling.
In sum, these are only preferred embodiment of the present invention, be not intended to limit protection scope of the present invention.Within the spirit and principles in the present invention all, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection scope of the present invention.
Claims (5)
1. a successive reaction tank for steam and material, is characterized in that, described successive reaction tank comprises: outer tank, inner canister, outer top ends of cans, inner canister bottom; Inner canister is along outer tank central shaft to being installed in outer tank inside, and by fixed head, is fixedly connected with between inner canister and outer tank, and fixed head is positioned at outside outer tank madial wall, inner canister lateral wall; Outer tank is fixedly connected with by the first flange with outer top ends of cans; Inner canister is fixedly connected with by the second flange with inner canister bottom; Wherein, between outer tank madial wall and inner canister lateral wall, be provided with outer ring deflection plate more than one deck; In inner canister, be provided with circular deflection plate more than one deck, interior ring baffle plate more than one deck, and arrangement is for alternately arranging; The outside side in outer tank bottom is provided with a charging aperture, pot bottom in charging aperture is communicated with by feed pipe; The outside opposite side in outer tank bottom is provided with a slag-drip opening, pot bottom in slag-drip opening is communicated with by scum pipe; Outer pot bottom is provided with a discharging opening.
2. the successive reaction tank of steam according to claim 1 and material, is characterized in that, described outer ring deflection plate, circular deflection plate, interior ring baffle plate are deflection plate with holes.
3. the successive reaction tank of steam according to claim 1 and material, is characterized in that, is also provided with exhaust outlet, more than one safety valve, more than one temperature survey mouth and interface of pressure measurement, rinse water interface on described outer top ends of cans.
4. the successive reaction tank of steam according to claim 1 and material, is characterized in that, is also provided with a minimum level-sensing device mouth, high charge level meter mouth in described outer tank.
5. the successive reaction tank of steam according to claim 4 and material, is characterized in that, is also provided with a manhole in described outer tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310618480.3A CN103638883A (en) | 2013-11-27 | 2013-11-27 | Continuous reaction tank for steam and material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310618480.3A CN103638883A (en) | 2013-11-27 | 2013-11-27 | Continuous reaction tank for steam and material |
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| Publication Number | Publication Date |
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| CN103638883A true CN103638883A (en) | 2014-03-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201310618480.3A Pending CN103638883A (en) | 2013-11-27 | 2013-11-27 | Continuous reaction tank for steam and material |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106277690A (en) * | 2015-05-11 | 2017-01-04 | 河南昂西特热能技术有限公司 | A kind of sequential continuous thermal hydrolysis reaction unit |
| CN108955296A (en) * | 2018-07-27 | 2018-12-07 | 重庆澳来思节能科技有限公司 | Steam heating power energy conserving system |
| CN112427002A (en) * | 2020-11-21 | 2021-03-02 | 贵州锦江生物能源科技有限公司 | Tower-type superfine contact reaction device for biodiesel |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202379752U (en) * | 2011-12-20 | 2012-08-15 | 广西华纳新材料科技有限公司 | Gas lifting type reactor for carbonation of precipitated calcium carbonate |
-
2013
- 2013-11-27 CN CN201310618480.3A patent/CN103638883A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202379752U (en) * | 2011-12-20 | 2012-08-15 | 广西华纳新材料科技有限公司 | Gas lifting type reactor for carbonation of precipitated calcium carbonate |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106277690A (en) * | 2015-05-11 | 2017-01-04 | 河南昂西特热能技术有限公司 | A kind of sequential continuous thermal hydrolysis reaction unit |
| CN108955296A (en) * | 2018-07-27 | 2018-12-07 | 重庆澳来思节能科技有限公司 | Steam heating power energy conserving system |
| CN108955296B (en) * | 2018-07-27 | 2020-04-21 | 重庆澳来思节能科技有限公司 | Steam heating power energy-saving system |
| CN112427002A (en) * | 2020-11-21 | 2021-03-02 | 贵州锦江生物能源科技有限公司 | Tower-type superfine contact reaction device for biodiesel |
| CN112427002B (en) * | 2020-11-21 | 2024-06-07 | 贵州锦江生物能源科技有限公司 | Tower-type superfine contact reaction device for biodiesel |
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Application publication date: 20140319 |