CN205761162U - A kind of reacting by heating still - Google Patents
A kind of reacting by heating still Download PDFInfo
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- CN205761162U CN205761162U CN201620634574.9U CN201620634574U CN205761162U CN 205761162 U CN205761162 U CN 205761162U CN 201620634574 U CN201620634574 U CN 201620634574U CN 205761162 U CN205761162 U CN 205761162U
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Abstract
The utility model discloses a kind of reacting by heating still, it includes reductor 1, support 2, charging aperture 3, dosing mouth 4, heating vapor interface 5, heating steam (vapor) outlet 6, adds cartridge case 7, adds heat pipe 8, heating chamber 9, checks handle hole 10, adds deep fat access port 11, agitator 12, adds deep fat exit 13, drain hole 14.Reductor 1, support 2, charging aperture 3, dosing mouth 4 are set on tank top and check handle hole 10.Tank body uses elliptic design, it is to avoid occur in tank that the situation of dead angle or buildup occurs.Tank deck checks that handle hole diameter can regulate according to tank diameter, and diameter is between 500mm ~ 700mm.Use gate stirrer 12 to substitute traditional paddle and can preferably improve reaction efficiency.The medium such as conduction oil, water can be poured in heating chamber 9, heat by being provided with steam-heating pipe 8, it is ensured that reactor is heated evenly.
Description
Technical field
This utility model belongs to technical field of chemical production equipment, particularly relates to a kind of reacting by heating still, is mainly used in
The production of chemical industry chemical products.
Background technology
Reacting by heating still is widely used in chemical industry, food and pharmaceuticals industry, the stirring generally arranged in reacting by heating still
Device, agitator uses blade stirrer oar, there is stirring dynamics inadequate, stirs uneven problem.Electrical bar is used directly to insert
Entering the mode of heating in reactor, use the method, heater is arranged on inside kettle, takies kettle inner space, and
Local temperature around heating rod can be caused in reactor too high, the effect of impact reaction.Common dosing method uses and directly adds
The mode of medicine mouth conveying, institute's adding medicine is put into by dosing mouth, there is medicament mixing shortcoming not in time.
Summary of the invention
It is an object of the invention to provide one to be heated evenly, mixing effect is good, the most uniform reacting by heating of medicament mixing
Still, overcomes the deficiencies in the prior art.
For achieving the above object, the invention discloses following technology contents:
A kind of reacting by heating still, it is divided into cover and tank body, including reductor 1, support 2, charging aperture 3, dosing mouth 4, adds
Vapours interface 5, heating steam (vapor) outlet 6, add cartridge case 7, add heat pipe 8, heating chamber 9, check handle hole 10, add deep fat access port
11, gate stirrer 12, add deep fat exit 13, drain hole 14；It is characterized in that being provided with on cover reductor 1, support 2,
Charging aperture 3, dosing mouth 4, checking handle hole 10, described tank body is elliptic design, it is to avoid occur dead angle or buildup in tank
Situation occurs.Tank body outer layer is provided with heating chamber 9, arranges gate stirrer 12 in tank body, and substituting traditional paddle can be more preferably
Raising reaction efficiency.In the perforate that the interior right side of tank body is provided with dosing mouth 4 adds cartridge case 7, tank body, left lower arranges heating
Oil exit 13, tank body inner bottom part arrange drain hole 14(, and is it right？).
Conduction oil, aqueous medium can be poured in heating chamber 9 described in the utility model, be provided with simultaneously and add heat pipe 8, it is ensured that be anti-
Still is answered to be heated evenly.Its material is stainless steel tube or pitch tube.
Described in the utility model adding, is evenly distributed with multiple 5mm micropore on cartridge case.Medicine system Chinese medicine passes through dosing
Mouthful entering in chemical feed pipe, chemical feed pipe is that on stainless steel tube or pitch tube, speed according to delivery of medicaments determines percent opening and perforate
Size, medicament is evenly distributed in reactor by uniform hole.
Inspection handle hole (10) diameter on cover described in the utility model can regulate according to tank diameter, and diameter exists
Between 500mm ~ 700mm.
Gate stirrer described in the utility model (12) is 4 layers, and it can be fast with the medicament of addition by the solution in tank body
Speed stirs, and improves the reaction efficiency of reactor.Described gate stirrer (12) is 4 layers, and the blade width of stirring is
100mm, spacing 700mm of levels stirring, orlop stirrer paddle distance reacting by heating bottom height is 400mm.
Tank diameter described in the utility model is 2000-2500mm, and the diameter of gate stirrer is generally 1200-
1500mm
In the present invention, reacting by heating still uses rustless steel or glass steel material, corrosion-resistant, resistance to temperature fluctuation, simultaneously
Intensity is higher.
Compared with prior art, the present invention possesses following advantage to reacting by heating still disclosed in this utility model:
(1) gate stirrer can guarantee that the raising reaction efficiency that stirs.
(2) use steam-heating pipe to improve in heating chamber to add the temperature of heat conductor and ensure that reactor is heated evenly.
(3) particular design of chemical feed pipe can guarantee that institute's adding medicine can be evenly distributed in reactor in time, improves reaction
Efficiency.
(4) reactor all uses fiberglass or stainless steel, corrosion-resistant.
Accompanying drawing explanation
Fig. 1 is the structural representation of reacting by heating still；Wherein:
Reductor 1, support 2, charging aperture 3, dosing mouth 4, heating vapor interface 5, heating steam (vapor) outlet 6
Add cartridge case 7, add heat pipe 8, heating chamber 9, check handle hole 10, add deep fat access port 11
Gate stirrer 12, add deep fat exit 13, drain hole 14.
Detailed description of the invention
The present invention is described below by specific embodiment.Unless stated otherwise, technological means used in the present invention
It is method known in those skilled in the art.It addition, embodiment is interpreted as illustrative, and the unrestricted present invention
Scope, the spirit and scope of the invention are limited only by the claims that follow.To those skilled in the art, without departing substantially from this
On the premise of invention spirit and scope, the various changes carrying out the material component in these embodiments and consumption or change are also
Belong to protection scope of the present invention.
Embodiment 1
A kind of reacting by heating still, it is divided into cover and tank body, and tank diameter is 2000-2500mm, and tank body is that ellipse sets
Meter, it is to avoid occur in tank that the situation of dead angle or buildup occurs.Mainly include reductor 1, support 2, charging aperture 3, dosing mouth 4, add
Vapours interface 5, heating steam (vapor) outlet 6, add cartridge case 7, add heat pipe 8, heating chamber 9, check handle hole 10, add deep fat access port
11, gate stirrer 12, add deep fat exit 13, drain hole 14；It is characterized in that being provided with on cover reductor 1, support 2,
Charging aperture 3, dosing mouth 4, inspection handle hole 10, diameter can regulate according to tank diameter, and diameter is between 500mm ~ 700mm.
Tank body outer layer is provided with heating chamber 9, can pour conduction oil, aqueous medium, heat by adding heat pipe, to ensure that reactor is heated
Uniformly.Arranging gate stirrer 12 in tank body, generally 4 layers, the medicament of the solution in tank body with addition can quickly be stirred by it
Uniformly, the reaction efficiency of reactor is improved.Mainly substitute traditional paddle, can preferably improve reaction efficiency.In tank body
Right side is provided with the perforate of dosing mouth 4 and adds many 5mm micropores of cartridge case 7(and be uniformly distributed) medicament divided uniformly by uniform hole
Cloth is in a kettle..In tank body, left lower setting adds deep fat exit 13, tank body inner bottom part arranges drain hole 14.
Embodiment 2
The reacting by heating still example of the present invention is described as follows
Spent acid uses glass steel material with red soil reactor, and tank deck reductor 1 rotating speed is 60r/min, and tank deck inspection operates
The a diameter of 500mm in hole 10, tank diameter is 2000mm, a diameter of 1200mm of agitator 12, and agitator 12 divides for frame type stirring
Four layers.Chemical feed pipe is the glass reinforced plastic pipe of DN100, above opens 5mm hole.Heating is filled with conduction oil in chamber, is uniformly distributed the seamless of DN15
Steam steel pipe.Spent acid is mixed homogeneously at reacting by heating still with red soil in the medicament energy of addition, and reaction efficiency is high.
Claims (8)
1. a reacting by heating still, it is divided into cover and tank body, including reductor (1), support (2), charging aperture (3), dosing mouth
(4), heating vapor interface (5), heating steam (vapor) outlet (6), add cartridge case (7), add heat pipe (8), heating chamber (9), check handle hole
(10), add deep fat access port (11), gate stirrer (12), add deep fat exit (13), drain hole (14)；It is characterized in that tank
Covering and be provided with reductor (1), support (2), charging aperture (3), dosing mouth (4), check handle hole (10), described tank body is ellipse
Circular design, tank body outer layer is provided with heating chamber (9), arranges gate stirrer (12) in tank body, and in tank body, right side is provided with
The perforate of dosing mouth (4) add left lower in cartridge case (7), tank body arrange add deep fat exit (13), tank body inner bottom part arranges and puts
Material mouth (14).
Reacting by heating still the most according to claim 1, it is characterised in that can pour in described heating chamber (9) conduction oil,
Aqueous medium, is provided with simultaneously and adds heat pipe (8).
Reacting by heating still the most according to claim 1, it is characterised in that the described heat pipe (8) that adds is stainless steel tube or nothing
Seam steel pipe.
Reacting by heating still the most according to claim 1, it is characterised in that it is glass that described perforate adds the material of cartridge case (7)
Steel pipe or stainless steel tube, add and be evenly distributed with multiple 5mm micropore on cartridge case (7).
Reacting by heating still the most according to claim 1, it is characterised in that the inspection handle hole (10) on described cover is straight
Footpath can regulate according to tank diameter, and diameter is between 500mm ~ 700mm.
Reacting by heating still the most according to claim 1, it is characterised in that described gate stirrer (12) is 4 layers, stirring
Blade width be 100mm, spacing 700mm of levels stirring, orlop stirrer paddle distance reacting by heating bottom height
For 400mm.
Reacting by heating still the most according to claim 1, it is characterised in that described tank diameter is 2000-2500mm, frame
A diameter of 1200-1500mm of formula agitator (12).
Reacting by heating still the most according to claim 1, it is characterised in that described reacting by heating still material be rustless steel or
Glass steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620634574.9U CN205761162U (en) | 2016-06-23 | 2016-06-23 | A kind of reacting by heating still |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620634574.9U CN205761162U (en) | 2016-06-23 | 2016-06-23 | A kind of reacting by heating still |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205761162U true CN205761162U (en) | 2016-12-07 |
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ID=58130401
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620634574.9U Active CN205761162U (en) | 2016-06-23 | 2016-06-23 | A kind of reacting by heating still |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205761162U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113926827A (en) * | 2021-10-09 | 2022-01-14 | 上海市政工程设计研究总院（集团）有限公司 | Incineration fly ash recycling treatment method |
-
2016
- 2016-06-23 CN CN201620634574.9U patent/CN205761162U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113926827A (en) * | 2021-10-09 | 2022-01-14 | 上海市政工程设计研究总院（集团）有限公司 | Incineration fly ash recycling treatment method |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |