CN105771861A - Internal heat exchange reactor - Google Patents
Internal heat exchange reactor Download PDFInfo
- Publication number
- CN105771861A CN105771861A CN201610274851.4A CN201610274851A CN105771861A CN 105771861 A CN105771861 A CN 105771861A CN 201610274851 A CN201610274851 A CN 201610274851A CN 105771861 A CN105771861 A CN 105771861A
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- Prior art keywords
- reactor
- shaft
- agitator
- heat exchange
- reactor body
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/074—Stirrers characterised by their mounting on the shaft having two or more mixing elements being concentrically mounted on the same shaft
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1125—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
- B01F27/11253—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis the blades extending oblique to the stirrer axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
- B01F27/191—Stirrers with two or more mixing elements mounted in sequence on the same axis with similar elements
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/95—Heating or cooling systems using heated or cooled stirrers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses an internal heat exchange reactor, comprising a reactor body, a reactor jacket, a stirring device and a reactor support. An external heat exchange chamber is formed between the reactor jacket and the reactor body; the stirring device is disposed on a center line of the reactor body; the stirring device comprises a servo motor, a stirring shaft and stirring blades; the stirring shaft is provided with a stirring shaft through along its center; the part of the bottom of the reactor body in contact with the stirring shaft is provided with a stirring device water inlet; the part of the upper portion of the reactor body in contact with the stirring shaft is provided with a stirring device water outlet; both the stirring device water inlet and the stirring device water outlet are communicated with the stirring shaft through hole; the stirring blades are of sector blade structure; the stirring blades are connected with the stirring shaft by welding; the center line part of each stirring blade is provided with a stirring blade cavity; the stirring blade cavities are communicated with the stirring shaft through hole. The use of the sector stirring blades enlarges heat transfer contact area, and the stirring shaft is hollowed and filled with a heat transfer medium so that the interior temperature of the reactor can be adjusted precisely.
Description
Technical field
The present invention relates to pressure vessel field, especially relate to a kind of built-in heat exchange reactor.
Background technology
At present, the synthetic method of polymer is generally adopted to put into several polymer reaction monomers used simultaneously and carries out polyreaction in reactor.Polymer reaction monomer is meeting neither endothermic nor exothermic in polymerization process, and selectivity and the yield of reacting substance are had great role by the control of temperature.Polymer reaction monomer, in course of reaction, needs intensification induced reaction during beginning, highly exothermic again after entering course of reaction, it is necessary to quickly remove heat.To control reaction temperature well, it is ensured that response speed, stabilized product quality.Owing to general polymerization thing reaction monomers polymerization process is all continuous feed, and with the course of reaction of very exothermic, conventional temperature control method is generally adopted the method passing into steam or coolant in reacting kettle jacketing and carries out heating, cooling control, this method temperature control precision is poor, energy consumption is high, additionally the cold and hot exchange of reacting kettle jacketing is too fast, and variations in temperature is too big, and the life-span of reactor is had impact.
Polymer reaction monomer polymerization reactions is to be continuously added to monomer, and adds related auxiliaries in course of reaction, and its response speed is very sensitive to reaction temperature, temperature is more high, reacting more fast, heat release is more violent, and temperature is height more, reaction is speed more, heat release is more few, therefore controls reaction temperature well, is control response speed, improving the selectivity of reacting substance and a key of yield: meanwhile, the Homogeneous phase mixing fully between several polymer monomers is also the key technical problem improving reaction efficiency.
For this, the designer of the present invention is because above-mentioned technological deficiency, and by concentrating on studies and designing, comprehensive experience and the achievement being engaged in related industry for a long time for many years, research design goes out a kind of built-in heat exchange reactor, to overcome above-mentioned technological deficiency.
Summary of the invention
Problem to be solved by this invention is, for above-mentioned shortcoming of the prior art, it is proposed to innovation scheme, and the built-in heat exchange reactor of especially a kind of reaction temperature that can effectively regulate reactor.
For solving the problems referred to above, the scheme that the present invention adopts is as follows: a kind of built-in heat exchange reactor, including reactor body, reacting kettle jacketing, agitator and reactor support, it is characterised in that described reactor body is arranged on reactor support；The upper end of described reactor body is provided with at least one reactor charging aperture；The lower end of described reactor body is provided with a reactor discharging opening；Described reacting kettle jacketing is arranged on reactor outer body；External hot exchange cavity is formed between described reacting kettle jacketing and reactor body；The lower end of described reacting kettle jacketing is provided with reacting kettle jacketing water inlet；The upper end of described reacting kettle jacketing is provided with reacting kettle jacketing outlet；Described agitator is arranged on the centrage of reactor body；Described agitator includes servomotor, shaft and stirring paddle；Described servomotor is arranged on the top of reactor body；Described shaft is connected with servomotor；Described stirring paddle is arranged on shaft；Described shaft is provided with shaft through hole along its centrage；The position that described reactor body bottom portion contacts with shaft is provided with agitator water inlet；The position that described reactor body upper part contacts with shaft is provided with agitator outlet；Described agitator water inlet all connects with described shaft through hole with agitator outlet；Described stirring paddle is sector structure；Described stirring paddle and shaft are welded to connect.
Further, built-in heat exchange reactor according to above-mentioned design, described agitator water inlet is provided with heat exchange medium delivery pump and heat exchange medium storage warehouse.
Further, built-in heat exchange reactor according to above-mentioned design, described agitator outlet includes agitator and goes out water hull；Described agitator goes out water hull and is arranged on the top of reactor body, is positioned at the lower section of servomotor；Described agitator water outlet valve jacket is located on shaft；Described agitator goes out water hull and has water outlet cavity；Described shaft is communicated with mouth；Described connected entrance connects with shaft through hole；Connected entrance on described shaft is positioned at water chamber body；Described agitator goes out water hull and is provided with agitator outlet；Described agitator outlet connects with water outlet cavity.
Further, built-in heat exchange reactor according to above-mentioned design, described agitator goes out water hull and is provided with lubricating gasket with shaft contact site；The outside of described lubricating gasket is provided with airtight and watertight padding circle；The outside of described airtight and watertight padding circle is provided with sealing lid.
Further, built-in heat exchange reactor according to above-mentioned design, described sealing lid goes out water hull screw threads for fastening and is connected with agitator.
Further, built-in heat exchange reactor according to above-mentioned design, described reactor bodies top is provided with three reactor charging apertures.
Further, built-in heat exchange reactor according to above-mentioned design, described stirring paddle is that be arranged on reactor this is internal for inverted triangle.
Further, according to above-mentioned design, built-in heat exchange reactor, is provided with reactor sleeve between described agitator and reactor body；Described reactor sleeve includes reactor sleeve lining and reactor sleeve outer wall；Built-in heat exchange cavity is formed between described reactor sleeve lining and reactor sleeve outer wall；Described reactor body bottom portion is provided with reactor sleeve water inlet；Described reactor bodies top is provided with reactor sleeve outlet.
The technique effect of the present invention is as follows: the built-in heat exchange reactor of the present invention, adopts the method that agitator is combined with heat transfer equipment, and stirring paddle is arranged to sector structure, increases heat transfer contact area；Stirring paddle can stir raw material mixing, again can as heat conducting device, and owing to stirring paddle is flat structure, its contact area with raw material is big, absorbs or to distribute heat all very fast, it is possible to fast and effectively the temperature in reactor is adjusted.Simultaneously, midline position at stirring paddle arranges stirring paddle cavity, and is connected with shaft through hole by stirring paddle cavity so that heat transfer medium can enter the shaft through hole of agitator from agitator water inlet, hence into, in stirring paddle cavity, accelerating the temperature in reactor is adjusted.
The stirring paddle of the present invention and the connection angle of shaft are chosen as 90 degree and are vertically arranged, and stirring paddle tilts certain angle so that the raw material in reactor can be mixed by stirring paddle fully, accelerates reaction, improves reaction efficiency.In order to allow the raw material in reactor mix more fully, through test of many times, it has been found that if the circulation stirring in the shape of a spiral of the raw material in reactor, it is possible to would accelerate mixing, therefore the stirring paddle of agitator is arranged to the arrangement of V shape, it is possible to realize the raw material helical form circulation stirring in reactor.
Accompanying drawing explanation
Fig. 1 is built-in heat exchange reactor structural representation.
Fig. 2 is that stirring paddle is inverted triangular structure schematic diagram.
Fig. 3 is agitator water outlet shell structure schematic diagram.
Fig. 4 is stirring paddle structural representation.
Wherein, 1 is reactor body；2 is reacting kettle jacketing；3 is agitator；4 is reactor support；11 is reactor charging aperture；12 is reactor discharging opening；21 exchange cavity for external hot；22 is reacting kettle jacketing water inlet；23 is reacting kettle jacketing outlet；31 is servomotor；32 is shaft；33 is stirring paddle；34 go out water hull for agitator；35 is agitator outlet；36 is agitator water inlet；37 is shaft through hole；38 is connected entrance；39 is water outlet cavity；310 is airtight and watertight padding circle；311 is lubricating gasket；312 for sealing lid；313 is stirring paddle cavity.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further details.
Embodiment 1: a kind of built-in heat exchange reactor, including reactor body 1, reacting kettle jacketing 2, agitator 3 and reactor support 4, described reactor body 1 is arranged on reactor support 4；The upper end of described reactor body 1 is provided with at least one reactor charging aperture 11；The lower end of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on outside reactor body 1；External hot exchange cavity 21 is formed between described reacting kettle jacketing 2 and reactor body 1；The lower end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 water inlet；The upper end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 outlet；Described agitator 3 is arranged on the centrage of reactor body 1；Described agitator 3 includes servomotor 31, shaft 32 and stirring paddle 33；Described servomotor 31 is arranged on the top of reactor body 1；Described shaft 32 is connected with servomotor 31；Described stirring paddle 33 is arranged on shaft 32；Described shaft 32 is provided with shaft 32 through hole along its centrage；The position contacted with shaft 32 bottom described reactor body 1 is provided with agitator 3 water inlet；The position that described reactor body 1 top contacts with shaft 32 is provided with agitator 3 outlet；Described agitator 3 water inlet all connects with described shaft 32 through hole with agitator 3 outlet；Described stirring paddle 33 is sector structure；Described stirring paddle 33 is welded to connect with shaft 32；The position of center line of described stirring paddle is provided with stirring paddle cavity 313；Described stirring paddle cavity 313 connects with shaft through hole.
Embodiment 2: a kind of built-in heat exchange reactor, including reactor body 1, reacting kettle jacketing 2, agitator 3 and reactor support 4, described reactor body 1 is arranged on reactor support 4；The upper end of described reactor body 1 is provided with at least one reactor charging aperture 11；The lower end of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on outside reactor body 1；External hot exchange cavity 21 is formed between described reacting kettle jacketing 2 and reactor body 1；The lower end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 water inlet；The upper end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 outlet；Described agitator 3 is arranged on the centrage of reactor body 1；Described agitator 3 includes servomotor 31, shaft 32 and stirring paddle 33；Described servomotor 31 is arranged on the top of reactor body 1；Described shaft 32 is connected with servomotor 31；Described stirring paddle 33 is arranged on shaft 32；Described shaft 32 is provided with shaft 32 through hole along its centrage；The position contacted with shaft 32 bottom described reactor body 1 is provided with agitator 3 water inlet；The position that described reactor body 1 top contacts with shaft 32 is provided with agitator 3 outlet；Described agitator 3 water inlet all connects with described shaft 32 through hole with agitator 3 outlet；Described stirring paddle 33 is sector structure；Described stirring paddle 33 is welded to connect with shaft 32, and described agitator 3 water inlet is provided with heat exchange medium delivery pump and heat exchange medium storage warehouse；The position of center line of described stirring paddle is provided with stirring paddle cavity 313；Described stirring paddle cavity 313 connects with shaft through hole.
Embodiment 3: a kind of built-in heat exchange reactor, including reactor body 1, reacting kettle jacketing 2, agitator 3 and reactor support 4, described reactor body 1 is arranged on reactor support 4；The upper end of described reactor body 1 is provided with at least one reactor charging aperture 11；The lower end of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on outside reactor body 1；External hot exchange cavity 21 is formed between described reacting kettle jacketing 2 and reactor body 1；The lower end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 water inlet；The upper end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 outlet；Described agitator 3 is arranged on the centrage of reactor body 1；Described agitator 3 includes servomotor 31, shaft 32 and stirring paddle 33；Described servomotor 31 is arranged on the top of reactor body 1；Described shaft 32 is connected with servomotor 31；Described stirring paddle 33 is arranged on shaft 32；Described shaft 32 is provided with shaft 32 through hole along its centrage；The position contacted with shaft 32 bottom described reactor body 1 is provided with agitator 3 water inlet；The position that described reactor body 1 top contacts with shaft 32 is provided with agitator 3 outlet；Described agitator 3 water inlet all connects with described shaft 32 through hole with agitator 3 outlet；Described stirring paddle 33 is sector structure；Described stirring paddle 33 is welded to connect with shaft 32, and described agitator 3 outlet includes agitator 3 and goes out water hull；Described agitator 3 goes out water hull and is arranged on the top of reactor body 1, is positioned at the lower section of servomotor 31；Described agitator 3 water outlet valve jacket is located on shaft 32；Described agitator 3 goes out water hull and has water outlet cavity 39；Described shaft 32 is communicated with mouth 38；Described connected entrance 38 connects with shaft 32 through hole；Connected entrance 38 on described shaft 32 is positioned at water outlet cavity 39；Described agitator 3 goes out water hull and is provided with agitator 3 outlet；Described agitator 3 outlet connects with water outlet cavity 39；The position of center line of described stirring paddle is provided with stirring paddle cavity 313；Described stirring paddle cavity 313 connects with shaft through hole.
Embodiment 4: a kind of built-in heat exchange reactor, including reactor body 1, reacting kettle jacketing 2, agitator 3 and reactor support 4, described reactor body 1 is arranged on reactor support 4；The upper end of described reactor body 1 is provided with at least one reactor charging aperture 11；The lower end of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on outside reactor body 1；External hot exchange cavity 21 is formed between described reacting kettle jacketing 2 and reactor body 1；The lower end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 water inlet；The upper end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 outlet；Described agitator 3 is arranged on the centrage of reactor body 1；Described agitator 3 includes servomotor 31, shaft 32 and stirring paddle 33；Described servomotor 31 is arranged on the top of reactor body 1；Described shaft 32 is connected with servomotor 31；Described stirring paddle 33 is arranged on shaft 32；Described shaft 32 is provided with shaft 32 through hole along its centrage；The position contacted with shaft 32 bottom described reactor body 1 is provided with agitator 3 water inlet；The position that described reactor body 1 top contacts with shaft 32 is provided with agitator 3 outlet；Described agitator 3 water inlet all connects with described shaft 32 through hole with agitator 3 outlet；Described stirring paddle 33 is sector structure；Described stirring paddle 33 is welded to connect with shaft 32, and described agitator 3 outlet includes agitator 3 and goes out water hull；Described agitator 3 goes out water hull and is arranged on the top of reactor body 1, is positioned at the lower section of servomotor 31；Described agitator 3 water outlet valve jacket is located on shaft 32；Described agitator 3 goes out water hull and has water outlet cavity 39；Described shaft 32 is communicated with mouth 38；Described connected entrance 38 connects with shaft 32 through hole；Connected entrance 38 on described shaft 32 is positioned at water outlet cavity 39；Described agitator 3 goes out water hull and is provided with agitator 3 outlet；Described agitator 3 outlet connects with water outlet cavity 39, and described agitator 3 goes out water hull and is provided with lubricating gasket 311 with shaft 32 contact site；The outside of described lubricating gasket 311 is provided with airtight and watertight padding circle 310；The outside of described airtight and watertight padding circle 310 is provided with sealing lid 312；The position of center line of described stirring paddle is provided with stirring paddle cavity 313；Described stirring paddle cavity 313 connects with shaft through hole.
Embodiment 5: a kind of built-in heat exchange reactor, including reactor body 1, reacting kettle jacketing 2, agitator 3 and reactor support 4, described reactor body 1 is arranged on reactor support 4；The upper end of described reactor body 1 is provided with at least one reactor charging aperture 11；The lower end of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on outside reactor body 1；External hot exchange cavity 21 is formed between described reacting kettle jacketing 2 and reactor body 1；The lower end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 water inlet；The upper end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 outlet；Described agitator 3 is arranged on the centrage of reactor body 1；Described agitator 3 includes servomotor 31, shaft 32 and stirring paddle 33；Described servomotor 31 is arranged on the top of reactor body 1；Described shaft 32 is connected with servomotor 31；Described stirring paddle 33 is arranged on shaft 32；Described shaft 32 is provided with shaft 32 through hole along its centrage；The position contacted with shaft 32 bottom described reactor body 1 is provided with agitator 3 water inlet；The position that described reactor body 1 top contacts with shaft 32 is provided with agitator 3 outlet；Described agitator 3 water inlet all connects with described shaft 32 through hole with agitator 3 outlet；Described stirring paddle 33 is sector structure；Described stirring paddle 33 is welded to connect with shaft 32, and described reactor body 1 top is provided with three reactor charging apertures 11；The position of center line of described stirring paddle is provided with stirring paddle cavity 313；Described stirring paddle cavity 313 connects with shaft through hole.
Embodiment 6: a kind of built-in heat exchange reactor, including reactor body 1, reacting kettle jacketing 2, agitator 3 and reactor support 4, described reactor body 1 is arranged on reactor support 4；The upper end of described reactor body 1 is provided with at least one reactor charging aperture 11；The lower end of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on outside reactor body 1；External hot exchange cavity 21 is formed between described reacting kettle jacketing 2 and reactor body 1；The lower end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 water inlet；The upper end of described reacting kettle jacketing 2 is provided with reacting kettle jacketing 2 outlet；Described agitator 3 is arranged on the centrage of reactor body 1；Described agitator 3 includes servomotor 31, shaft 32 and stirring paddle 33；Described servomotor 31 is arranged on the top of reactor body 1；Described shaft 32 is connected with servomotor 31；Described stirring paddle 33 is arranged on shaft 32；Described shaft 32 is provided with shaft 32 through hole along its centrage；The position contacted with shaft 32 bottom described reactor body 1 is provided with agitator 3 water inlet；The position that described reactor body 1 top contacts with shaft 32 is provided with agitator 3 outlet；Described agitator 3 water inlet all connects with described shaft 32 through hole with agitator 3 outlet；Described stirring paddle 33 is sector structure；Described stirring paddle 33 is welded to connect with shaft 32, is provided with reactor sleeve between described agitator 3 and reactor body 1；Described reactor sleeve includes reactor sleeve lining and reactor sleeve outer wall；Built-in heat exchange cavity is formed between described reactor sleeve lining and reactor sleeve outer wall；Reactor sleeve water inlet it is provided with bottom described reactor body 1；Described reactor body 1 top is provided with reactor sleeve outlet；The position of center line of described stirring paddle is provided with stirring paddle cavity 313；Described stirring paddle cavity 313 connects with shaft through hole.
Claims (8)
1. a built-in heat exchange reactor, including reactor body, reacting kettle jacketing, agitator and reactor support, it is characterised in that described reactor body is arranged on reactor support；The upper end of described reactor body is provided with at least one reactor charging aperture；The lower end of described reactor body is provided with a reactor discharging opening；Described reacting kettle jacketing is arranged on reactor outer body；External hot exchange cavity is formed between described reacting kettle jacketing and reactor body；The lower end of described reacting kettle jacketing is provided with reacting kettle jacketing water inlet；The upper end of described reacting kettle jacketing is provided with reacting kettle jacketing outlet；Described agitator is arranged on the centrage of reactor body；Described agitator includes servomotor, shaft and stirring paddle；Described servomotor is arranged on the top of reactor body；Described shaft is connected with servomotor；Described stirring paddle is arranged on shaft；Described shaft is provided with shaft through hole along its centrage；The position that described reactor body bottom portion contacts with shaft is provided with agitator water inlet；The position that described reactor body upper part contacts with shaft is provided with agitator outlet；Described agitator water inlet all connects with described shaft through hole with agitator outlet；Described stirring paddle is sector structure；Described stirring paddle and shaft are welded to connect；The position of center line of described stirring paddle is provided with stirring paddle cavity；Described stirring paddle cavity connects with shaft through hole.
2. built-in heat exchange reactor according to claim 1, it is characterised in that described agitator water inlet is provided with heat exchange medium delivery pump and heat exchange medium storage warehouse.
3. built-in heat exchange reactor according to claim 1, it is characterised in that described agitator outlet includes agitator and goes out water hull；Described agitator goes out water hull and is arranged on the top of reactor body, is positioned at the lower section of servomotor；Described agitator water outlet valve jacket is located on shaft；Described agitator goes out water hull and has water outlet cavity；Described shaft is communicated with mouth；Described connected entrance connects with shaft through hole；Connected entrance on described shaft is positioned at water chamber body；Described agitator goes out water hull and is provided with agitator outlet；Described agitator outlet connects with water outlet cavity.
4. built-in heat exchange reactor according to claim 3, it is characterised in that described agitator goes out water hull and is provided with lubricating gasket with shaft contact site；The outside of described lubricating gasket is provided with airtight and watertight padding circle；The outside of described airtight and watertight padding circle is provided with sealing lid.
5. built-in heat exchange reactor according to claim 4, it is characterised in that described sealing lid goes out water hull screw threads for fastening and is connected with agitator.
6. built-in heat exchange reactor according to claim 1, it is characterised in that described reactor bodies top is provided with three reactor charging apertures.
7. built-in heat exchange reactor according to claim 1, it is characterised in that described stirring paddle is that inverted triangle is arranged on reactor this is internal.
8. built-in heat exchange reactor according to claim 1, it is characterised in that be provided with reactor sleeve between described agitator and reactor body；Described reactor sleeve includes reactor sleeve lining and reactor sleeve outer wall；Built-in heat exchange cavity is formed between described reactor sleeve lining and reactor sleeve outer wall；Described reactor body bottom portion is provided with reactor sleeve water inlet；Described reactor bodies top is provided with reactor sleeve outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610274851.4A CN105771861A (en) | 2016-04-28 | 2016-04-28 | Internal heat exchange reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610274851.4A CN105771861A (en) | 2016-04-28 | 2016-04-28 | Internal heat exchange reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105771861A true CN105771861A (en) | 2016-07-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610274851.4A Pending CN105771861A (en) | 2016-04-28 | 2016-04-28 | Internal heat exchange reactor |
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| CN (1) | CN105771861A (en) |
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| CN108079929A (en) * | 2018-01-31 | 2018-05-29 | 四川普思瑞新材料有限公司 | A kind of production of resins system |
| CN110259399A (en) * | 2019-06-25 | 2019-09-20 | 成都华寰环保科技有限公司 | Base oil recovery process and its device in a kind of drilling well oil-base mud landwaste |
| CN110586007A (en) * | 2019-10-18 | 2019-12-20 | 深圳市驭智装备技术有限公司 | Environment-friendly heating device's reation kettle |
| CN111066813A (en) * | 2019-11-15 | 2020-04-28 | 嘉兴沃特泰科环保科技股份有限公司 | Preparation method and device of oxidation type bactericide |
| CN111298739A (en) * | 2020-04-03 | 2020-06-19 | 王光彪 | Reaction kettle with accurate temperature control |
| CN112892443A (en) * | 2021-01-14 | 2021-06-04 | 江西欧普特实业有限公司 | Modified silica gel reation kettle of upper and lower circulation material |
| CN113442321A (en) * | 2021-05-15 | 2021-09-28 | 台州市左岳钮扣有限公司 | PET beverage bottle waste recycling button resin preparation equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108079929A (en) * | 2018-01-31 | 2018-05-29 | 四川普思瑞新材料有限公司 | A kind of production of resins system |
| CN108079929B (en) * | 2018-01-31 | 2023-08-15 | 四川普思瑞新材料有限公司 | Resin production system |
| CN110259399A (en) * | 2019-06-25 | 2019-09-20 | 成都华寰环保科技有限公司 | Base oil recovery process and its device in a kind of drilling well oil-base mud landwaste |
| CN110259399B (en) * | 2019-06-25 | 2024-02-06 | 成都华寰环保科技有限公司 | Process and device for recovering base oil from drilling oil-based mud cuttings |
| CN110586007A (en) * | 2019-10-18 | 2019-12-20 | 深圳市驭智装备技术有限公司 | Environment-friendly heating device's reation kettle |
| CN111066813A (en) * | 2019-11-15 | 2020-04-28 | 嘉兴沃特泰科环保科技股份有限公司 | Preparation method and device of oxidation type bactericide |
| CN111066813B (en) * | 2019-11-15 | 2021-06-15 | 嘉兴沃特泰科环保科技股份有限公司 | Preparation method and device of oxidation type bactericide |
| CN111298739A (en) * | 2020-04-03 | 2020-06-19 | 王光彪 | Reaction kettle with accurate temperature control |
| CN112892443A (en) * | 2021-01-14 | 2021-06-04 | 江西欧普特实业有限公司 | Modified silica gel reation kettle of upper and lower circulation material |
| CN113442321A (en) * | 2021-05-15 | 2021-09-28 | 台州市左岳钮扣有限公司 | PET beverage bottle waste recycling button resin preparation equipment |
| CN113442321B (en) * | 2021-05-15 | 2022-05-31 | 台州市左岳钮扣有限公司 | PET beverage bottle waste recycling button resin preparation equipment |
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