CN105771860A - Reaction kettle with accelerated mixing pipeline - Google Patents
Reaction kettle with accelerated mixing pipeline Download PDFInfo
- Publication number
- CN105771860A CN105771860A CN201610274813.9A CN201610274813A CN105771860A CN 105771860 A CN105771860 A CN 105771860A CN 201610274813 A CN201610274813 A CN 201610274813A CN 105771860 A CN105771860 A CN 105771860A
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- reactor
- reactor body
- reaction kettle
- sub
- mixing
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Classifications
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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
-
- 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
- B01F27/50—Pipe mixers, i.e. mixers wherein the materials to be mixed flow continuously through pipes, e.g. column mixers
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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
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/823—Combinations of dissimilar mixers in two or more alternative mixing receptacles, e.g. mixing in one receptacle and dispensing from another receptacle
-
- 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
-
- 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
-
- 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 a reaction kettle with an accelerated mixing pipeline. The reaction kettle comprises a reaction kettle body, a reaction kettle jacket, a reaction kettle support and a stirring device. The reaction kettle jacket is arranged on the outer side of the reaction kettle body. A jacket water inlet is arranged at the bottom of the reaction kettle jacket. A jacket water outlet is arranged at the top of the reaction kettle jacket. The jacket water inlet and the jacket water outlet are connected with an external temperature adjustment cavity. The stirring device is arranged in the reaction kettle body along the center line of the reaction kettle body, and comprises two sub stirrers and a connection wall. The sub stirrers are arranged parallelly and the connection wall is used for connecting the sub stirrers. The two sub stirrers and the connection wall are connected to form the accelerated mixing pipeline. The connection wall connects the sub stirrers with the inner wall of the reaction kettle body. The connection wall is provided with an internal temperature adjustment cavity. The internal temperature adjustment cavity is communicated with the external temperature adjustment cavity. The reaction kettle has the advantages that circular stirring flows are formed in the reaction kettle body through the accelerated mixing pipeline to achieve sufficient material mixing, and accordingly, reaction speed and production efficiency are improved.
Description
Technical field
The present invention relates to pressure vessel field, especially relate to a kind of pipeline and accelerate the reactor of mixing.
Background technology
Reactor is combined reaction container, according to reaction condition to reactor structure function and the design configuring adnexa.All can complete pre-set reactions steps with higher automaticity from the charging-reaction-discharging started, the temperature in course of reaction, pressure, mechanics are controlled the important parameters such as (stirring, air blast etc.), reactant/product concentration and carry out strict regulation and control.Its structure is generally made up of kettle, actuating device, agitating device, heater, chiller, sealing device.Auxiliary equipment supporting accordingly: dephlegmator, condenser, water knockout drum, collecting tank, filter etc..
Temperature, reactant exposure level required when the reaction rate of reactor reacts with reactant are relevant, therefore, in order to improve production efficiency, under the premise that security is guaranteed, regulate temperature as much as possible so as to quickly enter optimal reaction temperature.Meanwhile, so as to be sufficiently mixed contact, it is thus achieved that fastest response speed.But, the hybrid technology that the reactor of prior art adopts appoints the requirement so not reaching production optimum speed, therefore to obtain higher production efficiency, the invention provides a kind of pipeline and accelerates the reactor of mixing.
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, especially one can be effectively improved response speed, and the pipeline improving production efficiency accelerates the reactor of mixing.
For solving the problems referred to above, the scheme that the present invention adopts is as follows: a kind of pipeline accelerates the reactor of mixing, it is characterised in that include reactor body, reacting kettle jacketing, reactor support and agitating device；Described reactor body is arranged on reactor support；The top of described reactor body is provided with at least two reactor charging aperture；The bottom of described reactor body is provided with a reactor discharging opening；Described reacting kettle jacketing is arranged on the outside of reactor body, and and forms external temp adjustment chamber between reactor body；Chuck water inlet it is provided with bottom described reacting kettle jacketing；Described reacting kettle jacketing top is provided with chuck outlet；Described chuck water inlet and chuck outlet all regulate chamber with external temp and are connected；Described agitating device is arranged on reactor body interior along reactor body central line；Described agitating device includes the sub-agitator of arranged in parallel two and the connection wall for connexon agitator；The sub-agitator of said two and connection wall form one and accelerate mixing duct；The inwall of sub-agitator with reactor body is connected by described connection wall；Described connection wall has built-in temperature and regulates chamber；Described built-in temperature regulates chamber and connects with external temp adjustment chamber.
Further, according to above-mentioned design, pipeline accelerates the reactor of mixing, and described sub-agitator includes stirring paddle, shaft and servomotor；Described stirring paddle is connected with servomotor by shaft；Described servomotor is arranged on outside reacting kettle jacketing；Described stirring paddle is arranged in acceleration mixing duct；The thrust that the liquid accelerated in mixing duct is downward can be provided during the work of described stirring paddle.
Further, according to above-mentioned design, pipeline accelerates the reactor of mixing, and the lower position of described reactor body interior is provided with drainage system；Described drainage system can the liquid drain of in the future autoacceleration mixing duct move upward.
Further, according to above-mentioned design, pipeline accelerates the reactor of mixing, and described drainage system is conical structure, and its taper seat is the arcuate structure caved inward.
Further, according to above-mentioned design, pipeline accelerates the reactor of mixing, and described reacting kettle jacketing is connected with temperature regulating medium holding vessel and circulating pump；Described external temp regulates intracavity and is provided with temperature regulating medium.
Further, according to above-mentioned design, pipeline accelerates the reactor of mixing, and the upper end of described reactor body interior is provided with pre-mixing apparatus；Described pre-mixing apparatus is connected with reactor charging aperture；Premixing discharging opening it is provided with bottom described pre-mixing apparatus；Described premixing discharging opening is positioned at the surface of recirculation unit.
The technique effect of the present invention is as follows: when the reactor that the pipeline of the present invention accelerates to mix utilizes stirring paddle to start, produce downward motive force, make the intrinsic downward liquid flow of reactor, when liquid haptoreaction still body bottom portion, turn under the effect of reactor body bottom portion and move upward, preferred reaction still body bottom portion is arcuate structure, the liquid flowed downward taps under the reactor body effect of curved bottom structure and flows to surrounding, finally move up to reactor body upper part, and then entrance agitating device, form circulation stirring.The agitating device of the present invention is for accelerating mixing duct structure, it is possible to reactor body is divided into two parts, under the effect of agitating device, circulates in this internal formation of reactor.Connection wall for splitting reactor body is set to hollow structure；Namely form built-in temperature and regulate chamber, and built-in temperature regulates chamber and connects with external temp adjustment chamber.Fill set temperature regulating medium in external temp adjustment chamber and built-in temperature adjustment intracavity, temperature regulating medium enters external temp from the chuck water inlet bottom reacting kettle jacketing and regulates chamber and built-in temperature adjustment chamber, then discharge from the chuck outlet on reacting kettle jacketing top, form a circulation.Reaction temperature in reactor is adjusted.
In the lower section of recirculation unit, reactor body interior be connected with drainage system, be used for improving the intrinsic liquid circulation stirring efficiency of reactor, be namely provided with drainage system at this internal bottom position that is positioned at of reactor.Drainage system is preferably conical structure, and its taper seat is the arcuate structure caved inward.
Further, it is provided above pre-mixing apparatus at circulation stirring device, for improving stirring efficiency further, improves production efficiency, reduce production cost.
Accompanying drawing explanation
Fig. 1 is the reactor structural representation that pipeline accelerates mixing.
Fig. 2 is agitating device cross section structure schematic diagram.
Fig. 3 is pre-mixing apparatus structural representation.
Fig. 4 is drainage system three-view diagram.
Wherein, 1 is reactor body；2 is reacting kettle jacketing；3 is reactor support；4 is sub-agitator；5 for connecting wall；6 regulate chamber for external temp；7 regulate chamber for built-in temperature；8 is drainage system；9 is pre-mixing apparatus；11 is reactor charging aperture；12 is reactor discharging opening；21 is chuck water inlet；22 is chuck outlet；41 is servomotor；42 is shaft；43 is stirring paddle；81 is drainage system left view；82 is drainage system front view；83 is drainage system top view；91 is premixing discharging opening.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further details.
Embodiment 1: a kind of pipeline accelerates the reactor of mixing, including reactor body 1, reacting kettle jacketing 2, reactor support 3 and agitating device；Described reactor body 1 is arranged on reactor support 3；The top of described reactor body 1 is provided with at least two reactor charging aperture 11；The bottom of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on the outside of reactor body 1, and and forms external temp adjustment chamber 6 between reactor body 1；It is provided with chuck water inlet 21 bottom described reacting kettle jacketing 2；Described reacting kettle jacketing 2 top is provided with chuck outlet 22；Described chuck water inlet 21 and chuck outlet 22 all regulate chamber 6 with external temp and are connected；It is internal that described agitating device is arranged on reactor body 1 along reactor body 1 centrage；Described agitating device includes the sub-agitator 4 of arranged in parallel two and the connection wall 5 for connexon agitator 4；The sub-agitator 4 of said two and connection wall 5 form one and accelerate mixing duct；Sub-agitator 4 is connected by described connection wall 5 with the inwall of reactor body 1；Described connection wall 5 has built-in temperature and regulates chamber 7；Described built-in temperature regulates chamber 7 and connects with external temp adjustment chamber 6.
Embodiment 2: a kind of pipeline accelerates the reactor of mixing, including reactor body 1, reacting kettle jacketing 2, reactor support 3 and agitating device；Described reactor body 1 is arranged on reactor support 3；The top of described reactor body 1 is provided with at least two reactor charging aperture 11；The bottom of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on the outside of reactor body 1, and and forms external temp adjustment chamber 6 between reactor body 1；It is provided with chuck water inlet 21 bottom described reacting kettle jacketing 2；Described reacting kettle jacketing 2 top is provided with chuck outlet 22；Described chuck water inlet 21 and chuck outlet 22 all regulate chamber 6 with external temp and are connected；It is internal that described agitating device is arranged on reactor body 1 along reactor body 1 centrage；Described agitating device includes the sub-agitator 4 of arranged in parallel two and the connection wall 5 for connexon agitator 4；The sub-agitator 4 of said two and connection wall 5 form one and accelerate mixing duct；Sub-agitator 4 is connected by described connection wall 5 with the inwall of reactor body 1；Described connection wall 5 has built-in temperature and regulates chamber 7；Described built-in temperature regulates chamber 7 and connects with external temp adjustment chamber 6, and described sub-agitator 4 includes stirring paddle 43, shaft 42 and servomotor 41；Described stirring paddle 43 is connected with servomotor 41 by shaft 42；Described servomotor 41 is arranged on outside reacting kettle jacketing 2；Described stirring paddle 43 is arranged in acceleration mixing duct；Described stirring paddle 43 can provide the thrust that the liquid accelerated in mixing duct is downward when working.
Embodiment 3: a kind of pipeline accelerates the reactor of mixing, including reactor body 1, reacting kettle jacketing 2, reactor support 3 and agitating device；Described reactor body 1 is arranged on reactor support 3；The top of described reactor body 1 is provided with at least two reactor charging aperture 11；The bottom of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on the outside of reactor body 1, and and forms external temp adjustment chamber 6 between reactor body 1；It is provided with chuck water inlet 21 bottom described reacting kettle jacketing 2；Described reacting kettle jacketing 2 top is provided with chuck outlet 22；Described chuck water inlet 21 and chuck outlet 22 all regulate chamber 6 with external temp and are connected；It is internal that described agitating device is arranged on reactor body 1 along reactor body 1 centrage；Described agitating device includes the sub-agitator 4 of arranged in parallel two and the connection wall 5 for connexon agitator 4；The sub-agitator 4 of said two and connection wall 5 form one and accelerate mixing duct；Sub-agitator 4 is connected by described connection wall 5 with the inwall of reactor body 1；Described connection wall 5 has built-in temperature and regulates chamber 7；Described built-in temperature regulates chamber 7 and connects with external temp adjustment chamber 6, and the lower position within described reactor body 1 is provided with drainage system 8；Described drainage system 8 can the liquid drain of in the future autoacceleration mixing duct move upward.
Embodiment 4: a kind of pipeline accelerates the reactor of mixing, including reactor body 1, reacting kettle jacketing 2, reactor support 3 and agitating device；Described reactor body 1 is arranged on reactor support 3；The top of described reactor body 1 is provided with at least two reactor charging aperture 11；The bottom of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on the outside of reactor body 1, and and forms external temp adjustment chamber 6 between reactor body 1；It is provided with chuck water inlet 21 bottom described reacting kettle jacketing 2；Described reacting kettle jacketing 2 top is provided with chuck outlet 22；Described chuck water inlet 21 and chuck outlet 22 all regulate chamber 6 with external temp and are connected；It is internal that described agitating device is arranged on reactor body 1 along reactor body 1 centrage；Described agitating device includes the sub-agitator 4 of arranged in parallel two and the connection wall 5 for connexon agitator 4；The sub-agitator 4 of said two and connection wall 5 form one and accelerate mixing duct；Sub-agitator 4 is connected by described connection wall 5 with the inwall of reactor body 1；Described connection wall 5 has built-in temperature and regulates chamber 7；Described built-in temperature regulates chamber 7 and connects with external temp adjustment chamber 6, and the lower position within described reactor body 1 is provided with drainage system 8；Described drainage system 8 can the liquid drain of in the future autoacceleration mixing duct move upward, and described drainage system 8 is conical structure, and its taper seat is the arcuate structure caved inward.
Embodiment 5: a kind of pipeline accelerates the reactor of mixing, including reactor body 1, reacting kettle jacketing 2, reactor support 3 and agitating device；Described reactor body 1 is arranged on reactor support 3；The top of described reactor body 1 is provided with at least two reactor charging aperture 11；The bottom of described reactor body 1 is provided with a reactor discharging opening 12；Described reacting kettle jacketing 2 is arranged on the outside of reactor body 1, and and forms external temp adjustment chamber 6 between reactor body 1；It is provided with chuck water inlet 21 bottom described reacting kettle jacketing 2；Described reacting kettle jacketing 2 top is provided with chuck outlet 22；Described chuck water inlet 21 and chuck outlet 22 all regulate chamber 6 with external temp and are connected；It is internal that described agitating device is arranged on reactor body 1 along reactor body 1 centrage；Described agitating device includes the sub-agitator 4 of arranged in parallel two and the connection wall 5 for connexon agitator 4；The sub-agitator 4 of said two and connection wall 5 form one and accelerate mixing duct；Sub-agitator 4 is connected by described connection wall 5 with the inwall of reactor body 1；Described connection wall 5 has built-in temperature and regulates chamber 7；Described built-in temperature regulates chamber 7 and connects with external temp adjustment chamber 6, and the upper end within described reactor body 1 is provided with pre-mixing apparatus 9；Described pre-mixing apparatus 9 is connected with reactor charging aperture 11；It is provided with premixing discharging opening 91 bottom described pre-mixing apparatus 9；Described premixing discharging opening 91 is positioned at the surface of recirculation unit.
Claims (6)
1. the reactor that a pipeline accelerates to mix, it is characterised in that include reactor body, reacting kettle jacketing, reactor support and agitating device；Described reactor body is arranged on reactor support；The top of described reactor body is provided with at least two reactor charging aperture；The bottom of described reactor body is provided with a reactor discharging opening；Described reacting kettle jacketing is arranged on the outside of reactor body, and and forms external temp adjustment chamber between reactor body；Chuck water inlet it is provided with bottom described reacting kettle jacketing；Described reacting kettle jacketing top is provided with chuck outlet；Described chuck water inlet and chuck outlet all regulate chamber with external temp and are connected；Described agitating device is arranged on reactor body interior along reactor body central line；Described agitating device includes the sub-agitator of arranged in parallel two and the connection wall for connexon agitator；The sub-agitator of said two and connection wall form one and accelerate mixing duct；The inwall of sub-agitator with reactor body is connected by described connection wall；Described connection wall has built-in temperature and regulates chamber；Described built-in temperature regulates chamber and connects with external temp adjustment chamber.
2. pipeline accelerates the reactor of mixing according to claim 1, it is characterised in that described sub-agitator includes stirring paddle, shaft and servomotor；Described stirring paddle is connected with servomotor by shaft；Described servomotor is arranged on outside reacting kettle jacketing；Described stirring paddle is arranged in acceleration mixing duct；The thrust that the liquid accelerated in mixing duct is downward can be provided during the work of described stirring paddle.
3. pipeline accelerates the reactor of mixing according to claim 1, it is characterised in that the lower position of described reactor body interior is provided with drainage system；Described drainage system can the liquid drain of in the future autoacceleration mixing duct move upward.
4. pipeline accelerates the reactor of mixing according to claim 3, it is characterised in that described drainage system is conical structure, and its taper seat is the arcuate structure caved inward.
5. pipeline accelerates the reactor of mixing according to claim 1, it is characterised in that described reacting kettle jacketing is connected with temperature regulating medium holding vessel and circulating pump；Described external temp regulates intracavity and is provided with temperature regulating medium.
6. pipeline accelerates the reactor of mixing according to claim 1, it is characterised in that the upper end of described reactor body interior is provided with pre-mixing apparatus；Described pre-mixing apparatus is connected with reactor charging aperture；Premixing discharging opening it is provided with bottom described pre-mixing apparatus；Described premixing discharging opening is positioned at the surface of recirculation unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610274813.9A CN105771860A (en) | 2016-04-28 | 2016-04-28 | Reaction kettle with accelerated mixing pipeline |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610274813.9A CN105771860A (en) | 2016-04-28 | 2016-04-28 | Reaction kettle with accelerated mixing pipeline |
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| Publication Number | Publication Date |
|---|---|
| CN105771860A true CN105771860A (en) | 2016-07-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610274813.9A Pending CN105771860A (en) | 2016-04-28 | 2016-04-28 | Reaction kettle with accelerated mixing pipeline |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111943158A (en) * | 2020-08-24 | 2020-11-17 | 朱泽波 | Mechanical process flow for extracting ammonium magnesium phosphate from brine |
| CN113264581A (en) * | 2021-05-27 | 2021-08-17 | 科源智水(北京)科技有限公司 | Double-chamber three-dimensional strong mechanical pipeline mixer |
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|---|---|---|---|---|
| SU1005870A1 (en) * | 1981-02-25 | 1983-03-23 | Дзержинский филиал Научно-исследовательского и конструкторского института химического машиностроения | Reactor for polymerization in liquid dispersed system |
| CN2055740U (en) * | 1989-07-26 | 1990-04-11 | 煤炭科学研究总院唐山分院 | Stirring barrel with flow guiding ring seat |
| CN202516545U (en) * | 2012-05-02 | 2012-11-07 | 广州金凯新材料有限公司 | Internal recycle heating device of reaction still |
| CN203018087U (en) * | 2013-01-07 | 2013-06-26 | 濮阳可利威化工有限公司 | Reaction kettle |
| CN203990390U (en) * | 2014-05-20 | 2014-12-10 | 安徽中能矿机制造有限公司 | Ore pulp high efficiency stirring tank |
| CN104383870A (en) * | 2014-12-03 | 2015-03-04 | 成都索伊新材料有限公司 | Reaction kettle capable of controlling polymerization reaction temperature of various organic monomers |
| CN205700537U (en) * | 2016-04-28 | 2016-11-23 | 庆丰鞋业（江苏）有限公司 | A kind of pipeline accelerates the reactor of mixing |
-
2016
- 2016-04-28 CN CN201610274813.9A patent/CN105771860A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1005870A1 (en) * | 1981-02-25 | 1983-03-23 | Дзержинский филиал Научно-исследовательского и конструкторского института химического машиностроения | Reactor for polymerization in liquid dispersed system |
| CN2055740U (en) * | 1989-07-26 | 1990-04-11 | 煤炭科学研究总院唐山分院 | Stirring barrel with flow guiding ring seat |
| CN202516545U (en) * | 2012-05-02 | 2012-11-07 | 广州金凯新材料有限公司 | Internal recycle heating device of reaction still |
| CN203018087U (en) * | 2013-01-07 | 2013-06-26 | 濮阳可利威化工有限公司 | Reaction kettle |
| CN203990390U (en) * | 2014-05-20 | 2014-12-10 | 安徽中能矿机制造有限公司 | Ore pulp high efficiency stirring tank |
| CN104383870A (en) * | 2014-12-03 | 2015-03-04 | 成都索伊新材料有限公司 | Reaction kettle capable of controlling polymerization reaction temperature of various organic monomers |
| CN205700537U (en) * | 2016-04-28 | 2016-11-23 | 庆丰鞋业（江苏）有限公司 | A kind of pipeline accelerates the reactor of mixing |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111943158A (en) * | 2020-08-24 | 2020-11-17 | 朱泽波 | Mechanical process flow for extracting ammonium magnesium phosphate from brine |
| CN113264581A (en) * | 2021-05-27 | 2021-08-17 | 科源智水(北京)科技有限公司 | Double-chamber three-dimensional strong mechanical pipeline mixer |
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Application publication date: 20160720 |
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