CN202270525U - Heat dissolving reaction device with impurity removing function - Google Patents
Heat dissolving reaction device with impurity removing function Download PDFInfo
- Publication number
- CN202270525U CN202270525U CN2011203864286U CN201120386428U CN202270525U CN 202270525 U CN202270525 U CN 202270525U CN 2011203864286 U CN2011203864286 U CN 2011203864286U CN 201120386428 U CN201120386428 U CN 201120386428U CN 202270525 U CN202270525 U CN 202270525U
- Authority
- CN
- China
- Prior art keywords
- agitated reactor
- heating
- reaction kettle
- reaction unit
- dissolving reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A heat dissolving reaction device with an impurity removing function comprises a reaction kettle (10), and a feed opening (11) and a discharge opening (12) which are formed on the casing wall of the reaction kettle (10), a motor (20) is mounted at the top of the reaction kettle (10), the output shaft of the motor is connected with a stirring shaft (30) leading to the reaction kettle (10) vertically, the end of the stirring shaft (30), which extends into the reaction kettle (10), is connected with a stirring vane (40), the heat dissolving reaction device further comprises a heat exchange pipeline (50) placed inside the reaction kettle (10) and positioned above the stirring vane (40), the pipe orifices at the two ends of the heat exchange pipeline (50) extend out of the casing wall of the reaction kettle (10) respectively and used as a vapor inlet (51) and a steam outlet (52); and an impurity outlet opening (13) is further formed at the bottom of the reaction kettle (10). The device has a simple structure, is low in cost, can effectively remove impurities in feed liquid after heated, thereby ensuring product quality.
Description
Technical field
The utility model relates to the relevant devices of implementing chemistry or physical method; Particularly relate to the general chemistry or the used device of physical method that are carried out under fluid and the solid particle situation having, relate in particular to industrial heating for dissolving reaction unit with removal of impurities function.
Background technology
Prior art copper sulphate heating for dissolving reaction unit; As shown in Figure 2; Its agitated reactor that uses 100 is box hat liner epoxy resin structural; Steam directly feeds to agitated reactor 100 through pipeline 500, contacts with liquid in the still and heats, discharging opening 120 dischargings at the bottom of still in the lump of copper sulphate after the heating for dissolving and insoluble impurity.There is following shortcoming in this reaction unit: 1) agitated reactor is the structure of box hat inner bushing ring epoxy layer, and in heating process, epoxy resin comes off easily, causes the interior feed liquid of agitated reactor by contaminating impurity; 2) the direct feed liquid in metallic conduit feeds still of steam causes ducted iron substance to come off because of temperature is high, thereby iron tramp is brought in the feed liquid; 3) the copper-bath product after the heating for dissolving through the discharging of Polycondensation Reactor and Esterification Reactor discharging opening, does not possess the removal of impurities function with insoluble impurity.
Summary of the invention
The technical problem that the utility model will solve is to avoid the weak point of above-mentioned prior art and a kind of heating for dissolving reaction unit with removal of impurities function is provided; It is simple in structure; With low cost and can effectively remove the impurity in the feed liquid of heating back, thus product quality guaranteed.
The technical scheme that the utility model solve the technical problem proposition is: a kind of heating for dissolving reaction unit with removal of impurities function; Comprise agitated reactor, and be arranged at charging aperture and discharging opening on this agitated reactor shell wall, said agitated reactor top is equipped with motor; Its output shaft links the shaft that vertically feeds in the said agitated reactor; The termination that this shaft stretches in the agitated reactor is connected with stirring arm, especially: also comprise placing in the said agitated reactor, and be positioned at the heat exchanging pipe of said stirring arm top; The two ends mouth of pipe of this heat exchanging pipe stretches out respectively outside the said agitated reactor shell wall, is used as steam inlet and steam (vapor) outlet; Said agitated reactor bottom also is provided with the impurity outlet.
Said heat exchanging pipe is the titanium pipe of multiple " U " shape.
The shell wall structure of said agitated reactor is the macromolecule polymeric material of steel casing liner vinyl.
The top of said agitated reactor is the hollow circular ring cylinder that binds, and the bottom is inverted hollow cone body, and said heat exchanging pipe places in the circle ring column on said agitated reactor top, and said stirring arm is positioned at the inversion hollow cone body of said agitated reactor bottom.
Said discharging opening is arranged on the nearly inversion hollow cone body root junction of said agitated reactor top shell wall, and said impurity outlet is arranged on the inversion hollow cone body tip of said agitated reactor bottom.
Compare with prior art, the beneficial effect that the utlity model has the heating for dissolving reaction unit of removal of impurities function is:
1, adopt the multiple U-shaped pipeline of titanium delivering vapor, carry out heat exchange with feed liquid in the agitated reactor, said pipeline is high temperature resistant, corrosion-resistant, can not cause line clogging because of corrosion; Because be indirect, avoided steam directly to contact feed liquid and the iron tramp in the pipeline has been brought in the still in the feed liquid;
2, the impurity outlet is arranged on the agitated reactor bottom, and then in the past a little upper part of agitated reactor shell wall, the supernatant after the dissolving separates with impurity at the bottom of the still discharging opening, thereby has guaranteed product quality;
3, its agitated reactor adopts phenolic aldehyde epoxy vinyl resin to do liner, has stronger heat-resisting ability, has avoided kettle internal layer heat ageing to come off and impurity is dissolved in the feed liquid.
Description of drawings
Fig. 1 is that the overall structure that the utlity model has the heating for dissolving reaction unit of removal of impurities function is partly cutd open sketch map;
Fig. 2 is the structural representation of prior art copper sulphate heating for dissolving agitated reactor.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is done further detailed description.
As shown in Figure 1, a kind of heating for dissolving reaction unit with removal of impurities function comprises agitated reactor 10; And be arranged at the charging aperture 11 and discharging opening 12 on these agitated reactor 10 shell walls; Said agitated reactor 10 tops are equipped with motor 20, and its output shaft links the shaft 30 that vertically feeds in the said agitated reactor 10, and the termination that this shaft 30 stretches in the agitated reactor 10 is connected with stirring arm 40; Also comprise and placing in the said agitated reactor 10; And be positioned at the heat exchanging pipe 50 of said stirring arm 40 tops, the two ends mouth of pipe of this heat exchanging pipe 50 stretches out respectively outside said agitated reactor 10 shell walls, is used as steam inlet 51 and steam (vapor) outlet 52; Said agitated reactor 10 bottoms also are provided with impurity outlet 13.
Said heat exchanging pipe 50 is the titanium pipe of multiple " U " shape.
The shell wall structure of said agitated reactor 10 is the macromolecule polymeric material of steel casing liner vinyl.
The top of said agitated reactor 10 is the hollow circular ring cylinder that binds; The bottom is inverted hollow cone body; Said heat exchanging pipe 50 places in the circle ring column on said agitated reactor 10 tops, and said stirring arm 40 is positioned at the inversion hollow cone body of said agitated reactor 10 bottoms.
Said discharging opening 12 is arranged on the nearly inversion hollow cone body root junction of said agitated reactor 10 top shell walls, and said impurity outlet 13 is arranged on the inversion hollow cone body tip of said agitated reactor 10 bottoms.
Claims (5)
1. heating for dissolving reaction unit with removal of impurities function; Comprise agitated reactor (10); And be arranged at charging aperture (11) and the discharging opening (12) on this agitated reactor (10) shell wall, and said agitated reactor (10) top is equipped with motor (20), and its output shaft links the shaft (30) that vertically feeds in the said agitated reactor (10); The termination that this shaft (30) stretches in the agitated reactor (10) is connected with stirring arm (40), it is characterized in that:
Also comprise and placing in the said agitated reactor (10); And be positioned at the heat exchanging pipe (50) of said stirring arm (40) top; The two ends mouth of pipe of this heat exchanging pipe (50) stretches out respectively outside said agitated reactor (10) shell wall, is used as steam inlet (51) and steam (vapor) outlet (52); Said agitated reactor (10) bottom also is provided with impurity outlet (13).
2. heating for dissolving reaction unit as claimed in claim 1 is characterized in that: said heat exchanging pipe (50) is the titanium pipe of multiple " U " shape.
3. heating for dissolving reaction unit as claimed in claim 1 is characterized in that: the shell wall structure of said agitated reactor (10) is the macromolecule polymeric material of steel casing liner vinyl.
4. heating for dissolving reaction unit as claimed in claim 1; It is characterized in that: the top of said agitated reactor (10) is the hollow circular ring cylinder that binds; The bottom is inverted hollow cone body; Said heat exchanging pipe (50) places in the circle ring column on said agitated reactor (10) top, and said stirring arm (40) is positioned at the inversion hollow cone body of said agitated reactor (10) bottom.
5. heating for dissolving reaction unit as claimed in claim 1; It is characterized in that: said discharging opening (12) is arranged on the nearly inversion hollow cone body root junction of said agitated reactor (10) top shell wall, and said impurity outlet (13) is arranged on the inversion hollow cone body tip of said agitated reactor (10) bottom.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203864286U CN202270525U (en) | 2011-10-12 | 2011-10-12 | Heat dissolving reaction device with impurity removing function |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203864286U CN202270525U (en) | 2011-10-12 | 2011-10-12 | Heat dissolving reaction device with impurity removing function |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202270525U true CN202270525U (en) | 2012-06-13 |
Family
ID=46190916
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011203864286U Expired - Lifetime CN202270525U (en) | 2011-10-12 | 2011-10-12 | Heat dissolving reaction device with impurity removing function |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202270525U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104711116A (en) * | 2015-03-11 | 2015-06-17 | 会同县贤胜油业有限责任公司 | Heat-agitation type slag-removing device used for walnut oil production process |
CN113731305A (en) * | 2021-09-16 | 2021-12-03 | 洛阳市三诺化工有限公司 | Conjoined stirring kettle for preparing TIBP triisobutyl phosphate |
-
2011
- 2011-10-12 CN CN2011203864286U patent/CN202270525U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104711116A (en) * | 2015-03-11 | 2015-06-17 | 会同县贤胜油业有限责任公司 | Heat-agitation type slag-removing device used for walnut oil production process |
CN104711116B (en) * | 2015-03-11 | 2017-10-03 | 会同县贤胜油业有限责任公司 | A kind of heat being used in production technology of walnut oil disturbs formula deslagging device |
CN113731305A (en) * | 2021-09-16 | 2021-12-03 | 洛阳市三诺化工有限公司 | Conjoined stirring kettle for preparing TIBP triisobutyl phosphate |
CN113731305B (en) * | 2021-09-16 | 2023-03-21 | 洛阳市三诺化工有限公司 | Conjoined stirring kettle for preparing TIBP triisobutyl phosphate |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202447086U (en) | Stainless steel reaction kettle | |
CN202173933U (en) | Preparation device for coal bar agglomerant | |
CN202270525U (en) | Heat dissolving reaction device with impurity removing function | |
CN204365129U (en) | Novel anticorrosion desulphurization plant | |
CN105561893B (en) | A kind of grease collar oxidation reaction apparatus | |
CN203971901U (en) | A kind of solid melting device | |
CN201969551U (en) | Separation kettle for producing T acid | |
CN205361349U (en) | Alkali fusion cauldron with steam heating device | |
CN206970510U (en) | A kind of Steam-Mixer for being used to extract carragheen | |
CN201558557U (en) | Adipic acid vacuum concentration device | |
CN203620636U (en) | Easily heated polycondensation reaction kettle | |
CN101672570B (en) | Vertical stirring vacuum furnace | |
CN202509007U (en) | Methacrylic acid heavy component recovery device | |
CN203778041U (en) | High-efficiency continuous sulfur melting kettle | |
CN202527164U (en) | Liquid medicament mixing reaction tank with steam heating | |
CN202376796U (en) | Spiral jet reaction tank for extracting natural medicine active ingredient by using subcritical water | |
CN206064413U (en) | A kind of employing reduced pressure distillation process disposes the reactor of the fluorine-containing material of separation and recovery | |
CN201997333U (en) | Reaction kettle | |
CN202526920U (en) | Internal spiral evaporator | |
CN206262121U (en) | A kind of starch sugar concentration evaporator | |
CN104496751B (en) | A kind of processing means for reclaiming glycerol in biodiesel and processing method thereof | |
CN204294218U (en) | A kind of retort of the tortuous bow shape agitating fins with turbine stirring dish | |
CN220142648U (en) | Extracting tank | |
CN108794301A (en) | A kind of refining plant of biological diesel oil byproduct crude glycerine | |
CN216934783U (en) | Steam recompression extraction device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20120613 |