CN204768643U - Reation kettle complete sets - Google Patents
Reation kettle complete sets Download PDFInfo
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- CN204768643U CN204768643U CN201520321477.XU CN201520321477U CN204768643U CN 204768643 U CN204768643 U CN 204768643U CN 201520321477 U CN201520321477 U CN 201520321477U CN 204768643 U CN204768643 U CN 204768643U
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- reation kettle
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Abstract
The utility model discloses a reation kettle complete sets, including a plurality of sub - reation kettle, still include female reation kettle, every sub - reation kettle's delivery outlet with all be provided with pipeline between female reation kettle's the pan feeding mouth, the last control valve that is provided with the interior conveying speed of control pipeline of pipeline. The reactant that obtains in a plurality of sub - reation kettle is carried to female reation kettle in through pipeline, carries out the intensive mixing and mix in female reation kettle, makes the liquid reactant that obtains at the stirring in -process in each sub - reation kettle, and the misce bene simultaneously can also be through the conveying speed of the sub - reation kettle internal reaction thing of the control of the control valve on the pipeline, and the reactant whole quality that further assurance finally obtained is even, effectively improves product quality.
Description
Technical field
The utility model relates to a kind of chemical production equipment field, and more particularly, it relates to a kind of reactor complete set of equipments.
Background technology
Namely the broad understanding of reactor has the container of physics or chemical reaction, by the structural design of container and parameter configuration, realizes the mixture function of the heating of technological requirement, evaporation, cooling and low high speed.Reactor is widely used in oil, chemical industry, rubber, agricultural chemicals, dyestuff, medicine, food, has been used for the pressure vessel of the technical process such as sulfuration, nitrated, hydrogenation, hydrocarbonylation, polymerization, condensation.
In the processing technology of phenolic resins, phenol and formaldehyde are injected reactor, fully after reaction, obtain the phenolic resins for the production of processing.In existing phenolic resins production line, a reactor produce the corresponding process line of the phenolic resins that obtains, directly the phenolic resins be obtained by reacting in reactor is delivered on streamline and processes.Because phenolic resins is in process of manufacture, according to the difference of extraneous reaction condition, the consumptions such as the uniformity coefficient such as, stirred in the temperature of reactor, reactor and curing agent, blowing agent, homogenize agent number, the phenolic resins performance produced all can be caused inconsistent.Therefore, after the production line by being connected with reactor is processed, the properties of product obtained also can have the difference of increasing, the liquid phenolic resin that batch reactor tank contemporaneity is produced is all be given in same client's hand, if the quality of the inconsistent meeting of properties of product to product affects greatly.
Utility model content
For the deficiency that prior art exists, the purpose of this utility model is to provide a kind of reactant quality that can make to obtain in multiple reactor uniform reactor complete set of equipments.
For achieving the above object, the utility model provides following technical scheme: a kind of reactor complete set of equipments, comprise some sub-reactors, also comprise female reactor, be provided with conveyance conduit between the delivery outlet of each described sub-reactor and the feeding mouth of described female reactor, described conveyance conduit be provided with the control valve controlling transporting velocity in conveyance conduit.
Preferably, the discharging opening of described female reactor is connected with some discharge nozzles, discharge nozzle described in every root is arranged the switch valve all having and control mass transport, described conveyance conduit is also provided with test tube, described test tube is provided with the check valve of control test pipe switch, described test tube position is arranged between control valve and sub-reactor delivery outlet.
Preferably, the paddle for being stirred by the material entered in female reactor is provided with in described female reactor.
Preferably, described female reactor is outside equipped with heat-insulation layer.
Compared with prior art, the reactant obtained in multiple sub-reactor, be delivered in female reactor by conveyance conduit, fully be uniformly mixed in female reactor, make the liquid reactant obtained in each sub-reactor in whipping process, mix, also control the transporting velocity of reactant in sub-reactor simultaneously by the control valve on conveyance conduit, the reactant total quality that further guarantee finally obtains is even, effectively improves the quality of products.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model reactor complete set of equipments embodiment;
Fig. 2 is the partial enlarged drawing in A portion in Fig. 1;
The female reactor cross section view in Fig. 3 position.
Reference numeral: 1, sub-reactor; 2, female reactor; 3, conveyance conduit; 4, discharge nozzle; 5, test tube; 11, delivery outlet; 21, discharging opening; 22, feeding mouth; 23, paddle; 24, heat-insulation layer; 31, control valve; 41, switch valve; 51, check valve.
Detailed description of the invention
Referring to figs. 1 through Fig. 3, the utility model reactor complete set of equipments embodiment is described further.
A kind of reactor complete set of equipments, comprise some sub-reactors 1, in phenolic resins production line, a reactor produce the corresponding process line of the phenolic resins that obtains, directly the phenolic resins be obtained by reacting in reactor is delivered on streamline and processes.Even if the reactant quality obtained in each reactor is qualified, but because how many meetings of the consumption such as uniformity coefficient and curing agent, blowing agent, homogenize agent stirred in the temperature of reactor, reactor there are differences, after putting into production, the product quality obtained can there are differences, make the mass deviation of finished product comparatively large, the product quality that impact is overall.Therefore, in order to obtain the product of uniform quality, improving the quality of products, arranging a rice reactor after sub-reactor 1, the delivery outlet 11 of every sub-reactor 1 is connected by conveyance conduit 3 with the feeding mouth 22 of female reactor 2.The reactant obtained in multiple sub-reactor 1, by after conveyance conduit 3, is delivered in female reactor 2.Preferably, the paddle 23 for being stirred by the material entered in female reactor 2 is provided with in female reactor 2.Because the reactant obtained in sub-reactor 1 is liquid resin, entering after in female reactor 2, the reactant obtained in each sub-reactor 1 can be made fully to mix by paddle 23, making overall capability and performance always, effectively improving the quality of products.
Preferably, paddle 23 in the shape of a spiral, in paddle 23 whipping process, can make reactant in female reactor 2, not only at female reactor 2 circumferentially mix and blend, by helical form paddle 23, can also flow in the axial direction, overall stir evenly.
Simultaneously, every root conveyance conduit 3 is provided with the control valve 31 controlling transporting velocity in conveyance conduit 3, simultaneously, the switch controlling conveyance conduit 3 is also driven by control valve 31, when reactant mass deviation in multiple sub-reactor 1 is larger, reduce transporting velocity, the compound entered in female reactor 2 can fully be stirred, make evenly overall; When reactant mass deviation in group reactor 1 is less, can transporting velocity be increased, increase transporting velocity, thus enhance productivity.
The outer setting of female reactor 2 also has heat-insulation layer 24, make the temperature in female reactor 2 can keep stable, when ensureing to stir in female reactor 2, the ambient temperature of reactant can be made all the time identical, avoid Yin Wendu different, cause the reactant stirred out in female reactor 2 in different time sections, occur the situation of mass deviation.
Further, the discharging opening 21 of female reactor 2 is connected with some discharge nozzles 4, every root discharge nozzle 4 is arranged the switch valve 41 all having and control mass transport, reactant in multiple sub-reactor 1 is all delivered in female reactor 2 and stirs, in order to improve overall production efficiency, the discharging opening 21 of female reactor 2 is connected with many with discharge nozzle 4, make a female reactor 2 can supply needed for the production of many production lines simultaneously, also control the conveying of reactant in female reactor 2 simultaneously by switch valve 41.
In sub-reactor 1, due to the deviation that material adds, the reactant that obtains in sub-reactor 1 can be made off quality, stir if underproof reactant is added in female reactor 2, the reactant total quality obtained in female reactor 2 can be caused to go wrong, affect in other reactors the normal use obtaining compound.Conveyance conduit 3 is also provided with test tube 5, test tube 5 is provided with the check valve 51 of control test pipe 5 switch, by test tube 5, sampling inspection can be carried out to the reactant exported in every sub-reactor 1, if there are quality problems, then closing the control valve 31 on this sub-reactor 1 output channel, avoiding reactant inferior to destroying the qualified reactant obtained in other sub-reactors 1.
Preferably, test tube 5 position is arranged between the delivery outlet 11 of control valve 31 and sub-reactor 1, is occurring quality problems, after rectifying and improving the reactor that there are quality problems, first open the check valve 51 on test tube 5, the reactant obtained after rectification is derived in test tube 5, proceeds to detect, after qualified, close check valve 51 again, open control valve 31, qualified reactant is delivered to female reactor 2 in carrier pipe, further ensure that the quality of product.
The above is only preferred embodiment of the present utility model, protection domain of the present utility model be not only confined to above-described embodiment, and all technical schemes belonged under the utility model thinking all belong to protection domain of the present utility model.It should be pointed out that for those skilled in the art, do not departing from the some improvements and modifications under the utility model principle prerequisite, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (4)
1. a reactor complete set of equipments, comprise some sub-reactors, it is characterized in that: also comprise female reactor, conveyance conduit is provided with between the delivery outlet of each described sub-reactor and the feeding mouth of described female reactor, described conveyance conduit is provided with the control valve controlling transporting velocity in conveyance conduit, described conveyance conduit is also provided with test tube, described test tube is provided with the check valve of control test pipe switch, described test tube position is arranged between control valve and sub-reactor delivery outlet.
2. reactor complete set of equipments according to claim 1, is characterized in that: the discharging opening of described female reactor is connected with some discharge nozzles, discharge nozzle described in every root is provided with the switch valve controlling mass transport.
3. reactor complete set of equipments according to claim 2, is characterized in that: be provided with the paddle for being stirred by the material entered in female reactor in described female reactor.
4. the reactor complete set of equipments according to claim 1 or 2 or 3, is characterized in that: described female reactor is outside equipped with heat-insulation layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520321477.XU CN204768643U (en) | 2015-05-19 | 2015-05-19 | Reation kettle complete sets |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520321477.XU CN204768643U (en) | 2015-05-19 | 2015-05-19 | Reation kettle complete sets |
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| CN204768643U true CN204768643U (en) | 2015-11-18 |
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| CN201520321477.XU Active CN204768643U (en) | 2015-05-19 | 2015-05-19 | Reation kettle complete sets |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107159061A (en) * | 2017-06-25 | 2017-09-15 | 盐城利民农化有限公司 | A kind of synthesizer of triazolone |
| CN107754999A (en) * | 2017-11-10 | 2018-03-06 | 江苏南方光纤科技有限公司 | Bare fibre reducing mechanism and bare fibre automatic recovery system |
-
2015
- 2015-05-19 CN CN201520321477.XU patent/CN204768643U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107159061A (en) * | 2017-06-25 | 2017-09-15 | 盐城利民农化有限公司 | A kind of synthesizer of triazolone |
| CN107754999A (en) * | 2017-11-10 | 2018-03-06 | 江苏南方光纤科技有限公司 | Bare fibre reducing mechanism and bare fibre automatic recovery system |
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| GR01 | Patent grant |