CN206082468U - Apparatus for producing of polyamide polyamine - Google Patents

Apparatus for producing of polyamide polyamine Download PDF

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Publication number
CN206082468U
CN206082468U CN201621116877.8U CN201621116877U CN206082468U CN 206082468 U CN206082468 U CN 206082468U CN 201621116877 U CN201621116877 U CN 201621116877U CN 206082468 U CN206082468 U CN 206082468U
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CN
China
Prior art keywords
kettle
process units
polyamide polyamines
treatment system
collection system
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Expired - Fee Related
Application number
CN201621116877.8U
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Chinese (zh)
Inventor
余建新
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Special Industry Co Ltd Of Hangzhou Pepsi
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Special Industry Co Ltd Of Hangzhou Pepsi
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Priority to CN201621116877.8U priority Critical patent/CN206082468U/en
Application granted granted Critical
Publication of CN206082468U publication Critical patent/CN206082468U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to an apparatus for producing of polyamide polyamine, including reation kettle, reation kettle is including the cauldron body, agitator, and reation kettle still is provided with the heating device who is used for heating the cauldron body, apparatus for producing of polyamide polyamine still including be arranged in the cooling and collect the produced vapor of production condensate collection system, be arranged in purifying the waste gas treatment system of the produced waste gas of production, condensate collection system and the switch -on of the cauldron body, waste gas treatment system and two condensate collection system, the cauldron bodies in at least one switch -on. The utility model discloses can promote polyamide polyamine midbody product quality, improve production efficiency, the exhaust emission of lowering system accords with current energy saving and emission reduction's trend.

Description

A kind of process units of polyamide polyamines
Technical field
This utility model is related to a kind of process units, and in particular to a kind of process units of polyamide polyamines.
Background technology
Polyamide-Polyamsne-Epichlorohydrin resin(Abbreviation PAE resin)It is a kind of water-soluble cationic thermosetting resin, Because its have it is nontoxic, pollute little, practical and convenient, the advantages of have resident, drainage concurrently, being widely used as wet strength agent by paper mill makes With;Some papermaking chemical product factories, can improve to PAE resin again, the emulsifier component as sizing agent.
As the intermediate of production PAE resin, polyamide polyamines, the stable type of its production technology, efficiency whether, meeting The quality of PAE resin product is directly affected, so as to affect using effect.Generally the production process of polyamide polyamines, is related to solid Reaction between the binary acid of state and the polyethylene polyamine of liquid, and both materials at normal temperatures will not mutually phased soln and difficulty To spread out, binary acid is in coherent condition in polyethylene polyamine, stirs very difficult, and these can all cause unfavorable to production Affect.
To solve the above problems, people can generally adopt two kinds of methods:First, the polyethylene polyamine of liquid is heated to first Uniform temperature and then binary acid is added in batches;2nd, by solid, liquid material all disposable input kettle, kettle cover is covered, After all melting Deng intensification solid material, stirring is then turned on.The first method, needs to be repeatedly opened kettle cover and adds materials, its mistake The volatilization loss of the polyethylene polyamine in reactor cannot be avoided in journey and because ammonia taste gets up to run out of brought environmental problem With occupational health problem.Second method, although loss of material is few, the situation that ammonia taste gas is run out of also improves many.But deposit Solid material melt before, solid-liquid contact is uneven, and the solid material thawing time is long, affect production efficiency the problems such as.
Additionally, in because of polyamide polyamines production process, the environmental issue brought because producing ammonia taste gas also can not be ignored.
The content of the invention
It is to overcome the deficiencies in the prior art to provide one kind to be exclusively used in producing polyamides that this utility model to be solved technical problem The polyamide polyamines process units of amine polyamines.
To solve above technical problem, the technical solution adopted in the utility model is:
A kind of process units of polyamide polyamines, including reactor, reactor includes kettle, stirring for agitating solution Device is mixed, reactor is additionally provided with the heater for heating kettle, particularly, the process units of polyamide polyamines is also included For cooling down and collect the condensation collection system of produced vapor in production, produce for purification in produced waste gas Exhaust treatment system, condensation collection system is connected with kettle, in exhaust treatment system and condensation collection system, kettle two extremely A few connection.
According to a preferred aspect, exhaust treatment system is turned on condensation collection system, kettle.
According to another preferred aspect, exhaust treatment system is only connected with kettle.
Preferably, condensing collection system includes the another of the condenser that connects with the top of kettle of one end and condenser The reception tank of end connection, and tank is received by pipeline and exhaust treatment system connection.
Further, exhaust treatment system includes spray scrubber and centrifugal blower, and spray scrubber passes through the first pipeline Connect with kettle or condensation collection system, spray scrubber is connected by second pipe with the air inlet of centrifugal blower.At waste gas Residual gas in waste gas and condensation collection system that reason system is produced reactor using centrifugal blower is extracted out.
Preferably, one end of the first pipeline is connected to the middle and lower part of spray scrubber, and one end of second pipe is connected to spray Drench the top of scrubbing tower.
Preferably, exhaust treatment system also includes the active carbon adsorber connected with the gas outlet of centrifugal blower, remaining portion After point waste gas adsorbs again in absorbent charcoal adsorber, clean gas Jing exhaust chimney enters air, such design be in order to By the more thorough of waste gas purification.
Preferably, exhaust treatment system also includes the exhaust chimney connected with active carbon adsorber, through purified treatment Gas, finally enters air by exhaust chimney.
Preferably, spray scrubber is made using the material of acid-alkali-corrosive-resisting.Spray washing process is former using acid-base neutralization Reason, i.e., processed alkaline waste gas using dilute sulfuric acid spray liquid.Spray mode takes circulated sprinkling, and in due course and When supplement spray liquid.
Preferably, heater includes the inner coil pipe being arranged on inside kettle and the chuck being arranged on outside kettle, inner disc Pipe and chuck are equipped with the passage of external circulating heat conduction oil.Such design, can be using circulating heat conduction oil from chuck and inner disc Two positions of pipe are heated to the reaction mass in kettle, are heated compared with single chuck, and the efficiency of heating surface is higher;Also, due to Using inner coil pipe, contact with the solid material in kettle more fully, the uneven and band because solid material is heated can be obviously improved The product quality problem for coming.
Due to the utilization of above-mentioned technical proposal, this utility model has compared with prior art following advantages:
The process units of this utility model polyamide polyamines, condensation collection system removes unwanted moisture from kettle, The quality of product is improved, exhaust treatment system will be discharged after produced waste gas purification, and can be made in process of production anti- Answer kettle to be reacted under negative pressure state, be conducive to plus fast response.The device can lift the product of polyamide polyamines intermediate Quality, improve production efficiency, reduce the waste gas discharge of system, meet the trend of current energy-saving and emission-reduction.
Description of the drawings
Fig. 1 is the structural representation of the process units of polyamide polyamines of the present utility model;
Wherein:1st, reactor;10th, kettle;11st, agitator;12nd, inner coil pipe;13rd, chuck;2nd, collection system is condensed;21、 Condenser;22nd, tank is received;3rd, exhaust treatment system;31st, spray scrubber;31a, the first pipeline;31b, second pipe;32nd, from Heart-wind syndrome machine;33rd, active carbon adsorber;34th, exhaust chimney.
Specific embodiment
Come with reference to the accompanying drawings and detailed description to be further elaborated the technical solution of the utility model.
As shown in Fig. 1, a kind of process units of polyamide polyamines of the present utility model, including reactor 1, reactor 1 Kettle 10, agitator 11 are included, reactor 1 is additionally provided with the heater for heating kettle 10, particularly, polyamide The process units of polyamines also includes for cooling down and collects the condensation collection system 2 of vapor produced in production, is used for The exhaust treatment system 3 of produced waste gas in purification production, condensation collection system 2 is connected with kettle 10, exhaust treatment system 3 It is turned on condensation collection system 2, kettle 10 2.Condensation collection system 2 specifically includes one end and connects with the top of kettle 10 The reception tank 22 that logical condenser 21 is connected with the other end of condenser 21.Tank 22 is received by pipeline and exhaust-gas treatment system System 3 is connected.
In this example, exhaust treatment system 3 includes spray scrubber 31, the centrifugal blower 32, activated carbon adsorption being sequentially connected Device 33 and exhaust chimney 34.The middle and lower part of spray scrubber 31 is connected by the first pipeline 31a with kettle 10, receives tank 22 and passes through Pipeline and the first pipeline 31a are connected.The top of spray scrubber 31 is connect by second pipe 31b with the air inlet of centrifugal blower 32 It is logical.The gas outlet connection active carbon adsorber 33 of centrifugal blower 32.Spray scrubber 31 is made using the material of acid-alkali-corrosive-resisting.
In this example, the heater of reactor 1 includes the inner coil pipe 12 being arranged on inside kettle 10 and is arranged on kettle 10 Outside chuck 13, inner coil pipe 12 and chuck 13 are equipped with the passage of external circulating heat conduction oil.
The technique for producing polyamide polyamines using the process units of the present embodiment is exemplified below:
By raw material diethylenetriamine, adipic acid with 1.08:In 1 ratio input reactor, kettle cover is covered, chuck and interior Coil pipe leads to the circulating heat conduction oil that temperature is for 130 ~ 135 DEG C simultaneously(In temperature-rise period, while opening centrifugal blower, vent gas treatment is allowed Device is in running order).After about 50min, material in kettle is observed from visor and is all melted, open stirring, be warmed up to 170 ~ 175 DEG C, 3 ~ 4h of insulation reaction;After reaction terminates, cooling, when temperature in the kettle is dropped to below 110 DEG C, dilute Cheng Gu The polyamide polyamines intermediate water solution of content about 45%.Gained intermediate viscosity be:180 ~ 250 mPa.s, pH value is:9.0 ~ 10.5。
To sum up, using the process units of this utility model polyamide polyamines, condensation collection system by unwanted moisture from Remove in kettle, improve the quality of product, exhaust treatment system will be discharged after produced waste gas purification, in this utility model polyamides In the process units production process of amine polyamines, centrifugal blower can provide certain negative pressure to whole response system, be conducive to Water byproduct is removed in time, so as to add fast response, shortens equilibration time, production efficiency is improve to a certain extent, the device Product quality, the improve production efficiency of polyamide polyamines intermediate can be lifted, the waste gas discharge of system is reduced, is met and is worked as prosthomere The trend that can be reduced discharging.
This utility model is described in detail above, its object is to make the personage's energy for being familiar with this art much of that Solve content of the present utility model and be carried out, protection domain of the present utility model, and this utility model can not be limited with this The above embodiments, all equivalence changes made according to spirit of the present utility model or modification are not limited to, all should be covered Within protection domain of the present utility model.

Claims (10)

1. a kind of process units of polyamide polyamines, including reactor (1), the reactor(1)Include kettle(10), stir Mix device(11), the reactor (1) is additionally provided with for heating the kettle(10)Heater, it is characterised in that:It is described The process units of polyamide polyamines also includes for cooling down and collects the condensation collection system of vapor produced in production (2), for the exhaust treatment system of produced waste gas in purification production(3), the condensation collection system(2)With the kettle (10)Connect, the exhaust treatment system(3)With described condensation collection system(2), the kettle(10)In two at least One connection.
2. the process units of a kind of polyamide polyamines according to claim 1, it is characterised in that:The exhaust treatment system (3)With described condensation collection system(2), the kettle(10)It is turned on.
3. the process units of a kind of polyamide polyamines according to claim 1 and 2, it is characterised in that:The condensation is collected System(2)Including one end and described kettle(10)Top connection condenser(21)With the other end of the condenser The reception tank of portion's connection(22).
4. the process units of a kind of polyamide polyamines according to claim 3, it is characterised in that:The reception tank(22)It is logical Piping and exhaust treatment system(3)Connect.
5. the process units of a kind of polyamide polyamines according to claim 1 and 2, it is characterised in that:The exhaust-gas treatment System(3)Including spray scrubber(31)And centrifugal blower(32), described spray scrubber(31)By the first pipeline(31a) With the kettle(10)Or condensation collection system(2)Connect, described spray scrubber(31)By second pipe(31b)With from Heart-wind syndrome machine(32)Air inlet connect.
6. the process units of a kind of polyamide polyamines according to claim 5, it is characterised in that:First pipeline (31a)One end be connected to described spray scrubber(31)Middle and lower part, the second pipe(31b)One end be connected to spray Drench scrubbing tower(31)Top.
7. the process units of a kind of polyamide polyamines according to claim 6, it is characterised in that:The exhaust treatment system (3)Also include and the centrifugal blower(32) active carbon adsorber of gas outlet connection(33).
8. the process units of a kind of polyamide polyamines according to claim 7, it is characterised in that:The exhaust treatment system (3)Also include and active carbon adsorber(33)The exhaust chimney of connection(34).
9. the process units of a kind of polyamide polyamines according to claim 5, it is characterised in that:The spray scrubber (31)Made using the material of acid-alkali-corrosive-resisting.
10. the process units of a kind of polyamide polyamines according to claim 1 and 2, it is characterised in that:The heater Including being arranged on the kettle(10)Internal inner coil pipe(12)Be arranged on the kettle(10)Outside chuck(13), it is described Inner coil pipe(12)With the chuck(13)It is equipped with the passage of external circulating heat conduction oil.
CN201621116877.8U 2016-10-12 2016-10-12 Apparatus for producing of polyamide polyamine Expired - Fee Related CN206082468U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621116877.8U CN206082468U (en) 2016-10-12 2016-10-12 Apparatus for producing of polyamide polyamine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621116877.8U CN206082468U (en) 2016-10-12 2016-10-12 Apparatus for producing of polyamide polyamine

Publications (1)

Publication Number Publication Date
CN206082468U true CN206082468U (en) 2017-04-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621116877.8U Expired - Fee Related CN206082468U (en) 2016-10-12 2016-10-12 Apparatus for producing of polyamide polyamine

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110773101A (en) * 2019-11-01 2020-02-11 孟庆超 Environment-friendly oil well acidizing fluid preparation facilities

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110773101A (en) * 2019-11-01 2020-02-11 孟庆超 Environment-friendly oil well acidizing fluid preparation facilities

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CF01 Termination of patent right due to non-payment of annual fee
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Granted publication date: 20170412

Termination date: 20171012