CN208727507U - Pot-type equipment for glyphosate formulation production - Google Patents
Pot-type equipment for glyphosate formulation production Download PDFInfo
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- CN208727507U CN208727507U CN201821395695.8U CN201821395695U CN208727507U CN 208727507 U CN208727507 U CN 208727507U CN 201821395695 U CN201821395695 U CN 201821395695U CN 208727507 U CN208727507 U CN 208727507U
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Abstract
The utility model discloses a kind of pot-type equipments for glyphosate formulation production, tank body includes the coppers set gradually from the top down, first reaction kettle, second reaction kettle and third reaction kettle, coppers include straight-through feeding chamber, store feeding chamber and rate controlling feeding chamber, the center of tank body is provided with condensation chamber, heating chamber is provided between the lateral wall and inner sidewall of tank body, straight-through feeding chamber, store feeding chamber, rate controlling feeding chamber, first reaction kettle, condensation interlayer and heating interlayer are respectively arranged on the inner sidewall and lateral wall of second reaction kettle and third reaction kettle, heating interlayer is connected with heating chamber, condensation interlayer is connected with condensation chamber；Condensation interlayer is provided on the inner wall of lower reaction chamber in third reaction kettle, roof and bottom plate, condensation interlayer is connected with condensation channel.Pot-type equipment provided by the utility model for glyphosate formulation production reduces energy loss convenient for the charging and temperature control to each reaction process.
Description
Technical field
The utility model relates to pesticide production technology fields, more particularly to a kind of for the canned of glyphosate formulation production
Equipment.
Background technique
Glyphosate is a kind of non-selective, noresidue steriland herbicide, highly effective to prennical root weeds, is used extensively
In rubber, mulberry, tea, orchard and sugarcane field.It is main to inhibit the intracorporal enolpyruvyl shikimene phosphate synthase of plant, to press down
Conversion of the shikimene processed to phenylalanine, tyrosine and tryptophan makes protein synthesis be interfered, leads to Plant death.
The synthesis route of glyphosate mainly has a glycine method and two kinds of iminodiacetic acid (salt) acid system, glycine method mainly with
Glycine, which is that raw material is reacted, obtains glyphosate, and iminodiacetic acid (salt) acid system is also known as IDA method, it is first anti-with IDA and formaldehyde, phosphorous acid
Double sweet phosphorus (PMIDA) should be obtained, then PMIDA is aoxidized to obtain glyphosate, whether producing glyphosate by using glycine preparation, still
Iminodiacetic acid (salt) acid system produces glyphosate formulation, is required to plurality of raw materials, carrying out multiple chemical reaction processes can be made
Glyphosate formulation is that corresponding addition conveys corresponding chemistry when being chemically reacted accordingly, then manually in the prior art
Raw material, and temperature required for each chemical reaction is different, and multiple condensers and heater, each condenser are arranged in the prior art
It is arranged in a one-to-one correspondence to realize the control to each chemical reaction process temperature with heater and each chemical reaction equipment, so
Increase equipment cost and maintenance cost, also increases energy loss, while during producing glyphosate formulation, needing to reaction
Object is crystallized, using long the time required to normal temperature circulation water decrease temperature crystalline, crystallization effect is poor in traditional crystallization processes.
Utility model content
The purpose of the utility model is to provide a kind of pot-type equipments for glyphosate formulation production, to solve the prior art
In shortcoming.
To achieve the goals above, the utility model provides the following technical solutions:
A kind of pot-type equipment for glyphosate formulation production, including tank body, the tank body include successively setting from the top down
Coppers, the first reaction kettle, the second reaction kettle and the third reaction kettle set, first reaction kettle, the second reaction kettle and third
Inlet port and outlet port are provided on reaction kettle, the coppers include straight-through feeding chamber, storage feeding chamber and rate controlling charging
Storehouse, one of them is connected the straight-through feeding chamber with first reaction kettle, the second reaction kettle and third reaction kettle, the storage
It deposits feeding chamber and the rate controlling feeding chamber includes storage chamber and tapping channel, be arranged on the tapping channel of the rate controlling feeding chamber
There is discharging speed adjuster, one of them is connected the tapping channel with first reaction kettle, the second reaction kettle and third reaction kettle
It is logical；It further include condensation chamber and heating chamber, the condensation chamber is located at the center of the tank body, and the heating chamber is located at the tank
Between the lateral wall and inner sidewall of body, be provided with heating mechanism in the heating chamber, the straight-through feeding chamber, storage feeding chamber,
Rate controlling feeding chamber, the first reaction kettle, the second reaction kettle and third reaction kettle inner sidewall and lateral wall on be respectively arranged with condensation
Interlayer and heating interlayer are provided with heating gate on the heating interlayer, and the heating gate is connected with the heating chamber, described cold
It is provided with condensate port on solidifying interlayer, the condensate port is connected with the condensation chamber；Separation is provided in the third reaction kettle
The third reaction kettle is separated to form upper reaction chamber and lower reaction chamber, the inner wall of the lower reaction chamber, top by plate, the demarcation plate
It is provided with the condensation interlayer on wall and bottom plate, is provided with inlet on the condensation interlayer, is provided in the condensation chamber
Condensation channel, the condensation channel are connected with the inlet.
The pot-type equipment of above-mentioned glyphosate formulation production is provided with lime set import and condensate outlet on the condensation chamber,
The lime set import is arranged in the bottom of the tank body, and the condensate outlet is arranged in the top of the tank body, the lime set into
The first condenser is provided between mouth and condensate outlet.
The pot-type equipment of above-mentioned glyphosate formulation production, further includes the second condenser, second condenser with it is described
Condensation channel is connected, and the cooling medium in first condenser and the second condenser is different.
The pot-type equipment of above-mentioned glyphosate formulation production, second reaction kettle by partition be separated into upper reaction kettle with
Lower reaction kettle, is provided with the heating interlayer on the outer wall of the lower reaction kettle, roof and bottom wall, on the heating interlayer
It is provided with the heating gate, the heating gate is connected with the heating chamber.
The pot-type equipment of above-mentioned glyphosate formulation production is provided with out vapour on the upper reaction kettle and lower reaction kettle
Mouthful, reclaimer is provided on the venthole.
The pot-type equipment of above-mentioned glyphosate formulation production, first reaction kettle, the second reaction kettle and third reaction kettle
On be provided at least one dosing mouth.
In the above-mentioned technical solutions, the pot-type equipment of glyphosate formulation provided by the utility model production, tank body include from
Upper down-set coppers, the first reaction kettle, the second reaction kettle and third reaction kettle, the feeding of corresponding glyphosate production and not
With chemical reaction process, coppers include straight-through feeding chamber, storage feeding chamber and rate controlling feeding chamber, by straight-through feeding chamber,
Storage feeding chamber and rate controlling feeding chamber, which can meet, adds different raw materials in the different stages of reaction, and can be conveyed to raw material
The speed of raw material is controlled, and tank body center is provided with condensation chamber, is provided between the lateral wall and inner sidewall of tank body
Heating chamber leads directly to the interior of feeding chamber, storage feeding chamber, rate controlling feeding chamber, the first reaction kettle, the second reaction kettle and third reaction kettle
Condensation interlayer and heating interlayer are respectively arranged on side wall and lateral wall, each interlayer that condenses is connected with condensation chamber, each heating folder
Layer is connected with heating chamber, is able to carry out temperature to each feeding chamber and reaction kettle by a condensation chamber and heating chamber and adjusts,
Multiple heaters and condenser are avoided the need for, the expense of equipment cost and maintenance is reduced, reduces energy loss, while demarcation plate will
The third reaction kettle is separated to form reaction chamber and lower reaction chamber, is all provided on the inner wall of the lower reaction chamber, roof and bottom plate
It is equipped with the condensation interlayer, condensation interlayer is connected with the condensation channel in condensation chamber, drops by upper reaction chamber and lower reaction chamber
The difference of temp effect and cooling effect increases the effect and efficiency of crystallization, it can be achieved that segmented crystallisation by cooling.
Detailed description of the invention
In order to illustrate the technical solutions in the embodiments of the present application or in the prior art more clearly, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only to record in the utility model
Some embodiments be also possible to obtain other drawings based on these drawings for those of ordinary skill in the art.
Fig. 1 is the structural representation for the pot-type equipment for glyphosate formulation production that a kind of embodiment of the utility model provides
Figure；
Fig. 2 is the plan structure for the pot-type equipment for glyphosate formulation production that a kind of embodiment of the utility model provides
Figure.
Description of symbols:
1, tank body；1.1, feed inlet；1.2, discharge port；1.3, interlayer is condensed；1.4, heating interlayer；2, coppers；2.1,
Straight-through feeding chamber；2.2, feeding chamber is stored；2.3, rate controlling feeding chamber；2.4, storage chamber；2.5, tapping channel；2.6, discharge rate controlling
Device；3, the first reaction kettle；4, the second reaction kettle；4.1, upper reaction kettle；4.2, lower reaction kettle；5, third reaction kettle；5.1, upper anti-
Answer room；5.2, lower reaction chamber；6, condensation chamber；6.1, condensation channel；6.2, lime set import；6.3, condensate outlet；6.4, first is cold
Condenser；6.5, the second condenser；6.6, condensate port；7, heating chamber；7.1, heating mechanism；7.2, heating gate.
Specific embodiment
In order to make those skilled in the art more fully understand the technical solution of the utility model, below in conjunction with attached drawing pair
The utility model is further detailed.
As shown in Figs. 1-2, a kind of pot-type equipment for glyphosate formulation production provided by the embodiment of the utility model, packet
Tank body 1 is included, tank body 1 includes coppers 2, the first reaction kettle 3, the second reaction kettle 4 and the third reaction kettle 5 being arranged from the top down,
Feed inlet 1.1 and discharge port 1.2 are provided on first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5, coppers 2 wrap
Straight-through feeding chamber 2.1, storage feeding chamber 2.2 and rate controlling feeding chamber 2.3 are included, feeding chamber 2.1 and the first reaction kettle 3, second are led directly to
One of them is connected for reaction kettle 4 and third reaction kettle 5, and storing feeding chamber 2.2 and rate controlling feeding chamber 2.3 includes storage chamber
2.4 and tapping channel 2.5, discharging speed adjuster 2.6, tapping channel 2.5 are provided on the tapping channel 2.5 of rate controlling feeding chamber 2.3
One of them is connected with the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5；It further include condensation chamber 6 and heating chamber 7,
Condensation chamber 6 is located at the center of tank body 1, and heating chamber 7 is located between the lateral wall and inner sidewall of tank body 1, setting in heating chamber 7
There is heating mechanism 7.1, leads directly to feeding chamber 2.1, storage feeding chamber 2.2, rate controlling feeding chamber 2.3, the reaction of the first reaction kettle 3, second
Condensation interlayer 1.3 and heating interlayer 1.4, heating interlayer are respectively arranged on the inner sidewall and lateral wall of kettle 4 and third reaction kettle 5
Heating gate 7.2 is provided on 1.4, heating gate 7.2 is connected with heating chamber 7, condenses and is provided with condensate port 6.6 on interlayer 1.3, cold
Solidifying mouth 6.6 is connected with condensation chamber 6；Demarcation plate is provided in third reaction kettle 5, third reaction kettle 5 is separated to form by demarcation plate
Upper reaction chamber 5.1 and lower reaction chamber 5.2 are provided with condensation interlayer 1.3 on the inner wall of lower reaction chamber 5.2, roof and bottom plate, cold
It is provided with inlet on solidifying interlayer 1.3, condensation channel 6.1 is provided in condensation chamber 6, condensation channel 6.1 is connected with inlet.
Specifically, coppers 2, the first reaction kettle 3, the second reaction kettle 4 and are disposed with inside tank body 1 from the top down
Three reaction kettles 5, coppers 2 are used to carry out conveying material to the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5, feed
Kettle 2 includes straight-through feeding chamber 2.1, storage feeding chamber 2.2 and rate controlling feeding chamber 2.3, leads directly to feeding chamber 2.1, storage feeding chamber 2.2
It can be one with rate controlling feeding chamber 2.3, be also possible to two or more, straight-through feeding chamber 2.1, storage feeding chamber 2.2 and control
Fast feeding chamber 2.3 leads directly to feeding chamber 2.1 for directly to the first reaction kettle 3, the second reaction kettle 4 and the along the circumferential setting of tank body 1
Material is added in three reaction kettles 5, is for general on and carries out reaction forward reaction kettle transferring raw material, straight-through feeding chamber 2.1 can lead to
It crosses tapping channel 2.5 and material is added to the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5, others can also be passed through
Structure feeds, and stores feeding chamber 2.2 and rate controlling feeding chamber 2.3 includes including storage chamber 2.4 and tapping channel 2.5, storage
Chamber 2.4 is deposited for storing to raw material, tapping channel 2.5 is connected with storage chamber 2.4, can be to each by tapping channel 2.5
Reaction kettle feeds, and stores feeding chamber 2.2 and rate controlling feeding chamber 2.3 is generally used for during the reaction to corresponding reaction kettle
Adding raw materials are provided with discharging speed adjuster 2.6 on the tapping channel 2.5 of rate controlling feeding chamber 2.3, it is slow so to can be realized raw material
Material continuously is conveyed into each reaction kettle, opening mechanism is provided on the tapping channel 2.5 of storage feeding chamber 2.2, passes through
Opening opening mechanism can be realized as the conveying and stopping of raw material, while in straight-through feeding chamber 2.1, storage feeding chamber 2.2 and control
It is provided with meter in fast feeding chamber 2.3, the quality of transferring raw material can be measured by meter, so passes through straight-through charging
Storehouse 2.1, storage feeding chamber 2.2 and rate controlling feeding chamber 2.3, which can meet, adds different raw materials in the different stages of reaction, and can be right
Raw material obtains adding speed and is controlled.First reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 successively separate from the top down
Setting, the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5, which correspond to, carries out different reaction process, in the present embodiment
A reaction process can be only carried out in first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5, can also be carried out multiple anti-
Process is answered, the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 can also be separated into multiple reaction chambers to carry out
Multiple and different reaction process, can also be according to the difference of synthesis material, and corresponding reaction process is different, increases the number of reaction kettle
Amount, for example be provided with the first reaction kettle 3, the second reaction kettle 4, third reaction kettle 5, the 4th reaction kettle etc., for example, with glycine,
When dimethylphosphite is that raw material carries out synthesizing glyphosate production, need to carry out depolymerization reaction, condensation reaction and esterification, no
Same reaction can be corresponded to be carried out in different reaction kettles；Such as when with methanol, triethylamine, paraformaldehyde, glycine, phosphorous acid
When dimethyl ester and hydrochloric acid are raw material, need to carry out depolymerization, addition, crystallization, synthesis, mixing, filtering, oxydrolysis and oxidation dephosphorization
Deng reaction, the glyphosate prepared by.Feed inlet is provided on first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5
1.1 and discharge port 1.2, the feed inlet 1.1 of the first reaction kettle 3 be connected with coppers 2, the feed inlet 1.1 of the second reaction kettle 4 with
The discharge port 1.2 and coppers 2 of first reaction kettle 3 are connected, the feed inlet 1.1 of third reaction kettle 5 and the second reaction kettle 4
Discharge port 1.2 and coppers 2 are connected, also settable between the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5
There is connecting tube, while it is good on the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 to be also provided with pressure regulating mechanism
PH value regulating mechanism.
In the present embodiment, condensation chamber 6 and heating chamber 7 are provided on tank body 1, it can be to straight by condensation chamber 6 and heating chamber 7
Logical feeding chamber 2.1, storage feeding chamber 2.2, rate controlling feeding chamber 2.3, the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5
Temperature be adjusted, the center of tank body 1 is arranged in condensation chamber 6, cooling medium is provided in condensation chamber 6, in tank body 1
Outside is provided with condenser, and condenser is connected to drive the flowing and replacement of cooling medium with condensation chamber 6, and heating chamber 7 is located at
Between the lateral wall and inner sidewall of tank body 1, be provided with heating mechanism 7.1 in heating chamber 7, heating mechanism 7.1 can be heater,
Heating tube or other structures lead directly to feeding chamber 2.1, storage feeding chamber 2.2, rate controlling feeding chamber 2.3, the first reaction kettle 3, second
The inner sidewall of reaction kettle 4 and third reaction kettle 5 is provided with condensation interlayer 1.3, is worth being proximate to 6 side of condensation chamber on inner sidewall
Side wall, condensation interlayer 1.3 can be fitted with condensation chamber 6, can also be spaced a distance, each to condense interlayer 1.3
On be provided with condensate port 6.6, condensate port 6.6 is connected with condensation chamber 6, by condensate port 6.6 can to condensation interlayer 1.3 in input
With output cooling medium, reaction kettle and feeding chamber can be cooled down by condensing interlayer 1.3, lead directly to feeding chamber 2.1, storage
The lateral wall for depositing feeding chamber 2.2, rate controlling feeding chamber 2.3, the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 is respectively provided with
There is heating interlayer 1.4, lateral wall is worth being proximate to the side wall of 7 side of heating chamber, it is provided with heating gate 7.2 on heating interlayer 1.4,
Heating gate 7.2 is connected with heating chamber 7, can be realized by heating gate 7.2 and be heated to heating interlayer 1.4, thus realization pair
Reaction kettle and feeding chamber are heated, while being correspondingly arranged on opening mechanism on each condensate port 6.6 and heating gate 7.2, are led to
Crossing opening mechanism can control the opening of condensate port 6.6 and heating gate 7.2, in straight-through feeding chamber 2.1, storage feeding chamber 2.2, rate controlling
It may be provided with temperature meter in feeding chamber 2.3, the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 and carry out temperature
Measurement is so able to carry out temperature to each feeding chamber and reaction kettle by a condensation chamber 6 and heating chamber 7 and adjusts, avoids needing
Want multiple heaters and condenser.
In the present embodiment, demarcation plate is provided in third reaction kettle 5, demarcation plate traverses inside third reaction kettle 5, by
Three reaction kettles 5 are separated to form reaction chamber 5.1 and lower reaction chamber 5.2, and the inner sidewall and lateral wall of upper reaction chamber 5.1 are respectively set
There is condensation interlayer 1.3, inner wall, roof and the bottom plate of lower reaction chamber 5.2 are provided with condensation interlayer 1.3, so lower reaction chamber 5.2
One lateral wall is heating interlayer 1.4, and excess-three side wall is provided with condensation interlayer 1.3, increases the speed of cooling, and lower anti-
Answer and be provided with inlet on the condensation interlayer 1.3 of room 5.2, be provided with condensation channel 6.1 in condensation chamber 6, condensation channel 6.1 with into
Liquid mouth is connected, and so realizes and conveys cooling medium in the condensation interlayer 1.3 of downward reaction chamber 5.2, what condensation channel 6.1 conveyed
The cooling medium of cooling medium and condensation chamber 6 may be the same or different, and in the production process for carrying out glyphosate, need
It is crystallized, by upper reaction chamber 5.1 and lower 5.2 cooling effect of reaction chamber and the difference of cooling effect, it can be achieved that segmented is cold
But it crystallizes, increases the effect and efficiency of crystallization.
The pot-type equipment of glyphosate formulation production provided by the embodiment of the utility model, tank body 1 include being arranged from the top down
Coppers 2, the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5, the feeding and different changes of corresponding glyphosate production
Reaction process is learned, coppers 2 include straight-through feeding chamber 2.1, storage feeding chamber 2.2 and rate controlling feeding chamber 2.3, pass through straight-through charging
Storehouse 2.1, storage feeding chamber 2.2 and rate controlling feeding chamber 2.3, which can meet, adds different raw materials in the different stages of reaction, and can be right
The speed that raw material obtains transferring raw material is controlled, and 1 center of tank body is provided with condensation chamber 6, in the lateral wall of tank body 1 and interior
Heating chamber 7 is provided between side wall, lead directly to feeding chamber 2.1, storage feeding chamber 2.2, rate controlling feeding chamber 2.3, the first reaction kettle 3,
Condensation interlayer 1.3 and heating interlayer 1.4 are respectively arranged on the inner sidewall and lateral wall of second reaction kettle 4 and third reaction kettle 5,
Each condensation interlayer 1.3 is connected with condensation chamber 6, and each heating interlayer 1.4 is connected with heating chamber 7, by a condensation chamber 6 and adds
Hot chamber 7 is able to carry out temperature to each feeding chamber and reaction kettle and adjusts, and avoids the need for multiple heaters and condenser, reduces equipment
The expense of cost and maintenance reduces energy loss, while third reaction kettle 5 is separated to form upper reaction chamber 5.1 under by demarcation plate
Reaction chamber 5.2 is provided with condensation interlayer 1.3, condensation interlayer 1.3 and condensation on the inner wall of lower reaction chamber 5.2, roof and bottom plate
Condensation channel 6.1 in chamber 6 is connected, not by upper reaction chamber 5.1 and lower 5.2 cooling effect of reaction chamber and cooling effect
With, it can be achieved that segmented crystallisation by cooling, increases the effect and efficiency of crystallization.
In the present embodiment, it is preferred that be provided with lime set import 6.2 and condensate outlet 6.3, lime set import 6.2 on condensation chamber 6
The bottom of tank body 1 is set, and condensate outlet 6.3 is arranged in the top of tank body 1, sets between lime set import 6.2 and condensate outlet 6.3
It is equipped with the first condenser 6.4；It is connected with condensation chamber 6, it can be achieved that straight-through feeding chamber 2.1, storage by the first condenser 6.4
Feeding chamber 2.2, rate controlling feeding chamber 2.3, the first reaction kettle 3, the second reaction kettle 4 and the progress cooling down of third reaction kettle 5, and by
In the conveying direction of the flow direction of cooling medium and raw material and reactant on the contrary, increasing the effect of condensation.
In the present embodiment, it is preferred that further include the second condenser 6.5, the second condenser 6.5 is connected with condensation channel 6.1
Logical, the first condenser 6.4 is different with the cooling medium in the second condenser 6.5；Pass through the second condenser 6.5 and condensation channel
6.1 are connected, and condensation channel 6.1 is connected with the condensation interlayer 1.3 of lower reaction chamber 5.2, can be realized pair by the second condenser 6.5
Lower reaction is so that fast cooling is cooling, so not by upper reaction chamber 5.1 and lower 5.2 cooling effect of reaction chamber and cooling effect
With, it can be achieved that segmented crystallisation by cooling, increases the effect and efficiency of crystallization.
In the present embodiment, it is preferred that the second reaction kettle 4 is separated into upper reaction kettle 4.1 and lower reaction kettle 4.2 by partition,
It is provided with heating interlayer 1.4 on the outer wall of lower reaction kettle 4.2, roof and bottom wall, is provided with heating gate on heating interlayer 1.4
7.2, heating gate 7.2 is connected with heating chamber 7；Outer wall, roof and the bottom wall of lower reaction kettle 4.2 are provided with heating interlayer 1.4,
So lower 5.2 1 inner sidewalls of reaction chamber are condensation interlayer 1.3, and excess-three side wall is provided with heating interlayer 1.4, and respectively adds
The heating gate 7.2 of hot interlayer 1.4 is connected with heating chamber 7, so that the heating speed of lower reaction kettle 4.2 and heating effect increase
Add, carry out chemical reaction process in, lower reaction kettle 4.2 can be used for quickly heat and heating carry out using.
In the present embodiment, it is preferred that be provided with venthole on upper reaction kettle 4.1 and lower reaction kettle 4.2, set on venthole
It is equipped with reclaimer；It can carry out the operation such as distilling in upper reaction kettle 4.1 and lower reaction kettle 4.2, the steam for distilling generation can lead to
Venthole output is crossed, the reclaimer of gas outlet can be recycled and be handled to steam.
In the present embodiment, it is preferred that be provided at least on the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5
One dosing mouth；It can be added into the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 required for reaction by dosing mouth
Raw material, catalyst etc., medicine can also be added to the first reaction kettle 3, the second reaction kettle 4 and third reaction kettle 5 by dosing mouth
Agent is to adjust the pH value in reaction kettle.
It is above that certain exemplary embodiments of the utility model are only described by way of explanation, undoubtedly, for
Those skilled in the art can be with a variety of different without departing from the spirit and scope of the utility model
Mode is modified described embodiment.Therefore, above-mentioned attached drawing and description are regarded as illustrative in nature, and should not be construed as
Limitation to the utility model claims protection scope.
Claims (5)
1. a kind of pot-type equipment for glyphosate formulation production, including tank body, which is characterized in that the tank body include on to
Under the coppers, the first reaction kettle, the second reaction kettle and the third reaction kettle that set gradually, first reaction kettle, the second reaction
Be provided with inlet port and outlet port on kettle and third reaction kettle, the coppers include straight-through feeding chamber, storage feeding chamber and
Rate controlling feeding chamber, the straight-through feeding chamber are connected with one in first reaction kettle, the second reaction kettle and third reaction kettle
Logical, the storage feeding chamber and the rate controlling feeding chamber include storage chamber and tapping channel, the discharging of the rate controlling feeding chamber
Be provided with discharging speed adjuster on channel, the tapping channel and first reaction kettle, the second reaction kettle and third reaction kettle its
In one be connected；
It further include condensation chamber and heating chamber, the condensation chamber is located at the center of the tank body, and the heating chamber is located at described
Between the lateral wall and inner sidewall of tank body, heating mechanism, the straight-through feeding chamber, storage charging are provided in the heating chamber
Storehouse, rate controlling feeding chamber, the first reaction kettle, the second reaction kettle and third reaction kettle inner sidewall and lateral wall on be respectively arranged with it is cold
Interlayer and heating interlayer are coagulated, is provided with heating gate on the heating interlayer, the heating gate is connected with the heating chamber, described
It is provided with condensate port on condensation interlayer, the condensate port is connected with the condensation chamber；
Be provided with demarcation plate in the third reaction kettle, the demarcation plate by the third reaction kettle be separated to form upper reaction chamber and
Lower reaction chamber is provided with the condensation interlayer on the inner wall of the lower reaction chamber, roof and bottom plate, sets on the condensation interlayer
It is equipped with inlet, condensation channel is provided in the condensation chamber, the condensation channel is connected with the inlet.
2. the pot-type equipment according to claim 1 for glyphosate formulation production, which is characterized in that on the condensation chamber
It is provided with lime set import and condensate outlet, the bottom of the tank body is arranged in the lime set import, and the condensate outlet setting exists
The top of the tank body is provided with the first condenser between the lime set import and condensate outlet.
3. the pot-type equipment according to claim 2 for glyphosate formulation production, which is characterized in that further include second cold
Condenser, second condenser are connected with the condensation channel, and the condensation in first condenser and the second condenser is situated between
Matter is different.
4. the pot-type equipment according to claim 1 for glyphosate formulation production, which is characterized in that second reaction
Kettle is separated into upper reaction kettle and lower reaction kettle by partition, is respectively provided on the outer wall of the lower reaction kettle, roof and bottom wall
Heating interlayer is stated, the heating gate is provided on the heating interlayer, the heating gate is connected with the heating chamber.
5. the pot-type equipment according to claim 4 for glyphosate formulation production, which is characterized in that the upper reaction kettle
It is provided with venthole on lower reaction kettle, is provided with reclaimer on the venthole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821395695.8U CN208727507U (en) | 2018-08-28 | 2018-08-28 | Pot-type equipment for glyphosate formulation production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821395695.8U CN208727507U (en) | 2018-08-28 | 2018-08-28 | Pot-type equipment for glyphosate formulation production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208727507U true CN208727507U (en) | 2019-04-12 |
Family
ID=66031601
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821395695.8U Expired - Fee Related CN208727507U (en) | 2018-08-28 | 2018-08-28 | Pot-type equipment for glyphosate formulation production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208727507U (en) |
-
2018
- 2018-08-28 CN CN201821395695.8U patent/CN208727507U/en not_active Expired - Fee Related
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Granted publication date: 20190412 Termination date: 20190828 |