CN204607896U - A kind of guanidoacetic acid production system - Google Patents
A kind of guanidoacetic acid production system Download PDFInfo
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- CN204607896U CN204607896U CN201520227082.3U CN201520227082U CN204607896U CN 204607896 U CN204607896 U CN 204607896U CN 201520227082 U CN201520227082 U CN 201520227082U CN 204607896 U CN204607896 U CN 204607896U
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Abstract
The utility model relates to a kind of guanidoacetic acid production system, comprise reactor, stir electric motor, test tank, hopper and induced draft fan, described reactor comprises venting port, discharge port and opening for feed, described opening for feed connects described hopper, described hopper comprises connection section, feeder and branch, also be provided with plate bottom described feeder, described branch part between described feeder and connection section, and is communicated with feeder with described connection section; Described fan inlet is connected to the branch of described hopper by pipeline, and described stirring electric motor is arranged on the top of described reactor and is connected with described reactor interior stirring device, and described test tank is connected with described reactor by pipeline.The utility model guanidoacetic acid production system, by increasing branch on hopper, at opening for feed, place is connected to induced draft fan, and by arranging induced draft fan, Dyhard RU 100 in reactor is decomposed the gas produced and extracts out, and enter absorb in water after be recycled.
Description
Technical field
The utility model relates to guanidoacetic acid Preparation equipment, particularly a kind of guanidoacetic acid production system.
Background technology
Feed additive guanidoacetic acid is by glycine and cyanamide Reactive Synthesis under 70 ~ 100 degree and pH value are the condition of 8 ~ 10, cyanamide is easily polymerized generation Dyhard RU 100 under this condition, make production declining, and at the end of reaction, in product, more or less have the Dyhard RU 100 that polymerization generates, product purity is reduced, and Dyhard RU 100 belongs to low toxicity harmful chemical, has a strong impact on feed safety, therefore, must strictly control during suitability for industrialized production.
Utility model content
In view of this, the purpose of this utility model is to provide a kind of guanidoacetic acid production system, to solve technical problem of the prior art.
The guanidoacetic acid production system that the utility model provides, comprise reactor, stir electric motor, test tank, hopper and induced draft fan, described reactor comprises venting port, discharge port and opening for feed, described opening for feed connects described hopper, described hopper comprises connection section, feeder and branch, also be provided with plate bottom described feeder, described branch part between described feeder and connection section, and is communicated with feeder with described connection section; Described fan inlet is connected to the branch of described hopper by pipeline, and described stirring electric motor is arranged on the top of described reactor and is connected with described reactor interior stirring device, and described test tank is connected with described reactor by pipeline.
Preferably, described reactor is provided with bleeding point.
Preferably, described induced draft fan is connected to described bleeding point by pipeline.
The guanidoacetic acid production system that the utility model provides, by increasing branch on hopper, at opening for feed, place is connected to induced draft fan, and by arranging induced draft fan, by in reactor Dyhard RU 100 decompose produce gas extract out, and enter absorb in water after be recycled.
Accompanying drawing explanation
By referring to the description of accompanying drawing to the utility model embodiment, above-mentioned and other objects of the present utility model, feature and advantage will be more clear, in the accompanying drawings:
Fig. 1 is the utility model guanidoacetic acid production system schematic diagram;
Fig. 2 is hopper schematic diagram.
Embodiment
Hereinafter with reference to accompanying drawing, various embodiment of the present utility model is described in more detail.In various figures, identical element adopts same or similar Reference numeral to represent.For the sake of clarity, the various piece in accompanying drawing is not drawn in proportion.
As shown in Figure 1, the utility model guanidoacetic acid production system comprises reactor 1, stirs electric motor 2, test tank 3, hopper 4 induced draft fan 5, described reactor 1 comprises venting port 11, opening for feed 12 and discharge port 13, described venting port 11 is for discharging the gas in described reactor 1, described opening for feed 12 connects described hopper 4, for throwing in reaction mass in described reactor 1; Described discharge port 13 is released for material reaction in described reactor 1 generated.As shown in Figure 2, described hopper 4 comprises connection section 41, feeder 42 and branch 43, also be provided with plate 44 bottom described feeder 42, described branch 43 between described feeder 42 and connection section 41, and is communicated with feeder 42 with described connection section 41.Described stirring electric motor 2 is arranged on described reactor 1 top, and is connected with the whipping appts in described reactor 1, drives whipping appts to stir material in described reactor 1; Described test tank 3 to be connected with described reactor 1 by pipeline and pipeline to be provided with valve 31, for dripping liquid material, as cyanamide in described reactor 1; The blast inlet of described induced draft fan 5 is connected to the branch 43 of described hopper 4 by pipeline, and pipeline is provided with air inducing valve 51, decompose for the Dyhard RU 100 that will be entrained in described reactor 1 in water vapour the gas produced to extract out, and the gas of extraction is passed into tank absorb.
Preferably, bleeding point (not shown) also can be set on described reactor 1 for connecting described induced draft fan 5.
The using method of the utility model guanidoacetic acid production system is:
Open the plate 44 of described hopper 4, close described air inducing valve 51 simultaneously, by material by described opening for feed 12 render to feed intake in described reactor 1 after described plate 44 is advanced in described hopper 4, make it close described opening for feed 12; Open described stirring electric motor 2 to stir the material in described reactor 1, carrying out heating to described reactor 1 makes its internal temperature reach 70 ~ 100 degree, meanwhile, open described valve 31 liquid material in described test tank 3 is dripped in described reactor 1.After in described reactor 1, material reaction terminates, open described air inducing valve 51, start described induced draft fan 5, and keep temperature in described reactor 1 70 ~ 100 degree of for some time, preferably, temperature-time is kept to be one hour, the Dyhard RU 100 decomposes now generated in material reaction process in described reactor 1, degradation production is absorbed by described induced draft fan 5 suction tank, and recoverable.
Preferably, when described reactor 1 is provided with bleeding point, described induced draft fan 5 is connected to described bleeding point by pipeline.
Last it is noted that obviously, above-described embodiment is only for the utility model example is clearly described, and the restriction not to embodiment.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And thus the apparent change of amplifying out or variation be still among protection domain of the present utility model.
Claims (3)
1. a guanidoacetic acid production system, it is characterized in that, comprise reactor, stir electric motor, test tank, hopper and induced draft fan, described reactor comprises venting port, discharge port and opening for feed, described opening for feed connects described hopper, and described hopper comprises connection section, feeder and branch, is also provided with plate bottom described feeder, described branch part between described feeder and connection section, and is communicated with feeder with described connection section; Described fan inlet is connected to the branch of described hopper by pipeline, and described stirring electric motor is arranged on the top of described reactor and is connected with described reactor interior stirring device, and described test tank is connected with described reactor by pipeline.
2. guanidoacetic acid production system according to claim 1, is characterized in that, described reactor is provided with bleeding point.
3. guanidoacetic acid production system according to claim 2, is characterized in that, described induced draft fan is connected to described bleeding point by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520227082.3U CN204607896U (en) | 2015-04-15 | 2015-04-15 | A kind of guanidoacetic acid production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520227082.3U CN204607896U (en) | 2015-04-15 | 2015-04-15 | A kind of guanidoacetic acid production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204607896U true CN204607896U (en) | 2015-09-02 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520227082.3U Active CN204607896U (en) | 2015-04-15 | 2015-04-15 | A kind of guanidoacetic acid production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204607896U (en) |
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2015
- 2015-04-15 CN CN201520227082.3U patent/CN204607896U/en active Active
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| GR01 | Patent grant |