CN202688220U - Step-by-step continuous chemical combination device - Google Patents
Step-by-step continuous chemical combination device Download PDFInfo
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- CN202688220U CN202688220U CN 201220336721 CN201220336721U CN202688220U CN 202688220 U CN202688220 U CN 202688220U CN 201220336721 CN201220336721 CN 201220336721 CN 201220336721 U CN201220336721 U CN 201220336721U CN 202688220 U CN202688220 U CN 202688220U
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Abstract
The utility model relates to a step-by-step continuous chemical combination device, and belongs to the field of explosive manufacture. The step-by-step continuous chemical combination device comprises two structurally same material metering devices and three structurally same independent chemical combination devices including a reactor, an ager and a crystallizer, the material metering devices are respectively connected with the reactor through pipelines, the reactor is connected with the ager through a pipeline, the ager is connected with the crystallizer through a pipeline, the mounting position of each material metering device is higher than that of the reactor, the mounting position of the reactor is higher than that of the ager, the mounting position of the ager is higher than that of the crystallizer, and liquid flows among containers by the aid of liquid level difference. The step-by-step continuous chemical combination device has the advantages of novel and simple structure and safety and convenience in use. Production efficiency is improved, product quality can be accurately controlled, product quality uniformity is improved, the number of operators is decreased, working time of the operators in harmful environments is shortened, and practicability is high.
Description
Technical field
The utility model relates to explosive and makes the field, relates to not relate to the continuous combination apparatus of a kind of multiple step format.
Background technology
The medicament that detonates is relatively more dangerous fiery explosive, is mainly used in loading the various ignition and blasting equipment such as detonator, safety fuse.Its friction sensitivity, electrostatic sensitivity, impact sensitivity are all higher, because its this inflammable and explosive property, make it be not easy to long-distance transport, and the usage comparison of the medicament that detonates dispersion, very general, large usage quantity, the also relatively dispersion, general of the production of medicament so detonate, and have great danger in the production process.
The chemical combination operation is requisite critical process in the priming explosive production process, and this operation directly determines performance, the Quality and yield of product, affects the safety in production of subsequent handling, and the major equipment of its use is combination apparatus.
China all is to adopt to finish the chemical combination process in single tank body for the production of the general outmoded backwardness of the combination apparatus of the medicament that detonates at present, yields poorly; Manually production technique falls behind, and all technological actions adopt manual operation substantially, and feeding quantity and feed rate Artificial Control, chemical combination temperature Artificial Control, quality product are difficult to assurance, and consistence is poor, and the various ignition and blasting equipment versatilities such as filling detonator, safety fuse are poor.Production process needs 2-3 people, and there is obnoxious flavour in Working environment, to healthy harmful, demands urgently improving.
Summary of the invention
The purpose of this utility model is to provide a kind of multiple step format continuous combination apparatus, has solved the problems referred to above that present technology exists.The utility model adopts substep continous way chemical combination process and automated control technology, namely three free-standing chemical combination devices, continuously self-emptying transmission, automatic temp closed-loop control (thermometric and control), self-feeding amounts and control feeding quantity feed rate, automatically control stepless adjustable, the rotating speed automatic monitoring of stirring velocity and automatic cleaning technology, realize improve production efficiency and product quality, reduced the purpose that the workman works and endangers.
Above-mentioned purpose of the present utility model is achieved through the following technical solutions:
The continuous combination apparatus of multiple step format comprises material measuring apparatus and the identical free-standing chemical combination device of three cover structures that two cover structures are identical, and described free-standing chemical combination device refers to reactor 10, ager 13 and crystallizer 14; Described material measuring apparatus is connected with reactor 10 by pipeline respectively, described reactor 10 is connected with ager 13 by pipeline, described ager 13 is connected with crystallizer 14 by pipeline, and the installation site of described material measuring apparatus is higher than the installation site of reactor 10, the installation site of described reactor 10 is higher than the installation site of ager 13, the installation site of described ager 13 is higher than the installation site of crystallizer 14, and material relies on liquid level difference to flow between each container.
Described material measuring apparatus comprises material scale tank I, II 1,3, overflow self-acting valve 2, adjustment height pipeline 4, self-feeding valve 5, explosion-proof under meter 6 and automatic regulating valve 7, and described overflow self-acting valve 2 is connected with material scale tank I, II 1,3 by adjustment height pipeline 4 respectively; Described material scale tank I, II 1,3 bottom are connected with reactor 10 by pipeline respectively, and on pipeline, be connected in series successively self-feeding valve 5, explosion-proof under meter 6 and automatic regulating valve 7.
Described reactor 10 comprises agitator motor step-down gear 8, temperature sensor 9, automatic discharger 11, reaches stirring rake 16, described agitator motor step-down gear 8 is installed in the top of reactor 10, described temperature sensor 9 is arranged on the top, side of reactor, described automatic discharger 11 is installed in the bottom of reactor 10, and described stirring arm 16 is arranged in the reactor 10.
Described reactor 10, ager 13 and crystallizer 14 are connected with pure water pipe B by pipeline and cleaning self-acting valve 17 respectively.
Described reactor 10 is sandwich structure, this sandwich structure respectively with advance, backheat water pipe C, D be connected, and this advances to arrange on the hot-water line C heating self-acting valve 12.
Described ager 13 is sandwich structure, this sandwich structure respectively with advance, backheat water pipe C, D be connected.
Described crystallizer 14 is sandwich structure, this sandwich structure respectively with advance, return cold water pipe E, F and is connected, and this advances to arrange on the cold water pipe E and cools off self-acting valve 15.
The beneficial effects of the utility model are: novel structure, simple, use safety, convenient.Adopt the free-standing chemical combination device of three covers that the chemical combination process is divided into reaction, slaking and three steps of crystallization, the twice of enhancing productivity.Adopt advanced automatic control technology, realize self-feeding, automatically control feeding quantity and feed rate, the control of chemical combination temperature automated closed-loop, control is stirred automatically, and the stirring velocity frequency conversion is adjustable and automatic monitoring, the material automatic transmission, combination apparatus cleans automatically.Improved production efficiency, but the precisely control product quality, and the consistence of improving the quality of products reduces operator's quantity (only needing 1 people), has shortened the working hour in hostile environment.Practical.
Description of drawings
Accompanying drawing described herein is used to provide further understanding of the present utility model, consists of the application's a part, and illustrative example of the present utility model and explanation thereof are used for explaining the utility model, do not consist of improper restriction of the present utility model.
Fig. 1 is structural representation of the present utility model.
Among the figure: 1. material scale tank I; 2. overflow self-acting valve; 3. expect the scale tank II; 4. adjustment height pipeline; 5. self-feeding valve; 6. explosion-proof under meter; 7. automatic regulating valve; 8. agitator motor step-down gear; 9. temperature sensor; 10. reactor; 11. automatic discharger; 12. heating self-acting valve; 13. ager; 14. crystallizer; 15. cooling self-acting valve; 16. stirring rake; 17. cleaning self-acting valve.
Embodiment
Further specify detailed content of the present utility model and embodiment thereof below in conjunction with accompanying drawing.
Referring to Fig. 1, the continuous combination apparatus of multiple step format of the present utility model comprises material measuring apparatus and the identical free-standing chemical combination device of three cover structures that two cover structures are identical, and described free-standing chemical combination device refers to reactor 10, ager 13 and crystallizer 14; Described material measuring apparatus is connected with reactor 10 by pipeline respectively, described reactor 10 is connected with ager 13 by pipeline, described ager 13 is connected with crystallizer 14 by pipeline, and the installation site of described material measuring apparatus is higher than the installation site of reactor 10, the installation site of described reactor 10 is higher than the installation site of ager 13, the installation site of described ager 13 is higher than the installation site of crystallizer 14, and material relies on liquid level difference to flow between each container.
Described material measuring apparatus comprises material scale tank I, II 1,3, overflow self-acting valve 2, adjustment height pipeline 4, self-feeding valve 5, explosion-proof under meter 6 and automatic regulating valve 7, and described overflow self-acting valve 2 is connected with material scale tank I, II 1,3 by adjustment height pipeline 4 respectively; Described material scale tank I, II 1,3 bottom are connected with reactor 10 by pipeline respectively, and on pipeline, be connected in series successively self-feeding valve 5, explosion-proof under meter 6 and automatic regulating valve 7.
Described reactor 10 comprises agitator motor step-down gear 8, temperature sensor 9, automatic discharger 11, reaches stirring rake 16, described agitator motor step-down gear 8 is installed in the top of reactor 10, described temperature sensor 9 is arranged on the top, side of reactor, described automatic discharger 11 is installed in the bottom of reactor 10, and described stirring arm 16 is arranged in the reactor 10.
Described reactor 10, ager 13 and crystallizer 14 are connected with pure water pipe B by pipeline and cleaning self-acting valve 17 respectively.
Described reactor 10 is sandwich structure, this sandwich structure respectively with advance, backheat water pipe C, D be connected, and this advances to arrange on the hot-water line C heating self-acting valve 12.
Described ager 13 is sandwich structure, this sandwich structure respectively with advance, backheat water pipe C, D be connected.
Described crystallizer 14 is sandwich structure, this sandwich structure respectively with advance, return cold water pipe E, F and is connected, and this advances to arrange on the cold water pipe E and cools off self-acting valve 15.
Referring to Fig. 1, workflow of the present utility model is as follows:
After feed liquid enters material scale tank I, II 1,3, unnecessary feed liquid flows out by overflow port A through adjustment height pipeline 4 and overflow self-acting valve 2, feed liquid in material scale tank I, the II 1,3 adds in the reactor 10 through self-feeding valve 5, explosion-proof under meter 6 and automatic regulating valve 7 automatically, explosion-proof under meter 6 forms closed-loop control with automatic regulating valve 7, automatically controls feed rate and feeding quantity.
The chemical combination process was divided into for three steps, i.e. reaction, slaking and crystallization, in reactor 10, ager 13 and crystallizer 14, finish respectively, reactor 10, ager 13 and crystallizer 14 are sandwich structure, logical hot water in reactor 10, ager 13 interlayers, crystallizer 14 interior logical cold water, temperature sensor 9 forms closed-loop control with heating self-acting valve 12 or cooling self-acting valve 15, automatically controls the feed temperature in the container.
Agitator motor step-down gear 8 drives stirring rake 16 rotations, the automatic stirring of realization response device 10, ager 13 and crystallizer 14, and the stirring velocity frequency conversion is controlled automatically, and rotating speed detects monitoring automatically.
Cleaning automatic valve 17 controls respectively to combination apparatus 10, ager 13 or crystallizer 14 interior automatic water spraying for cleanings.
The above is preferred embodiment of the present utility model only, is not limited to the utility model, and for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (8)
1. continuous combination apparatus of multiple step format is characterized in that: comprise material measuring apparatus and the identical free-standing chemical combination device of three cover structures that two cover structures are identical, described free-standing chemical combination device refers to reactor (10), ager (13) and crystallizer (14); Described material measuring apparatus is connected with reactor (10) by pipeline respectively, described reactor (10) is connected with ager (13) by pipeline, described ager (13) is connected with crystallizer (14) by pipeline, and the installation site of described material measuring apparatus is higher than the installation site of reactor (10), the installation site of described reactor (10) is higher than the installation site of ager (13), the installation site of described ager (13) is higher than the installation site of crystallizer (14), and feed liquid relies on liquid level difference to flow between each container.
2. the continuous combination apparatus of multiple step format according to claim 1, it is characterized in that: described material measuring apparatus comprises material scale tank I, II (1,3), overflow self-acting valve (2), adjustment height pipeline (4), self-feeding valve (5), explosion-proof under meter (6) and automatic regulating valve (7), and described overflow self-acting valve (2) is connected with material scale tank I, II (1,3) by adjustment height pipeline (4) respectively; The bottom of described material scale tank I, II (1,3) is connected with reactor (10) by pipeline respectively, and is connected in series successively self-feeding valve (5), explosion-proof under meter (6) and automatic regulating valve (7) on pipeline.
3. the continuous combination apparatus of multiple step format according to claim 1 and 2, it is characterized in that: described reactor (10) comprises agitator motor step-down gear (8), temperature sensor (9), automatic discharger (11) and stirring rake (16), described agitator motor step-down gear (8) is installed in the top of reactor (10), described temperature sensor (9) is arranged on the top, side of reactor, described automatic discharger (11) is installed in the bottom of reactor (10), and described stirring arm (16) is arranged in the reactor (10).
4. the continuous combination apparatus of multiple step format according to claim 1 is characterized in that: described reactor (10), ager (13) and crystallizer (14) are respectively by pipeline and clean self-acting valve (17) and be connected with pure water pipe (B).
5. the continuous combination apparatus of multiple step format according to claim 3, it is characterized in that: described reactor (10) is sandwich structure, this sandwich structure respectively with advance, backheat water pipe (C, D) is connected, and this advances to arrange on the hot-water line (C) heating self-acting valve (12).
6. the continuous combination apparatus of multiple step format according to claim 4, it is characterized in that: described reactor (10) is sandwich structure, this sandwich structure respectively with advance, backheat water pipe (C, D) is connected, and this advances to arrange on the hot-water line (C) heating self-acting valve (12).
7. according to claim 1 or the continuous combination apparatus of 4 described multiple step formats, it is characterized in that: described ager (13) is sandwich structure, this sandwich structure respectively with advance, backheat water pipe (C, D) is connected.
8. according to claim 1 or the continuous combination apparatus of 4 described multiple step formats, it is characterized in that: described crystallizer (14) is sandwich structure, this sandwich structure respectively with advance, return cold water pipe (E, F) and is connected, and this advances to arrange on the cold water pipe (E) and cools off self-acting valve (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220336721 CN202688220U (en) | 2012-07-12 | 2012-07-12 | Step-by-step continuous chemical combination device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220336721 CN202688220U (en) | 2012-07-12 | 2012-07-12 | Step-by-step continuous chemical combination device |
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| Publication Number | Publication Date |
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| CN202688220U true CN202688220U (en) | 2013-01-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220336721 Expired - Lifetime CN202688220U (en) | 2012-07-12 | 2012-07-12 | Step-by-step continuous chemical combination device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104130089A (en) * | 2014-07-31 | 2014-11-05 | 王吉风 | Two-segment type dangerous-explosive tiny manufacturing apparatus and production method for dangerous explosive finished product |
-
2012
- 2012-07-12 CN CN 201220336721 patent/CN202688220U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104130089A (en) * | 2014-07-31 | 2014-11-05 | 王吉风 | Two-segment type dangerous-explosive tiny manufacturing apparatus and production method for dangerous explosive finished product |
| CN104130089B (en) * | 2014-07-31 | 2016-06-22 | 上海桥键能源科技有限公司 | The production method of two-part danger quick-fried medicine small manufacture device and quick-fried medicine finished product of endangering |
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| CX01 | Expiry of patent term |
Granted publication date: 20130123 |