CN109336724A - A kind of system and method for emulsion continuous automatic production - Google Patents
A kind of system and method for emulsion continuous automatic production Download PDFInfo
- Publication number
- CN109336724A CN109336724A CN201811561605.2A CN201811561605A CN109336724A CN 109336724 A CN109336724 A CN 109336724A CN 201811561605 A CN201811561605 A CN 201811561605A CN 109336724 A CN109336724 A CN 109336724A
- Authority
- CN
- China
- Prior art keywords
- powder stick
- pump
- tank
- belt
- latex
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B31/00—Compositions containing an inorganic nitrogen-oxygen salt
- C06B31/28—Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate
- C06B31/285—Compositions containing an inorganic nitrogen-oxygen salt the salt being ammonium nitrate with fuel oil, e.g. ANFO-compositions
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
- C06B21/0008—Compounding the ingredient
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B31/00—Compositions containing an inorganic nitrogen-oxygen salt
- C06B31/02—Compositions containing an inorganic nitrogen-oxygen salt the salt being an alkali metal or an alkaline earth metal nitrate
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Medicinal Preparation (AREA)
Abstract
The invention discloses a kind of system and method for emulsion continuous automatic production, including the crusher for comminuting ammonium nitrate and sodium nitrate, the air compressor machine and air accumulator being placed in workshop, in the screw conveyor transporting nitric acid ammonium and sodium nitrate to water phase tank connected on crusher, it is sent after processing is completed by the pipeline with water conveying pump to pre- newborn tank in water phase tank, pre- cream tank with oily phase delivery pump pipeline with oily phase tank also by connecting, matrix screw pump is installed in pre- cream tank, long-range control point uses PROFIBUS bus communication technology, vision detection system is increased simultaneously, subsequent quality is carried out to powder stick to check on, reject unqualified powder stick, underproof powder stick is allowed to do over again again, improve the quality of powder stick.Also synchronize increase powder stick reflux belt flow back into previous procedure when powder stick has accumulation not case all and grab vanning again.
Description
Technical field
The present invention relates to a kind of system and method for emulsion continuous automatic production, in particular to a kind of emulsification
The system and method for explosive continuous automatic production.
Background technique
The production process of emulsion be mainly grease mutually prepare, emulsify respectively, cooling down, being sensitized, powder charge, packaging, it is each
Process has corresponding production line, and each production line, which is sequentially connected, forms entire emulsion explosive production line.Wherein, present chargehand
Sequence transmits product generally by conveyer belt and by manually being packed come testing product, but this detection mode efficiency
It is not high, and be easy to be unable to reach the automatic of emulsion product packaging there are mistake when the quantity to product counts
Change.
Summary of the invention
The purpose of the present invention is to provide a kind of system and method for emulsion continuous automatic production, have and improve
The advantages of quality and production efficiency, to solve the problems mentioned in the above background technology.
To achieve the above object, the invention provides the following technical scheme: a kind of emulsion continuous automatic production is
System connects on crusher including the crusher for comminuting ammonium nitrate and sodium nitrate, the air compressor machine and air accumulator that are placed in workshop
In the screw conveyor transporting nitric acid ammonium and sodium nitrate to water phase tank connect, after processing is completed by having water conveying in water phase tank
The pipeline of pump is sent to pre- newborn tank, and pre- cream tank with oily phase delivery pump pipeline with oily phase tank also by connecting, installation in pre- cream tank
Have matrix screw pump, the oil phase material in oily phase tank by raw material from melting tank fusing after enter, the matrix screw pump with it is quiet
State mixer communicates, and the tee tube connected on static mixer connects with two latex pumps respectively, is connected with foaming on latex pump
Agent storage tank and foaming agent delivery pump, latex pump are also connected with static sensitized systems and charging machine, and matrix comes out from static mixer
Enter the feed bin of latex pump afterwards, latex pump can just be switched under conditions of charging machine allows and is switched on, and latex is pumped toward powder filling machine
During sending latex, the foaming agent additional amount that foaming agent delivery pump starts in foaming agent storage tank simultaneously be proportionally automatically with
The flow of the latex of track latex pumping is conveyed, and charging machine is equipped with Film laminating apparatus on one side, after Film laminating apparatus is fabricated to powder stick, powder charge
Machine powder charge and sealing of checking card into powder stick；
The bottom of the charging machine discharging is equipped with powder stick belt, and it is cold that the packaged powder stick of powder stick belt-conveying enters powder stick
But belt carries out immersion cooling, drying after the powder stick dryer group of the cooling belt outlet connection of powder stick, and the powder stick dried passes through
Belt is accelerated to transport minor diameter packaging facilities and major diameter packaging facilities respectively according to classification；
The minor diameter packaging facilities and major diameter packaging facilities are respectively equipped with vision detection system and detect to powder stick, qualified
Powder stick transport big powder stick stacking belt and small medicine coil stacking belt respectively and carry out medicine-chest stacking, packed and transported is gone out, is not conformed to
The powder stick of lattice eliminates.
Further, matrix screw pump stirs the water phase oil of pre- newborn in-tank mixing mutually in pre- cream stirring by effect i.e. fast slowly
Under, water oil mutually interpenetrates, and is sufficiently mixed, and static mixer under the pressure that matrix pumps, forms the colloidal stroma after pre- cream
The bright emulsified bases of Water-In-Oil.
Further, big powder stick stacking belt and small medicine coil stacking belt are connected separately with big powder stick conveyer belt and small medicine coil
It is connected with recrater on the end of conveyer belt, big powder stick conveyer belt and small medicine coil conveyer belt, recrater will be transported from make-up room
Packing case and powder stick vanning.
Further, powder stick flows back belt between big powder stick stacking belt and small medicine coil stacking belt.
Another technical solution of present invention offer, a kind of method of the system of emulsion continuous automatic production, including with
Lower method；
S1: ammonium nitrate, sodium nitrate respectively by ammonium nitrate library, sodium nitrate library with automobile be transported into emulsification pharmacy worker-house it is broken between,
Charging hopper is poured into after weighing, and water phase tank is conveyed by screw conveyor after being crushed into crusher；
S2: by the water of filtration treatment, flowing through metering device, and after reaching set amount, the water in water phase tank is increased to work
After skill temperature, crusher water phase tank and ammonium nitrate spiral are opened, material is added into corresponding tank by selecting artificial control
In, heat up side stirring in charging, and temperature reaches process warm angle value by automatic temperature control valve closed-loop control in the process；
S3: oil phase material by raw material store be transported into emulsification oil phase material between, after platform balance weighs, slice be added melting tank,
Lead to steam indirect heating, oily phase tank is put into after the temperature as defined in all melting and reaching, stirring is uniformly mixed it, by certainly
The automatic adjustment of dynamic temperature control valve, keeps temperature spare；
S4: to process pipeline hot water thermal insulating before production, after having working condition, while water conveying pump and oily phase being opened
Delivery pump, water phase oil-phase solution are sent into pre- newborn tank through filter, water phase pipeline, valve, pump and flowmeter, in pre- cream stirring by slow
Under the action of i.e. fast, water oil is mutually interpenetrated, and is sufficiently mixed；
S5: the colloidal stroma after pre- cream squeezes into static mixer by matrix screw pump, and matrix is in static mixer, and shape
At the emulsified bases that Water-In-Oil is bright；The adjusting of revolving speed is able to maintain the more stable height of the material position of pre- newborn tank, so as to sufficiently newborn
Change；
S6: matrix enters the feed bin that latex pumps after coming out from static mixer, and latex pumps the process that latex is sent toward medicine pump
In, foaming agent delivery pump starts simultaneously, and the revolving speed of latex pump is to give and control because powder charge needs, but work as latex feed bin
When material position reaches lower limit, latex will be automatically stopped rotation, to prevent from dallying；
S7: the emulsion after sensitization is pumped into mixer through latex, further enters charging machine dress after homogenizing and mixing
Medicine, Film laminating apparatus carry out medicine-chest sealing, and the packaged emulsion of charging machine impregnates cold through powder stick belt-conveying, the cooling belt of powder stick
But it is air-dried again with powder stick dryer group；
S8: after the magnitude classification of diameter, powder stick is detected by vision detection system, qualified powder stick transports respectively
Medicine-chest stacking is carried out to big powder stick stacking belt and small medicine coil stacking belt, packed and transported is gone out, and underproof powder stick eliminates
It goes.
Further, in S7, touch screen can show various data, control production, while host computer passes through WINCC
Monitoring software can grasp the various signals such as all temperature, pressure electric currents, and controllable production, if event occurs in charging machine midway
Barrier clicks latex pump on the touchscreen and ceases and desist order, and latex pump, foaming agent delivery pump and static mixer can stop immediately.
Compared with prior art, the beneficial effects of the present invention are:
The system and method for this emulsion continuous automatic production, long-range control point use PROFIBUS bus communication
Technology, while vision detection system is increased, subsequent quality is carried out to powder stick and is checked on, unqualified powder stick is rejected, allows unqualified
Powder stick do over again again, improve the quality of powder stick.Also it synchronizes and increases powder stick reflux belt, when powder stick has accumulation whole
When vanning, flows back into previous procedure and grab vanning again.
Detailed description of the invention
Fig. 1 is whole side view of the invention；
Fig. 2 is overall top view of the invention；
Fig. 3 is packaging return-flow structure figure of the invention；
Fig. 4 is overall flow figure of the invention.
In figure: 1, crusher；2, air compressor machine；3, water phase tank；4, water conveying pumps；5, melting tank；6, oily phase tank；7, oily phase
Delivery pump；8, pre- newborn tank；9, matrix screw pump；10, static mixer；11, latex pumps；12, foaming agent storage tank；13, foaming agent
Delivery pump；14, static sensitized systems；15, charging machine；16, Film laminating apparatus；17, powder stick belt；18, the cooling belt of powder stick；19, medicine
Roll up dryer group；20, minor diameter packaging facilities；21, major diameter packaging facilities；22, powder stick reflux belt；23, big powder stick stacking
Belt；24, small medicine coil stacking belt；25, vision detection system.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear；It is complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments, is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
A kind of system of emulsion continuous automatic production referring to FIG. 1-2, including it is used for comminuting ammonium nitrate and nitric acid
The crusher 1 of sodium, the air compressor machine 2 being placed in workshop and air accumulator, the screw conveyor transporting nitric acid ammonium connected on crusher 1
In sodium nitrate to water phase tank 3, sent after processing is completed by the pipeline with water conveying pump 4 to pre- newborn tank 8 in water phase tank 3
Interior, pre- cream tank 8 is also connected by having oily 7 pipeline of phase delivery pump with oily phase tank 6, is equipped with matrix screw pump 9 in pre- cream tank 8,
Oil phase material in oily phase tank 6 is entered after the fusing of melting tank 5 by raw material, the matrix screw pump 9 and static mixer 10
It communicates, the tee tube connected on static mixer 10 connects with two latex pumps 11 respectively, is connected with foaming agent on latex pump 11
Storage tank 12 and foaming agent delivery pump 13, latex pump 11 are also connected with static sensitized systems 14 and charging machine 15, and matrix is mixed from static state
Clutch 10 enters the feed bin of latex pump 11 after coming out, matrix screw pump 9 stirs the water phase oil mixed in pre- newborn tank 8 and mutually stirs in pre- cream
Mix by under the action of i.e. fast slowly, water oil is mutually interpenetrated, be sufficiently mixed, static mixer 10 by it is pre- it is newborn after water oil mix liquid
Under the pressure of matrix pump, the bright emulsified bases of Water-In-Oil is formed, without the effect of any machinery, without any friction, from
The risk factor of latex manufacture is fundamentally eliminated, latex pump 11 can just be switched under conditions of charging machine 15 allows and is switched on,
During latex pump 11 send latex toward powder filling machine 15, foaming agent delivery pump 13 starts the foaming in foaming agent storage tank 12 simultaneously
Agent additional amount is proportionally to automatically track the flow of latex that latex pump 11 is sent to be conveyed, and 15 one side of charging machine is equipped with
Film machine 16, the powder stick that Film laminating apparatus 16 makes are installed and are sealed through charging machine 15；Without cap-sensitivity before powder charge is completed during this,
Promote Emulsion Explosive Production intrinsic safety.The bottom that charging machine 15 discharges is equipped with powder stick belt 17, and powder stick belt 17 transports
Packaged medicine-chest enters the cooling belt 18 of powder stick and carries out immersion cooling, the powder stick drying machine of the cooling outlet of belt 18 connection of powder stick
Dry after group 19, the medicine-chest dried is by accelerating belt to transport minor diameter packaging facilities 20 and major diameter respectively according to classification
Packaging facilities 21, minor diameter packaging facilities 20 and major diameter packaging facilities 21.
It please refers to Fig. 3-4, minor diameter packaging facilities 20 and major diameter packaging facilities 21 and is respectively equipped with vision detection system
25 pairs of powder stick detections, qualified powder stick transports big powder stick stacking belt 23 respectively and small medicine coil stacking belt 24 carries out medicine-chest code
Pile, packed and transported are gone out, and big powder stick stacking belt 23 and small medicine coil stacking belt 24 are connected separately with big powder stick conveyer belt and small
Recrater is connected on the end of powder stick conveyer belt, big powder stick conveyer belt and small medicine coil conveyer belt, recrater will be transported from make-up room
Defeated packing case and powder stick vanning, underproof powder stick eliminate.
A kind of method of the system of emulsion continuous automatic production, including following methods；
Step 1: ammonium nitrate, sodium nitrate are transported into emulsification pharmacy worker-house with automobile and are crushed by ammonium nitrate library, sodium nitrate library respectively
Between, charging hopper is poured into after weighing, and water phase tank 3 is conveyed by screw conveyor after being crushed into crusher 1；
Step 2: by the water of filtration treatment, flowing through metering device, and after reaching set amount, the water in water phase tank 3 is increased
To after technological temperature, crusher water phase tank 3 and ammonium nitrate spiral are opened, material is added into corresponding by selecting artificial control
Tank in, while charging while heat up side stir, temperature reaches process warm angle value by automatic temperature control valve closed-loop control in the process；
Step 3: oil phase material by raw material store be transported into emulsification oil phase material between, after platform balance weighs, slice be added fusing
Slot 5 leads to steam indirect heating, and oily phase tank 6 is put into after the temperature as defined in all melting and reaching, and stirring is uniformly mixed it,
By the automatic adjustment of automatic temperature control valve, keep temperature spare；
Step 4: to process pipeline hot water thermal insulating before production, after having working condition, while water conveying pump 4 is opened
With oily phase delivery pump 7, water phase oil-phase solution is sent into pre- newborn tank 8, in pre- cream through filter, water phase pipeline, valve, pump and flowmeter
Under the action of stirring is by being fast slowly, water oil is mutually interpenetrated, and is sufficiently mixed
Step 5: the water oil after pre- cream mixes liquid and squeezes into static mixer 10 by matrix screw pump 9, and matrix is mixed in static state
In clutch 10, the bright emulsified bases of Water-In-Oil is formed；The adjusting of revolving speed is able to maintain the more stable height of the material position of pre- newborn tank 8,
So as to fully emulsified；
Step 6: matrix enters the feed bin of latex pump 11 after coming out from static mixer 10, and latex pump 11 is sent toward medicine pump
During latex, foaming agent delivery pump 13 starts simultaneously, and the revolving speed of latex pump 11 is given and controls because powder charge needs,
But when the material position of latex feed bin reaches lower limit, latex will be automatically stopped rotation, to prevent from dallying；
Step 7: the emulsion after sensitization is sent to mixer through latex pump 11, further enters dress after homogenizing and mixing
15 powder charge of medicine machine, Film laminating apparatus 16 make powder stick and are transported by the packaged emulsion of charging machine 15 through powder stick belt 17, and powder stick is cold
But belt 18 impregnates cooling and powder stick dryer group 19 and air-dries again, and touch screen can show various data, and control produces, while on
Position machine can grasp the various signals such as all temperature, pressure electric currents, and controllable production by WINCC monitoring software, if powder charge
Machine 15 breaks down halfway, clicks latex pump 11 on the touchscreen and ceases and desist order, latex pump 11, foaming agent delivery pump 13 and static state
Mixer 10 can stop immediately；
Step 8: after the magnitude classification of diameter, powder stick is detected by vision detection system 25, qualified powder stick point
Big powder stick stacking belt 23 is not transported and small medicine coil stacking belt 24 carries out medicine-chest stacking, and packed and transported is gone out, underproof
Powder stick is rejected to going out.
It emulsifies line and core control is carried out using S7-300 controller, host computer is communicated using Industrial Ethernet, is touched
Screen, frequency converter, long-range control point use PROFIBUS bus communication technology, and this industrial communication method can quickly transmit temperature
It spends the data-signals and facility switching etc. such as pressure and controls signal, the temperature control of water oil phase uses automatic temperature control valve, according to setting
Automatic temperature control valve door aperture makes temperature of charge control in processing range, while increasing vision detection system 25, to medicine
Volume carries out subsequent quality and checks on, and improves the quality of powder stick.Also it synchronizes and increases powder stick reflux belt 22, when powder stick has accumulation
When can not all case, flows back into previous procedure and grab vanning stacking again.
In conclusion the system and method for this emulsion continuous automatic production, long-range control point is used
PROFIBUS bus communication technology, while vision detection system 25 is increased, subsequent quality is carried out to powder stick and is checked on, is improved
The quality of powder stick.Also it synchronizes and increases powder stick reflux belt 22, when powder stick has accumulation not case all, before flowing back into together
Process grabs vanning stacking again.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Anyone skilled in the art within the technical scope of the present disclosure, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (6)
1. a kind of system of emulsion continuous automatic production, including for comminuting ammonium nitrate and sodium nitrate crusher (1),
Air compressor machine (2) and the air accumulator being placed in workshop, which is characterized in that the screw conveyor transport nitre connected on crusher (1)
In sour ammonium and sodium nitrate to water phase tank (3), sent after processing is completed by the pipeline with water conveying pump (4) in water phase tank (3)
To pre- newborn tank (8), pre- cream tank (8) with oily phase delivery pump (7) pipeline with oily phase tank (6) also by connecting, in pre- cream tank (8)
It is equipped with matrix screw pump (9), the oil phase material in oily phase tank (6) enters after being melted by raw material from melting tank (5), the base
Matter screw pump (9) is communicated with static mixer (10), and the tee tube connected on static mixer (10) is pumped with two latexes respectively
(11) connect, foaming agent storage tank (12) and foaming agent delivery pump (13) are connected on latex pump (11), latex pump (11) is also connected with
Enter the material of latex pump (11) after thering are static sensitized systems (14) and charging machine (15), matrix to come out from static mixer (10)
Storehouse, latex pump (11) and can just be switched under conditions of charging machine (15) allows and is switched on, and latex pumps (11) and pumps toward charging machine (15)
During sending latex, foaming agent delivery pump (13) starts simultaneously, the foaming agent additional amount in foaming agent storage tank (12) be according to
The flow that ratio automatically tracks the latex that latex pump (11) is sent is conveyed, and charging machine (15) is equipped with Film laminating apparatus (16) on one side,
Emulsion medicine body is packed into that powder stick make by Film laminating apparatus (16) is interior and sealing of checking card by charging machine (15)；
The bottom of the charging machine (15) discharging is equipped with powder stick belt (17), the good medicine-chest of powder stick belt (17) transportation and packing into
Enter powder stick cooling belt (18) and carry out immersion cooling, the powder stick dryer group (19) of powder stick cooling belt (18) outlet connection is done afterwards
Dry, by accelerating, belt transports minor diameter packaging facilities (20) according to classification to the medicine-chest dried respectively and major diameter packaging is set
Standby (21), minor diameter packaging facilities (20) and major diameter packaging facilities (21)；
The minor diameter packaging facilities (20) and major diameter packaging facilities (21) are simultaneously respectively equipped with vision detection system (25) to medicine
Volume detection, qualified powder stick transports big powder stick stacking belt (23) respectively and small medicine coil stacking belt (24) carries out medicine-chest code
Pile, packed and transported are gone out, and underproof powder stick eliminates.
2. a kind of system of emulsion continuous automatic production according to claim 1, it is characterised in that: matrix screw rod
Pump (9) stirs the oily phase of water phase of mixing in pre- newborn tank (8) under the action of pre- cream stirring by being fastly slowly, and water is oily mutually to be interpenetrated,
It is sufficiently mixed, the water oil after pre- cream is mixed liquid under the pressure of matrix screw pump (9) by static mixer (10), forms oil packet
The bright emulsified bases of water.
3. a kind of system of emulsion continuous automatic production according to claim 1, it is characterised in that: big powder stick code
Pile belt (23) and small medicine coil stacking belt (24) are connected separately with big powder stick conveyer belt and small medicine coil conveyer belt, big powder stick conveying
Recrater is connected on the end of band and small medicine coil conveyer belt, recrater cases the packing case and powder stick that transport from make-up room.
4. a kind of system of emulsion continuous automatic production according to claim 1, it is characterised in that: powder stick reflux
Belt (22) is between big powder stick stacking belt (23) and small medicine coil stacking belt (24).
5. a kind of method of the system of emulsion continuous automatic production as described in claim 1, which is characterized in that including
Following methods；
S1: ammonium nitrate, sodium nitrate respectively by ammonium nitrate library, sodium nitrate library with automobile be transported into emulsification pharmacy worker-house it is broken between, through claiming
Charging hopper is poured into after amount, and water phase tank (3) are conveyed by screw conveyor after being crushed into crusher (1)；
S2: by the water of filtration treatment, flowing through metering device, and after reaching set amount, the inner water of water phase tank (3) is increased to technique
After temperature, crusher water phase tank (3) and ammonium nitrate spiral are opened, material is added into corresponding tank by selecting artificial control
In, heat up side stirring in charging, and temperature reaches process warm angle value by automatic temperature control valve closed-loop control in the process；
S3: oil phase material by raw material store be transported into emulsification oil phase material between, after platform balance weighs, slice be added melting tank (5), lead to
Steam indirect heating, is put into oily phase tank (6) after all melting and reaching defined temperature, and stirring is uniformly mixed it, passes through
The automatic adjustment of automatic temperature control valve keeps temperature spare；
S4: keeping the temperature process pipeline before production, and need soak according to the technological requirements uses steam, cannot use high temperature dwell
Temperature uses hot water thermal insulating, after having working condition, while opening water conveying pump (4) and oily phase delivery pump (7), water phase oil mixes
Liquid is sent into pre- newborn tank (8) through filter, water phase pipeline, valve, pump and flowmeter, under the action of pre- cream stirring is by being slowly fast, water
Oil mutually interpenetrates, and is sufficiently mixed
S5: the water oil after pre- cream mixes liquid and squeezes into static mixer (10) by matrix screw pump (9), in static mixer (10)
In, form the bright emulsified bases of Water-In-Oil；The adjusting of revolving speed is able to maintain the more stable height of the material position of pre- newborn tank (8), so as to
It is fully emulsified；
S6: matrix enters the feed bin of latex pump (11) after coming out from static mixer (10), and latex pump (11) send cream toward medicine pump
During glue, foaming agent delivery pump (13) starts simultaneously, and the revolving speed of latex pump (11) is given and controls because powder charge needs
, but when the material position of latex feed bin reaches lower limit, latex will be automatically stopped rotation, to prevent from dallying；
S7: the emulsion after sensitization further enters charging machine powder charge, upper film after homogenizing and mixing through 11) being sent to mixer
Machine (16) provides piece film and carries out powder charge sealing, and charging machine (15) packaged emulsion is transported through powder stick belt (17), powder stick
Cooling belt (18) are impregnated cooling and powder stick dryer group (19) and are air-dried again；
S8: after the magnitude classification of diameter, powder stick is detected by vision detection system (25), qualified powder stick transports respectively
Medicine-chest stacking is carried out to big powder stick stacking belt (23) and small medicine coil stacking belt (24), packed and transported is gone out, underproof medicine
Volume eliminates.
6. a kind of method of the system of emulsion continuous automatic production as claimed in claim 5, which is characterized in that be directed to
In S7, it is all that touch screen can show that various data, control production, while host computer can be grasped by WINCC monitoring software
The various signals such as temperature, pressure electric current, and controllable production is clicked on the touchscreen if charging machine (15) midway is broken down
Latex pump (11) is ceased and desisted order, and latex pump (11), foaming agent delivery pump (13) and static mixer (10) can stop immediately.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811561605.2A CN109336724A (en) | 2018-12-20 | 2018-12-20 | A kind of system and method for emulsion continuous automatic production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811561605.2A CN109336724A (en) | 2018-12-20 | 2018-12-20 | A kind of system and method for emulsion continuous automatic production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109336724A true CN109336724A (en) | 2019-02-15 |
Family
ID=65304623
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811561605.2A Pending CN109336724A (en) | 2018-12-20 | 2018-12-20 | A kind of system and method for emulsion continuous automatic production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109336724A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110452074A (en) * | 2019-08-08 | 2019-11-15 | 江西吉安国泰特种化工有限责任公司 | A kind of automatic control system of emulsifying ammonium nitrate fuel explosive production |
| CN110627589A (en) * | 2019-08-08 | 2019-12-31 | 江西吉安国泰特种化工有限责任公司 | Emulsified ammonium nitrate fuel oil explosive production system |
| CN113800991A (en) * | 2021-09-22 | 2021-12-17 | 浙江顺源化工有限公司 | Emulsion explosive unmanned production line and production method |
| CN114907174A (en) * | 2022-05-24 | 2022-08-16 | 湖北凯龙化工集团股份有限公司 | Emulsion explosive production line without fixed operators in dangerous workshop |
| CN115009638A (en) * | 2022-05-25 | 2022-09-06 | 湖南金聚能科技有限公司 | Automatic production line and production process of emulsion explosive |
| CN116969803A (en) * | 2023-08-30 | 2023-10-31 | 四川今点企业管理咨询服务有限公司 | Emulsion explosive unqualified product reworking equipment and use method thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2011153155A (en) * | 2011-12-26 | 2013-07-10 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | METHOD FOR PRODUCING SPHERICAL POWDER |
| CN107540490A (en) * | 2017-08-29 | 2018-01-05 | 江西吉安国泰特种化工有限责任公司 | A kind of Safe production technology for emulsifying ANFO explosives prill |
-
2018
- 2018-12-20 CN CN201811561605.2A patent/CN109336724A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2011153155A (en) * | 2011-12-26 | 2013-07-10 | Федеральное казенное предприятие "Государственный научно-исследовательский институт химических продуктов" (ФКП "ГосНИИХП") | METHOD FOR PRODUCING SPHERICAL POWDER |
| CN107540490A (en) * | 2017-08-29 | 2018-01-05 | 江西吉安国泰特种化工有限责任公司 | A kind of Safe production technology for emulsifying ANFO explosives prill |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110452074A (en) * | 2019-08-08 | 2019-11-15 | 江西吉安国泰特种化工有限责任公司 | A kind of automatic control system of emulsifying ammonium nitrate fuel explosive production |
| CN110627589A (en) * | 2019-08-08 | 2019-12-31 | 江西吉安国泰特种化工有限责任公司 | Emulsified ammonium nitrate fuel oil explosive production system |
| CN110627589B (en) * | 2019-08-08 | 2021-05-04 | 江西吉安国泰特种化工有限责任公司 | Emulsified ammonium nitrate fuel oil explosive production system |
| CN110452074B (en) * | 2019-08-08 | 2021-08-24 | 江西吉安国泰特种化工有限责任公司 | Automatic control system for production of emulsified ammonium nitrate fuel oil explosive |
| CN113800991A (en) * | 2021-09-22 | 2021-12-17 | 浙江顺源化工有限公司 | Emulsion explosive unmanned production line and production method |
| CN114907174A (en) * | 2022-05-24 | 2022-08-16 | 湖北凯龙化工集团股份有限公司 | Emulsion explosive production line without fixed operators in dangerous workshop |
| CN115009638A (en) * | 2022-05-25 | 2022-09-06 | 湖南金聚能科技有限公司 | Automatic production line and production process of emulsion explosive |
| CN115009638B (en) * | 2022-05-25 | 2024-04-05 | 湖南金聚能科技有限公司 | Automatic production line and production process of emulsion explosive |
| CN116969803A (en) * | 2023-08-30 | 2023-10-31 | 四川今点企业管理咨询服务有限公司 | Emulsion explosive unqualified product reworking equipment and use method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109336724A (en) | A kind of system and method for emulsion continuous automatic production | |
| CN107540490A (en) | A kind of Safe production technology for emulsifying ANFO explosives prill | |
| CN106631636B (en) | A kind of emulsified detonator loading system | |
| CN110052209A (en) | A kind of continuous homogenization system of double-screw shaft of lithium battery slurry | |
| CN209552139U (en) | A kind of concrete feeding and agitating device | |
| CN104109057A (en) | Method for continuously producing emulsion explosive without charge pump through emulsification and sensitization under static state | |
| CN107008181A (en) | The automatic batch mixing ager of capsule and pill and method | |
| CN108714397A (en) | A kind of portable powder feed system | |
| CN105903367A (en) | Weighing and burdening system and production process for weighing and burdening | |
| CN106916042A (en) | A kind of package-type emulsifying ammonium nitrate fuel explosive and preparation method thereof | |
| CN111253198A (en) | Formula and production process of detonator-free sensitivity emulsified granular ammonium nitrate fuel oil explosive | |
| US4339202A (en) | Asphalt weigh and mix apparatus and process | |
| CN112723966A (en) | Safety interlocking protection system and method for automatic explosive production line | |
| CN208035013U (en) | Automatic mixing pulping system | |
| CN104857888A (en) | Automatic batching system | |
| CN208694763U (en) | A kind of batcher automatically controlling dosage | |
| CN109515787A (en) | A kind of more specification high-precision material filling machines and placement method | |
| CN109464959A (en) | A kind of feeding system and method further increasing chemical industry slurry consecutive production charge ratio precision | |
| CN207267846U (en) | A kind of static sensitization apparatus of emulsion | |
| CN107027647A (en) | One kind pig feeding device and its control method | |
| CN114699985B (en) | Aqueous solution configuration method, apparatus, and computer-readable storage medium | |
| CN112479794A (en) | High-performance emulsified granular ammonium nitrate fuel oil explosive and preparation method thereof | |
| CN204933388U (en) | A kind of automatic batching system | |
| CN108654542A (en) | A kind of modified asphalt waterproof coiled material continuous batching device and distribution | |
| CN206160846U (en) | Blasting is with emulsion explosive scene system of loading in mixture |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: 510000 Guangda Road, Lianyi Village, Zengjiang Street, Zengcheng District, Guangzhou City, Guangdong Province, 28 Applicant after: Guangdong Hongda Civil Explosion Group Co., Ltd. Address before: 510640 Guangda Road, Lianyi Village, Zengjiang Street, Zengcheng District, Guangzhou City, Guangdong Province, 28 Applicant before: Guangdong Hongda Zenghua Blasting Co., Ltd. |
|
| CB02 | Change of applicant information | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190215 |
|
| RJ01 | Rejection of invention patent application after publication |