CN206566222U - A kind of full closed aseptic intelligent integral pharmacy system - Google Patents
A kind of full closed aseptic intelligent integral pharmacy system Download PDFInfo
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- CN206566222U CN206566222U CN201621234670.0U CN201621234670U CN206566222U CN 206566222 U CN206566222 U CN 206566222U CN 201621234670 U CN201621234670 U CN 201621234670U CN 206566222 U CN206566222 U CN 206566222U
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- Prior art keywords
- separator
- cyclone separator
- centrifugal cyclone
- sterilizing
- full closed
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- 239000000463 material Substances 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 230000001954 sterilising effect Effects 0.000 claims abstract description 18
- 238000004140 cleaning Methods 0.000 claims abstract description 8
- 238000011084 recovery Methods 0.000 claims abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 25
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 239000000843 powder Substances 0.000 description 13
- 239000007789 gas Substances 0.000 description 11
- 230000008676 import Effects 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 238000002156 mixing Methods 0.000 description 6
- 229910001220 stainless steel Inorganic materials 0.000 description 6
- 239000010935 stainless steel Substances 0.000 description 6
- 238000010992 reflux Methods 0.000 description 5
- 101100298222 Caenorhabditis elegans pot-1 gene Proteins 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 244000144985 peep Species 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000006399 behavior Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Cyclones (AREA)
Abstract
The utility model discloses a kind of full closed aseptic intelligent integral pharmacy system.Including device for charging material, gas generator, sterilizing separator, cleaning device, the sterilizing separator includes a separator and second separator and its corresponding Steam Recovery device, the separator is a centrifugal cyclone separator, water conservancy diversion separation spiral ring flat-plate is arranged with along its axis direction on described its perisporium of centrifugal cyclone separator, the rotating curve that the axial direction line that the bottom of centrifugal cyclone separator and the entrance and exit on top are opened in respectively separates spiral ring flat-plate with the water conservancy diversion respectively is tangent.This full closed aseptic intelligent integral pharmacy system can be truly realized the dustless of material, sterileization conveying, and transfer efficiency is high, safe and reliable, it is possible to prevente effectively from primary and secondary pollution, improves enterprise scale production degree.
Description
Technical field
The utility model is related to a kind of pharmaceutical equipment technical field, more particularly to a kind of full closed aseptic intelligent integral system
Medicine system.
Background technology
The existing equipment for used in raw material medicinal powder, the sterilizing-drying of chemical powder, is batch (-type) multiple operation mixing system
Need to set a turnover equipment between the independent production equipment made, each operation or manually had enough to meet the need, container and powder are multiple
It is exposed in the work environment, so easily make sterilizing complete dry cooling after raw material exposure in atmosphere, generate secondary
Pollution, and so production efficiency is low, and labor strength is big, while large-scale production is limited to a certain extent, it is special
Be not that amount of bacteria is exceeded, it is easy to produce secondary pollution and infection, seriously perplexed modern enterprise powder material production it is suitable
Profit is carried out, so that the development of the serious scale intensive manufacture for constraining enterprise.
Utility model content
The purpose of this utility model is that there is provided a kind of full closed aseptic intelligent integral the problem of presence for prior art
Pharmacy system.This full closed aseptic intelligent integral pharmacy system can be truly realized the dustless of material, sterileization conveying, conveying
It is efficiency high, safe and reliable, it is possible to prevente effectively from primary and secondary pollution, improves enterprise scale production degree, improves product
Quality and production efficiency.
The technical scheme of the utility model full closed aseptic intelligent integral pharmacy system includes device for charging material, gas
Generator, sterilizing separator, cleaning device, the sterilizing separator include a separator and second separator and its phase
The Steam Recovery device answered, the separator is along its axle on a centrifugal cyclone separator, described its perisporium of centrifugal cyclone separator
Line direction is arranged with water conservancy diversion separation spiral ring flat-plate, and the bottom of centrifugal cyclone separator and the entrance and exit on top are opened in respectively
The axial direction line rotating curve that separates spiral ring flat-plate with the water conservancy diversion respectively it is tangent.
The water conservancy diversion separation spiral ring flat-plate of the centrifugal cyclone separator its from external diameter side toward internal diameter side downward or upward
Tilt oblique.
Device such as control device of its each composition system of full closed aseptic intelligent integral pharmacy system of the present utility model,
Device for charging material, gas generator, sterilizing separator etc. use modularized design, can enter according to the different demands of client
Targetedly multimode is combined row, is played the different technologies advantage of each submodule block system, is that client makes optimization to measure
System production decision, and itself automaticity of each submodule block system is higher, with production efficiency is high, labor intensity is low, behaviour
The features such as making intelligent control.Its oil-free air pump, air heater can be provided for line production system health, oil-free, it is sterile,
The adjustable clean air source of pressure and temp.
Its control device can automatic detection, adjustment, control cleaning agent process units is cleaned, meet on a large scale,
The efficiency produced for a long time.The design of cleaning device improves the security of product with application, saves the operating time, improves
Efficiency, saving labour, guarantee safe operation, save water, steam equal energy source, production equipment can realize maximization, Automated water
Flat height.
Brief description of the drawings
Fig. 1 is the example structure schematic diagram of the utility model one.Fig. 2 is the example structure of air heater one in Fig. 1
Schematic diagram.Fig. 3 is the example structure schematic diagram of cyclone separator one in Fig. 1.Figure 4 and 5 are respectively the whirlwind in utility model
The structural representation of the embodiment 2 and 3 of separator.Fig. 6 is the example structure of steam generator one signal in the utility model
Figure.
Embodiment
To there is further understanding to the utility model, by the following examples with reference to accompanying drawing to principle of the present utility model
It is described with feature, as shown in Figure 1-2, the system, control device, device for charging material, gas generator, sterilizing separation dress
Put, cleaning device etc., its control device includes manual overvide and intellectual automaton, and manual overvide includes
Corresponding operation control platform, operational control cabinet.
Its device for charging material is arranged at described manual overvide side, and device for charging material includes raw material memory
10th, material lifting conveyer 11, control cabinet, feed hopper 13, described raw material memory 10, its port of export by pipeline with it is described
Material lifting conveyer 11 inlet end connection, described material lifting conveyer 11, its exit end by pipeline with
The inlet end connection of described feed hopper 13.Raw material memory 10 is connected with a material-pulverizing device 4.Material-pulverizing device
A device for transporting objects can be connected between raw material memory 10.
The top of feed hopper 13 is provided with Butterworth Hatch, and its side is provided with stuff level switch, gas generator, and it is arranged at
The bottom of the operation control platform of manual overvide, gas generator, including air pump 5, air heater 6, special-shaped t-bend
7a, steam generator 8, special-shaped t-bend 7a, its one end are provided with an import, another import, and the other end sets outlet, described sky
Its exit end of air pump 5 is connected by pipeline and corresponding control valve with the import of described air heater 6, described sky
Air pump 5, it is specially oil-free air pump, described air heater 6, its exit end by corresponding threeway, pipeline and/or
And corresponding control valve is connected with a special-shaped t-bend 7a import；Described steam generator 8, its inlet end by pipeline,
Corresponding control valve is external to steam, and the exit end of steam generator 8 passes through pipeline, corresponding control valve and special-shaped t-bend 7a
Another import connection.
The air heater 6 enters including heating chamber 61, combustion chamber 62, combustion exhaust 63, combustion air intake 64, air
Gas port 65, air exhaust port 66, fuel from combustion air intake enter combustion chamber in burnt, the waste gas produced during burning is from combustion
Burn exhaust outlet discharge；Cold air absorbs temperature after the heat of combustion chamber and raised from air inlet enters heating chamber, then from sky
Gas exhaust outlet is exported.
Sterilizing separator is arranged at manual overvide one end, and sterilizing separator includes rotary valve 14, special-shaped t-bend
7b, separator 18, separator 18 are a cyclone separator, and cyclone separator includes cyclone separator 18a, a secondary cyclone point
It is described from device 18b, primary steam recover 22a, indirect steam recover 22b, filter 23a, aflter-fillter 23b
Mixing duct 15, its one end is connected with the port of export of rotary valve 14, the other end and a cyclone separator 18a inlet end
Connection, described its upper outlet of cyclone separator 18a passes through pipeline, corresponding control valve and primary steam recover 22a
It is connected, described its top of primary steam recover 22a is provided with a filter 23a, and special-shaped t-bend 7b its one ends are set
It is equipped with two imports and an outlet, an import, outlet and a cyclone separator 18a that air duct 16 passes through special-shaped t-bend 7b
The threeway of lower outlet, corresponding control valve be connected with secondary cyclone separator 18b inlet end, secondary cyclone separator
18b upper outlet is connected by corresponding pipeline, control valve and indirect steam recover 22b.
Cyclone separator 18a and secondary cyclone separator 18b is cyclone separator, described indirect steam recover
Its top of 22b is provided with aflter-fillter 23b.
It is arranged at the side of sterilizing separator to described cleaning device, and described cleaning device includes support, heat and handed over
Parallel operation 20, reflux pump 26, feed pump 29, pure water pot 1, acid solution tank 2, alkali liquid tank 3, peep hole, blow-down pipe, pressure gauge etc..Heat
Exchanger 20, reflux pump 26 and feed pump 29 are arranged on corresponding support.Described heat exchanger 20 is heat-exchangers of the plate type.
It cleans the port of export of the flow container including pure water pot 1, acid solution tank 2 and the/bottom of alkali liquid tank 3 and passes through corresponding three respectively
The inlet end of logical, control valve, pipeline and heat exchanger 20 is connected, and its exit end of heat exchanger 20 passes through pipeline and feed pump
29 inlet end connection.
The Butterworth Hatch on the top of feed hopper 13 that the exit end of described feed pump 29 passes through flexible pipe and device for charging material
Connection.The refluxing opening one end at the top of pure water pot 1, acid solution tank 2 and alkali liquid tank 3 passes through threeway, corresponding control valve and pipe
Road is connected with the port of export of reflux pump 26.
The arrival end of described reflux pump 26 is another by flexible pipe and the special-shaped t-bend 7b's of described sterilizing separator
Import is connected, and described pure water pot 1, acid solution tank 2, the top of alkali liquid tank 3 are respectively arranged with peep hole, blow-down pipe, pressure gauge,
The entrance point of the port of export of the feed hopper 13 of described device for charging material and the rotary valve 14 of described sterilizing separator connects
Connect, described sterilizing its one end of air duct 16 of separator is heated by the air of corresponding control valve and gas generator
The threeway connection of the exit end of device 6, one end of mixing duct 15 of described sterilizing separator and the abnormity of gas generator
Threeway 7a outlet connection.
During operation, powder material is put into raw material memory 10, transported material to by material lifting conveyer 11
Feed hopper 13, opens rotary valve 14, and powder material enters mixing duct, starts gas generator, and air pump 5 sends into air
Air heater 6, what the steam and air pump 5 that special-shaped t-bend 7a produces steam generator 8 were heated through air heater 6
Corresponding mixing duct is imported after air mixing, steam carries out high-temperature sterilization to powder material, while powder material is blown into one
Secondary cyclone separator 18a, a cyclone separator 18a starts to be separated high-temperature steam and powder material, and high-temperature steam leads to
The top duct of separator 18 is crossed to carry out high-temperature steam into corresponding primary steam recover 22a, primary steam recover 18a
Reclaim, filter, powder material is entered by the threeway of separator 18a bottoms is sent to air heater 6 by air pump 5 again, passes through
Powder material Jing Guo first separation is sent into secondary cyclone separator 18b, secondary cyclone by the air that air heater 6 is heated
Powder material is carried out secondary separation by separator 18b, and the steam isolated enters indirect steam recover by corresponding pipeline
22b is reclaimed, filtered.
In the utility model embodiment 2, its cyclone separator is as shown in figure 3, including separator body 31, separator sheet
The inside of body 31, which has, can make to set in the cyclonic separation chamber 32 that the air-flow of dust-laden internally rotates, separator body 31
Be equipped with for the air-flow of dust-laden is introduced to cyclonic separation chamber entrance 33, after dust is by cyclonic separation by air-flow from
The exhaust outlet 35 of described cyclonic separation chamber discharge and after dust is by cyclonic separation by dust from the row of cyclonic separation chamber 32
The ash port 34 gone out, the inside of entrance 33, exhaust outlet 35, ash port 34 with cyclonic separation chamber 32 is connected.The embodiment
In, cyclonic separation chamber 32 includes top cyclonic separation chamber 36 and bottom cyclonic separation chamber 37, and top cyclonic separation chamber 36 is in interior
The truncated cone-shaped that footpath is tapered into from top to down, both handing-over of top cyclonic separation chamber 36 and bottom cyclonic separation chamber 37, and
The two cavity wall smoothly transits at the place of connecting.Exhaust outlet 35 is located at the upper end of top cyclonic separation chamber 36, ash port 34
In the bottom of bottom cyclonic separation chamber 37, air-flow rotates, under in top cyclonic separation chamber 36 around first axle 38
Rotated in portion's cyclonic separation chamber 37 around second axis 39, first axle 37 is a straight line, second axis 39 and first axle
Line 39 is in the same plane and both intersect at a point.In the embodiment, second axis can for line or broken line always or
Curve, and the tangent line of first axle 38 and second axis 39 or second axis 39 in intersection is in be more than 90 folders for being less than 180 °
In angle a, embodiment, second axis 39 is a straight line, and the angle a of first axle 38 and second axis 39 is 115 °, the second axle
Line 39 through ash port 24 end face where plane, and second axis 39 with the plane where the end face of ash port 24 in phase
Angle b at friendship is 85 °.
In the utility model embodiment 3, its separator is as shown in figure 4, the separator is a centrifugal cyclone separator 41 is
Water conservancy diversion separation spiral ring flat-plate 42 is arranged with one cylinder, its housing internal perisporium of centrifugal cyclone separator 41 from bottom to top, respectively
The axial direction line for being opened in the bottom of centrifugal cyclone separator 41 and the entrance 44 on top and outlet 45 is separated with water conservancy diversion respectively
The rotating curve of spiral ring flat-plate 42 is tangent so that the boiler smoke for entering centrifugal cyclone separator 41 is formed in its inner chamber from lower
On make the flue dust of centrifugal rotational flow and separated, make hollow bulb and/or water conservancy diversion point of its smokeshade from centrifugal cyclone separator
Fallen into from spiral ring flat-plate in the collecting chamber 43 of its underpart.
In the utility model embodiment 4, its separator is as shown in figure 5, centrifugal cyclone separator 41 is in a truncated cone-shaped, and it is led
Flow separation spiral ring flat-plate 42 and its housing are reduced diameter from bottom to top.Remaining structure can be similar with above-described embodiment.
The water conservancy diversion of centrifugal cyclone separator separates spiral ring flat-plate from its external diameter（It is connected with its housing internal perisporium）Side is toward internal diameter（By it
Center line）Side is downward or upper oblique, further to improve separating effect.
In the utility model embodiment 5, as shown in fig. 6, the steam generator of its gas generator includes housing, housing
The calandria 51 of interior setting, steam flow channel, the two ends of steam flow channel are respectively water inlet 54 and go out to steam mouth 52.Such as Fig. 3, Fig. 4 institute
Show, steam flow channel is set to spiral shape stainless steel metal pipe（Spiral metal coil pipe）, heating tube 53 is set to spiral shape（Spiral
Formula metal coil pipe）, heating tube coated by stainless steel metal pipe, and the direction of spiraling of heating tube and stainless steel metal pipe is mutually perpendicular to,
Heating tube is by metal tube clad.Metal tube is set to stainless steel tube.Steam generator can install temperature detect switch (TDS) and TEMP
Device.
When steam generator works, aqueous water enters in stainless steel tube from water inlet, after stainless steel tube, due to pipe
Footpath is limited, and aqueous water can be caused quickly to heat vaporization, via helical pipe, heat transfer is fully completed, finally by going out to steam mouth spray
Go out steam.
In the embodiment 6 of powder material sterilizing-drying conveying cleaning integral system of the present utility model, its control device
Including intelligent controller, this intelligent controller is a PLC.It is electrically-controlled valve in the rotary valve 14 of sterilizing separator, it is automatically controlled
Electric signal is connected to PLC to the calandria of valve and its steam heater respectively.Intellectual automatic control is implemented by PLC
System.
Claims (2)
1. a kind of full closed aseptic intelligent integral pharmacy system, device for charging material, gas generator, sterilizing separator,
Cleaning device, the sterilizing separator includes a separator and second separator and its corresponding Steam Recovery device, described
Separator is a centrifugal cyclone separator, it is characterized in that being arranged with described its perisporium of centrifugal cyclone separator along its axis direction
Water conservancy diversion separates spiral ring flat-plate, and the axial direction line of the bottom of centrifugal cyclone separator and the entrance and exit on top is opened in respectively
The rotating curve for separating spiral ring flat-plate with the water conservancy diversion respectively is tangent.
2. full closed aseptic intelligent integral pharmacy system according to claim 1, it is characterized in that the centrifugal cyclone is separated
The water conservancy diversion of device separates spiral ring flat-plate, and it is tilted obliquely downward or upward from external diameter side toward internal diameter side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621234670.0U CN206566222U (en) | 2016-11-17 | 2016-11-17 | A kind of full closed aseptic intelligent integral pharmacy system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621234670.0U CN206566222U (en) | 2016-11-17 | 2016-11-17 | A kind of full closed aseptic intelligent integral pharmacy system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206566222U true CN206566222U (en) | 2017-10-20 |
Family
ID=60062408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621234670.0U Active CN206566222U (en) | 2016-11-17 | 2016-11-17 | A kind of full closed aseptic intelligent integral pharmacy system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206566222U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106619122A (en) * | 2016-11-17 | 2017-05-10 | 宜春万申制药机械有限公司 | Fully-closed sterile intelligent integrated pharmaceutical system |
-
2016
- 2016-11-17 CN CN201621234670.0U patent/CN206566222U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106619122A (en) * | 2016-11-17 | 2017-05-10 | 宜春万申制药机械有限公司 | Fully-closed sterile intelligent integrated pharmaceutical system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: No. 28, Chunfeng Road, Yichun Economic Development Zone, Yichun City, Jiangxi Province Patentee after: Yichun Wanshen Intelligent Equipment Co.,Ltd. Address before: No. 28, Chunfeng Road, Yichun Economic Development Zone, Yichun City, Jiangxi Province Patentee before: YICHUN WANSHEN PHARMACEUTICAL MACHINERY Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder |