CN105157394B - Pharmacy bacterium dregs innocent processing system - Google Patents
Pharmacy bacterium dregs innocent processing system Download PDFInfo
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- CN105157394B CN105157394B CN201510430513.0A CN201510430513A CN105157394B CN 105157394 B CN105157394 B CN 105157394B CN 201510430513 A CN201510430513 A CN 201510430513A CN 105157394 B CN105157394 B CN 105157394B
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Abstract
The invention discloses a kind of pharmacy bacterium dregs innocent processing system, including：Several level-one bacteria residue desiccation machines, pharmacy bacteria residue are uniformly transmitted to by transmission device in each level-one bacteria residue desiccation machine；Two level bacteria residue desiccation machine, the discharge port of each level-one bacteria residue desiccation machine are connect by particle conveyer with the feed inlet of the two level bacteria residue desiccation machine；Divide gas bag, the air inlet for dividing gas bag respectively with the level-one bacteria residue desiccation machine and two level bacteria residue desiccation machine connects；Cyclone dust collectors, respectively the exhaust outlet with the level-one bacteria residue desiccation machine and two level bacteria residue desiccation machine connect；Steam trap is connect with the air outlet of the cyclone dust collectors；Aeration tower is connect with the air outlet of the steam trap；Vent gas treatment tower is connect with the air outlet of the aeration tower.The present invention efficiently solves the technical issues of pharmacy bacteria residue is not easy to deal carefully with.
Description
Technical field
The present invention relates to a kind of industry, rubbish Disposal System, it is more particularly related to a kind of pharmacy bacteria residue
Innocuity disposal system.
Background technology
With the gradually development of pharmaceutical technology, the gradual perfection of pharmaceutical field is pushed, the pharmacy amount of pharmacy producer is quick
Increase, various drugs are provided for common people, however, with the increase of pharmacy amount, inevitably produce various each
The pharmacy bacteria residue of sample, general producer by pharmacy bacteria residue by directly carrying out drying burning disposal.
But this processing mode is disadvantageous in that, there are many moisture in pharmacy bacteria residue, and quite sticky, using common dry
Dry machine is not easy the fast and reliable drying of pharmacy bacteria residue, and drying process is slow and drying effect is bad so that during the burning process,
The burning of pharmacy bacteria residue is not thorough and generates a large amount of pernicious gas, pollutes environment, largely there is soya-bean oil, esters in pharmacy bacteria residue
The harmful components such as class, carcinogenic substance lead to that in drying process pernicious gas, dust and smog can be generated, if in pharmacy bacteria residue
Drying is not thorough, and root can cause these harmful substances to pollute environment during the burning process.
Invention content
It is an object of the invention to solve at least the above, and provide the advantages of at least will be described later.
It is a still further object of the present invention to provide a kind of pharmacy bacterium dregs innocent processing systems, which can be quickly and effectively
Pharmacy bacteria residue is dried, and the system uses the drying process of totally-enclosed, the exhaust gas in drying process is handled, most
No pollution discharge is realized eventually, efficiently solves the technical issues of pharmacy bacteria residue is not easy to deal carefully with.
In order to realize these purposes and other advantages according to the present invention, a kind of pharmacy bacterium dregs innocent processing system is provided
System, including：
Several level-one bacteria residue desiccation machines, each level-one bacteria residue desiccation machine are set up in parallel, and pharmacy bacteria residue passes through biography
Device is sent uniformly to be transmitted in each level-one bacteria residue desiccation machine；
Two level bacteria residue desiccation machine, the discharge port of each level-one bacteria residue desiccation machine pass through particle conveyer and described two
The feed inlet connection of grade bacteria residue desiccation machine；
Point gas bag, accommodated inside have desiccation steam, it is described divide gas bag respectively with the level-one bacteria residue desiccation machine and two level
The air inlet connection of bacteria residue desiccation machine；
Cyclone dust collectors, respectively the exhaust outlet with the level-one bacteria residue desiccation machine and two level bacteria residue desiccation machine connect；
Steam trap is connect with the air outlet of the cyclone dust collectors；
Aeration tower is connect with the air outlet of the steam trap；
Vent gas treatment tower is connect with the air outlet of the aeration tower.
Preferably, the level-one bacteria residue desiccation machine is identical with the structure of two level bacteria residue desiccation machine, bacteria residue desiccation machine it is specific
Structure is：
Rack is placed on the ground, and the rack both ends are respectively arranged with support base, are arranged at intervals on the support base
There are two bearings；
Host is erected in the rack, and the host is made of cylinder with the cover for being arranged on the cylinder upper end,
Two arc-shaped depression portions are symmetrically divided into " W " type airtight cavity structure, the cylinder body bottom inside the host, the cylinder
Outer wall is set as hollow jacket structure, and the cylinder upper wall offers several thermal medium air inlets, the thermal medium air inlet
Gas bag is divided to connect with described, the cylinder body bottom offers several the first refluxing openings, is offered on the side wall of the cylinder both ends
Two through-holes, the cylinder body bottom offer discharge port；
Paddle shaft is vacantly arranged in the cavity, and the paddle shaft is divided into active paddle shaft and driven paddle shaft, institute
It states active paddle shaft and driven paddle shaft is disposed in two arc-shaped depression portions, the blade shaft end head is respectively from described
It is drawn in through-hole, the paddle shaft is cylindrical cavity structure, and the cavity center is provided with drainpipe, is welded on the paddle shaft
There are several hollow paddles, connected respectively with the cylindrical cavity with the drainpipe inside the hollow paddle.
Preferably, bacteria residue feed inlet, access hole, observation window, hot wind air inlet and exhaust outlet are provided in the cover,
The outlet of the feed inlet and the transmission device connects, and the hot wind air inlet divides gas bag to connect with described, the exhaust outlet and
The cyclone dust collectors connection.
Preferably, the bearing of the rack side is run through in first end of paddle shaft, two paddle shafts the
It is respectively arranged with toothed disc on one end, two toothed discs engagement connections, the feed inlet is arranged on the paddle shaft the
The first side in one end.
Preferably, driving mechanism is further included, is made of driving motor and gearbox, first end of active paddle shaft
Outermost end on be additionally provided with paddle shaft turntable, the gearbox output turntable is connect with the paddle shaft turntable.
Preferably, the bearing of the rack opposite side, each described blade are run through in second end of paddle shaft
Rotary joint is provided on the second end of axis, steam inlet and the second refluxing opening, the steaming are provided on the rotary joint
Vapour air inlet is connected with the cavity, and second refluxing opening is connected with the drainpipe, the steam inlet with described point
Gas bag connects, and the discharge port is arranged on the first side of the second end.
Preferably, radially opposite sides are welded with two rows of hollow paddles, two rows of hollow paddle phases on the paddle shaft
Mutual stagger setting, and the welding angle of each hollow paddle bottom and paddle shaft circumferential direction is between 80 °~90 °,
The active paddle shaft and the inwardly rotation, and the hollow paddle on the active paddle shaft and driven paddle shaft simultaneously of driven paddle shaft
Leaf mutually staggers 90 ° and is connected in a manner that complementation is engaged.
Preferably, the hollow paddle is in covering of the fan wedge structure, is had by the big end of blade, blade small end and company
It is connected on intermediate covering of the fan portion to form, the big end of blade is higher than the blade small end, and the big end of the blade is arranged on
The tail end of the hollow paddle direction of rotation.
Preferably, the big end upper end of the blade is provided with scraper plate, and the discharge port upper end is provided with striker plate.
Preferably, the host is inclined in the rack, and first end is set higher than second end, institute
It states and is connected inside hollow paddle by air inlet pipe with the cavity, the air inlet pipe is extended on inside the hollow paddle,
The air inlet pipe is positioned close on the paddle shaft of the blade small end, is offered on the paddle shaft and the hollow paddle
The backwater hole of inside connection, the backwater hole pass through pipeline and the drainpipe close to the big end of the blade, the backwater hole
Connection.
The present invention includes at least following advantageous effect：
1st, using the drying process flow of stagewise, the dehydration degree of pharmacy bacteria residue is improved；
2nd, using double blade shafts drying machine, the drying and dehydrating ability of unit is improved, while equipment is greatly improved
Heat utilization efficiency；
3rd, using intelligentized drive control mode, the speed of drying process is effectively adjusted；
4th, using totally enclosed process flow, by the exhaust gas timely processing in processing procedure, high-temperature steam is recycled,
The energy consumption of equipment is reduced, while realizes that no pollution discharges.
Part is illustrated to embody by further advantage, target and the feature of the present invention by following, and part will also be by this
The research and practice of invention and be understood by the person skilled in the art.
Description of the drawings
Fig. 1 is the dimensional structure diagram of the desiccation machine；
Fig. 2 is the side structure schematic view of the desiccation machine；
Fig. 3 is the desiccation machine internal structure schematic diagram；
Fig. 4 is the overlooking the structure diagram of the desiccation machine；
Fig. 5 is the present invention looks up structural representation of the desiccation machine；
Fig. 6 is that the desiccation machine and the driving mechanism turn distribution structure schematic diagram；
Fig. 7 is the assembling structure schematic diagram of the active paddle shaft and the driven paddle shaft；
Fig. 8 is the assembling structure schematic diagram of the paddle shaft and the hollow paddle；
Fig. 9 is the dimensional structure diagram of the paddle shaft and the hollow paddle.
Specific embodiment
The present invention is described in further detail below in conjunction with the accompanying drawings, to enable those skilled in the art with reference to specification text
Word can be implemented according to this.
It should be appreciated that such as " having ", "comprising" and " comprising " term used herein do not allot one or more
The presence or addition of a other element or combinations.
As shown in Figs. 1-5, the present invention provides a kind of pharmacy bacterium dregs innocent processing system of household, including：
Several level-one bacteria residue desiccation machines, each level-one bacteria residue desiccation machine is set up in parallel, and in the present embodiment, is used
Two level-one bacteria residue desiccation machines being set up in parallel, two level-one bacteria residue desiccation machines are arranged on sustained height, and pharmacy bacteria residue passes through biography
Device is sent uniformly to be transmitted in each level-one bacteria residue desiccation machine；
Two level bacteria residue desiccation machine, the discharge port of each level-one bacteria residue desiccation machine pass through particle conveyer and described two
The feed inlet connection of grade bacteria residue desiccation machine, two level bacteria residue desiccation machine are arranged in relatively low height so that through level-one bacteria residue desiccation
The dried bacteria residue of machine is instantaneously entered in two level bacteria residue desiccation machine；
Point gas bag, it is described to divide gas bag by main steam range respectively with described one for the steam needed for stocking system desiccation
Grade bacteria residue desiccation machine is connected with the air inlet of two level bacteria residue desiccation machine；
Cyclone dust collectors, respectively the exhaust outlet with the level-one bacteria residue desiccation machine and two level bacteria residue desiccation machine connect, it is special
Be not two level desiccation machine since material is done, Dust Capacity is more, must be equipped with cyclone dust collectors, cyclone dust collectors effectively remove desiccation
Large dust particle in machine exhaust gas；
Steam trap is connect with the air outlet of the cyclone dust collectors, and the gas that desiccation production line is evaporated passes through
Pipeline, which is sent into spray column, carries out steam-water separation；
Aeration tower is connect with the air outlet of the steam trap, for the little particle dust in exhaust gas of going out；
Vent gas treatment tower is connect with the air outlet of the aeration tower, in exhaust gas of going out harmful substance, stink,
And sterilization processing is carried out, realize no pollution discharge.
Concrete principle is as follows, divides gas bag to providing 150 degrees Celsius to 180 degrees Celsius for level-one, two level bacteria residue desiccation machine
Steam, pharmacy bacteria residue are initially pre-heated to 120 degrees centigrades, can effectively strengthen desiccation effect, then equal by transmission device
Even to be transported in each level-one bacteria residue desiccation machine, the structure of each bacteria residue desiccation machine is identical, in each bacteria residue desiccation machine
The rotating mechanism rotating speed in portion is maintained at 6~10rap/min, after the drying of level-one desiccation machine, moisture in bacteria residue from
80% or so is reduced to 50% or so, while volume-diminished, ensures after level-one drying and other treatment, two level-one bacteria residue desiccation machines
Discharging can smoothly adapt to the capacity of two level bacteria residue desiccation machine, without the two level bacteria residue desiccation machine inner space saturation for being, two
The discharge port of platform two level bacteria residue desiccation machine is connected, and be and desiccation discharging is by particle transmission crusher machine and transmits such as two level
Bacteria residue desiccation machine, after two level bacteria residue desiccation machine desiccation, bacteria residue moisture is reduced to 20% or so, becomes granular solid,
Grain size is in grade, and discharging volume is greatly reduced compared to feed volume, so as to complete the drying and other treatment of bacteria residue.Meanwhile often
The waste gas outlet of platform bacteria residue desiccation machine is connected with cyclone dust collectors, is dusted processing, be then fed into steam trap into
Row dehydration is re-fed into the fine dust particles removed in aeration tower in gas, is finally sent to vent gas treatment tower, carries out
The processing of harmful substance is carried out in totally enclosed environment in processing procedure, no pollution discharge is realized, so as to solve not
The technical issues of easily dealing carefully with saves waste processing cost, while realize environmentally friendly tupe for enterprise,
With great promotional value.
In above-mentioned technical proposal, the level-one bacteria residue desiccation machine is identical with the structure of two level bacteria residue desiccation machine, bacteria residue desiccation
The concrete structure of machine is：
Rack 100 is placed on the ground, and 100 both ends of rack are respectively arranged with support base 110, described in each
Bearing 111 there are two being arranged at intervals on support base 110；
Host is erected in the rack 100, and the host is by cylinder 210 and is arranged on 210 upper end of cylinder
Cover 220 is formed, and two arcs are divided into " W " type airtight cavity structure, 210 bottom symmetrical of cylinder inside the host
Recess portion, as shown in fig. 7, the outer wall of the cylinder 210 is set as 213 structure of hollow jacket, for storing high-temperature steam, to bacteria residue
Be thermally dried, 210 upper wall of cylinder offers several thermal medium air inlets 211, the thermal medium air inlet 211 with
Described point of gas bag connection, 210 bottom of cylinder offers several the first refluxing openings 212, for being produced in hollow jacket 213
Raw condensed water carries out timely drainage sunk well, increases the heat utilization efficiency of steam, two are offered on the 210 both ends side wall of cylinder
A through-hole, 210 bottom of cylinder offer discharge port 213, as shown in Figure 5；
Paddle shaft is vacantly arranged in the cavity, and the paddle shaft is divided into active paddle shaft 310 and driven paddle shaft
320, the two is arranged side by side, and the active paddle shaft 310 and driven paddle shaft 320 are disposed on two arc-shaped depression portions
In, the blade shaft end head is drawn from the through-hole respectively, and the paddle shaft is cylindrical cavity structure, and the cavity center is set
Drainpipe 350 is equipped with, as shown in figure 8, several hollow paddles 340 are welded on the paddle shaft, in the hollow paddle 340
Portion connects respectively with the cylindrical cavity with the drainpipe 350.
In above-mentioned technical proposal, be provided in the cover 220 bacteria residue feed inlet 221, access hole 223, observation window 225,
Hot wind air inlet 224 and exhaust outlet 222, the feed inlet 221 are connected with transmission device outlet, the hot wind air inlet
224 divide gas bag to connect with described, and the exhaust outlet 222 is connect with the cyclone dust collectors.
In above-mentioned technical proposal, first end of paddle shaft run through 100 side of rack the bearing 111, two
Toothed disc 311 is respectively arranged on a 310 and 320 first end of the paddle shaft, two engagements of toothed disc 311 connect,
So as to fulfill inside rotation is synchronized, the feed inlet 221 is arranged on the first side of paddle shaft first end.
Driving mechanism 500 is further included in above-mentioned technical proposal, in processing system, by driving motor 510 and gearbox 520
It forms, driving motor 510 is controlled by frequency conversion servo system, also set up in the outermost end of 310 first end of active paddle shaft
There is paddle shaft turntable 312, the gearbox 520 exports turntable 530 and connect with the paddle shaft turntable 312, as shown in Figure 6.
The bearing 111 of 100 opposite side of rack is run through in above-mentioned technical proposal, second end of paddle shaft, often
Rotary joint 400 is provided on one second end of paddle shaft, steam inlet is provided on the rotary joint 400
410 and second refluxing opening 420, the steam inlet 410 connected with the cavity, provided for paddle shaft and hollow paddle 340
Steam, second refluxing opening 420 are connected with the drainpipe 350, and the condensed water in hollow paddle 340 is passed through drainpipe
350 discharge body from the second refluxing opening 420 so that condensed water separates with steam, improves the thermal efficiency of steam, and conventional drying is set
Standby heat utilization efficiency is 30% or so, and the desiccation machine thermal efficiency in the present invention can reach more than 90%, the steam inlet
Mouth 410 divides gas bag to connect with described, and the discharge port 213 is arranged on the first side of the second end so that bacteria residue passes through from the beginning to the end
It crosses inside desiccation machine, improves drying effect.
In above-mentioned technical proposal, radially opposite sides are welded with two rows of hollow paddles 340 on the paddle shaft, such as Fig. 9 institutes
Show, two rows of hollow paddles 340 mutually stagger setting, and each described 340 bottom of hollow paddle and paddle shaft week
To welding angle between 80 °~90 ° so that the hollow paddle on paddle shaft is twist pushed ahead to by bacteria residue, institute
The inwardly rotation simultaneously of active paddle shaft 310 and driven paddle shaft 320 is stated, plays stirring well, reversion, shear effect, bacterium
Material of the slag when having just enter into desiccation machine for flowing shape after bringing-up section enters expansion arc, starts a large amount of evaporation moisture, gradually
Solid-like is become from flowing shape.That is the effect of hollow paddle is exactly that the bacteria residue actuating of flowing shape is got up to reach rapid evaporation moisture
Effect.And the hollow paddle 340 on the active paddle shaft 310 and driven paddle shaft 320 is mutually staggered 90 ° and is engaged with complementation
Mode connect, during rotation, the blade being meshed plays the role of squeezing, stir, crush and pushing to bacteria residue, such as
Shown in Fig. 7.
In another embodiment, the hollow paddle 340 is in covering of the fan wedge structure, as shown in figure 8, it is with big by blade
End 341, blade small end 342 and the covering of the fan portion composition being connected between, the big end 341 of blade is higher than the blade
Small end 342, and the big end 341 of the blade is arranged on the tail end of 340 direction of rotation of hollow paddle.
In above-mentioned technical proposal, big 341 upper end of end of blade is provided with scraper plate 380, the main function of scraper plate 380
It is：Ensure that bacteria residue is fully stirred；The bacteria residue for being attached to desiccation machine inner wall is cleaned up.213 upper end of discharge port is provided with
Striker plate 330, the effect of striker plate is extremely important, can adjust height of the bacteria residue in discharging according to working condition, also controllably
The moisture content of bacteria residue after system is dry.
In above-mentioned technical proposal, the host is inclined in the rack 100, and first end is set higher than described
Second end so that condensed water can take advantage of a situation, be discharged from body in time, the relative increase contact surface of bacteria residue and calandria
Product, improves steam thermal utilization, is connected inside the hollow paddle 340 by air inlet pipe 370 with the cavity, the air inlet
Pipe 370 is extended on inside the hollow paddle, and the air inlet pipe 370 is positioned close to the paddle shaft of the blade small end
On so that condensed water will not be entered in steam pipe, improve the heat utilization efficiency of steam naturally, offered on the paddle shaft with
The backwater hole 360 connected inside the hollow paddle, the backwater hole pass through pipe close to the big end of the blade, the backwater hole
Road is connected with the drainpipe, and condensed water can take advantage of a situation with the direction of rotation of paddle shaft and enter in backwater hole 360, pass through draining
Pipe discharges body so that condensed water will not gather in hollow paddle, that is, condensed water separates with steam, it is achieved thereby that school
The steam thermal utilization of original text.
Although the embodiments of the present invention have been disclosed as above, but its be not restricted in specification and embodiment it is listed
With it can be fully applied to various fields suitable for the present invention, for those skilled in the art, can be easily
Realize other modification, therefore without departing from the general concept defined in the claims and the equivalent scope, it is of the invention and unlimited
In specific details and legend shown and described herein.
Claims (5)
1. a kind of pharmacy bacterium dregs innocent processing system, which is characterized in that including：
Several level-one bacteria residue desiccation machines, each level-one bacteria residue desiccation machine are set up in parallel, and pharmacy bacteria residue is filled by transmitting
It puts and is uniformly transmitted in each level-one bacteria residue desiccation machine；
Two level bacteria residue desiccation machine, the discharge port of each level-one bacteria residue desiccation machine pass through particle conveyer and the two level bacterium
The feed inlet connection of slag desiccation machine；
Point gas bag, accommodated inside have desiccation steam, it is described divide gas bag respectively with the level-one bacteria residue desiccation machine and two level bacteria residue
The air inlet connection of desiccation machine；
Cyclone dust collectors, respectively the exhaust outlet with the level-one bacteria residue desiccation machine and two level bacteria residue desiccation machine connect；
Steam trap is connect with the air outlet of the cyclone dust collectors；
Aeration tower is connect with the air outlet of the steam trap；
Vent gas treatment tower is connect with the air outlet of the aeration tower；
Wherein, the level-one bacteria residue desiccation machine is identical with the structure of two level bacteria residue desiccation machine, and the concrete structure of bacteria residue desiccation machine is：
Rack is placed on the ground, and the rack both ends are respectively arranged with support base, and two are arranged at intervals on the support base
A bearing；
Host is erected in the rack, and the host is made of cylinder with the cover for being arranged on the cylinder upper end, described
Inside host two arc-shaped depression portions, the outer wall of the cylinder are symmetrically divided into " W " type airtight cavity structure, the cylinder body bottom
Hollow jacket structure is set as, the cylinder upper wall offers several thermal medium air inlets, the thermal medium air inlet and institute
A point gas bag is stated to connect, the cylinder body bottom offers several the first refluxing openings, opened up on the side wall of the cylinder both ends there are two
Through-hole, the cylinder body bottom offer discharge port；
Paddle shaft is vacantly arranged in the cavity, and the paddle shaft is divided into active paddle shaft and driven paddle shaft, the master
Dynamic paddle shaft and driven paddle shaft are disposed in two arc-shaped depression portions, and the blade shaft end head is respectively from the through-hole
Middle extraction, the paddle shaft are cylindrical cavity structure, and the cavity center is provided with drainpipe, if being welded on the paddle shaft
A hollow paddle is done, is connected respectively with the cylindrical cavity with the drainpipe inside the hollow paddle；
Bacteria residue feed inlet, access hole, observation window, hot wind air inlet and exhaust outlet, the feed inlet are provided in the cover
It exports and connects with the transmission device, the hot wind air inlet divides gas bag to connect with described, and the exhaust outlet is removed with the whirlwind
Dirt device connects；
The hollow paddle is in covering of the fan wedge structure, has by blade big end, blade small end and is connected between
Covering of the fan portion is formed, and the big end of blade is higher than the blade small end, and the big end of the blade is arranged on the hollow paddle
The tail end of leaf direction of rotation, the big end upper end of blade are provided with scraper plate, and the discharge port upper end is provided with striker plate；
The host is inclined in the rack, and first end is set higher than second end, the hollow paddle
Inside is connected by air inlet pipe with the cavity, and the air inlet pipe is extended on inside the hollow paddle, the air inlet pipe
It is positioned close on the paddle shaft of the blade small end, offers what is connected with hollow paddle inside on the paddle shaft
Backwater hole, the backwater hole are connected close to the big end of the blade, the backwater hole by pipeline with the drainpipe.
2. pharmacy bacterium dregs innocent processing system as described in claim 1, which is characterized in that first end of paddle shaft is passed through
The bearing of the rack side is worn, toothed disc, two teeth are respectively arranged on two first ends of paddle shaft
Wheel disc engagement connection, the feed inlet are arranged on the first side of paddle shaft first end.
3. pharmacy bacterium dregs innocent processing system as claimed in claim 2, which is characterized in that driving mechanism is further included, by
Driving motor and gearbox are formed, and paddle shaft turntable is additionally provided in the outermost end of first end of active paddle shaft, described
Gearbox output turntable is connect with the paddle shaft turntable.
4. pharmacy bacterium dregs innocent processing system as claimed in claim 3, which is characterized in that second end of paddle shaft is passed through
The bearing of the rack opposite side is worn, rotary joint, the rotation are provided on each described second end of paddle shaft
Steam inlet and the second refluxing opening are provided on connector, the steam inlet is connected with the cavity, second reflux
Mouth is connected with the drainpipe, and the steam inlet divides gas bag to connect with described, and the discharge port is arranged on the second end
First side.
5. pharmacy bacterium dregs innocent processing system as claimed in claim 4, which is characterized in that radially opposite sides on the paddle shaft
Two rows of hollow paddles are welded with, two rows of hollow paddles mutually stagger setting, and each described hollow paddle bottom
Welding angle with paddle shaft circumferential direction is between 80 °~90 °, and the active paddle shaft and driven paddle shaft are simultaneously to inward turning
Turn, and the active paddle shaft and the hollow paddle on driven paddle shaft mutually stagger 90 ° and connected in a manner that complementation is engaged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510430513.0A CN105157394B (en) | 2015-07-21 | 2015-07-21 | Pharmacy bacterium dregs innocent processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510430513.0A CN105157394B (en) | 2015-07-21 | 2015-07-21 | Pharmacy bacterium dregs innocent processing system |
Publications (2)
| Publication Number | Publication Date |
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| CN105157394A CN105157394A (en) | 2015-12-16 |
| CN105157394B true CN105157394B (en) | 2018-06-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510430513.0A Expired - Fee Related CN105157394B (en) | 2015-07-21 | 2015-07-21 | Pharmacy bacterium dregs innocent processing system |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107075927A (en) * | 2015-12-22 | 2017-08-18 | 苏州美泓环保科技有限公司 | A kind of oil landwaste mud processing equipment and its method |
| CN105670657B (en) * | 2016-02-01 | 2019-08-02 | 苏州美泓环保科技有限公司 | The innoxious and recycling processing method of municipal sludge |
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| CN102532603A (en) * | 2011-12-31 | 2012-07-04 | 南京天华化学工程有限公司 | Flame retardant drying/cooling method |
| CN102538426A (en) * | 2012-02-29 | 2012-07-04 | 南京天华化学工程有限公司 | Continuous drying process and equipment for cyclohexanone oximation catalyst |
| CN203405066U (en) * | 2013-06-20 | 2014-01-22 | 常州力马化工机械有限公司 | Paddle drying machine |
| CN103968657A (en) * | 2014-05-28 | 2014-08-06 | 常州市金陵干燥设备有限公司 | High vacuum multi-axis paddle dryer |
| CN205027081U (en) * | 2015-07-21 | 2016-02-10 | 苏州市自力化工设备有限公司 | Pharmacy fungus sediment innocent treatment system |
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| CN105157394A (en) | 2015-12-16 |
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