CN207112777U - A kind of pharmaceutical factory's water circulation system - Google Patents
A kind of pharmaceutical factory's water circulation system Download PDFInfo
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- CN207112777U CN207112777U CN201720791108.6U CN201720791108U CN207112777U CN 207112777 U CN207112777 U CN 207112777U CN 201720791108 U CN201720791108 U CN 201720791108U CN 207112777 U CN207112777 U CN 207112777U
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Abstract
The utility model discloses a kind of pharmaceutical factory's water circulation system, including boiler module, prepared slices of Chinese crude drugs workshop module and Water Sproading module, boiler module, prepared slices of Chinese crude drugs workshop module and Water Sproading module are interconnected；Boiler module is used to provide pharmaceutical purpose high-temperature steam to pharmaceutical factory's water circulation system for moisturizing and to prepared slices of Chinese crude drugs workshop module；Prepared slices of Chinese crude drugs workshop module includes more pharmaceutical processing equipments, for being processed to medicinal material；Water Sproading module is used to recycle waste vapour caused by the module pharmacy procedure of prepared slices of Chinese crude drugs workshop, caused hot and humid waste vapour in pharmacy procedure can be reclaimed liquefaction discharge or be continued cycling through and used for the module pharmacy of prepared slices of Chinese crude drugs workshop by the utility model by Water Sproading module, not only reduce environmental pollution, greenhouse effects are avoided, also allow the health of plant personnel to be ensured.
Description
Technical field
It the utility model is related to a kind of sewage treatment equipment, more particularly to a kind of pharmaceutical factory's water circulation system.
Background technology
At present, in pharmaceutical factory, to during the dixie cup of Chinese medicine, it is necessary to be dried to medicinal material, warm water/hot-water soak, wet
The techniques such as steaming.
But there is following defect in existing pharmaceutical factory's pharmacy procedure：
(1) substantial amounts of tail gas can be produced in the process to Chinese medicine to produce, and environment is polluted, also to pharmacy car
Between internal environment and personnel health form influence.
(2) due to the caused hot and humid a large amount of heat energy of tail gas intension in pharmacy procedure, tail gas of leaving discharges extraneous ring
Border can not only accelerate the environmental pollutions such as global warming, also waste the hot and humid vapor with a large amount of heat energy significantly, continue
Pharmaceutical manufacturing line water is wasted, adds production cost.
Utility model content
For overcome the deficiencies in the prior art, the purpose of this utility model is to provide a kind of pharmaceutical factory's water circulation system,
Tail gas caused by pharmacy procedure is carried out reclaiming liquefaction and recycled, reduces environmental pollution, reduces production cost.
The purpose of this utility model adopts the following technical scheme that realization：
A kind of pharmaceutical factory's water circulation system, including boiler module, prepared slices of Chinese crude drugs workshop module and Water Sproading module, it is described
Boiler module, prepared slices of Chinese crude drugs workshop module and the Water Sproading module are interconnected；
Boiler module is used to provide pharmaceutical purpose height to pharmaceutical factory's water circulation system for moisturizing and to prepared slices of Chinese crude drugs workshop module
Warm steam；
Prepared slices of Chinese crude drugs workshop module includes more pharmaceutical processing equipments, for being processed to medicinal material；
Water Sproading module is used to recycle waste vapour caused by the module pharmacy procedure of prepared slices of Chinese crude drugs workshop.
Further, the boiler module includes softened water equipment, water supply tank, boiler and gas-distributing cylinder, the softened water
Equipment, the water supply tank, the boiler, the gas-distributing cylinder pass sequentially through pipeline connection；The softened water equipment and external source
Connection；The gas-distributing cylinder is connected with prepared slices of Chinese crude drugs workshop module by pipeline, is prepared slices of Chinese crude drugs workshop module assignment
Supplying high temperature steam.
Further, prepared slices of Chinese crude drugs workshop module includes mesh-belt drier, baking oven, demulcen pond, medicine boiler, steaming the medicinal hebrs
Machine, the mesh-belt drier, the baking oven, the demulcen pond, the medicine boiler, described steaming the medicinal hebrs machine one end pass through pipeline respectively
It is connected with the gas-distributing cylinder, the other end is connected with the Water Sproading module by pipeline respectively.
Further, the Water Sproading module includes condensate recovering device and waste gas recovery pond；The condensing hot air furnace
The regulator of device is connected with the mesh-belt drier, the baking oven, the demulcen pond, the medicine boiler by pipeline, is used
In high temperature caused by the collection mesh-belt drier, the baking oven, the demulcen pond, medicine boiler processing medicinal material process
High moisture vapor；The draining valve of the condensate recovering device is connected with the water supply tank by pipeline, after recovery is liquefied
Condensed water is discharged into the water supply tank and used for pharmaceutical factory's water circulation system again；
The steaming the medicinal hebrs machine is connected with steaming the medicinal hebrs discharge duct, the steaming the medicinal hebrs discharge duct wear connect the waste gas recovery pond and with
External environment connect, for by after hot and humid waste vapour cooling liquid caused by the steaming the medicinal hebrs mechanism medicine from pharmaceutical factory's water
Discharged in the circulatory system；
The waste gas recovery pond is additionally provided with the drainpipe connected with external environment.
Further, the Water Sproading module also includes softened water tank, soft water water making device and hot-water cylinder, the soft water system
Wetting system is connected with external source and the softened water tank respectively, and soft water is prepared for the softened water tank；Described in the softened water tank connection
Waste gas recovery pond, for being that the waste gas recovery pond supplies to mend soft water；
The hot-water cylinder is connected with the waste gas recovery pond and the condensate recovering device respectively, described useless for reclaiming
After hot water in gas recovery pond, hot water is reclaimed by the condensate recovering device and recirculates use.
Further, the blast pipe peripheral seal of the condensate recovering device is arranged with cooling cylinder, the cooling cylinder both ends
It is connected respectively by pipeline with the softened water tank, one end forms cooling import, and the other end forms coolant outlet, by from described cold
But import is to water filling in the cooling cylinder, and water is discharged into the softened water tank again by the coolant outlet, to described cold
The blast pipe of condensate recover carries out cooling down.
Further, the waste gas recovery pond be provided with for monitor waste gas recovery pond internal temperature first
Temperature inductor；The blast pipe of the condensate recovering device is provided with the second temperature sensing for being used to monitor blast pipe internal temperature
Device；The 3rd temperature inductor for being used for monitoring the softened water tank internal temperature is provided with the softened water tank.
Further, the water supply tank, the waste gas recovery pond, the softened water tank, be equipped with prison in the hot-water cylinder
Control the condensate tank of dehumidifier of water level inside height.
Further, the water supply tank includes the first water supply tank and the second water supply tank, first water supply tank and institute
The second water supply tank is stated to connect by placed in series；The boiler includes the first boiler and the second boiler, first boiler with
Second boiler is connected by placed in series, and first boiler passes through pipeline and second moisturizing with second boiler
Case connects；The waste gas recovery pond include first recovery pond and second recovery pond, it is described first recovery pond and
The second recovery pond is arranged side by side, and the steaming the medicinal hebrs discharge duct is connected to the first recovery pond and described second successively
Pond is reclaimed, and the side wall in the described second recovery pond is passed and connected with external environment.
Compared with prior art, the beneficial effects of the utility model are：
Pharmaceutical factory's water circulation system of the present utility model, by setting boiler module to provide system to prepared slices of Chinese crude drugs workshop module
High-temperature steam needed for medicine, and Water Sproading module is connected with prepared slices of Chinese crude drugs workshop module respectively, to prepared slices of Chinese crude drugs workshop module
Hot and humid waste vapour caused by pharmacy procedure carries out reclaiming liquefaction or the heel row that liquefies goes out the external world, avoids hot and humid waste vapour direct
The external world is discharged in a manner of gas pollution is directly contributed to external environment, and connect boiler module by partially recycled liquefied condensation
Water supplies and is conveyed to boiler module again, is continuing with for prepared slices of Chinese crude drugs workshop module, reduces the waste of water resource, while by
The a large amount of heat energy of intension after hot and humid waste vapour condensation liquefaction, pH value are neutral high quality water, are available for prepared slices of Chinese crude drugs workshop weight
It is new to utilize, reduce the pressure of boiler module, while workshop condition and enterprise employee health are also greatly improved.
Brief description of the drawings
Fig. 1 is the engineering drawing of the utility model pharmaceutical factory water circulation system.
In figure：10th, boiler module；20th, prepared slices of Chinese crude drugs workshop module；30th, Water Sproading module；11st, softened water equipment；12、
Water supply tank；13rd, boiler；14th, gas-distributing cylinder；21st, mesh-belt drier；22nd, baking oven；23rd, demulcen pond；24th, medicine boiler；25th, steaming the medicinal hebrs
Machine；251st, steaming the medicinal hebrs discharge duct；31st, condensate recovering device；32nd, waste gas recovery pond；321st, drainpipe；322nd, the first temperature sense
Answer device；33rd, softened water tank；34th, soft water water making device；331st, the 3rd temperature inductor；311st, cylinder is cooled down；312nd, import is cooled down；
313rd, coolant outlet；314th, second temperature inductor；121st, the first water supply tank；122nd, the second water supply tank；131st, the first boiler；
132nd, the second boiler；323rd, the first recovery pond；324th, the second recovery pond；35th, hot-water cylinder.
Embodiment
Below, with reference to accompanying drawing and embodiment, the utility model is described further, it is necessary to explanation is,
On the premise of not colliding, it can be formed in any combination between various embodiments described below or between each technical characteristic new
Embodiment.
As shown in figure 1, in order to avoid the tail gas in herbal pharmaceutical process is expelled directly out air, environmental pollution, and increase
Add the situation of production cost, the utility model provides a kind of pharmaceutical factory's water circulation system, and pharmaceutical factory's water circulation system includes pot
Oven module 10, prepared slices of Chinese crude drugs workshop module 20 and Water Sproading module 30, boiler module 10, prepared slices of Chinese crude drugs workshop module 20 and
Water Sproading module 30 is interconnected；Boiler module 10 is used to supply moisturizing to pharmaceutical factory's water circulation system and gives prepared slices of Chinese crude drugs workshop mould
Block 20 provides pharmaceutical purpose high-temperature steam；Prepared slices of Chinese crude drugs workshop module 20 includes more pharmaceutical processing equipments, for being carried out to medicinal material
Working process；Water Sproading module 30 is used to carry out at recovery waste vapour caused by the pharmacy procedure of prepared slices of Chinese crude drugs workshop module 20
Reason.
By increasing Water Sproading module 30 on boiler module 10 and prepared slices of Chinese crude drugs workshop module 20, during boiler module 10 is
Medicine medicine materical crude slice workshop module 20 provides the high-temperature steam of Chinese medicine processing, and the distinct device in prepared slices of Chinese crude drugs workshop module 20 is right respectively
Caused hot and humid waste vapour after the processing of medicinal material progress different process, such as dry the baking oven 22 of medicinal material, net belt type is dried
Machine 21, by the demulcen pond 23 of high-temperature steam or the vexed demulcen material of warm water, medicine boiler 24, steaming the medicinal hebrs machine 25 etc., in technical process all
Big amount temperature height, the gas of high humidity can be produced, this kind of gas is due to by pharmaceutical technology, a large amount of impurity of intension, it is impossible to directly
Used for system circulation or be expelled directly out air, therefore, the hot and humid waste vapour in part is condensed by Water Sproading module 30
Liquefaction heel row goes out external environment, avoids hot and humid waste vapour from being directly discharged into air in the form of steam state and pollution is directly contributed to environment,
At the same time boiler mould is discharged into again after carrying out condensation liquefaction to the hot and humid waste vapour of another part by Water Sproading module 30
Block 10, used for the pharmacy of prepared slices of Chinese crude drugs workshop module 20, the waste of water resource is reduced, due in waste gas caused by pharmacy procedure
Containing a large amount of heat energy, the condensation water ph value after condensation liquefaction is neutrality, therefore can be directly direct for prepared slices of Chinese crude drugs workshop module 20
Use, reduce the operating pressure of boiler module 10, decrease the waste of water resource.
Boiler module 10 includes softened water equipment 11, water supply tank 12, boiler 13 and gas-distributing cylinder 14, softened water equipment 11,
Water supply tank 12, boiler 13, gas-distributing cylinder 14 pass sequentially through pipeline connection；Softened water equipment 11 is connected with external source；Gas-distributing cylinder 14
It is connected with prepared slices of Chinese crude drugs workshop module 20 by pipeline, distributes supplying high temperature steam for prepared slices of Chinese crude drugs workshop module 20, soft water can
Avoid in water supply tank 12, boiler 13 and follow-up equipment content is also easy to produce the situation of incrustation scale.
Prepared slices of Chinese crude drugs workshop module 20 includes mesh-belt drier 21, baking oven 22, demulcen pond 23, medicine boiler 24, steaming the medicinal hebrs machine
25, mesh-belt drier 21, baking oven 22, demulcen pond 23, medicine boiler 24, the one end of steaming the medicinal hebrs machine 25 pass through pipeline and gas-distributing cylinder 14 respectively
Connection, the other end are connected with Water Sproading module 30 by pipeline respectively, and the different pharmaceutical processings of prepared slices of Chinese crude drugs workshop module 20 are set
The standby working process for carrying out different process to medicinal material respectively in pharmaceutical factory's water circulation system running, while produce a large amount of
Hot and humid waste vapour.
Water Sproading module 30 includes condensate recovering device 31 and waste gas recovery pond 32；The pressure regulation dress of condensate recovering device 31
Put and be connected with mesh-belt drier 21, baking oven 22, demulcen pond 23, medicine boiler 24 by pipeline, for collecting mesh-belt drier
21st, baking oven 22, demulcen pond 23, medicine boiler 24 process hot and humid steam caused by medicinal material process；Condensate recovering device 31
Draining valve is connected with water supply tank 12 by pipeline, and pharmaceutical factory is supplied for the condensed water reclaimed after liquefying to be discharged into water supply tank 12 again
Water circulation system uses, due to hot and humid caused by mesh-belt drier 21, baking oven 22, demulcen pond 23 and medicine boiler 24
Contain large quantity of moisture and heat energy in waste vapour, by after the condensation liquefaction of condensate recovering device 31 can condensate quality it is higher, can
It is directly discharged into water supply tank 12 and continues the firing use of boiler of feeding 13, is reclaimed by the condensation to waste vapour, softened water can be greatly reduced and set
Standby 11 operating pressure and the waste for reducing external source；Steaming the medicinal hebrs machine 25 is connected with steaming the medicinal hebrs discharge duct 251, steaming the medicinal hebrs blast pipe
Road 251, which is worn, to be connect waste gas recovery pond 32 and is connected with external environment, for that hot and humid caused by the pharmacy of steaming the medicinal hebrs machine 25 will give up
Discharged after vapour cooling liquid from pharmaceutical factory's water circulation system, waste vapour liquefaction rear impurity is more caused by steaming the medicinal hebrs machine 25, uncomfortable
Preferably it is continuing with for system, therefore pharmaceutical factory's water circulation system will be discharged after waste vapour liquefaction caused by steaming the medicinal hebrs machine 25, avoids waste vapour
Directly discharged, reduced environmental pollution with steam state；Waste gas recovery pond 32 is additionally provided with the drainpipe 321 connected with external environment, when
Waste gas recovery pond 32 to steaming the medicinal hebrs discharge duct 251 when continue chilling temperature rise, the heat in waste gas recovery pond 32
Water can be expelled directly out, and refilled soft water and continued to cool down steaming the medicinal hebrs discharge duct 251.
Water Sproading module 30 also includes softened water tank 33, soft water water making device 34 and hot-water cylinder 35, soft water water making device 34
Connected respectively with external source and softened water tank 33, soft water is prepared for softened water tank 33；Softened water tank 33 connects waste gas recovery pond 32, uses
In being that waste gas recovery pond 32 supplies to mend soft water, soft water can effectively prevent the situation of apparatus inwall accumulation incrustation scale, softened water tank 33
For being supplied water to waste gas recovery pond 32 and being the cooling down of condensate recovering device 31；Hot-water cylinder 35 respectively with waste gas recovery pond
32 and condensate recovering device 31 connect, after reclaiming the hot water in waste gas recovery pond 32, hot water is passed through into condensing hot air furnace
The recovery of device 31, which recirculates, to be used, and when temperature is stepped up in the cooling procedure of system detectio waste gas recovery pond 32, conducting is useless
Gas reclaims the pipeline between pond 32 and hot-water cylinder 35, the high-temperature water in waste gas recovery pond 32 is discharged into hot-water cylinder 35, then pass through
Pipeline between hot-water cylinder 35 and condensate recovering device 31 is discharged into hot water after condensate recovering device 31 reclaims to follow for pharmaceutical factory's water
Loop system is continuing with, and reduces cost, reduces water resource waste.
The blast pipe peripheral seal of condensate recovering device 31 is arranged with cooling cylinder 311, and cooling cylinder 311 both ends pass through pipe respectively
Road is connected with softened water tank 33, one end formed cooling import 312, the other end formed coolant outlet 313, by from cooling import 312
To water filling in cooling cylinder 311, and water is discharged into softened water tank 33 again by coolant outlet 313, to condensate recovering device 31
Blast pipe carries out cooling down, when the blast pipe of system detectio condensate recovering device 31 is carried out in condensate recovering device 31 to waste vapour
Radiating exhaust and then temperature is when gradually rising during recovery, by turning on the pipeline between cooling cylinder 311 and softened water tank 33, notes water
Enter to cool down cylinder 311 to radiate to the blast pipe of condensate recovering device 31, the warm water after heat absorption reenters softened water tank 33 and carried out
Radiating, the work load of condensate recovering device 31 is reduced, decrease greenhouse effects pollution.
Waste gas recovery pond 32 is provided with the first temperature inductor for monitoring the internal temperature of waste gas recovery pond 32
322；The blast pipe of condensate recovering device 31 is provided with the second temperature inductor 314 for being used for monitoring blast pipe internal temperature；It is soft
The 3rd temperature inductor 331 for being used for monitoring the internal temperature of softened water tank 33 is provided with water tank 33, the first temperature inductor 322 is used for
The temperature in waste gas recovery pond 32 is detected, when the temperature of waste gas recovery pond 32 is higher than the first 322 design temperature of temperature inductor,
Pipeline between the control system of first temperature inductor 322 conducting waste gas recovery pond 32 and hot-water cylinder 35 carries out draining；Second
Temperature inductor 314 is used for the Tail Pipe Temperature for detecting condensate recovering device 31, when Tail Pipe Temperature senses higher than second temperature
During 314 design temperature of device, the pipeline between control system conducting cooling cylinder 311 and softened water tank 33 radiates to blast pipe；The
Three temperature inductors 331 are used to detect the temperature in softened water tank 33, when the temperature of softened water tank 33 is higher than the 3rd temperature inductor 331
During design temperature, system control 33 external draining of softened water tank, then water filling again is carried out to it by soft water water making device 34.
It is the application method of above-mentioned pharmaceutical factory's water circulation system below, comprises the following steps：
(1) softened water equipment 11 is connected into water filling with external source, running water is injected inside softened water equipment 11, softened water
After running water is prepared into soft water by equipment 11, soft water is discharged into water supply tank 12 and laid in；
(2) soft water is discharged into boiler 13 and heated by water supply tank 12, and caused high-temperature steam is entered by pipeline after heating
Enter gas-distributing cylinder 14 and high-temperature steam is allocated by gas-distributing cylinder 14；
(3) high-temperature steam is separately dispensed into mesh-belt drier 21, baking oven 22, demulcen pond 23, medicine boiler by gas-distributing cylinder 14
24th, in steaming the medicinal hebrs machine 25；
(4) caused hot and humid waste vapour after mesh-belt drier 21, baking oven 22, demulcen pond 23 and the pharmacy of medicine boiler 24
It is discharged into the regulator of condensate recovering device 31 and carries out cavitating elimination and be liquefied as condensed water；
(5) draining valve of condensate recovering device 31 is opened, and condensed water is discharged into water supply tank 12 and supplies water circulation system of pharmaceutical factory
System is continuing with；
(6) at the same time, hot and humid waste vapour caused by the pharmacy procedure of steaming the medicinal hebrs machine 25 passes through steaming the medicinal hebrs discharge duct 251,
The external world is gone out by the cooling liquid heel row of waste gas recovery pond 32；
(7) when second temperature inductor 314 senses that the Tail Pipe Temperature of condensate recovering device 31 is too high, system control
Cooling cylinder 311 turns on softened water tank 33, and the soft water in softened water tank 33 flows through weight after cooling import 312 and coolant outlet 313
Newly enter softened water tank 33, cooling down is carried out to the blast pipe of condensate recovering device 31；
(8) when the first temperature inductor 322 senses the water temperature over-high in waste gas recovery pond 32, system conducting waste gas
The pipeline between pond 32 and hot-water cylinder 35 is reclaimed, the hot water in waste gas recovery pond 32 is discharged into hot-water cylinder 35 and cooled down, hot water
Water is discharged into condensate recovering device 31 and then is discharged into water supply tank 12 again and is continuing with by tank 35；
(9) pipeline between softened water tank 33 and waste gas recovery pond 32 is opened, waste gas recovery pond 32 is refilled soft
Water, cooling liquid is carried out to hot and humid waste vapour caused by steaming the medicinal hebrs machine 25.
Water supply tank 12, waste gas recovery pond 32, softened water tank 33, the water that monitoring water level inside height is equipped with hot-water cylinder 35
Level detecting apparatus (not shown).
Water supply tank 12 includes the first water supply tank 121 and the second water supply tank 122, the first water supply tank 121 and the second moisturizing
Case 122 is connected by placed in series；Boiler 13 includes the first boiler 131 and the second boiler 132, the first boiler 131 and second
Boiler 132 is connected by placed in series, and the first boiler 131 is connected with the second boiler 132 by pipeline with the second water supply tank 122；
Waste gas recovery pond 32 includes the first recovery pond 323 and second and reclaims pond 324, the first recovery pond 323 and second
Recovery pond 324 is arranged side by side, and steaming the medicinal hebrs discharge duct 251 is connected to the first recovery pond 323 and the second recovery pond successively
324, and the side wall in the second recovery pond 324 is passed and connected with external environment.
Above-mentioned embodiment is only preferred embodiment of the present utility model, it is impossible to is protected with this to limit the utility model
Scope, the change of any unsubstantiality that those skilled in the art is done on the basis of the utility model and replacing belongs to
In the utility model scope claimed.
Claims (9)
- A kind of 1. pharmaceutical factory's water circulation system, it is characterised in that：Including boiler module, prepared slices of Chinese crude drugs workshop module and Water Sproading module, the boiler module, the prepared slices of Chinese crude drugs workshop Module and the Water Sproading module are interconnected；The boiler module is used to provide to pharmaceutical factory's water circulation system for moisturizing and to prepared slices of Chinese crude drugs workshop module Pharmaceutical purpose high-temperature steam；Prepared slices of Chinese crude drugs workshop module includes more pharmaceutical processing equipments, for being processed to medicinal material；The Water Sproading module is used to recycle waste vapour caused by the prepared slices of Chinese crude drugs workshop module pharmacy procedure.
- 2. pharmaceutical factory's water circulation system as claimed in claim 1, it is characterised in that：The boiler module is set including softened water Standby, water supply tank, boiler and gas-distributing cylinder, the softened water equipment, the water supply tank, the boiler, the gas-distributing cylinder lead to successively Piping connects；The softened water equipment is connected with external source；The gas-distributing cylinder passes through with prepared slices of Chinese crude drugs workshop module Pipeline connects, and is the prepared slices of Chinese crude drugs workshop module assignment supplying high temperature steam.
- 3. pharmaceutical factory's water circulation system as claimed in claim 2, it is characterised in that：Prepared slices of Chinese crude drugs workshop module includes net Band drier, baking oven, demulcen pond, medicine boiler, steaming the medicinal hebrs machine, the mesh-belt drier, the baking oven, the demulcen pond, institute State medicine boiler, described steaming the medicinal hebrs machine one end is connected by pipeline with the gas-distributing cylinder respectively, the other end respectively with the Water Sproading mould Block is connected by pipeline.
- 4. pharmaceutical factory's water circulation system as claimed in claim 3, it is characterised in that：The Water Sproading module is returned including condensed water Receive device and waste gas recovery pond；It is the regulator of the condensate recovering device and the mesh-belt drier, the baking oven, described Demulcen pond, the medicine boiler are connected by pipeline, for collecting the mesh-belt drier, the baking oven, the demulcen pond, institute State hot and humid steam caused by medicine boiler processing medicinal material process；The draining valve of the condensate recovering device and the water supply tank Connected by pipeline, pharmaceutical factory's water circulation system is supplied for the condensed water reclaimed after liquefying to be discharged into the water supply tank again Use；The steaming the medicinal hebrs machine is connected with steaming the medicinal hebrs discharge duct, the steaming the medicinal hebrs discharge duct wear connect the waste gas recovery pond and with the external world Environmental communication, for by after hot and humid waste vapour cooling liquid caused by the steaming the medicinal hebrs mechanism medicine from pharmaceutical factory's water circulation Discharged in system；The waste gas recovery pond is additionally provided with the drainpipe connected with external environment.
- 5. pharmaceutical factory's water circulation system as claimed in claim 4, it is characterised in that：The Water Sproading module also includes soft water Case, soft water water making device and hot-water cylinder, the soft water water making device connect with external source and the softened water tank respectively, for institute State softened water tank and prepare soft water；The softened water tank connects the waste gas recovery pond, for supplying benefit soft for the waste gas recovery pond Water；The hot-water cylinder is connected with the waste gas recovery pond and the condensate recovering device respectively, is returned for reclaiming the waste gas After receiving the hot water in pond, hot water is reclaimed by the condensate recovering device and recirculates use.
- 6. pharmaceutical factory's water circulation system as claimed in claim 5, it is characterised in that：Outside the blast pipe of the condensate recovering device Enclose sealing shroud and be provided with cooling cylinder, the cooling cylinder both ends are connected by pipeline with the softened water tank respectively, one end formation cool down into Mouthful, the other end forms coolant outlet, by cooling down water filling in cylinder to described from the cooling import, and passes through the coolant outlet Again water is discharged into the softened water tank, cooling down is carried out to the blast pipe of the condensate recovering device.
- 7. pharmaceutical factory's water circulation system as claimed in claim 6, it is characterised in that：The waste gas recovery pond, which is provided with, to be used for Monitor the first temperature inductor of waste gas recovery pond internal temperature；The blast pipe of the condensate recovering device, which is provided with, to be used In the second temperature inductor of monitoring blast pipe internal temperature；It is provided with the softened water tank and is used to monitor temperature inside the softened water tank 3rd temperature inductor of degree.
- 8. pharmaceutical factory's water circulation system as claimed in claim 7, it is characterised in that：The water supply tank, the waste gas recovery pond, The condensate tank of dehumidifier of monitoring water level inside height is equipped with the softened water tank, the hot-water cylinder.
- 9. pharmaceutical factory's water circulation system as claimed in claim 8, it is characterised in that：The water supply tank include the first water supply tank with And second water supply tank, first water supply tank and second water supply tank are connected by placed in series；The boiler includes the One boiler and the second boiler, first boiler are connected with second boiler by placed in series, first boiler with Second boiler is connected by pipeline with second water supply tank；The waste gas recovery pond include first recovery pond and Second recovery pond, it is described first recovery pond and it is described second recovery pond be arranged side by side, the steaming the medicinal hebrs discharge duct according to It is secondary be connected to it is described first recovery pond and it is described second recovery pond, and in described second recovery pond side wall pass with outside Boundary's environmental communication.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720791108.6U CN207112777U (en) | 2017-06-30 | 2017-06-30 | A kind of pharmaceutical factory's water circulation system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720791108.6U CN207112777U (en) | 2017-06-30 | 2017-06-30 | A kind of pharmaceutical factory's water circulation system |
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| Publication Number | Publication Date |
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| CN207112777U true CN207112777U (en) | 2018-03-16 |
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| CN201720791108.6U Active CN207112777U (en) | 2017-06-30 | 2017-06-30 | A kind of pharmaceutical factory's water circulation system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107366898A (en) * | 2017-06-30 | 2017-11-21 | 康美药业股份有限公司 | A kind of pharmaceutical factory's water circulation system and its application method |
| CN109718109A (en) * | 2019-02-22 | 2019-05-07 | 安徽华润金蟾药业股份有限公司 | A kind of prepared slices of Chinese crude drugs concocting process heat reclaim unit |
-
2017
- 2017-06-30 CN CN201720791108.6U patent/CN207112777U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107366898A (en) * | 2017-06-30 | 2017-11-21 | 康美药业股份有限公司 | A kind of pharmaceutical factory's water circulation system and its application method |
| CN109718109A (en) * | 2019-02-22 | 2019-05-07 | 安徽华润金蟾药业股份有限公司 | A kind of prepared slices of Chinese crude drugs concocting process heat reclaim unit |
| CN109718109B (en) * | 2019-02-22 | 2021-07-06 | 安徽华润金蟾药业股份有限公司 | Heat recovery device for processing process of traditional Chinese medicine decoction pieces |
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Effective date of registration: 20190726 Address after: 637 400 No. 8 Qili Avenue, Qili Economic Development Zone, Langzhong City, Nanchong City, Sichuan Province Patentee after: Kangmei Pavilion of Prince Teng (Sichuan) Pharmaceutical Co., Ltd. Address before: The middle Changchun road 515300 in Guangdong province Jieyang City quicksand Town, Puning City Patentee before: Kangmei Pharmaceutical Co., Ltd. |
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