CN109373776A - A kind of cooling circulating water accelerated cooling device - Google Patents
A kind of cooling circulating water accelerated cooling device Download PDFInfo
- Publication number
- CN109373776A CN109373776A CN201811377879.6A CN201811377879A CN109373776A CN 109373776 A CN109373776 A CN 109373776A CN 201811377879 A CN201811377879 A CN 201811377879A CN 109373776 A CN109373776 A CN 109373776A
- Authority
- CN
- China
- Prior art keywords
- cooling
- circulating water
- water
- cooling device
- oblique flow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 91
- 238000001816 cooling Methods 0.000 title claims abstract description 78
- 239000006185 dispersion Substances 0.000 claims abstract description 11
- 238000009434 installation Methods 0.000 claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007105 physical stamina Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C1/00—Direct-contact trickle coolers, e.g. cooling towers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/04—Distributing or accumulator troughs
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Other Air-Conditioning Systems (AREA)
Abstract
The invention discloses a kind of cooling circulating water accelerated cooling devices, including cooling back installation, the cooling back installation is by circulating water pool, vacuum concentrator, water ring vacuum pump and cooling tower pass sequentially through pipeline and connect into closing loop system composition, the cooling tower is arranged in top of building, auxiliary cooling device is provided between the cooling tower and the circulating water pool, the auxiliary cooling device includes drip tray, annular cold water tank, oblique flow sink and orifice plate water dispersion trough, the lower end of the cooling tower is arranged in the drip tray, the annular cold water tank setting is having acclive building surrounding, the upper end connects the drip tray, lower end connects the oblique flow sink, the orifice plate water dispersion trough is arranged in the surface of the circulating water pool and is connected to the lower end of the oblique flow sink, the present invention carries out that cooling is accelerated to follow by auxiliary cooling device Ring water, improves work efficiency, and energy saving reduces production cost.
Description
Technical field
The present invention relates to a kind of medical fluid cooling cycle water installations, and in particular to a kind of cooling circulating water accelerated cooling device.
Background technique
Medical fluid extracts enrichment process as reduced vacuum concentration, has in concentration process to the inflow temperature of cooling circulating water
More harsh requirement, as inlet water temperature is higher than 32oThe vacuum degree that C then influences inspissator is formed, and equipment can not work normally, often
The cooling water system installation of rule is to be located at cooling tower above circulating water pool, by cooling column body water-distributing device and heat dissipation
Fan precipitation temperature, and the water temperature of equipment discharge is often as high as 40 in process of productionoThe average water temperature drop of C or more, cooling tower are big
About 5oC or so, it is difficult to meet the duty requirements of concentrator.
Met in a manner of being used according to the water temperature of actual measurement and manually intermittently supplementing new water into circulating water pool at present
The duty requirements of concentrator, so not only waste of energy, artificial, but also it is difficult to ensure the stable operation of concentrator.
Summary of the invention
The technical problems to be solved by the present invention are: overcoming the shortcomings of the prior art, a kind of cooling circulating water is provided
Accelerated cooling device accelerates cooling circulating water using having the auxiliary cooling devices such as acclive annular cold water tank, makes average temperature
Overall decline 10oC meets the duty requirements of concentrator.
The present invention is adopted the technical scheme that in order to solve the technical problem: a kind of cooling circulating water accelerated cooling device, packet
Cooling back installation is included, the cooling back installation is successively led to by circulating water pool, vacuum concentrator, water ring vacuum pump and cooling tower
Piping connects into closing loop system composition, and the cooling tower setting is in top of building, the cooling tower and the recirculated water
Auxiliary cooling device is provided between pond, the auxiliary cooling device includes drip tray, annular cold water tank, oblique flow sink and orifice plate
The lower end of the cooling tower is arranged in water dispersion trough, the drip tray, and the annular cold water tank setting is having acclive building
Surrounding, the upper end connects the drip tray, lower end connects the oblique flow sink, and the orifice plate water dispersion trough is arranged in the recirculated water
The surface in pond and the lower end for being connected to the oblique flow sink.
The top of building that it is 6m apart from ground level that the cooling tower, which is arranged in, the annular cold water tank is by four sections of cold water
Slot forms square structure, and the size of the cold water tank is 800mm × 400mm, and the tilt angle of the oblique flow sink is 30 °,
The size of the orifice plate water dispersion trough is 1500mm × 3000mm.
The right end of the circulating water pool connects the vacuum concentrator, the vacuum concentrator and the water by water inlet pipe
It is connected between ring vacuum pump by connecting tube, the upper end of the water ring vacuum pump connects the cooling tower by outlet pipe, described
Vacuum concentrator is vacuum-concentrcted device.
The beneficial effects of the present invention are: the configuration of the present invention is simple, easy to use, the operating condition for not only meeting concentrator is needed
It asks, is also saved greatly energy consumption, reduce production cost, improve work efficiency.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Specific embodiment
The present invention will be further explained in the following with reference to the drawings and specific embodiments:
Referring to Fig. 1, in figure, 1- circulating water pool, 2- vacuum concentrator, 3- water ring vacuum pump, 4- cooling tower, 5- pipeline, 51- water inlet
Pipe, 52- connecting tube, 53- outlet pipe, 6- drip tray, 7- annular cold water tank, 8- oblique flow sink, 9- orifice plate water dispersion trough, shown in arrow
Direction is water (flow) direction.
Embodiment: a kind of cooling circulating water accelerated cooling device, including cooling back installation, cooling back installation is by recycling
Pond 1, vacuum concentrator 2, water ring vacuum pump 3 and cooling tower 4 pass sequentially through pipeline 5 and connect into closing loop system composition, cooling
The setting of tower 4 is provided with auxiliary cooling device between top of building, cooling tower 4 and circulating water pool 1, and auxiliary cooling device includes
The lower end of cooling tower 4 is arranged in drip tray 6, annular cold water tank 7, oblique flow sink 8 and orifice plate water dispersion trough 9, drip tray 6, and annular is cool
The setting of sink 7 is having acclive building surrounding, and the upper end connects drip tray 6, lower end connects oblique flow sink 8, orifice plate aproll
Slot 9 is arranged in the surface of circulating water pool 1 and is connected to the lower end of oblique flow sink 8.
Height of the cooling tower 4 apart from ground is 6m, and annular cold water tank 7 forms square structure, cold water by four sections of cold water tanks
The size of slot is 800mm × 400mm, and the tilt angle of oblique flow sink 8 is 30 °, the size of orifice plate water dispersion trough 9 be 1500mm ×
3000mm。
The right end of circulating water pool 1 connects vacuum concentrator 2 by water inlet pipe 51, vacuum concentrator 2 and water ring vacuum pump 3 it
Between connected by connecting tube 52, the upper end of water ring vacuum pump 3 connects cooling tower 4 by outlet pipe 53, and vacuum concentrator 2 is vacuum
Decompression concentrator.
Construction method: former cooling tower 4 is moved into a 6m high top of building from the ground, and is pressed centainly in building surrounding
One circle 800mm × 400mm cold water tank of gradient installation, annular 7 one end of cold water tank connects with the lower part drip tray 6 of cooling tower 4, another
End is connected by 30 ° of oblique flow sinks 8 with 1500mm × 3000mm orifice plate water dispersing disc 9 of 1 top of circulating water pool, high temperature circulation water warp
After cooling tower 4 is cooling, then flows to after oblique flow sink 8 enters orifice plate water dispersing disc 9 and uniformly trickled down to recirculated water through annular cold water tank 7
In pond 1, total 10 DEG C of physical stamina letdown of average temperature are tested through actual motion, meets the duty requirements of concentrator.
The above described is only a preferred embodiment of the present invention, be not intended to limit the present invention in any form, it is all
It is any simple modification, equivalent change and modification to the above embodiments according to the technical essence of the invention, still falls within
In the range of technical solution of the present invention.
Claims (6)
1. a kind of cooling circulating water accelerated cooling device, including cooling back installation, the cooling back installation is by circulating water pool
(1), vacuum concentrator (2), water ring vacuum pump (3) and cooling tower (4) pass sequentially through pipeline (5) and connect into closing loop system group
At, it is characterised in that: the cooling tower (4) setting in top of building, the cooling tower (4) and the circulating water pool (1) it
Between be provided with auxiliary cooling device, the auxiliary cooling device includes drip tray (6), annular cold water tank (7), oblique flow sink (8)
With orifice plate water dispersion trough (9), drip tray (6) setting is arranged in the lower end of the cooling tower (4), the annular cold water tank (7)
Having acclive building surrounding, the upper end connects the drip tray (6), lower end connects the oblique flow sink (8), the hole
Plate water dispersion trough (9) is arranged the surface in the circulating water pool (1) and is connected to the lower end of the oblique flow sink (8).
2. a kind of cooling circulating water accelerated cooling device according to claim 1, it is characterised in that: the cooling tower (4)
The top of building for being 6m apart from ground level is set.
3. a kind of cooling circulating water accelerated cooling device according to claim 1, it is characterised in that: the annular cold water tank
(7) square structure is formed by four sections of cold water tanks, the size of the cold water tank is 800mm × 400mm.
4. a kind of cooling circulating water accelerated cooling device according to claim 1, it is characterised in that: the oblique flow sink
(8) tilt angle is 30 °.
5. a kind of cooling circulating water accelerated cooling device according to claim 1, it is characterised in that: the orifice plate water dispersion trough
(9) size is 1500mm × 3000mm.
6. a kind of cooling circulating water accelerated cooling device according to claim 1, it is characterised in that: the circulating water pool
(1) right end connects the vacuum concentrator (2), the vacuum concentrator (2) and the Water-ring vacuum by water inlet pipe (51)
It pumps and is connected between (3) by connecting tube (52), the upper end of the water ring vacuum pump (3) connects the cooling by outlet pipe (53)
Tower (4), the vacuum concentrator (2) are vacuum-concentrcted device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811377879.6A CN109373776A (en) | 2018-11-19 | 2018-11-19 | A kind of cooling circulating water accelerated cooling device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811377879.6A CN109373776A (en) | 2018-11-19 | 2018-11-19 | A kind of cooling circulating water accelerated cooling device |
Publications (1)
Publication Number | Publication Date |
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CN109373776A true CN109373776A (en) | 2019-02-22 |
Family
ID=65389694
Family Applications (1)
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CN201811377879.6A Pending CN109373776A (en) | 2018-11-19 | 2018-11-19 | A kind of cooling circulating water accelerated cooling device |
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CN (1) | CN109373776A (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103727834A (en) * | 2014-01-03 | 2014-04-16 | 中国轻工业武汉设计工程有限责任公司 | Energy-saving type dual-combination circulation cooling water device |
KR20140075399A (en) * | 2012-12-11 | 2014-06-19 | 정양전 | Heating tower and cooling and heating equipment using it |
CN105283720A (en) * | 2013-12-17 | 2016-01-27 | 株式会社前川制作所 | Sublimation defrost system for refrigeration devices and sublimation defrost method |
CN205975781U (en) * | 2016-08-18 | 2017-02-22 | 山西广誉远国药有限公司 | Extraction of traditional chinese medicine material workshop circulating water system |
CN108796543A (en) * | 2018-06-24 | 2018-11-13 | 茌平信发华兴化工有限公司 | The secondary lime set electrolyzer system of piece alkali |
CN209131436U (en) * | 2018-11-19 | 2019-07-19 | 洛阳远洋生物制药有限公司 | A kind of cooling circulating water accelerated cooling device |
-
2018
- 2018-11-19 CN CN201811377879.6A patent/CN109373776A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20140075399A (en) * | 2012-12-11 | 2014-06-19 | 정양전 | Heating tower and cooling and heating equipment using it |
CN105283720A (en) * | 2013-12-17 | 2016-01-27 | 株式会社前川制作所 | Sublimation defrost system for refrigeration devices and sublimation defrost method |
CN103727834A (en) * | 2014-01-03 | 2014-04-16 | 中国轻工业武汉设计工程有限责任公司 | Energy-saving type dual-combination circulation cooling water device |
CN205975781U (en) * | 2016-08-18 | 2017-02-22 | 山西广誉远国药有限公司 | Extraction of traditional chinese medicine material workshop circulating water system |
CN108796543A (en) * | 2018-06-24 | 2018-11-13 | 茌平信发华兴化工有限公司 | The secondary lime set electrolyzer system of piece alkali |
CN209131436U (en) * | 2018-11-19 | 2019-07-19 | 洛阳远洋生物制药有限公司 | A kind of cooling circulating water accelerated cooling device |
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